IFT19- Migration models and their reliability in safety validation

Packaging Technology and Research, LLC
Packaging Technology and Research, LLCFood Packaging Expert at Packaging Technology and Research, LLC
Food Packaging
Migration Models and
Their Reliability in
Safety Validation
Created by:
Ziynet Boz, Ph.D.
Packaging Technology and Research LLC.
Created by:
Migration Overview
 Migration mechanism in food-
packaging systems
 Several affecting factors
 Several packaging technologies,
conditions, food types
 Databases generated with food
simulants for compliance
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Migration
Temperature
Concentration
MW
Solubility
Time
Compositions
Partition
Coefficients
Surface/
Volume
Ratio
Contact
type
Mobility
Created by:
Why models?
• Experimental procedures are time-
intensive, costly
• Numerous combinations of packaging-
food-environment
• Risk assessment in decision-making
• Limited migration packaging design
• Lowering the additive diffusivity during
synthesis
• Monomers, antioxidants, stabilizers,
antimicrobials etc.
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Created by:
Regulatory Opinions on Models
 Current state of the models in compliance
• Accepted models for FCMs are oversimplified, deterministic, “worst case”
scenario
• Initial Conditions: uniform distributions, no-migrant in food
• Boundary Conditions: No interface resistance
• No spatial distribution after migration
• Total migration amount is constant (No reaction / generation)
• High solubility of migrant in food (Partition coefficient = 1)
 If result is lower than SML
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Created by:
Migration Models: Deterministic
 Diffusion: Fick’s Law
• Fick’s Second Law of Diffusion
• MW distribution, density, crystallinity, orientation, solubility,
migrant molecular size, shape, plasticization effect, Tg, Tm
 Diffusion coefficient 𝐷𝐴
𝑃
 Partition coefficient 𝐾𝑝
 Assumptions
• C0, food = 0 , migrant is homogenously distributed in Pkg
• Good approximation for single layer packages
• Overestimation ageing, long storage, low MW ->
Overestimation
• Absence of chemical reaction, loss (e.g. evaporation)
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𝜕𝐶𝐴
𝑃
𝜕𝑡
= 𝐷𝐴
𝑃
𝜕2 𝐶𝐴
𝑃
𝜕𝑥2
𝐾𝑝 =
𝐶𝐴
𝑃
(∞)
𝐶𝐴
𝐹
(∞)
𝛼 =
𝑀𝐴
𝐹
(∞)
𝑀𝐴
𝑃
(∞)
=
𝐶𝐴
𝐹
(∞)
𝐶𝐴
𝑃
(∞)
=
𝑉 𝐹
𝐾𝑝 𝑉 𝑃
If 𝛼>>1 & Kp < 1 -> 100% migration
Created by:
Migration Models: Deterministic
6
Bi>100
No Resistance
h is not
infinitive
Diffusion
coefficient
Interaction
effects
Swelling of the packaging materials -> Swelling layer
E.g. Olive oil into PP
(Poças, Oliveira, Oliveira, & Hogg, 2008)
Created by:
Migration Models: Empirical
 Disregarding underlying mechanism
behind coefficients
• Empirical equations for D: LDPE, HDPE, PP -> f(T, MW)
(Arrhenius-like)
• Partitioning, mass transfer, polymer morphology, shape/polarity
of the migrant are not considered
• Piringer Model to determine D with overestimated diffusion
(50% of the results)
• Underestimate the effect of temperature for high MW migrants
• Limm and Hollifield model for additive diffusion in polyolefins
(Arr. Type)
 Weibull model
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Piringer model
Created by:
Migration Models: Probabilistic
 Variability in migration model outputs as a result of the uncertainty in model inputs
 Mixed effect models with deterministic models
 Probability distribution of the diffusion coefficient using Molecular mass
 Distribution of outputs
 Monte Carlo sampling
 Fourier Amplitude Sensitivity Test (FAST)
 Latin hypercube sampling
 Capturing lack of knowledge
• Temperature fluctuations
• Time of contact
• Non-systematic errors
 Uoverall Migration = 2 mg/dm2 or 12 mg/kg
Created by:
Migration Models: Plastics
 Majority of the migration studies are
polyolefins
 Low partition coefficients with non-polar
simulants/foods due to Tg
 Lack of data on polymers glassy at their
temperature of use
 PET requires longer testing time
• Recent studies: Virgin layer migration barrier
 Adhesives, urethane polymers, repeated Pkg
use
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Hexanal Olive oil migration (Gavriil,
Kanavouras, & Coutelieris, 2018)
Created by:
Migration Models: Paper & Paperboard
 Inhomogeneous medium:
Heterogenous, porous, fiber-
based
 Solid products
adsorption/desorption
 Fickian diffusion seems to poorly
estimate low porosity low thickness
 Simulants: Tenax®, Propak®
 Weibull model provides good fit
 Phthalates
 Migrant volatility, polarity, affinity
impact
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(Poças, Oliveira, Pereira, Brandsch, & Hogg, 2011)
Created by:
Migration Models: Other materials
 Ceramic and printing inks
 Cadmium and lead migration from
ceramic into acid food simulants was
studied
• Time-temperature influence
