I ‘ LIBRARY 2 002* Michigan State University This is to certify that the thesis entitled EXPERIMENTS FOR CLIMATE ZONE IV HYPOTHESIS presented by XIN Ll has been accepted towards fulfillment of the requirements for the MS. degree in PACKAGING MM 9. Jam/1% Mfibr Prpfessor’s Signature Sag] 4153 Q 1; £007 Date MSU is an affinnative-action, equal-opportunity employer - -.-.-.-.-.-.-.-.- -n-a-s-IQr-Iq-IIQ-J'Q PLACE IN RETURN BOX to remove this checkout from your record. TO AVOID FINES return on or before date due. MAY BE RECALLED with earlier due date if requested. DAIEDUE DATEDUE DAIEDUE 6/07 p:lClRC/DaleDue.mdd-p.1 EXPERIMENTS FOR CLIMATE ZONE 1v HYPOTHESIS By Xin Li ATHESIS Submitted to Michigan State University in partial fulfillment of the requirements for the degree of MASTER OF SCIENCE Department of Packaging 2007 ABSTRACT Experiments for Climate Zone IV Hypothesis By Xin Li Stability tests are required for all drug products. The purpose of the stability test is to find the shelf life of the products; the test should be performed under the climatic conditions of the destination marketplace. In order to make the test widely applicable, the world is divided into four climate zones with different test conditions specific to each zone. Climate Zone IV represents the hot and humid zone. The conditions 30°C/65°/o RH were specified by WHO (World Health Organization) as the test condition for this area. However, the Association of Southeast Asian Nations (ASEAN) proposed to WHO in 2004 to change this condition to 30°C/7 5% because of the severe environmental condition of ASEAN countries (27°C/79%). Based on a theoretical calculation, 30°C/65°/o RH could be used as the stability test condition for ASEAN’s countries.'The purpose of this study was to support the result of theoretical calculation using experimental data. HDPE bottle, one of the most popular packages for pharmaceutical products, was selected as the test sample. The WVTR for the bottles was determined under 5 different conditions, 30°C/59.6°/o RH, 30°C/60.9% RH, 30°C/64.5% RH, 30°C/74.5% RH and 27°C/79°/o RH, using a gravimetric method. More water vapor permeated into the bottle at 30°C/65°/o RH than it did at 27°C/79% RH. This result supports the theoretical calculation. ACKNOWLEDGEMENTS There are many people to thank for their contributions toward the completion of my master degree during my time at MSU. First, I want to thank my advisor, Dr. Hugh E. Lockhart, for his support and guidance. I also want to express my thanks to Dr Dennis Gilliland and Dr Maria Rubino who serve on my committee. Thanks to my friends for their support and friendship. To my parents, parents-in- law, and brother, thanks for the encouragements and the sacrifices they have made. Most importantly, I would like to express my deepest gratitude to my husband, Hui, for all of the love and support she has given me over the years. I would not have been able to accomplish any of these without you. iii TABLE OF CONTENTS LIST OF TABLES ................................................... _ .............................. v LIST OF FIGURES ............................................................................... vi Chapter 1. Introduction ............................................... ' ......................... 1 Chapter 2. Literature Review ................................................................ 4 Chapter 3. Materials and Methods ........................................................ 27 Chapter 4. Results and Discussion ....................................................... 33 Chapter 5. Conclusion ........................................................................ 54 References ......................................................................................... 55 iv Table 1.1. Table 2.1. Table 3.1. Table 3.2. Table 3.3. Table 3.4. Table 4.1. Table 4.2. LIST OF TABLES Definitions and stability test conditions of climatic zones .............. 2 Definitions, criteria and stability test conditions of climatic zones...8 Thickness of the bottle walls ................................................. 28 Crystallinity of the bottles ....................... » .............................. 28 Salt solutions used to provide specified RH for bottle test ........... 29 The balances used in the test for the bottles ............................ 31 WVTR value for each bottle .......................... i ........................ 4 1 t-test for WVTR values gotten from 30°C/64.5%RH and 27°C/79%RH ..................................................................... 45 Figure 2.1. Figure 2.2. Figure 3.1. Figure 4.1. Figure 4.2. Figure 4.3. Figure 4.4. Figure 4.5. Figure 4.6. Figure 4.7. Figure 4.8. Figure 4.9. Figure 4.10. LIST OF FIGURES Schematic drawing of ASTM E 96 test method: Desiccant Method and Water Method .............................................................. 21 Schematic drawing of ASTM 1249 test method ........................ 22 Schematic drawing of exposure bucket for WVTR test of bottles .............................................................................. 31 The temperatures recorded during the test of the bottles .............................................................................. 33 The RH recorded during the test of the bottles .......................... 34 The weight gains of the bottles stored at condition 30°C/59.6%RH from day 0 to day 63 ........................................................... 36 The weight gains of the bottles stored at condition 30°C/59. 6%RH from day 64 to day 119 ....................................................... 36 The weight gains of the bottles stored at condition 30°C/60.9%RH from day 0 to day 63 ........................................................... 37 The weight gains of the bottles stored at condition 30°C/60.9%RH from day 64 to day 119 ........................................................ 37 The weight gains of the bottles stored at condition 30°C/64.5%RH from day 0 to day 63 ........................................................... 38 The weight gains of the bottles stored at condition 30°C/64.5%RH from day 64 to day 119 ........................................................ 38 The weight gains of the bottles stored at condition 30°C/74.5%RH from day 0 to day 63 ........................................................... 39 The weight gains of the bottles stored at condition 30°C/74.5%RH from day 64 to day 119 ........................................................ 39 vi Figure 4.11. Figure 4.12. Figure 4.13. Figure 4.14. Figure 4.15. Figure 4.16. Figure 4.17. Figure 4.18. Figure 4.19. Figure 4.20. Figure 4.21. Figure 4.22 Figure 4.23 Figure 4.24 Figure 4.25 The weight gains of the bottles stored at condition 27°C/79%RH from day 0 to day 63 ........................................................... 40 The weight gains of the bottles stored at condition 27°C/79%RH from day 64 to day 119 ........................................................ 4O Scatter plot of WVTR from two different periods ........................ 43 Comparison of all the WVTR values of the bottles (day 0 ~ day 63) .................................................................................. 44 Comparison of all the WVTR values of thebottles (day 64 ~ day ' 119) ................................................................................. 44 The weight gains of the control bottles stored in condition 30°C/59.6%RH from day 0 to day 63 ...................................... 47 The weight gains of the control bottles stored in condition 30°C/59.6%RH from day 64 to day 119 ................................... 47 The weight gains of the control bottles stored in condition 30°C/60.9%RH from day 0 to day 63 ...................................... 48 The weight gains of the control bottles stored in condition 30°C/60.9%RH from day 64 to day 119 ................................... 48 The weight gains of the control bottles stored in condition 30°C/64.5%RH from day 0 to day 63 ...................................... 49 The weight gains of the control bottles stored in condition 30°C/64.5%RH from day 64 to day 119.... .............................. 49 The weight gains of the control bottles stored in condition 30°C/74.5%RH from day 0 to day 63 ...................................... 50 The weight gains of the control bottles stored in condition 30°C/74.5%RH from day 64 to day119...........' ........................ 50 The weight gains of the control bottles stored in condition 27°C/79°/oRH from day 0 to day 63 ......................................... 51 The weight gains of the control bottles stored in condition 27°C/79%RH from day 64 to day 119 ..................................... 