.23. i t : l. 3;... v . i. 1'? 3.2.1.! 2.7. 1...... If: a. ) .. r r. ~4 A z I .gayfi. Tia; &, .. p... 32.3.... .3 .. 4.0 ‘n .u 4 2:5; «3.. ‘ 3v. ‘1. . 5.3 .43?! I a!!! . ‘5... .14. ....:.t¢pa 0‘ .. I . .. . .‘Jfix i... h .. h x.‘53: I‘;g a“:‘ ,‘v’ ‘5 I , fr; 9. ,i .-.‘- P 555%? I l. .3 3-; .4... . 2.3%? . a.“ a. S n ‘ .- > nr:t|.yfi§a . .v .71... 1.12. . EILf;\~.9.. hill-III 1. ..L..u... IL. n11 D r‘nun.» l‘tc~ HIGV i‘ . .‘N. u . . ‘i..31 leh. v... t.‘ )I... . luv . IVESR SITY LI IBRARIES IIIIIIIIIIIIIII I IIIIIIIIIIIIIIIIIIIIIIIIIIIII III THESIS This is to certify that the thesis entitled An Investigation Of The Fundamental Chemical, Physical and Thermodynamic Properties of Polymer Modified Asphalt Cement presented by Jeffrey C. Shull has been accepted towards fulfillment of the requirements for M. S . degree in Chemical Engineering MKM Major professor Dr. Martin C. Hawley Date 6/30/95 0-7639 MS U is an Affirmative Action/Equal Opportunity Institution —.—_._ _____.—_ A ____ -4 LIBRARY Mlchlgan $tate I University I PLACE N RETURN BOX to remove We checked from your record. TO AVOID FINES return on or before dete due. DATE DUE DATE DUE DATE DUE MSU IeAnNflnnetive ActiorVEquel Opportmlty mutation Wm: ——..___.—_.. An Investigation Of The Fundamental Chemical, Physical and Thermodynamic Properties Of Polymer Modified Asphalt Cement by Jefl‘rey C. Shull A THESIS Submitted to Michigan State University in partial fulfillment of the requirements for the degree of MASTER OF SCIENCE Department of Chemical Engineering 1995 smoke” “PM: binds daem’lining Women}, r “SOCiazionSE method for d the expefime pIOCeSS that 0 ABSTRACT An Investigation Of - The Fundamental Chemical, Physical and Thermodynamic Properties Of Polymer Modified Asphalt Cement by Jeffrey C. Shull The chemical compositions and physical properties of straight and polymer modified asphalts were studied using gel permeation chromatography, infrared spectroscopy, dynamic mechanical analysis, thermal mechanical analysis, bending beam rheometry, rotational viscometry, and differential scanning calorimetry. It was concluded that the combination of chromatography and infrared spectroscopy is an excellent tool for fingerprinting and quality control of polymers and asphalt binders. The rheological properties of an asphalt binder were good indices for determining the optimum polymer concentrations for efl‘ective modifications. The calorimetry results indicated that different asphalt grades have different leveIs of polar associations as detected from changes in enthalpy. Thermal mechanical analysis was a fast method for determining the highest possible service temperature of the pavement. All of the experimental work, also suggested that polymer modification reduces the aging process that occurs during the processing and service-life of an asphalt pavement. To my parents, Jim and Pat and My wife, Renee Thank-you for your support, patience, and understanding. Pmiecx I Smflures telTIM-Lie Import; ECI‘ll-“Tm: Th SIWon. Patience‘ 1 Th ACKNOWLEDGMENTS The author wishes to thank Dr. Martin C. Hawley for his encouragement and guidance during the course of this investigation. Thanks are also extended to Dr. Lawrence T. Drzal and Dr. Gilbert Baladi who served as co-principle investigators on this project. Thank-you to the staff at Michigan State University's Composite Materials and Structures Center; especially Mike Rich for his guidance with respect to experimental technique. Thank-you also to John Barak and the staff at the Michigan Department of Transportation, Bituminous Lab for their experimental support concerning the new SHRP equipment. The author wishes to express his gratitude to his family for their emotional support. Finally, the author wishes to thank his wife, Renee, for her understanding, patience, and encouragement throughout the duration of this work. This research was supported by the Michigan Department of Transportation. TABLE OF CONTENTS List of Tables ................................................................................................................ ix List of Figures ............................................................................................................... xi Chapter One: Scope ...................................................................................................... 1 Chapter Two: Introduction ............................................................................................ 5 2.1 Reasons for the modification of asphalt binders ................................................... 5 2.2 A systematic study of polymer-fiber-rubber modified asphalt pavement ............................................................................................................ 7 Chapter Three: Background ........................................................................................ 14 3.1 Asphalt characterization .................................................................................... 14 3.2 The basic characteristics of potential polymer modifiers .................................... 21 3.3 Characteristics of polymer modified asphalt binders .......................................... 32 Chapter Four: Problem Definition And Research Goals ............................................... 35 4.1 ‘ Research goals .................................................................................................. 35 4.2 Materials .......................................................................................................... 36 4.3 Experimental Protocol ...................................................................................... 37 4.3.1 Preparation of aged asphalts .................................................................. 37 4.3.2 Thermal transitions and temperature dependent structure ...................... 37 4.3.3 Molecular weight distribution ................................ . ................................ 38 4 Chapter I 5.1 R; 52 Mi. 5.3 E— f Chemica} 4.3.4 Determination of useful chemical firnctional groups ............................... 38 4.3.5 Bending beam analysis ........................................................................... 39 4.3.6 Viscosity measurement .......................................................................... 39 Chapter Five: Experimental Details .............................................................................. 41 5. 1 Raw material preparation .................................................................................. 41 5.2 Mixing procedure for asphalt and SB S/SEBS .................................................... 42 5 . 3 Experimental methods ...................................................................................... 43 5.3.1 Aging .................................................................................................... 45 5.3.1.1 Thin Film Oven Test (AASHTO T179 or ASTM D 1754-87) ................................................................................ 46 5.3.1.2 Pressure Aging Vessel Test (AASHTO PPl) ............................. 48 5.3.2 Chemical properties ............................................................................... 50 5.3.2.1 High performance gel permeation chromatography system ...................................................................................... 50 5.3.2.2 Liquid chromatography transform unit ....................................... 53 5.3.2.3 Fourier transform infrared spectrometer ..................................... 53 5.3.3 Physical properties ..................................................................... ‘ ........... 54 5.3.3.1 Dynamic mechanical analysis ..................................................... 54 5.3.3.2 Thermal mechanical analysis ...................................................... 59 5.3.3.3 Differential scanning calorimetry ................................................ 61 5.3.3.4 Bending beam rheometer ............................................. . .............. 62 5.3.3.5 Rotational viscometry ................................................................ 65 Chapter Six: Experimental Results and Discussion ....................................................... 68 6' 1 Chemical properties .......................................................................................... 68 vi 7.2 7.3 6.1.1 High performance gel permeation chromatography ................................ 68 6.1.2 Fourier transform infrared spectroscopy ................................................ 79 6.1.3 Liquid chromatography transform unit ................................................... 90 6.2 Physical properties ............................................................................................ 90 6.2.1 Dynamic mechanical analysis ................................................................. 93 6.2.2 Thermal mechanical analysis ................................................................ 114 6.2.3 Differential scanning calorimetry ......................................................... 124 6.2.4 Bending beam rheometer ..................................................................... 125 6.2.5 Rotational viscometry .......................................................................... 134 Chapter Seven: Conclusions and Theories ................................................................. 137 7. 1 Theoretical models .......................................................................................... 137 7.1.1 Asphalt ............................................................................................... 137 7.1.2 Network thennoplastics (SBS and SEBS) ........................................... 140 7.1.3 Dispersed Therrnoplastics (PE) 148 7.1.4 Reactive polymers (Elvaloy®AM) ....................................................... 148 7.1.5 Crumb rubber particles ........................................................................ 148 7-2 Mixing procedure theory ................................................................................. 152 7- 3 Aging phenomena ........................................................................................... 154 7.3.1 Effect of polymer modification ............................................................ 154 7.3.2 Effect of elevated temperatures during processing ............................... 157 7'4 Optimum and critical polymer contents ........................................................... 158 7: 5 Fingerprinting protocol ................................................................................... 164 vii 76 SF‘ 7.6 Chapter Eié 8.1 Ma: 8.2 MO’I 7.5.1 Asphalt grades .................................................................................... 164 7.5.2 Polymer modifiers ............................................................................... 164 7.5.3 Polymer modified asphalt .................................................................... 165 7.5.4 Methodology ................................................................. 165 7.6 Specifications ................................................................................................. 167 7.6.1 SHRP binder specification ................................................................... 167 7.6.2 MDOT binder specification ................................................................. 172 Chapter Eight: Suggested Future Work ..................................................................... 176 8.1 Materials ........................................................................................................ 176 8.2 Modeling ........................................................................................................ 176 8.2.1 Level one modeling ............................................................................. 178 8.2.2 Level two modeling ............................................................................. 178 8.2.3 Level three modeling ........................................................................... 180 8-3 Topics and experiments .................................................................................. 181 List of References .................................................................. ‘ .................................... 1 83 General References .......... 187 viii Table 3.1 J. Table 3.2 . Table 3.3 Table 3.4 lele 4.1 Table 5.1 Table 6.2 Table 6.3 Table 6. .1 Table 6.5 Table 6.6 LIST OF TABLES Chapter Three Table 3.1 - Elemental analysis ...................................................................................... 15 Table 3.2 - Asphaltene/resin/oil ratios .......................................................................... 18 Table 3.3 - Potential reacting functional groups in asphalt ............................................ 22 Table 3.4- Studied polymers ...................................................................... 24 Chapter Four Table 4.1 - Materials used in the study ......................................................................... 37 Chapter Six Table 6.1 - Percentages of constituents in an unaged, unmodified AC-S grade asphalt ............................................................................................. 70 Table 6.2 - Percentages of constituents in an unaged, unmodified AC-lO grade asphalt .................................................................................. 71 TIlble 6.3 - Molecular weight averages for unmodified, unaged AC-S grade and AC—lO grade asphalts ................................................................. 72 Table 6.4 - Molecular weight averages for unmodified, aged and unaged AC-S grade asphalt .................................................................................... 73 Til ble 6.5 - Molecular weight averages for pure SBS and SEBS polymer modifiers ................................................................................................... 74 Table 6.6 - Percentage of SEBS polymer in unaged, polymer modified AC-S grade asphalt .................................................................................... 76 Table 6. Table 6.. Table 6.9 Table 7.1 Table 7.2 . Table 7.3 . Table 8.] . Table 8.2 . _ Table 6.7 - Molecular weight averages for unaged, normally aged, and severely aged unmodified AC-S grade asphalt ............................................ 78 Table 6.8 - Molecular weight averages for normally aged and severely aged AC-S grade asphalt modified with three weight percent SBS polymer ................................................................................. 80 Table 6.9 - Optimum and critical polymer contents of studied asphalt/polymer blends based on rheological properties .............................. 94 Chapter Seven Table 7.1 - Optimum and critical polymer contents of studied asphalt/polymer blends based on rheological properties ............................ 163 Table 7.2 - SHRP performance graded asphalt binder specification ............................ 168 Table 7.3 - MDOT polymer modified asphalt specification ......................................... 175 Chapter Eight Table 8.1 - Suggested materials for future research .................................................... 177 Table 8.2 - Suggested topics and experiments for fiature research ............................... 182 rIgure 2.1 “but: “anzs “flnz4 finals “unlL FlZure 3.2 . Ennis. Figure 34 . Ennis. “SUI-g 5.1 . . “80115.2 ‘ _ rims“ figure 54 ‘ R LIST OF FIGURES Chapter Two Figure 2.1 - Modifier effect on rutting ........................................................................... 8 Figure 2.2 - Modifier effect on fatigue cracking ............................................................. 9 Figure 2.3 - Modifier effect on low temperature cracking ............................................ 10 Figure 2.4 - Modifier effect on ravelling/stripping ........................................................ 11 Figure 2.5 - Material and property hierarchy for modified asphalt pavement ................................................................................................. 13 Chapter Three Figure 3.1 - A typical organic structure of an asphalt molecule .................................... 16 Figure 3.2 - Two phase asphalt model ......................................... I ................................ 19 I“igure 3.3 - Three types of polymer modified binders .................................................. 23 Figure 3.4 - Chemical structure of Elvaloy®AM .......................................................... 30 Figure 3.5 - Viscoelastic asphalt model ........................................................................ 34 Chapter Five Figure 5.1 - Schematic of mixing apparatus ................................................................. 44 Figure 5.2 - Thin Film Oven ........................................................................................ 47 Figlare 5.3 - Pressure aging vessel and components ....................................................... 49 Figure 5.4 - Reproducibility of refi'active index detector (AC-10) ................................ 52 xi Figure . Figure 5 fiflni Figure 5. Figure 5. “nail “unit FIgure 6.1 . Fl{lure 6.2 . figure 6.3 . Fig"?! 6.4 . “fl"ees. Hungfi. nunfl7. figure 6-8 ‘ Figure 5.5 - Stress-strain output for a constant strain rheometer .................................. 56 Figure 5.6 - Stress-strain response of a Viscoelastic material ........................................ 57 Figure 5.7 - Dynamic mechanical analysis asphalt specimen calculations .............................................................................................. 58 Figure 5.8 - Storage modulus as a function of temperature for a triplicate .................................................................................................. 60 Figure 5.9 - Schematic of the bending beam rheometer ................................................ 63 Figure 5.10 - Bending beam rheometer sample mold .................................................... 64 Figure 5.11 - Schematic of a rotational viscometer ...................................................... 67 Chapter Six Figure 6.1 - Gel permeation chromatography raw data for unaged, unmodified AC-S grade asphalt ................................................................ 70 Figure 6.2 - Gel permeation chromatography raw data for unaged, unmodified AC-lO grade asphalt .............................................................. 71 Figure 6.3 - Comparison of molecular weight distributions between unmodified, unaged AC-S grade and AC-lO grade asphalts ...................... 72 Figure 6.4 - Comparison of molecular weight distributions between unmodified, aged and unaged AC-S grade asphalt .................................... 73 Figure 6.5 - Comparison of molecular weight distributions between pure SBS and SBBS polymer modifiers ........................................................... 74 Figure 6.6 - HP-GPC raw data for unaged AC-S grade asphalt modified with four weight percent SEBS polymer .................................................. 76 Figure 6.7 - HP-GPC raw data comparing aged, four percent SBS polymer modified and unmodified AC-S grade asphalt ............................. 