t um This is to certify that the dissertation entitled PROCESSING STRATEGIES TO IMPROVE DRY BEAN (PhaseoTus vulgaris) DIGESTIBILITY AND FOOD UTILIZATION presented by Liiiian Geraldine Occefia has been accepted towards fulfillment of the requirements for Ph.D. degree in TFOOd SCIENCE Major professor MM fl gap/74 Date ApriT 29, 1994 MSU is an Affirmative Action/Equal Opportunity Institution 0-12771 IIII’IHIIlHlllllllllIIIfll‘lllllllllllHHIHMHIIIHII 3 1293 01053 0743 LIBRARY Michigan State Unlversity MENRETUFII wxwmmummmm TOAVOIDFINEOMunonorbdmddoduo. 1:, DATE DUE DATE DUE DATE DUE mun-mmmmwom' mum“ ‘ Was-9.1 \a- K _ ‘ ‘— PROCESSING STRATEGIES TO IMPROVE DRY BEAN (Phaseolus vulgaris) DIGESTIBILITY AND FOOD UTILIZATION By Lillian Geraldine Oooefia A DISSERTATION Submitted to Michigan State University in partial fulfillment of the requirements for the degree of DOCTOR OF PHILOSOPHY Department of Food Science and Human Nutrition 1994 ABSTRACT PROCESSING STRATEGIES TO IMPROVE DRY BEAN (Phaseolus vulgaris) DIGESTIBILITY AND FOOD UTILIZATION By LillianGeraldineOccefia Dry edible beans serve as a major source of protein in many developing countries. However, many constraints, including antinutritional and flatulence factors which interfere with protein digestibility, limit wider utilization of dry edible beans. Processing strategies designed to eliminate these factors and provide a precooked ingredient suitable for food formulations are warranted. Whole and split dry beans (Phaseolus vulgaris) soaked and hydrated for 16 hrs. (25°C) were subjected to hot water (60°C/60 mins.), steam (100°C/15 mins.) and differential enzymatic pretreatments. Cooked CONTROL beans contained all original soak and rinse waters, cook water or condensate (formulation water) prior to milling to a homogeneous slurry whereas leachate of EXTRACT and cooked beans was replaced with fresh formulation water. Bean slurries pre-heated to 95°C were dried on a double drum- dryer. Enzymatic pretreatment involved the use of both indigenous ("sprout slurry") and commercial enzymes (Viscozyme, Alcalase, Neutrase and Celluclast). The drum-dried bean meals were analyzed for proximate composition (moisture, 5%; protein, 23%; fat, 2%; and ash, 4%), total soluble sugars (stachyose, 0.3% to 0.8%), dietary fiber (soluble, 5% and insoluble, 15-21%), total mineral content (plasma emission spectrometry) and in-vitro starch and protein digestibilities. Functional properties of the drum-dried bean meals, including color, water absorption index, water solubility index and degree brix of the soluble fraction were also evaluated. The resultant bean meals were differentiated by soluble losses and quality characteristics. Hot water extraction provided an approximately 8% increase in protein digestibility (in-vitro). Soluble dietary fiber content was approximately 5%, whereas insoluble dietary fiber averaged 18%. Hot water extraction resulted in significant reduction of minerals (K, Ca, Al, Cu, Fe, Zn and Mg) and soluble sugars (stachyose, 0.3%-0.8% ). The processed product had neutral color and did not possess the frequently objectionable "beany" flavor. The DDBMs were incorporated in a pumpkin quick bread formulation (0%, 20%, 40%, and 60% levels of substitution) and a weaning beverage (5%, 8% and 10%). Acceptable quality breads were produced at the 20% and 40% levels of substitution. Enzyme pre-digested DDBMs possess great potential in weaning food formulations, especially at the 8% concentration level. The use of indigenous enzymes (i.e., sprouting ) to modify the functional properties of DDBM used in weaning beverage formulations warrants additional research. Microwave preconditioning of dry beans demonstrated the potential of microwave energy to improve whole bean seed cooking, ensure rapid processing of beans by disrupting starch granules and facilitating gelatinization. The physical and functional properties (swelling power, solubility, degree of syneresis, appparent viscosity and elasticity) of pure bean starch were significantly affected by microwave heating. To my parents, who have provided me a strong foundation to go through life's challenges iv. ACKNOWLEDGMENTS My sincere appreciation goes to my Graduate Committee members: Dr. Maurice Bennink, Dr. George Hosfield, Dr. Mary E. Zabik and Dr. Wanda Chenoweth, for their valuable advice and guidance throughout my Ph.d Graduate program: I am most grateful to my Advisor, Dr. Mark A. Uebersax, who has become a mentor, colleague, teacher and friend; thank you for providing me the support and opportunities for my professional growth. I am fortunate to have wonderful friends in: Ahmad Shirazi, who was always encouraging and available to lend a helping hand and listening ear Sharon Hart, Miriam Nettles, Virginia Vega, Nirmal Sinha, Danny Campos, Leticia Carpio, Cheribeth Tan, who always cheered me up when the going got rough Danny, Letlet and Muhammad Siddiq, for helping and staying up with me during those last nights before the defense. My brother, Luis, who is always around when I need help. I am forever grateful to my family for their love, support and encouragement. Sincere gratitude is extended to Gerber Products Company in Fremont, M1 for the use of their facilities; thank you Jerry Stroven and Duane Dougan, for all your assistance. I also thank the Bean-CowpealCRSP for partial support of this project To the Aggie family of Xavier University, especially Fr. Ledesma & the Food Tech faculty and staff, for holding the fort while I was on study leave Above all,IamgratefultotheAlmightyforkeepingmein thepalmofI-Iishand. TABLE OF CONTENTS LIST OF TABLES ............................................................................... xi LIST OF FIGURES ............................................................................. xiii LIST OF PLATES ............................................................................... xvii INTRODUCTION ............................................................................... 1 REVIEW OF LITERATURE ................................................................. 4 Chemical Composition of Dry Beans (Phaseolus vulgaris) .................................... 4 Carbohydrates ....................................................................... 4 Proteins ............................................................................... 11 Minerals and Vitamins .............................................................. 12 Lipids ................................................................................. 13 Tannins and Polyphenols ........................................................... 14 Bean Flavor Constituents ........................................................... 14 Nutritional Digestibility and Physiology of Dry Edible Beans ........................ 16 Factors Affecting Digestibility of Dry Legume Starch and Protein ............ 16 Digestibility of Legume Protein .................................................... 22 Digestibility of Legume Starch ..................................................... 25 Flatulence Associated with Legume Consumption ............................... 27 Raffinose, Stachyose and Verbascose ...................................... 28 Dietary Fiber ................................................................... 31 Resistant or Indigestible Starch 33 Hypocholesterolemic and Hypoglycemic Responses of Bean Dietary Fiber. 39 Processing and Utilization of Dry Edible Beans as Specialized Foods .............. 44 Bean Sprouts, Curds and Ferments ............................................... 46 vi Bean Meals, Flours and Powders ................................................ . 47 Functional Characteristics and Applications ...................................... 48 Drum-Drying of Legumes ................................................... 51 Description of Equipment and Process System .................... 51 Control of Drying Process ............................................ 53 Thermal Extrusion ................................................................... 54 Microwave Heating of Legumes ................................................... 56 Mechanism of Microwave Heating ........................................ 56 Microwave Effects on Food Composition ................................. 57 Potential for Dry Edible Beans as Weaning Foods .............................. 61 Potential for Soybean as a High -Protein Weaning Beverage .................. 66 MATERIALS AND METHODS ............................................................. 72 Hot Water/Steam Extractions of Whole Navy Beans ................................... 72 Enzymatic Pre-digestion of Whole Navy Beans ....................................... 75 Aqueous Extractions and Enzymatic Pre-digestion of Split Navy Beans ............ 76 Drum—Drying of Bean Meals .............................................................. 78 Chemical and Biological Analyses ....................................................... 79 Proximate Composition ............................................................. 79 Moisture ........................................................................ 79 Protein .......................................................................... 80 Fat ............................................................................... 80 Ash .............................................................................. 80 Soluble Sugars by HPLC ........................................................... 80 Extraction of Soluble Sugars ................................................ 80 Separation and Quantitation .................................................. 82 Total Mineral Content ............................................................... 83 Insoluble and Soluble Dietary Fiber ............................................... 83 vii In-vitro Starch Digestibility ......................................................... 86 Determination of Total Starch 86 Determination of Available Starch 88 In-vitro Protein Digestibility ........................................................ 9O Methionine ............................................................................ 92 Amino Acid Analysis ................................................................ 92 SDS-PAGE Electrophoresis ........................................................ 93 Assessment of Antinutritional Factors 94 Screening for Heat-Stable Trypsin Inhibitory Activity .................. 94 Screening for Phytohemagglutinins ........................................ 96 Phytic Acid .................................................................... 96 Physical and Functional Properties of Drum-Dried Bean Flours ..................... 98 Color .................................................................................. 98 Cellular Structure and Starch Granule Appearance .............................. 98 Solubility ............................................................................. 99 Water Absorption Index ...................................................... 99 Water Solubility Index ........................................................ 99 Water Holding Capacity ............................................................ 99 Bulk Density ......................................................................... 100 Nitrogen Solubility Index (NSI) ................................................... 100 Incorporation of Drum-Dried Bean Flour in Food Product ..................... 100 Quick Bread .......................................................................... 100 Weaning Food Beverage ............................................................ 102 Objective Quality Evaluation of Bean Products ......................................... 103 Viscosity ............................................................................. 103 pH .................................................................................... 103 Texture ....... ~ ......................................................................... 103 viii Volume of the bread ................................................................. 103 Density ................................................................................ 105 Moisture .............................................................................. 105 Microstructure ....................................................................... 105 Weaning Food/Beverage .................................................................. 105 Suspension Stability ................................................................ 105 Visual Stability ................................................................ 105 Micro Quantitative Method ................................................... 105 Consistency .......................................................................... 107 Apparent Viscosity ........................................................... 107 Relative Viscosity ............................................................. 107 Physico-Chemical Tests ........................................................... . 107 Color ........................................................................... 107 pH .............................................................................. 107 Soluble solids ................................................................. 107 Total Solids .................................................................... 108 Microwave Preconditioning of Whole Dry Navy Beans .............................. 108 Texture ................................................................................ 108 Color .................................................................................. 108 Cellular Structure and Starch Granule Appearance .............................. 110 Microwave Heating of Bean Starch ...................................................... 110 Bean Starch Isolation ............................................................... 110 Bean Starch Chemical Composition ............................................... 111 Heating of Bean Starch ............................................................ . 111 Microwave Heating ........................................................... 111 Conventional Heating ........................................................ 112 Bean Starch Physical Properties ................................................. . 112 ix Starch Swelling Power and Solubility ..................................... 112 Degree of Syneresis .......................................................... 112 Gel Rheological Properties .................................................. 112 Scanning Electron Microscopy (SEM) ..................................... 112 Statistical Analysis ......................................................................... 113 CHAPTER I. EXTRACTIVE PRETREATMENTS TO IMPROVE DRY BEAN DIGESTIBILITY ...................................................................... 114 Introduction ................................................................................. 114 Materials and Methods ..................................................................... 115 Results and Discussion .................................................................... 117 Conclusion .................................................................................. 159 CHAPTER II. FUNCTIONAL CHARACTERISTICS OF DRUM-DRIED BEAN MEALS AND THEIR INCORPORATION IN SELECTED FOOD SYSTEMS .......................................................................................... 162 Introduction ................................................................................. 162 Materials and Methods .................................................................. . 163 Results and Discussion .................................................................... 166 Conclusion .................................................................................. 189 CHAPTER III. MICROWAVE HEATING CHARACTERISTICS OF WHOLE BEANS AND BEAN STARCH ................................................. 191 Introduction ................................................................................. 191 Materials and Methods ..................................................................... 192 Results and Discussion .................................................................... 195 Conclusion .................................................................................. 209 SUMMARY AND RECOMMENDATIONS .............................................. 213 LIST OF REFERENCES ...................................................................... 216 Table 1. Table 2. Table 3. Table 4. Table 5. Table 6. Table 6. Table 7. Table 7. Table 8. Table 9. Table 10. Table 11. Table 12. Table 13. Table 14. Table 15. Table 16. LIST OF TABLES Nutritional composition of selected raw dry edible beans (Phaseolus vulgaris) ............................................................................... 8 Constraints limiting utilization of dry beans ........................................ l7 Pumpkin bread formula ............................................................... 102 Proximate chemical composition (% db) of split bean drum-dried meals ....... 120 Proximate chemical composition of non-extracted (CONTROL) with subsequent enzyme-predigested treated whole drum-dried bean meals ....... 121 Total mineral content (ppm) split bean drum-dried meals ......................... 125 (Cont.'d) Total mineral content (ppm) split bean drum-dried meals ............. 126 Total mineral content (ppm) of non—extracted (CONTROL) with subsequent enzyme pre-digested treated whole drum-dried bean meals.................... 127 (Cont.'d) Total mineral content (ppm) of non-extracted (CONTROL) with subsequent enzyme pre-digested treated whole drum-dried bean meals ...... 128 Effect of extractive pre-treatments on the total starch content of bean drum- dried meals ........................................................................... 132 Effect of extractive pre-treatments on the in-vitro digestibility of starch in raw split navy beans and split bean drum-dried meals 135 Effect of enzymatic pre-digestion on in-vitro digestibility of starch in raw whole Navy beans and whole bean drum-dried meals .......................... 136 Amino acid content (p moles) of split drum-dried bean meals .................... 156 Methionine content of drum-dried bean meals ...................................... 156 Heat stable Trypsin Inhibitor Activity (TIA) inositol phosphates (%) and phytate content (%) in split bean drum-dried meals ............................. 158 Visual reaction for screening of dry bean lectin (phytohemagglutinin) .......... 160 Physical and functional properties of split bean drum-dried bean meals ........ 169 Physical characteristics of pumpkin breads substituted with 0-60% drum- dried bean meal ..................................................................... . 172 xi Table 17. Table 18. Table 19. Table 20. Multiple Blade Shear Compression Mode of pumpkin breads with 0 to 60% drum-dried bean meal substitution ................................................. 175 Mean values of physical Texture Profile Analysis (T PA) of drum-dried bean meal pumpkin breads ................................................................ 176 Physical characteristics of weaning bean beverages ............................... 180 Microwave pre-conditioning and re-heating times (min.) using a Nordicware microwave pressure cooker ....................................................... . 201 xii Figure 1. Figure 2. Figure 3. Figure 4. Figure 5. Figure 6. Figure 7. Figure 8. Figure 9. Figure 10. Figure 11. Figure 12. Figure 13. Figure 14. Figure 15. Figure 16. Figure 17. Figure 18. Figure 19. Figure 20. LIST OF FIGURES Proximate composition of selected raw legumes (Phaseolus vulgaris) ......... 5 Macro-mineral content of selected raw legumes (Phaseolus vulgaris) .......... 6 Micro—mineral content of selected raw legumes (Phaseolus vulgaris) .......... 6 Vitamin content of selected raw legumes (Phaseolus vulgaris) .................. 7 Energy values of selected raw legumes (Phaseolus vulgaris)................... 7 Outline summarizing factors influencing digestibility and bioavailability of nutrients in dry beans ............................................................. . 18 Nitrogen digestion, absorption and retention ..................................... 19 Proposed mechanism of gas production involving oligosaccharides and resistant starch ..................................................................... . 29 Outline illustrating processing strategies and edible by-products of common dry beans in LDC and industralized countries ................................... 45 Schematic components of a double surface drum-drier ......................... . 52 World production of major food legumes .......................................... 67 Illinois method for processing soymilk from whole soybeans .................. 69 Flowchart for hot water extraction of dry navy beans ............................ 73 Designation of treatment tenninology and extraction treatment differentiation used during cooked bean preparation............................................ 74 Flowchart for enzyme pre-digestion of whole and split Navy beans prior to drum-drying ......................................................................... 77 Flowchart for the extraction of soluble sugars from drum-dried bean meals. 81 Flowchart of enzymatic method to determine the insoluble and soluble dietary fiber of drum-dried bean meals .................................................. . 84 Flow diagram for determination of total starch .................................... 87 Flowchart for the determination of available starch ............................... 89 Flowchart for in-vitro protein digestibility ......................................... 91 xiii Figure 21. Figure 22. Figure 23. Figure 24. Figure 25. Figure 26. Figure 27. Figure 28. Figure 29. Figure 30. Figure 31. Figure 32. Figure 33. Figure 34. Figure 35. Figure 36. Figure 37. Figure 38. Figure 39. Figure 40. Figure 41. Figure 42. Figure 43. Flowchart for the Trypsin Inhibitor Assay (TIA) ................................. 95 Flowchart for the separation and quantitative determination of phytic acid as inositol phosphate ................................................................. . 97 Flowchart of utilization of drum-dried bean flour in pumpkin bread ........... 101 Flowchart of the objective evaluation of drum-dried bean meal products ...... 104 Experimental flowchart for the preparation of the weaning bean beverage... 106 Experimental design for the microwave pre-conditioning of dry navy beans. 109 The experimental flow chart for study [-1. Extractive pre-treatment to improve dry bean digestibility ..................................................... 116 Moisture-solids balance for drum-dried bean meals .............................. 118 Soluble sugars of split drum—dried bean meals .................................... 123 Soluble sugar content of enzyme pre-digested whole drum-dried bean meals 123 Insoluble and soluble dietary fibers of split bean drum-dried meals ............ 130 Insoluble and soluble dietary fibers of whole bean drum-dried meals ......... 130 Total starch content of raw and split bean drum-dried meals .................... 133 Total starch content of raw and enzyme pre-digested whole bean drum- dried meals ......................................................................... . 133 Hydrolysis of starch in raw and split bean drum-dried meals by pancreatic alpha—amylase ....................................................................... 137 Hydrolysis of starch in raw and whole bean drum-dried meals by in-vitro pancreatic alpha-amylase ........................................................... 138 In-vitro protein digestibility of split bean drum-dried meals ..................... 151 In-vitro protein digestibility of whole bean drum-dried meals ................... 151 Graphical representation of the SDS-gel electrophoretic pattern of enzyme pre-digested whole drum-dried bean meals .................................... . 153 The experimental flowchart for Study H: Functional characteristics of drum-dried bean meals and their incorporation in selected food systems... 164 Flowchart of the experimental design for Study H-2: Incorporation of drum-dried bean flour in pumpkin bread ....................................... . 165 A generalized Texture Profile Analysis (TPA) curve and a typical pumpkin bread TPA curve .................................................................... 177 Comparative visual stability of bean beverage DDBMs and soy formula ...... 182 xiv Figure 44. Figure 45. Figure 46. Figure 47. Figure 48. Figure 49. Figure 50. Figure 51. Figure 52. Figure 53. Figure 54. Figure 55. Figure 56. Figure 57. Figure 58. Figure 59. Figure 60. Figure 61. Absorbance vs concentration for 5% EXTRACT and 5% Viscozyme bean beverages ............................................................................ 184 Absorbance vs Concentration of 8% EXTRACT and 8% Viscozyme bean beverages ............................................................................ 184 Absorbance vs Concentration of 10% EXTRACT and 10% Viscozyme bean beverages ...................................................................... 184 Comparative absorbance of 5% bean beverages ................................. . 186 Comparative absorbance of 8% EXTRACT and enzyme pre-digest (Viscozyme) beverages ............................................................ 186 Comparative absorbance of 10% EXTRACT and enzyme pre-digest bean beverages ............................................................................ 186 Comparative transmission (%) of bean beverage separated supemate from DDBM EXTRACT and soy formula ....................................... 187 Comparative visual stability of bean beverage from DDBM and soy formula .............................................................................. 187 Viscosity of bean beverages from drum-dried bean meals at different concentration levels ................................................................. 188 Time for the bean beverage (5%) to flow through the two marks of an Oswald pipette ...................................................................... 188 Apparent viscosities of 5% EXTRACT bean beverages with different levels of emulsifiers ........................................................................ 190 Time for 5% EXTRACT and 5% Viscozyme bean beverages with caregeenan (0.02 & 0.03%) to flow through the two marks of an Oswald pipette ................................................................................ 190 Comparative transmission (%) of 5% EXTRACT with and without carageenan ........................................................................... 190 Comparative transmission (%) of 5% Viscozyme bean beverage with and without carageenan ................................................................. 190 The experimental flowchart for Chapter III: Microwave pre-conditioning of dry beans (Study 1) and microwave heating of bean starch (Study H) ....... 193 Moisture content of dry navy beans soaked at 25°C for various time periods. 196 Maximum force required to shear Navy beans pre-conditioned by microwavesin a Nordicware pressure cooker ................................... 197 Maximum force required to shear pre—conditioned Navy beans after re— heating (0.5 min., 740 W) in a Nordicware pressure cooker ................. 197 XV Figure 62. Figure 63. Figure 64. Figure 65. Figure 66. Figure 67. Figure 68. Figure 69. Figure 70. Figure 71. Total increase (% above soak weight) in weight of pre-conditioned Navy beans after re-heating ( 0.5 min., Nordicware pressure cooker)......... 198 Maximum force required to shear Navy beans cooked in a conventional retort (45 min., 116°C) or subjected microwave energy levels in Nordicware pressure cooker ..................................................... . 198 Color of final product as affected by post-soaking moisture content and microwave energy levels used for pre-conditioning (Nordicware pressure cooker) ............................................................................... 199 Swelling power pattern of bean starch with conventional and microwave he at in g ............................................................................... 204 Swelling power pattern of corn starch with conventional and microwave he at i n g ............................................................................... 204 Solubility Index (SI) of corn and bean starches during microwave heating... 205 Solubility Index (SI) of corn and bean starches during conventional heating. 205 Degree of syneresis (%) of 8% (w/w) starch gels stored at room temperature for 1 week ............................................................. 207 Apparent viscosity (poise) of 8% (w/w) starch gels stored at room temperature for 7 days ............................................................. 208 Apparent Elasticity of 8% (w/w) starch gels stored at room temperature for 7 days ............................................................................ 208 xvi Plate 1. Plate 2. Plate 3. Plate 4. Plate 5. Plate 6. Plate 7. Plate 8. Plate 9. Plate 10. Plate 1 1. Plate 12. Plate 13. Plate 14. LIST OF PLATES Raw split meal (a-b) under LSM microscopy and (c-d) under polarizing light microscopy ...................................................................... 142 EXTRACT DDBM (a—b) under LSM microscopy and (c-d) under polarizing light microscopy ...................................................................... 