51 vii Chapter 1. Introduction In United States Pharmacopeia, “stability is defined as the extent to which a product retains, within specified limits, and throughout its period of storage and use (i.e., its shelf life), the same properties and characteristics that it possessed at the time of its manufacture.” There are generally five types of stability: chemical, physical, microbiological, therapeutic and toxicological. These five factors are evaluated through stability testing (USP 1 2004). The purpose of stability testing is to determine proper storage conditions and expiration dates of an active substance or pharmaceutical product. It is required by United States food and drug regulations for all drug products. In the regulation for Current Good Manufacturing Practice of Finished Pharmaceuticals, at 21CFR 211.166, the Food and Drug Administration (FDA) says: "There shall be a written testing program designed to assess the stability characteristics of drug products. “ The stability of finished pharmaceutical products depends on several factors. Basically, those factors can be divided into two parts: one is environmental factors, such as ambient temperature, humidity and light; the other is product related factors, such as chemical and physical properties of the active substance, excipients, dosage form, manufacturing process, container closure system and packaging material (WHO, 1). The shelf life should be established based on the climatic conditions of the destination marketplace. Since the result of stability testing is affected by the environmental conditions, different testing conditions are adopted for different areas. In order to be able to reduce the amount of stability testing, the number of different long term testing conditions must be reduced to a sufficient extent. Based on the proposals to World Health Organization (Schumacher, 1972; Grimm, 1986 and Grimm, 1998), the world is divided into four different climatic zones (CZ), and different testing conditions are used for each of them. Table 1.1 Definitions and stability test conditions of climatic zones (WHO 1) CZ Definition Long term testing conditions I Temperate climate 21°C/45% RH II Subtropical and Mediterranean 25°C/60% RH climate III Hot and dry climate 30°C/35% RH IV Hot an humid climate 30°C/65% RH At the “Consultation to Discuss Stability Studies in a Global Environment” on 13- 14 December 2004 at WHO Headquarters in Geneva, the Association of South East Asian Nations (ASEAN) proposed to WHO to change the stability testing condition for Climate Zone IV from 30°C/65% RH to 30°C/75% RH. Three recommendation were made after the meeting: A) revert to 30°C/70% RH as the long-term stability testing condition for Zone IV; 8) change to 30°C/75% RH as the long-temI stability testing condition for Zone IV; C) add a new Climate Zone IVb to accommodate hot and very humid areas (30°C/7 5%), and keep the current Zone IV as Climate Zone IVa (WHO, 2). This proposal was made just based on the ASEAN climate zone average condition which is 27°C, 79% RH. The effect of barrier packaging on control of the humidity inside the package was not considered. Actually, it is the storage temperature, partial pressure for water vapor and moisture permeability of the package that affect the result of stability testing. Based on the theoretical calculation (Lockhart, 2006), the current Climate Zone IV stability condition 30°C/65°/o RH should be adequate to represent the ASEAN average condition 27°C/79°/o RH. The hypothesis was made: the stability test condition 30°C/65% RH should be severe enough to represent the ASEAN average condition 27°C/79%. This theoretical conclusion needs to be tested by direct experimentation. The objective of this research was: Use HDPE bottles as test samples to demonstrate that the stability test condition 30°C/65% RH should be severe enough to represent the ASEAN average condition 27°C/79%. Chapter 2. Literature Review Association of South East Asian Nations ASEAN was founded on 8 August 1967 in Bangkok. The original member countries included: Indonesia, Malaysia, Philippines, Singapore, and Thailand. The ASEAN Declaration was made on the same day by all the members. It states that the aims and purposes of the Association are: “(1) to accelerate economic growth, social progress and cultural development in the region, (2)'to promote regional peace and stability through abiding respect for justice and the rule of law in the relationship among countries in the region and adherence to the principles of the United Nations Charter" (ASEAN, 1). As the development of the ASEAN continued and the collaboration increased, Brunei Darussalam, Vietnam, Lao People’s Democratic Republic, Myanmar and Cambodia joined the ASEAN later. Now, the ASEAN region has a population of about 500 million, a total area of 4.5 million square kilometers, a combined gross domestic product of almost US$ 700 billion, and a total trade of about US$ 850 billion. In order to facilitate and liberalize trade and investment in the region, ASEAN Consultative Committee for Standards and Quality (ACCSQ) was set up in 1992. The purpose of the organization is to facilitate and liberalize trade and investment in the region. It has endeavored to harmonize national standards with international standards and implement mutual recognition arrangements on conformity assessment to achieve its end—goal of “One Standard, One Test, Accepted Everywhere”. All Member Countries have accomplished the harmonization of standards for 20 priority products and 81 standards for Safety and Electromagnetic Compatibility (EMC). New areas for harmonization are currently being identified. Priority for harmonization will be given to those standards used in technical regulations in Member Countries (ASEAN 2). At the 13th Meeting of the ACCSQ held in March 1999 in Manila, the members agreed to set up a Pharmaceutical Product Working Group (PPWG), with Malaysia as the lead country. Accordingly, ACCSQ-PPWG was launched in September 1999 in Kuala Lumpur, Malaysia. The objective of the ACCSQ-PPWG is to develop harmonization schemes of pharmaceuticals' regulations of the ASEAN member countries to complement and facilitate the objective of ASEAN Free Trade Area (AFTA), particularly the elimination of technical barriers to trade posed by these regulations, without compromising on drug quality, safety and efficacy (ASEAN 3). Stability Testing “The purpose of stability testing is to provide evidence on how the quality of a drug substance or drug product varies with time under the influence of a variety of environmental factors, such as temperature, humidity, and light, and to establish a retest period for the drug substance or a shelf life for the drug product and recommended storage conditions” (WHO, 1). In the stability testing, the marketed container-closure systems for the products must be involved. Therefore, the environment that the products are exposed to may not be as severe as the storage environment because of the protection of the package. This is especially true when a barrier package limits the ingress of water in vapor form. Stability testing should be performed for both drug substances and drug products. In manufacturing, the stability of the drug substance should be decided at first. And based on the information of the behavior and properties of the active substance, stability test for drug product is performed. Generally, at least three primary batches of product should be used in the stability study, and the product should be packaged in the container closure system that is the same as the packaging proposed for storage and distribution. The testing should cover the physical, chemical, biological, and microbiological attributes, preservative content and functionality test. About the storage condition used in the testing, generally, a drug product should be evaluated under storage condition that test its thermal stability and, if applicable, its sensitivity to moisture or potential for solvent loss. The storage conditions and the lengths of studies chosen should be sufficient to cover storage, shipment, and subsequent use (WHO 1). Based on the results from the stability testing, a storage statement should be established for the labeling. Specific instructions should be provided if applicable. An expiration date should be displayed on the container label. Climate Zone (CZ) The shelf life should be established with regard to the environmental condition in which the product is to be marketed. For certain preparations, the shelf life can be guaranteed only if specific storage instructions are complied with. So, different testing conditions are supposed to be used for different climate zones. In order to reduce the amount of stability testing