77 Figure 6.8 - Comparison of molecular weight distributions between unaged, normally aged, and severely aged unmodified AC-5 grade asphalt .................................................................................. 78 xii Figure 6.1 “anal finn6u “finam Flgure 6.17 Figure 6.13 “3“" 6.19 fig"! 6.20 figure 6_21 “80116.22 . Figure 6.9 - Comparison of molecular weight distributions between normally aged and severely aged AC-S grade asphalt modified with three weight percent SBS polymer ..................................... 80 Figure 6.10 - Fourier transform infrared spectrum of an aged, unmodified, AC-S grade asphalt sample ................................................. 81 Figure 6.11 - FTIR wavelength absorbance intensity ratios analysis ............................. 82 Figure 6.12 - FTIR spectrum of SBS polymer modifier ................................................ 83 Figure 6.13 - FTIR spectrum of SEBS polymer modifier ............... g .............................. 84 Figure 6.14 - Determination of absorbance band ratio for asphalt/SBS polymer finger printing calibration curve ................................................ 86 Figure 6.15 - FTIR absorbance band ratio calibration curve for unaged AC-S grade asphalt/SBS polymer blends ................................................. 87 Figure 6.16 - FTIR absorbance band ratio calibration curve for aged AC-S grade asphalt/SBS polymer blends ................................................. 88 Figure 6.17 - FTIR wavelength absorbance intensity ratios analysis for unmodified AC-S grade asphalt .............................................................. 89 Figure 6.18 - FTIR spectrum of SBS afier separation from an AC-5/SBS blend using an LC-transform unit ........................................................... 91 Figure 6.19 - FTIR spectrum of A05 afier separation from an AC-S/SBS blend using an LC-transfonn unit ........... 92 Figure 6.20 - Storage and loss moduli as a fianction of temperature for AC-S grade asphalt modified with one weight percent SBS polymer .................................................................................................. 95 Figure 6.21 - Storage and loss moduli as a function of temperature for AC-5 grade asphalt modified with seven weight percent SBS polymer .................................................................................................. 96 Figure 6.22 - Storage and loss moduli as a firnction of temperature for AC-S grade asphalt modified with ten weight percent SBS polymer .................................................................................................. 97 xiii ‘1 l Figure 6‘ fifln6 bani. Figure 6.2 rIgure 6.2 Figure 6.2. figure 6.25 FlEure 6.30 Flglll't 63] Flgure 532 Hill" 6.33 . Figure 6.34 - l‘. 3‘" 5.35. (1 m In Figure 6.23 - Storage and loss moduli as a fianction of temperature for 125/ 150 penetration grade asphalt modified with five weight percent SBS polymer ................................................................... 98 Figure 6.24 - "Log" slope of storage and complex moduli as a function of increasing SBS polymer content in AC-S from 25 to 60°C .............. 100 Figure 6.25 - Loss and storage moduli as a function of percent SBS polymer content in AC-S at 60°C ...................................................................... 101 Figure 6.26 - Tan delta as a function of SBS polymer content in AC-S at 60°C ............................................................................................... 102 Figure 6.27 - Inverse loss compliance as a function of SBS polymer content in AC-5 at 60°C ...................................................................... 103 Figure 6.28 - Storage modulus ratio of SBS polymer modified AC-S to unmodified AC-S grade asphalt binder at 60°C as a firnction of polymer content ................................................................ 105 Figure 6.29 - Storage modulus ratio of SBS polymer modified AC-S grade asphalt at 25°C to 60°C as a fimction of polymer content ............. 106 Figure 6.30 - Sensitivity of tan delta with respect to SBS polymer content and temperature for modified AC-S grade asphalt ............... , ................. 108 Figure 6.31 - Sensitivity criteria of tan delta as a function of SBS polymer content for modified AC-5 grade asphalt ................................ 109 Figure 6.32 - Storage modulus as a function of temperature for unmodified AC-S grade asphalt ............................................................ 110 Figure 6.33 - Loss modulus as a fianction of temperature for unmodified AC-5 grade asphalt ............................................................................... 111 Figure 6.34 - Tan delta as a function of temperature for unmodified AC-S grade asphalt ............................................................................... 112 Figure 6.35 - Percent increase in the storage modulus at 60°C as a firnction of aging for unmodified AC-S grade asphalt ........................... 113 Figure 6.36 - Storage modulus as a fianction of temperature for AC-S grade asphalt modified with three weight percent SBS polymer ............................................................................................... 1 15 xiv Figure Figure Figured Figure 6 Figurg 6 rIgure 6. fifln6. “3"“ 6‘4 “8111164I figure 6.48 Figure 6.37 - Loss modulus as a function of temperature for AC-S grade asphalt modified with three weight percent SBS polymer ..................... 116 Figure 6.38 - Tan delta as a fimction of temperature for AC-S grade asphalt modified with three weight percent SBS polymer ..................... 117 Figure 6.39 - Percent increase in the storage modulus at 60°C as a fimction of aging for AC-S grade asphalt modified with three weight percent SBS polymer ...................................................... 118 Figure 6.40 - TMA data for the determination of the glass transition temperature of SBS polymer ................................................................ 119 Figure 6.41 - Final softening temperatures of asphalt grade/polymer blends as a function of polymer content determined by TMA ................................................................................................... 121 Figure 6.42 - Final softening temperatures of aged and unaged AC-5 grade asphalt/ SBS polymer blends as a fianction of polymer content determined by TMA ................................................... 122 Figure 6.43 - Differences in the final softening temperatures of aged versus unaged AC-S grade asphalt/SBS polymer blends as a function of polymer content determined by TMA .............................. 123 Figure 6.44 - DSC data for the determination of the glass transition temperature of AC-S grade asphalt ...................................................... 126 Figure 6.45 - DSC data depicting the intensity of transitions as a . function of asphalt grade ...................................................................... 127 Figure 6.46 - DSC data depicting transitions as a function of temperature history ................................................................................................. 128 Figure 6.47 - DSC data depicting transitions as a function of repetitive temperature cycling .............................................................................. 129 Figure 6.48 - Bending beam rheometer measured stiffness for SBS polymer modified AC-S grade asphalt at -24°C .................................... 130 Figure 6.49 - Bending beam rheometer measured stiffness for SBS polymer modified AC-lO grade asphalt at -24°C .................................. 132 Figure 6 fiflnfi. Figure 6.5“ Figure 7.1 Figure 7.2 Flgure 7.3 . Flgure 7.4 . Flgnre 7.5 . Figure 7.6 . . figure 7.7 'T (I “311nm. S ngure 7.9. s.' if “We 7.10. q I. niW‘UJL-rl All p. Figure 6.50 - Bending beam rheometer m-value data as a fianction of polymer content for SBS polymer modified AC-S grade asphalt at -24°C .................................................................................. 133 Figure 6.51 - Viscosity of SBS polymer modified AC-S grade asphalt as a function of temperature ........................................................................ 135 Figure 6.52 - Viscosity of SBS polymer modified AC-S grade asphalt at 270°F as a function of polymer content ................................................ 136 Chapter Seven Figure 7.1 - Two phase asphalt model ....................................................................... 139 Figure 7.2 - Schematic of SBS polymer ..................................................................... 141 Figure 7.3 - Storage and loss moduli at 60°C as a function of polymer content (AC-5/SBS) .............................................................................. 143 Figure 7.4 - Schematic of SBS modified asphalt at service temperatures .................... 144 Figure 7.5 - Depiction of SBS modified asphalt theory at service temperatures .......................................................................................... 145 Figure 7.6 - Schematic of SBS modified asphalt at high (processing) temperatures .......................................................................................... 146 Figure 7.7 - Depiction of SBS modified asphalt theory at high (processing) temperatures ...................................................................... 147 Figure 7.8 - Schematic of PE modified asphalt at service temperatures ....................... 149 Figure 7.9 - Schematic of Elvaloy®AM modified asphalt at service temperatures .......................................................................................... 150 Figure 7.10 - Schematic of crumb rubber modified asphalt at service temperatures ........................................................................................ 151 Figure 7.11 - Tan delta as a fimction of temperature and mixing time for AC-S grade asphalt modified with five weight percent SBS polymer ............................................................................................... 153 Figure figure Figure ’ final fiwnl Flgure .. Figure 7.1. Figure 7.1. FlKurt 8.1 . Figure 7.12 - Tan delta as a fimction of temperature and mixing time for AC-S grade asphalt modified with seven weight percent SBS polymer ........................................................................................ 155 Figure 7.13 - Comparison of mixing times for AC-20 grade asphalt modified with seven weight percent SBS polymer ................................ 156 Figure 7.14 - Elevated temperature aging data ........................................................... 159 Figure 7.15 - Schematic of unaged asphalt constituents .............................................. 160 Figure 7.16 - Schematic of asphalt constituents after aging at normal temperatures ........................................................................................ 161 Figure 7.17 - Schematic of asphalt constituents after aging at elevated temperatures ........................................................................................ 162 Figure 7.18 - SHRP performance grading of AC-S grade asphalt/SBS polymer blends .................................................................................... 173 Figure 7.19 - SHRP performance graded temperature range of A06 grade asphalt/SBS polymer blends ................................................................ 174 Chapter Eight Figure 8.1 - Schematic of proposed modeling hierarchy ............................................ 179 xvii TE funcuon c cmironmer timeaw llselfin tc”Warm COm‘entiona lzllgue and [I aSillTAlt binge: Hen“? mod: and Wider ”a Such modifica Chapter One Scope The long term pavement performance of asphalt concrete surfaced roads is a firnction of traffic load and volume, material properties, construction practices, and environmental factors. A typical asphalt concrete surfaced pavement deteriorates over time and with increasing number of load repetitions. Pavement deterioration manifests itself in several common types of distress including rutting, fatigue cracking, low temperature cracking, reflective cracking, aging, ravelling, and stripping”. The conventional materials used in an asphalt concrete mixture may perform satisfactorily relative to one distress type but fail prematurely relative to the others. For example, asphalt concrete mixtures made by using hard binders will have low rutting but, high fatigue and temperature cracking potentials. On the other hand, mixtures made with sofi asphalt binders will have low fatigue and temperature cracking but, high rutting potentials. Hence, modification of the asphalt to enhance its performance at extreme temperatures and under traffic loading is essential to the success of constructing superior pavements. Such modifications include the addition of polymers to enhance the binder properties at both low and high temperatures. And indeed, it has been shown that polymer modified asphalts can improve pavement performance“. However, most studies have been concentrated on specific materials and properties. The need for a systematic study of polymer-fiber-rubber modified asphalt pavement is required. asphalt-egg 5111: of Mail This r Mal. an: experimental i 2 Michigan State University is currently conducting a study of polymer modified asphalt pavements that will address the above considerations. The study is divided into three sections including: the fundamental physical, chemical, and thermodynamic properties of asphalt binders; the basic morphology and microstructure of polymer-fiber- asphalt-aggregate mixtures; and the structural and engineering properties of polymer-fiber- asphalt-aggregate mixtures under the extreme low and high temperatures found in the State of Michigan. This major objective of this study was to provide a wealth of fundamental physical, chemical, and thermodynamic data for the binder materials under study through both experimental and theoretical investigations. These studies led to the major deliverable of this research; initial, pictorial, physical and chemical models of polymer modified asphalt blends that account for difi‘erent asphalt grades, sources, and polymer types. Secondary deliverables of the study include: determination of the optimum polymer modification contents required for optimum physical properties; a fingerprinting protocol for determining the type and amount of polymer present in an unknown sample to be used by the Michigan Department of Transportation (MDOT); and a review of the SHRP and MDOT binder specifications with suggested revisions for use with polymer modified aspalt binders. Based on the suitability of materials for Michigan weather, the asphalt grades and polymer modifiers used in this study were AC-2.5, A05, A010, AC-20, styrene- butadiene-styrene, and styrene-ethylene-butylene-styrene. The asphalts were all supplied by Amoco and were graded from low viscosity, AC-2.5, to high viscosity, AC-ZO. Both i... poljmer: combine: butylenc- Tl" follouing 3 polymers are Shell Kraton polymers and were used in powder form. All possible combinations of AC-S and AC- 1 O with styrene-butadiene-styrene and styrene-ethylene- butylene-styrene were tested fi'om 1 through 10 weight percent polymer modification. The deliverables of the research were accomplished through the completion of the following set of experiments: 0 High Performance Gel Permeation Chromatography; o Fourier Transform Infrared Spectroscopy; 0 Dynamic Mechanical Analysis; 0 Thermal Mechanical Analysis; 0 Differential Scanning Calorimetry; - Bending Beam Rheometry; o and, Rotational Viscometry. Beyond the original deliverables, two additional findings concerning asphalt aging processes were discovered. First, polymer modification was found to decrease the amount of aging that occurs during the processing and service-life of an asphalt pavement. Second, a degradation aging process was identified for asphalt when it is heated to extremely high temperatures during processing. Chapters Two and Three of this thesis will introduce the reader to the problem at a more in depth level and provide any relevant background information found in recent literature. Chapter Four is an expansion of the study's objectives and materials. Chapter Five discusses the experimental procedures and theories used during this study and 3 Chapter Six presents the actual data collected for the studied materials. The thesis is .l conclude. future res 4 concluded in Chapters Seven and Eight which provide the final findings as well as possible future research. :‘u the Slate c 0f the 19;; l asPhalt pat lm'tSIlgate 8061 of this “Plan mod Pavements n understandin. might “phi 2‘1 R8050“) Chapter Two Introduction Asphalt concrete surfaced pavements are showing signs of premature distress in the State of Michigan. It has been suggested in recent studies that polymer modification of the asphalt binder will enhance the properties and thus the service life of the final asphalt pavement. Research is currently being conducted at Michigan State University to investigate the benefits of adding polymer modifiers to the asphalt mixture. The ultimate goal of this study is to provide a systematic and comprehensive protocol for selecting asphalt modifiers and for establishing asphalt mixture processing conditions to provide pavements with long service lives. The focus of the research in this thesis is a greater understanding of the firndamental physical, chemical, and thermodynamic properties of straight asphalt binders, polymer modifiers, and polymer modified asphalt binders. 2. 1 Reasons for the modification of asphalt binders The long term pavement performance of asphalt concrete surfaced roads is a firnction of traffic load and volume, material properties, construction practices, and environmental factors. A typical asphalt concrete surfaced pavement deteriorates over time and with increasing number of load repetitions. Pavement deterioration manifests itself in several common types of distress including: Ul'lS" Slrc: 6 0 Rutting, which is caused by consolidation or lateral movement under traffic in one or more of the underlying courses, or by displacement in the asphalt surface layer itself. The rutting resistance can be improved by increasing the elasticity of the asphalt binder at high temperatures. 0 Fatigue cracking, which is caused by excessive deflection of the surface over unstable subgrade or lower courses of the pavement. An increase in the tensile strength of the asphalt binder will reduce the fatigue cracking potential. 0 Low temperature cracking, which is caused by a volume change of aggregate and binder in the mixture, especially in pavements with a high content of low penetration asphalt. This distress can be reduced by increasing the tensile strength and flexibility of the asphalt binder at low temperatures. 0 Joint reflective cracking, which is caused by vertical or horizontal movements in the pavement beneath the overlay. This distress can be redUced by increasing the flexibility and tensile strength of the asphalt mixture. 