143 LSM micrographs of non-extracted (CONTROL) (a-b) and enzyme pre- digested whole bean drum- dried meals. Viscozyme (c- d), Sprout (e- f), Alcalase (g- -,h) Neutrase (i-j) and Celluclast (k- l) ............................ 144-145 LSM micrograph of canned and subsequently freeze-dried whole navy bean... 146 LSM micrographs of (a) soft canned bean and (b) firm canned bean (92 RNK 8P) .......................................................................... 147 General appearance of a) raw navy bean splits and b) EXTRACT DDBM...... 167 Crystalline structure of drum-dried bean meal under a stereomicroscope (50x): a) EXTRACT, b) VISCOZYME ............................................ 168 Appearance of pumpkin quick breads prepared with different levels (20%, 40% and 60%) of pre-treated DDBMs (CONTROL, EXTRACT, VISCOZYME and SPROUT) ....................................................... 171 General appearance of pumpkin quick breads prepared with CONTROL DDBM substituted at 20% to 60% reference sample in 100% wheat flour formulation ............................................................................ 173 LSM micrographs of pumpkin bread cellular microstructure: a) Reference (100% all-pu urpose flour), b) CONTROL DDBM, c)" EXTRACT DDBM, d) VISCOZYME DDBM, e) SPROUT DDBM... ... 179 Appearance of weaning beverage prepared with different levels (5%, 8%, 10%) of pretreated (a) EXTRACT and Viscozyme DDBMs and .(b) CONTROL and Sprout DDBMs ................................................ 183 Structural components of dry (a) and soaked (b) (25°C, 16 hours) navy beans. Pictures were taken from the cross-section of the seeds using a LSM .................................................................................... 202 Cellular structure of navy beans pre—conditioned (a) at 590 watts for 5 min. and subsequently re-heated (b) at 740 watts for 3.5 min. from frozen state. Pictures were taken from a cross-section of the whole beans using LSM ..... 203 8% starch gels stored at room temperature for 7 days .............................. 207 xvii Plate 15. Scanning Electron Micrographs of (a) Bean and (b) Corn Starch granules microwave-heated at 70°C for 2 minutes .......................................... 210 Plate 16. Scanning Electron Micrographs of (a) Bean and (b) Corn Starch granules with conventional heating at 70°C for 2 minutes ....................................... 211 xviii INTRODUCTION Seeds of the annual legume (Phaseolus vulgaris L.), commonly termed dry edible beans, serve as the major alternative source of protein and calories in lesser developing countries (LDC's) of Latin America and Africa, and are also frequently considered for applications in world food relief programs in regions experiencing sustained crop failure. Although per capita bean consumption is significantly much less in developed countries compared to LDCs, it is projected to increase due to focused dietary recommendations as well as diet and health positioning currently presented by health authorities. Dry bean fiber is now being promoted as the "Fiber of the 90's" due to potential hypocholesterolemic and hypoglycemic effects . Major constraints still limit wider dry bean utilization. Biological or nutritional concerns include antinutritional and flatulence factors which interfere with protein digestibility and bioavailability of minerals. The preference for convenient and fast foods in industrialized economies also presents a major drawback to consumer utilization of beans due to the excessive time and expense involved in their preparation. Thus, the technological challenge is to develop highly digestible, preprocessed, prolonged shelf-life food products 'and ingredients from dry edible beans with minimum process inputs and appropriate technologies. The World Health Organization (WHO) and the United Nations International Children and Educational Fund (UNICEF) which have been promoting and supporting appropriate "complementary" or "weaning" feeding practices in LDCs, have encouraged the use of indigenous food resources such as dry beans. Dry edible beans therefore possess potential in the development of improved, low-cost weaning food 2 formulations, which could alleviate protein and energy malnutrition in young children. This dissertation was conducted in conjunction with the Bean/Cowpea Collaborative Research Support Program (cusp) of coordinated projects in Africa and Latin America focusing on removal of constraints to the production and utilization of beans and cowpeas. The program is funded by a Title XII grant from the United States Agency for International Development (U SAID)/BIFAD with the ultimate goal of reducing hunger and malnutrition in developing countries. In many of the countries where beans and cowpeas are staple foods, responsibility of production and preparation for family consumption rests with women and children. It is envisioned that village-level food centers, possibly managed by cooperatives, could centrally process locally produced raw materials such as dry edible beans into nutritious foods which can be distributed through day-care centers, school lunch programs and nutrition intervention clinics. Such a strategy will not only benefit infants, young children, pregnant and lactating women, but will also serve as an activity which will directly involve women in management and employment enterprises. The purpose of this research was to investigate possible processing strategies which will reduce antinutritional and digestibility factors, as well as decrease the time involved in the preparation of dry beans. Individual studies were conducted to address specific hypotheses associated with the objectives, and are discussed in three Chapters. Chapter I (Studies [-1 and I-2) involved the development of shelf-stable drum-dried bean meals which possess potential in preparation of improved weaning food formulations. The effects of different extractive pretreatrnents (hot water, steam and enzymatic ) on drum- dried bean meal composition and digestibility were evaluated in-vitro. ther, the feasibility of the use of germinated sprouted dry beans to serve as an indigenous source of enzymes was investigated. Chapter 11 (Studies II-l, II-2 and II-3) was undertaken to characterize the functional properties of the drum.dried bean meals and to evaluate their performance in selected food systems (quick bread and weaning food beverage). Chapter 3 III (Studies III-1 and 111-2) was conducted to assess the feasibility of using microwave energy as a preconditioning treatment to reduce cooking time of dry beans. The physical properties of isolated bean starch during microwave heating and conventional cooking were further compared in this study. REVIEW OF LITERATURE CHEMICAL COMPOSITION OF DRY EDIBLE BEANS (Phaseolus vulgaris) Although dry edible beans clearly differ in size and seedcoat color, there is a very basic commonality among commercial classes (navy, pinto, dark and light red kidney, Great Northern, pink, cranberry and black turtle soup beans). The compositional components of dry edible beans including protein, starch, fiber and minerals are generally very similar among these classes of dry beans (Figures 1, 2, 3 and 4). Further, the total dietary caloric energy derived from different bean classes is identical (Figure 5). Dry beans are of lower caloric value than soybeans (Glycine max L. Merr.) and peanuts (Arachis hypgea L.), both of which contain significantly higher amounts of lipids. These data (Table 1) are compiled from a major USDA funded analytical screening project and represent numerous sampling points of raw edible beans. It is most evident that only minor variations in each component exists among the diverse bean types presented. Thus, the interchange or substitution of different bean types within a major seedcoat class in recipes which require milling, mashing or mixing can be readily accomplished without dramatic functional or nutritional consequences (Uebersax and Occefia, 1991). An outlined overview of the major constituents is provided to specifically delineate and to further demonstrate the similarity in composition among different commercial classes of dry beans. Carbohydrates The total carbohydrates of dry legumes range from 24.0% in winged beans to 68.0% in cowpeas (Reddy et al., 1984). Starch constitutes the most abundant legume COMMERCIAL CLASSES Cranberry I G. Northern I Black Beans fl .\ '. - \\\‘ . ~‘v ‘..'.\.\. \ ' . — Kidney D Navy I Pink E Pinto - \\\\V lilillilllllllpliiiiiiliiIIHIHIIIIHHHEIHIH:IiiilIHHliiliilliilviiiililil[illilliHillilliiii:llllliilllIillllllllllllllllllI WWW ”- Fat m zrnnnnnuuuunuunuuuunun — .I ' ("F.V'F. . Illlilihlililililllil — C. Flbr. D. F lbr. Ash Tot CHO Protein Moisture Figure l. Proximate composition of selected raw legumes (Phaseolus vulgaris) Source: Uebersax and Ocean. 1991 \\\\\\\\\\\\V Black Crberry G.North. Kidney Navy Pink Pinto Figure 2. Macro-mineral content of selected raw legumes (Phaseolus vulgaris) (SamUebaxumemlWl) 20 D Sodium I Zinc Cl Manger“ H Copper I Iron 8 10" ‘\\‘\\\‘ °_ '2: I I5? I; I; I: I: Crberry G.Nor1h. Kidney Navy Pink Pinto Figure 3. mac-mineral cmtentof selected raw legumes (Phaseolus vulgm's) MUMMMIQI) i ., rll. ...... m m m m m m m m m. m m m I I I I U I E m 1%. m .... m s M m Niacin ..................... legumes (Phaseolus vulgaris) 82 Figure 4. 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Among the sugars, oligosaccharides of the raffinose family (raffinose, Stachyose, verbascose, and ajugose) predominate in most legumes and account for 31.1% to 76.0% of the total sugars (Akpapunam and Markakis, 1979; Kon, 1979; Rockland et al., 1979; Ekpenjong and Borchers, 1980; Reddy and Salunkhe, 1980; Fleming, 1981 and Sathe and Salunkhe, 1981). Walker and Hymowitz (1972) found that the sugar content ranged from 4.4% to 9.2% in 28 varieties of Phaseolus vulgaris. Sucrose accounted for 46.4% of total sugars present, while rafftnose and Stachyose made up 10.4% and 43%, respectively. The predominance of a particular oligosaccharide depends on the type of legume. For example, Stachyose represents the major oligosaccharide in most varieties of Phaseolus vulgaris while verbascose is the major oligosaccharide in black gram, red gram, mung bean and broad beans (faba beans); raffinose is present in moderate to low amounts. Starch. Variations in reported starch contents (24-56%) are partially due to differences in cultivars and analytical procedures. The physimhemical properties and internal molecular structures of bean starches differ depending on the original source, maturation and environmental factors. Most bean starch granules have wide variability in size (1-80 u) and shape which could be due to genetic control and seed maturity. For dry beans, a wide variability in shape (oval, oblong, round) is found in starch granules from the same source (Reddy et al., 1984). Biliaderis et a1. (1979) reported that the major portion of legume starches have molecular weights higher than 2 x 106 kd , and over 90% of them have molecular weights above 4 x 104 ltd. Amylose contents ranging from 10% to 66%, may influence starch solubility, lipid binding, and other functional properties. Biliaderis et al. (1981) fractionated legume starches and reported that the variability between amyloses from different legumes may be due to: l) maturity of seed, 2) genetic control of amylose synthesis, 3) cultivar l O differences, and/or 4) seed storage history. A high degree of amylose polymerization may confer structural stability to the granule but may also be partially responsible for its resistance toward in-vitro alpha-amylolysis. Most legume starches have gelatinization temperatures of 60°C to 90°C and are characterized by no distinctive pasting peak, but rather, a very high viscosity which remains constant or increases during cooling. The crystalline nature of the starch granule manifests birefringence (exhibited by the appearance of a "Maltese cross" under polarizing light) which is lost when starch is completely gelatinized. Indigestible or resistant bean starch and its possible role in flatulence is an area of interest in bean fiber research (Thompson et al., 1987 ). Lai and Varriano-Marston (1979) indicated that bean starch had lower swelling power than wheat starch within the temperature range 60°C to 74°C; however, above 75°C, bean starch surpassed wheat starch in swelling power. The restricted swelling, plus the single-stage swelling pattern, have been interpreted to explain the crystalline (ordered) and amorphous (unordered) regions of starch granules and the presence of strong binding forces which relax within a temperature range. The restricted swelling characteristics are similar to those shown by chemically cross-linked starches (Schoch and Maywald, 1968; Lineback and Ke, 1975; Vose, 1977; Lai and Varriano-Marston, 1979; Naivikul and D'Appplonia, 1979; Li and Chang, 1981; Sathe and Salunkhe, 1981). According to Schoch and Maywald (1968), these restricted swelling pastes are classified as Type C starches which show no pasting peak, but rather possess a very high viscosity which remains constant or increases during cooling and have relatively constant cold-paste viscosity during a holding period at 50°C. An important feature of dry beans is their relatively high content of non-starch polysaccharides (N SP), and their reported hypocholesterolemic and hypoglycemic efi‘ects. Although in general beans contain slightly more insoluble than soluble fiber, they are rich sources of soluble NSP, particularly in comparison with cereals grains. Cellulose is the major component of fiber in smooth and wrinkled peas, red kidney and navy beans, while 11 in other legumes (lupins, lentils and broad beans), hemicellulose is the major component. Cotyledon cell walls contain higher levels of pectin than cellulose. The seed coats are primarily composed of cellulose (29 - 41%) with small amounts of lignin (1.2 — 1.7%). Total dietary fiber is higher in cooked beans than in raw beans. Water-soluble fractions can be lost with cooking water even though the beans are intact, while long boiling may cause modifications in certain constituents of other fiber fractions. Proteins Dry bean (Phaseolus vulgaris) protein content ranges from 18.8 to 29.3% (Meiners et al., 1976; Varriano-Marston and De Omana, 1979; Hosfield and Uebersax, 1980 and Chang and Satterlw, 1982). Koehler et a1. (1987) investigated thirty-six varieties of eight types of dry beans for protein content (kjeldahl nitrogen) and protein quality (digestibility) as determined by Tetrahymena pynformis on the raw bean flour. There was a great deal of variability among different commercial classes of Phaseolus vulgaris and also among cultivars within a class. The amount of protein ranged from 17.5% for the Pinto (cultivar NW-590) to 28.7% for the red kidney (cultivar Royal Red). Except for kidney beans, there was little varietal difference in protein content. Pinto beans had the highest protein quality with six varieties having values of 90 % or greater and the remaining having values of 80 % or greater. Red kidney beans had the lowest protein quality with a mean value of 59%. The proteins in beans can be classified into two categories: metabolic and storage proteins. The storage proteins tend to be found in the globulin fractions (salt soluble Gl ) while the metabolic (enzymatic or non-storage) proteins are primarily found in the (water soluble GZ) albumin fraction (Deshpande and Nielsen, 1987; Nielsen, 1991). The storage proteins have high affinity for water and contribute dramatically to the nutritional and functional properties of the cooked seed (Boulter, 1981). They also serve as a source of nitrogen and carbon compounds for the germinated seedling. 12 Total biological utilization of the legume protein is relatively low. Protein digestibility may be impaired possibly by the presence of numerous anti-nutritional compounds which must be removed or destroyed during processing (Bressani et al., 1982 and Aw and Swanson, 1985). Raw legumes are poorly digested, but adequate heat treatment improves the digestibility significantly. However, in many parts of the world. the thermal treatment provided for bean preparation in the home setting is not sufficient to inactivate toxic phytohcmagglutinins (lectins), but is often just sufficient to heat and hydrate the beans (Coffey et al., 1985). Gomez-Brenes et a1. (1975) reported that peak digestibility and Protein Efficiency Ratios (PER) of dry P. vulgaris were obtained after soaking for 8 or 16 hours and cooking at 121°C for 10 to 30 minutes. Heating for longer than this resulted in lowered protein quality and decreased available lysine. Bean proteins have been reported to be resistant to in-vitro enzymatic digestion (Satire etal., 1981; Bressani, 1975); however, heating improved in-vitro susceptibility to enzymatic hydrolysis (Sathe et al., 1982). Bean proteins are relatively rich in essential amino acids, particularly lysine, threonine, isoleucine, leucine, phenylalanine and valine (Sathe et a1. 1981; Bressani, 1975). However, they are deficient in sulfur-containing amino acids, particularly methionine and cystine. This explains their complementation with cereal grains (deficient in lysine) in plant-based diets. Besides their low content, the bioavailability of the sulfur- containing amino acids is also quite low even after cooking (Liener and Thompson, 1980). Minerals and Vitamins The total ash content of P. vulgaris ranges from 3.5% to 4.1% (db) (Table 1). Beans are generally considered to be substantial sources of calcium and iron. They also contain significant amounts of phosphorus, potassium, zinc and magnesium (Augustin et al., 1981, Koehler et al., 1987, Meiners et al., 1976, Watt and Merrill, 1963 and Sgarbieri et al., 1978). Differences among bean classes (Figures 2 and 3) and environmental factors l3 influence variability (Augustin et al., 1981). Ash content decreases after cooking due to leaching, with losses ranging from 10 to 70%. The wide range of reported losses could be due to different soaking and cooking methods. Although dry beans are relatively rich sources of some minerals, high mineral values cannot be equated with high bioavailability of some of these minerals because of the presence of significant amounts of phytic acid (myoinositol hexaphosphoric acid) which impedes the absorption of multivalent cations, e. g. calcium, magnesium, zince and iron (Augustin and Klein, 1989). Dry edible beans provide several water soluble vitamins (thiamine, riboflavin, niacin and folic acid), but very little ascorbic acid. However, variability of vitamin content is high. Both genetic and environmental factors, e.g., storage time and conditions as well as differences in analytical methodologies could attribute to the variability among these reported values (Augustin and Klein, 1989). Commercial methods of preparation of canned beans cause a significant loss of water soluble vitamins. The mineral and vitamin composition of dry beans are summarized in Figures 2,3 and 4 and Table 1. These data further demonstrate the compositional similarity among various dry bean classes. Lipids Dry beans possess relatively low total fat content, generally 1-2% (Korytnyk and Metzler, 1963 ; Koehler and Burke, 1981; Sathe and Salunkhe, 1981; Drum et al., 1990). Neutral lipids are the predominant class and account for 60% of the total lipid content. Phospholipids make up 24-35%, while glycolipids account for up to 10% of the total lipid content of legume seeds. The fatty acid composition of legumes shows a signifith amount of variability. However, legume lipids are generally highly unsaturated (1% to 2%), with Phaseolus vulgaris containing 63.3% (Watt and Merrill,l963; Takayama et al., 1965), hence the storage of legumes can result in a loss of quality, 14 nutritional value and functionality. Unsaturated linolenic acid ispresent in the highest concentration, while palmitic acid is the predominant saturated fatty acid. Tannins and Polyphenols The procyanidin and condensed tannin content of dry beans ranges from 0.4 to 1.0% (Sgarbieri and Garruti, 1986). These compounds are localized in the bean seed coat with low or negligible amounts present in the cotyledon (Ma and Bliss, 1978). The hydroxyl groups of the phenol ring enable the tannins to form crosslinks with proteins which may be implicated in post-harvest seed hardening or decreased digestibility (Ma and Bliss, 1978). During cooking, polyphenolic compounds are partially leached into the cooking medium and may interact with cotyledonary constituents, yet complete destruction of the tannins does not occur during heat processing (Elias etal., 1979; Bressani and Elias, 1980; Bressani et al., 1982). According to Leakey (1988), some colored seeded beans also produce particular flavonoids, proanthocyanidins, which polymerize to form phlobaphenes implicated in the afterdarkening process with seed storage (aging). Afterdarkened beans resist water inhibition, become hard-to—cook and are less digestible than freshly harvested seeds. Bean Flavor Constituents Native Flavor Precursors. The development of the characteristic flavors of dry beans accompanies heat treatment, with non-enzymatic browning (Maillard) reactions contributing significantly to the formation of numerous flavor compounds. The formation of Maillard reaction products has been shown to be influenced by the temperature of the reaction and the amine and carbonyl source (Hodge, LE. and Hofreiter, B.T., 1972). Oxidative degradation, catalyzed by heat, enzymes, light or metals, leads to the formation of hydroperoxides which decompose to react with other components in the system to produce off-flavors. 15 Ofi-flavor. Phenolic acids are localized in the cotyledon of the bean. These compounds are characterized by sour, bitter, phenol-like, and astringent flavor notes, and contribute to the formation of adverse flavors and colors, and changes in nutritional quality during processing (Sosulski, 1979). Saponins are present in dry beans and are present following processing. These compounds are suspected of causing bitter off-flavors and may be associated with frost damaged seed. Further off-flavor development during post-harvest storage has been associated with mold growth (Uebersax, M.A. and Bedford, 1980; Maddex, 1978). All dry beans posess remarkably similar compositional and nutritional characteristics and serve well to supply energy and nutrients in diverse dietary forms. The associated common traits of dry bean have practical applications commercially for cormninuted or formulated foods, and in developmental world food relief programs. NUTRITIONAL DIGESTIBILITY AND PHYSIOLOGY OF DRY EDIBLE BEANS Dry legumes are important dietary sources of protein, complex carbohydrates, essential nutrients and energy. However, legume protein is generally less digestible than protein in grains and animal products (Tobin and Carpenter, 1978; Wolzak, Elias and Bressani, 1981; Wolzak, Bressani and Gomez Brenes, 1981). Table 2 and Figure 6 summarize the major constraints to utilization of dry edible beans (Uebersax et al., 1991). The relatively poor digestion of legume protein limits the biological value of the protein and reduces the overall contribution of legumes towards providing a nutritionally well balanced diet. Bean starch, the main component of dry legumes, is digested at a slower rate than starch from grains and root crops (Thompson et al., 1987). Protein digestibility is expressed in terms of calculated responses related to body nitrogen balance. "True" digestibility gives consideration to the component of the fecal nitrogen originating from the body (mucosal cells of the gastrointestinal tract and digestive enzymes) or endogenous N, while "apparent" digestibility considers only the relationship between total fecal N and total dietary N. The relationships of absorption, retention and digestibility are shown diagrarmnatically in Figure 7. Factors Affecting Digestibility of Dry Legume Starch and Protein. A factor that affects digestion of legume protein and starch is the physical form of the protein and starch when it enters the stomach and small intestine. Grains and root vegetables are usually ground and/or cooked prior to consumption. Grinding and cooking serve to break the cell structures and to release the protein and starch so that proteolysis and amylolysis can occur. Legumes are generally consumed as whole seeds that have been cooked. Cellwallstructuresincookedbeansareintactandsunoundtheproteinbodiesand starch granules. Chewing rrracerates sorrre of the cells, but most of the cells remain whole 16 l7 Tablez- CominljminngUfinnonofDryBe-n Constraints PHYSICAL Reference 0 Preparation (time, convenience and expense) Usher-uni . Post Harvest Stora e Changa (seed hardening)g BIOLOGICAL . Anti-nutrients - pretense inhibitors end lectin: - enrylnee inhibitors - procyanidin lnlencdone - Digestibility 4am.- acid - protein - elerch . Flatulence Factors - oligosaccharides - protein: - retrograded starch .Mr W 0989) Sofa-Dada: a II. (1979); Vern-rem nd Jar-hat (1981); Stanley and Ann- (1985): Shauna n M1989) Lin-u I. 8.0978); 'lbanpeon n al.(1983. 1986) June at al.( 19») Cdey a a1. 0985) laflen £11973); Pom. J. R. and Whitaker. LR.( 1977): Pick. LE. and Weber, G. (1979) Bressani ad. (1982) Map (1982): Your 6 IL (1983) Wolzak a a1. (1981); Chat, LC. and L D. Sundae (1981); Emmi a al. (1982) Cdfey a :1. (1985) “had. (1937) How, I. and F. Saulaki (1985); Harpoon a :1. GM); Bellini all Srieune (1989);Tover a aL(l990); Englyn nd Cunning (1990) WY¢¢ (1972); Plain (1981ng Olsen net. (1981) m (1971) Brian, RN. and LH. My (1990) Helm (1978); Planing (198le Reddy n nL. 1934 18 ”52. E. s 253:: ..o $523383 23 EEEomB ”583:5 «88.: ”ENEEEE 2550 .e 2:3..— oEF 9.380 «:3 . .83.: ~33~em 35:35.5 ..BE . 39:63 8.33.— . mz_2<.=> a m4555 23E Alrlt 2.52: map—.05— JP—a—E<‘=<>SO _ Ebu EC! Ail—Mal. JIIIJITTciUMIT-IJII 135$?ljci1 is G28; 0.3.3.53 8.— . 1"! 1.1....11rlqlslrl1r. 3.11.1.1] 11.1.3. ’ i — P — i S! .1 nu. . I 566.965 1.1 02—38: 2:- >5— 46 could thus be devoted to more effective child care or additional income-generating activities. Drum-dried bean meals possess potential for pre-cooked, prolonged shelf-life weaning food formulations which can provide both protein and energy to the infants as well as offer preparation convenience for mothers. The demand for convenient food items has resulted in specialized pre-processed food products and ingredients from dry edible beans, possessing diversified functional properties which may be used directly, or utilized as a component of formulated foods (Uebersax et al., 1991). The technological challenge presented is to achieve these improvements within the scope of minimum process inputs and appropriate technologies. Potential increased consumption of novel bean products is dependent on the individual processing economics associated with the specific product. Bean Sprouts, Curtis and Ferments Utilization of legumes in LDC‘s still entail long and tedious preparation procedures. However, traditional methods of legume preparation, such as germination and fermentation, have found wide acceptability in Afiican and Asian countries for their potential in improving digestibility and reducing antinutritional factors. Germination and fermentation have been reported to reduce phytic acid which interferes with protein digestibility and mineral bioavailability (Rao and Belavady, 1978; Silva and Luh, 1979; Sathe and Salunkhe,]982) and oligosaccharides which have been associated with flatulence (Rackis et al., 1970; Calloway, et al., 1971; Murphy et al., 1972; Rao and Belavady, 1978 and Fleming, 1981). Enzymatic treatment of beans have also been reported to remove much of the oligosaccharides (Calloway et al., 1971). Germination results in at least a ten-fold increase in phytase activity and a simultaneousdecreaseinphytate,andifdonecarefully,thebean seedcanstillbeusedfor cooking in the customary manner (Reddy et al., 1978). Sprouting was found to increase the digestibility coefficient of red kidney beans from 29.5% in the raw to 66.4% in the 47 cooked kidney bean. Nielsen and Liener (1984) reported a thiol protease with an acid pH optimum to be responsible for the disappearance of the major storage protein, 01, during germination. During the process of sprouting, enzymes released from the embryo hydrolyze portions of the linear and branched starch molecules into short-chained dextri- maltose which does not swell when cooked into a gruel (Ebrahim, 1983). Sprouted grains may also be consumed fresh or when followed by seed coat removal, can be roasted or ground for use in soups or side dishes. Soybeans are fermented to produce a variety of nutritious Oriental food products including tofu (calcium precipitated curd), natto, misc, tempeh, shoyu and tamari. Indian fermented delicacies like idly and dosa can be prepared from black gram (Phaseolus mango); dhokla and khaman utilize Bengal gram (Cicer arr'etr'nwn). 