required, the number of different long term testing conditions must be reduced to a sufficient extent. Therefore, the concept of climate zone was proposed by Schumacher (Schumacher, 1972). In the proposal, the world was divided into four zones based on the temperature and humidity, and the storage conditions for stability testing were recommended for each zone. The mean annual temperature and the mean annual partial pressure of water vapor are the main criteria used for the Inclusion of a region in a particular set of climatic conditions (Bott, 2007). The mean annual partial pressure of water vapor can be calculated using equation (1) P = P" x RH (1) Where P is the partial water vapor pressure in the environment, P' is the saturated water vapor pressure at the same temperature and RH is relative humidity of the environment. Table 2.1 Definitions, criteria and stability test conditions of climatic zones CZ Definition Criteria Long term Mean annual testing temperature in open air/ conditions mean annual partial water vapor pressure I Temperate climate s 15°C I s11hPa' 21°C/45% RH II Subtropical and >15 to 22°C / > 11 to 18 25°C/60% RH Mediterranean climate hPa I” Hot and dry climate > 22°C / s15hPa 30°C/35% RH IV Hot an humid climate > 22°C / >15hPa 30°C/70% RH * 1 hPa = 0.75 mmHg This concept is described in WHO’s regulatory standards (WHO, 1996) and The United States Pharmacopeia and became an established standard in developing pharmaceutical products. In fact, the storage conditions for the stability testing in a region are determined based on the mean kinetic temperature (MKT) and the average of the relative humidity. The MKT is a single calculated temperature at which the total amount of degradation over a particular period is equal to the sum of the individual degradations that would occur at various cycles of higher and lower temperature (WHO, 2004). It expresses the cumulative thermal stress undergone by a product at varying temperatures during storage and distribution. It can also be considered as an isothermal storage temperature that simulates the non-isothermal effects of storage temperature variations. The temperature dependence for the degradation of drug products is based on principles of chemical kinetics, especially the Arrhenius equation. The relationship between the reaction rate constant and the temperature can be expressed as (PMA’s, 1991 ): AE where K is the degradation rate, A is a constant dependent on the molecule of interest, AE is the activation energy. R is the universal gas constant and T is the absolute temperature. Based on Equation 2, MKT can be calculated (Bailey,1993): T _ — AE/R MKT '- _AE/RT, 45/er —AE/RT.. (3) lnie + e + + e ] n Where TMKT is MKT, n is the number of temperatures collected and T is absolute temperature. AE is generally considered as 20 kcal/mol, since the activation energies of most reactions of organic molecules are about 20 kcal/mol. Using Equation 3, the temperature of stability testing for each climate zone can be obtained. Relative humidity can be calculated based on Equation 1. But the relative humidity specified for the stability testing for each climate zone was selected based on the average condition of each zone. And there are not generally accepted methods to build a relationship between RH and time or temperature. That’s also why the argument about stability testing condition always focuses on the relative humidity. Argument about Stability Testing Condition for Zone IV Climate Zone IV represents a hot and humid climate. It corresponds to central Africa and south Pacific, such as Zaire, Kenya, Indonesia, and Philippines etc. The stability testing condition for Zone IV has always been in dispute since the beginning of the concept. Testing at 30°C/70% RH used to be the condition used in industry, and it was also recommended by WHO In 1996. In 2000, WHO changed the testing condition from 30°C/70% RH to 30°C/60% RH based on a suggestion from the International Conference on Harmonization (ICH) Q1 Stability Expert Working Group. But, African countries objected to it later. They believed the condition could not represent the high humidity of some coastal African countries. After a series of meetings, in 2001, WHO made the final decision: they changed the condition from 30°C/70% RH to 30°C/65%. Consequently, ICH Stability Guideline 01F recommended the same condition (Singh, 2006). In Dec. 2004, ASEAN proposed to WHO to change the stability testing condition for 10 Climate Zone N from 30°C/65% RH to 30°C/75% RH because the average environmental condition for ASEAN countries is 27°C/79% RH. After gathering the responses from manufacturers and regulators, in Oct. 2005, the 40th WHO Expert Committee on Specifications for Pharmaceutical Preparations decided to split the current Climatic Zone IV (hot and humid countries) into CZ IVA, for which 30°C/65% RH will remain the standard long-term testing condition, and CZ IVB, for which 30°C/75% RH will become the testing condition (WHO 2). The Expert Committee also agreed that each individual Member State within the former Zone IV would need to indicate which of these conditions (Zone lVa or lVb) would be applicable in its territory. Moisture Permeation Mechanism of Container-Closure System A container-closure system can be classified as either permeable or impermeable system. Generally, most of those packages used in pharmaceutical industry are permeable. Only flame-sealed glass ampuls and aluminum blisters can be considered impermeable systems. Commonly used moisture permeable container-closure systems in pharmaceutical industry are: high—density polyethylene (HDPE) containers with any metal or plastic screw closures, low- density polyethylene (LDPE) containers with any metal or plastic screw closures, glass containers with any metal or plastic closure, polyvinyl chloride (PVC) blisters with lidding, PVC/polyvinylidene chloride (PVdC) blisters with lidding, and PVC/Aclar (polychIorotrifluoroethylene) blister with lidding. Aluminum blisters are 11 a special case. The permeation rate is so low that it is difficult to measure with current methods, but there is permeation. For the glass container-closure system, moisture permeates into the container mainly through the cap liner which is part of the closure and is used as a moisture seal. The permeability of glass itself is considered zero. For plastic containers, most of them are semi-crystallized materials. So, permeation is the result of ingress of water vapor through the wall of the container and the ingress of water vapor through the liner in the cap. If a hermetic wax seal is made for the closure, the permeation of the bottle alone can be measured. For aluminum blisters, a very low rate of ingress can occur through the seal between the backing and the blister. Theory of Permeation This discussion of theory is taken from course pack of School of Packaging, Michigan State University, for class PKG 815. (Rubino, 2005). Permeability is a measure of how easily a permeant compound transports through a solid medium. The permeation process takes place when a permeable wall separates two fluid phases (air or liquid) having different concentration values in each phase. For water vapor, there are two mechanisms of permeation: 1) convective mass transfer through channels, 2) diffusion-controlled molecular exchange through semi-permeable materials such as plastic. The first 12 mechanism is generally not taken into account for the permeation of the moisture into a package used for pharmaceutical product. This is because it only happens when the packages have significant defects like pinholes or cracks. Diffusion- controlled permeation can be described as a three-step event: 1) the permeant molecule from the contacting fluid phase permeates the polymer surface, 2) the permeant diffuses within the polymer material, 3) the diffused permeant desorbs from the polymer interface into the adjacent continuous phase which has low concentration. The fundamental driving force that prompts a molecular specie to transfer within the polymer, or between a polymer and a surrounding phase is, according to the solution theory, the tendency to equilibrate the species’ chemical potential across the thickness of the polymer. Fick’s laws of diffusion can be used to describe the permeation process in packaging systems. It includes two parts. The first Fick’s law is used for steady state diffusion. It describes the rate of transfer of diffusing substance through unit area of a section as being propotional to the concentration gradient aclax. the equilibrium unidirectional diffusion along the x-axis can be expressed as, F = -—D x a (4) where F is the rate of transfer of diffusing substance per unit of area, c is the permeant concentration, x is the spatial coordinate in the direction of transfer, and D is the molecular diffusion coefficient which is assumed to be independent of penetrant concentration. 