0 Ravellinystripping, which is caused by a lack of compaction during construction, construction during wet or cold weather, dirty or disintegrating aggregate, too little asphalt binder in the mixture, or over heating of the asphalt mixture. Ravelling/stripping can be reduced if the adhesion between asphalt and aggregate can be improved"3 . In general. these distresses can be reduced by improving the temperature susceptibility, moisture resistance, and rheological properties of asphalt binders and the adhesion between binder and aggregate within the asphalt concrete mixture. - r A ‘ ”'5. 4" . ao- satisfac: 503 asp}. putentiais [Ellipcratu Pavements 7 The conventional materials used in an asphalt concrete mixture may perform satisfactorily relative to one distress type but fail prematurely relative to others. For example, asphalt concrete mixtures made by using hard binders will have low rutting but, high fatigue and temperature cracking potentials. On the other hand, mixtures made with soft asphalt binders will have low fatigue and temperature cracking but, high rutting potentials. Hence, modification of the asphalt to enhance its performance at extreme temperatures and under traffic loading is essential to the success of constnrcting superior pavements. Such modifications include the addition of polymers, fibers, and/or rubber particles to enhance the binder properties at both low and high temperatures. And indeed, it has been shown that polymer modified asphalts can improve pavement performance“. 2.2 A systematic study of polymer-flber-ru bber modified asphalt pavement Numerous studies have been conducted in the area of polymer modified asphalt binders. However, due to the large scope of the final question of enhanced pavement performance, most previous research has been limited in its objectives and has only covered a few aspects of the modification and a small number of materials. Figures 2.1- 2.4 summarize the change of performance properties due to polymer modifications. The inconclusiveness of the results suggest that a systematic study of polymer-fiber-rubber modified asphalt pavement is required. ‘1 YT‘TTV M353 =0 .3wa BEE: .. ~ .N {ENE o_o_t0n_ a o 25 mmefimmm YrTYY‘VTY'V ' T I'Y‘YjY'Y'l {0362 009390 :m 22... a .22 \\\\\\\\\n :25 U ALAILIAJ sasog) pog 5950:) p005) Viv} V T usesoaau Erwiwxze .3wa BS3»: . 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V .N 38%.; Bufom {0.362 ummemaflo o :mo 8828 mummmm on. we $6 fl eczeeem mmm m fl .r m . . an: I W a: g . eeeea .HU l ALAILJLJ AlLLAlALklA 1 L4 5950:) p08 sasog p009 Michigan aspialt pavements according to the it. ll production of a 25) These SCCllC Womamic pro Whoa-fiber-aspha whmer-fiberasph; found in Michigan [ht above dlxisions Ween final paw constituents. 11m“; WWI when sel 561131101 “PM! pa This thesis Properties of Slrai; binders" Chapter lamination presen' 12 Michigan State University is currently conducting a study of polymer modified asphalt pavements that will address the above considerations. The study was constructed according to the three parts of pavement processing including: 1) processing of the binder, 2) production of a binder/aggregate mixture, and 3) pavement construction (see Figure 2.5). These sections are in turn controlled by, the fundamental physical, chemical, and thermodynamic properties of asphalt binders, the basic morphology and microstructure of polymer-fiber-asphalt-aggregate mixtures, and the structural and engineering properties of polymer-fiber-asphalt-aggregate mixtures under the extreme low and high temperatures found in Michigan. When studied in conjunction with each other for a matrix of materials, the above divisions form a systematic study that will enable relationships to be formed between final pavement performance and the fundamental properties of the mixture constituents. It will also allow for the identification of any control parameters that may be ilnportant when selecting materials, specifications, and construction practices for designing superior asphalt pavements. This thesis will focus on the fundamental physical, chemical, and thermodynamic properties of straight asphalt binders, polymer modifiers, and polymer modified asphalt binders. -' Chapter three is a summary of the background information relevant to the information presented in this thesis. 13 28533 :3me .33th «QéoLEeE bummeihzo 3.2.83: 1 u. .N 95%: 35.5359... ace—:26.“ _ aceEcocgcmL — 83259;. . . A A 3.82.. casuazmcoo 33:5 ll .1. . l. lllllll'iilln 9:332“. 35002 In order t: i asphalt cement an: the properties of th the literature regar: poiyrner modifiers. 3.1 Asphalt Chara Asohalr is of molecules that r Inaiysis shows tr hydrogen 1 per; including nitrogen Emit asphalt r aningttrrient of th M the tom amc plex Organic ScWaxed into Two Chapter Three Background In order to better understand the effect of polymer modifiers on the properties of asphalt cement and the performance of asphalt concrete, it is necessary to first understand the properties of the raw materials. Chapter three will present recent information found in the literature regarding: 1) asphalt characterization, 2) the basic characteristics of potential polymer modifiers, and 3) characteristics of polymer modified asphalt binders. 3. I Asphalt characterization Asphalt is a complex mixture of many different hydrocarbons consisting primarily of molecules that contain mainly carbon and hydrogen atoms. A generic asphalt elemental analysis shows that approximately 84 percent of the sample is carbon, 10 percent hydrogen, 1 percent oxygen, and the remainder consists of several trace elements including nitrogen, sulfur, vanadium, nickel, and iron7. The average molecular weight of a generic asphalt molecule ranges from 500 to 5000 as shown in Table 3.17. The arrangement of the various elements in an asphalt binder is of much greater importance than the total amounts of the elements themselves. Asphalt consists mainly of linear and complex organic ring structures as shown in Figure 3.18. The ring structures can be separated into two groups: naphthenic and aromatic. Naphthenic compounds are simple 14 II-'||I' ." .--'-|"----‘-'--'|--|-'--'|-‘t'--'-'-'-'--'-::-II'-""". b.\.o..q.\~»=~h \~\\~\.15~0\. n\ t N .hi “\sth 15 82.8w 8.” 2m 2: an a an and 2 1: 2.» add 3ch SH Q: 2 on cam Ev vnd «.0 od— Qua ad cowéhm QNH n.~m on me— «6 «nd 0.2 5.3 Angus—ob 2303 3.30.02 * .5 03302 .x .U nausea can do: EGG Juxumz can .Eauacg a .323 R 60mg;— R .60»th * .cowE—i: R £35 “.3333 323:33 .. ~ .M ~2§ 2k 45 m»«nu n10 I o/fo nzofoufenufnvfnvfnuflrnvfof“ 16 32.3.3... 5:33 .5 \: 3:333. 2:943 39:3 V - TM 93%: fufexofofofofufogx 45 or complex saturat. trebarier moleco» For cont-er. ttsins and asphalte melanin weights Afitpted criteria for ‘53 than 0.6 and I ”Winds (800 . nitrogen Resins an in soluble in “El mallow earlier Carbonwmmonde ”WWW 23:: MOM“ gt! pe mm“ Weillhr d 1 7 or complex saturated rings that have a large number of side chains. Aromatic compounds are heavier molecules that consist of stable six atom rings with few side chains“. For convenience, asphalt constituents are classified into three categories: oils, resins, and asphaltenes. Oils are the light compounds in asphalt which have the lowest molecular weights (24 - 800) and have a large number of side chains and few rings. Accepted criteria for the oil classification are molecules with carbon/hydrogen atom ratios less than 0.6 and are soluble in hexane'. Resins are intermediate molecular weight compounds (800 - 2000). It is important to note that resins can contain sulfur and nitrogen. Resins are polar, have carbon to hydrogen atom ratios between 0.6 and 0.8 and are soluble in light petroleum naphtha'. Asphaltenes contain the trace elements mentioned earlier which may react with potential polymers and are soluble in carbont-errachloride. An average asphalt sample has an asphaltene/resin/oil ratio of approximately 23/27/509 and the asphaltene content is higher for harder asphalts. High performance gel permeation chromatography (HP-GPC) is usually used to determine the molecular weight distribution, molecular weight, and the fraction of each constituent in an asphalt sample. Table 3.2 shows the ratios for three different samples”. Note. that the asphaltene content is larger for the harder sample. Using the asphaltene/resin/oil classifications, a two phase asphalt model is c1¢=‘~’eloped'. Phase 1 is an assembly phase consisting of asphaltenes and resins that is dispersed in phase 2, the solvent phase consisting of the oily constituents. Figure 3.2 is a syntbolic depiction of this model. The resins behave as peptizingagents that stabilize the a$13 haltenes in the oily constituents. l\“ a I .o.«~\\~v.\ \ssx. ~\\.o..v.\\..0\\.d\\~vu\\\o4‘\ I N .h- ”\Qhfifi 18 3 mm. S» cm AX.“ m=0 hem mm Exam 9m— mm mm 333 8:5 ~.~e\=.~§.~\2§~u4%w .. m .~. wash 83¢. \ =2. ”3 zasam< 58922 8~-o< \ =2. 2: =2&< 53:22 0.95% omfio>< gamma 19 Phase 1 = Asphaltenes + Resins (Assemblies) Phase 2 = Oils (Solvent) Figure 3.2 - Two phase asphalt model The 35>?hé in diameter A51? also mum‘s" T propeflifi and rut defining faaor b compounds sub 51:: the rings than characteristics oft medium. Asphalt: phase. Colloidal) but can be stabiliz oriented particle ag groups (water, silic to form an oil-me micelle). The grow content, and the pi 20 The asphaltene core of the assembly phase can vary between 40 and 60 angstroms in diameter. As the asphaltene content of an asphalt sample increases, the assembly phase also increases. This adds structure to the asphalt and gives it better high temperature properties and rutting resistance. The percentage of the assembly phase present is the defining factor between different grades of asphalts. The resins contain aromatic compounds substituted with longer alkyls and a larger number of side chains attached to the rings than asphaltenes. The combination of the saturated and the aromatic characteristics of the resins stabilizes the colloidal nature of the asphaltenes in the oil medium. Asphaltenes are present as discrete or colloidally dispersed particles in the oily phase. Colloidally dispersed asphaltenes are not stable in the oil medium by themselves, but can be stabilized through polar resins. Asphaltenes can exist both in a randomly oriented particle aggregate form or in an ordered micelle form. In micelle form, the polar groups (water, silica, or metals such as V, Ni, an Fe) are either oriented toward the center to form an oil-external micelle or oriented outward to form an oil-internal micelle (Hartley trucelle). The growth and ultimate size of the micelles are dependent on temperature, resin content, and the presence of other chemicals such as polymer modifiers. The engineering PrOperties of asphalts are directly related to the quantity of asphaltenes, the size of the micelle structure, and the nature of the dispersion medium, oils and resins. Another important aspect of asphalts for polymer modification is that the fi-ll'lctional groups present in asphalts may react with polymers during processing. Table 3 - 3 lists the functional groups that have been identified in asphalts including: carboxylic acids, ketones, phenols, sulfoxides, acid anhydrides, pyrroles, and quincnes’. 12 The basic c'» The basic processing, and cc We, modifi Wplastics, re mOplastics be ”blue the the before fonmng a “in fOffn a new h Bphah (no Meier behav mplmics Ming Swim Fsure 3.3 is a 2 1 3, 2 The basic characteristics of potential polymer modifiers The basic criteria for selecting a polymer modifier are performance, ease of processing, and economics. According to the firnctions and behaviors of various modifiers in asphalts, modifiers can be categorized into five types: dispersed thennoplastics, network thennoplastics, reacting polymers, fibers, and crumb rubber (CRM) particles. Dispersed thennoplastics behave like asphaltenes and normally require peptizing agents like resins to stabilize the modified systems. Usually, it requires a considerable amount of material before forming a macrostructural network. Network thennoplastics behave like resins and will form a network of themselves inside asphalts. Reacting polymers bond chemically to the asphalt (normally to the asphaltenes) and form asphalt/polymer networks. CRM particles behave as aggregates if there sizes are large and behave as dispersed theflnOplastics if there sizes are small (below lOOum). Fibers increase the available wetting surface area and behave as binder thickeners which reduce asphali bleeding. Figure 3.3 is a pictorial representation of the polymer modified asphalt types". In all cases, the goal is to create more structure inside an asphalt without losing its low temperature properties. Table 3.4 lists polymers that have been studied as additives to asphalt and their resPfictive cost. Reactive polymers cost more than network polymers and dispersed Polymers are the least expensive. However, a larger amount of dispersed polymer is “med to create a network structure in an asphalt than that of a network polymer. Reactive polymers require the least amount of material among the three polymer groups. Func Cam Keto Pher gulf: Acid Pym Qulr 22 Table 3.3 - Potential reacting functional groups in asphalt Functional Group Structure 9. Carboxilic Acids R - COH Ketones R - ('3' - R Phenols - a CH . O Sulfoxides R - s' - 0 Acid Anhydrides R - 3' - O - g- R /\o o Pyrroles W ' R Quinones O :/\=/ ‘20 23 2%.: 33385 aufiécmxo numb uuai - Mfi 333% scia< 5.3 9830: Egon 5:531 :— eofloama =EEu< =agaa< 5 “.53qu Sci—on. - 1! =Sam< .5 392.2: .9529". ,_ I e‘. ‘I.I.ei‘ .A.l““..d~‘... .‘o‘-’.~‘.‘A‘.’.-~ Ililf infill til .I. w. d — .4an 2:... v .93...v35u.€ =€=l‘bhb.-é a .3-3- fist; .n.\~vs\\\«i\\5\\\u~v\\v§\.w. I \. .\r “\anh 24 0:... a... .a .3233... 2.2 . aha-«9.9.- 23- n. Ohauua-ucn —l9~3—0——8 .2...— c c i"-.n!| I II- - t i ...... . .wni—w 3.33... ._ or... 5.: 59:59.2... - Z<.h...a>.n.. 3.5.5.3..- 95.3.“.— m=m=>..c._ m>..-.< styrene-ethylene-butylene-styrene AC-20 4.3 Experimental Protocol 4. 3. 1 Preparation of aged asphalts To determine the effect on binder properties, straight and modified asphalt samples were aged and tested. Aging during processing was simulated by using the: 0 Thin Film Oven Test (AASFTO T 240; ASTM D 2872); o and, the Thin Film Oven Test (AASFTO T 240; ASTM D 2872) at a temperature 10 to 15°C higher than the suggested value, depending on the processing conditions required for the modification. Aging during the service life was simulated by using the: 0 Pressure Aging Vessel Test (SHRP B-005). 4. 3. 2 Thermal transitions and temperature dependent structure Asphalt is a very temperature dependent material. The ultimate goal of adding polymer to an asphalt mixture is to reduce the blends temperature dependency. Improved properties of ; decreases irt th analysis and di h transition tempe used to locate a B Wtil as any ( mmMatures are analysis was us: 03713336 mechar over a mld‘lempt 43-3 Molecula, High pe' determme the m‘ C(instituent in th “hipped With a 161ng w“ appli- afingerpfiming p 4.3.4 Dem—MIMI FoufieT it til . t”total {Unmon 38 properties of polymer modified asphalt binders at low temperatures are do partly to decreases in the materials’ effective glass transition temperatures. Thermal mechanical analysis and differential scanning calorimetry tests were used to measure the glass transition temperature of selected materials. Differential scanning calorimetry was also used to locate and examine any temperature dependent stnrcture in the studied materials as well as any other phase transitions. Improved properties of asphalt binders at high temperatures are due partly to an increase in a material’s viscosity. Thermal mechanical analysis was used to measure the final softening temperature of selected materials. Dynamic mechanical analysis was used to measure the Viscoelastic properties of binders over a mid-temperature regime. 4. 3.3 Molecular weight distribution High performance gel permeation chromatography (HP-GPC) was used to determine the molecular weight distribution, molecular weight, and thus, fi'action of each constituent in the studied binders. The study used a state of the art, Waters’ system equipped with a Millennium software package. The results obtained from the HP-GPC testing was applicable in every objective of the study with an emphasis placed on creating a fingerprinting protocol. 4. 3. 4 Determination of useful chemical functional groups Fourier transform infrared (FT IR) spectroscopy was used to determine usefiil chemical functional groups and their relative amounts in asphalt binders. A liquid droning-'43. ' rust‘orm Will it spec-ta of spec-ft tests were also a; creation of a huge. 4.3.5 Bending bed The SHRP properties of asp: determine any in Unified binders millimples a ‘5 in index for re ‘36 IlSCOSIlt' p 39 chromatography (LC)—transfonn unit was also used to accomplish this goal. The LC- transfonn unit was part of the HP-GPC system and allowed for the inspection of infrared spectra of specific molecular weight ranges of asphalt binders. The results from these tests were also applicable to every objective of the study with an emphasis placed on the creation of a fingerprinting protocol. 4. 3.5 Bending beam analysis The SHRP bending beam test was conducted to examine the low temperature properties of asphalt binders related to thermal cracking. The data was also used to determine any modifications needed for the SHRP specifications to handle polymer modified binders. In future studies, the change in fiexural properties between unaged asphalt samples and unaged asphalt in combination with aged asphalt samples may be used as an index for recyclability. O 4. 3. 6 Viscosity measurement Viscosities at various temperatures were measured using a Brookfield viscometer to examine. how polymer modification will affect processing temperatures and equipment. The data was also used to examine any high temperature structure present in polymer modified asphalt as well as any modifications needed for MDOT and/or SHRP binder specifications to handle polymer modified binders. Chapter smdy. 40 Chapter Five expands on the experimental details and procedures used in this study. such a all exr l‘ 5.1 R Ifans: Study comm" Place: PrCVel Salon Chapter Five Experimental Details Extreme care was taken to ensure that all of the tested materials were handled in such a way that the results could be trusted and compared. In order to accomplish this task, protocols were established for raw material preparation, asphalt/polymer mixing, and all experimental methods. Chapter Five will detail these procedures. 5. 1 Raw material preparation Five gallon containers of asphalt were obtained from the Michigan Department of Transportation at the initiation of the project in a large enough quantity to sustain the StUdy through its conclusion. The material was stored in its original, sealed five gallon containers. As the asphalt was needed for testing, it was handled using the following Procedure to insure a uniform sampling base from which all testing could begin. This Prevented non-uniform aging of samples due to a repetitive heating of the original five 8311011 container. ’ An oven was heated to an equilibrium temperature of 270 °F. A covered five gallon sample of the asphalt was placed in the oven and heated for 3.5 hours. 41 Chet: “761: 5.2 .l 42 o The five gallon sample of asphalt was removed from the oven and stirred by hand using a wood dowel for 1 minute to ensure a good melt and homogeneity. 