'Dhal' is prepared by cooking beans until soft, mashing, mixing with water, then boiling to yield a homogeneous gruel. They can also be cooked with vegetables, spices and condiments. Roasting and puffing of dhal and whole seeds to improve flavor and maintain maximum protein quality involve the application of dry heat (100°C to 200°C) for a short period (1-5 min). Dry beans and other legumes could be prepared by methods which include protein and production or fermentation to improve quality and digestibility. Swanson and Raysid (1984) found that there was a significant increase in protein digestibility and PER in tempeh made from red beans (P. Vulgaris L.) and corn. Further research is needed to assess the potential of Phaseolus vulgaris in fermented foods. Bean Meals, Flours and Powders Beans may be consumed as whole cooked seeds where seed distinctives are readily perceived by the consumer, or as cornminuted meals, pastes or curds where seed integrity is lost and the functional properties are a direct function of the seed components and their interaction with waterandheat. Inproductsutilizingbeansin milledormashedforms,the consumer may not readily discern the bean type (Uebersax and Occeiia, 1991). High 48 protein food ingredients can be produced as either flour processed by pin milling & air classification, or as concentrates and isolates processed by alkali, salt and acid extraction with subsequent use of isoelectric precipitation or ultrafiltration (Uebersax et al., 1991). Chang and Satterlee (1979) produced bean protein concentrates containing 72% and 81% protein by wet processing using water extraction techniques. Dry beans have been milled into whole flour and air-classified into high starch and high protein fractions (Kon,l979; Ekpenyong and Borchers, 1980; Reddy and Salunkhe,1980; Aguilera et al., 1982 a and b). High protein flour fractions generally contain twice the original whole bean seed protein content. Bean bulls are readily separated by cracking rolls and air aspiration and then milled into a high fiber fraction. Air classification of roasted beans produced high fiber, starch and protein fractions, each suitable as food ingredients in a variety of food products such as cookies, doughnuts, quick breads and leavened doughs (Defouw, et al., 1982; Dryer et al., 1982; Zabik et al., 1983; Uebersax and Zabik, 1986). Instant precooked bean powders have also been prepared by soaking, cooking, slurrying and drum or spray drying of edible beans (Bakker, 1973). Functional Characteristics and Applications. Much research has been conducted to investigate the functionality of high protein bean products to broaden their use in various foods. Air-classified high protein bean flour contains a residual starch which offers some particularly desirable functional applications. Lee et al. (1983) reported that wheat flour substituted with 10% navy bean fractions (whole, hull and high protein and starch ) resulted in increased water absorption and decreased mixing performance. Whole bean flour and high starch flours produced viscous solutions with controlled swelling at high temperature. Bean slurries remained stable during high temperature holding, and upon cooling, showed moderate increase in viscosity, indicating a tendency toward association of starch molecules. Zabik et al. (1983) demonstrated that dry roasted air-classified navy 4 9 bean protein flours substituted for 10% bread flour exhibited increased water absorption but decreased arrival and peak times of the flours processed with increased roasting temperature. Mixing stability of the flours showed a decreasing trend as the bean/bead ratio and roasting time increased. Lorirner et al. (1991) studied the effect ofprime and cull navy bean high-protein flours on rheological parameters and microstructure of composite doughs. Composite flours with increased protein exhibited the expected increase in absorption, delay in arrival and peak time and reduction in stability. The microstructure of composites with cotyledon flour from culled beans showed slightly greater gluten disruption than was evident in the doughs prepared from the wheat-prime cotyledon composites. Kohnhorst et al. (1990) reported that navy and kidney bean flours formed significantly higher volume foams but had lower foam stability compared to soy products at pH 6.5, possibly indicating compositional or structural differences between the proteins. The emulsion capacity, gel strength and foaming properties of navy and kidney bean flours were similar and were significantly higher than that of soy flours. Navy bean flours substituted for wheat flour in baked products such as pumpkin and banana breads and fiied "doughnuts holes" increased protein quality and quantity since they are relatively high in lysine. Dry roasted navy bean flour incorporated into pumpkin bread increased tenderness because of the reduced gluten formation and of the diluted nature of the gluten. Volume decreased with increasing levels of bean flour substitution because of decreased gluten formation. The pumpkin bread with bean flour was darker than the control made from wheat flour because of increased reducing sugars in the navy bean flour, promoting Maillard browning. Pumpkin bread containing 35% navy bean protein substitution appeared to be optimum and contained about 25% more protein than the control (Dryer et al., 1982). Extruded navy bean flour incorporated at either 20 or 35% level of substitution produced acceptable quick breads (Kane et al., 1991). Doughnuts with 13% bean substitution had less fat, were softer and showed less firming 50 after 6 days storage compared to control doughnuts and other bean substitutions (Uebersax et al., 1981 and 1982). Raised doughnut holes prepared at a 25% navy bean protein florn' substitution level exhibited greater tenderness than did the wheat flour control (Zabik et al., 1983). Volume and crumb color of bread were not adversely affected at a 10% bean protein substitution, and raised the protein level by 20% (Zabik et al., 1983). Silaula et al. (1989) reported that dry-roasted navy and pinto bean high -protein fractions blended with bread or whole wheat flour increased tenderness and reduced lightness of breads. Substitution of legume flour for bread or wheat flour dilutes the gluten and interferes with the formation of a well-defined protein-starch complex. Substitution of 5 and 10% high- protein flour for bread flour increased absorption and lengthened arrival and peak times in farinograph studies but decreased dough stability, causing a faster rate and greater magnitude of breakdown ( Lorimer et al. 1991). Navy bean flour incorporated into Chinese steam bread decreased volume but increased tenderness with increased bean substitution (Uebersax and Zabik , 1983 ). DeFouw et al. (1982) reported that navy bean hulls incorporated into sugar-snap cookies resulted in less acceptable interior color as the level of hull substitution increased. Texture was not significantly affected by less than 30% substitution with unroasted or moderately roasted hulls. Flavor, top grain and spread were adversely affected as the level of substitution increased. Navy bean protein substitution for wheat flour increased water holding capacity and cookie tenderness, but decreased cookie spread slightly (Zabik et al., 1983). Breads prepared with wheat flom' blend (10% pinto flour) had a slight decrease in volume, while those with bread and pinto flour blend had fewer differences in volume and tenderness (Uebersax and Zabik, 1986a and b). Noodles produced with pinto bean flour at % wheat substitution were more tender and slightly darker, with decreased flavor and acceptability as substitution level increased (U ebersax and Zabik, 1986). 51 Numerous studies assessing the funtional characteristics of other legume flours have been conducted. For instance, heat processing of winged bean flour have been observed to lower nitrogen solubility, emulsification and foam capacity, but increased water and fat absorption capacity (Narayana and Rao, 1982). Sathe and Salunkhe (1981) reported that Great Northern bean flour had lower oil and water absorption capacities compared to those of soybean and sunflower flours. Emulsion capacity and stability of the flour was the lowest compared to those of the protein concentrates and isolates and albumin and globulin proteins. Drurrr - Drying of Legumes. Drum drying of dry beans into precooked flakes and powders could be used to produce ingredients suitable for convenience foods or replacements for cooked bean purees or refried beans. Drum-driers have high drying rates and high energy efficiencies, and are suitable for slurries in which the particles are too large or thick for spray drying. Bakker et al. (1967 and 1969) produced instant pea bean, pea and lentil powders using a modified single-drum—drier. An acceptable drum-dried infant cereal using banana (40% dw), rice (10.5% dw) and soybean (16.5% dw)was developed on a commercial scale to supply the needs of the Costa Rican Program for Food and Nutrition aimed at children under age 2. The process consisted of the following steps: 1) cooking the soybeans at 121°C for 30 minutes; 2) boiling the rice for 5 minutes to gelatinize the rice starch; 3) inactivation of the banana enzymes by boiling with the rice and soybeans for 3 minutes, and 4) drum-drying to 5% moisture (Lastreto et al., 1986). W A basic drum dn'cr. as illustrated in Figure 10, is comprised of one or more hollow steel drums (rollers) which slowly rotate and are heated internally by pressurized steam to 120-1700C. Drum-driers use conduction heat transfer; condensation of the steam inside the drum provides energy 52 HQ 0 G" . L Figure 10, Schematic Components of a Double Surface Drum-Drier: A - Steam- Heated Drums; 3, C - Slurry “Feed and Puddle”; D - “Nip"; E - Dehydration Surface; F - “Doctor” Blade (knife); G - Dehydrated Sheet; H - Conveyor; l - Vapor Hood. 53 for vaporization of water at the external drying surface ( Batty and Folkman, 1983). The drum are mounted to rotate about the symmetrical axis. A feeding device is used to apply a thin, uniform layer of food material to be dried on the hot cuter sm'face. There are a variety of methods for distributing the stock feed over the surface, including a) dipping, b) spraying and c) spreading or use of auxiliary feed rollers. Before the drum completes one revolution (within 20 secs to 30 mins.), the feed material applied on the periphery is dried as the heated drum rotates toward the 'doctcr' blade (knife ) which contacts the drum surface uniformly along its length, and scrapes the thin layer of dry material from the drum surface. Drum driers are classified as single-drum, double-drum, or twin—drum systems. A single-drum drier has only one roll while a double-drum drier has two rolls which rotate toward each other at the top. The two parallel drums of a twin-drier may either rotate toward each other or away from each other at the top, and are not spaced close together (Harper, 1979). The single drum is widely used as it has greater flexibility, a larger proportion of the drum area is available for drying, easier access for maintenance and no risk of damage caused by metal objects falling between the drums (Fellows, 1988). Was, Therearefourbasicdrumdriercontrols inan atmospheric double drum drier; these include : a) puddle level, b) drum speed (rpm), c) steam pressure and d) drum clearance ("nip"). The speed of the rotation is adjusted so that the desired moisture is obtained when the product is scraped off the drum (Batty and Folkman, 1983). Other control points of the drum—drying process include initial solids content, feed rate and drum-drier temperature. A typical commercial single drum dryer has the following dimensions: 1.65 m in diameter and 4 m long. The drums are run at about 8 to 9 atm. steam pressure (115-135 psig) with surface temperature of about 240°C. The rotation speed of the drums is 3.5 to 4 rpm and the effective drying surface 31 m2. . Pretreated slurry is pumped through a tangential steam heater where starch is fully gelatinized. The hot slurry enters the flash tank which serves as a surge reservoir for 5 4 uniformly supplying slurry to the drum drier. Following application and dehydration, the thin continuous sheets of dried beans falling from the drier knives is broken by a screw conveyor and the resultant flakes collected are passed through a Fitzpatrick comminuting mill to provide uniform particle size. Developments in drum design to improve the sensory and nutritional qualities of dried food include the use of auxiliary rolls to remove and reapply food during drying, the use of high-velocity air to increase the drying rate or the use ofchilled air to cool down the product. Drums may be enclosed in a vacuum system to dry food at lower temperatures which is especially suitable for high-value heat-sensitive food products (Fellows, 1988). Thermal Extrusion High starch navy, pinto and black bean flour fractions yield good expansion properties during high pressure and high temperature extrusion (Zabik et al., 1983b; Aguilera et al., 1984). When the cooking and extrusion processes are combined, the increased pressure differential will facilitate expansion and a final dry formed 'bean' particle which readily hydrates and softens when reconstituted is achieved. Die configuration can be designed to produce a variety of intricate product shapes which can be further Optimized to produce simulated beans. Appropriate binders and coating agents can be added to improve appearance of pre-ccoked or quick cooking bean products resulting in promising prototypes of extrusion cooked - formed 'beans' (Uebersax et al., 1991). Legume flours can also find application in extruded snack items, breakfast cereals, pasta products and infant foods. Extrusion of millet flour to prepare instant infant foods yielded a product that was much less dispersible ( d0% for millet flour at 85°C compared to >70% for corn starch at 35°C). Increased lipid and fiber contents of millet flour probably contributed to these observations. However, a similar decrease in soluble starch was observed in both materials when the extrusion moisture content decreased from 17% to 12%. More amylopectin was dispersed from the millet extrudate when the extrusion 55 moisture content was 13.6% and 15.0% (Waniska, RD. and Gomez, M.H., 1992). The formation of amylose-lipid complexes reduces the digestibility and water solubility of cooked starches (Galloway et al., 1989). Amylose in starch will complex with lipids during extrusion cooking. As starch in the presence of lipids is exposed to increasing amounts of heat and pressure, the amount of amylose-lipid complexing increases (Huber, 1991). Extruded navy bean and lentil flours substituted (20 and 35%) for all-purpose flour in pumpkin bread demonstrated the feasibility of extruded starchy legumes as food ingredients (Hartet al., 1991). Giese (1992) provided a review of new types of pasta developed from unconventional raw materials such as legumes. High temperature extrusion cooking allows added proteins such as egg albumen to form a coagulated network to improve pasta quality. Thin-walled macaroni formulations, incorporating durum wheat semolina with 15% and 25% drum-dried navy bean flour or 15% whole raw navy bean meal, have been successfully developed at Michigan State University (MSU) using a high temperature twin-screw extrusion cooker (Lin et. al., 1993). Borejszo and Khan (1992) reported lower levels (3.69%) of flatulence causing sugars (raffinose and Stachyose) in extruded pinto bean high starch fractions compared to non-extruded samples (5.29%) with higher reduction occurring at higher process temperatme (163°C). According to Chauchan et al. (1988), protein efficiency ratio values of extruded rice-legume blends (rice-soybean, 2.25; rice-bengal gram, 2.30 and rice- black gram, 2.28) were improved compared to the respective raw blends (2.10, 1.89 and 1.98 respectively). They also demonstrated that extrusion processing reduced the phytates in the products to the extent of 20.3% to 26.8%. Ummadi et a1. (1993) determined the effect of low and high impact extrusion processing on iron dialyzability, forms of iron, tannin content and degradation of phytic acid in navy beans, chickpeas, cowpeas and lentils. Dialyzable iron increased following low impact extrusion in all the legume products, but only in navy beans with high impact extrusion. Low impact extrusion 56 resulted in increased total soluble and ionic iron. However, high impact extrusion did not result in any change in total soluble iron but increased ionic iron in cowpeas and lentils. Degraded phytate products increased to 51-71% in extruded legumes. Tannin content decreased with low and high impact extrusion. Microwave Heating of Legumes Microwave heating has a direct potential for use as a preconditioning treatment for common dry beans to reduce processing time, and to inactivate antinutritional factors (Uebersax et al., 1991). Mechanism of Microwave Heating. Microwaves are generated by a magnetron (a device that converts electrical energy at low frequencies) into an electromagnetic field with centers of positive and negative charges that change direction at a frequency of 109/sec. As microwaves enter the product, they interact with regions of positive and negative charges on water molecules, (electrical dipoles) that rotate the molecules in the electrical field by forces of attraction and repulsion between oppositely charged regions of the field and the dipoles. This results in the disruption of hydrogen bonds between adjacent water molecules and generates heat by "molecular friction" (Decareau, 1988; Mudgett, 1989; Giese, 1992). The molecules in the microwave paths oscillate around their axes in response to reversal of the electric field that occurs 915 or 2450 million times per second, creating intermolecular friction that results in the generation of heat (Cross and Fung, 1989). Food cooked by microwave involves heat generated from within the food through a series of molecular vibrations. In contrast, conventional heating methods transfer thermal energy from product surfaces toward their center 10 - 20 times slower than microwave heating (Mudgett, 1989). In developing products for microwave processing, it is important to recognize that microwaves are a form of energy, not a form of heat, and are only manifested as heat upon interaction with an aqueous material as a result of one or more energy-transfer mechanisms. 57 Microwave Effects on Food Composition Magnum. Greater losses in moisture in microwave-cooked compared to conventionally heated products could be due to a greater rise in post-oven temperature, causing more dehydration through evaporation and increased shrinking. Very few studies provided data on water content of foods prior to and following microwave cooking ( Schiffmann, 1988). Emma, Hafez et al. (1985) conducted experiments to determine in vivo protein digestibility and metabolizable nitrogen using male Sprague-Dewley rats. They observed that proper microwave treatment increased the digestibility of soybean. Optimum microwave heating time was around 9-12 minutes for 1 kg whole soybeans to improve weight gain, digestibility and intestinal proteolytic activity under experimental conditions maintained during the study. They also did not observe alteration of fatty acid composition of soy oil. 7 A study by Yoshida and Kajimoto (1988) showed that microwave heating might be effective in the inactivation of the trypsin inhibitor in whole soybeans. Microwave treatment of whole soybeans for 8-10 minutes after soaking to approximately 25% moisture would be optimal to prepare soyflour or soy grits without a burnt odor, and completely inhibiting trypsin activity. The loss of molecular species of soy triglycerides containing more than four double bonds in a triglyceride was less than that obtained from native soybeans prior to soaking (8.6% moisture). In an earlier study, Yoshida and Kajimoto (1986), found that microwave heating for about 5 minutes did not cause a loss of unsaturated fatty acids, nor did it change molecular species of soybean triacylglycerols. Susceptibility to heat processing has been observed with protein containing significant amounts of carbohydrates. Interactions between functional groups with the protein chain or between the protein chain and other food constituents during heating lead to cross-linkages which are resistant to normal digestive processes. 58 Overall, nutritional effects of microwaves on animal proteins appear minor, however, many studies have demonstrated that microwave heating may aid retention of total protein in foods (Decareau, 1986). For example, microwave treatment of potatoes favored protein retention over other preparation methods (boiling or oven-baked) investigated (Mudgett, 1982). W Overall, much work needs to be done on the effects of microwave heating on the carbohydrate fraction of foods. Aref et al. (1972) observed the inactivation of alpha-amylase in wheat flour after 60-second exposures to microwave energy without pronounced deleterious effects on the principal characteristics of the flour or the subsequently prepared doughs . The exposme also drastically reduced the number of viable organisms in the flow, but seemed to cause a relatively high loss in moisture. Microwave baking is usually done at 896 to 2450 MHz, the range also used in normal household ovens. The lower frequency is to be recommended in some cases, as this enables both higher penetration depth to be obtained and thus avoids the risk of the core not being sufficiently baked. The main problem of baking with microwaves is the lack of both crust formation and surface browning. This may be achieved by short-time conventional re-baking for about 4-5 min at a temperature of ZOO-300°C. Flour with a high alpha—arnylase concentration and low protein content have been used for dough preparation. In microwave baking, the entire loaf is heated rapidly, and the development of 002 and steam in the dough is accelerated, thus resulting in breads with a relatively high specific volume despite the low protein content The temperature range essential for alpha-amylase is reached rapidly, so that the amount of undesired decomposition products remain low. Microwaves are currently used for commercial leavening and proofing, thus enabling the process of gas development and adhesive formation to be completed within a 5 9 period of only 2-4 min. Microwave treatment might require changes in the dough recipe, leading to new final products. A lack of crust formation and differences in the color were observed in whole-grain baked products, and the microwave breads were tough and rubber-like (Schiffmann, 1988). The taste was less significant than that of conventionally prepared bread because the microwave products lacked both caramelization and development of aroma components. Loaf volume and crumb condition were not of the quality obtained in conventional bread production. The following are advantages of microwave baking: 1) provides a final product with a higher nutritive value than conventional baking, provided the same ingredients are used; 2) baking times are reduced to a few minutes - the entire baking process of a 1 -kg loaf only takes 7-8 minutes and 3) microwave equipment requires less space. Microwavable pasta and pasta made from a primary material other than wheat have been developed Strategies for improving pasta performance during microwave heating include modifying the wall thickness and adding selected ingredients such as egg albumen to assist shape retention. The increased protein content allows for the formation of polypeptide chains which interact to form a fibrillar network which subsequently entraps starch granules and slows gelatinization (Giese, 1992). Cabello et al. (1992) reported a highly acceptable precooked and dehydrated pasta suitable for microwave heating using 15% substituted navy bean cotyledon flour. The navy bean flour pasta had a richer yellow color which was favored over 100% semolina pasta. Microwave cooked legume pasta made from different levels of extruded drum-dried bean flour demonstrated higher cooked weight and was less firm than 100% semolina control pasta. Microwave preparation (740 watts, 5 mins.) also resulted in lower cooking loss than conventional cooking (100°C, 2 mins.) (unpublished data). 60 WE“ No general statement can be made flomreported literature studies regarding total fat in microwave versus conventionally prepared food products due to the differing procedlnes, conditions, and products used (Decareau, 1982). Industrial investigations of the function of fats, oils and emulsifiers in microwave food formulations reported fats/oils and emulsifiers to function optimally, and not to be chemically altered by microwaves (Durkee Foods Corporation, 1989). Emulsifiers interface with water, within the food matrix, due to the polar hydroxyl end of the emulsifier. This interaction may maintain moisture within microwave prepared foods. They also interact with proteins, starches, and gases such as air, further stabilizing and improving texture (Connerton and Shuleva, 1989). Fats/oils can function thermodynamically as a "heat source" to absorb energy, generate heat, and release heat to adjacent non-fat molecules of lower polarity. Lipids remain totally unchanged by the microwave energy, thereby aiding moisture retention within a product. Mina“ Investigation of some vegetables cooked by oven heat and in a microwave oven revealed negligible loss of water and minerals regardless of cooking method, although microwave heating was suggested to be superior to conventional heating since less nutrients were lost to the aqueous cooking medium. More recent studies showed that nutrient retention in his and vegetables was greater with microwave heating than with conventional heating due to less water-to-product ratio and consequent reduced leaching in foods cooked with microwave energy, therefore the microwave heating increased retention of nutrients. Specific studies like those of four potato varieties prepared by various home cooking methods and microwave cooking suggested that the latter enhances macro-nutrient retention. Mineral determinations for meat drippings showed significant differences of selected minerals (Na, Cl, P, Fe) from oven-roasted pork, beef and lamb drippings. It was suggested that the greater concentration of minerals in the drippings from 61 conventionally cooked roasts could be related to the lower moisture content of the drippings. Therefore comparisons of absolute mineral losses remain unclear. Wm, Studies have indicated that destruction of thiamine in food systems is primarily related to heat level rather than exposure to microwaves. Studies with pork, beef and lamb suggested that vitamin retention was not related solely to length of exposure to high temperatures. The contribution of vegetables to the riboflavin and niacin content in the diet is minimal, so few studies have investigated microwave effects on these components. Thereviewofmany selected studiesindicatedthat noappreciablelossesinascorbic acid were attributed to microwave heating compared to conventional heating methods. Any increased retention of ascorbic acid in microwave-cooked foods cannot be attributed entirely to the dielectric heating. A combination of factors including ratio of water-to- vegetable, cooking length, and variability of cooking loads may account for the variations in reported data (Harrison, 1980). Except for significant losses of Vitamin A in microwave-cooked meat, limited data on fat-soluble vitamins are available. Potential for Dry Edible Beans as Weaning Foods The Codex Alimentarius Commission (Food and Agriculture Organization/World Health Organization, 1976) prepared the official guidelines ”Recommendations for International Standards of Infant Foods." Dried products included in this section are based on cereals (wheat, rice, barley, oatmeal, rye, millet, corn, sorghum) and legumes (ex. soybeans) of low water content processed under conditions that allow their reconstitution withmilkorwater. Iftheproduct istobemixedwithwater,itisrequiredthattheprotein content be at least 15% (db) and protein quality at least 70% of casein value. The addition of protein concentrates, isolates and essential amino acids is allowed only in concentrations 62 needed to meet these criteria. Supplemental sugar and fruit addition is also allowed under these guidelines. The Thirty-fourth World Health Assembly of the World Health Organization (1981) adopted the "International Code of Marketing of Breast-milk substitutes” in the form of a recommendation which aims to protect and promote breast-feeding and ensure the proper use of breast-milk substitutes when these are necessary to ensure adequate nutrition. The Code defines "Infant formula" as a breast-milk substitute formulated industrially in accordance with applicable Codex Alimentarius standards, to satisfy the normal nutritional requirements of infants between four and six months of age, and adapted to their physiological characteristics. Infant formula may also be prepared at home, in which case it is described as "home-prepared" formula. "Weaning food" or "complementary food" are defined as any food, whether manufactured or locally prepared, suitable as a complement to breast-milk or to infant formula, when either becomes insufficient to satisfy the nutritional requirements of the infant. Such food is also commonly called as "breast-milk supplement" (WHO, 1981). WHO and United Nations International Children and Educational Fund (UNICEF) promote and support appropriate and timely complementary (weaning) feeding practices, usually when the infant reaches four to six months of age, and further encourage the use of locally available food resources. In LDCs, research efforts on weaning food formulations have focused on the utilization of indigenous or locally-available protein-rich foods such as legumes and oil seeds. Digestibility and flatulence-producing components are important factors to consider when feeding legumes to children. Processing techniques including dehulling, fine grinding, roasting or any form of prolonged cooking and sometimes germination and fermentation, have been found to reduce flatus from beans. A challenge limiting starch-based gruels such as rice and corn as primary supplement stocks are their characteristically high ingestion volumes required to achieve 6 3 adequate nutrient delivery (low nutrient density) and the high viscosity which might cause choking in young children. The ability of starch to bind more water leads to dilution which increases bulk which subsequently limits the amount of nutrients that could be derived per serving of gruel. Industrial methods which have been reported to modify starch structure to lower its water-binding capacity have included enzyme pre-treatment (amylase), precookin g or extrusion and drum»drying, and germination or sprouting (Lastreto et al., 1982 and Marero et al., 1988). Enzymes released from the embryo of sprouted grains hydrolyze portions of the starch molecules into short-chained dextri-maltose which does not swell when cooked into a gruel (Ebrahim, 1983) and therefore possess great potential in the preparation of flour from sprouted grains for use in weaning foods. Flour from sprouted grains can be used in greater amounts to give the same viscosity as flour from unsprouted grain, thereby improving nutrient and energy density (Mosha and Svanberg, 1983; Desikachar, 1981 and Brandtzaeg et al., 1981). Weaning foods suitable for use in the Philippines were developed by Marero et al.