13 Fick’s second law is used to describe non-steady state, one-dimensional diffusion in an isotropic phase. It can be described as, 2 6_C=Dx6c at 6x2 (5) where t is time. In order to use the previous two equations efficiently, the concentration of the penetrant both in the packaging material phase and in the contacting fluid phase must be known. Henry’s law can be used to calculate the concentration: C = Sp (6) Where 0 is the concentration of the diffusing substance in the solid or liquid phase, S is the Henry’s law constant, which is the solubility coefficient, and p is partial pressure of permeant at the contacting phase interface. Henry’s law only applies for the non-interactive permeant/polymer system. Based on equations (4), (5), (6), and assuming that the D and S are independent of concentration, which is true for water vapor permeating through polymers that do not strongly interact with water, the following equation can be obtained: P = DS = ql (7) AtAp Where P is the permeability coefficient, D is the diffusion coefficient which describes how fast the permeant molecules move through the material, S is the 14 solubility coefficient which describes how many permeant molecules are absorbed by the material, q is the amount of permeant transferred through the material during time t, A is the area available for permeation, I is the thickness of the material being permeated, and Ap is the difference in partial pressure of the permeating substance in the gas phase in contact with the two surfaces of the material. Equation (7) is valid for both steady-state transfer and nonsteady-state transfer. If the mass transfer is not at steady state, the permeability coefficient can be calculated for different time t and integrated over time. When water vapor is permeating into a package that is maintained at a constant temperature and relative humidity and the package contains a desiccant, steady state permeation can be assumed because the RH inside the package is maintained at a low level (around zero) by the desiccant. The time to reach steady state depends on the thickness of the material, its initial condition, and its barrier characteristics but generally is short in relation to desired shelf life. If one of the three conditions is not met (constant temperature, RH and desiccant inside package), steady state cannot be assumed. When water vapor is permeating into a package that is maintained at a constant temperature and relative humidity but contains a product other than desiccant, the water vapor partial pressure inside the package changes with time. In such cases, the moisture sorption isotherm for the product can be used to relate the moisture content of the product to the 15 partial pressure inside the package. It can also tell a great deal about the physical nature of the association between water and product. This assumes that moisture in the product and the package headspace equilibrate relatively rapidly in comparison to the rate of transfer of moisture through the package and that chemical consumption of water is negligible. When the permeability coefficient of a package is calculated, generally equation (8) is used: q p = tAp (8) In the equation, P represents the permeability coefficient of the whole package for the specific package because the thickness of the package wall varies for different areas. Equation (6) still can be used for differential areas of the material and can be integrated over the entire area. As a practical matter this is a tedious process. For this reason, permeation for a package is usually measured on a per package basis. Water Vapor Transmission Rate (WVTR) is another parameter to evaluate the moisture barrier of a specific material. It is the amount of water vapor that permeates per unit time through a film or a package at specified conditions of temperature and relative humidity. Values are generally expressed in g/100 in2/day for film, or g/package/day for package. For permeation of barrier packages for drugs, it is accepted practice to calculate and report WVTR in 16 mg/day/package. Sometimes it is also useful to report the permeation of water vapor into a package on the basis of unit partial pressure differential. This is called permeance. The relationship between WVTR and permeance for a specific film or package can be expressed using equation (9). WVTR P = (9) A p Where P is the permeance of the package or material, Ap is the difference in water vapor partial pressure on the two sides of the material, and the WVTR is the water vapor transmission rate for a whole package. Factors Affecting the Permeability This discussion is taken from course pack of School of Packaging, Michigan State University, for class PKG 815 (Rubino, 2005). Chemical structure The chemical structure of material of package and permeant is the primary factor in determining the permeability. The basic rule for each pair of material/permeant is “like dissolves like”. For example, a polar material can be more or less hydrophilic. And the permeability can be changed because of the presence of water. Similarly, non-polar materials are not affected by the presence of water. HDPE and LDPE are used as good water vapor barrier because there is no polar group in the structures, so they are non-polar. 17 Crystallinity and Orientation Crytallinity of the material can affect the permeability. Generally, permeation occurs in the amorphous regions. Therefore, increasing the crystallinity will decrease permeability. Orientation itself does not increase crystallinity. But after orientation, molecules are packed tightly; free volumes inside the structure are decreased. Therefore, permeability is decreased. Temperature Based on equation (7), the permeability coefficient is the product of diffusion and sorption coefficients. Both of the two coefficients are affected by temperature. The diffusion coefficient follows the Arrhenius relationship: -Ed D=D0xeRT (1o) Where Do is a constant, Ed is the activation energy of diffusion which is usually a linear function of temperature. R and T stand for the universal gas constant and absolute temperature, respectively (Van Krevelen, 1997). Generally, the diffusion coefficient increases with temperature for both gases and vapors. For sorption coefficient, the temperature dependence of the solubility coefficient over relatively small ranges of temperature can also be expressed by an Arrhenius-type relation (Van Krevelen, 1997), —AHS S = SO xe RT (11) 18 Where So is a constant, AHs is the heat consumed by dissolving a mole of permeant in the polymer. For volatile substances, it is common for solubility to decreases as temperature increases, but for solids and liquids, solubility generally increases as temperature increases. Generally, over reasonably small temperature ranges, the change in permeability coefficient is given by the following equation (Van Krevelen, 1997), —Ea P = P0 X 6 RT (12) Where E, is the activation energy. R is the gas constant, P0 is a pre-exponential term and T is temperature in degree Kelvin. Since P0 is a constant, we can rewrite the equation as: aaa, R T T Bzfixe '2 am And this equation can be used to calculate the permeability P2 at temperature at T2 when the permeability P1 at temperature T1 is known. Measuring Permeability Many experimental techniques have been developed for measuring the permeability of gases and vapors through polymeric materials. Some techniques have been adapted as standard methods but many of them have remained non- standardized procedures and are used for development and research purposes. 