0 While still hot, the asphalt was poured directly into 17.25 x 11.5 x 1 inch sampling trays lined with non-stick plastic. The trays were filled to a depth of approximately 0.5 inches. This required approximately 12 trays per five gallon container of asphalt. o The asphalt was then covered with an additional piece of non-stick plastic, cooled at room temperature for one hour, and stacked in a freezer at -10°C. This temperature is close to the glass transition temperature of the material and very little aging should occur. 0 For each test, the proper asphalt weight was determined and obtained by either cutting the appropriate amount of binder from the fi'ozen asphalt sheet using a hot wire or by cracking the frozen sheet using a hammer. Kraton rubbers Gl650 (SEBS) and D1101 (SBS) were obtained fi'om Shell Chemical Company. These materials were stored in their original containers, sealed mastic bags, at room temperature in a dry location. 5-2 Mixing procedure for asphalt and SBS/SEES In general, industry has recommended a mixing time that corresponds to a homogeneous asphalt/polymer blend based on visual inspection. This was found to be a poo: pnctzc based upon lining ten to ten per: properties aspialt all and aspha ”“237 m Should be “M 52 15 ll'lt m limbo 1 fillings Blend ' l"35 Chc 5.3 b 43 poor practice for laboratory procedures. A mixing procedure was therefore developed based upon the improvement of rheological properties of an asphalt/polymer blend for varying temperatures and mixing times. The polymer concentration was varied from zero to ten percent by the total weight of the asphalt/polymer blend. It was found that the properties of the blend were maximized for a procedure that included heating of the asphalt at 270°F for one hour (to obtain a good melt) followed by mixing of the polymer and asphalt at 350°F (industry standard for polymer modified asphalts) for two hours. Longer mixing periods caused more aging and slightly lower rheological properties. It should be noted that, to eliminate difi‘erences due to the effects of aging, the unmodified asphalt samples used in this study were stirred at the same temperature and mixing period as the polymer modified samples. The mixing was performed using a Fischer-Scientific Jumbo 115V low shear mixer equipped with a four blade, 5 cm diameter impeller. The stirring speed (~1600 rpm) varied as a function of the consistency and concentration of the blend. Figure 5.1 is a schematic of the mixing apparatus. The above mixing procedure was chosen based on a study detailed in Chapter Seven 5.3 Experimental methods The experiments performed in this study can be divided into three sections. The second and third groups of experiments examine the chemical and physical properties of asphalt binders, respectively. The first set of experiments are aging procedures that simulate the environments seen by an asphalt binder during its life span. 44 ”Suite 3.3.: \o £323ou. .. ~ .9. 95%.: 2195 Egon o... 0' ‘l o o. :0 939235 . = e U. h flfl . . LL - / 53 ._o c. o_aEmm\3 Exam: oEEmm o3m>oEmm VA EEG 5:05:00 tooum cl. w I i ll 3326 826d 0... .222 955 22223 of. Ina/:7. llithVl limit: can: PM Ql‘. 45 5. 3. 1 Aging According to the literature, asphalt binders age due to two individual mechanisms”. The first process is an oxidation process, and the second is a volatilization of the low molecular weight oils present in the material. The oxidation process occurs at moderate and high temperatures in the presence of oxygen. The volatilization process, however, occurs mostly only at very high temperatures. During processing, an asphalt binder will encounter both high temperatures and a steady air flow, creating optimum conditions for both aging mechanisms. After processing, during the service life of the pavement, the extreme conditions are relaxed and the rate of aging is decreased. It was therefore necessary to have two aging procedures, if the entire aging process was to be simulated. It was determined that aging during processing would be simulated by using the Thin Film Oven Test (TFOT) at normal (163°C) and elevated (177°C) temperatures. The higher temperatures were investigated to determine if any significant property changes occurred due to the increased temperatures required for processing of polymer modified a$Phalts. Aging during the service life of an asphalt binder was simulated by using SHRP's Pressure Aging Vessel Test (PAV). Only one set of temperature conditions was necessary fm’ this Experiment because the service life temperatures of polymer modified and “MOdified asphalts are the same. It is important to note that the PAV test was performed 0“ samples that had already been aged by the TFOT. be r cont 5m; lllllll Shel: mill m of n SliOl 46 5.3.1.1 Thin Film Oven Test (AASHTO T179 or ASTMD 1754-87) The Thin Film Oven Test requires an electrically-heated convection oven that can be maintained at a temperature of 163°C for a time period of five hours. The oven must contain a circular, horizontal, rotating shelf suspended from the center that can hold the sample containers. The shelf is required to rotate at a rate of 5.5 :t 1.0 revolutions per minute. A thermometer should be located in the center of the oven just above the rotating shelf. Figure 5.2 is a schematic of the Thin Film Oven Samples are prepared by heating the material until it becomes the consistency of motor oil. It is important to be careful of not over-heating the sample. A temperature of 150°C should not be exceeded during sample preparation. After heating, 50.0 t 0.5 grams of material are poured into two or more previously weighed cylindrical pans. Each pan should be 140 mm in diameter, 9.5 mm deep and have a flat bottom. The pans are allowed to cool to room temperature after which the samples are weighed to the nearest 0.001 grams. The pans are then quickly put into a preheated Thin Film Oven and allowed to heat for five hours after the system has regained the equilibrium temperature. The total heating time should be no longer than 5.25 hours. After heating, the pans are removed and again allowed to cool to room temperature. The pans are weighed to the nearest 0.001 grams. If the material is to be aged further using the Pressure Aging Vessel Test, the samples may be stored in the pans. If not, the pans should be heated until the sample flows and can be transferred into storage tins to be tested at a later date. Motor Thermometer Sample Tins 47 if; Controls Figure 5.2 - Thin Film Oven anc’canb l‘QSSel c Salim 48 A convenient and simple measure of aging during processing is percent mass loss and can be calculated using the following equation: Mass Loss, % = Original mass - Aged Mass x 100 Original mass 5.3.1.2 Pressure Aging Vessel Test (AASH T 0 PP!) The Pressure Aging Vessel Test requires a pressure vessel and a forced-draft oven. The vessel is connected to a regulated cylinder of clean, compressed air and a temperature probe. The vessel must be able to withstand a pressure of 2070 kPa and a temperature of 100°C for a time period of twenty hours. The oven should be able to control the temperature of the vessel to .4: 0.5°C during the twenty hours of heating. The pressure vessel contains a sample rack that will hold at least ten TFOT sample pans. Figure 5.3 is a schematic of the pressure aging vessel and its components. The pressure vessel is preheated to a temperature of 100 i 2°C while still unpressurized. When the equilibrium temperature is reached, the vessel is quickly opened, the sample rack is loaded, and quickly closed again to prevent heat loss. When the vessel has once again equilibrated at 100 :l: 2°C, the pressure is slowly increased to 2070 kPa. After twenty hours of heating, the pressure is slowly released over a time span of ten to twelve minutes. The samples can now be removed from the vessel. The samples are heated at 163°C for 0.5 hours to remove air bubbles and transferred into storage tins for testing at a later date. I‘l' "II‘LEE E.‘ 49 3228328 EB 3.8»; M53» 233$ - ma. ”taut z mmzmmumn— mmozm MEDPSEQEE. mmbmmmmm ”=4 5.3..” patio llC) 5.3.2 on tl lllro1 Colu the: 0V: let in 50 5. 3. 2 Chemical properties Basic chemical characteristics of asphalt binders were studied using a high performance gel permeation chromatography (HP-GPC) system, a liquid chromatography (LC) transform unit, and a Fourier transform infi'ared (FT IR) spectrometer. The experimental details of each piece of equipment are summarized as follows. 5. 3. 2.1 High performance gel permeation chromatography system High performance gel permeation chromatography is a separation technique based on the sorting of particles by molecular size. A sample is put into solution and pumped through a column packed with a porous material. As the solution flows through the column, the smaller particles are faced with a longer and more tortuous path due to the many pores that they encounter. The larger particles do not enter as many pores and therefore exit the column first. By measuring the number of particles that exit the column over a given time period, a size distribution of the sample can be created. The molecular weight of a particle can be related to its molecular size through calibration of the column, thus creating a molecular weight distribution. Gel permeation chromatography is sometimes called size exclusion chromatography and has the ability to separate molecules in the 100 to 1 million molecular weight range. During this study, a MilliporeANaters' high performance gel permeation chromatography system was used to analyze the molecular weight distributions of straight asphalts, polymer modifiers, and polymer modified asphalt binders. The system was equipped with a differential refractometer, a photodiode array detector, a chromatography additiomi l angel ll mobile p'h llllttofs measure “LII Will L, 51 manager (Millennium software), a dual reciprocating pump, and a manual injection port. A Lab Connections' liquid chromatography transform unit was also installed as an additional detector for the system. The HP-GPC system was equipped with four Waters' styragel HR columns that encompassed an effective molecular weight range fi'om 0 to 600,000. I-IP-GPC grade tetrahydrofiiran at a flow rate of 1.0 ml/min. was used as the mobile’lphase for this study. The sample concentration was kept constant at 10 grams per 1 liter of solvent as was the injection volume of 250 ml. A difi‘erential refractometer is a detection device that uses optical refraction to measure the concentration of a given material dissolved in a solvent phase. A beam of light will travel at different velocities when passing through different materials. Therefore, if a beam of light enters a material at an angle that is not perpendicular to the material, it will bend or refi'act. The refractive index of a material is a measure of this phenomena and is defined as the ratio of the velocity of light in a vacuum to the velocity of light in the ' given material. The refractive index of a medium is a constant for a given temperature, pressure, and wavelength of light. For this study, a Waters' 410 refractometer was used to measure the molecular weight distributions of asphalts, polymers, and polymer modified asphalts. The refiactometer was operated at 35°C, 20psi, and used a 930 nm monochromatic beam of light. The differential refractometer was very reproducible. Figure 5.4 is an overlay of two AC-10 chromatograms prepared independently fi'om each other. The photodiode array detector allows for the characterization of usefirl chemical I functional groups present in asphalt. PDA was not used extensively in this study, but will S TD 3 332%» as}: 95.32%» \o beSBfiSanK t m. a. pint us Ho: non .on.~. . . .oonm. . . .ommm. . . oo.. 52 'II thrill lll‘lltllrn i ll .lllllll . ' 'l“ III II ‘nl‘ll till .i too. -oH. -ON. -on. .0v. tom. -om. -on. (#01:) P/W 53 be useful in the future to discriminate between certain asphalts and polymers based on their ability to absorb UV light. The axes of PDA data are time (molecular weight), UV absorbance, and wavelength. Using the Millennium software package, dissection of this data is possible that allows individual spectra and chromatograms at a fixed molecular weight or wavelength to be examined. 5. 3. 2. 2 Liquid chromatography transform unit The LC-transform unit is an off-line system that collects the effluent from the differential refractometer (separated by molecular weight) on a germanium disc that can be analyzed using Fourier transform infrared spectrometry at a later date. The LC- transform/FT IR arrangement allowed for the detection of useful chemical functional groups that absorb infrared light. During this study, a Lab Connections' LC-transform unit was used. 5. 3. 2. 3 Fourier transform infrared spectrometer Fourier transform infrared spectroscopy is a technique that measures the infrared absorbtion capabilities of functional groups present in a material. All molecules posses natural resonating frequencies due to either elemental bond stretching, bending, or twisting that fingerprint them. Infrared spectroscopy is able to detect this fingerprint by shining an infrared beam through the sample and measuring the light transmitted through the material. Wavelengths that are the same as those of the molecule are absorbed and not detected, creating an infrared spectra. pozlm SOlllllC using little 54 Fourier transform infrared spectroscopy was used to examine unaged, aged, and polymer modified asphalts. The samples were prepared by evaporating a THE/binder solution on a potassium bromide pellet leaving a thin film of the material to be examined. The solution was mixed at a concentration of 0.5 g of sample per 10 ml of tetrahyrofuran. 0.35 milliliters of the solution was pipetted onto 0.35 g potassium bromide salt pellets and allowed to dry for one hour at room temperature, followed by drying in an oven at 135°C for fifteen minutes. The pellets were made using a dye under a pressure of six metric tons for two intervals of five minutes each. This study used a Perkin Elmer 1800 series spectrometer. The instrument was run using a single beam arrangement with a scan time of 3 seconds. The detector used was a Deuterated Triglycine Sulphate Detector with a diameter of 2mm. 5. 3. 3 Physical properties Basic physical characteristics of asphalt binders were studied using dynamic mechanical analysis (DMA), thermal mechanical analysis (TMA), differential scanning calorimetry (DSC), a bending beam rheometer (BER), and rotational viscometry. The experimental details of each technique are summarized as follows. f 5. 3. 3. 1 Dynamic mechanical analysis Dynamic mechanical analysis is 3 experimental technique that measures the Viscoelastic behavior of a material. The technique is conducted by sandwiching an asphalt Wple between two plates. One plate oscillates at a predetermined sinusoidal frequency lln‘. Po let be. eii 'h llil 5.6 Kit Fla: “’hj C 55 and the other plate remains motionless. As the one plate oscillates, the response of the material is measured using a transducer connected to the opposite plate. If the material responds with no lag time, the material is completely elastic. If the material shows a lag time, the material has a viscous component. The lag time is measured as the phase angle (delta) between the applied shear strain and the resulting shear stress as seen in Figure 5.5”. A phase angle of zero degrees is a perfectly elastic material and one of ninety degrees is a purely viscous material. Polymer modified asphalt shows both viscous and elastic properties. At high temperatures, asphalt is mostly viscous and thus ruts. At lower temperatures, asphalt becomes mostly elastic and cracks. Viscoelastic properties are reported as the loss (6", viscous) and storage (6', elastic) moduli of a material. These moduli are both components of the complex moduli (6") according to the following equation. The instrument that was used in this study measures the complex modulus. The complex modulus is the ratio of the total shear stress to the total shear strain as shown in Figures 5.6 and 5.7”. In this study, dynamic mechanical experiments were performed using a Rheometrics RMS-800 apparatus. All experiments utilized smooth, 25 mm diameter plates in a parallel arrangement with a gap width between 1.4 and 2.0 mm. Sample handling procedures were consistent with those used for the SHRP Bohlin instrument in which the sample is poured hot directly onto the plates and allowed to cool to room 56 .5358? 53:. 23:28 a ao\=§=o 552.32%. r u. u. {Rafi 55>. m At mm. 2:: as: 1.. ICE» 55». ESE as: . ICE-P moo om .l. m ”mzoomS l, .85 met—33— ICE» £25 - 1 32m _ 33% IIEP man 0 .... m ”25mm. :co it It V C .r\.-U.F¢¢OUW.~> 57 3.283: gemstone? axe 2433.8 235.43%.0 .. e .u. when: ©hl 929::an 5:. > I .85». SE B. l anP «U 6.5» 0E: 05> ~ fl A! 1U ._ G «E l P N l P 5 v mace c0299 . E 9.92 59 temperature. Temperature sweeps were then conducted from 25 to 75°C with measurements taken at five degree intervals with an equilibration period of two minutes. A frequency of 10 radians per second was used in compliance with SHRP specifications and strain levels were controlled to insure that the testing was conducted in the linear Viscoelastic range. All tests were replicated between three and seven times to insure accurate and reproducible results. For example, Figure 5.8 shows the reproducibility of the storage modulus versus temperature data for a triplicate. 5. 3. 3. 2 Memo] mechanical analysis Thermal mechanical analysis is an experimental technique that measures the change in shape of a material as a function of temperature. A sample is heated at a given rate and changes in its height are measured using a probe loaded with a predetermined force. Distinct changes in the rate or direction of a height change represent a thermal transition in the material. For this study, thermal mechanical tests were performed on representative asphalt binder samples using a Dupont Instruments, 943 Thermal Mechanical Analyzer. The samples were placed in a 5 mm diameter by 5 mm deep glass boat at rooni temperature and packed firmly forming a flat top surface. The sample was then covered with a 3.5 mm diameter by 1.5 mm thick glass plate upon which a one gram load was placed. The sample was then cooled at approximately 15°C per minute to a temperature of -70°C and allowed to equilibrate. The temperature was then raised at a rate of 5°C per minute and the sample's height change was measured until a total softening (corresponding to a 1 mm depression of the sample) was achieved. After testing, the boats were retrieved to ensure 60 2323.5 3 ae\e§=e§§e& \e =e=o==.\e .3 2:555 9453.4 t a .u. 23w: an 2953 loM - Nu oEEum ll 3 oEEum l-l .09. 2323th ON «cameo.— - «cameo... - 23.95... 2:95... 23mg. _. (ea) .9 that the 5am; the reproduc: heat absorber; This is accom Simple and m direction of the For representative calorirneter. allowed to eq: quenched in n '70°C. The temperatum v time, changes rttfieved to Cr reP63821641 multi 61 that the sample did not flow over the glass cover/plate. All tests were duplicated to check the reproducibility of the results. 5. 3. 3. 