(1988) and prepared from flours obtained from germinated rice- mungbean, germinated rice-cowpea, germinated corn-mungbean and germinated com- cowpea. The low viscosity and high caloric density formulations were found stable for 6 months, microbially safe and well-tolerated by infants. The blends had amino acid values which approximated the FAO reference pattern, except for the S-containing amino acids. The rice-based formulations were demonstrated to be superior to the corn-based gruels based on chemical score for cystine/methionine, net dietary protein energy and PER. The use of germinated legumes was also reported to increase the micronutrient contents of the weaning food formulations (with the exception of calcium ), compared to control formulations without the incorporation of germinated legumes. Kusin et al. (1984) reported that in rural Indonesia, growth faltering from the third month and the high percentage of wasting at age 0-3 years in preschool children were mainly due to the 6 4 inadequacy ofweaning foods andthelowintakesofvitaminsandmineralsresultingfiom low consumption of pulses and leafy vegetables . In South and CentralAmericaarldpartsofcentral andeastem Africa, drybeansare commonly served without dehulling, a form unsuitable for children. Thus, young children are merely given the broth or soup in which the beans have been cooked, resulting in poor protein digestibility, diarrhea, and other gastrointestinal distresses. Protein digestibility of the soup was lowered by the tannins present in the seed-coats of colored beans and are partially leached into the cookin g medium. The hydroxyl groups of the phenol ring enable the tannins to form crosslinks with proteins which may be implicated with decreased digestibility (Ma and Bliss, 1978 and Haslam 1979; Elias et al., 1979; Aykroyd and Doughty, 1982; Bressani and Elias, 1980; Bressani et al., 1983 and 1988). The Institute of Nutrition of Central America and Panama (INCAP) introduced in the late 1950's "Incaparina", a mixture of predominantly vegetable protein origin having a nutritional value similar to that of milk and suitable for the mixed feeding of infants and young children. The first one tested clinically was "Mixture 8" made with entirely indigenous materials having the following formulation : lime-treated corn flour flour (50%), sesame meal (35%), cottonseed meal (9%), torula yeast (3%) and powdered kikuyu leaf (3%), and was supplemented with vitamin A. "Mixture 9" was the first mixture recommmended for commercial production , and was made of lime-treated (CaCO;;; 1%) corn flour (29%), sorghum (29%), cottonseed flour (38%), torula yeast (3%), and supplemented with 4,500 ID. of vitamin A per 100 grams of the dry product. Alternate formulas were subsequently developed with soy, peanut and sesame as the alternate vegetable protein sources and with rice as the cereal component (Scrimshaw, 1980). These modifications were recommended due to agricultural availability and least cost formulation considerations. Other recommendations to improve the product included the addition of amylase to make a thinner gruel, and marketing it as a precooked product. However, these were not endorsed protocols due to inherent additional costs, departure from the traditional practice of plottil COHCCI feedln BaI-A. in Ind witho lochnl ftrmc Comm cowpc Plantal' not On “111th inm'nsl'. 901th New low-grad mineral Sorgum7 him the 65 preparing thick corn gruels or the potential encouragement of feeding by bottle which would have introduced problems of contamination and displacement of breast milk. Other efforts which have have been made to develop low-cost nutritive infant foods included : 1) Del Valle et al.'s (1981) "Soyaven," an infant formula already in commercial production; 2) "Nutrisoy", a blend of corn and soybeans (Easterbrook, Gregg, 1986; malted and roller dried sorghum and cowpea weaning food formulations (Malleshi et al., 1989); 3) sesame protein-based weaning food (Moharram et al., 1989); 4) ultrafiltered chickpea protein concentrate in infant formula (Ulloa et al., 1988; Reddy et al., 1990). Traditional germinated legume and cereal seeds have also been used in mixtures for feeding young children in India. An Incaparina-type of precooked weaning food, named Bat-Altar ("nutritious child"), played an important role in government nutrition programs in India (Scrimshaw, 1980 and Reddy et al., 1990). It was provided to the consumer without cost and largely displaced imported weaning foods. Traditional processing techniques which have been utilized include roasting, malting (germination), puffing and fermentation (Reddy et al., 1990). Legumes which have been successfully utilized in commercial preparations include soybeans, green and black gram, chickpeas, pigeon peas, cowpeas and groundnuts. Multimixes consisting of local staples (ex. cassava and plantain), legumes and vegetables (ex. dark-leafy greens), or sometimes even meat, raised not only the protein but also the vitamins, minerals and energy content as well. The addition of fat or legume oil is recommended when the legume or pulse component is intrinsically low in fat. Gupta and Sehgal (1991) reported lower levels of phytic acid, polyphenols and saponins and higher in-vitro digestibility of low-cost weaning mixtures prepared by mixing malted pearl millet, roasted amaranth, roasted green gram, jaggery (a low-grade molasses residual fraction) and malted barley. Olaofe (1988) compared the mineral contents of imported baby foods with those of selected Nigerian grains (maize, sorgum, cowpea and soya beans) suitable for baby foods and found the iron contents to be in the same range but calcium to be much lower in the Nigerian grains. Corn-flour 66 infant feeds consumed in Nigeria were reported to have considerably lower amounts of mineral elements than popular brands of infant formula (Fatoki, 1990). Moharram et al. (1989) also reported that weaning foods based on sesame protein in combination with dry skim milk and either corn or rice starch were successfully prepared and found to be feasible for production in developing countries . Potential for Soybeans as a High-Protein Weaning Beverage The soybean and suitable processing methodology have been extensively studied for use in weaning foods. This review is presented to provide a basis for use of these technologies in preparation of dry bean (Phaseolus vulgaris) based products. W Soybeans (Glycine max (L.) Merr.) are the most widely grown of the grain legumes. It is essentially a temperate crop but can be grown up to an elevation of 5000 meters depending upon the location. Production of soybeans is dominant in both developed countries and lesser developed countries (Figure 11). Dry beans, peas and peanuts are of similar total production scale, with noted differentiation among predominant sectors (Uebersax and Occer‘la, 1991). Soybeans serve as the major source ofprotein to supplement a variety of grains in the diet in LDCs and are utilized to help alleviate malnutrition, especially in the Asian region. The approximate composition of soybeans is as follows: protein, 40%; lipid, 20%; cellulose and hemicellulose, 17%; sugars, 7%; crude fiber, 5% and ash, 6% (Erickson et al., 1980). Isolated soy proteins are now used commercially in many food applications such as infant formulas, emulsified meats, imitation cheese, bakery products, high-protein diet products and formulated soymilk (Haytowitz and Matthews, 1989). The preparation of soymilk requires five basic steps: cleaning the soybeans soaking, grinding, filtering the soy residue and cooking the soymilk. Commercial production of soymilk include Total Production (1000 MT) 1 20000 67 100000 . 80000- 60000- 40000 - 20000 Soybean Grantham DryPesr Dryberns Olickpees Broadbuns Source of production Lesser Developed Countries I Developed Countries \\\\\\\\\ \\\\\\ \ \ \ \ I I I I I A A \ \ \ \ \ \ \ H 1 l . . r ‘I Lentils Legume Figure l 1. World production of major food legumes (Scmce: Data adaped frcrn FAO, 1989). 68 additional steps of dehullin g, formulating, homogenization, sterilization and packaging. The flowsheet for commercial soymilk production using the Illinois Method is outlined in Figure 12. The advantages of this method include: very high yield ( 89% solids, 95% protein); removal of oligosaccharides and beany flavor. However, the use of an expensive, powerful hornogenizer to produce a smooth, stable emulsion is a major disadvantage. Cleaning reduces or eliminates damaged soybeans in which activated lipoxygenase has catalyzed oxidation of the unsatm'ated fatty acids producing compounds with the characteristic beany flavor. Good quality soymilk can be made without dehulling of the soybeans, but dehulling offers the following advantages: improved protein recovery, improved soymilk flavor and slightly whiter color; improved digestibility; reduced oligosaccharides, soaking time, grinding energy and bacterial count. Soybeans are generally soaked in about three times their weight of water. Cold soaking requires a longer time ( 8 to 10 hours at 20°C or 14 to 20 hours at 10°C) for hydration of soybeans compared to hot soaking. Longer soaking periods result in greater loss of soluble components, particularly the water-soluble carbohydrates. Soaking reduces energy input required for grinding, enables better dispersion and suspension of the solids during extraction and increases yield and decreases cooking time. Soaking in alkaline solution containing sodium bicarbonate or sodium citrate are reported to decrease the beany soymilk flavor, tenderize the soybeans leading to reduced cooking time and enhanced homogenization, reduce oligosaccharides and accelerate the inactivation of the soybean trypsin inhibitor. Blanching or steaming in a solution of sodium bicarbonate initiates inactivation of the lipoxygenase causing the beany flavor, washes out water-soluble oligosaccharides and inactivates trypsin inhibitors. Hot water grinding to achieve a 150 mesh colloidal suspension further inactivates the lipoxygenase. Filtering the insoluble soy residues fiom the slurry is done using a decanter centrifuge and results in improved flavor, mouthfeel and facilitates removal of oligosaccharides. 69 SOYMILK PROCESSING PROCEDURE Whole Soybeans i Soaking in 0.5% NaHCO3 solution for 6 to 12 hours (Bean : Water 8 1:3) (Water hardness 84 ppm on CaCO3 basis) i [ Blanching by boiling for 10-20 min Draining and rinsing Grinding with a Fitzpatrick mill (Fust 0.25 inch screen and second. 0.073 inch screen) i Heating slurry to 82 C Homogenizing at 3500 psi and 500 psi Adding water to give 12% solid i Neutralizing to pH 6.8 to 7.2 with 6N HCl Formulating by adding water. sugar. flavoring (0.02% salt. 0.2% vertillirl, calcium 25 mM, earcWater=1:10) i | Heating to 82 c l Homogenizing at 3500 psi and 500 psi i Battling & sterilizing at 121 C: 15 min. Cooling i | Shelf-Stable Ready-to-Use Beverage _— Figure 12. Illinois Method for processing soymilk from whole soybeans (Nelson et al., 1975) 7 0 Cooking or heating the soymilk destroys the spoilage microorganisms, inactivates trypsin inhibitors and also reduces viscosity to facilitate extraction and give higher yields of protein and solids. Heating soymilk to 100°C for 14 to 30 minutes or at 110°C for 8 to 22 minutes was reported by Van Buren et al. (1964) to inactivate 80 to 90% of the native trypsin inhibitors. Appropriate formulation of soymilk using sweetening and flavoring agents increases the acceptability of soymilk. Flavored soyrnilks already currently commercially produced in Asian nations include vanilla, milk, egg, strawberry, apple, peanut, chocolate, coffee, almond, orange (Taiwan), malt (Hong Kong), pandan (Singapore and Malaysia), and fruit, vegetable, beef, yakult, lactic acid, honey and sesame (Japan). The additon of soy oil, lecithin or an emulsifier improves the mouthfeel of soymilk. WWW There are three major problems to be overcome to produce good quality soymilk : 1) elimination of the beany/bitter flavor, 2) inactivation of trypsin inhibitors and 3) removal of flatulence- causing oligosaccharides. Wilkens et al.(1967) reported that lipoxygenase (or lipoxydasc) present in the soybean is responsible for the undesirable flavors and odors upon grinding soybeans and is the cause of the beany flavor in soymilk. Soybean lipoxygenase catalyzes the oxidation of cis,cis 1,4 pentadiene containing fatty acids to form 1,3, cis, trans hydroperoxides. These hydroperoxides decompose to form greenish beany, painty flavors. Several methods have been developed to eliminate off-flavors in soymilk Lipoxygenase is often inactivated by hot water blanching of soybeans in boiling water prior to cracking or hot water grinding with boiling water to produce a slurry having a temperature of 80°C or above and holding at this temperature for 10 minutes. Removal of the soy oil to prevent it from reacting with the lipoxygenase has also been suggested to yield a bland soymilk. Steinkraus (1973) patented a method for producing defatted soy flour which involves 71 extracting full-fat soy flour with 95% ethanol, followed by a mixture of equal volume of 95% ethanol and n-hexane. This procedure extracts remaining phospholipids which tend to form off flavors. The beany flavor in soymilk was reported to be reduced by fermentation with Lactobacillus acidophilus (Wang et al., 1974) orAspergillus oryzae and Rhizopus oligosporus (Ebine, 1976). Nelson et al.(1976) reported that soaking and/or blanching soybeans in 0.5% alkaline solution (NaHCO3) improves soymilk flavor, removes oligosaccharides and decreases cooking time. BadenhOp (1969) reported that alkaline soaking reduces a beany flavor compound, 1-ccten-3-ol. Acidic grinding (below pH 3 ) will inactivate lipoxygenase, but is not utilized commercially. Flavor of soymilk has also been improved by slurryin g soy flour in hot water or in-line dispersement of soyflour which minimizes water contacting time followed by rapid hydrothermal cooking (154°C for 30—40 sec) (Johnson et al., 1981), or by ultra-high temperature (UHT) sterilization of soymilk by steam injection at 140°C for 4 sec. Two of the five or more trypsin inhibitors have been purified and studied : the Kunitz (1.4%) and the Bowman Birk (0.4%) inhibitors. Van Buren et al. (1964) indicated that 90% of trypsin inhibitors in soymilk could be inactivated at 100°C for 14 to 30 minutes or at 110°C for 8 to 22 minutes. Soybeans contain the oligosaccharides raffinose (1.1%) and Stachyose (3.8%). Oligosaccharides can be removed by alkaline soaking of soybeans (Nelson et al., 1976), heat treatment and removal of soy fiber residue. Sugimotc and Van Buren (1970) also used an enzyme system of alpha galactosidase and invertase to remove oligosaccharides. These enzymes are a commercial product extracted from Aspergillus saitoi free from protease activity. The soymilk-enzyme mixture was incubated for 3 hours at 55°C, then boiled for 10 minutes to stop the enzyme reaction. The enzyme treated soymilk contained no oligosaccharides because they had been hydrolyzed by enzymes to their constituent monosaccharides. MATERIALS AND METHODS Sample Preparation Commercially produced whole and split dry navy beans grown in the 1991 crop year were obtained from the Cooperative Elevator Company , Pigeon, MI. The beans were field-dried, harvested, sorted, packaged and transported to Michigan State University where they were stored in a walk-in cooler maintained at 4°C (39°F) prior to use. Extractive Pretreatments Hot Water/Steam Extractions of Whole Navy Beans Whole dry navy beans were soaked for 16 hours at 25°C (77°F) in stainless steel tanks and kettles. The hydrated beans were subjected to either hot water (60°C/60 mins) (140°F/60 mins) or steam extraction (100°C/15 mins) (212°F/15 mins) procedures as outlined in Figure 13, respectively. "CONTROL" meal contained cooked beans and all original soak and rinse waters, cook water or condensate. Leachate of "EXTRACT" beans was discarded and replaced with fresh formulation water (Figure 14). Cooking involved holding the beans at the designated temperatures and times in covered stainless steel tanks and kettles (Groen Model N60 Sp, Illinois) equipped with either a vortex mixer or rotating paddles to provide gentle agitation which would facilitate extraction and avoid thermal gradients. Extraction prowdures were as follows: a) Aqueous extraction. Hydrated beans were submerged in water at the ratio of a 3:1 water to bean. The mixture was continuously agitated and held at 60°C (140°F) for 30 minutes for split beans, and for 60 minutes for the whole beans. The cooking water was drained and mixed with the soak and rinse waters. The accumulated formulation water was added to the "CONTROL" beanspriortomillingina 1:1 watertobeanratio 72 73 HOT WATER EXTRACTION OF DRY NAVY BEANS Was Soak 820 ‘—.l DRY NAVY BEANS (hi/hole or Split) L l-I20:8aluu(‘3:l) COLD-WATER SOAK (25 Cl 16 Hrs ) -——--.- Saki-{20* ——> RinseI-UO—DI , INDIRECT STEAM HEAT ‘- cw! “20 <— (Ccoking/Extraction) —>Cooluing mo —— Whole : 60 C / 60 min. split: 60C/30mirr. W am, Wm COOKED BEANS “if; Wm ..— l=l° mam mm“ 2 1°“) 1:1' moan... COOKIE!) BEANS COOKED BEANS (CONTROL) (EXTRACT) CONTROL EXTRA Homogeneous Slurry Homogeneouscglurry S ion Suspension Fitzpatrickmill 0.03" Fitzpatrickmill 0.03” -l-{E - Direct: Steam mica Direci1 Steamed (Tangential Heating) (Tangential Heating) 95 C 95 C DOUBLE DRUM- DRY DOUBLE DRUM- DRY (Dammit/soybean oil Wuhan oil added as process'm and added as processirt aid SIZE REDUCTION SIZE REDUCTION (FLAKES) FINTSI-IER (1/8") FINISHER (1/8") CONTROL EXTRACT [ Drum-dried Meal Drum-dried Meal 1 Figure 13. Flowchart for hot water extracrion of dry navy beans 74 W HOT WATER or STEAM (60 mm C) (15 urinal 100 C) BEAN DILUTION DIFFERENTIATION [ Accumulated th (mmmweofin mm, mm m (131:1-I20:Beans) 8 (111; H20: Beans) l ? | CONTROL II._’IREATMENT1ERMINOLOGL_. EXTRACT Figure 14. Designation of treatment terminology and extraction treatment differentiation used during cooked bean preparation. E M) Slum both with Bioi 75 while an equivalent amount of fresh formulation water was added to the "EXTRACT" beans. b) Steam extraction. Hydrated beans were held in a stainless steel mesh basket and placed into a covered steam kettle. Live steam was injected into the base of the covered kettle and continuously refluxed through the beans during the 60 minute extraction pa'iod. Condensate accumulated at the base of the kettle below the bean surface and was drained and added to the accumulated formulation water. After heating, the beans and formulation water (1:1) were milled to a homogeneous slurry with a Frtzpatrickmill (Model D Comminuting Machine, Fitzpatrick 00., Chicago, IL) using a 0.04 inch mesh screen. Enzymatic I’m-digestion of Whole Navy Beans Whole dry navy beans soaked for 16 hours at 25°C (77°F) were milled to a slurry and subjected to enzymatic pretreatment. Enzymatic pie-digestion involved the use of both commercial and indigenous enzyme preparations. Commercial enzyme preparations with selective substrate specificity and activity were obtained from Novo Nordisk Bioindustrials Inc. (Danbury, CT). 1. Commercial enzyme preparations were as follows: a) Viscozyme120L (a multienzyme complex of the carbohydrases cellulase, B-glucanase, hemicellulase, arabanase and xylanase; activity of 120 FBG/ml); b) Celluclast 1.5L (cellulase from fungus Tn'choderma reeset' ; activity of 1500 NCU/g) c) Neutrase (metallo—bacterial protease produced by a selected strain of neutral Bacillus subtilis; activity of 0.5 AU/g) and 90m 76 d) Alcalase Food Grade (an endoproteinase prepared from Bacillus lichemfonnis; activity of 2.5 AU/g ). II. Indigenous preparation was obtained as follows : Seed germination was conducted in the seed research facilities of the Michigan Department of Agriculture, East Lansing, MI, using the the standard procedure for dry beans of the Association of Official Seed Analysts (1991). Hundred dry seed were uniformly positioned on 2 cm centers using a manual seed depositor on clean, saturated fiber padding. The whole navy bean seeds were allowed to germinate in chambers for three days under controlled temperature and dual light cycle (20°C at night and 30°C during daylight), and humidity. The sprouted beans were pureed (referred to as ”sprout slurry") and held frozen ( 4°C] 24°F) until used to serve as an intrinsic source of catabolic enzymes with substrate diversity. Small batches (approximately 5 kg) of the "CONTROL” (soak, rinse and heating water added back) and hot water-extracted whole bean bean slurries were individually incubated and predigested for 16 hours (overnight ) at 4°C (39°F) with each of the selected commercial enzymes ( 0.1 % w/w ) and "sprout slurry" (5% w/w) prior to drum-drying (Figure 15). A batch with no added enzyme served as a comparative control for the experiment. Aqueous Extraction and Enzymatic Pie-digestion of Split Navy Beans Commercial scale-up of the drum-drying process utilizing split navy beans was conducted following the aqueous extraction (Figure 13) and enzyme pie-digestion 77 DRY NAVY BEANS (Whole or Split) “Tn-nn-n‘ (3:1) COLD-WATER SOAK (25C [16 Hrs. ) . H20 INDIRECT STEAM HEAT ‘_ Coolant 6‘ (Cooking/Extraction) Whole: 60 C / 60 min. Split: 60 C / 30 min. 1:1:H2028eam NE) , L . f L I prout Fem) like amj | WI tear ”Earl its?“ flat" I INCUBATION Wholerl6HrsJ4C S lit : 2Hrs./20C ‘ DOUBLE DRUM-DRY moi! Figure 15. Flowchart for enzyme predigestion oof whole and split navy beans prior to drum-dryin g ‘Commereial- ~scalenmsusing splitbeansalsopreparedforthese designated treatments 78 (Figure 15) protocols. The cooking time was reduced to 30 minutes holding at 60°C (140°F) to minimize excessive disintegration of the split beans. Two separate batches of the "CONTROL" split bean slurries were incubated (55°C / 2 hours) (131°F12 hours) and pre—digested with either the Viscozyme (0.1% w/v) or "sprout slurry” (3% w/v) prior to drum-drying. Drum-Drying of Bean Meals Various drum-drying systems were utilized during selected phases of this research. Each system was steam heated and operated with batch sizes appropriate to maintain full operating capacity. Nomenclature and description of these drum-drying systems are as follows: a) W. A 6” x 8" (38 cm x 52 cm) fabricated double-drum-drier with a heating surface area of 1134 cm2 was utilized to produce the enzyme pre-digested whole bean drum-dried meals. ”211262315. Aqueous and steam extracted whole bean drum-dried meals were produced using a pilot-scale American drum-drier (Overton Machine Co., Dowagiac, MI) with drum dimensions of 12" x 19 1/8" (77 x 123 cm) and (total surface area of 10.24 n2 ) (9509 cm2)with drying surface area nip to doctor blade equal in 5.12 n2 (4755 em2). It was set up to simulate a single drum operation by running one drum as a cold applicator (Bakker-Arkema et al., 1966). c) W. A 5' 4" x 2' (413 cm x 155 cm) atmospheric double drum—drier (Overton Machine Co., Dowagiac, MI) with a heating surface area of 62.83 {:2 (58357 cm2)was used to produce split bean drum—dried meals. Drying conditions of 4.5 rpm and 75 psig per drum were maintained. After holding the slurries at the desired temperatures and times, total solids content was checked using a Computrac Moisture Analyzer Model MA5A (Quintel Corp.) to control slurry viscosity and ensure a uniform film formed on the dryer surface. The 79 temperature of the slurry was then brought up to 90-950C (203°F) by steam injection, prior to pumping the slurry into a stainless steel flash tank (Perma-San Model 75 OVC, Process Equipment Corp., MI) serving as a reservoir for continuously supplying slurry to the drum-drier. The slurry was pumped through a tangential steam heater which gelatinized the starch and reduced microbial load of the slurry. A 0.1% mixture (1:1 ) of lecithin and soya oil was sprayed on the surface of the drum-drier to prevent the sheets from sticking to the drum-drier surface. The drum-dried bean sheets obtained from the drum heating smface were scraped by the drier knives (doctor blades) and collected using a continuous belt conveyor, weighed and flaked through a finisher (Reeves Pulley Co., Indiana) with a 1/4" (1.61 cm) stainless steel mesh screen. Drum-dried bean flakes were thoroughly mixed to obtain a homogeneous product and stored in sealed polyethylene bags which were held in fiber drums at 4°C (39°F) . The drum-dried bean flakes were further milled into flour using a Udy Cyclone Mill with a 20 mesh screen (Udy Co., Fort Collins, CO), prior to analyses. Chemical and Biological Analyses All the analyses were conducted using the described methodologies and were replicated three times, unless otherwise stated. Proximate Composition Moisture. Approximately 2.0 grams of the raw bean or drum-dried bean meal sample was weighed into previously weighed aluminum dishes and dried to a constant weight at 80°C (176°F) (ca 7 hrs.) in partial vacuum having pressure equivalent to 25 mm Hg. Percentage moisttu'e was calculated from the weight loss on a fresh weight basis (AACC Method 4440): (Eq. 1) % Moisture = loss in moisture (g)! initial weight of sample (g) x 100 80 Protein. Protein content was determined by the classical Kjeldahl nitrogen analysis using a modification of the AOAC (1984 ) method. Five millimeters of concentrated sulfuric acid and one catalyst (1(2804 and Selenium) tablet ( (Tecator Co., Sweden) were added into each of the digestion tubes containing the pre-weighed samples (ca 150 mg). The tubes were slowly heated until digestion was complete. The protein content was calculated on a dry weight basis using a nitrogen conversion factor of 6.25. (Eq. 2) % Protein = % Total "Kjeldahl" Nitrogen x 6.25 Fat. Approximately 3.0 grams of the raw bean or drum-dried bean meal sample was refluxed for 4 hours with 60.0 ml petroleum ether using a Goldfish Extractor, or for 25 mins with 40.0 ml petroleum ether using the Soxtec System HT6 (Tecator, England). Solvent was evaporated to yield a fat soluble residue. Percent crude fat was calculated on a dry weight basis (AACC Method 30-25). (Eq. 3) % Crude Fat = wt. of fat (g)/ dry weight of sample (g) x 100 Ash. Approximately 2.0 grams raw bean or drum-dried bean meal sample was weighed into pro-weighed crucible amd incinerated at 525°C for 24 hours. The ash was cooled in a dessicator and weighed at room temperature. Percent ash was reported on a dry weight basis (AACC Method 08—01). (Eq. 4) % Ash = weight of incinerated residue (g)/ dry weight of sample (g) x100 Soluble Sugars Quantitated by High Performance Liquid Chromatography (HPLC) The extraction of the soluble sugars for the drumcdried bean meals was determined using a modified HPLC procedure developed by Agbo (1982) as outlined in Figure 16. Extraction of Soluble Sugars. Approximately 2.0 g representative raw or drum-dried bean meal sample was placed in a 50-ml polyethylene centrifuge tube. Twenty- five ml of 80% ethanol was added and the mixture was then vortexed. The tube was (1) F 81 2.0 g Sample *— Addwrnisonernrnoi Shakaiamhathataoc forlSmin I Sample Mixture L... Residue a ‘_ AddSmIMemanol l Residue b Maroinimmnnoi tproceedaain (l) l I Cenu'ifugeumrpmforiim'm 1 Supernatanta +b +c Residue c I scard Supernatant c I I Pre-filter I a lasin (1) ‘_ Add2ml10‘h ] leadacetab Supernatantb I Mixture I cram eSm'InZMrpm I l Supernatant2a Residue2 Di AdlemllO‘h oxalicacid [ I Supernatant 2b Residue I Bringlovohna manners-not 'mZSleolmithk HPLC ANALYSIS Figure 16. Flowchart for the extraction of soluble sugars from drum-dned bean meals (adapted from Agbo, 1982) 82 placed in a shaking water bath (Model 1024 Tecator, Hoganas, Sweden) and held at 80°C (176°F) for 15 minutes. The sample was then cooled to room temperature and centrifuged using a Sorvall RC-SB refrigerated centrifuge (Du Pont Inc., IL) at 2000 rpm (755 x g) for 3 minutes. One ml of 10% lead acetate (w/v) solution was added to the supernatant to precipitate ethanol soluble proamines, then the tube was again centrifuged for another 3 minutes at 2000 rpm (755 x g). One ml of 10% oxalic acid (w/v) solution was added to the filtrate to precipitate excess lead acetate. The sample was again centrifuged at 2000 rpm (755 x g) for another 3 minutes. The final supernatant was evaporated down to 3 ml and made-up to a final volume of 5-ml using 80% ethanol. Extracts were stored at -4°C (25°F) prior to analysis. Separation and Quantitation. The extracted sample was filtered through a 0.45am millipore filter (Waters Associates, Milford, MA). The filtered sample was injected into a 125 A, 10 um, 3.9 x 300 mm ID. Carbohydrate Analysis column (Waters Associates, Milford, MA). The elution solvent was acetonitrilezwater (65:35, v/v) at a flowrate of 2.0 ml/min. A 50 ul sample was injected using a 100 ul pressure-lock Hamilton microsyringe. The HPLC consisted of a Solvent Delivery System 6000A, a Rheodyne Injector equipped with a 50-ul sample loop and a Differential refractometer R401 (Waters Associates, Inc.). The refractometer was set at 4x to resolve the soluble sugars as discrete peaks. A mixed standard solution was prepared containing a known amount of standard glucose, sucrose, raffinose and Stachyose sugars (Sigma Chemical Co., St. Louis, MO). Quantitation and identification of the sugars were done using the external standard method programmed in the Data Module Model 730 (Waters Associates, Inc.) to calculate the absolute amounts of each component in the injected sample. These data were used to express the percent sugar content based on a dry bean flour weight. 