19 Most techniques for measuring permeability share a number of basic elements: permeant source, permeation unit (cell or device to support the test sample), permeant detector and temperature controlled environment. These techniques can be grouped in one of the three basic methods based on the way the permeated compound is collected: pressure-variable, volume-variable, and isostatic or isobatic. When a pressure-variable method is used, a two-chamber cell is separated by the test film. The high-pressure chamber is filled with the permeant at relatively high pressure and the permeated gas diffuses to the other side of the film. The permeant is collected in a constant volume chamber, and the pressure increase in the low-pressure chamber is measured by a pressure gauge as a function of time. This method was used to measure the water vapor permeability through packaging polymer (Doty, 1946). The volume-variable method is also uses a two-chamber cell separated by the test film. But the permeant is allowed to expand against a constant atmospheric pressure. And the change in volume as a function of time is measured in a capillary tube by displacement of a liquid. This method offers some advantages over the pressure-variable by the fact that the test proceeds under constant pressure differential and during the steady state the gas transmission rate, measured as change in volume, is also constant with time. 20 In the isostatic method, the partial pressure differential across the test film for permeating gas remains constant during the total permeation process. While the high pressure side remains constant at a certain value, the low pressure side is maintained in most cases, at zero partial pressure by either sweeping a gas stream or using a trapping agent. The isostatic technique itself can be divided into continuous flow method, cup method, and dish method. It is one of the most popular techniques used to test the permeability of water vapor. Two test methods described in ASTM International standards for water vapor transmission are set up based on the isostatic technique. One is ASTM E 96 — Standard Test Methods for Water Vapor Transmission of Materials. The other is ASTM F 1249 - Standard Test Method for Water Vapor Transmission Rate through Plastic Film and Sheeting Using a Modulated Infrared Sensor, using continuous technique. ASTM E 96 includes two basic methods, the Desiccant Method and the Water Method. Testing is performed by sealing a specimen to the open mouth of a test dish containing either desiccant or water and placing the assembly into a controlled atmosphere. The test unit is weighed periodically and the weight is plotted as a function of time. Water vapor transmission is taken as the slope of the curve (in the linear region) divided by the area of the dish opening (ASTM E 96) 21 Test specimen Controlled Test atmosphere specimen —" Controlled atmosphere Desiccant Water Figure 2.1 Schematic drawing of ASTM E 96 test method: Desiccant Method and Water Method In the method of ASTM F 1249, the test specimen is held such that it separates two sides of a test chamber. The "wet side” of the specimen is exposed to a high relative humidity atmosphere, while the "dry side" is subjected to a zero relative humidity atmosphere. Infrared sensors on the "dry side" detect the amount of water vapor present. Testing is complete when the concentration of water vapor in the dry side atmosphere is constant (ASTM F 1249). SQIISOI' Figure 2.2 Schematic drawing of ASTM 1249 test method 22 For packages used for drug products, the United States Pharmacopeia (USP) also provides the guidelines for a water vapor permeation test. They are contained in USP <671> - Permeation. There are two sections in USP Chapter <671>. One is Multiple-Unit Containers for Capsules and Tablets, which describes the test applied to multiple-unit containers. The other is Single-Unit Containers and Unit-Dose Containers for Capsules and Tablets, which describes the test applied to single-unit and unit-dose containers. In this chapter, it is specified that the term “container’ refers to the entire container-closure system comprising, usually, the container itself, the cap and the cap liner in the case of multiple-unit containers (bottles). In the case of single-unit and unit-dose containers (blisters or pouches), the container is the Iidding sealed to the blisters or a sealed pouch. The method described in USP is similar to the Desiccant Method in ASTM E 96. For its application in USP, it provides a means for classifying containers as tight, or well-closed with respect to water vapor transmission. Multiple-Unit Containers for Capsules and Tablets (USP 2, 2004) 12 containers (bottle and cap) are used to perform the test. 10 of the bottles, designated test containers, are filled with desiccant. Then, the screw — capped containers are closed with adequate torque and stored at 75 :I: 3% relative humidity and a temperature of 23 :I: 2°C for 336 :1 hours (14 days). The other 2 bottles, designated controls, are filled with glass beads and stored in the same condition for 14 days. The weight of the glass beads is similar to the weight of the 23 desiccant. The bottles are weighed before and after the storage. The rate of moisture permeability is calculated using equation 14. 1 OOO WX[(Tr‘TI)’(Cf—Cl)i (14) in which V is the volume, in mL, of the container, (Tf — Ti) is the difference, in mg, between the final and initial weights of each test container, and (Cf - Ci) is the difference, in mg, between the average final and average initial weights of the 2 controls. Based on the calculation result, the containers are labeled as either tight containers or well-closed containers. For the tight containers, no more than 1 of the 10 test containers exceeds 100 mg per day per liter in moisture permeability, and none exceeds 200 mg per day per litter. For the well-closed containers, no more than 1 of the 10 test containers exceeds 2000 mg per day per liter in moisture permeability, and none exceeds 3000 mg per day per litter. Single-Unit Containers and Unit-Dose Containers for Capsules and Tablets (USP 2 2004) There are two test methods described in the section. Method l 10 unit-dose containers with 1 pellet desiccant in each are designated as test containers. 10 empty unit-dose containers are used to provide the controls. All the containers are stored at 75 :I: 3% relative humidity and at a temperature of 23 :t 2°C. Weigh all the containers every 24 hours. After weighing, the containers are returned to the chamber. And the rate of moisture permeation of each container is calculated using equation 15. 24 TL-XKWf-WI-i-(CI-Ciii (15) in which N is the number of days expired in the test period; (Wf — W) is the difference, in mg, between the final and initial weights of each test container, and (Cf - Ci) is the difference, in mg, between the average final and average initial weights of the controls. Method 2 This method is used for packs that incorporate a number of separately sealed unit-dose containers or blisters. Four or more packs and a total of not less than 10 unit-dose containers or blisters filled with 1 desiccant pellet in each unit are used as test containers. The same amounts of empty packs are used as the controls. All the containers are stored at 75 :I: 3% relative humidity and at a temperature of 23 1: 2°C. Weigh all the containers every 24 hours. After weighing, the containers are returned to the chamber. And the rate of moisture permeation of each container is calculated using equation 16. figXKWI-WII- (Cf-0.11 (16) in which N is the number of days expired in the test period; X is the number of separately sealed unit per pack; (WI - W.) is the difference, in mg, between the final and initial weights of each test container, and (Cf — Ci) is the difference, in mg, between the average final and average initial weights of the controls. For the two methods, the containers are classified as Class A, Class B, Class C or Class D according to the calculation result in both of the two methods. In method I, the individual unit-dose containers are designated Class A if not more 25 than 1 of 10 containers tested exceeds 0.5 mg per day in moisture permeation rate and none exceeds 1 mg per day; they are designated Class B if not more than 1 of 10 containers tested exceeds 5 mg per day in moisture permeation rate and none exceeds 10 mg per day; they are designated Class C if not more than 1 of 10 containers tested exceeds 20 mg per day and none exceeds 40 mg per day, and they are designated Class D if the containers tested meet none of the requirements above. In method II, the packs are designed Class A if no pack tested exceeds 0.5 mg per day in average blister moisture permeation rate; they are designed Class B if no pack tested exceeds 5 mg per day in average blister moisture permeation rate; they are designed Class C if no pack tested exceeds 20 mg per day in average blister moisture permeation rate; and they are designed Class D if the packs tested meet none of the above average blister moisture permeation rate. For both of the methods, the test intervals are determined based on the classification: 24 hours for Class D; 48 hours for Class C; 7 days for Class B; and not less than 28 days for Class A. 26 Chapter 3. Materials and Method 3.1 Materials and Test Conditions 3.1.1 Material Plastic bottle is one the most popular packages used in the pharmaceutical industry. It can provide enough protection for many drugs although it is permeable. High-density polyethylene (HDPE) bottle was used as the package which the WVTR would be tested at five different conditions. The bottles were provided by Eli Lilly and Company. For each bottle, the overall capacity is 50 cc, and the thickness of 5 randomly selected bottles was measured. The results were shown in table 3.1. The crystalllinity of the bottle was measured using TA Instruments DSC 0100. The temperature of the test ranged from -10° C to 160° C. 5 bottles with 5 samples from each bottle were tested. For each bottle, 4 of the 5 samples were gotten from the side wall of the bottle. The other one was the bottom of the bottle. The results of the crystallinity were shown in table 3.2. The 28/400 white child resistant closures came with the bottles. The closures included two parts: Polypropylene (PP) caps and induction heat seal liners which were made of aluminum foil and paper board. 