3 Differential scanning calorimetry Differential scanning calorimetry is an experimental technique that measures the heat absorbed by, and/or given off by a material under given environmental conditions. This is accomplished by comparing the temperature of a loaded sample to that of a blank sample and measuring the difference between the two. Distinct changes in the rate or direction of the heat flow represent a thermal transition in the material. For this study, differential scanning calorimetry tests were performed on representative asphalt binder samples using a TA Instruments, 910 Differential Scanning Calorimeter. A fifteen milligram asphalt sample was placed in a DSC sample pan and allowed to equilibrate at a predetermined temperature for one hour. The sample was then quenched in liquid nitrogen and placed in the DSC cell that had been previously cooled to -70°C. The system was allowed to equilibrate for fifteen minutes, afier which the temperature was ramped at 5°C per minute to a final temperature of 200°C. During this time, changes in the heat flow were continuously measured. After testing, the sample was retrieved to ensure that none of the sample had leaked out of the DSC pan. All tests were repeated multiple times to ensure reproducible results. 5.3.3.4 Bent The deflection of insmiment is ' dataofthet" given temper Where; 5(1) is' dim“ betwi the deflection 1°§i$tifiness) ‘ 0f 15 the fate rheometer is Shifting asp During asPhalt Sampl “regency 01 581”: 51033. pOSSlbiiity of: Mom temp: safflple 5° that t 62 5. 3.3.4 Bending beam rheometer The bending beam rheometer is an experimental technique that measures the deflection of an asphalt beam under constant load at low temperatures. Specifically, the instrument is set up as a three point bending beam test as can be seen in Figure 5.9”. The data of the test is reported as the creep stiffness and the creep rate of the material at a given temperature and loading time. Creep stiffness is defined as: PL 4bh36(t) S (t) = where; S(t) is the creep stiffness (MPa) at time,t; P is the applied constant load; L is the distance between beam supports; b is the beam width; h is the beam thickness; and S(t) is the deflection in millimeters at time, t. Creep rate is defined as the slope of the curve, log(stiffness) versus log(time). The creep stiffness is often called the m-value and thought of as the rate at which the material can dissipate the applied energy. The bending beam rheometer is used as a prediction method for low temperature thermal cracking when specifying asphalt. During this study, a bending beam rheometer was used to test representative asphalt samples. The samples were prepared by heating a binder until it was the consistency of motor oil and then pouring it into a mold similar to the one pictured in Figure 5.10”. The mold was poured in such a way (single pass), as to eliminate the possibility of creating any air bubbles or forced structure. The mold was allowed to cool at room temperature for one hour and then put in a freezer for ten minutes to harden the sample so that the mold could be removed. Afier removing the sample, it was placed in a 63 nausea? =83 M5323 us \e £3839” - a u. 9.3%.: I 5850855. «tonazm oEmE \\ 9.68.. I v. 58 92“. \ Emmm .333 __mo 33 :o_._m_:ao< 2.3 9.53 .__< \‘ new .ozcou 52695; 832.8 \‘ 64 3a.: .4353. aaaieui :53 355.5 - E .u. 953k EE mmo mnEw Ewe .m 9% a _ 5 223m 20E 53:55.... low tempera mien at thinj nfnrniation beam was re: sample. Selec 5.3.3.5 Rota: Retati of a material liseometry is $11th mate Sample is den Sample‘ Spinn dim” relan “hematic of Dunn were pr eparci A”moxifnatell Climber Ap for thin? minu 65 low temperature bath (-6, -12, ~18, or -24°C) and allowed to equilibrate for another one hour time period. The sample was then loaded into the bending beam apparatus. The test used a 102 mm distance between beam supports and a 100 gram constant load. Data was taken at thirty second time intervals over a four minute period, but only the sixty second information was used for specification purposes. Upon completion of the test, the asphalt beam was removed and broken to check that no air bubbles were captured inside the sample. Selected samples were run multiple times to insure reproducibility of the results. 5. 3. 3.5 Rotational viscometry Rotational viscometry is an experimental technique used to measure the viscosity of a material at temperatures at which the material flows easily. Specifically, rotational viscometry was used to test the viscosity of asphalt at processing temperatures to ensure that the material could be pumped without using excessive energy. The viscosity of a sample is determined by measuring the torque required to keep a spindle, immersed in the sample, spinning at a given rotational velocity and temperature. The necessary torque is directly related to the materials viscosity at the testing temperature. Figure 5.11 is a schematic of the operation. During this study, samples were tested using a Brookfield Viscometer. Samples were prepared by heating them at 135°C until they were the consistency of motor oil. Approximately ten grams of the material was then poured into a preheated sample chamber. A preheated No.27 spindle was immersed in the sample, allowed to equilibrate for thirty minutes at the initial temperature, and the test was started. The spindle was programmed n'scosin' of n. was reported sample was te: of 30°F. At fifteen minutes lht reported re Chapter described in cr. 66 . programmed to rotate at a rotational speed between 5 and 100 rpm depending on the viscosity of the material. The final viscosity of the material at any one given temperature was reported as the average of three data points taken at one minute intervals. Each sample was tested over a temperature range between 220°F and 370°F with interval steps of 30°F. At each proceeding temperature, the sample was allowed to equilibrate for fifteen minutes. Selected samples were tested multiple times to insure reproducibility of the reported results. Chapter Six will discuss the experimental results found from using the tests described in Chapter Five. TORQUE SAM PLE 67 CD 2 4:: :I: Q 'i'l CL 5 d w ter wscorne ' fa rotational “:0 Figure 5. I l - Schema! The , Ir chemical pn Both sectior- and material 6.] 015mm The '. gel permw WISform U' disCussion fi Chapter Six Experimental Results and Discussion The experimental results from this study can be divided into two sections: 1) the chemical properties of asphalt binders, and 2) the physical properties of asphalt binders. Both sections will explore unmodified asphalts and modifiers, polymer modified binders, and materials that were aged according to different processes. 6. 1 Chemical properties The basic characteristics of asphalt binders were studied using a high performance gel permeation chromatography (HP-GPC) system, a liquid chromatography (LC) transform unit, and a Fourier transform infrared (FT IR) spectrometer. The results and discussion fi'om the use of each piece of equipment are summarized as follows. 6.1. 1 High performance gel permeation chromatography Gel permeation chromatography was used to examine the differences between ' unaged AC-S grade asphalt and unaged AC-IO grade asphalt. Three distinct molecular weight ranges (divided by lines A and B) were found to be present in straight asphalt as shown in Figures 6.1 and 6.2. These separations do not correspond to the molecular weight ranges that classify the oil, resin, and asphaltene constituents found in the literature. However, the reported percentages of the constituents do exist if the molecular 68 weight ran: 61 and 61 separation r. asphalt and A o asphalt and 6.3. Asitca A col isshonn in ‘ “We in tl 0.2% weigh Gel 1 We SBS a that Was m and a Polyd Weight at- These p01)“ Beca chmmatogra asphalt/P0131 A05 grade,- AC.5 Sta de a 69 weight ranges (divided by lines C and D) reported in the literature are followed. Tables 6.1 and 6.2 list the percentages of the constituents according to the chromatography separation and separation according to reported literature values for unaged AC-S grade asphalt and unaged AC-lO grade asphalt, respectively. A comparison of HP-GPC chromatograms of unmodified, unaged AC-S grade asphalt and unmodified, unaged AC-10 grade asphalt is depicted in Figure 6.3 and Table 6.3. As it can be seen, it is difficult to distinguish between asphalt grades at this time. A comparison of HP-GPC chromatograms of aged and unaged AC-S grade asphalt is shown in Figure 6.4. It can be seen that when AC-S grade asphalt is aged, there is an increase in the high molecular weight material. During aging there is only approximately a 0.2% weight loss suggesting that the low molecular weight material is being reacted. Gel permeation chromatography was also used to examine the differences between pure SBS and SEBS polymers. Figure 6.5 and Table 6.5 indicateithat the SBS polymer that was studied had a weight average molecular weight of approximately 62,000 g/mol and a polydispersity of two. The SEBS polymer that was studied, on the other hand, had a weight average molecular weight of about 45,000 g/mol and a polydispersity of 1.35. These polymers may therefore, behave difl‘erently in an asphalt/polymer blend. Because polymer molecules are larger than asphalt molecules, gel permeation chromatography was used as an effective tool for determining the polymer content of the aS‘Phtllt/polymer blends that were studied. Figure 6.6 is an example of this technique for AC-S grade asphalt modified with four weight percent SEBS polymer. When the original AC-S grade asphalt chromatogram is subtracted fi'om the asphalt/polymer blend «coal i 0.00.“- F'é’we tr . Table 11 . 7O 80.00- D 60.00- ‘0000' 20.00. 0.00‘ V‘ V 22.00 24.00 26.00 20.00 30.00 32.00 34.00 36.00 38.00 40.00 mutate: Figure 6. 1 - Gel permeation chromatography raw data for unaged, unmodified AC -5 grade asphalt Table 6. 1 - Percentages of constituents in an unaged, unmodified AC -5 grade asphalt Classification WM __:§% Ar High MW (GPC) 7100 + 7 Mid MW (GPC) 2900 - 7100 12 Low MW (GPC) 2900 - 81 High MW (Literature) 2000 + 27 Mid MW (Literature) 800 - 2000 29 Low MW (Literature) 800 - 44 50.357 40.00 E 30.30. 20.00.. moo: 0. col ‘q *6 Figure 6. 2 ' Tableaz. 71 50.00- 40.00- . ,/ 30.00- 20.00- 10 0 00° 3., i if 22.00 24.00 26.00 20.00 30.00 32.00 34.00 36.00 30.00 40:00 minutes Figure 6.2 - Gel permeation chromatography raw data for unaged, unmodified AG] 0 grade asphalt Table 6.2 - Percentages of constituents in an unaged, unmodified AC -1 0 grade asphalt Classification Mglgulag Weight Range % Arg . High MW (GPC) 7200 + 6 Mid MW (GPC) 3000 - 7200 11 Low MW (GPC) 3000 - 83 High MW (Literature) 2000 + 24 Mid MW (Literature) 800 - 2000 31 Low MW (Literature) 800 - 45 3 you C ’d‘lu I064 figure 6.; Table 6.3 . “\me i105 .4010 72 0.60- AC-lO dwt/dtluqfll 0.40- AC-S AC-S AC-lO 0.20- 0.00- 4.40 4.20 4.00 3.00 3.60 3.00 3.20 3.00 2.00 2.00 2.00 2.20 Log lb). «2' Figure 6.3 - Comparison of molecular weight distributions between unmodified, unaged AC—5 grade and AG] 0 grade asphalts Table 6.3 - Molecular weight averages for unmodified unaged AC -5 grade and AC -1 0 grade asphalts Name Mn Mp Mw m Polydispersity AC-S 669 862 2099 6725 3. 14 AC-lO 630 922 1865 5660 2.96 73 O ‘0- 02°- 0101: Id (109“! “E \ /‘ '. 004 0.00 0.00 0.20 0.00 3.00 3.00 3.00 ’ 3.20 3.00 ' 2.00 ' 2.00 ‘ 2.00' 2320 Log 0001 I: Figure 6. 4 - Comparison of molecular weight distributions between unmodified, aged and unaged AC -5 grade asphalt Table 6.4 - Molecular weight averages for unmodified aged and unaged AC -5 grade asphalt Earns m. M0 Mg ‘ _M_z 11011033313133 aged 792 876 3348 11121 4.23 unaged 669 862 2099 6725 3. l4 (flat I.‘ ( I any“) 0‘) C) I figure 6. 5 74 SEBS dwt/dUogH) 0.00 0.00 5.00 5.00 5.205.00 0.00 0.00 0.00 0,200.00 3.00 3.00 3.003.20 Log 0001 we Figure 6.5 - Comparison of molecular weight distributions between pure SBS and SEBS polymer modifiers Table 6. 5 - Molecular weight averages for pure SBS and SEBS polymer modifiers SB S 30002 67865 61900 106729 2.06 SEBS 32730 44092 44445 58327 1 .36 75 chromatogram, the original chromatogram can be divided into three regions: A, B, and C with corresponding areas of 2.52%, 1.49%, and 95.99%, respectively. The areas represent the weight percent of each constituent because the refi'active index detector is a mass sensitive instrument. Region A is the large polymer molecules that are totally separated from the asphalt. Region B is the small polymer molecules that are eluted with the asphalt. This can be easily seen by a comparison of Figure 6.4 with Figure 6.6. A total of four weight percent SEBS polymer modifier can be identified from the HP-GPC data as shown in Table 6.6. It is important to note that it appears that the polymer is being degraded, sheared, or reacted during the mixing process. Similar results were obtained for AC-S/SBS, AC-lO/SEBS, and AC-lO/SBS asphalt grade/polymer modifier blends. A comparison of HP-GPC chromatograms of aged, unmodified AC-S grade asphalt and aged, four weight percent SBS polymer modified AC-S grade asphalt is shown in Figure 6.7. Upon addition of polymer to asphalt, we would expect to see an increase in the amount of the high molecular weight asphalt constituent for the aged sample due to both aging and possible polymer degradation. Instead, we see a decrease in this value suggesting that the polymer has reduced the amount of aging that has occurred. Gel permeation chromatography was also used to examine the difi‘erences between unaged, aged at normal conditions, and severely aged unmodified AC-S grade asphalt and three weight percent SBS polymer modified AC-S grade asphalt. Figure 6.8 and Table 6.7 show that severely aging unmodified AC-S grade asphalt changes the molecular weight distribution very little as compared to the molecular weight distribution of the unmodified " 40.4 m 3 ’1 0 r. ! 76 500.002 400.009 300.009 200.009 AK 100.00‘ 0.004 \A 22.00 20.00 26.00 28.00 30.00 32.00 34.00 36.00 30.00 40.00 Minutes Figure 6. 6 - HP-GPC raw data for unaged AC-5 grade asphalt modified with four weight [mercmnmtEBEHBEipnoiynmer Table 6. 6 - Percentage of SEBS polymer in unaged, polymer modified AC -5 grade asphalt 91235315906213 Start—Mm E___end Tim 23mm SEES 22.38 24.58 2.52 degraded SEBS 25.33 27.28 1.49 AC-S 24.58 39.62 95.99 77 $216 03.2% 0.3.. 10336523 E6 ESBE 2.656% «fin 3.820% .36\ 60%: 3:61:66 863 35 Ukuit - n .6 6.5%.: .83... / .00H.. . on“: . 03:. noun: .2: 0.“... 0.“... 0.“... 0.“... euc=x== 3532...... 03% . Sufi. cad oo.o=q Oc.oo~ cc .2: 06.2: 78 dwt/dlloqfll 0.00- / i O 0. 00- 0 ‘0: normally & ' severely aged 0.20- unaged 0.00.1 4.40 4.20 4.00 3.80 3.60 3.40 3.20 3.00 2.80 2.60 2.40 2.201 200000101: ' Figure 6. 8 - Comparison of molecular weight distributions between unaged normally aged, and severely aged unmodified AC -5 grade asphalt Table 6. 7 - Molecular weight averages for unaged, normally aged and severely aged unmodified AC-5 grade asphalt N_L_§m be ME m M2. P 1 i unaged 669 862 2099 6725 3. 14 normally aged 792 876 3348 l 1121 4.23 severely aged 786 876 3356 11213 4.26 “W‘ 79 material aged under normal conditions. Figure 6.9 and Table 6.8 show a similar result for three weight percent SBS polymer modified AC-S grade asphalt. 6. 1.2 Fourier transform infrared spectroscopy Fourier-transform infrared spectroscopy (FTIR) was used to examine both aged and unaged AC-S grade, and AC-lO grade asphalts. It was determined that there are several defining wavelengths of interest including: 1375, 1450, 1600, and 1700 cm". These wavelengths correspond to CH3, CH2, C=C, and C=O groups respectively. Figure 6.10 is a representation of these groups for an unmodified, aged AC-S grade asphalt sample. Ratios of the absorbance intensities of these functional groups yielded useful information when fingerprinting different asphalt grades. Figure 6.11 indicates that an AC-lO grade asphalt sample has a greater percentage of double bonded carbon than an AC-S grade asphalt sample as would be expected, suggesting a larger resin and/or asphaltene content. However, the AC-lO grade asphalt sample appears to have less CH2 fianctional groups than the AC-S grade asphalt sample, suggesting a lesser resin content. Analysis such as this in combination with gel permeation chromatography could be useful when selecting materials for construction and dealing with recyclability concerns. Fourier-transform infiared spectroscopy was also used to determine any possible defining functional groups of styrene-butadiene-styrene (SB S) and styrene-ethylene- butylene-styrene (SEBS) polymer modifiers that could be used for finger printing. Figures 6.12 and 6.13 are the infrared spectra of SBS and $1538 respectively. The SBS polymer can be identified by a characteristic adsorption/transmitence peak at a wavelength of 965 80 0.00- ’ 0.00- 6 0 :1 2 s 0000- l 3 severely aged 5 002°- / normally aged 0.00- i 5.00 0.50 0.00 3.50 3.00 2.50 Log 0101 00: Figure 6. 9 - Comparison of molecular weight distributions between normally aged and severely aged AC—5 grade asphalt modified with three weight percent SBS polymer Table 6. 8 - Molecular weight averages for normally aged and severely aged AC -5 grade asphalt modified with three weight percent SBS polymer Hams m Mn m m 13936359553! normally aged 803 876 5508 48220 6.86 severely aged 804 867 5692 49201 7.08 81 0383 .338 ova.» m-U< 35.58:: .39 5 .6 8.58% .0235 .5888. Corset .. 2.6 6.5%: b h h r h « an. % a 82 min—£5 8:2 57.5.5 85.13% 59.2995 1:."— - ~ ~ 6 95%.: mass: 55:03.62. mun :8: 3.3692 mun =83 mun tom: :69: m-o< I 2-95 m-o6 - Q ~ 6 6.33% 69% cc" _ 9:6 _ 25” econ - . .2: 93 calorimetry (DSC), a bending beam rheometry (BER), and rotational viscometry. The results and discussion from the use of each piece of equipment are summarized as follows. 6. 2. 1 Dynamic mechanical analysis The creation of a polymer network structure inside an asphalt is the main cause of improved binder properties seen in polymer modified asphalt. Regardless of polymer type, binder properties will not be substantially improved until the formation of a network is completed at an optimum concentration of modifier. Several criteria were examined for selecting the optimum and critical polymer contents, based on rheological properties, of the four asphalt/polymer blends (AC-S/SBS, AC-SISEBS, AC-lO/SBS, and AC-lO/SEBS) studied during this project. The optimum was defined as the point at which there was no longer a significant increase in the rheological properties of the blend with increasing polymer content. The critical content, on the other hand, was defined as the polymer concentration where a deviation fi'om the normal trend in the rheological properties was detected. The optimum and critical polymer contents for the asphalt/polymer blends being studied are reported in Table 6.9. It should be noted that all of the asphalt/polymer blends (polymer contents from zero to ten percent) used in this section of the study met the SHRP binder specification for original asphalt binders. AC-S modified with SBS polymer will be used to demonstrate the criteria used when determining the optimum and critical polymer contents of a given asphalt/polymer ‘w cacti-Lain“ # 1 ' , 94 Table 6. 