83 Total Mineral Content Mineral content of raw beans, drum-dried bean meals and water used during processing was determined using an inductively coupled argon plasma (ICP) emission spectrometer (Janell-Ash Model 955 Atomcornp) equipped for simultaneous analysis of 19 elements (Al, As, Ca, Cd, Co, Cr, Cu, Fe, Hg, K, Mg, Mn, Mo, Na, P, Pb, Se, T1 and Zn) and maintained by the Department of Pharmacology and Toxicology at Michigan State University. Triplicate samples were combined with 2 ml of concentrated Baker Instra- analyzed nitric acid in 15 ml screw-capped teflon vials (Tuff-Tainer, Pierce Chem. Co., Rockford, 11). The samples were incubated overnight at 70-75°C (167°F), cooled and quantitatively transferred to 10 ml Class A volumetric flasks containing 1.0 ml of 100 ppm Yttrium (internal standard). They were diluted to final volume with water purified by a Millipore water purification system Class 1 (Millipore Corp, Bedford, MA). Along with the bean samples, blanks and standard materials were prepared to serve as controls. Mineral content was determined and values reported in ppm on a dry weight basis. Insoluble and Soluble Dietary Fiber The enzymatic method of Prosky et al. (1988) for determining insoluble and soluble dietary fiber is outlined in Figure 17. Four replicate 1.0 g drum-dried bean meal samples were weighed into 400 ml polyethylene beakers to which was added 50 ml of pH 6.0 phosphate buffer. A 0.1 ml heat-stable bacterial a-amylase (Sigma Chemical Co., St. Louis, MO) was added, the beaker covered with aluminum foil and the mixture was incubated in a shaking boiling water bath for 15 minutes. The mixture was then cooled to room temperature and pH adjusted to pH 7.5102 using a 0.275N NaOH solution. Five milligrams of protease was next added and the mixture was incubated for 30 minutes in a 1024 Tecator (Hoganas, Sweden) shaking water bath maintained at 60°C (140°F). The mixture was cooled and pH was adjusted to pH 4.0-4.6 with 0.325M HCI. A 0.3 ml amyloglucosidase solution (Sigma Chemical Co., St. Louis, MO) was added and the 84 Drum-dried Bean Meal Sample (1.0 g) m butter (50 ml: pH at» a . mylaan (0.1 ml) Incubate (100 015 mins.) Adjust pH 7.5:;02 I..— MWEdmg) Incubate (60 C00 mins.) Adjust pH 4 .0-4. 6 ME— Amylogbeoaidam, $32.13 (03 ml) (60Cf3'0mins.) lOmldaiaIind WIDOCZX) Residue WIN-e- (2:): lOml95§etbel . lOmlaauma w Oven-Dry 0! -Dry 105 C 105 C i nrzr’l‘riill-‘éhi arm nréfli'k‘ll’l'fim (snr) Figure 17. Flowchart of the enzymatic method to determine the insoluble and soluble dietary fiber of drum-dried bean meals (Prosky et al.,l988) 85 mixture incubated for another 30 minutes at 60°C (140°F). Insoluble and soluble fiber fractions were determined sequentially on this digest. Insoluble fiber. The solution was cooled and filtered through a previously ashed and weighed fritted glass crucible (No.2) containing celite, using the Fibertec System B 023 Filtration Module (Tecator, England). The residue was washed with two 10 ml portions of deionized-distilled water. The filtrate and water washings were set aside for the determination of soluble fiber. The residue was washed with two 10 ml portions of 95% ethanol and then with two 10 ml portions of acetone. The crucible containing the residue was dried overnight in a 105°C (221°F) air oven. Residue from one set of duplicates was analyzed for protein, while the duplicate was incinerated overnight at 525°C (977°F) to analyze for ash content. Blank determinations were maintained throughout the procedure. Percent Insoluble Dietary Fiber (lDF) was calculated using the following formula: (Eq. 5) IDF(%)= mg insoluble residue- . sample weight. (mg) Soluble fiber. The weight of combined filtrate and water washings was adjusted to 100 g with water. Four 100 ml portions of 95% ethanol preheated to 60°C (140°F) was added and allowed to precipitate at room temperature for at least an hour. The enzyme digest was filtered through previously ashed and weighed fritted crucibles containing Celite. The residue was sequentially washed with three 20 ml portions of 78% ethanol, two 10 ml portions of 95% ethanol and finally two 10 ml portions of acetone. The residues were dried and analyzed for protein and ash following the same protocol for the insoluble fiber. Percent Soluble Dietary Fiber (SDF) was calculated as follows: (Eq. 6) SDF(%)= -mg soluble residue - . ‘ sample weight. (mg) 86 In-ritro Starch Digestibility Total and available starch content of the drum-dried bean meal samples were determined using a modification of the enzymatic methods of Holm et al.(1986 and 1985). The released glucose was measured by the colorimetric Glucose oxidase/peroxidase Assay using a glucose diagnostic kit (#510-A, Sigma Chemical Co., St. Louis, MO). The combined enzyme-color reagent contains the two enzymes, glucose oxidase and horseradish peroxidase, and the color reagent, o—dianisidine. The procedure is based upon the following coupled enzymatic reactions: Glucose Oxidase Glucose + 2H20 + 02 > Gluconic Acid 4» 211202 Peroxidase H202 + o-Dianisidine > Oxidized o-Dianisidine (Colorless) (Brown) The intensity of the brown color measured at 450 nm is proportional to the original glucose concentration. The total amount of glucose in samples was calculated from a standard curve prepared from known concentrations of glucose. The total starch content in each sample was obtained by multiplying the mg of glucose in each sample by a factor of 0.9 to account for the weight of the water gained during the hydrolysis of starch to glucose. Total Starch. The modified enzymatic/colorimetric methods of Holm et al. (1986) and Tovar et al. (1992) were followed to determine total starch content of the drum- dried bean meals (Figure 18). A 500 mg drum-dried bean sample was weighed into a beaker which was tared containing a magnetic stir bar. The sample was dispersed in 10.0 ml distilled water and 10.0 ml 4N NaOH, and allowed to stand at room temperature for 1.0 hour. Twenty milliliters of 0.08 M phosphate buffer was added and pH was adjusted to 6.0 with 5N HCl. The mixture was incubated with 50 ul of thermostable a-amylase Type 87 500 m sample Distilled H20 (10 ml) 4N NaOH (10 ml) Stand in Room Temperature (1 hour) 0.03 M Phosphate Buffer(20 ml) 5N HCl Adj u5t to pH = 6.0 a-amylase (T ermamyl) (50 ul) Incubate (90-100 C; 1.0 hour) Cool; Mak up to 50 g 50 ul amyloglucosidase/buffer solution (450 ul) Incubate (55 - 60 C; overnight) 1 40 ul Enzyme-color Reagent (5.0 ml) Incubate (45 mins; oom Temp) Absorbance (450 nm) Figure 18. Flow diagram for determination of tOtal starch. [611 the 37‘ 101 St. 2.C inc “'21 31¢ ca; 88 XII-A (Bacillus lichenifomu's, Sigma Chemical Co., St. Louis, M0) at 90-100°C(203- 212°F) for 1.0 hour. The mixture was cooled to room temperattue and distilled water added so that the total aqueous weight is 50.0 g. A 50.0 ul sample aliquot was pipetted into a screw—capped tube and incubated with 450 ul of amyloglucosidase enzyme solution (Aspergillus niger (Boehringer Mannheim) 10 mg of lyophilizate/ml of 3.2 M (NH4)2804; )lbuffer solution (dilute enzyme stock solution 1:10 with 0.1M sodium acetate, pH 4.5) and incubated overnight at 55-60°C(140°F). The mixture was cooled to room temperature and 40 ul sample aliquot used for the glucose assay. Available Starch. Figure 19 outlines the protocol for determining in-vitro digestibility of starch. A 500 mg sample was weighed into a 100 ml beaker tared with a magnetic stir bar and mixed with 10.0 ml of deionized—distilled water (For raw bean samples and reference cornstarch and all-purpose flour, samples were gelatinized with 10.0 ml distilled water in a 90-100°C(212°F) water bath for 20 mins. and then cooled to room temperature before proceeding to the next steps). BC] (200 ul , 5N)was added to bring the pH to approximately 1.5. Pepsin (100 mg) was added and the mixture incubated at 37°C (99°F) for 1.0 hour. Twenty ml of 0.1M phosphate buffer (pH 6.0 - 7.0, and containing 0.1% Thimersal)® and 215 ul of 4N NaOH were added and pH was adjusted to 6.0. Deionized distilled water was added so that the total aqueous weight was 50 g. The mixture was incubated with 15.3 ul of porcine pancreatic a-amylase (Sigma Chemical Co., St. Louis) at 37°C(99°F). The rate of starch hydroysis was monitored by removing a 2.0-ml sample of the digest at appropriate time intervals (15 and 60 min., and 24 hours of incubation). This aliquot was immediately added to 8.0 ml of 95% ethanol. Precipitation was allowed to occur for 1.0 hour at room temperature and then centrifuged at 2000 g (3000 rpm) for 10 mins. (For zero time sampling, a 2.0 ml sample was taken prior to adding the porcine a-amylase solution). A 50.0ul supernatant was pipetted into a screw- capped tube and incubated with 450 ul of amyloglucosidase (Aspergillus niger, 14 enzyme 89 500 m mple Heat (90-100 C; 20 mins) 5N HQ (200 uL) squirt. EC 3.4. 23.1 (100 mg) Incubate ( 37 C: 60 mins) 0.1M Phosphate buffa'whnl *— 4N NaOH 215 111) ) Distilled water (20 ml) Porcine amylase solution, EC 3.2.1.1 (15.3 141) Adjust to pH 6 Incubate (37 C) Remove 2.0 m1 sample (0.15. 60 & 380 min) Centrifuge (2000xg; 10 mins) Amyloglucosidase. EC 3.2.1.3 solution ( 450 1:1) Pipette ul supematant Incubate (24 hrs.: f5 - 60 C) GLUCOSE ASSAY (Glucose oxidase/Peroxidase reagent) Figure 19. Flowchart for the determination of available starch ( Holm. 1984) 9 0 units/mg protein, 10 mg protein/ml; Boehringer Mannheim) enzyme solution overnight at 55-60°C (131°F). The mixture was cooled to room temperature and 100 ul was used for the glucose assay. The release of free glucose was measured with a glucose oxidase/peroxidase reagent and the starch content was calculated as glucose x 0.9. Reagent blanks with the starch degrading enzymes were run in each case. Corn, potato and wheat starch suspensions and all-purpose (wheat) flour were assayed as reference samples. (Eq. 7) % Total or Available Starch = WW2. x 100 sample weight (mg) In-vitro Protein Digestibility The sequential multi-enzyme system (AOAC, 1990) for determining in-vitro protein digestibility is outlined in Figure 20. Drum-dried bean meal samples and control casein (ANRC Na caseinate) were weighed to contain approximately 10 mg nitrogen. Nitrogen content of the drum-dried bean meal samples was determined by Kjeldahl method (Eq. 2). Ten ml of deionized distilled water was added to the casein control (Sigma Chemical Co., St. Louis, MO ) or to the sample in a test tube containing a stirring bar. Protein suspensions were held in a water bath maintained at 37°C (99°F)for at least an hour. One ml of "Enzyme A" solution (porcine pancreatic trypsin, Type IX; bovine pancreatic achymotrypsin, Type II and porcine intestinal peptidase, Grade 1; Sigma Chemical Co., St. Louis, MO) which had previously been equilibrated to pH 8.01-0.03, was added to the protein suspension after it had also been equilibrated to pH 8.01003. After incubation with Enzyme A for 10 minutes at 37°C (99°F), 1.0 ml of "Enzyme B" solution (bacterial protease, Pronase E; Sigma Chemical Co., St. Louis, MO) was added to the protein suspension which was further incubated for 9 minutes in a water bath maintained at 55°C(l31°F). At precisely 20 minutes from the addition of "Enzyme A" solution, pH was read at 37°C(99°F). The extent to which pH of the protein suspension 91 Sampl (10 mg N) deionized distilled H2000 ml) Soaék (1 hr: 7 C) Equilibrate to pH 8.03003 Enzyme A (Tm. EC 3.21.4 & a-Chymotrypsin, EC 3.21.1) In b (10 mic“; 3‘7 C) Enzyme B (Protease, EC 3 l4 16) In b (9.0 “sags C) Read pH (X) (at precisely 20 min. after addition of Enzyme A; 37 C) Calculate % Ligestibility = 23484-2256 (X) Figure 20. Flow chart for in-vitro protein digestibility (AOAC, 1990) 9 2 dropped was used as a measure of protein digestibility. Percent digestibility was calculated as follows: (Eq. 8) % Protein Digestibility = 234.84 - 22.56 (X) whereX=pHat20min. Methionine Content The improved gas chromatography procedure of MacKenzie (1977) for the analysis of methionine in plant materials was followed. A 200 ul of the cyanogen bromide reagent (5% in 50% formic acid) was added to 20 mg of the drum-dried bean meal in a microcentrifuge tube. After 2 hours at room temperature, the tube was centrifuged at 2000 g (1300 rpm) for 15 min. and 2 ul aliquots of the supernatant were injected directly on the chromatographic column using a Hamilton syringe (No.7001). All analyses were performed using a SRI 8610 gas chromatograph (SRI Instruments, California) equipped with both flame ionization and flame photometric detectors. The column ( 4 ft x 1/8" SS ) was packed with Porapak QS, 80-100 mesh (Applied Science Labs., State College, Pa, USA.) and conditioned at 160°F (110°C) for 2 hr. with a hydrogen carrier gas. The GC conditions used were as follows: column temperature, thermal gradient 145 to 160°C (293 to 320°F) at 5°C] min., and l60°(320°F) for 3 min. Quantitation and data reduction were performed by a laboratory data system using an internal standard program. (139- 9) nmolcsMcthioninc= MW x 100 (g) protein Amino Acid Analysis Oxidation, acid hydrolysis and amino acid anlysis of the oxidized samples were performed at the Macromolecular Structure Facility maintained in the Biochemistry Department at Michigan State University. Constant boiling HCl (200141 (Pierce Chemical Co., Rockford, IL) was added to the bottom of the vacuum vial. Three alternate vacuum 93 nitrogen flushing steps were required to ensure the oxygen-flee atmosphere. Vapor phase hydrolysis was conducted at 112-116°C for 24 hours. Following hydrolysis, the samples were re-dried with ethanolzwaterztriethylamine (2:2:1, v/v), and derivatized. The derivatization reagent consisted of a 7:1:l:1 solution of ethanol, triethylamine, water and phenyllisothiocyanate (PITC). After 10 min. derivatization, the samples were vacuum-dried and redissolved in 500 111 of 5 mM sodium phosphate, pH 7.8. A Waters 600 HPLC system (Waters Associates, Milford, MA) was used for the analysis of the derivatized amino acids. The two component (A and B) gradient mobile phase system consisted of the following : A, 15 mM sodium acetate buffer, pH 5.9, and 0.05% triethylamine and B, acetonitrile:H20 (60:40). An injection volume of 40 it! and ultraviolet absorbance at 254 nm were used for detection of the Pl'I‘C-labelled amino acids. SDS-PAGE Electrophoresis Crude extracts of the raw and drum-dried bean meals were subjected to discontinuous SDS-PAGE using an electrode buffer at pH 8.3 following the procedure of Hames (1990). A 7.5% to 24% acrylamide gradient with a 3.75% acrylamide stacking gel was employed (180 x 160 x 1.5 mm slab, Protean 16 cm electrophoresis unit, Bio—Rad Laboratories, Richmond, CA). The sample and standards were loaded onto the gel and the gel was run at 20 mA constant current. The SDS-PAGE gels were stained with silver nitrate to resolve bands, and destained with a 5% MeOH, 7.5% HOAc solution. Standard proteins used for molecular weight estimation were from an electrophoresis calibration kit for molecular weight determination of low molecular weight proteins (Electrophoresis Calibration Kit, Pharmacia-LKB, Piscataway, NJ). The kit consisted of phosphorylase b (94 kD), bovine serum albumin (67 kD), ovalbumin (43 kD), carbonic anhydrase (30 kD), soybean trypsin inhibitor (20.1 kD), and a - lactalbumin (14.4 kD). 94 Assessment of Antinutritional Factors Screening for Heat-Stable Trypsin Inhibitor Activity (TIA) A modification of the spectrophotometric assay of Kakade et al. (1974) by Rayas-Duarte et al. (1992) to determine trypsin inhibitor activity using the substrate BAPNA (N -benzoyl-DL-arginine-p—nitroanilide),is summarized in Figure 21. Approximately 5.0 gram drum-dried bean meal samples were homogenized with 100 ml deionized-distilled water using a high-shear Polytron (Brinkman Instruments Co, Westbury, NY), Model [’1‘ 10/35, at medium speed (setting=5). 'Ihe homogenized bean solutions were centrifuged at 15000 g (10000 rpm) for 30 minutes at 20°C(68°F) . The supernatants were used to assay for . TIA. The total sample volume was adjusted to yield a final volume of 400 ul. Control tubes contained 400 ul of deionized water. The reagent blank tubes contained 400 ulofdistilledwater+200ulof30%aceticacid,whilethe sampleblanktubes contained400ulofsample+21Dul of30%aceticacid.Samplealiquotswere selected to yield a 40-60% inhibition of trypsin activity compared to a control containing no sample. A 400 ul sample aliquot of trypsin (EC 3.4.21.4 bovine pancreas Type III- 8, Sigma Chemical Co, St. Louis, MO) was added to all tubes at 10 second intervals toensure thatallofthetubeswereincubatedforthesametimeperiod. The tubes were then incubated at 37°C (99°F) for a total of 10 minutes before addition of 1.0 ml BAPNA solution (Sigma Chemical Co., St. Louis, MO). The tubes were incubated for another 10 minutes before addition of 200 ul of 30% acetic acid to all tubes except the reagent and sample blank tubes. The tubes were vortexed before reading absorbance using a Spectronic-70 spectrophotometer at 410 nm. One unit oftrypsin activity (TA) was defined as an increase of0.001 absorbance unit at 410 nm of the reaction mixture under assay conditions. One unit 95 I 5.0 g Sample I I . Hogenize I (3.0 mm; Polytrtn, Medium Speed (05)) Cenuifuge (15000 xG/1000 rpm: 30 min: 25 C) Residue Supernate f (Din-d) (Stock) Aliquot (20 it!) 380 ul deionized-distilled n20 Trypsin. EC 1421.4 (0.4 ml) I VortexI Incubate (37 C shakrn' g waterbath: 10min.) _BAPNA‘(1.0 ml): @ 15 sec. intervals Incubate (37 C shaking water built; 10 min.) 0.2ml30%Aceticacid Vortex I l AbsorbanceJ (410nm) Figure 21. Flowchart for the trypsin inhibitor assay (TIA) (Kakade etal., 1974) 96 oftrypsininhibitoryactivityCTIA)wasdefinedat asa10%decreaseinthenumber of units of TA under assay conditions. Thus, a 50% decrease in units of TA (i.e., 50% inhibition of TA) would equal 5 units of TIA (Rayas-Duarte, etal., 1992). Screening for Phytohemagglutinin Phytohemagglutinin (PHA) was determined using Sigma Kit No. P-0526 (Sigma Chemical Co., St. Louis, MO) containing purified Phasolus vulgaris erythroagglutinin (kidney bean lectin) as immunogen. A 0.01 g/ml slurry of raw bean or drum-dried bean meal in deionized distilled water was prepared. Different aliquots (10 to 40 ul) ofthe raw and drum-dried bean meal slurries were pipetted into round bottom microtiter wells and reacted with 10 ul of antibody. The reaction of the antibody with purified Phaseolus vulgaris lectin (Sigma Chemical Co., St. Louis, MO) was used as a reference. For comparative control so as to distinguish sample settling fiorn agglutination, the same quantifies of raw and drum-dried bean meal slurries were pipetted into adjacent rows of wells, but no antibody was added to it. The formation of a lectin-antibody precipitate was monitored every 30 minutes. Phytic Acid Purified inositol phosphate fractions were prepared by hydrolysis of sodium phytate using a modification of the procedure of Graf and Dintzis (1982) as summarized in Figure 22. A 0.5 g drum-dried bean sample was extracted with 20 ml of 0.5M HCl for 2 hr. at 20°C under vigorous mechanical agitation. The extract was centrifuged and the supernatant decanted, frozen overnight and filtered using No. 1 Whatman filter paper. The inositol phosphates were separated from the filtrate by ion-exchange using plastic columns with glass wool filter and containing 0.65 ml resin (AG 1-X8, ZOO-400 mesh). The filtrate was passed through the 97 0.5 g Sample a 20 ml 0.5M HCl Extract (Mechanical agitation; 2 hr.: 20 C) Centrifuge (15 min.) I I Supernatant Residue (Discard) , Freeze (Overnight) Filter (Whatrnan No. l) I Make-up to Volume (1:1; 1120: Sample) 1 I Collect eluent I [Evaporate to dryness I I‘ ma 1 Pass through column (AG 1-X8, 200400 mesh; 0.65 ml resin) 10ml 0.02m HCI ‘ , 5.rnl 0.025M HCI fig ‘ .‘ 1.0ml 2M HCl (10x) 1.0mlHPLCgradewater Figure 22. Flowchart for the separation and quantitative determination of phytic acid as inositol phosphates 98 column (ca 0.4 ml/min) followed by 10 and 5 ml rinsings of 0.025M HCI. The inositol phosphates were eluted from the resin with ten l-ml portions of 2M HCl, and the eluent evaporated to dryness and diluted with 1.0 ml of HPLC Baker Analyzed reagent water. Inositol phosphates were then identified and quantified by HPLC using the method of Sandberg et al. (1989). Physical and Functional Properties of Drum-Dried Bean Meals Color Drum-dried bean meal surface color was evaluated using a Hunter Lab Model D25- PC2 system (Hunter Associates Laboratory, Inc., Reston, Virginia) which includes an optical sensor and a sensor interface unit (SIU) interfaced to a Zenith computer. The calorimeter measures reflectance on three coordinates labeled L, aL, and bL. The L value measures darkness (0) to lightness (100); aL ( green to red) and bL (blue to yellow) values were expressed as hue angle by calculating the corresponding x, y and 2 values. A white tile (L: 95.35, aL = -O.6, bL=+0.4) was used to standardize the system. Cellular Structure and Starch Granule Appearance The microstructure of the drum-dried bean meals and starch granule appearance were observed under Laser Scanning Confocal Microscope (LSM) (Carle Electron Optics Limited, Tokyo, Japan). A polarizing light microscope (Carl Zeiss, West Germany) was also utilized to determine the effect of the extraction pretreatrnents and the drum-drying process on the gelatinization and birefringence of bean starch. Visual examination and selected representative photomicrographs were prepared as the basis to draw conclusions Solubility Drum-dried bean meal solubility characteristics were determined by dissolving approximately 0.5 g sample in 50.0 ml distilled water. The mixture was slowly stirred on a magnetic stir plate at room temperature for one hour, after which it was filtered through a 99 Whatrnan No. 1 filter paper. The filtrate was weighed and dried in a vacuum-oven. The following solubility indices were determined: Water Absorption Index (WAI) was determined by weighing the wet residue. (Eq- 1 1) WAI = missus) sample dry weight (g) Water Solubility Index (WSI) was determined by weighing the dry soluble solids. (EQ- 10) WSI= 331W sample dry weight/50 ml water Soluble Solids (SS, °B) of the filtrate from the above preparation was determined using an Abbe refractometer (Bausch and Lomb) and recorded as degrees Brix (°B). Water Holding Capacity (WHC) WHC, frequently referred to as hydration capacity (HC), was determined using AACC (1984) Method 56-20. Triplicate 2.0 g samples were weighed into centrifuge tubes. Forty ml distilled water was added and the tubes vortexed to suspend the sample. The suspension was allowed to stand for 10 min., inverting the tubes three times at the end of the 5-min and 10-min periods. The tubes were then centrifuged for 15 minutes at 1000 g (and the supernatant decanted. The tubes were then inverted and allowed to drain for 5 minutes. The wet samples were weighed and hydration capacity calculated using the formula: (Eq. 11) WHC = 4» ° - sample wt (dry basis) 100 Bulk density Bulk density was determined as the weight of drum-dried bean meal sample tightly packed into a 11X) ml graduated cylinder and recorded as g/lm ml. Nitrogen Solubility Index (NS!) NSI of the drum-dried bean meals was determined using AACC Method 46-23. A 5.0 g sample was weighed into a 400 ml beaker and mixed with 200 ml distilled water. The mixture was stirred with a mechanical stirrer at low speed for 120 min at 30°C(86°F). The mixture was centrifuged at 15000 rpm (for 10 min and the supemate was filtered through a funnel plugged with glass wool to obtain a clear liquid. Percent water-soluble nitrogen was determined from the liquid using the Kjeldahl method. Nitrogen solubility index, expressing water soluble nitrogen as a percentage of the total nitrogen was calculated as follows: (Eq. 12) Nitrogen Solubility Index (NSI) = W x100 % total nitrogen Incorporation of Drum-Dried Bean Flour in Food Products Quick Bread The procedure for baking the pumpkin bread is outlined in Figure 23. The pumpkin bread formula (Rombauer and Becker, 197 8) is presented in Table 3. The composite flours consisted of all-purpose and drum-dried navy bean flour blended in 80:20, 60:40 and 40:60 ratios, respectively. Batter samples of 325 grams were poured into 3" x 5" (7.62 cm x 12.7 cm) greased baking pans and baked at 177i2°C (350°F) for 45 min. in a National Reel Type Test Baking Oven. Bread loaves were removed from the pan 30 min after baking, for 15 min of additional cooling and weighed to determine the percentage weight loss during baking. 101 WEIGH INGREDIENTS 1 PREPARATION J (Ingedient Blending & Mixin BAKE (177L045 mins) (30 mins.) I Lwratctt j I I EVALUATE I I coon I Color IMoistureW Density 7 Texture (CC) I a. ab) I V (96) ) cm) Figure 23. Flowchart of utilization of drum-dried bean flour in pumpkin bread 102 Table 3. Pumpkin Bread Formula1 Ingredient Weight (g) All purpose or composite flour2 100.65 Baking powder, SAS 0.45 Baking soda 2.00 Salt 3.00 Cinnamon, ground 0.50 Cloves, ground 0.25 Brown sugar, dark 133.35 Vegetable shortening 31.35 Egg, fresh whole 50.00 Pumpkin, Canned 123.00 Milk, whole fluid 60.50 Vanilla 1.23 I Rombauer and Becker, 1978 as cited by Alani et al., 1989 2 Composite flours contained all-purpose/drum-dried bean flow in 80:20. 60:40, 40:60 rados Weaning Food The drum—dried bean meals were utilized to formulate a bean-based weaning food/beverage similar to soymilk. Different concentrations ( 5%, 8% and 10%) of the ”EXTRACT"(aqueous), and "ENZYME-DIGEST" (Viscozyme) drum-dried bean meals were prepared by homogenizing ('I‘ekmar Tissumizer) weighed quantities of the sample with 200 ml distilled water for 2 min. Objective evaluations (Figure 24) were conducted to assess the quality of the bean weaning food/beverage. Selected emulsifiers (carageenan products and xanthan gums) at differential levels were combined with the 5% EXTRACT and ENZYME-DIGEST drum-dried bean meal samples to enhance stability of the beverage. 103 Objective Quality Evaluation of the Bean Products Quick Bread Viscosity. Batter viscosity was determined using a Brookfield viscometer (model DV-II) equipped with a no. 7 spindle and rotating at 20 to 100 rpm, depending on the sample consistency. Results were recorded as centipoise (cps) at 23i3°C (73°F). pH. A portable pH meter (VWR Scientific Inc.,San Francisco, CA) was used to measure the pH of the pumpkin batter. Volume. Bread volume was measured by rapeseed displacement and results were recorded as cubic centimeters (cm3). Texture Tenderness. The standard shear compression cell of the Kramer Shear Press (Model TMS-90, Food Technology Corp., Maryland) equipped with a 300-lb transducer was used and texture reported as Newtons per gram. Bread slices 0.5 cm thick were used for evaluation. Texture Profile Analysis (TPA). A Texture Press TMS-90 was used, equipped with a parallel plate compression cell TPA-l (Food Technology Corp., Maryland). The TPA test is a two-bite compression mode programmed to a specified percentage of deformation. A 1.0 cm thick pumpkin bread sample sliced from the middle portion of the loaf was trimmed using a 0.5 cm x 0.5 cm square-shaped dough cutter. The bread slice was placed at the center of the lower compression plate. The upper compression plate of the transducer was initially lowered down to about 1 cm above the sample. By pressing the "RUN” command, the bread slice was compressed twice with a designated 50% compression distance. After each two-stage compression sequence, the TPA force-distance curve and complete TPA analysis data was plotted directly using the TMS-90 Control Panel. 104 90263 30:. 53 35-5.5. ..e cocoa—«>0 o>_.8.3e 2: me 5:36.". .vm Baum m... mm 880 In .3885 9.58m 9::on .9330 2:502 8.00 082.5 $885 a _r_______.__ Lam beam =8: «...—:33 23.5 eta—E... 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However, the values were still within the reported range of values for dry beans (3.5% to 4.1%). Soluble Sugars Soluble sugars (particularly the oligosaccharides raffinose and Stachyose) were present in lower amounts following hot water extraction compared to steam extraction (Appendix A). Figure 29 illustrates that sugar content of split bean CONTROL and EXTRACT DDBMs are not significantly different (p < 0.05). However, the differential enzymatic pretreatments employed had an influence on the soluble sugar content of whole DDBMs, especially the simple sugars (glucose and sucrose) which increased with processing (Figure 30). The aqueous extraction in this study resulted in a more significant reduction of the soluble sugars compared to the steam pretreatment, indicating leaching of soluble components (Appendix A). However, there was no significant difference (p < 0.05) in theoligosaccharide content between CONTROL DDBM and EXTRACT DDBM, although the latter did possess slightly less Stachyose. This suggests that the hot water extraction conditions (60°C/30 mins.) may not have sufficiently leached out the soluble components. A temperature of 60°C was deemed sufficient to initiate bean starch gelatinization, mobilize soluble constituents and yet not result in a mushy product which woulddecrease yieldandeaseofbean separation The enzymatic pretreatments (Viscozyme and Sprout) lowered the Stachyose content of split DDBMs, particularly in the case of the Sprout split DDBM. According to Chavan and Kadam (1989), germination or sprouting of grains causes a significant reduction in raffinose saccharides. Viscozyme exhibited a darker surface color (brown hue), indicating occurrence of Maillard reaction as a result of increased glucose content. Borejszo and Khan (1992) reported reduction of raffinose and Stachyose by high temperature extrusion of pinto bean high starch fractions, possibly due 123 l .0 Aiv 38.