27 Table 3.1 Thickness of the bottle walls Bottle Thickness (in) Sidewall Bottom 1 0.0402 0.0385 0.0421 0.0401 0.0611 2 0.0427 0.0399 0.0431 0.0406 0.0634 3 0.0426 0.041 0.044 0.0396 0.0601 4 0.0419 0.039 0.0434 0.0399 0.0567 5 0.0439 0.0396 0.0429 0.0409 0.0547 Table 3.2 Crystallinity of the bottles Bottle Crystallinity % Sidewall Bottom 1 42.85 44.41 44.66 43.67 45.96 2 41 .26 44.39 43.45 43.27 46.57 3 43.78 42.82 42.95 44.78 43.92 4 41.88 44.76 43.72 44.51 44.26 5 41.28 43.82 43.49 44.58 42.95 3.1.2 Test conditions 28 The tests for the bottles were performed under 5 different conditions: 27°C/79% RH, 30°C/60% RH, 30°C/65% RH, 30°C/70% RH and 30°C/75% RH. Among them, 27°C/79% RH is the average environmental condition of the ASEAN countries. 30°C/60% RH, 30°C/65% RH and 30°C/70% RH have been used as the stability test condition for Climate Zone IV. 30°C/65% RH was the condition used for Zone IV stability test when ASEAN proposed to WHO to change the stability test condition to 30°C/75% RH. 3.2 Test Method - Gravimetric Method The gravimetric method was also used to detect the WVTR of the HDPE bottles. USP Chapter <671> was used as the reference. Some changes were adopted. Five different conditions were prepared using five different salt solutions combined with two temperature-controlled chambers. The salt solutions were made following the description about Salt-Water System in ASTM E 104 (ASTM E 104). Based on the references (Wexler, 1954 and O’Brien, 1948), the five salts selected were: Table 3.3 Salt solutions used to provide specified RH for bottle test Salt Target RH @ 30°C Real RH 30°C" (average during the test) Cobalt Chloride (COCIz) 62% 59.5%. Sodium Nitrite (NaNOz) 65% 61 %' Potassium Iodide (KI) 68% 64.5%T Sodium Chloride (NaCl) 75% 74.5%' Ammonium Sulfate 80% 79%. @ 27°C" (NH4)2SO4 ' Humidity variances: :I_-2%; " Temperature variances: i2°C 29 Two controlled chambers were used to provide the temperatures needed. But the relative humidities of the chambers were also set based on the condition needed. The purpose of this is to decease the influence from the outside environment once the lid of the bucket is opened. One of the chambers was set at 30°C, 60% RH, the other was set at 27°C, 79% RH. the relative humidity of the two chambers were set based on the The salt solutions were stored in the two chambers for stabilization for 2 weeks before the test. Salt solution CoCIz , NaNOz, KI and NaCl were stored in the chamber set at 30°C. While, (NH4)ZSO4 solution was placed in another chamber which was set at 27°C. Five randomly selected bottles filled with calcium sulfate desiccant (about 50 gram) were tested for each condition. Two bottles filled with the same amount of glass beads were used as controls (blanks) for each condition. Enough torques were applied to all the bottles once the desiccants or glass beads were added. Then, the bottles were induction heat sealed and retorqued. Each set of 7 bottles was placed in a bucket with humidity sensor. 30 H um idity Samples sensor Connect to the humidity +controls : collector Bucket Figure 3.1 Schematic drawing of exposure bucket for WVTR test of bottles The samples were weighed every 7 days at the beginning. After 63 days, the bottles were weighed every 14 days till the end. Two balances were used because the first one was broken in the middle of the test. The information about the two balances is listed in table 3.4 Table 3.4 The balances used in the test for the bottles Description Maximum Readability Test duration Sartorious 210 g 0.1 mg Beginning ~ day 63 Ohaus 110 g 0.1 mg Day 64 ~ end 31 The temperatures for both of the chambers were recorded continuously using analog recorders. The relative humidity of each bucket was measured using humidity sensor which was placed in the bucket. For the two chambers, the temperature variances are -_l-2°C. For all the humidity sensors inside the buckets, the humidity variances are i2%. The temperature and the relative humidity of each bucket were monitored before each weighing. Average WVTR value for each bottle was calculated based on the weight gain of the sample. When the test was finished, visual check was made for all the bottles. The seal and the body of the bottle were checked. 32 Chapter 4. Results and Discussion In the test, the temperature of each storage chamber and the relative humidity of each bucket were checked every time before weighing. The temperatures recorded were the digital reading of the chambers. The figure 4.1 and 4.2 show the temperature and the relative humidity during the test. 32 I 30 90000.... O O O .— 28 .. -------—— III..IIIIIIIIII II I II I ‘ 0 Chamber 30°C 26 i I Chamber 27°C 24 L_._- - . -_____-. I Temperature °C 22 -- - 4H ,m i 0 50 100 1 50 Figure 4.1 The temperatures recorded during the test of the bottles 33 .__ -_#- _—.-—_— _.-._ ._._ _- .-_ _ ---» -u r A? I 90 1 i 80 x x i ‘i x X x x 1* fi‘“ 7 “i a: $ x x x x x x x x x x x x x 70 o\° AAAAAAAAA A A A A OBucket1 3. 60 JJHJIm—Je—J—l—U _____, .‘9 I Bucket 2 E 5° ‘“ “’ “’* ‘—‘ :3 A Bucket 3 5 40 P _ _r _ _ __ __ ‘ Li M.— a; x Bucket4 E 30 _.., fl _ FT ‘_—_ 'T x Bucket 5 3:) 20 4* a 4 —— — - I 10 _____. _E__#_E _-__ —— - —————— I I 0 . . i i o 20 4o 60 so 100 120 140 i I I Figure 4.2 The RH recorded during the test of the bottles From the two figures, it can be seen that both temperature and the relative humidity were very stable during the test. The records of temperature gotten from the analog recorder were also checked each time. They also demonstrated the stability of the temperature during the test. The effect of opening the lids of the buckets (either to- take the samples out of the buckets or to put the samples into the buckets) was also evaluated. Once the lid was opened, the reading of RH sensor was monitored hourly till the RH went back to the original relative humidity. It was found the RH inside the bucket decreased when the lids were opened, and the RH would come back to the original value in about 6 hours once the lid is closed. 34 4.1 Result of the test bottles The weight gains vs time for each bottle was plotted in Fig 4.3 to 4.12. The weight gain was considered as the amount of water vapor transmitted into the bottle. When the first balance used to weigh the samples was broken after 63 days, another balance was used as the substitute. So, for each condition, two figures were plotted, one for each balance/time period. The Water Vapor Transmission Rate (VVVT R) was calculated from linear regression of the weight gained of the test bottle versus time. The WVTR of each bottle and the average of five for each condition are shown in table 4.1. 35 i Bottles stored in 30°C. 595% R“ Chambe' i 40 I 23 3o — —— —— —— —V——— ——))I((—;~~— —— "T'BottIe—lfi B 20 4— ——— -- —— —f——%- j . Bottle 3 :5, 15 if . . x Bottle 4 g 10 ~—-—,, if . e - x actual: 0 0 20 40 60 80 Day Figure 4.3 The weight gains of the bottles stored in condition 30°C/59.6%RH from day 0 to day 63 i Bottles stored in 30°C, 59.6%RH chamber 120 110 - — R+*_____fiw ’cE?) 100 -- 0 Bottle 1 E 90 mum -- x x “a I Bottle 2 ‘3, 80 — —--———— ——y ———-- A Bottle 3 E, 70 »—‘~.——++e—------—~—i—! ‘ xBottIe4 i g so -— -_ 3532sz 50 — —— — —— —— a 40 * 0 50 100 150 Figure 4.4 The weight gains of the bottles stored in condition 30°C/59.6%RH from day 64 to day 119 36 60 I . _________ is?) 50 ~———~— —— oBottIe1 E, 40 __ _ - V A r' IBottle2 'ITI __ ABottle3 m 30 i R — — ' B ttl 4 vo-v ‘ X 0 e J: __ ___I § _, _ .3 2° x i! 3' fix Bottle5 ; 10 ‘ o 1 . 0 20 40 60 80 . Day Figure 4.5 The weight gains of the bottles stored in condition 30°C/60.9%RH from day 0 to day 63 [—____ ”A W, .._-_.a Bottles stored in 30°C, 60.9%RH chamber 100 ,\ 95 if E 90 ——-— - ---—~ ~ I I r 0 Bottle 1 7' E 85 E“ I Bottle 2 3: 80 as — f—M—--——— A Bottle 3 E, 75 LL - hr" ‘x Bottle 4 g 70 ‘— ’———+%+ — x Bottle 5 65 ——m~--- -- - - 60 0 50 100 150 Day Figure 4.6 The weight gains of the bottles stored in condition 30°C/60.9%RH from day 64 to day 119 37 A-‘NNww-b-h 0100100! Weight gain (mg O 01 O 01 O Bottles stored in 30°C, 64.5%RI-l chamber —— F - ‘ — —~—-+A——~—— ;:fi:m;:m____ ‘ i _c___.. 