9 - Optimum and critical polymer contents of studied asphalt/polymer blends based on rheological properties Optimum Content Critical Content ercn ttlweihtofth ashal l erln AC-S/SBS 3 or 5 4 AC-S/SEBS 2 or 5 3 - 4 AC-lO/SBS 2 3 AC-lO/SEBS 2 or 4 3 blend. The other asphalt/polymer blend combinations showed similar results as those seen with the AC-S/SBS blends. The initial criteria for selecting the optimum polymer content to be added to an asphalt based on rheological properties was an intersection of the loss and storage moduli when plotted versus temperature indicating the formation of a pseudo-crosslinked polymer network within the asphalt. Figures 6.20, 6.21 and 6.22 show that this phenomena did not occur until ten weight percent SBS was added to the AC-S grade asphalt. At this time, it was suggested that the research was possibly being conducted with an asphalt that was incompatible with SBS polymer. A second asphalt was tested and the results were comparable to those seen previously as depicted in Figure 6.23. It has also been reported that the minimum amount of polymer modification required to significantly enhance the properties of an asphalt/polymer blend will be recognized as a distinct change in the slope of the storage and/or complex moduli for most asphalts that are modified with a styrenic block copolymer”. However, plots of the 95 xufiéom .43. 252% 339: 25 5...: 3330.: £238 fiesta new ae\uh§.§§2 \: ~S.=.2=.~\e .3 @555 was 3.5 nausea. - 3 6 93.4.5 .0... 2322.80» on on on on av on om T-..-.!--.,_----I..----L $3-1 Till..- _ ,- , .3-..i-,--- -. 8.68% 3&2: firm“... .. SE2... 9 .3301? w. 8&2... w m vo+uaoé ( 3&2: oo+moo€ aefibem .354 25.2.1 EMS... :23. 5.3: heSfiaE £533 macaw WU V ac\u.=:c§$§. \c =e.=o§\a .3 :555 was 33 9.33% .. 2.. 6 95%: .0... 0.33.038»... 8 E. 8 on 8 an an Tlul-+--!..ii_ _1 _ . .\ -Z.Ti|ll-fi 8&2: 8&2... fiammhi ., «Ema: 9 ..~a..o.|au w. - 8&8; m... m. 2:33 ( 3&2... 09.993... 97 in. .JO‘E-Jl: .. . b basa‘am 3%. 232...: 3.4.5: :2 5...: EuSth $33.3 #55 “(UV Bx. HSEKES xv =e.=.25\u .3 ‘3‘er has 33 wages”. - Nm .e 95%: 3.. 9.322.th 8 2. 8 8 8 an 8 _-i-.. _ _ l; il+.--:ilt..--._ _ - fl°+m°°.—. Ere r... Enron? 3&2... 9 E U D. e m 368.— ( warms. p 98 «350% ha. 38.8% EMS... mzKSe: fiflxfiofi Sign» whoam $3333 aims Le\ ESEMKES \e =c=o=§c .3 :5er .23 ES umugea. - a 6 ennui .0... 829.3th on on on em av on ON a a + + a a 3&8; 1 l nc+mcc. w .8. .01? .4 vo+woo€ (ed) snlnpow mc+mco. p l I memos: l l 99 average ”log" slope of G' and G‘ from 25 to 60°C versus increasing polymer content show a straight line with no distinct breaks as shown in Figure 6.24. This behavior does not support the formation of an entangled and continuous polymer network. Instead, the data suggests that this asphalt/SBS polymer blend forms localized and dispersed networks. At approximately 8.5 percent SBS polymer content, the blend exhibits a ”matrix inversion”. This phenomena is depicted in Figure 6.25 by an intersection of the storage and loss moduli at 60°C and in Figure 6.26 by a tan5 value less than one at a polymer content of about 8.5 percent. Similar observations were also reported by Brule who witnessed matrix inversions at polymer contents between 7.5 and 12.5 percent polymer content”. King has reported that the loss modulus at 60°C can be used as a predictive tool for determining the optimum polymer content necessary to maximize the rheological properties of a polymer modified binder". In this study, no significant increase in the values of G' and G” were measured by increasing the polymer content above five percent as shown in Figure 6.25. It is important to note that the data shows a deviation from the normal trend at four percent polymer content. This deviation was observed in every test. The SHRP original binder specifications set a minimum l/J" value of 1 kPa at 60°C. Based on the SHRP specification and the test data shown in Figure 6.27, all of the samples including the unmodified binder used in this study satisfy the specification. Once again, a deviation from the normal trend in the rheological properties at four percent polymer content can be seen. 100 I Elli. i: . .er . Do E. 8 2 Set. 90‘ 5 E828 qubcm v.5. «.5622: \e zozoziu .3 .Sfiefi quEou ES» umuaofixw one}. ewes. . 32. 93%.: 33:00 3820.. wmm «caged c9 l “2 '9 It) I In ‘7' (,orX) 0.09 or 92 won odors “601.. ‘T «3. r? 101 U. 00 3 SUV 5 .5269 #502. mm... .292»an 8.0.25.5 .3 .335 unset. 36 .980 - MN .0 230.5 . 28:00 3.5.-om mmm Eco-on o F a o v u l ..0.0 . 0...0 00... 1- 00.0.. . 00.00.. (can) 3.09 :2 rrnpow 102 . 1.3.! ”mutt-J. l D. 00 B 30 V 2.. 33:8 @232. v.94? 29:95.? .8 SB.» .3. - 3.0 83%.... 22:00 3520.. wow .523. 0r 0 0 v N p q A— «r- 009 12 Lotus) also I121 Du an B “60‘ 5 38:8 quéckmfiwxw =S~u§xd 8 828358 .83 3.335 - «N.» Hang 52:00 .8520."— mmm 2.083. or o c v N o qh dr- — 1- 103 é 0.09 :2 (can) um : cop 1 04 Bouldin has also suggested two ratios which may help in determining the effectiveness of a polymer modification". These ratios are l) a comparison of the storage modulus for the modified binder (G’m) versus that of the unmodified material (G’u) at 60°C, and 2) a comparison of the storage moduli for the modified binder at 25°C versus 60°C (G’zs/G’60)m. In an ideal asphalt/polymer blend, the ratio (G’m/G’u) should be a maximum, while the ratio (G’zs/G’60)m should be one (rel). Figure 6.28 depicts the ratio (G’m/G’u) versus polymer content. Examination of the figure indicates that: 0 Increasing SBS polymer content from zero to three percent causes about a 100 fold increase in the ratio. 0 At four percent SBS polymer content, there is a deviation (depression) from the normal trend. 0 Increasing polymer content above five percent causes no significant change in the ratio. Based on these observations, it is concluded that the optimum polymer content is five percent and the critical polymer content is four percent. On the other hand, Figure 6.29 shows that changes in the values of (G’zs/G’50)m are insignificant after an optimum SBS polymer content of three percent. The data presented in Figures 6.28 and 6.29 imply that the optimum polymer content is sensitive to the temperature at which properties are measured and depends on the type of data analysis. . The sensitivity of tanfi to temperature (a two-temperature curve) can also be a powerful 'predictive tool for determining the optimum polymer content”. However, no specifications of the average slope of the curve or tano values that denote the optimum 105 38:8 goEbok \o =o.=.o§.\o .8 be an 3 .5253 5:38 uhEM WUV EuSfiofiaa o. WU V 3338.: .35on ham? 2:: 3335 uwogofi .. QN 6 9335‘ 28:00 3820.“ mmm “cocoon 3 a o e N o w a w o h .3 a w. m . m 9 m a :3 m. U m 0 m.. w. is. m w 9 m. I; . ocow 106 lnrltrlnllb'l 58:8 amfibomsso zoaozfid .3 P 8 S P Wm 3 £233 REE urbv. E3532: amEbom ammo 952 ”$585 owoaoa. .. mm 6 Exam 2.2.30 .2:on mmm 2.3.8.“. cop OON can can (one) .9 I (3.92) .9 com och com 107 polymer content have been suggested and/or reported. Figure 6.30 indicates a continual flattening (decrease in the sensitivity) of the tan8 curve with increasing polymer content which suggests improved rheological properties. Therefore, an exact optimum polymer content cannot be determined without first specifying a flatness criteria or a degree of sensitivity. In this study it is suggested that the following criteria for the temperature sensitivity of tanfi, F(r.t.) be used. F(r.t.) = {log [(tan5 @ 25°C) / (tan6 @ 60°C)]} At a value of zero, tan5 is considered flat or insensitive to temperature (tan5250C = tano 60°C)' Figure 6.31 shows that "F(r.t.)" has a value of zero at five percent polymer content agreeing with several of the previous data analyses. Moreover, the value of tan5 at 60°C versus polymer content depicted in Figure 6.26 shows a deviation fi'om the normal trend at four percent polymer content. This further suggests the need for a specified value of tanfi at a given temperature. Dynamic mechanical analysis was also used to measure the storage modulus, G', and loss modulus, G" at high pavement temperatures of AC-S/SBS polymer blends that were aged under severe conditions (15°C higher than normal). Figures 6.32 through 6.34 are a comparison of G', G", and tan8, respectively of unaged, aged at normal conditions, and aged at severe conditions of unmodified AC-S. It is clear that the elevated aging temperature increased both the loss and storage moduli over the given temperature regime. In addition, tan delta decreased with accelerated aging, suggesting that the storage modulus was increasing at a faster rate than the loss modulus. Figure 6.35 depicts the percent increase in G' at 60°C of the severely aged versus normally aged, and severely 108 :35: omega new 3&3er «ox. 25533.... 33 3.3.6... Logan ha. 8 32?: is: 8?} =3 \e eatifin - 3.6 332.2 .0... 238258... 8 2 8 8 8 8 a Tli. . a s ..... . . ..... o. 8... mmm s31? .- 8.. wow s «IT . . . mom x air .\ .. 8 u . 1 mom :7? .- 8.” m mom .\. all so new «.7? . .. 8... m." man 3 cl: . m mm» «.7? - 8.... m mom :7? .. 8.x. 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Y cod. co.” 09v cod V. cod # 00.» L 00.0 r . % cod fl 8.: 4}— ! .— l | m5m< t2§2m I... m:_m.< .9502 [ml tuna—5 In: (.91..9) also 021 113 autumn «Sim «(UV 3585:: S\M:.~Mu\c zetszfiu a: P cc 3 .3335 «M563. m5 5 83...qu =89ng - 2.6 233% msmu EEO: 3925 3mg: .2, 9:9 .m> 95mm .m> 55mm “.8263 $326.» .250: Tllll w * : o u w nun : 82. w m. % coca m «map a -- coon « , 83. m. s 41 83 m... 88 m w % coon m" nu ,- 88 m 33 .r v 88 m. A _ 114 aged versus unaged, unmodified, AC-S grade asphalt. Increasing the processing temperature, caused over 300 percent more aging based on this criteria for unmodified AC-S. Figures 6.36 through 6.38 are a comparison of G', G", and tanfi, respectively of unaged, aged at normal conditions, and aged at severe conditions of A05 grade asphalt modified with three weight percent SBS. It is clear that the severe aging process again increased both the loss and storage moduli over the given temperature regime. In addition, tan delta again decreased with accelerated aging, suggesting that the storage modulus increased at a faster rate than, the loss modulus. Figure 6.39 depicts the percent increase in G‘ at 60°C of the severely aged versus normally aged, and severely aged versus unaged three weight percent SBS polymer modified AC-S grade asphalt. Increasing the processing temperature, caused only 65 percent more aging based on this criteria for three weight percent SBS polymer modified AC-S grade asphalt. It appears that even under severe processing conditions, the addition of SBS polymer to AC-S grade asphalt may be retarding the aging process. 6. 2. 2 Thermal mechanical analysis Thermal mechanical analysis tests showed that the glass transition temperatures of both SBS and SEBS polymers are in the range from -60 to -90°C as depicted in Figure 6.40 for the SBS polymer. These results agree with information supplied by the polymer manufacturer. IKE“. v nt..ddyr.u.u..lui 115 $233 .05. ~56an EMS: ~25 5.3. VmShoE 5:38 omega 5.0 V S\ESE~§§ \o =o§o§\o .3 «Saves uMESm. .. 3:» Exam .0.» 2322.88. on 2. cm on 3 on ow T w a T a n «958... m5m< “5355+ - 3&2: Guise—321ml R. tomuchcl m n ,. I, 3&2... w , W o o. ,, n r- 3&3... N ., e. um - W - u u l «cameo... L- some: 116 _ .ili' [IL $5on hm“. Emoaom 3M3: ~25 5.3. 3332: £933 whoam nrbw 3.x 255333 No 2323\3 3 3385 anew - u Me {ant .0... 2322.th on on cm on ov on cm a a a a e T 3.58; m£m< 3.265 + m5m< 35.3le i 21mg; noun—5 lo: M. a m L1 mews; m. M 8 \41. but 23mg; L- 3.52:. 117 gufiéam «fin 23.23 33.9: 925 5...: BEBE 533.3 ghagm “69V Bx. EEEKEXE =e.:u==\c an 83: SQ - an 6 95qu .0... 23238»... on an em on 3 on an Tl’T‘JinIfIT? 5T . f {LIJ‘ 8.9 on; : a: f °°.F l . w ‘ 8F 0 a ; oo.~ W. : o~.~ m 9 ; 3N (u a m :. 2m+ -1 on." 9.5 «53 . 5 2+ ‘ 8N 3925+ , co.” 118 22.59% Ma. E~2~m SS2. ~25 5.3. 535505 53% 5.2% anew 22.5233? 253553 .3 P 3 3 .2552: ~M28~ ~5 5 ~82~5 E~2~m - 3.6 238% 55mm .250: amuse: among: .9, mean .2, mafia .m> 9.35 @3553 63263 35.5: Ill w L 1.. no 1- 03 d O 1, a3 w W : :8 m «E m J, :8 m. u a : 83 P- 83 119 28.30% .43.? 252~QE- 25.565 3.5% ~5 \e 205355.225 ~5 55335 g - 5‘ 6 2.3K Go. 3.5 2...???» O3” . cm- ' Gnar— > A“... m. > Om“ - =3P— - - gum; O. I n— o I t n W a .u... U \I 3 U O U a a m I a .fl. 0 120 Thermal mechanical analysis tests were also used to look at the final sofiening temperatures of the four asphalt grade/polymer blend combinations that were studied during this project. Examination of Figure 6.41 indicates that: 1. All of the TMA data support the conclusions drawn in the critical and optimum polymer content study. 2. The final softening temperature of AC-lO grade asphalt is greater than that of AC-S grade asphalt as was expected. 3. At their respective optimum polymer contents, there is little difference in the final softening temperatures of the difl'erent asphalt grade/polymer blends. 4. At their respective optimum polymer contents, there is an increase of approximately 25°C in the final softening temperature of the asphalt grade/polymer blends with respect to the unmodified asphalt. It is very important to note however, that thermal mechanical analysis tests do not account for any elastic recovery of the sample when the load is removed. Aged AC-S grade asphalt/SBS polymer blends were also tested using thermal mechanical analysis to determine the final softening temperatures of the samples. Examination of Figure 6.42 indicates that increasing the polymer content beyond the optimum percentage had an insignificant efi'ect on the final softening temperature of the aged AC-S grade asphalt/SBS polymer blends. Figure 6.43 shows the difl‘erences in the final softening temperatures of the aged versus unaged samples for increasing polymer content. At approximately nine weight percent polymer modification, there is no difference in the final softening temperatures between the aged and unaged samples. This 121 g .3 355225 58:8 22$?»an $5353 .3 .4283 2~§¢o$~m~2m 53335» “252355 M5358 35K . NV .5 233k 28:00 .8520.— “cocoon. Np 2. m o v N "F- qt— -o- qr— J.— -0— O O «mum? 2.2T? . mum} 2.0T? ‘ mama; 997? imv.’ mm» 3 m-o<+ \ O I l l I I In 0 o: a: J. {a J. é. u. 0 Q h h 0 (a) mntmodwal Buguauos |eug=| l i 2:. .2 me. a, o: 122 E .3 5255225 5228 2253? 552:5: no “3&3 253.3% adv. 5523.3 52% «(UV 5&2: 5:: 5~me\o “2562558 @5559. EEK - NV .5 23%: 58:00 3820.". «mm “neocon— m a n m m w n N _. o w a a x n n + w n . 8 .. mm H .. .. 2 w... flam<+ - n: uh m 9 non—25+ .. - on m. .. 5 .r mu I. 8 .fi 8 .m . m ,L -r “G Im— . . .. 8. M O .- m2. ( .5 o: 123 g A5 5255255 5858 22.3.33? =o.=~==\ c .3 “5235 22.3% 53.53%: 532% 5.9V V~M-§ 2:22 5&9? “2523.52 M5=~§oa 35x. ~5 5 -~=2~§Q - M» .5 235.3 22:00 3520.. mm» «520.. .4.— «>- «>— -— o F (O. ) untuodmu Buguouos led u! oauuouga 124 polymer content corresponds to the level of modification thought to cause a matrix inversion of the A05 grade asphalt/SBS polymer blend. It appears that addition of polymer retards age hardening and at the matrix inversion, no further hardening occurs. 6. 2. 3 Differential scanning calorimetry Differential scanning calorimetry was used to examine any temperature dependent structure that may exist in asphalt. It was found that there are three distinct transitions that exist in straight asphalt at approximately -12, 10, and 33°C as depicted in Figure 6.44. Figure 6.45 shows that these transitions were more pronounced in the softer grades of asphalt suggesting that they are dependent on the samples' oil contents. It was also shown that upon heating for a period of one hour at various temperatures followed by quenching, the transitions at 10 and 33° could be eliminated as seen in Figure 6.46. This was found to be a reversible process however. If a heated sample was allowed to equilibrate at room temperature, the transitions reappeared as shown in Figure 6.47 suggesting that these were structural and not chemical transitions. It is believed that at the higher temperatures, the aSphalt samples' polar structure is destroyed. Dr. Lawrence Drzal’s group has used an environmental scanning electron microscope to visually examine asphalt structure. A network-like structure was discovered at room temperature that is believed to correspond to the transitions observed using differential scanning calorimetry. After heating the samme, Dr. Drzal's group visually observed the structure disappear. The sample was allow to equilibrate at room temperature and the stmcture reappeared. 125 This phenomena may be important for practical pavement construction practices. Many asphalt pavement roads that are laid in the cold, Fall months crack before the following Spring. Currently, the cracking has been contributed to poor compaction practices. However, this study suggests that the cracking may be a material problem. If a hot asphalt is compacted during construction with a cold, snowy roller, it may have the efl‘ect of quenching in the structureless, high temperature properties. The final pavement would be very brittle and crack easily. Upon addition of polymer to asphalt, the transitions were altered in a different manner and were difficult to analyze without further investigation. 6. 2. 4 Bending beam rheometer The bending beam rheometer was used to measure the stiffness, and m-values of SBS polymer modified AC-S grade asphalts that were aged at normal conditions. Figure 6.48 shows how the stiffness of SBS polymer modified AC-S grade asphalts that have been aged at normal conditions vary as a function of polymer content at a temperature of - 24°C. As the polymer content is increased, the stiffness of the binder decreases thus enhancing the low temperature properties. However, unmodified AC-S grade asphalt behaves similarly to four weight percent SBS polymer modified AC-S grade asphalt. It appears that initial addition of SBS polymer to AC-S grade asphalt may actually worsen the low temperature properties of the binder. It is interesting to note that four weight percent SBS polymer content was identified as the critical amount of polymer modification based on high temperature rheological and thermal mechanical analysis results. 53% 52% 5.0 V \o 252358 55.585 35% ~55 \o =o5§5§§~5 ~5 22.85 bud - V5. .5 235.55 5... 2.... 5......53 mm . o c . b r ? p Ll :0 p p 3.. 12E5 > Aug; “4.:\ . _ 2 2 15/"l ~|OI: 133M 127 52% 53% a. as. one - a}. 2:5 \o 5285‘: .3 3.5.58.5 \e b.5255 ~.5 «2.52% .30. vim-c.2594». O... . _ .. .. m an ... - . . . - . . . . . Qé - b p r r Tm.ee e. 6 N O I O O i5/Hl “CIA aaau use 128 bag: 825388 \c 8.55%.3 .3 gas 3:3.in SS» UMQ - 3.» {ant EL 9:395:29... .\ on . mm o b p b » p P u p P n b h D p h h > r > n p b P > N c o co n o / U S 3 .m ox h on ... 4/ ‘3 w «01; .e '3 I ’ l ' 25:: Z: : 2:2: 129 wt.%.? 255353 2.5.32? 202.05%: .3 30333. Méfiawh SUE DmQ .. n V 6 23%: fr; .. :.......u:=.m.—.. c. A: :_ : h - N. .c U :3 :— 130 P VN- 3 £35.: £65 WUV 3339: ksécm an“. .6\&§§=. 325.35 gang»? =63 M5355 .. aw 6 234: 2.2—.00 3:53.. mom 2.33.. c a v N a v w w .1 3' 1'. 02 m e m 4 08 m D. m. f OmN mm u «3. tr can 9 m .- cmn R g- 00? 