-o.— Figure 29. Soluble sugars of split drum-dried bean meals ( p < 0.05) iv 38.!— Figure 30. Soluble sugar content of enzyme predigested whole drum-dried bean meals (p < 0 05) 124 to Maillard reaction between charged protein groups and reducing sugars. The enzyme predigested whole DDBMs also exhibited lower stachyose compared to the CONTROL DDBM, clearly indicating the potential of selective enzyme pretreatments to reduce oligosaccharides. Processing increased glucose content of the DDBMs as a result of starch gelatinization. The CONTROL DDBM exhibited the highest glucose content, brought about by the retention of the formulation waters; glucose content of the EXTRACT DDBM was lower as a result of the removal of the leachate. The Sprout split DDBM demonstrated almost two times the sucrose content of the CONTROL DDBM. According to Chavan and Kadam, (1989), during germination of wheat, starch content is decreased whereas reducing sugars are increased The sucrose peak may actually be a composite of sucrose and some other disaccharide (such as maltose) having almost the same retention time as sucrose. Total Mineral Content Tables 6 and 7 summarize the total mineral content of split and whole DDBMs, respectively. Calcium and iron concentrations of split beans increased with processing. Sprout split DDBM demonstrated a significantly higher (p < 0.05) calcium value than the other split DDBMs while CONTROL DDBM exhibited a higher iron content compared to the other DDBMs. Processing had no significant influence on the zinc, phosphorus, magnesium, manganese and copper contents of split DDBMs. Calcium content of Alcalase pretreated DDBM is significantly lower (p < 0.05) compared to that of the other enzyme pretreated whole DDBMs. Sprout pretreated DDBM demonstrated a significantly higher (p < 0.05) iron value than the other pretreated DDBMs. The differential enzymatic pretreatments likewise had no significant effect on the zinc, manganese, copper and potassium values of the whole DDBMs. However, iron, phosphorus, aluminum and sodium concentration increased with processing. 125 ...—5.» 335:5» ob. £55m 83:53:. 3.808800 68.885 "cougar—c. 5.2... ...Dgxm ”38.55.82 ...OEZOU ”.83. 58.. 0.9.3.33. m cozogxm. 35$ 8: N God v 5 388.? ...ancEma Be 32.0. 320...... .3 332.8 5.5.8 a £55 «502 mu: . 0363...... oomsflofivw... omvdflmnfie. «8633. www.cfiomsncw ..vcdflv. acmdflod Spam emcdflbd. owmdflofivvh. 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According to Tecklenburg et al.(1984), total phosphorus content correlated well with phytic acid content and protein content. Results of this study demonstrated a slight increase in phosphorus and a significant increase in calcium for the Sprout split DDBMs, contrary to the observation of (Chavan and Kadam, 1989) that calcium, total phophorus and phytate-P decreased during sprouting of millets. Dietary Fiber The insoluble dietary fiber comprised approximately 73% to 80% of Total Dietary Fiber ('I'DF), with the soluble fiber making up approximately 25% of TDF. CONTROL and EXTRACT split DDBMs were not significantly different (p < 0.05) in their soluble and insoluble fiber components (Figure 31). Dietary fiber content of whole DDBMs was influenced by the enzyme used for predigestion (Figure 32). According to Hughes (1991), dietary fiber extracts or isolates derived from whole foods possess a ratio of soluble to insoluble dietary fiber similar to that of food from which they are derived, but are higher in total dietary fiber. Dry beans contain approximately 7% soluble dietary fiber and 13% insoluble dietary fiber. Dry bean dietary fiber is primarily structural (includes lignin, cellulose and hemicellulose) in nature, and not easily isolated or extracted because it is intimately involved in maintaining cellular structure and cannot be easily separated from the other cellular components. Nonstructural dietary fibers include the soluble pectin, gums and mucilages. Srisuma et al. (1991) reported that the cell wall strcuture of bean cotyledon possesses a high content of matrix polysaccharides (Hot water soluble polymer, 25.7% - Total Dietary Flber (S) 130 ‘ \\\\\ IIIIA \\\\\ \’\’\’\’\‘ s 'l' \ III/a IlGh/r \\\\\ \\‘.\ lllld Ill/4 20- \\\\\ \\\\\ Ill/A III/4 \\\\\ \\\\\ I’ll; Ill/4 \\\\\ \\\\\ Ill/A Ill/4 \\\\\ \\\\\ ll’la III/4 \\\\\ \\\\\ III/a l Ila 4 \\\\\ \\\\\ Ill/4 III/4 \\\\\ \\\\\ ’Il’A III 4 \\\\\ \\\\\ llll IIIIA \\\\\ \\\\\ llll III4 \\\\\ \\\\\ I’ll I 10‘ \\\\\ \\\\\ I’ll Ill/4 \\\\\ \\\\\ I’ll III/4 \\\\\ \\\\\ I’ll I 4 \\\\\ 0-1 Raw 0mm EXTRACT Viscozyme Sprout Figure 31. Imoluble and soluble dletary fibers of split been drum-dried meals Total Dletary fiber (%) . ll], 5155c,“ L\\\ lllI L\\ m. II’I ’\ 1‘ '\’ L’\’\’\" 1‘1b\ L\\\‘ I ’3’" .\.\.‘\l I\I\I\I‘ L L :15 I I’ll III t\\\ \\\ L\\\ I’ll I’ll llI’ s\\\ \\\ s\\\‘ Illl IIII III ‘t\\\‘ \\\ s\\\* IIlI IllI Illl t\\ \\\ \\' IllI IllI I II t\\\‘ \\\ s\\\‘ III IIlI Illl b\\\‘ \\\ L\\\‘ IIII IIII IIII s \‘ \\\ L\\\‘ IlII IIII IIII 1o..t\\\‘ \\\ s\\\‘ I’ll l’l’ ’ll’ L\\\‘ \\\ h\\\‘ l\l\l\" I\I\l\l I I I I IIII IIII L’\’\ \ i ’\’\’\I L\’\\‘ \\\ “mum—mambo“ Figure 32. Insoluble and soluble dietary fiber: of whole drum-dried been meals 131 322.5% and Hemicellulose B, 14.6% to 19.2%) with less cellulose, Hemicellulose A and lignin. Results of this study demonstrated a higher content of insoluble dietary fiber for the DDBMs (16 - 22.1% IDF) compared to the figure (13%) reported by Hughes (1991) for dry beans, although the soluble fiber approximated the reported value of 7%. The higher TDF content obtained in this study is attributed to the loss of moisture with processing, thereby increasing the concentration of TDF. The IDF and SDF contents of DDBMs subjected to enzymatic pretreatments more closely approximate the figures reported by Hughes (1991), and indicate the potential of enzymatic predigestion as a processing pretreatment to influence product dietary fiber content. The higher TDF value obtained for the raw bean meal also suggest the inherent presence of indigestible or resistant starch which was made more accessible to enzymatic digestion during drum- drying and enzymatic pretreatments. Dietary fiber has been implicated in the flatulence problem associated with consumption of dry beans, and has been attributed to the soluble component pectin. Effect of Extractive Pretreatments on the Irv-vitro Digestibility and Microstructure of Starch in Drum-dried Bean (Phaseolus vulgaris) Meals Starch Content Table 8 and figures 33 and 34 summarize the effects of various extractive pretreatments on the apparent starch content of drum-dried split and whole bean meals, respectively. All the raw and drum-dried bean meal (DDBM) samples were significantly lower (p < 0.05) in total starch content than the reference samples, cornstarch (95%) and all-purpose flour (wheat) (75%). Starch content of raw whole and split navy bean meals were estimated to be 48 and 60%, respectively. Split CONTROL (54%), Viscozyme (61%) and Sprout (57%) DDBMs had slightly higher starch contents than their 132 Table 8. Effect of enzymatic pretreatments on the total starch content of bean drum-driedmeals1 'I'reatrrrentz,3 Starch content (% dbL A. Split Drum-Dried Bean Meals Raw 68.02 1 2.71b CONTROL 57.29 1 2.2111 EXTRACI‘ 60.16 1 0.04a Viscozyme 64.58 1 3.0% Sprout 60.35 1 1.00ab Reference Samples C 99.76 1 2.81d All-Purpose Flour 75.04 1 1.22c LSD(0_05) 5.07 B. Whole Drum-Dried Bean Meals Raw 55.77 1 1.24ac CONTROL 56.08 1 7.31a Sprout 56.07 1 0.25ab Viscozyme 61.92 1 3.16b Alcalase 49.77 1 7.86a Neutrase 59.74 1 2.3bc Celluclast 60.16 1 3.39bc Reference Samples C 99.76 1 2.81e All-Purpose Flour 75.04 1 1.22d LS13(0.05) 9.33 1 n=2; Values are the means of two assays Means within a treatment group followed by different letters are significantly different (p < 0.05) 2 Hot Water Extraction (60°C/60 minutes) 3 Raw.the been meal; CONTROL. non-extracted; Sprout. 1% germinaed bean slurry; Connnereial Enzyme preparations (V iseozyrne. Alcalase. Neutrase and Celluclast) 133 3:22.30 5:8 Cornstarch All-purpose Sprout Flgure33. Total starch content ofraw and splltbean drum-dried meals 100 /./ / w w m 0 3:22.30 5:8 ,H .. . . _ m u hmm Treatment Figure 34. Total starch content of raw and enzyme pro-digested whole bean drum-dried meals 134 corresponding whole drume bean meals (52%, 59% and 51%, respectively) due to hull loss in split beans. The starch content of the split CONTROL DDBM ( 54%) was not significantly different (p < 0.05) floor the EXTRACT DDBM samples (53%), but significantly lower (p < 0.05) than the enzyme predigested samples, Viscozyme (61%) and Sprout (57%). The enzyme pre-digested whole DDBMs yielded significantly higher (p < 0.05) apparent starch contents (55% to 59%) than the CONTROL DDBM (52%), except for the Alcalase (44%) and Sprout (51%) treated DDBMs which were not significantly different (p < 0.05). In-vitro Starch Availability Tables 9 and 10 summarize the digestibility of starch (%) in variously treated split and whole DDBMs held under different incubation periods (0, 15, 60 and approx. 380 mins.). Figures 35 and 36 depict the a-amylolysis curves of split and whole DDBMs, respectively. All the split and whole DDBMs were hydrolyzed at a significantly lower (p < 0.05 ) rate than the boiled (20 min. at 100°C) cornstarch used as a reference sample. The other reference, boiled all-purpose flour, exhibited a lower degree of hydrolysis than cornstarch, but was not significantly different (p < 0.05) from the EXTRACT and enzyme predigested split (V iscozyme and Sprout) DDBMs. The boiled raw bean flours (split and whole) were not significantly different (p < 0.05) from the CONTROL DDBMs and exhibited the lowest degree of hydrolysis. The various extraction pretreatments employed prior to drum-drying all resulted in an increased rate of amylolysis, with the enzyme pre-digested DDBMs demonstrating the largest increment in starch availability. The degree of hydrolysis increased in the following order : a) for split bean, raw = CONTROL < EXTRACT = Sprout < Viscozyme; whereas b) for whole beans, raw = CONTROL = Sprout ”mu: . 135 3.3 H cnmdn ....— .n H $3.? .5»... H c319. send H can... ...eE o......r..._.=... 3m.— H Ecde en...» H 89% £12 H 83:. .53 H can... :oBmEeU .3256 H 8. dm 2.8... H coo...“ .:~.c H 92.6 _ :8... H cnmw mm .38....— H chvem nah—.2 H ommNm 33“ H 856 Bed H cmmd Um 33.. H 8.2% ozfi H 2a.? .52 H 2.0% _ ..86 H Sew m3: «2.6 H cm. on fined H 8nd. .3ch H sawd— anc; H ca: 0?: 3m... H 3...: «and H omnm. ...—S. H coed «N. d H 8. .m 33. Hag—flag 2252... .... m . .. .....5 «...: 3:33..— «39.53:. 123... 3.5-8.5. .30.. 0.9.3 ...... «.30.. .93.. 293. 3.: 5 :22... .3 525283.. 8.3.... .5 2.8.58: 8:25.... .3 80.5 d 935. 136 22.32.90 e:- 8§82 .328? 6:58.42 «8.3.8:... 9.5%. 3.8.5.50 5...... :8: 8.3.5.0» .3. ....pam "8.98.3.8: ...OEZOU ".38 :8: 0.9.3.2.... N .8... v a .a .8883... 385:3. 0.8.8. ...:28 :08 :23... 22.9. 329...... “8.3.3.. .53.... ...... 82.... :82 .5... 8.. ..e 28.: o... o: 3...; Nip 2.... ...... ...... .... ......c... 3...: H cnmdn 3.. .n H 2...: can... H 93.9. and H can... .52... 885.22 cc...— H :86: 32..” H 83% 03.2 H 83:. an: H Sm... 8.2.280 End H 31% u-.~ H 94...... 8.... H 82h .3... + coma 328.30 Sand. H 8:... on; H can...” :5...» H 8:...— ammfi + 85. 8.....82 3... . a 89:. as... H :8... .78.. H :8... 5.: + :3... 32...... an ... H n 5.2 an... H NEH—N .185 H 95.: :25... H vm~.~ 2.58.3 5...: H «3.3. .12... H 39.2 .3... H can 3...: H 8: .....am ...—...... H 26.3 8.6.: H 25.." 83.. H 8...: .8... + End SE28 .3“... H 2:.— anvd H nond— -:.d H936 .2... H 8; ......— al.—.5333...— ...m..::e .... m. .. .....5 0...: 8:38..— 18.52.... .38... 8......52: :3: 0.9.... ....n ”:3... bi: 0.9.3 3:. :_ 8.... .... 3.3.88... 8......:. .3 8:33.79... 3.3.58 .0 .85. .... 03a... 137 Degree 0! hydrolysis (%) 0r . r T r - r r f I - - —O— EXTRACT 0 20 40 60 80 —0— WE Wh(fll) —I— SHOUT 8° —o— eon-wen ‘ —.— Al-PmpoeeFlou T E °°‘ - a 1 Us '5 - _/ -B ‘ I f D. a. ‘ ‘0‘ 'r/ = I S ‘ - 20- / T T r ' 0 100 200 300 400 Incubation the(nh) Figure 35. Hydrolysis of starch in raw and split bean drum-dried meals by pancreatic a-amylase 138 so 1 t! V 2 D 3.‘ o L 1: h .1: ‘- e 8 h u 0 G —0— Raw —0— comm —i— Viscozyme "‘0— Sprout —I— Abuse 0 I l ' ' I V v r v , ..., , —o— Neutrase ° 2° Incubauon t1me(mln) 6° 3° 80 —*— Comet-d: —I— AI-PupouFlour A 8 oo- V U '3 2' e l- '6 h .: e. ‘0‘ e 8 4 i- u o D f 0 I f I ' l ' r ' O 100 200 300 ‘00 Incubation time (min) Figure 36. Hydrolysis of starch in raw and whole bean drum-dried meals by in-vitro pancreatic a-amylase 139 Degree of hydrolysis for whole beans which were preheated with hot water versus steam cooking increased as follows: raw < HWC < SC < SE < HWB (Appendix C). An additional gelatinization step (boiling for 20 min.) prior to the starch assay, of previously pre-gelatinized split bean DDBMs further increased the rate of amylolysis (Appendix C). Total and available starch contents of the drumodried bean meals were determined by following the method of Holm et al. (1986 and 1985, respectively). The following steps were incorporated prior to enzyme digestion : a) solubilization with 4N NaOH at room temperature for 1 hour to measure total starch content and b) pepsin incubation at 37°C for 1 hr. at pH 1.5 for the determination of "potentially available" starch. According to Tovar et al. (1990b), these pretreatments enhanced accessibility of starch to amylases and destroy the integrity of remaining intact cell walls. The alkaline pretreatment used provides for the dispersion of crystalline raw starch and retrograded amylase fractions, resulting in higher starch yields (Englyst and Cummings, 1990). Underestimation of starch content as a consequence of encapsulated starch have been previously reported for precooked legume flours (PCFs). The NaOH or KOH treatment thus provides a way to measure "total starch content" by solubilizing so-called "resistant starch". A preincubation with pepsin has a thinning effect on the cell surface with accompanying alteration of fiber/protein associations occurring in the cell walls (Tovar et al., 1990a). Total starch yields of the CONTROL and EXTRACT split DDBMs were not significantly different (p < 0.05), indicating that the aqueous extractive pretreatment employed did not have a significant effect on starch content (p < 0.05), as it did for relatively more soluble simple sugars. Total starch yields of the CONTROL and EXTRACT DDBMs were significantly lower (p < 0.05) compared to that of the raw bean meal. Tovar et al. (1990b) reported that differences in susceptibility to enzymatic attack in PCFs and raw flours are mainly due to the release of starch granules during milling of uncooked seeds, whereas starch-containing cotyledon cells remain in the PCFs. 140 The enzyme pro-digested split bean DDBMs, Viscozyme (commercial), possessed significantly higher (p < 0.05) starch contents than the CONTROL and EXTRACT DDBMs. The Sprout DDBM was not significantly different from the CONTROL and EXTRACT DDBMs. Both Viscozyme and Sprout contain cell wall degrading enzymes which could hydrolyze cell wall or starch with a corresponding increase in released glucose. The reference samples, cornstarch and all-purpose flour, possessed significantly higher (p < 0.05) starch contents than the boiled raw seed and DDBM flours. The enzyme pre-digested whole bean DDBM flours did not differ significantly (p < 0.05) in their apparent starch contents. However, the cell-wall degrading enzymes, Viscozyme and Celluclast. resulted in the highest starch yields, followed by the protease, Neutrase. These results again indicate the need for the disruption of cotyledon cell wall in order for the starch to be exposed to the amylases. The Sprout DDBM possessed similar starch content as the unextracted sample, CONTROL, indicating that the indigenous amylases present during germination did not sufficiently hydrolyze the starch. The "potentially available" starch represents the amount of starch which can be hydrolyzed by amylolytic enzymes, and is starch measrn'ed after pepsin or homogenization pretreatments of cooked beans (Tovar et al., 1990a; Tovar, 1992). According to Holm et al. (1985), preincubation with pepsin increased the starch availability of raw and boiled wheat to a-amylase, indicating a large fraction of the starch was encapsulated in a protein matrix. The disintegration of protein aggregates released highly available gelatinized starch that was readily hydrolyzed by a subsequent incubation with a -amy1ase. The release of starch from the protein matrix indicates that gelatinization alone is not the only factor involved in increasing the starch susceptibility to enzyme action. 141 Laser Scanning and Polarizing Light Microscopy Abundant free starch granules with adhering protein bodies were observed in the navy bean flour from milled raw seeds (Plate 1a). The raw bean starch granules exhibited birefringence, as evidenced by the presence of the characteristic "Maltese cross" pattern when viewed under polarizing light microscopy (Plate 1d). The differential extractive pretreatments employed prior to drum-drying resulted in microstructural changes as demonstrated by extensive disruption of the cotyledon cells and exposure of the starch granules (Plates 2a and b, and 3a to e). No evidence of defined cellular structures nor intact starch granules were identified in bean meals subjected to enzymatic pre-digestion of the slurries prior to drum-drying, particularly those meals pre-digested with the commercial enzymes Neutrase and Celluclast (Plates 3i to j) which appeared amorphous. For comparative purposes, LSM micrographs of flour obtained from canned and subsequently freeze-dried whole navy beans are shown in Plate 4. Abundant agglomerates of intact cellular structures entrapping starch granules were evident in these hydrated and thermally processed canned samples. Similar intact cellular structures were observed under LSM of canned whole navy beans (Plate 5). Further, when viewed under polarizing light microscopy, the "Maltese crosses" were still present with relatively greater frequency "crosses" observed in the "firm" (92 RNK 8P) breeding line compared to the "soft" (92 RNK 17E) breeding line, indicating incomplete and differential gelatinization of starch in these thermally processed samples (data not shown). Plate 1a illustrates the free starch granules released by the breakdown of cell walls of raw navy bean seeds during milling. A high proportion of the starch granules iembedded in a protein matrix (Plate 1d), as evidenced by the preponderance of fluorescent protein bodies. The "Maltese cross" observed under polarizing light microscopy (Plate 1d) is a manifestation of birefringence exhibited by ungelatinized crystalline starch granules. The short boiling step (20 mins. at 100°C) employed prior to the enzyme digestion of the Plate '- Raw Split mcal (a—h) undcr LSM microscopy and (c-d) under polarizing light microscopy 143 '0 Ltll Plate 2. EXTRACT DDBM (ll-bl UlldCl' LSM microscopy and (c-d) under polarizing light microscopy 144 I‘ - . ' ‘3: ”we ilk ~‘Pfrgfh . . I, 0.. v . ‘ ‘I . _ r' o ) _ I . :f 53'. «3 ‘a “2| 3'?" bin ‘0 Ll" :oon-SI Hz. :-262 mu n U" f ”mu-o v.2. rues l-rZ? ‘0 L483 Plate 3. LSM micrographs of non-extracted (CONTROL) (a-b) and enzyme pre- digested whole bean drum-dried meals: Viscozyme (c-d). Sprout (c-D. Alcalase (g-h). Neutrase (i-j) and Celluclast (k-l) 145 lflvn ‘ ...—— IN“ V. Ll" I C-llé Ill” ‘0 L488 146 e ZOOM-20 T-Zs CI368 It“ F0 L488 0 ZOOHIZO TIZr CISlO 3'405 F0 L488 Plate 4. LSM micrograph of canned and subsequently freeze-dried whole navy bean 147 Plate 5. LSM micrographs of (a) soft canned and (b) firm canned bean (92 RNK 8P) 148 raw bean may have resulted in partial swelling of the bean starch granules. The a-amylases cannot easily penetrate through the protein matrix encapsulating starch (Holm et al., 1986) or within incompletely gelatinized granules due to steric hindrance (Wursch, 1986). These factors could explain the lowest degree of hydrolysis (Figure 5) demonstrated by boiled raw bean seeds. I Birefringence was not exhibited by pregelatinized EXTRACT DDBM under polarizing light microscopy (Plate 2), indicating complete gelatinization during the drum- drying process which involved exposure to temperatures as high as l49°C(300°F). Wursch et al. (1986) observed that a-amylase digested starch granules progressively from outside of the cell walls. Thus, the absence of the intact cotyledon cells in DDBMs which may be attributed to wet homogenization (Fitzmill) of heated beans prior to drum-drying has resulted to a greater surface area being available to the amylases, rendering the DDBMs susceptible to amylolytic attack with resultant increased digestion rates. According to Tovar et al. (1992), acidic preincubation of PCFs with pepsin, simulating the gastric phase of digestion, resulted in a greater rate of hydrolysis. The resulting thinned or even missing cell surface and higher amylolytic rate observed in PCFs may be regarded as an enzymatic rather than merely a pH dependent effect. Wursch et al. (1986) also reported a minor change in digestion of leguminous starch during incubation under acidic conditions in the absence of pepsin. Results of LSM in this study demonstrated that enzymatic pre-digestion of bean slurries prior to drum-drying affected the integrity of the cell walls and facilitated the amylolytic process by exposure of starch (Plate 3a-f). DDBMs from whole beans incubated (prior to drum-drying) with the proteases Alcalase (food grade) and Neutrase, exhibited a higher degree of hydrolysis than those pre-digested by Viscozyme and Sprout, indicating potential denaturation of the pretein mauix and increased accessibility of a-amylase to the substrate. The LSM micrographs (Plate 3d and e) illustrate the disruption of the starch granules increased the total granule 149 surface area exposed to enzyme action. These results further confirm the observation of Wong et al., (1985) and Tovar et al., (1989) of a possible occurrence of protein/starch interactions which decrease carbohydrate digestibility. The presence of intact cellular structures encapsulated by a protein matrix (fluorescing) in whole beans canned and subsequently freeze-dried (Plate 4) confirm the observations of Tovar et al. (1992) that freeze-dried PCFs contained more intact cells than vacuum-dried flour. Plate 5 also demonstrates the same observation with canned whole beans ("frrm" versus "soft" cultivars) hydrated and thermally processed, clearly demonstrating that the high retort temperature 115°C (240°F) was not sufficient to disrupt cell walls, or to completely gelatinize legume starch, and that gelatinization alone is not the only factor involved in increasing starch susceptibility to amylolytic activity. These results are contrary to the observation of Hughes and Swanson (1989) that flours prepared after autoclaving and warm-air drying of common beans do not contain intact cells. Commercially canned beans have been previously reported to contain resistant starch (Siljestrom and Bjorck, 1990). During cooking, some of the amylose leaches out from the starch granule, remaining within the intact cell and filling spaces between protein bodies and starch granules. If amylose retrogradation occurs, another indigestible matrix is formed in and around the protein and starch granules, thereby contributing to slow protein and starch digestion (Bennink and Srisuma, 1989). During methodology development and screening, it was observed that canned and freeze-dried samples (as in Plate 4 ) had to undergo a gelatinization step (boiling for 20 mins.) prior to the starch availability assay to enable normal digestion rates. Lower rates of digestibility were observed for samples tested without this additional heat treatment(data not shown). Tovar et al.(1990b) reported that a second boiling treatment promotes a further rise in the enzymatic susceptibility of starch. This could also account for the increased degree of hydrolysis observed with 150 pregelatinized split DDBMs subjected to a boiling step (20 mins.) prior to the starch assay (data not shown). The reference cornstarch exhibited the highest degree of hydrolysis, while the all- purpose (wheat) flour was not significantly different (p < 0.05) from the enzyme pre- digested DDBMs. Holm et al. (1985) reported that pure starch was more available to salivary a-amylase in-vitro than starch present in flour. The cohesive properties of wheat proteins result in the formation of glutinous lumps when these samples are being dispersed, making it difficult for the enzymes to degrade the starch completely to glucose. lit-vitro Protein Digestibility In-vitro protein digestibility of raw split navy beans improved significantly (p < 0.05) with processing ( Figure 37). The effect of the differential aqueous extractive pretreatments employed prior to drum-drying on in-vitro protein digestibility of the split DDBMs were not significantly different (p < 0.05). The differential enzymatic pretreatments (Figure 38) did not significantly enhance (p < 0.05) in-vitro protein digestibility of whole raw bean meals, with the exception of the Celluclast predigested DDBM which did increase. The CONTROL DDBM (no enzyme predigestion) demonstrated a significantly higher (p < 0.05) protein digestibility value than the enzyme pre-digested DDBMs. Heat treatment greatly improves the digestibility of most dry bean protein fractions. The improved performance upon heating is partially attributed to inactivation of antinutritional factors such as protease inhibitors and lectins (Nielsen, 1991) and opening of the protein structure through denaturation (Hsu et al., 1977). However, processing can also cause a decrease in protein digestibility via the nonenzymatic browning reaction and thermally induced cross-linking reactions. Hence, a sensitive in-vitro protein digestibility method should detect digestibility changes due to protease inhibitors, substrate-bound inhibitors and processing effects. The multienzyme technique utilized in this study for estimating in-vitro apparent protein digestibility can 5 hotel- Dlluflblllty 5 Protein Dlguflblmy 151 IN-VITRO PROTEIN DIGESTIBILITY 0F DRUM-BRIE) BEAN MEALS W Figure”. In-viu-oprotelndlguflblfltyofwholebun drum-driedbeanmeals 152 detect the effects of trypsin inhibitor and heat treatment on protein digestibility (Hsu et al., 1977). Results of this study demonstrated the improvement in protein digestibility of the DDBMs with heat processing. Although the effects of the aqueous extractive pretreatments were not significantly different, the EXTRACT split DDBMs exhibited a slightly higher (%) protein digestibility over the CONTROL DDBM which indicated the importance of discarding leacheate, thereby removing soluble antinutritional factors. The high temperature involved in drum-drying gelatinized starch, opening the carbohydrate- protein structure and facilitating hydrolysis of proteins by the proteolytic enzymes. This same phenomenon was reported for thermoplastic extrusion involving high temperature, short time heat processing, thereby increasing digestibility of puffed corn grits (Hsu et al., 1977). The slightly higher (%) protein digestibility exhibited by the Split DDBMs over the whole DDBMs demonstrated the significance of the removal of bean hulls (containing less digestible proteins) to improving bean digestibility. Results also indicated that the enzymatic pretreatments with Viscozyme and Sprout (both containing amylases which increased reducing sugars), could have resulted in Maillard reaction as evidenced by the resultant browning reaction in the DDBMs, thereby lowering digestibility of whole DDBMs compared to CONTROL DDBM. According to Hsu et al. (1977), digestibility of bread was decreased due to the Maillard reaction between the reducing sugars which was created from the hydrolysis of starch by the enzymes in the barley malt, and the proteins. The effect of enzymatic predigestions on improved protein digestibility has potential, although it is also clearly demonstrated that the nature of the specific enzyme involved is critical. Sodium Dodeeyl Sulfate (SDS) Gel Electrophoresis Figure 39 is a graphical representation of the electrophoresis gel which was run for the whole DDBMs subjected to enzymatic predigestion. Gel Lane (A) represents the 153 xhv . .852 - 2 m 88.32 - D ”838? - E 333330 - m "eminence - ..zoam - U JON—.200 - .— ”Bax - < cod—32 - E " v.32: :3; BEES. was” 330335 Since he E033 oueofiohoofi Em mam 05 he coca—.8052 302926 .9“ Ben—m E 6 n. m o 0 m on , 3 am on I I am «a on as an mnmumnnnuwnufifiu an an E co cm on 00 ....... . Pm .nu.n.u.u.u.u.u.u. Fm ”unuuunuuuuuuunuuuuuum Pm 6 PD "g E111 3 .. an .. . mm mm m" - . ... WM ................... 