20 40 60 80 Day "M’I I I iBottle 1 I Bottle 2 A Bottle 3 x Bottle 4 a: Bottle 5 Figure 4.7 The weight gains of the bottles stored in condition 30°C/64.5%RH I j 110 I 90 80 70 60 50 Weight gain (mg) from day 0 to day 63 Bottles stored In 30°C, 64.5%RH chamber 100 ~ 100 150 Day ”WRRRI i786tt|e 1 I I Bottle 2 A Bottle 3 x Bottle 4 1: Bottle 5) I Figure 4.8 The weight gains of the bottles stored in condition 30°C/64.5%RH from day 64 to day 119 38 Bottles stored in 30°C, 74.5%RH chamber W“ W W I I 5" . I 3’40 — ——-———— +I——- oBottle1I E 30 H z __ w Th! _, I Bottle 2 3 A Bottle 3 E, 20 ”_i ‘ ‘W ‘ W W W W x Bottle 4 £10 J . —- ——— ———— xBottIeSJ- ‘ __ - I 0 1 . f o 20 4o 60 so I I Day I I , __ _. a- Z J Figure 4.9 The weight gains of the bottles stored in condition 30°C/74.5%RH from day 0 to day 63 W I j Bottles stored in 30°C, 74.5%RH chamber I I 120 I I A 110 —~-- A fl __g f ,I g 100 F‘. ii _ A L ____ 0 Bottle 1 i c A 8 - Bottle 2 I a) 80 ‘ f—i ,. _ __ A Bottle 3 f9, 70 I x Bottle 4 I é’ W WW W R WT”_ a: Bottle 5: 60 J» _-»__ _ __ __, 50 ' 1 0 50 100 150 I Day Figure 4.10 The weight gains of the bottles stored in condition 30°C/74.5%RH from day 64 to day 119 39 Figure 4.11 The weight gains of the bottles stored in condition 27°C/79%RH from Figure 4.12 The weight gains of the bottles stored in condition 27°C/79%RH from Weight gain (mg) -t N on A o O O O O 100 — 90 80 70 Weight gain (mg) 60 50 Bottles stored in 27°C, 79%RH chamber I I ______ T+ML _ ”*fn‘ ’ z c — _4_l__..___ _ _ __ ____ . 20 40 60 80 day 0 to day 63 Bottles stored in 27°C, 79%RH chamber L ,L-_- ‘ I ___, _ cc ‘ 1 __ _. ”i _E__ _-___-- 50 100 150 Day day 64 to day119 40 ,, _fi-___.,7 TI I I SERIES] I Bottle 2 I A Bottle 3 I x Bottle 4} {Bottle 5: L. I W I Bottle 2 i A Bottle 3 I x Bottle 4 l .*@%&I $ Bottle 1‘ Table 4.1 WVTR value for each bottle Storage Bottl Balance 1/Day1 ~day 63 Balance 2/Day64 ~day condition* e 119 Linear regression R2 Linear regression R2 (WVTR mg/d/bt) (WVTR g/d/bt) 30°C/59.6%RH 1 0.4138 0.975 0.4171 0.995 2 0.3986 0.972 0.4071 0.996 3 0.3952 0.970 0.4093 0.996 4 0.4579 0.980 0.4721 0.998 5 0.4064 0.973 0.4186 0.995 Average 0.4144 0.4248 30°C/60.9%RH 1 0.4500 0.977 0.4293 0.990 2 N/A N/A N/A N/A 3 N/A N/A N/A N/A 4 0.4788 0.980 N/A N/A 5 0.4299 0.994 0.4264 0.984 Average 0.4529 0.4279 30°C/64.5%RH 1 0.4798 0.981 0.4879 0.997 2 0.5240 0.984 0.5479 0.998 3 0.5498 0.986 0.5471 0.999 4 0.4781 0.981 0.4964 0.998 5 0.4840 0.981 0.4943 0.999 Average 0.5031 0.5147 30°C/74.5%RH 1 0.5243 0.989 0.5093 0.999 2 0.5526 0.987 0.5621 0.987 3 0.6607 0.991 0.6393 0.999 4 0.5264 0.982 0.5236 0.998 5 0.5095 0.984 0.5136 0.999 Average 0.5547 0.5496 27°C/79%RH 1 0.4398 0.975 0.4214 0.998 2 0.4267 0.974 0.4114 0.998 3 0.4929 0.979 0.4743 0.998 4 0.5238 0.984 0.5121 0.998 5 0.4840 0.978 0.4714 0.998 Average 0.4743 0.4581 *Humidity variances: i2%; Temperature variances 41 : i2°C In figure 4.5 and 4.6, it can be found that bottle 2 and 3 reacted abnormally at day 56, 63 and 77 comparing with other bottles. The weight gains for these two bottles were much higher than other bottles at the three measurements. Linear regression could not be made for them. So, in table 4.1, they are listed as WA. For bottle 4, WVTR from day 64 to day 119 was also listed as N/A because the R2 value is less than 0.9 when the linear regression was made. When the test was finished, visual check was made for the three bottles. No defect was found. The seal was intact and the body of the bottle was undamaged. In order to make sure that there is no difference for WVTR values which were calculated based on the data from two different balances, a scatter plot Fig 4.13 was made of x = WVTR for period 0 - 63 and y = WVTR for period 77 - 119 for the n = 22 bottles (25 bottles minus the 3 for which there were no slopes computed for at least one of the periods). 42 c.__-____ M-) Scatterplot of Slopes y = 0.9437x + 0.0264 I . I I 0 7 R2 = 0.9504 i . I ' I I §_>‘ I 5 I (’6‘ I e I 0‘ I E i I , I I I 0.35 I , L . ‘ I 0.35 0.4 0.45 0.5 0.55 0.6 0.65 0.7 | I WVTR (Day 0 - 63) I L- ___. ______ _______ _ _.- _J Figure 4.13 Scatter plot of WVTR from two different periods Linear regression was made for all the data. The plot shows a consistency between the two periods in regard to WVTR determinations. The regression line is essentially the 45-degree line. This tells us that there is no difference between the WVTR for the two different periods. From table 4.1, it can be seen that the average WVTR value of the bottles at 30°C, 65.4%RH is higher than the average value at 27°C, 79%RH. The WVTR values for all the bottles stored in 5 different conditions were compared in the two figures, Figure 4.14 and 4.15. It also can be found that the range of the WVTR values of the bottles at 30°C, 64.5%RH are higher than the range of the values at 27°C, 79%RH. 43 m—,__' w.] I I I 0.7 i ’5‘ 0.65 ——-—- ———— x '* ocondition1 , I E 06 A ”fl #2. ___, fl _ __ E___ 30/59.6 f g ' I condition 2 I 3 0.55 ~ — # —————— —A# —><— ——~— — —~~ 30/60.9 I 2 0 5 b. __ _ _ __ _____‘ § X J Acondition 3 , . g ' u A if 30/64.5 I I v 0.45 e ——1 - E —- § — 2“ ~——-——~ xcondition 4 I I m 0 4 4 __ __:_ _§ * J +____'_____ 30/745 I i E ” ‘ ' xcondition5 I 0.35 -—— —— 27/79 ’ 0.3 I 0 2 4 6 I Condition , Figure 4.14 Comparison of all the WVTR values of the bottles (day 0 ~ day 63) I" *T “T— WW WI I WVTR Comparison (day 64 ~ day 119) i I ,6. 0-7 0 condition 1 I a 0.65 x -* '~— 30/59.6 g 0 6 a?-—— --——A I condition 2 ,5 0 55 4. _-* _ . x 30/69-9 2 0 5 __.__~__ _ it A condition 3 3’ - . r 30/64.5 V 0.45 ~~——~— I x condition 4 o: 0.4 , __,_ ____ ,____._,___ __ 30/74.5 0 35 %_ a: condition 5 - 27/79 I 0.3 I I I 0 2 4 6 I I condition Figure 4.15 Comparison of all the WVTR values of the bottles (day 64 ~ day 119) 44 One tail, two-sample t-tests were performed for the WVTR values gotten from the two different conditions 30°C, 64.5%RH and 27°C, 79%RH. Separate analyses were done for the two periods where different balances were used. In each test, the null hypothesis is that there is no difference in means and the alternative is that mean WVTR values gotten from 30°C, 64.5%RH exceeds that of WVTR values gotten from 27°C, 79%RH. The p-values are reported in Table 4.3. Using the 0.05 level as indicating significance, the difference in average WVTR values 0.5031 — 0.4743 = 0.0297 mg/day for Days 0 - 63 is not significant whereas the difference in average WVTR values 0.5147 - 0.4581 = 0.0566 mg/day for Days 64 -- 119 is significant Table 4.3 P-values for t-tests of T-test for WVTR values gotten from 30°C/64.5%RH and 27°C, 79%RH Result from Result from balance 1 balance 2 (Day 0~63) (Day 64~119) P-value 0.12 0.02 The P-values in both cases are small and the null hypothesis can be rejected for the second period. These results support the hypothesis that the current WHO 45 long test condition is severe enough to represent the condition of ASEAN countries for purpose of measuring WVTR of package 4.2 Result of the control bottles The weight gain of every control bottle vs time was also plotted, and shown in Fig 4.16 to 4.25. Same balances were used for weighing the controls as were used for weighing the test bottles. Two figures were plotted for the bottles stored in each condition. 46 TC _Iwfl_m_ _I I Control bottles stored in 30°C, 59.6%RH chamber I I 6 I As~w——w 4L - I c» I___.’_,. _*_ ____#__H s§_4 - ”1- _« I % 2 __._£ ‘7 “-4 '“’I --_----r_ _ ocontrol bt1 I 3’31::f‘Tfifi::i;:;f;f::;:::i '“m_m“m2I a -1 _..__.._-_fio _ _ _. I -3 . . __. 4w.» __ O. __ a I .4 o 20 4o 60 80 I I Day I I Figure 4.16 The weight gains of the control bottles stored in condition 30°C/59.6%RH from day 0 to day 63 .5 O I I A 38 —~ I °’ I g I I .E 36 - r ' - --—' ~ I g l 0 control bt 1 II E 34 #H F IIcontrol bt2I U) W . .5 I 3 32 —-- a --—--. 9 a I I . I I 30 I I o 50 100 150 I I Day I. ____ ______.__*I,- _ _ .. _ I Figure 4.17 The weight gains of the control bottles stored in condition 30°C/59.6%RH from day 64 to day 119 47 Control bottles stored in 30°C, 60.9%RH chamber 30 I I €20 - - ~~ —~—— —--fi m--___I % 15 ' Iocontrol bt1 II D) *‘ ”i 'f a «— _ _____~_ I E ’ LEMPQII .2>1o —mv~ ____. --m__I II‘ #_ __fl é, o e e I o 5 TTI‘fi“”‘t I 1 ~-- I I I 0 I I . I 0 20 4O 60 80 I I Day I I I Figure 4.18 The weight gains of the control bottles stored in condition 30°C/60.9%RH from day 0 to day 63 _ ,,, i;A,___.____._, Control bottles stored in 30°C, 60.9%RH chamber I ,_I V.— ’ _ __ _. Iocontrolbt’1-II . . e Icontrolbt2I I I I I o 50 100 150 I I Day L______________ "MAI Figure 4.19 The weight gains of the control bottles stored in condition 30°C/60.9%RH from day 64 to day 119 48 I _ -__ _ Control bottles stored in 30°C, 64.5% RH chamber I 12 310 —— -— —— ——-——— -—— ~ —— E . ° Z 3 — ”* r,“ 1 . ‘ —— _____ ~— '66 . . ’ ° . ocontrolbt1I O) 6 ’- —— _'I_« .