1 31 Figure 6.49 is a similar presentation of the stiffness of SBS polymer modified AC- 10 grade asphalt samples that were aged under normal conditions. A similar trend of enhanced low temperature properties was not seen for this asphalt/polymer blend. It is important to note however, that the average difference in stiffness between AC-lO grade and AC-S grade polymer modified asphalt samples was much greater than the enhancement seen due to polymer modification. Therefore, it is suggested that the low temperature properties of an asphalt/polymer blend be controlled by softening the asphalt grade, and not by increasing the polymer content. Only the AC-S grade asphalt samples modified with five or more weight percent SBS polymer met the applicable SHRP binder specification. Figure 6.50 shows the m-values, or creep rates, of SBS polymer modified AC-S grade asphalts that have been aged at normal conditions vary as a function of polymer content at a temperature of ~24°C. It appears that the m-value is not a function of polymer content as suggested by the SHRP binder specifications for polymer modified systems. A similar analysis of SBS polymer modified AC-lO grade asphalt samples draws a similar conclusion. However, there is an average increase of the m-value by 10% when comparing AC-S grade to AC-lO grade asphalt. This further suggests controlling the low temperature properties of a polymer modified binder by softening the asphalt grade, and not by increasing the polymer content. It should be noted that none of the samples tested met the minimum SHRP m-value specification of 0.3 at -24°C. 132 P X- 3 £356 £35m 2.9 V hoSheE $5on ”mm ao\uu§§~u heaEduE @3585 :63 MSESQ .. as. 6 93%: 2.8.30 .85on wow Eugen. -r- db on” .4.— : on” i can i a; l, cue -r cmv (can) sseugns pamseew 11 95v : omv 133 D. VN- :6 63.3.8 whosm 6.9V BmShoE L333 .63. .6\=§=oo augng 29:23.?» .3 836 26975 games»? 586 363.3% - a. 6 95%: 2.2.30 8520“. mam, :8an a s m m c n N p a pd .. «.3 .- 36 .1 2.6 3.6 -. Nd .. and i «Nd % mud 4. mad H a... —o— «+- -0— -1r- d!- db .4.— l amen-w 1 34 The bending beam rheometer was also used to measure the stiffness and m-values of severely aged SBS polymer modified AC-S grade asphalt samples. It was determined that severe aging caused the stiffness of the samples to decrease by an average of approximately 30 MPa. The m-values of the severely aged samples were similar to those of the samples aged under normal conditions. 6. 2.5 Rotational viscometry Rotational viscometry was used to measure the viscosity of polymer modified asphalts at processing temperatures, 220 - 370°F, to determine whether conventional equipment could be used during road construction. Figure 6.51 is the data collected for AC-S grade asphalt cement, modified with SBS polymer. It should be noted that all of the materials tested met the appropriate SHRP specification for the viscosity of an original binder. Figure 6.52 shows how viscosity is afi‘ected by increasing polymer content at the specification temperature of 270°F. At processing temperatures, a critical polymer content is no longer witnessed. All of the asphalt/polymer blend combinations studied, showed similar results. 135 3552?». \o =EB==\= .3 $3un $32M 66V 3&382 #2:ka mfihfi 5.20%.: n a. 6 Rant C... 9.323th on" can can 3n emu Eh emu can an a a n w 8.. fi 88.. + wmm $ml¢l wmm 36+ wmm $vlon wmm $nl¢l mmw .x. wlfiT wmw $o+ (d9) Ausoosrn 136 33:8 nugget? =o..§=.\o .3 is E N B $23.3 who...» 6Q... 3339.. awsboa .65.? b.3903 .. Na. 6 233% 2.2.30 3:50.. mmm 2.33m n v n N p c T . .r . . _. n. 2.an uaoulol f 3 "— omulol A ..._ 3an m. a l 2:. m .M mu H o\o\..l \ 82 002:. Chapter Seven Conclusions and Theories 7. 1 Theoretical models 7.1.1 Asphalt Asphalt is a complex mixture of many different hydrocarbons consisting primarily of molecules that contain mainly carbon and hydrogen atoms. A generic asphalt elemental analysis shows that approximately 84 percent of the sample is carbon, 10 percent hydrogen, 1 percent oxygen, and the remainder consists of several trace elements including nitrogen, sulfur, vanadium, nickel, and iron’. The average molecular weight of a generic asphalt molecule ranges from 500 to 5000. The arrangement of the various elements in an asphalt binder is of much greater importance than the total amounts of the elements themselves. Asphalt consists mainly of linear and complex organic ring structures. The ring structures can be separated into two groups: naphthenic and aromatic. Naphthenic compounds are simple or complex saturated rings that have a large number of side chains. Aromatic compounds are heavier molecules that consist of stable six atom rings with few side chains. For convenience, asphalt constituents are classified into three categories: oils, resins, and asphaltenes. Oils are the light compounds in asphalt which have the lowest molecular weights (24 - 800) and have a large number of side chains and few rings. Accepted criteria for the oil classification are molecules with carbon/hydrogen atom ratios 137 138 less than 0.6 and are soluble in hexane”. Resins are intermediate molecular weight compounds (800 - 2000). It is important to note that resins can contain sulfiir and nitrogen. Resins are polar, have carbon to hydrogen atom ratios between 0.6 and 0.8 and are soluble in light petroleum naphtha“. Asphaltenes contain the trace elements mentioned earlier which may react with potential polymers and are soluble in carbon tetrachloride. An average asphalt sample has an asphaltene/resin/oil ratio of approximately 23/27/509 and the asphaltene content is higher for harder asphalts. High performance gel permeation chromatography (HP-GPC) is usually used to determine the molecular weight distribution, molecular weight, and the fraction of each constituent in an asphalt sample. Using the asphaltene/resin/oil classifications, a two phase asphalt model is developed“. Phase 1 is an assembly phase consisting of asphaltenes and resins that is dispersed in phase 2, the solvent phase consisting of the oily constituents. Figure 7 .1 is a symbolic depiction of this model. The resins behave as peptizing agents that stabilize the asphaltenes in the oily constituents. The asphaltene core of the assembly phase can vary between 40 and 60 angstroms in diameter. As the asphaltene content of an asphalt sample increases, the assembly phase also increases. This adds structure to the asphalt and gives it better high temperature properties and rutting resistance. The percentage of the assembly phase present is the defining factor between different grades of asphalts. The resins contain aromatic compounds substituted with longer alkyls and a larger number of side chains attached to the rings than asphaltenes. The combination of the saturated and the aromatic characteristics of the resins stabilizes the colloidal nature of the asphaltenes in the oil 139 Ewes $23.3 3.3% 9:5 . ~ N 333% c528. 25 u N 8...... $335925 v.58: + 8:3.2En< .I.. _ 3.2..— WWII. I noguufiaaa< \ ago s© . 140 medium. Asphaltenes are present as discrete or colloidally dispersed particles in the oily phase. Colloidally dispersed asphaltenes are not stable in the oil medium by themselves, but can be stabilized through polar resins. Asphaltenes can exist both in a randomly oriented particle aggregate form or in an ordered micelle form. In micelle form, the polar groups (water, silica, or metals such as V, Ni, an Fe) are either oriented toward the center to form an oil-external micelle or oriented outward to form an oil-internal micelle (Hartley micelle). The growth and ultimate size of the micelles are dependent on temperature, resin content, and the presence of other chemicals such as polymer modifiers. The engineering properties of asphalts are directly related to the quantity of asphaltenes, the size of the micelle structure, and the nature of the dispersion medium, oils and resins. Another important aspect of asphalts for polymer modification is that the fiinctional groups present in asphalts may react with polymers during processing. Functional groups that have been identified in asphalts include: carboxylic acids, ketones, phenols, sulfoxides, acid anhydrides, pyrroles, and quinones". 7.1.2 Network thennoplastics (SBS and SEBS) The theorized behavior of SBS in asphalt can best be examined by looking at the effect of increasing polymer content at three temperature regimes. It should first be noted that SBS is composed of two hard sphere-like styrene ends joined by an elastic butadiene component. As depicted in Figure 7.2, the styrene ends are attracted to each other forming a network-like polymeric structure. At service temperatures, a plot of the storage modulus versus polymer. content depicts a non-continuous curve with a distinct optimum and critical polymer content as 141 .32:er any. \e .3353qu .. m N uncut 9.5.9250 ”gonzo wzm—Ctm 142 seen in Figure 7.3. It is theorized that as the polymer is being added to the system, it is slowly destroying the natural structure of the base asphalt by absorbing the oily constituent. At some critical polymer content, this interaction affects the stability of the asphalt system by interacting with the resin constituent. At the same time, the polymer is adding structure to the blend and at a difi‘erent polymer content, a network structure is achieved thus dramatically enhancing the properties of the system. Figures 7.4 and 7 .5 are depictions of this theory. Experimental data on asphalts with varying amounts of oil support the theory. At high temperatures, the physical structures of both the asphalt and polymer styrene interactions are overcome by the energy of the environment. The polymer acts as simply a molecule of higher molecular weight in the system. This theory is supported by linear viscosity data as a function of polymer content. Figures 7 .6 and 7 .7 are a depiction of the high temperature theory. At low temperatures, the system shows a critical polymer content with respect to bending beam rheometry data. However, this data is hard to duplicate. At low temperatures, it is believed that the polymer can not absorb as much of the oily constituent and therefore does not affect the resin constituents. The difficulty in the reproduction of experimental data may be due to sample handling. Samples for the bending beam rheometer are prepared at high temperatures. The amount of oil absorption will depend on the rate at which the samples are allowed to cool and the final equilibration temperature. 143 25%... i 32:8 §§i§ §=2=.\e as .. v S E SSE: as 3:: sauce? - a N Eaui 2.3.30 35301 mmm Eon-com S. o wad ._ 3.6 cc. _. - oodw - 2.63. (can) 3,0919 unpow $253358 3.353. E #933 Vflhfiofi 33% 23539.4 - V N EEMQ mzwagbm wzwmtw 145 aaaiusukfia 3.35.5 E ASE: :35?» 3.4332: v5.4 \m. 35:32 - u. N 23.4.: Euhzoo unmade r ‘1 hast. m< paw—3.2.01 anatomical->- czzuio_ioo_o<_r 146 limit?! I a..a§:=bi=§~ «M:2§.5a$ <3: 3 i213 3.9%}..3 any. \: .Szfiaeuh . e N 35%.: 1.0510: 0‘ z Ti. 147 awaioaunfie «aziauooke $43 3 .035 55%: 3:35.: ham. \: 5:3.in - N N 333% #25290 paw—gag AL hizmm< waif—On— z..E,...§.z 3 >_muom_r->- 1 48 7.1.3 Dispersed Thermoplastic: (PE) It is theorized that PE adds to asphalt in a dispersed fashion. There are no styrene interactions like those found in SBS. Therefore, in order to form a network of dispersed polymer, it must be added until a matrix inversion occurs and the system becomes asphalt dispersed in PE. Much more PE will be needed to modify an asphalt than SBS. Figure 7.8 is a schematic of this model. 7.1.4 Reactive polymers (Elvaloy @AM) It is theorized that Elvaloy®AM chemically reacts with asphalt cement creating a new material. Elvaloy®AM contains an epoxy firnctional group that is believed to react with aromatic carboxylic acid functional groups found in the asphaltene constituent of asphalt cement. Because the system uses the asphalt itself to create a network-like structure, less Elvaloy®AM would be needed for asphalt modification than SBS. Figure 7.9 is a schematic of this model. 7. 1.5 Crumb rubber particles Crumb rubber, like asphalt, consists of three constituents: rubber, carbon black, and oils. It is theorized that when crumb rubber is added to asphalt, there is a migration and sharing of oily constituents thus forming an interpenetrating network or an adhesive- like structure. From the literature it appears as if this process is extremely sensitive to both time and temperature. Figure 7.10 is a schematic of this model. 149 autcoankEE 3.53». 3 $313 3336.: mm \e 255234 - a N 83%: Eddramd 150 .§.==E~QE& 8.35:. 3 Sci?» EuSNSE :VQAoNgNm \e .33E39m. .. a N 233% ., fififinfia .3. no} n.u.u....”.n.vvu xanauxx 151 9.3.2535». 8‘23. 3 53%: 3.33.5 53$: efifiufiy 3.353%. - ¢ ~ N usaumk 1 52 7.2 Mixing procedure theory It has been the industry standard to mix asphalt and polymer unlit it appears homogeneous to the naked eye. This has been found to be a poor practice for laboratory procedures. A mixing procedure was therefore developed based upon the improvement of rheological properties for varying temperatures and mixing times. The optimized procedure calls for heating the asphalt at 270°F for one hour to obtain a good melt, followed by mixing of the polymer and asphalt at 350°F for two hours. The above procedure was chosen based on the following study. Figure 7.11 depicts a typical curve of tan6 (G"IG') versus temperature at various mixing times for an AC-S grade asphalt modified with five weight percent SBS polymer. After a mixing period of forty-five minutes, the asphalt polymer blend appeared to be homogeneous. However, the blend phase separated in two days. Seventy minutes of mixing prevented the blend from separating for approximately one week and for mixing times equal to or greater than two hours, no phase separation was ever observed within a two month period. It can be seen that the curve corresponding to a two hour mixing period shows insignificant changes of tan6 with increasing temperatures. In addition, for all polymer contents used in this study, as the mixing time increased from 0 to 120 minutes, the rheological properties (storage modulus, G'; loss modulus, G"; and complex modulus, G“) of the material continued to increase. At a mixing time of 180 minutes, however, the properties of the blend began to degrade as 153 Ezeéca .35 585.1 33...... ERSF: 3:955 .33?» “Scam 5...va gex.»E.= 3.3.2: 3:: u..=:~.§§2§ \e =2.=.2=.\.= a: 33% :5. u : N 33%.: .0... 239.095; . . . _. . . .r . 2. . - cod . ooé cod co.” W. 8... a . m. .. I; ...... - -....-I.l1 com m .5... 8:8“.87T 8... aw 5:. 2. Biennial co.» m .. SE mv .8 n. cmn lol , cad :3: 50 . 8a I87? .. 8... 5x50 to! ....... -- ---,.z.--..-, .. 8.2 ' 154 would be expected from the discussion given by Brule who stated that there is an optimum mixing time for maximizing the mechanical properties of an asphalt/polymer blend”. It was assumed that the highest concentration of polymer that would be added and still be economically feasible was seven weight percent SBS. Figure 7.12 shows the effect of mixing time on the rheological properties of an AC-S grade asphalt modified with seven weight percent SBS polymer. After mixing for 120 minutes, no substantial change in tan6 can be detected. . A worse case mixing scenario of A020 grade asphalt modified with seven weight percent SBS polymer was also studied to ensure that the procedure was acceptable for all asphalt/network thermoplastic blends. This combination of materials was chosen because of the large polymer content and the lack of low molecular weight oils found in A020 grade asphalt that are beneficial to the mixing procedure. Figure 7 . 13 shows the effect of mixing time on the rheological properties of the worse case scenario. It can be seen from Figure 7.13 that increasing the mixing time beyond 120 minutes does not increase the rheological properties of the blend. 7.3 Aging phenomena 7. 3. 1 Eflect of polymer modification After carefiJl analysis of the data collected in this study, it has been concluded that the addition of SBS and SEBS polymers to AC-S and AC-lO grade asphalt retards the aging process. Data supporting this conclusion are as follows. 155 «2.5.3: .43. 23.2.: 33...: 5...»... 5...: 3&355 $233 .53...» m... :x .5.\ 2...: $53: NE: 935335~ \e ..e.:.»==\= .3 SEN. =3. - .. N N N 33%.: 8o. 23235.0... cm on cm on 3. an cm 2!-.. «.0. cm? ccwhmmmownlol . .. ed 58 o~_...o_u_omn|m: . ed M. 5:. 83:33:..- .3 M \ .- 2:2 .- . p m.- ..\- Ill 3 m .\ .. . . - . . 3 W n . . m... cé ..- u 156 .35.... .090 ...~......& 339: 2...; .3. 5...: 3.5.35... :35... $5..» an. V .5535... w.......=.\o zenizksfi. . - M. N 33...: . .0... 239.2.th on 2. on an 3. on em . 32 .22.:- ....... . -- .. 32:2.- - - :Tln-i 2.. c p a m. n u 0 . , .- 2 - MW e m 5:. 8.3::an tow. 55828.87? m at“ w . N 157 0 Upon addition of polymer to asphalt, an increase in the amount of the high molecular weight asphalt constituent for the aged sample would be expected due to both aging and possible polymer degradation. Instead, a decrease in this value is observed. This phenomena is seen for both normally aged and severely aged material. 0 FTIR spectra of aged, polymer modified asphalt binders show the formation of less C=O functional groups than those of unmodified materials. The formation of C=O functional groups is an indication of oxidative aging. This phenomena was also seen for both normally aged and severely aged asphalt binders. 0 Dynamic mechanical analysis shows that the storage modulus increases less for asphalt that has been modified with SBS and SEBS polymers than for unmodified asphalt, after aging. This phenomena was observed for both normally aged and severely aged binders. It is theorized that the decrease in aging is a result of low molecular weight material entrapment through oil absorbtion and or physical hindrance. Future testing must be conducted to determine the cause of this phenomenon. 7. 3. 2 Eflect of elevated temperatures during processing Aging asphalt binders at elevated temperatures caused unexpected results when testing the final materials using infrared spectroscopy, dynamic mechanical analysis, gel permeation chromatography, and thermal mechanical analysis. It was theorized that materials aged at elevated temperatures would show similar trends with respect to the 158 above experiments as materials aged under normal conditions. This was not the case however. Figure 7.14 is a summary of the unanticipated results. The results can be explained by the introduction of a second aging process. This process is a degradation process that affects the resin type material found in asphalt. Figures 7.15 through 7.17 are a theoretical depiction of the aging phenomena being discussed. Future studies should be conducted to investigate this theory. 7.4 - Optimum and critical polymer contents The optimum and critical polymer contents for asphalt modification were defined based on rheological properties of asphalt/polymer blends. The optimum was defined as the point at which there was no longer a significant increase in the rheological properties with increasing polymer content. The critical content was defined as the polymer concentration where a deviation from the normal trend in the rheological properties is detected. The optimum and critical polymer contents were determined for the asphalt/polymer blends being studied in this project and are summarized in Table 7.1. These polymer contents are specific to the sources of both the polymers and asphalts. It is therefore suggested that the reported optimum contents be used only as a guide. It is strongly suggested that the dynamic shear rheometer be used to examine the relative increase in properties between the unmodified and modified material. Addition of the optimum polymer contents resulted in average increases of approximately 1500°/o for the 159 FTIR: CH2 (unaged) - CH: (normal aging temperature) < 932 (high aging temperature) CH3 CHJ CHJ Ci (unaged) = Cfl (high aging temperature) < E010“ aging temperature) CH3 - CH3 CH3 Cimnaged) = C:C(high aging temperature) < Cgcmormal aging temperature) CH2 CH2 CH2 EQ (unaged) < EEO (high aging temperature) < 932 (normal aging temperature) CH3 CH3 CH3 DMA: G' (unaged) < 0' (normal aging temperature) < 0' (high aging temperature) GPC : unaged MW < normal aging temerature MW = high aging temperature MW TMA: (softening point) unaged SP 5 high temperature aging SP < normal temperature aging SP - Figure 7. 