8 EH 3 a 8 8 on a E E E Ev E .... m c c z “‘u) (00L x muqow annals: 154 protein components present in uncooked or untreated whole (raw) dry bean. CONTROL DDBM (B) represents the processed sample with the retained formulation water. General banding patterns between raw (A) and cooked (B) bean flour are quite similar with little indication of major band position shifts. However, the cooked sample bands were generally less intense than those obtained for raw beans. Gel lanes (C - F) present the CONTROL DDBM (B) upon exposure to selective enzyme pretreatments of the slurry. It was noted that each enzyme pretreatment resulted in a new band (Rm 60) not evident in the raw or untreated DDBM. Sprout DDBM (C) demonstrated an increased number of protein bands and intensity compared to CONTROL DDBM. It is speculated that these effects (C) have resulted from protein synthesis during the germination or sprouting process when enzymes are generated and overall enzymatic activity increased. However, no dramatic increase in total crude protein was noted for the Sprout-treated sample (Table 5). Whole DDBM subjected to Viscozyme (D), a multienzyme complex made up of cell-wall degrading enzymes, also demonstrated increased numbers of protein bands and a general increase in intensity of handing patterns, which could be a result of the release of the matrix proteins associated with the cell wall. The banding pattern obtained for Celluclast (E), a cellulase which is also a cell-wall degrading enzyme, could also represent release of cell wall associated proteins. Alcalase (F) and Neutrase (G) are both proteases and clearly demonstrate increased in hydrolytic degradation of large molecular weight proteins and partitioning of peptides. Neutrase (G) exhibited increased evidence of hydrolysis and extensive degradation through the formation of lower molecular weight peptides following enzymatic predigestion. These data demonstrate no major changes in protein patterns as a result of cooking; however, selective hydrolysis of the native proteins was evident upon enzymatic digestion and may be associated with differential ill-vitro protein digestibility. 155 Amino Acid Composition Table 11 summarizes the amino acid composition of split raw beans and DDBMs. Methionine content of split beans increased with processing; CONTROL DDBM was almost two times the amount of the EXTRACT and Viscozyme DDBMs. Cystine was not present in any of the DDBMs. Lysine in EXTRACT DDBM was two times that found in raw split beans; lysine in CONTROL DDBM was similar to that in raw beans, while a decrease was observed in the enzyme pre-digested Viscozyme. Isoleucine, valine and phenylalanine concentration increased with processing of DDBMs, with the EXTRACT DDBM containing the highest concentration followed by the CONTROL and either a decrease or a similar level observed in Viscozyme compared to the raw bean meal. The sulfur amino acids cystine/cysteine (Cys) and methionine are of primary concern in protein utilization because they are first-limiting in dry beans. Cys has been found to be more heat- sensitive than methionine. Measuring Cys of beans receiving heat treatment is important in estimating the deterioration of nutritive value due to heating. In navy beans, Cys destruction was 30% at 100°C for 10 mins. but increased with increased cooking time (Dhurandhar and Chang, 1990). In this study, cysteine content for both the raw beans and DDBMs was 0.00 prnole, which could be a result of an analytical problem. Lysine content for the Viscozyme-treated DDBM was lower than that of the other DDBMs. This could be attributed to the non-enzymatic browning (Maillard) reaction, demonstrated by the brown hue of the flakes. Lysine losses resulting from Maillard reaction involve the reaction of the E-amino group on the lysine residue which becomes blocked by a sugar, yielding a biologically unavailable lysine residue. Heating of dry bean protein improves the rate of release of methionine by in-vitro treatment with enzymes (Rayas-Duarte et al., 1988). Methionine increased with processing, and was highest in the CONTROL DDBM indicating retention of the amino acid with the original formulation water. This 156 Table ll. Amino acid content (packs) of split drum-dried bean meals. Amino acid RAW CONTROL EXTRACT VISCOZYME Asparfic 1337.63 3030.13 4264.42 2047.05 Giuramie 2952.91 5052.50 7155.03 3374.45 Hydroxyproline 43.58 0.00 97.94 43.23 Serine 1390.13 2360.30 3536.96 1706.30 Giyeine 1609.90 2343.92 4553.57 2007.64 Histidine 430.43 322.74 1337.53 566.54 Arginine 557.13 920.70 1393.47 631.51 Threonine 1111.19 2027.04 3349.60 1431.46 Alanine 1349.96 2406.43 3463.09 1609.24 Praline 1352.50 2433.36 3314.26 1652.53 Tyrosine 120.37 193.79 653.42 145.10 Valine 979.03 1367.45 2931.52 1133.35 Methionine 122.34 290.43 142.60 145.94 Cysteine 0.00 0.00 0.00 0.00 lsoleucine 677.03 1224.71 200757 305.93 Leucine 1256.67 2191.53 3659.46 1479.15 Phenylalanine 601.14 1009.36 1796.19 675.71 Lvsine 310.94 396.81 670.65 250.51 Table 17.. Methionine contentofsplit beandrurn-dried menial Truman Methionine ' (uncles Met/Mdp'ocin) A. Split Benn Drum-Dried Meals Raw 19126; 5.253 comor. 203.21;29.ma met 196.99; 153a Viscozyrrz 201.95;13.70a Sprout 207.96; 7.49:1 B. Whole Bean Drum-Dried Meals Raw 192.7o;3.39a CONTROL 220.67;0.67e Vmoayme 22617;6.36d Sprout 205.09:2.41b m 21550;6.36c Nennaae 210.66;2.36e Ccmndm 210.66;2.33e 1rI-z: ValueslethemdMI-ys “mammwmflausnnmmkwcfl zllotWaerExmwO‘CGOn-na) 3M.Splu¢mnml4¢lz CONTROLW mane-6 M Can-em m wmmmm Elly-e Wynne-“3.11." 157 observation confirms previous reports that methionine was not decreased by conventional cooking or alkaline treatment (Table 12). Trypsin Inhibitory Activity (TIA) Table 13 summarizes the units of TIA present in split raw and DDBMs. Processing significantly reduced (p < 0.05) TIA from 18,703 units of TIA per gram of raw split beans to a range of 1000 to 3300 units of TIA per gram of split DDBM. The EXTRACT DDBM was significantly lower in residual TIA compared to the other split DDBMs. The antinutritional factor trypsin inhibitor (TI) has been reported to be heat resistant, and 50-80% of the original trypsin inhibitor activity is retained after various heat treatments. TIs are high in cystine. Trypsin activity of navy beans (1.9 to 2.7%) was retained even after cooking for 40 min at 100°C. Heat inactivation of TI activity in soaked whole navy beans was more effective compared to dry roasting (Dhurandar and Chang, 1990). The significant reduction (p < 0.05) of trypsin activity in the split DDBMs indicated that they have received adequate heat processing. The drum-drying process called for an extremely high temperature of approximately 240°C; in addition, pretreatments including a 16-hr soaking period and hot water extraction (60°C/30 min) facilitated effective reduction of TI. Phytic Acid Table 13 summarizes the results of the HPLC analyses of split bean DDBMs for separation and quantitative determination of inositol tri-, tetra, penta and hexaphosphates (1P3 - 1P6). Fractional data are expressed as a percentage of the sum of inositol phosphates. Soaking has been reported to decrease the content of phytate in cereals and legumes. This is readily apparent in the degradation of phytate (1P6) in the EXTRACT DDBM (leachate discarded), with a corresponding increase in the formation of lower 158 Table 13. Heat Stable Trypsin Inhibitor Acrivity (mum. inositol phosphates (%) and phytate content (%) in split been drum-dried meals ..lmsitalflasnhatafla). 1‘0le Treatment3'4 units of'l'IA lg DDBM 193 194 195 195 Phytate (%) Raw 18.7031318d 6.72 6.33 16.21 70.74 100 CONTROL 3.292130c ND ND 25.39 74.61 100 EXTRACT 1.0881113 16.27 9.34 20.71 53.68 100 Viscozyme 2.5061-41b 4.78 1.21 15.75 78.26 100 Sprout 3.221112% ND 4.95 18.22 76.83 100 1 n=3, Means within a column followed by different letters are significantly different (p < 0.01) 2 Rayas-Duarte et al., 1991 3HotWarerExtraction 4 Raw,Whole Bean Meal; comm. Non-extracted; EXTRACT, Fresh formulation; Viscozyme, Commercial preparation; Sprout, 1% germinated slurry 5 Total Phytate 8 Sum of 1P3, TP4, [PS and 1P6 (Inositol tri-, tetra-, penta- and hexaphosphates) 159 inositol phytates. No difference in phytate content was exhibited by the raw, CONTROL and enzyme pre-digested DDBMs. These data demonstrate the potential of discarding the soak water in reducing phytate content in processed bean products. The heat treatment employed in drum-drying did not effectively reduce the phytate content of DDBMs. Lectin (Phytohemagglutinin) Table 14 summarizes results of a diagnostic assay for screening phytohemagglutinin activity. Only the raw bean split demonstrated the presence of agglutination within half an hour when reacted with the antibody (erythroagglutinin) for lectin. The EXTRACT DDBM showed no visible precipitation after reacting with the antibody, after a holding period of one hour at room temperature. Phytohemagglutinin is also heat stable, but the absence of agglutination when reacted with an antibody again indicated sufficient heat treatment of the DDBMs to inactivate the bean lectin. Lectin activity in raw navy beans was half as much in raw red kidney beans, and cooking for 10 min at 100°C inactivated all lectin activity in navy beans. Wet heat was more effective in inactivating lectins than dry heat (Dhurandar and Chang, 1990). Coffey et al. (1992) reported that purified phytohemagglutinin is sensitive to enzymatic treatments, particularly proteolytic digestion, hence the hemagglutinating activity and enzyme pre- digested DDBMs warrant investigation. Further, erythroagglutination by lectin is affected by the molecular properties of the lectin, cell surface properties, metabolic state of cells and conditions of assay such as temperature, cell concentration and mixing, hence the lectin assay method to use should take these factors into consideration. Conclusion The composition of the drum-dried bean meals varied with the process pretreatments utilized. CONTROL and EXTRACT DDBMs did not differ significantly in their oligosaccharide content, but were significantly different in their in-vitro starch 160 Table 14. Visual reaction for screening of dry bean lecrin ( phyooheningglnnnin)1 Sample Sample Volume Visual Reaction (ul) Andbody (Ab) 10 + Raw Navy Bean Splits O 1 - 20 - 30 - 40 - Raw Beans with Ab (ul) 10 +- 20 +4- 30 +++ 4O +—+-++ INDBhiEXHILACT‘ 10 - 20 - 3o - 4o - INDBthDGniACHT with Ab (10 til) 10 - 20 - 30 - 4o - EkkmmdeWuur 10 - 1 n=3 2 + indicates presence of a precipitate; number of + indicates the degree of precipitation - indicates absence of a precipitate 161 digestibilities. Protein digestibility of the DDBM was significantly enhanced by the drum— drying process with increases approximating 9 % over the unprocessed bean. The enzymatic pretreatments of DDBMs prior to drum-drying significantly increased starch availability by disrupting intact cellular structures and exposing starch. It was proposed that the denaturation of the protein matrix increased the accessibility of the a-amylases to starch molecules. Sprouting of beans demonstrated potential as an extractive pretreatment to improve dry bean digestibility and warrants further investigation for applications in appropriate village-level situations in LDCs. Results of this study suggest that dry bean digestibility has been substantially improved by the extractive pretreatments employed. Oligosaccharide content was reduced by the aqueous and enzymatic pretreatments. Trypsin activity has been significantly reduced and phytohemagglutinin was inactivated by the heat treatments utilized. Results indicated that indigestible starch may be the main factor affecting dry bean digestibility, which could also be implicated with the flatulence problem associated with dry bean consumption. Ho: the pretreatment of dry beans by physical and biological methods will not enhance their digestibility through removal or inactivation of interfering components prior to drum-drying. Reject the Ho as stated and conclude that pretreatment and processing influences bean digestibility. CHAPTER II FUNCTIONAL CHARACTERISTICS OF DRUM-DRIED BEAN MEALS AND THEIR INCORPORATION IN SELECTED FOOD SYSTEMS Introduction Decline in overall bean consumption in the United States and potential dietary benefits of beans have prompted investigations into the use of legume flours in food systems (Zabik et al., 1983a and b). Legumes are successful in increasing the quality of protein through amino acid complementation and through increasing the total quantity of protein in formulated food products. The utilization of bean flour from dry roasted split navy beans has been investigated for bread making (D'Appolonia, 1978). The effect of the addition of navy bean flour and concentrate on the rheological properties of dough and baking quality of bread were studied by Sathe et al. (1981) and Lorimer et al. (1991). Lee et al. (1983) reported on the physicochernical characteristics of dry-roasted navy bean flour fractions and demonstrated differential functional performance of fractions based on processing conditions. The substitution of navy bean flour for wheat flour in pumpkin and banana breads and doughnut holes produced acceptable and nutritious products (Uebersax et al., 1982; Uebersax and Zabik, 1986). Drum drying of dry beans into precooked flakes, meals or powders could be used to produce versatile ingredients in baked products, convenience food formulations or replacements for cooked bean purees or refried beans. There is also potential in the development of improved weaning food formulations especially suitable for the LDCs. The Null Hypothesis tested in the studies is stated as follows: HozDrum-driednavybeanmealsdonotpossesspotential foruseinfoodsystems. The purpose of this research was to characterize the functional properties of preheated drum—dried navy bean meals produced using selective predigestion or extraction 162 1 6 3 treatments and to evaluate the suitability of these bean meals in model formulated food systems (quick bread and weaning beverage). This chapter is comprised of three studies as outlined in Figure 40. Study II-l involved the characterization of the physical and functional properties of the drum-dried bean meals (DDBM); Study II-2 focused on the utilization of these various drum-dried bean meals in a quick bread (pumpkin) 1311111101. and Study II-3 involved the incorporation of DDBM in a weaning beverage formulation. Drum-dried meal prepared by aqueous exu'action of split navy beans termed "EXTRACT" (soak, rinse and cook waters discarded and replaced with fresh formulation water) and enzyme predigested (Viscozyme) split bean drum-dried meal were utilized in Study II-3. Materials and Methods Split dry navy (Phaseolus vulgan's) beans grown in the 1991 crop year were obtained from the Cooperative Elevator Company, Pigeon, MI. The beans soaked and hydrated for 16 hours. (25°C) were subjected to hot water extraction (60°C/30 mins.) prior to milling to a homogeneous slurry. Heated bean slurries were dried using a double drum-dryer. The physical and functional properties of the drum-dried bean meals, including water holding capacity (WHC) and nitrogen solubility (N SI) were evaluated using standard AACC (1984) methods (Figure 40). The microstructure of the DDBMs was observed under Laser Scanning Confocal Microscopy (LSM). The recipe of Rombauer and Becker (197 8) was followed in making the pumpkin quick bread. The composite flours consisted of wheat flour and drum-dried bean meals blended in 80:20, 60:40 and 40:60 ratios, respectively (Figure 41). The drumodried bean meals were ground to a flour using the Fitzrnill with a 0.04 mesh screen. All formulation ingredients were weighed to the nearest 0.01 g, sealed in clear polyethylene bags, randomly coded and held at —23.9°C until blended, mixed to a batter and baked. Three 164 FUNCTIONAL CHARACTERISTICS OF DRUM-DRIED BEAN MEALS AND THEIR INCORPORATION IN SELECTED FOOD SYSTEMS SPLIT NAVY BEANS 3511-:an PRETREATMENTS 1 | | l | l CONTROL EXTRACT VISCOZYME SPROUT DRUM-DRIED BEAN MEALS Functional Properties Incorporation in Food Sysrems Color Solubility WSI WAl WHC Bulk NSI Quick Bread Beverage density (20%. 40%. 60%) (5%. 8%. 10%) 1 OBJECTIVE QUALITY EVALUATION O . I O O m. gure . Th perrmental flowchart for Study II . Functronal CharaCterlstrcs of Dru H 40 dr'feccleean Meals and their Incorporation in Selected Food Systems 165 SPLIT BEAN DRUM-DRIED BEAN FLOUR l I | I CONTROL EXTRACT VISCOZYME SPROUT l l Pumpkin Bread SUBSTITUTION LEVELS 0% 20% 40% 60% BAKING (3 X) OBJECTIVE QUALITY EVALUATION Figure 41. Flowchart of the experimental desi for Stud II-2' Incorpo ' drum-dried bean flour in pumpkin Buread y . ranon Of 166 replications of each variable were baked in a rotary oven at 177°C (350°F) for 45 mins. Objective quality evaluations were conducted on both the batter and baked products (Figure 41). Different concentrations ( 5%, 8% and 10%) of the weaning food beverage were prepared by homogenizing DDBM slurries with 200 - ml deionized distilled water in a 400- ml polyethylene beaker for 2 minutes. A Tissumizer (T ekrnar Co., Cincinnati, OH) with the large probe size (# 180) was used. Figure 24 summarized theevaluation ofthe physical quality characteristics of the fully prepared bean beverage. Results and Discussion Physical and Functional Properties of Drum-Dried Bean Meals Plate 6 illustrates the general appearance of the raw split beans and split bean DDBM, as well as representative crystalline structures of the DDBM observed under a stereomicroscope (Wild Type 256530, Heerbrugg, Switzerland). Plate 7 shows the fine crystals of the EXTRACT DDBM compared to the coarse crystals of Viscozyme DDBM. The microstructure of the DDBMs and starch granule appearance were also observed under LSM (Plate 2) and discussed in detail in the study on starch digestibility (Chapter I). The physical and functional properties of the split DDBMs are summarized in Table 15. The DDBMs exhibited a neutral color, and although CONTROL samples appeared slightly darker than the EXTRACT samples due to the retention of the original formulation water, they were not significantly different (p < 0.05). The DDBMs possessed a bland flavor, and did not exhibit the distinct and frequently objectionable "beany" flavor. The different extractive pretreatments did not have a significant effect (p < 0.05) on the water holding capacity (WHC) and soluble solids content (°Bx) of the DDBMs, but had a significant influence (p < 0.05) on solubility indices (WSI and WAI) and bulk density (g/100 ml) . WAI and W8] give indications of likely cold-paste viscosity and gelatinization, respectively (Holm et al., 1985). The enzymatic predigestion treatments 167 \ \\ \ HI: \\ SI’IIIS (‘()\'I'R()l G \\ \'l‘lxR l' \ IR \( "|‘I()\ Plate (1. General appearance of (a) raw navy bcan splits and (h) [iX'l‘RAC'l' DDBM Plate 7. Crystalline structure ot‘drum-dried bean meal under a stereomicroscope (50x): (a) EXTRACT (b) VISCOZYME 169 at...“ eossEom am; £55m 82.830... _n_o._oEEeU .Eefieas ESE—Eco. 52"— ..rugxm 62253-82 455.28 m A 36 v a .n 86:20.:6 535:3.» 286:. 5:38 :28 5.23 325. Santa: 32338 38:3... 33 82.? :32 ”mu: m A 36 v a .n ”853:6 385:»: 2865 5:28 :28 £53 €28. 828:3 8253—. E85: 93 moan.» :32 ”Nu: _ 35.33... 8343.2. .8345... 86.33. _ . a. 5.32 d 38.3. ...e 3 3.38.2 .8542..- 68.38.: 59% 25.33.: 32.352 38.3 a... 834%.. _ 58.3.... .o be. a}: .5 38.332 35.36. .c 38.93. .2 2.5835 25.33... 83438 382.8... .5343: 2.34:... 322.423 38.322 2348.... 2938.2 ELEV—km 25.3.5. 8. .332 £3.48... 32:: 38¢: _ .c 23.4.: .n 2:38.: 2:38.? 2348.? 155.28 am. A 8:. C 2.328. :3: as: as: .... ... ._ .353 «3.28 .3: ~52 .23 .53 3:3 .335 3353.593 23:. Sax. voters—E. .33 5% ..e nonhuman 3835 93 333.5 .2 use... 170 (Viscozyme and Sprout) significantly increased (p < 0.05) the water absorption index (WAI) of the DDBMs. WAI serves as an index of product functionality and is therefore important to obtain a maximum value. Avin et al., (1992) reported an increase in WAI of red kidney beans with increased extrusion temperature, but no significant influence on density and water solubility index (W SI). Incorporation of Drum-Dried Bean Meals in Food Products Quick Bread A quick bread (pumpkin) formulation was utilized in this study because it minimizes the problems previously encountered with incorporation of legume rich breads and bread products (decreased flavor, volume and color) by using spices, ensuring consistent specific volume through the method of preparation and decreased color change. Quick breads are baked as breads, yet they lack a strong gluten development and contain a high ratio of sugar to flour, as in a cake system; hence, incorporation of protein substitutes is feasible (Dryer et al., 1982). There were no significant differences (p < 0.05) in the color of the pumpkin breads with increasing levels of drum-dried bean meal substitution (Plate 8 and Table 16). Since these products are characteristically dark, no objective difference was observed in the color of the products due to the promotion of Maillard browning reaction generally associated with increased levels of reducing sugars inherent in the bean flour. Bread loaf volume decreased with increasing levels of drum-dried bean meal substitution, with differences most significantly apparent (p < 0.05) between the Reference (all-purpose flour, 100% level) and breads prepared with 60% drum-dried bean meal (particularly, CONTROL and EXTRACT) (Plate 9). Bread volume (cm3) decreased with a corresponding increase in crumb density (Table 16) when levels of DDBM substitution were increased, because of increased gluten formation and its inherently more compact product structm'e. 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With higher levels of substitution (60%), it was possible that the DDBMs were not fully hydrated by the available fluid. Shear force values increased (i.e., decreased tenderness) with increased level of bean meal substitution; however, no statistical differences were detected among the various substituted-pumpkin breads (Table 17). It is likely that increased shear force values are a result of the decreased gluten formation and the resulting decrease in size and number of the air cells present within the crumb structure. With higher levels of DDBM substitution (60%), bread density is greater as a result of decreased air cells needed to develop and expand gluten, which in turn leads to increased shear resistance force. Table 18 summarizes the textural data obtained from the Texture Profile Analysis (TPA) of the pumpkin breads. The TPA is a two bite method of texture analysis in which the food is compressed twice and a complete texture profile of the sample is calculated from the data recorded. A generalized TPA curve, a typical pumpkin bread (CONTROL DDBM) curve and the definition and calculations of textural parameters are illustrated in figure 42. Hardness is the area under the primary force deformation curve. Adhesiveness refers to the area under the third curve measured during the second bite in the downstroke mode. Cohesiveness is obtained from the ratio of area 2 (adhesive force) to area 1(hardness) in the upstroke mode during the first bite. Stringiness is measured as the distance of area 3 (adhesiveness) from area 1 (hardness) measured in the upstroke mode, while springiness is measured as the distance ofarea 2. A typical pumpkin bread curve consists of only two peaks with areas corresponding to the parameters hardness and adhesiveness. Hardness values increased with increasing levels of drum-dried bean meal substitution, for all the different pretreated DDBMs. Increased adhesiveness. gumminess (hardness x cohesiveness) and chewiness (gumminess x springiness) were also observed with increased DDBM substitution levels. Conversely, springiness and cohesiveness of the pumpkin breads decreased as substitution with drum- dried bean meals was increased. These TPA results confirm observations that as DDBM 175 $300 $9 :5: 82.3 $9: .mozmdmmmm p.033 cog—3:28 smut 639:9. 25.03. Emma .ngm ”Eman— uoaahxméez JOmFZOU N A36 v s 580%“. 3.58:3»? 8a 338. Bengt .3 330:8 28:. ”mu: _ azfiwmév «as was ancémadfl $8 «aflfiwoaamm navdwmfi; Savages”... $9. sva.m~+mo.mvm «NS +8.8 a-.~_+8.-~ $3 kacmmm 2_.8_Mo_.mnm Sod Hhvdm «a: was: $8 «355363 «32 Mafia «and H862 $3 a8.o~+m>.2m 2n." +3.2 Sad—+3.8. seem HE>NCUE> ashmmmmadmv «cadwcndm «Nod Madm— $8 «3.0 +2.63. £3. 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FORCE 177 A Hardness 1 Fracturability Point Hardness 2 U q; :-:-:-.-:-:-:-:-: Qt .-:.:.:-:-:-:-:-:-:~. .5 g sisisisfsisisisisisisis ............. 2 o :5§§§§§§§§§§§§§§§§§§§§§§§§§é§§§§§§§§§§§§§§§§§§§ ...... 2 < ' ' ' :‘2' 23332325232525: 522222222: o °- -E:E:E:E:EIE:E:E23:33:5:323:52:ErEtirErirftirirS 531523352523: a '- .:E:E:£:E:EIE23323522313323:33525132322215: .EtétirérirEIEIEIE ..2iéiiiiiééiiiiiiéiESEEEEESEEEEEEESESEEES2323333532? Stringiness . . . . Area: 0 ..... , . . . .- ........ F: ..... T-t-f-T-i-T-.~I-t-?-f-.- A ...... : ...... Area: 5%?! -=:s:2:2:2:2:z:s:sgs:=-' kiss:- Adhesive Force vfi as *——I Downstroke Upstroke Downstroke Upstroke or HI Typical Product Curve (control pumpkin bread) Figure 42. A generalized Texture Profile Anal 0 First Bite Second Bite PARAMETER FORMULA V Hardness Value of Hardness 1 Cohesiveness Area 2/Area 1 Adhesiveness Area 3 Stringiness Distance of Area 3 Gumminess Hardness x Cohesiveness Chewiness Gumminess x Springiness Springiness Distance of Area 2 Fracturability User Defined pumpkin bread TPA curve. TIME or DISTANCE UNITS Lbs. or Newtons Dimensionless (ratio) ln.-Lbs. or Newton-Cm In. or Cm Dimensionless (ratio) Dimensionless (ratio) In. or Cm Lbs. or Newtons ysis (TPA) curve and a typical 178 substitution levels increased, pumpkin bread volume decreased, with a corresponding increase in crumb density and shear force. Plate 10 demonstrates the cellular microstructures of the various pumpkin breads substituted with 20% DDBM. The pumpkin bread with all-purpose flour (100%) demonstrated a thick protein matrix enveloping starch granules. The microstructure of the DDBM-substituted pumpkin breads were characterized by a thinner, discontinuous gluten matrix over the flow starch granules. The protein matrix is indicated by the fluorescent bodies. The flour and bean starch granules can not be easily distinguised, but widt the low level of substitution, flour starch granules predominate. Microstructure of pumpkin breads with the enzyme pre-digested DDBMs (Viscozyme and Sprout) (Plate 10d and e) demonstrated a more extensive gluten matrix compared to those substituted with CONTROL or EXTRACT DDBMs (Plate 10b and c), and could partly account for the slightly taller height of resultant pumpkin breads. Weaning Food/Be verage The beverage concentrations utilized in this study were 5%, 8% and 10% drum- dn'ed bean meal (DDBM) suspensions. Preliminary trials utilizing lower concentrations (2.5% and 4%) of the beverages (Appendix D) demonstrated very limited stability, whereas concentrations higher than 10% exhibited too viscous a consistency for a weaning beverage. Table 19 summarizes the physical characteristics of the bean beverages. The soybean control and the DDBM beverages all exhibited a neutral color. The extractive pretreatments employed did not have a significant effect (p < 0.05) on the color of the weaning beverage. Total solids increased with the increased beverage concentrations, and the enzyme predigested beverage exhibited a higher soluble solids content compared to the product with EXTRACT DDBM. 179 Plate 10. LSM micrographs of pumpkin bread cellular microstructure: a) Reference (100% all-purpose flour) b) CONTROL DDBM c) EXTRACT DDBM d) VISCOZYME DDBM e) SPROUT DDBM THlS PHOTOGRAPH WAS PRODUCED BY MSU I \NSTRUCTlONAL MEOlA CENTER (517) 353-3960 MSU rs an Attrrmatwe Action ! Equal OppOrtumty institution . 180 God v a a 353% asuama 38% 9.3 35.2. 58 as? 3.2 age ".835 268a «8 82.; :82 a": «8.0395 noudflcod 8.0 5.2.3.86— «Bdfiood «fidflfimn 35°83 «Sdflvod «2.393 8.0 «Sdfioos Seduced «Sdflhmn Baum— ouuegom 53m 83 amodflnns £8.0Hon.~ 3.0 flodflnd «8.32.7 «2.93.? 08.6955 «8.9355 £8.33.— 86 «modufin «8.386. «8.3"an 5% our—95m :3: a.» «modfivné 28.362 odd fiode.» «8.32.. «863%? 25803, «8.3%.». 38.0.30.— 86 «86.3.0 anodflovd. «8.9593. 5% «9:26.— 33: 8m 33 came .5 .3 a 8:8 as... 8:8 0528 E. 8.8 39am .835 83 «5803 a 835.950 3%.: .2 3.3 181 Visual stability of the weaning bean beverages was expressed as the amount of clear, separated supernatant (ml) plotted against time (min), within a 2—hour observation period A commercially prepared soybean based weaning formula (Isornil Soy Protein Formula, Ross Laboratories, Columbus, OH )(15%) was utilized as a comparative control. Frgure 43 demonstrates that for both the EXTRACT and enzyme predigested (Viscozyme) bean beverages, suspension stability increased with increased beverage concentration. The 15% soybean formula was completely stable with time and did not exhibit any settling of solids. With very low concentrations of the beverage (2.5%, Appendix D), settling of solids with a corresponding increase in separated supernatant, occurred almost immediately after homogenization. The 10% Viscozyme sample closely approximated the stability of the soybean control; however, the consistency was highly viscous. In general, the Viscozyme DDBM beverages were relatively more stable than the EXTRACT DDBM suspensions. Plate 11 demonstrates the effect of extractive pretreatments as well as concentration on the relative stabilities of the weaning beverages. After a one hour static holding period, the 8% and 10% concentrations were still stable, particularly the enzyme- predigested (V iscozyme) sample. However, the 10% level might be too viscous a product for a weaning food. A recommended weaning product is one which will produce a low paste viscosity or high calorie density to prevent choking of infants, hence the 8% level was judged to be a more appropriate level. A micro-quantitative method designed to evaluate beverage stability involved measuring spectrophotometric Absorbance (565 nm) (or % Transmission, Appendix D) of dilute suspensions prepared using differential quantities (ranging from 2.5 to 40 ul) of the weaning beverages prior to the settling of the solids immediately after the homogenization step. Figures 44 to 46 illustrate the effects of the different concentrations (5%, 8% and 10%) of EXTRACT and Viscozyme DDBMs on the stability of the bean beverages. The regression equations derived demonstrated good correlation between the absorbance readings and concentration, and provided a tool to quantitate the influence of DDBM 182 ”Vin-y- law lfiSoy 2.5 33.9.2.3. 