-I #~.——~———I E - . - control bt2 I .9 4 ~— ‘ "W on 3 2 -w __ #-_- ___# *_. I 0 T ‘ I I o 20 4o 60 80 I I I Day - __________ ._ _ _ _ ____ ._ _____ _I Figure 4.20 The weight gains of the control bottles stored in condition 30°C/64.5%RH from day 0 to day 63 I, ,,___ I Control bottles stored in 30°C, 64.5%RH chamber 50 A 48 — 8’ v46 . f u r ————— few _s ______,W_ '§ 9 control bt 1I= a: 44 F , 7 I E I control bt 2 I g 42 —— o . e o I 3 4o _-_______-_,_, ._ ' u ' - __ I I 38 I I o 50 100 150 I I Day I I ,I________W___,_.____ M- __ I Figure 4.21 The weight gains of the control bottles stored in condition 30°C/64.5%RH from day 64 to day 119 49 I,_.__‘,._._ Control bottles stored in 30°C, 74.5%RH chamber 20 I A 15 __.-, w—w +-———————e---——r-»-L—i~ . I a) . I g 10 __._ _ Q : L_._.._ _.__ __ I % 5 _ _ f __ A_ 2 w _ ocontrolbth 3:3 I control bt 22I; .% O I——— ii 74. __.___L_ _._.___ l____ I I 3 '5 I _ _l—_“Li—"“ I 10 I I I I I I I ' I I 0 20 40 60 80 Day I Figure 4.22 The weight gains of the control bottles stored in condition 30°C/74.5%RH from day 0 to day 63 Control bottles stored in 30°C, 74.5%RH chamber ! (A) o I I I I I 50 O o O . I I A45-~—f Jm—w—~n_~w— I I a, I E 40 ——‘ I w_r______ I m ____._ I E omMmWHI ‘31 35 — I I .. Icontrol bt2I. c l .9 (D 3 N 01 I I I I ' o 50 100 150 I I Day I Figure 4.23 The weight gains of the control bottles stored in condition 30°C/74.5%RH from day 64 to day 119 50 ____.___~ _—.— gur— L, a ___ H Control bottles stored in 27°C, 79% RH chamber _I m A 16 Lee TTT‘T fleece—es C» __ ___-.. M“ _ __ “ ___ EEDWW lbw: -Iwg * E10 _,- ' ‘ . .D ocontrolbt1I. E 8 M__ T“ ”a“ ~ m— I-contnolthI a, 6 ___ .‘______ e__ ., _.e__ _._ _ % ,_ g 4 ___.. ._. ____ -_~___ W_W __*v__~_ ‘_I 2 —— — ——_—_ _ _ __ __ __ _ o o 20 4o 60 so Day “J Figure 4.24 The weight gains of the control bottles stored in condition 27°C/79%RH from day 0 to day 63 Control bottles stored in 27°C, 79%RH chamber I I I I I I ~——~ +~ww»~~-m__ :ammmq LogntmLtflII Weight gain (mg) 8 s t 8 3 8 a; 2 8 8 I I I I Day I I I e I I I I I i I Figure 4.25 The weight gains of the control bottles stored in condition 27°C/79%RH from day 64 to day 119 51 Theoretically, the weight of the control bottle should increase first, then become stable once the steady state is reached and the control bottle is at equilibrium. The weight gain of the control bottle mainly comes from the sorption of the package system and the permeation of water vapor. Once the stable state is reached, which means the RH inside the control bottle is equal to the RH of the storage environment, the weight of the bottle shouldn’t change any more. If linear regression is performed between the weight gain of the control bottle and time under steady state, the slope should be zero. From the figures above, it could be found the control bottles displayed erratic behaviors. Some bottles lost weight instead of gaining weight. And stable state could not be found for any control bottle. In this test, the control bottles served as the reference of the system error produced in measuring and handling. The result was expected to be used in data analysis. However, from the outcome gotten from the control bottles, it’s hard to relate it to the results of the test bottles. And WVTR, which is the rate of weight gain, should be a constant when the steady state is reached. Therefore, it ‘3 possible to ignore the change of the control bottles. In this test, there are a few possible reasons that could affect the results of the test and control bottles: 1. The variance of the bottles. Although the bottles are from the same batch, there are still some differences in thickness, crystallinity and etc which affect the WVTR of the bottle. 52 . When the bottles were induction sealed, there might be differences of the current used for each bottle. If the current is strong enough, micro hole could be produced on the aluminum layer of the liner. That could affect the WVTR of the bottles. . During the test, the temperature and the relative humidity were stable. However, there were some small variance that could affect the result. . System error was produced by handling and measuring. . Sample size was not big enough. 53 Chapter 5 Conclusion The water vapor transmission rates of HDPE bottles in five different conditions were tested using gravimetric method, and statistical analysis was performed for all the data. The hypothesis that the stability test condition 30°C/65% RH should be severe enough to represent the ASEAN average condition 27°C/79% was verified. It means that 30°C/65% RH could be used as the stability test condition for all the countries in Climate Zone IV. And it’s not necessary to use 30°C/75% RH as the test condition, although it’s helpful to make the drug products safer. The results also proved that the relative humidity of the environment alone is not the only issue that affects the result of stability testing. Actually, it is the storage temperature, partial pressure for water vapor and moisture permeability of the package that affect the result of stability testing, because they all affect the humidity inside the package. It is the humidity inside the package that affects the product. There is some further investigation which could lead to an increased understanding of this research. 1. Monitor and record the change of storage condition continuously. In this case, more information could be gathered and used in data analysis. 2. Enlarge the sample size. 3. Investigate the behavior of the control bottles, such as sorption of the bottle and liner. 54 REFERENCES ASEAN 1, “Overview Association of Southeast Asian Nations”, http://www.aseansec.org_/64.htm ASEAN 2, “ASEAN Cooperation on Standards and Conformance to Facilitate Trade in The Region”, http://www.aseansec.org/6667.htm) ASEAN 3, “ACCSQ Pharmaceutical Product Working Group”, http://www.aseansec.org/14903mm. ASTM E 96, “Standard Test Methods for Water Vapor Transmission of Materials”, ASTM lntemational ASTM F 1249, “Standard Test Method for Water Vapor Transmission Rate through Plastic Film and Sheeting Using a Modulated Infrared Sensor", ASTM lntemational ASTM E 104, “Standard Practice for Maintaining Constant Relative Humidity by Means of Aqueous Solutions”, ASTM lntemational Bailey, L.C.; Medwick, T. 1993, “Mean Kinetic Temperature — A Concept for Storage of Pharmaceuticals”, Phannacopeial Forum, 19(5), 6163-6166 Bott, R. F.; Oliveira, W. P. 2007, “Storage Conditions for Stability Testing of Pharmaceuticals in Hot and Humid Regions”, Drug Development and Industrial Pharmacy, 33, 393-401 Doty, P.M.; Aiken, W.H.; Mark, H. 1946, “Temperature Dependency of Water Vapor Permeability”, Ind & Eng. Chem, 38(8), 788-791 Grimm, W. 1986, “ Storage conditions for Stability Testing (Part 2)”, Drug made in Germany, 29, 39-47 55 Grimm, W. 1998, “Extension of the lntemational Conference on Harmonization Tripartite Guideline for Stability Testing of New Drug Substances and Products to Countries of Climatic Zones Ill and IV”, Drug Development and Industrial Pharmacy, 24, 313-325 Lockhart, H.; Selke, 8.; Yoon, S. 2006, “The Role of Container-Closure Systems in Stability Testing For Climate Zone IV”, Phannacopeial Forum, 32(2), 688-694 O’Brien, F.E.M. 1948, “The control of Humidity by Saturated Salt Solutions — A Compilation of Data”, J. Sci. lnstr., 25, 73 PMA’s Joint QC-PDS Stability Committee 1991, “Room-Temperature Stability Studies: Storage Conditions”, Pharmaceutical Tech., Sep., 93-96 Rubino, M. 2005, “Permeability and Shelf Life” Course pack for School of Packaging, MSU PKG 815, 2.1-3.30 Schumacher, P. 1972, “The Impact of Climate Classification on The Stability of Medicines”, Pharm Ind, 34, 481-483 Singh, S.; Kumar, V. 2006, “Recent Developments on Long — Term Stability Test Conditions”, The Pharma Review, Dec, 61-68 USP 1 2004, “Stability Considerations in Dispensing Practice”, United States Pharmacopeia, 27, 2605 USP 2 2004, “Containers — Permeation” United States Pharmacopeia, 27, 2296 - 2297 Van Krevelen, D.W. 1997, Properties of Polymers. Their come/ation with chemical structure: their numerical estimation and prediction from additive group contributions. 3’“ edition, Elsevier, Amsterdam Wexler, A.; Hasegawa, S. 1954, “ Relative Humidity-Temperature Relationship of Some Saturated Salt Solutions in the Temperature Range 0° to 50°C”, J. Research NBS, 53, 19 56 WHO 2004, “Aspects of the Quality Assurance”, WHO Drug lnfonnation, 18(2), 113-116 WHO 1, “Stability Testing of Active Substances and Pharmaceutical Products”, WHO, Working Document OAS/06.179 WHO 2, “Stability Studies in a Global Environment” WHO, Working Document OAS/05.146 57 II IIIIIIIIIIIIIIIIIIIII