14 - Elevated temperature aging data 160 5:25.33 #33:. 3M3... \e 8.32234 - u. ~ N 9.3%.... 161 8.3.32.3». .35.... ... 3...... 8.x... a...u............... £338.? 2.35.2.5 - e N N 9......- <2._. :5... .52. @338 .o 88.2.. Ugo :5... 3825.59 :29... 32 32.3 88.8.. Em?- UmO Ea... 3:92:88 :23: .52 :3; .0 8.8.2.. <20 Ea... 0.25.52: :0 .2... .0 .o 88.2.. 5?. =8... 2.2.2.93 5 522.825“. 9.2m 2.2.38 .2... 355.8 .0 38.2.. / O 162 82.3.33... 3...... u... .a 3...? 8%. 2.83.222... 538...? u................. - m ~ N 9.33% 2.82.85... 58. :. 2.28.6... 2!... 8.88 o. 0.... 23.8.... 2.2. 3.828 .c 88.2... 228.95..» 2...... o. 8... 25.8.... 2.2.2.2.. .0 .o 88.2.. 5.x. :5... 202.82... £8. E 22.2.838 9...... .29 .2... .. 5.... 88.2.. on... :5... 2...... 2222.22 .252. 8.. 2.25:8... 32 2:8 82.24. a .s :21 163 Table 7. I - Optimum and critical polymer contents of studied asphalt/polymer blends based on rheological properties Optimum Content Critical Content erc nt ot wei ht f h MW 01 r l n AC-S/SBS 3 or 5 4 AC-S/SEBS 2 or 5 3 - 4 AC-lO/SBS g 3 AC-lO/SEBS 2 or 4 3 SHRP original binder specification of (G‘lsin delta) at 60°C. The critical polymer contents resulted in increases as low as 300% for the same specification. It is therefore recommended that if the measured increase is less than 500%, more polymer should be added and the property remeasured to determine if there is any substantial benefit. The addition of the optimum polymer contents resulted in specification values of approximately 20 kPa. It should be noted that all of the tested samples (0-10 wt% polymer) met the SHRP original binder specification of (G’lsin delta). At this time, there is no information regarding the relation to pavement performance of the actual specification level and thus it can not be said whether the specification value needs to be increased. 1 64 7. 5 Fingerprinting protocol 7.5.1 Asphalt grades Asphalt grades are difficult to fingerprint. However, it is possible to characterize an asphalt based on viscosity, DMA, GPC, FTIR TMA, DSC, and BBR. It is the industry standard to grade an asphalt by using viscosity or penetration. This leads to inconsistencies. Two AC-S grade asphalts may have the same viscosity but be very difi‘erent chemically and thus show different performance properties. Viscosity, dynamic mechanical analysis, thermal mechanical analysis, and the bending beam rheometer are good methods of characterizing the physical properties of asphalts. Fourier transform infrared spectroscopy and gel permeation chromatography can be used to characterize the chemical structure of asphalts. GPC allows for the examination of the molecular weight distribution of an asphalt and FTIR allows for the examination of the chemical functional groups present in an asphalt. There are three distinct molecular weight ranges found in asphalt that can be monitored using GPC. Similarly, there are four distinct absorption wavelengths found in asphalt, that can also be monitored. 7. 5.2 Polymer modifiers SBS and SEBS polymer modifiers can be fingerprinted using GPC and FTIR technology. Every polymer will have a defining FTIR spectrum and a characteristic molecular weight range associated with it. Upon construction of a central library of spectra, polymer modifiers fiom specific companies will be easily identifiable. 1 65 7. 5. 3 Polymer modified asphalt SBS and SEBS polymer modified asphalts can be fingerprinted through the use of GPC, FTIR, and DMA in correlation with working libraries. GPC allows for the determination of the exact amount of polymer modifier added. It also gives molecular weight information about the base asphalt, polymer modifier, and the aging processes experienced by the blend. FTIR gives a chemical fingerprint to all constituents of a polymer/asphalt blend. Thus, it tags the polymer, asphalt grade, and any unusual aging that has occurred. FTIR can also be used to check the polymer content with the use of a calibration curve. DMA should be used as a final indicator of the blends performance over a wide temperature range. Materials will behave in characteristic ways with respect to rheological testing at difl‘erent temperatures. 7. 5. 4 Methodology The following series of steps can be used as a method of fingerprinting asphalt grades, polymer modifiers, and polymer modified asphalts. 1. Scan the sample using FTIR. o- Ratios of characteristic asphalt peaks determine the asphalt grade. :> Hard grade asphalts should show larger amounts of C=C (1600 cm“) bonding than soft grade asphalts. :> A large amount of the C=O (1700 cm") functional group indicates that the material has been aged. 0 A peak at 965 cm" indicates the possible presence of an SBS or SBR polymer. 166 :> A ratio of the 965" (polymer) peak to the 1375" (asphalt) peak can be used for the determination of the amount of polymer present in a sample using calibration curves. 2. Examine the sample using HP-GPC. o The areas of the three distinct regions under the chromatogram can be used for determining asphalt grade. :> Hard grade asphalts should show lager amounts of the high molecular weight material than sofi grade asphalts. :> The presence of excessive amounts of the high molecular weight constituent suggests that the sample has been aged. :> The presence of irregularities or sharp peaks in the low molecular weight region may suggest that the sample has been spiked with oil to meet a softer viscosity grade. 0 The presence of a high molecular weight peak greater than that of the asphalt suggests the presence of a polymer modifier. => The percent area under the polymer peak with respect to the entire chromatogram is the weight percent polymer in the binder. * SBR is a broad peak that can be detected using FTIR. * SBS is a sharp peak that can be detected using FTIR * SEBS is a sharp peak that can not be detected using FTIR. 1 67 0 Further fingerprinting can be accomplished through the use of an LC-transform unit. This system allows for the examination of the sample using FTIR after it has been separated by molecular weight using HP-GPC. 3. Test the sample using dynamic mechanical analysis. 0 Check the results against a calibration-like curve to insure that the conclusions drawn fi'om FTIR and HP-GPC analysis are correct. 7. 6 Specifications 7. 6.1 SHRP binder specification At this time it is felt that the SHRP binder specification is a step in the right direction. The reason for this support is because it is performance related, temperature dependent, and material independent. However, there are some suggestions to be considered about the specification. The specification can be found in Table 7 .232. The following discussion is a critique of the specification based on its subheadings. Performance Grade - This classification of asphalt performance is superior to the standard viscosity and penetration graded systems because it is a function of temperature. The performance grading system is based on the environments that an asphalt will encounter during its life. It should be noted that the high temperature classification is the maximum seven. day pavement temperature and the low temperature classification is the maximum seven day pavement temperature. It is felt that the binder classification should also be a filnction of 168 Table 7. 2 - SHRP performance graded asphalt binder specification i: _ .:.:.:.:_E .==..=¢. 25.3... “$5. .EJrArJF .5...— c 5.... =3, .7. 5:. :8: D . .._._. 2....an 3.2.3 9:15... M... .92....2 c. a 5.... :~ a M.» H... .r 1......— ...I .5. 5.. f... :33 9.... m 2.: 2 2....2 $.72. _. . _...x.=.;._. :17}. 5.5.9:... .: . c... b 93.55, 31...... 9 51:95.3; 1 69 the loading environment. Therefore, an asphalt grade may have to be increased for a harsh loading environment, such as standing traffic. 0 Flash Point Temperature - The flash point temperature is a safety specification placed on the original binder. The addition of polymer will not change this specification. The material must still not flash. All of the samples tested met the flash point temperature specification. 0 Viscosity - The viscosity of the original binder is a specification used to ensure that the material is easily processable in conventional equipment. A polymer modified material must be able to be handled at similar temperatures to those of unmodified asphalt. Again, all of the samples tested met the viscosity specification. Therefore, the SHRP viscosity specification of 3 Pa‘s at 135°C appears to be appropriate for polymer modified asphalt. - Dynamic Shear - The dynamic shear test of the original binder, thin film oven residue, and the pressure aging vessel residue are extremely important tests. They examine directly the visco-elastic nature of the binder material at three different times in an asphalts life. The tests are used as high ternperature, ‘ rutting and fatigue life predictors. Although the test itself is a good one, the actual specification value cannot be judged at this time without more experimental data. To date, all of the samples tested met these specifications. 0 Mass Loss - The mass loss after TFO aging is a safety and quality control specification. The addition of polymer will not change this specification. The 1 70 material must still not lose mass upon aging. All of the samples tested met the mass loss specification easily. Thin Film Oven Test - The thin film oven test simulates the aging that occurs during processing and the early life of and asphalt. Polymer modified asphalt is processed at a higher temperature (330 - 350°F) than that of unmodified asphalt (270 - 290°F). It would therefore suggest that the thin film oven test temperature should be raised to account for this difference. However, the thin film oven test is already run at 325°F. Also, above 350°F, it appears that a secondary high temperature aging reaction which degrades asphalt properties becomes dominant that will not be seen in the field. Experimental results have shown that the current test temperature best resembles the chemical characteristics of recovered samples from the field. A test temperature of 355°F has shown signs of the degradation aging process. The degradation aging process has not yet been seen in recovered samples. At this time, it is suggested that the current TFOT temperature is applicable to the polymer modified asphalts studied. However, this may not be the case for other polymers and mixing procedures. 3 It should be noted that asphalt in the field should not be elevated to high temperatures (>400°F) for long periods of time. Pressure Aging Vessel - The pressure aging vessel test simulates long term asphalt pavement aging. The addition of polymer to asphalt should not alter this test. However, no long term aged, recovered samples have been tested to verify the test itself. 171 o Creep Stiffness - The bending beam rheometer is used to measure the low temperature properties, and thus thermal cracking resistance, of asphalt binders. This specification is meant to be a function of temperature only and should be the same for any material used including polymer modified asphalt. The creep stimiess was effected more by asphalt grade than polymer content, and thus it is suggested that low temperature properties be controlled by changing to a softer asphalt grade. Also, the m-value (defined as the slope of the log stiffness versus log time curve at 60 seconds) specification did not appear to be affected by polymer content, but instead appeared to be affected by asphalt grade. At this time, there is not enough data to suggest absolute specification values with respect to pavement performance. It should be noted though, that the m-value has been found to be the defining low temperature specification. 0 Direct Tension - The tension test can not be used at this time because the facilities do not exist. The direct tension test simulates the cohesive strength of the asphalt binder at low temperatures. Some of the literature suggests that the . test is dependent on the type of polymer modification. At this time, a judgment can not be made concerning the direct tension test. It is also suggested that a separation test and an adhesion test be added to the specification. Chemical characterization tests such as FTIR and GPC would also be useful but require specialized research equipment and add analysis. FTIR and GPC tests could 172 be used once per job or in random testing. FTIR and GPC tests can also be used when problems arise concerning polymer content or type and asphalt quality. The addition of the optimum amount of SBS and SEBS polymers to AC-S and AC-10 grade asphalts will increase the high temperature SHRP specification by up to four grades. The low temperature specification is not affected by the addition of polymer. It is negatively affected, however, by one grade due to the mixing process required for polymer modification. This is further support for selecting an asphalt that is one or two grades softer than usual when using polymer modifiers. This procedure will result in the enhancement of both low and high temperature properties with respect to the original, unmodified binder. Figure 7.18 shows how SBS polymer modification affects the SHRP performance grade of an AC-S grade asphalt. Figure 7 . 19 shows the increase in the temperature range that the material can operate in as a function of increasing polymer content. 7. 6.2 WOT binder specification The MDOT polymer modified binder specification can be found in Table 7 .3. It is intended to show improvements in an asphalt’s physical properties due to modification with a polymer. It is suggested that the SHRP specification may be used in this same fashion by grading both the straight and modified asphalt binder. FTIR and GPC can be used in correlation with the MDOT binder specification to test for polymer content and, type and quality of an asphalt. 173 P $2.»... $253 mmhéaiwc “55% may V6 933% 3.65.5?3 5:3. .. 2 N 834.5 .0... 8382.th '7 mi—F 174 .42.»... $258 amass—Emu ~32» orb v.6 was: Ezfiaemfiu. 3.63% 3.8.5:.me “$2.4 - Q ~ N 33.43 . 3 I I'! -l. ‘%S '%V '%8 '%Z I I I I Q a lo.) umuadmt 0:100 -ii:.:;-; .--ul§ll-.sl:. ao- --i.-b i a: 1 75 Table 7.3 - MDO T polymer modified asphalt specification Testing and Acceptance . Separation of Polymer - a sample of the polymer modified aspnalt cement will be :ested for separation of the polymer (HTH 310-92). The seplrtthfl "St in" insure that the modifier and the asphalt cement blend do not pose a storage stability problem and that handling be the same as for conventional asphalt cement. Acceptable differences for top and bottom halves of test specimens shall not exceed: Z.5°C in softening point per ASTM 0 36-86 (reapproved). Testing will be done after 2 days of heating and 7 days of heating. The polymer modified shall be compatible with the reference asphalt such that the following properties are exhibited: Softening Point. °C Raise from Reference Asphalt. ASTM C 35. minimum ........... 8 Penetration at 25°C. 1009, 3 sec.. dml drop from Reference Asphalt. ASTM D 5. minimum . . . . 6 l Viscosity. Poises raise from Reference Asphalt. 60°C, minimum ................... 150 percent Penetration at 4°C. 2909, 60 sec.. dllll increase from Reference Asphalt ASTM D 5. minimum ....... 1 Elastic Recovery from 10 cm. 5 cm/min.. ZS'C. minimum .................... 40 percent Original penetration and viscosity test results on the daily sample of polymer modified asphalt cement shall meet the above specifications to show uniformity in the product being supplied througnout the urine“- The recovered penetration test results on the mixture sample must meet-the reouirements of Taole 4.00-3 of the 1990 Standard Specifications. for Construction. Chapter Eight Suggested Future Work The research that has been started in this study is only the beginning of polymer modified asphalt research. There is a limitless number of questions that have been left unanswered. Chapter Eight will suggest some possibilities of fiiture work based on the author's understanding of the subject. 8.1 Materials This study used only a small number of materials. It is believed that every asphalt grade and polymer type will behave differently when used in an asphalt pavement. It is therefore necessary to study a wide array of materials. Table 8.1 is a list of some suggested materials for future research. 8.2 Modeling The ultimate goal of modeling polymer modified asphalt pavements should be to be able to predict pavement performance based on the chemical composition of the pavement constituents. This goal should include all of the processing steps needed to produce a polymer modified asphalt pavement from its raw materials. It should be the 176 177 Table 8. 1 - Suggested materials for future research Polymers Fibers Asphalts SBR latex Elvaloy®AM Polyethylene Crumb rubber in the form of recycled tires Polyester fibers Cellulose fibers AC-2.5 grade asphalt AC-20 grade asphalt Penetration graded asphalt Different sources of asphalt Engineered asphalt Recycled asphalt 178 objective of this model to create a base on which sound engineering design of polymer modified asphalt pavements may begin. The suggested modeling approach can be divided into a hierarchy consisting of three levels. Each proceeding level should be able to use the previous models as input for the current model. The models should also be able to be used individually or in series depending on the level of information available to the user. As would be expected, the accuracy of the models, unfortunately, will most likely be reduced when used in series due to added assumptions implemented at each level. Figure 8.1 is a schematic representation of the suggested modeling hierarchy. 8. 2. 1 Level one modeling Level one modeling should consist of developing a physical picture of the studied asphalt/polymer blend. This model should be based on data gathered in the chemical analysis of straight and blended materials but will ultimately be based on theory and intuition. The models presented in this thesis can be used as level one modeling. 8. 2. 2 Level two modeling Level two modeling should consist of creating empirical models that will correlate chemical analysis data with physical property data of straight asphalts, polymer modifiers, and asphalt/polymer blends. The chemical analysis data may come in several forms including: high performance gel permeation chromatography, photo-diode array, liquid chromatography-transform, Fourier transform infrared spectrosc0py, and differential scanning calorimetry data. The physical property data should include: rheological, direct 179 a 'Il'll’ Ill. Gaze—yo: 02...... .25.. "IE u'tIII-Ill.l .e-llil 2282 22m 882.. .81.... .306qu $5.38... ESE» .u..3£u