3.9.2.3 200 150 100 50 Time (min. may 4 roam Yf'vrvr'rr'f'rvfiVVvVI'V’v' 1““1“‘11‘q4““““‘q1 .‘1“““““ ““ ‘J““““‘ ‘ w w m m 0 -10 ..l. ...-cubesla ...-bosom 300 200 100 ‘l'lmo (min) Figure 43. Comparative visual stability of bean beverage from DDBMs and soy formula 183 VISCOZYME Wing, r G ‘ _ ' “"“""cr-m.,m.... Plate 1 1. Appearance of weaning beverage prepared with different levels (5% 8%, l()‘7c)of pretreated (a) EXTRACT and Viscozyme DDBMs and (b) CONTROL and Sprout DDBMs “CI-l MI.) mqu-muss EXTRACT W ‘SSWb-n "unmana- ".001! um v v 0.2 0.3 on...” p) he“ AWINJN “TRACT-ll Ii Win-m - um y. Aunt-.0410.- In... I g. a '1 o g c 3 r . . . . 0.0:. 0.00 0.1 0.20 0.: mm—) M‘anhlfimflm m lumba- I 1 i “ a d t I I q u .1. 0.: Count-lb (DDIMg-a) y-OJWvL’II‘I Iva-out - n ' ...... 0.1 0‘; or: of; 0.5 Quintin-Ml.) I“.- y- mow-haunt Ira-0.” I a 1 1 I g r t . . u '0." 0.04 0.0- 0.." o.i0 0J2 more». III) 185 concentration on stability of the beverage suspensions. As sample concentration was increased, absorbance reading increased (decreased % transmission) which indicated a decrease in settling of solids or a corresponding increase in suspension stability. Figures 47 to 49 demonstrates that at higher concentrations (8% and 10%), the Viscozyme DDBM beverage exhibited higher absorbance readings, indicating a relatively more stable suspension than the EXTRACT DDBM beverage. Figures 50 and 51 illustrate the comparative transmission (%) of the DDBM beverages over time, another index of stability/settling of solids with time. The higher beverage concentration (10%) exhibited lower transmission (%), indicating decreased settling of solids or increased suspension stability compared to the lower concentration (5%). The 15% soybean control exhibited consistent transmission (%) with time, indicating no separation of solids and therefore complete stability during the period studied. Figure 52 summarizes the apparent viscosities of the various weaning bean beverages measured using a Brookefield viscometer. The 8% and 10% concentrations of the enzyme prc-digest (V iscozyme) beverage were significantly (p < 0.05) higher than the corresponding concentrations of the EXTRACT beverage. The 5% beverages did not differ significantly (p < 0.05). Relative viscosities of the 5% beverages are illustrated in Figure 53. Viscozyme was significantly (p < 0.05) higher than the 5% EXTRACT beverage, confirming the results for apparent viscosity . The 8% and 10% concentrations produced extremely viscous suspensions which were too thick to pass the Oswald pipet; hence relative viscosities were not measured. Figures 54 and 55 illustrate the apparent and relative viscosities of the bean beverages with the addition of commercial emulsifiers and stabilizers (Methylcellulose, xanthan gum, Carageenan systems - Seakem®, Lactarin MU®, Viscarin GP and SD®; details in Appendix D) obtained from FMC Corporation (Marine Colloids Division, Philadelphia, PA) . Results demonstrate the dramatic increase in apparent viscosity with the addition of 1% levels of carageenan systems (LactarinO, Viscarin® GP and SD and Seakem®). The emulsified beverages demonstrated greater Absorbance (0“ an) Absorb-co (0“ an) About... (“I In) 1 86 0 i .1 i 4- "i '1 4 V“- 11 q o - , - , - 0.001 0.002 0.000 maufi M0.wa¢$% b- m u 1.2" 1.0-1 1 0.0-4 4 1 0.0-‘ 1 d 0.4- i 01-1 d 0.0 - , - 1 - 0 t 2 3 MM“ M40. CWW‘IS EXTRACT-d nay-prod“ (Vb-yank". 4 i h :1 4 m :1 d I q 4 0 - v - . fi fi f 0.000 0 001 0.002 0.000 0.000 MM“ MO. C sharia-110% many-Wham Transmission (9.) 187 60 50 < ‘ fiEXiIACi 1 ‘0 at x ct 20 " “M J L : I 'o . manner 4 ms.) 0 1 J j.’;:i.,::==;===_____. 0 50 100 150 Time (min) Figure 50. Comparative transmission (%) of bean beverage 'l‘ransmlulun (%) separated supemate from DDBM EXTRACT and soy formula ‘0 1 1 1 1 1 1 1 1 1 ”‘1 4 I 1 1 1 Sfivkoan 204 1 1 I 1 1 ‘0 .1 “Vineg- 1 1F._—.——fl-—l-—-fiv;-————f 1/ ' lav-my- I I 15.-Soy o e ' . f ' - r ' - 'r - O N 0 fi 0 a O 80 Time (mint Figure 51. Comparative visual stability of bean beverage from DDBM and soy formula 188 IIIIIIIIIIII \\\\\\\\\\\\\ IIIIIIIIIII’ \\\\\\\\\\\\\ \\\\\\\\\ I’ll/Ill \\\\\\\\\ III/I’ll A38 ...-3.: drum-dried bean meals at different Figure 52. Viscosity of bean beverages from concentration levels A8: to: so 0!; 15% Say Figure 53. Time for the bean beverage (5 %) to flow through the two marks of an Oswald pipette Viscozyme Extract l 8 9 stability (Figures 56 and 57) by exhibiting less settling of solids over a given period compared to those bean beverages without added emulsifier. The levels of emulsifiers utilized in this study were based on the recommendations of the manufacturer according to the dispersion media (water or milk) and functional categories or applications (gelation, viscosity and cold solubility). Conclusion Results demonstrated the feasibility of incorporating drum-dried navy bean meals in pumpkin quick breads and weaning food/beverages. Acceptable quality breads were produced at the 20% and 40% levels of substitution. Enzyme predigested DDBMs possess great potential in weaning food formulations, especially at the 8% concentration level. The use of indigenous enzymes ( i.e., sprouting ) to modify the functional properties of DDBM used in weaning beverage formulations warrants additional research. Potential optimization of pretreatments exists to obtain specific functional properties of the meals. High quality products were obtained by the extractive pretreatments and drum-drying process. The functional properties demonstrated through incorporation of DDBM in a quick bread indicated potential use in a broader spectrum of baked products. Potential of the drum.dried bean meals in weaning food formulations to enhance the nutrient density of infant diets also warrants further research. Ho: Drum-dried navy bean meals do not possess potential for use in food systems. Reject the Ho and conclude that drum-dried bean meals possess functional properties suitable for incorporation into nutritional food products. 190 .253 3.! va- 5.’ «OEBJ a! alluvial 1A- 5.! '08.; I: .! r Stan: has-...: I: i. 3506 .In:aa8 ... u All-g!!! n. «.o ... 2. n... «.9 ... ... . . p re .2 .o I. m .8 n .8 '2 ( «I . it |0Il .3 huh?!“ |0lu «3.5::- aai. .Iarl Into!!- |0lr .3185)!!— ll sanit- |0i .. l 381 also list..- o... .4. £010.86 .34. algae-.3 5.! nil-1.1%. Iii-I033! ‘1}! ‘n Ilb<§ ‘nkdulfi. dn :3: BE 'n‘ii<‘§ ”muwnw. m m,‘a_3_fi.-_ m (I) -”—11 ('b) ”Fm CHAPTER III MICROWAVE HEATING CHARACTERISTICS OF WHOLE BEANS and BEAN STARCH Introduction A major deterrent to the utilization of dry beans is the long cooking times involved in their preparation. Consumers favor convenience foods which provide consistently high quality with minimum delay. Commodities receiving some pre-preparation which reduce cooking requirements enhancing the potential for microwaveable reheating are sought. Although numerous specialized applications of microwave energy for processing or cooking food products have been developed, little attention has been directed towards its utilization in legumes. Microwave heating has a direct potential for use as a preconditioning treatment for process time reduction of dry beans. Starch granules undergo physico-chemical changes during thermal processing. Dry bean starch granules are resistant to swelling and rupture; their gelatinization temperatures range from 60°C to over 75°C, relatively high compared to many standard cereal grains (Hahn et al., 1977). Bean starch has a higher percentage of amylose ( generally 30-37%) than most plant starches, which increases the potential for formation of indigestible retrograded starch (Hoover and Sosulski, 1985). During cooking, some of the amylose leaches from the starch granule. Since the cell structure in cooked beans remain intact, much of the leached amylose remains within the cell and fills spaces between protein bodies and starch granules. The unique properties of bean starch can have practical applications in food systems, particularly in modifying product textural quality. The Null Hypothesis of this study is stated as Ho: Microwave energy will not adequately disrupt starch granules and facilitate gelatinization in rim to irrrprove whole seed cooking, functional properties and digestibility. 191 192 The objectives of the studies were : 1) to evaluate microwave heating as a pretreatment to dry beans prior to processing, storage and final preparation and 2) to compare the effects of microwave and conventional heating on the physical and functional properties of navy bean starch. This chapter is comprised of two parts : Study I - the microwave preconditioning of whole dry navy beans and evaluation of resultant bean characteristics; and Study 11 - determination and comparison of the effects of conventional and microwave heating on the physical and functional properties of isolated navy bean starch were compared. Materials and Methods Microwave Preconditioning of Whole Dry Navy Beans The experimental plan for this Chapter is presented in Figure 58. Standard (C-20) whole dry navy beans were ambient soaked for different time periods and allowed to equilibrate at 4°C for 2 days. The beans were thus rehydrated to different moisture contents ( range 47% to 54% ) and subjected to microwave heating at three microwave energy levels (440, 590 and 740 watts) for 2 minutes in a Radarange microwave oven (Model - RS458P, Amana Refrigeration, Inc.). A microwavable pressure cooker (Nordicware) was used to contain the beans and reduce dessication during heating. The heated beans were subsequently packaged in polyethylene ziplock bags and stored at (-)18°C. The frozen preconditioned beans were heated in the microwave oven for 30 seconds. Microwave heating time was established after a come-up time ranging from 3 to 7 minutes. Control beans were conventionally cooked in an open kettle for 15, 30 and 45 minutes. Texture of microwave and conventionally cooked beans were evaluated using a Kramer Texture Test System ( Model TMS-90) equipped with the FT 3000 transducer and MICROWAVE HEATING CHARACTERISTICS OF WHOLE BEANS and BEAN ST ARCH 193 DRY NAVY BEANS PRODUCT APPUCATION] CHARACTBUZATION OF TRIAL HEATED ST ARCH WHOLE BEANS Mm ' ‘Wb'fj" BEAN STARCH W7 . [4.8 % Mm . 34.9 % Amylase 'MI' ca' _owxva r'iiacoanmomo -02¢ a. Man . 47445 Noam . I 6 hours soak . Room Town . PM Levels: MICRO“! AVE 440 W. 590 W, 740W TING . Tune - 2 sin. “EA . 70. an. 90 C , 100 c . 2 min. FROZB‘J STORAGE - 18 C I FUNCTIONAL PROPERTIES CHARACIERIZATION MICROWAVE HEATING] - Nu”! ram , . Sobrbrhrylnda I . Degree (JIM . W Viscosity & elasticity EVALUATION OF PRODUCT . Tantra . Color . Mia-cam Figure 58. The experimental flowchart for Chapter III: Microwave preconditioning of dry CONVHITIONAL beans (Study 1) and microwave heating of bean starch (Study 11) 194 the No. 015 standard multiple blade shear compression cell. Color of beans was obtained using a Hunter Lab Model D25-PC2 (Hunter Associates Laboratory, Inc., Reston, Va.). Cellular structure and starch granule appearance of microwave pre-conditioned beans was observed under SEM (Model JSM 35CF, Japan Electron Optics Limited, Tokyo, Japan) and LSM (Carle Zeiss, Inc., West Germany). Microwave Heating of Bean Starch Navy beans (Fleetwood cultivar [firm texture) grown during the 1987 crop year in research plots in Saginaw, Michigan, were used in this study. Bean starch was isolated using the method described by Naivikul and D'Appolonia (1979) with slight modifications. Commercial corn starch (Argo R Pure Corn Starch, CPC International Inc., Englewood Cliffs, NJ) was used as a comparative control. Proximate Analyses were conducted using the standard methods (AACC, 1983 and AOAC, 1984). The amylose content was determined by a modification of the colorimetric procedure of Morrison and Laignelet (1983). Starch slurries were heated in screw-cap culttue tubes ( 14 mm ID.) using a Radarange microwave oven (Model - RS458P; Amana Refrigeration, Inc.) with a 700 watt rated power. Temperatures were monitored using a Luxtron 755 unit with MIW-02-10740 fiber optic probes. For conventional heating, starch slurries were heated in screw-cap test tubes (14 mm ID.) placed in a thermostat-controlled water bath. Bean starch physical properties including swelling power, solubility, degree of syneresis, gel rheological properties and examination of cellular structure and starch granule appearance using SEM were evaluated. 195 Results and Discussion Microwave Preconditioning of Whole Dry Navy Beans Figure 59 illustates the moisture gain in dry beans during soaking, yielding a typical water uptake response which plateaued after 5 hours of soaking at room temperature. Moisture content of the soaked beans ranged from 50 to 55% during an overnight soak period (16 hours). These results are consistent with numerous previous reports (Uebersax, M., 1985; Tittiranonda, A., 1984; Burr, et. al., 1968). Significant differences in bean texture (p < 0.05) were observed after microwave preconditioning (Figure 60). Preconditioned samples with higher initial moisture content (54%) possessed a softer texture (required a lower shear force ) compared to samples with lower initial moisture content (47%). Figure 61 demonstrates that texture of the frozen preconditioned samples was significantly softer (p < 0.05) after the 30-second cook. Lower microwave energy level (440W) was associated with longer come-up times which resulted in significantly higher weight gains (Figure 62) (p < 0.05) during cooking due partly to longer sample/water contact. Figure 63 illustrates that as weight gain (% above soak weight) increased, the texture of microwave cooked bean samples approached that of the conventionally retorted 115°C (240°F) canned bean samples, regardless of the preconditioning microwave power levels used. Initial bean hydration level and the maintenance of moisture during microwave heating are critical factors which affect final product texture. Sufficient thermal energy and adequate moisture are needed to produce a desirable and palatable texture. A desirable texture of cooked beans was associated with a weight gain of approximately 30% above the initial bean soak weight. Figure 64 demonstrates that color of the final product (expressed as lightness, L) was a function of both initial moisture content of the bean and microwave processing power level. In general, beans of softer texture, darker color and higher yield were produced using the Content (96, w.b.) Holatura 196 60 1 + fl 50 -' 40 d 30 - 20 - I 10 r r 0 1 O 2 O Soak Tlme (mln.) Figure 59. Moisture content of dry navy beans soaked at 25 C for various time periods Shear Force (N) Shear Force (N) 197 4000 c 1%“!qu WWW) I 440W ‘ Z 590w : D 740W 3000‘ L 50 54 Been Mdature Quint (5, rub.) Figure 60. Maximum force required to shear navy beans preconditioned by microwaves In a Nordicware Presure Cooker zooo WWau-p I 440W Minn-”much I 590w . b I 740W 47 50 54 Been MdstnreCartcat (%, sub.) Figure 61. Maximum force required to shear preconditioned navy bears after reheating (0.5 min., 740 W) in a Nordicware premre cooker 198 MW 440W ‘ (Mbowavel’owulaveh) ISOOW Weight gain (5 above soaked wt.) l H5EliUllllllllltlilillii limilillliili! 50 54 WWMUJ.) Figure 62. Total incense (‘5 above soak weight) in weight of preconditioned Cooked Product Texture (Max Shear Force, N) navy beans after retreating (0.5 min., Nordicware pressure cooker) 1000 1400 - ' y - 1034.5 ° 10%-Leeann) Fl‘z - 0.4e2 1 1200 - we. Cab (95 Above Seded Weight) Flgure63. Maximum forcerequlredtoshearnavybeanscookedlna conventional retort (45 minutes, 116 C) or subjected to microwave energy levels in a Nordicware Pressure Cooker Lightness (L) value 199 80 J 60‘ .— E El 440w 40.. E 590W E E 740W 20‘ 'E O :— SO Moisture Content (96, Mb.) Figure 64. Color of final product as affected by post-soaking moisture content and microwave energy levels used for preconditioning (Nordicware pressure cooker) 200 pressure cooker at lower microwave energy levels with subsequent longer total cooking times (Table 20). Plate 12 demonstrates that the average diameter of starch granules in soaked beans was approximately twice as large as that in dry seeds as a result of water uptake during the 16 hours of ambient soaking. Microstructm'al changes including cellular disruption and separation were observed as a result of microwave preconditioning and reheating (Plate 13). Microwave Heating of Bean Starch The chemical composition of corn and isolated navy bean starch is presented in Table 21. The moisture and protein contents of the two starches are significantly different (p < 0.05). Corn starch has a much lower (p < 0.05) amylose content than navy bean starch. There was a significant difference (p < 0.05) in the swelling power between microwave and conventionally heated corn and bean starches. Both corn and bean starches microwave heated at 70°C exhibited a higher swelling power compared to those conventionally heated (Figures 65 and 66). With microwave heating, the characteristic 2- stage pattern of swelling of corn starch was not observed. For both methods heat treatments, corn starch granules exhibited a much higher degree of swelling compared to bean starch. Bean starch demonstrated the characteristic restricted swelling pattern under microwave heating. Swelling power of conventionally heated bean starch more than doubled when heated within the range of 70-80°C. Microwave heating did not have a significant effect (p < 0.05) on swelling power at the same temperatme range. Microwave heating at 70°C had a significant effect (p < 0.05) on swelling potential of bean starch which was observed to be more than double that of starch heated using the conventional heating method 201 Goodvs 3283.. 5.585%? ca 328. .555. 3 332—8 5:28 « cm 232 .mnf .59: H wwém «86 H 3.23 «cad H 85 :35 H Env— 303.35 «and H mvdm 985 H and nmcd H mod «Ed H $6 :50 3; 3e .«3 3e .«3 38 8:5m 53% E 081:3 £29m amt. 2:332 535 12335 :«om .0228— o:« :80 be 85.9.2835 33525 ..N 3%... n.» nd m m m c2. n.~_ n6 .0. m n can me. nd 5 m A. 9:. 3.5 2.5 3.5 3.5 cote.— naéEeU e23.— ...—.255 veto.— _a.e.—. 9.23:3. "ESE—ego»...— oua..«>> cote.— .oxcoo 2:32.. 03322:. 23.6682 « «Em: Ada—c «2:: 9:522 93 «5.55388; o>«>68_2 .om oE«.—. SBA warn: mecca 2: Co 5.5%. -205 E0: :93 22: 855E .339 >>«: 3:5; as: 00mm X8 nee—«om o:« C: be do 3:259:00 233835 .2 SEA 203 $54 was: .2000 20:3 2: m0 5:08-308 3 80¢ :38 20? 853$ .8“; 58¢ 80¢ .EE Wm 08 883 o: a By 083:2 30550083 0:0 .58 m 08 283 com. 5 3 025295020 £500 xi“: .«0 220:3 33:00 .2 93¢ Swelling Power Swelling Power 204 I Ban Convcn. I Bean/Microwv. 70 90 00 Temperature (degree C) Figure 65. Swelling power pattern of bean starch with conventional and microwave heating 7 0 80 Temperature (degree C) Figure 66. Swelling power pattern of corn starch with conventional and microwave heating 205 ///////////// . //////// %// beans“; .0 C) “We Figure67.so|ubi “218M!“(noncomm .......... b //////////////////.w «m b '///////, 70 TW Figure 68. Solubility Index (81) corn and bean starches during conventional hen g 206 Solubility of both starches was low with microwave treatment, indicating some leaching of amylose molecules out of the starch granules (Figures 67 and 68). Corn starch solubility was higher than bean starches throughout the temperature range 70—90°C for microwave heating. Increased solubility of starches with increased temperature was observed for conventional heating. The restricted swelling power and solubility patterns of the bean starch indicates the existence of strong bonding forces within the granules, allowing the starch to gradually relax when heated ova the temperature range 70-900C. Conventional heating resulted in a significantly higher degree of syneresis for both corn and bean starches (p < 0.05) than observed for microwave heating, as demonstrated by a greater amount of exudate. Corn starch gels have a well recognized ability to hold liquid, and are expected to have only slight exudate, as illustrated by the microwave heated sample (Figure 69). However, the conventionally heated corn starch sample exhibited a very low liquid holding capacity, as demonstrated by the greater gel shrinkage and higher percentage of exudate. The conventionally heated bean starch sample exhibited a significantly higher (p < 0.05) degree of syneresis and percentage of exudate compared to microwave-heated bean starch, as shown in Plate 14 This observation was consistent with results which demonstrated relatively low swelling power at 70°C (Figure 65). According to Ring (1985), starch gel rigidity is affected by granule deformability and the strength and stability of matrix amylose gel. Results demonstrated conventional heating had a significant increase (p < 0.05) on the rigidity of heated corn starch gels compared to microwave heating, while bean starch gels exhibited a slightly softer gel when microwaved (Figures “IO-71). Corn starch has been previously reported to have a low amylose content and weak bonding strength within its starch granules, which could partly account for its ease of deformation. Bean starch possesses a higher amylose content (p < 0.05) and a higher tendency for retrogradation than corn starch. 207 Degree of Syneresls (%) ShrehMeat Treatment Figure 69. Degree of syneresis(%) of 8% (w/w) starch gels stored at room temperature for 1 week x!“ mm \\ l~ lll‘..\'l'|.\(;. 700C Plate 14. 8% starch gels stored at room temperature for 7 days Apparent Vlacoalty (polaa) Apparent Eaatlelty (NlernZ) 208 Starch/Heat Treat-eat Figure 70. Apparent viscosity (poise) of 8%(w/w) starch gels atoredatroomtemperaturefor‘ldays 1.0 4 "f: 55] // o.o ' Strch [Red Meat Figure‘ll. ApparentElasticityof 8% (wlw)starchgelsstoredatroorn tem‘ldaperaturefor 209 The Scanning Electron Micrographs (SEM) of corn and bean starches microwave and conventionally heated at 70°C for 2 minutes are shown in Plates 15 and 16, respectively. Corn starch granules appeared to have collapsed and melted under both methods of heat treatment, possibly as a result of solubilization of the amylose. However, for the microwave heated corn starch, disintegration of the starch granule was more pronounced with matrix formation of the leached materials. These data for corn starch coincide with the very high swelling power, without the characteristic 2-stage pattern, observed at 70°C . The more resistant bean starch granules still appeared swollen under both methods of heating. Fibrous-like exudates, generally recognized to be amylose, leached out of the granules. However, the microwave-heated starch appeared to have a greater quantity of fibrous-like exudate leaching , with some evidence of matrix formation. The bean starch granules also exhibited shrinkage and deformation within the central region, indicating a weak bonding region. Conclusion Microwave preconditioning of dry beans demonstrated the potential of microwave energy to improve whole bean seed cooking, ensure rapid processing of beans by disrupting starch granules and facilitating gelatinization. A number of factors must be controlled in microwave processing of beans to assure appropriate quality. These factors include: a) bean initial moisture, b) the water to bean (liquid/solids) ratio, c) microwave power level (wattage) and d) heating period. Palatable products may be obtained upon application of a suitable combination of these factors. The physical and functional properties of pure bean starch were significantly affected by microwave heating. Microwave heated starch gels exhibited a significantly lower degree of syneresis and a slightly softer texture than did conventional heated gels. Amylose molecules leached out from the bean starch granules when microwave heated at 210 Plate 15. Scanning Electron Micrographs of (a) Bean and (b) Corn starch granules microwave—heated at 700C for 2 minutes 211 a ISKU X466 6683 19.6U eaten SKU H488 8886 19.5D £5099 Plate 16. Scanning Electron Micrographs of (a) Bean and (b) Corn starch granules with conventional heating at 700C for 2 minutes 212 70°C for 2 minutes, compared to conventionally heated bean starch. Microwave heating of isolated bean starch slurries confirmed the potential for the use of microwave preconditioning of dry beans in rim to facilitate subsequent cooking. Further work to provide continuous in-line process treatments which could facilitate improved ease of cookability in bean is warranted Ho: Microwave energy will not adequately disrupt starch granules and facilitate gelatinization in rim to improve whole seed cooking and functional properties. Reject the Ho as stated and conclude that microwave energy preueatments dramatically influence cooking properties of dry beans. SUMMARY and RECOMMENDATIONS The research conducted in the course of this dissertation has been directed towards the improved utilization of dry edible beans. The hypothesis and objectives have been focused on the development of processing methodologies which may be adaptable to centralized small and intermediate-scale processing operations and provide products of utility for feeding of young children. All of the studies incorporated practical applications of fundamental technologies and have provided results which indicate that improved functional and nutritional properties may be obtained through process manipulation. The process pretreatments employed in this research influenced the composition of the drum-dried bean meals. CONTROL and EXTRACT DDBMs significantly differed in their in-vitro starch digestibilities. Oligosaccharide content was reduced by the aqueous and enzymatic pretreatments. The use of enzymatic predigestions was conducted with commercially available enzyme preparations to provide fundamental information regarding the changes in intrinsic properties of bean meals. The use of germinated seed as a resource for development of indigenous enzymes was provided to assure linkage to appropriate village-based technology . The enzymatic pretreatments of DDBMs significantly increased starch digestibility by disruption of intact cellular structures and denaturation of protein matrix, thereby increasing accessibility of the amylases to starch. The results reported indicated that the use of enzymatic digests derived from indigenous enzyme sources has potential for immediate adoption. Further research is warranted in the development of selected enzymes from native plant materials. The dmmdrying technology utilized in this research has direct application for village-level and cooperative centralized processing. Such a facility would enable the Pmduction of nutritious food ingredients derived from dry edible beans for use in a variety 0f products. Protein digestibility of DDBMs was significantly improved by the drum- drying process. Trypsin activiity was significantly reduced, and phytohemagglutinin was inaCtivated by the high heat treatment utilized during the drum-drying process. 213 2 l 4 The feasibility of incorporating DDBMs in pumpkin quick breads and weaning food/beverages was demonstrated. Acceptable breads were produced at the 20% and 40% levels of substitution. Enzyme pre-digested DDBMs possess great potential in weaning food formulations, particularly at the 8% concentration level. The research conducted on the functional properties of prepared bean meals has demonstrated that these products are functionally suitable for use in standardized foods. Further research is warranted to develop specific recipes for use in regionalized traditional foods. The potential for development of weaning beverages with reduced viscosity and improved nutritional value has a significant potential for improving the nutritional status of young children. Ingredients for these foods have been prepared and provide a readily accessible option. The bean ingredient could be blended with other appropriate ingredients mixed with water and available without additional cooking. Work is warranted to develop additional native products suitable for blending with the DDBM to enhance and optimize the formulation. The use of microwave energy although appearing as an advanced technology, was demonstrated to have potential as a pretreatment for enhancing the cookability of dry beans, and for modifiying physical and functional propterties of bean starch for applications in food systems. Such a protocol could be established in a centralized and public sector framework to facilitate pre-processing of dry beans. Whole dry beans could be prepared and pretreated with microwave energy to enable enhanced cookability and storage of dry, shelf-stable bean products with improved cooking potential. This methodology could be established as a continuous operation and provide sound whole seed for consumer use. Such atechnology wouldreducetherequirements forlongtermcookingandthe associated requirements for fuel gathering and use. The development and use of technologies to enhance the use of dry beans must be Pursued within the context which is sensitive to the endproduct outcome. The products derived under a village-level organizational scheme could benefit families, especially those 21 5 with young children, and the overall economic development within the region through the utilizationn of women in the development and processing of value-added nutritious food products. Additional processing methodologies could be incorporated into this central pre- processing regime. These enterprises would enable women to serve in managerial, supervisory and labor roles. 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