• Fickian Diffusion
• 600 h & 130 days
• Ion exchange -> hydrolysis
© INSTITUTE OF FOOD TECHNOLOGISTS | ALL RIGHTS RESERVED11 (Dong, Lu, & Liu, 2015)
Created by:
Simulation Software
 MIGRATEST 2000/2001 Fabes GmbH, Germany
 AKTS SML by Advanced Kinetics Technology Solution, Switzerland
 SMEWISE (Simulation of Migration Experiments with Swelling Effect)
 MULTITEMP, MULTIWISE by Safe Food Packaging Portal
 SFPP3 France
 FMECAengine
 FACET (Flavors, Additives and Food Contact Materials Exposure
Task)
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Created by:
Decision-making Based on Models
 FDA Model, EU Piringer model -> Overestimation 95%
• E.g. HDPE-food simulant, PET-water, AO-Tenax®, Photoinitiator-paper-Tenax®
 Oversimplification and assumptions: Over- or under-estimated
migration
 Possibility of rejecting potentially safe materials and chemicals
 Trained professionals
 Only for known chemicals IAS
 Target group: Converters and Chemical Industry
 High-throughput models only suitable for multiple migrants
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Created by:
Research Gaps
 A more realistic estimation of diffusion coefficients are needed
 Effects of swelling phenomenon
 Environment-package-food systems should be considered
 Data needed beyond regulatory compliance but a food quality perspective
 Actual interactions should be considered E.g. Oxygen effects, Flavor desorption
etc.
 Models of migrants from multilayer materials with numerical methods
 Industrial tools to assess the migration: Practical, Robust
 Non-plastic materials: E.g. paper and paperboard
 Nanomaterial migration assessment
 Emerging modeling methods E.g. Molecular modeling, molecular
thermodynamics, coupled models with human exposure
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Created by:
References
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https://doi.org/10.1016/j.fct.2017.09.024
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Created by:
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Created by:
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 Welle, F., & Franz, R. (2011b). Migration of antimony from PET bottles into beverages: determination of the activation energy of diffusion and migration modelling compared with
literature data. Food Additives & Contaminants: Part A, 28(1), 115–126. https://doi.org/10.1080/19440049.2010.530296
 Zülch, A., & Piringer, O. G. (2010a). Measurement and modelling of migration from paper and board into foodstuffs and dry food simulants. Food Additives and Contaminants, 27(09),
1306–1324. https://doi.org/10.1080/19440049.2010.483693
 Zülch, A., & Piringer, O. G. (2010b). Measurement and modelling of migration from paper and board into foodstuffs and dry food simulants. Food Additives and Contaminants, 27(09),
1306–1324. https://doi.org/10.1080/19440049.2010.483693
© INSTITUTE OF FOOD TECHNOLOGISTS | ALL RIGHTS RESERVED18
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IFT19- Migration models and their reliability in safety validation

  • 1. Food Packaging Migration Models and Their Reliability in Safety Validation Created by: Ziynet Boz, Ph.D. Packaging Technology and Research LLC.
  • 2. Created by: Migration Overview  Migration mechanism in food- packaging systems  Several affecting factors  Several packaging technologies, conditions, food types  Databases generated with food simulants for compliance © INSTITUTE OF FOOD TECHNOLOGISTS | ALL RIGHTS RESERVED2 Migration Temperature Concentration MW Solubility Time Compositions Partition Coefficients Surface/ Volume Ratio Contact type Mobility
  • 3. Created by: Why models? • Experimental procedures are time- intensive, costly • Numerous combinations of packaging- food-environment • Risk assessment in decision-making • Limited migration packaging design • Lowering the additive diffusivity during synthesis • Monomers, antioxidants, stabilizers, antimicrobials etc. © INSTITUTE OF FOOD TECHNOLOGISTS | ALL RIGHTS RESERVED3
  • 4. Created by: Regulatory Opinions on Models  Current state of the models in compliance • Accepted models for FCMs are oversimplified, deterministic, “worst case” scenario • Initial Conditions: uniform distributions, no-migrant in food • Boundary Conditions: No interface resistance • No spatial distribution after migration • Total migration amount is constant (No reaction / generation) • High solubility of migrant in food (Partition coefficient = 1)  If result is lower than SML © INSTITUTE OF FOOD TECHNOLOGISTS | ALL RIGHTS RESERVED4
  • 5. Created by: Migration Models: Deterministic  Diffusion: Fick’s Law • Fick’s Second Law of Diffusion • MW distribution, density, crystallinity, orientation, solubility, migrant molecular size, shape, plasticization effect, Tg, Tm  Diffusion coefficient 𝐷𝐴 𝑃  Partition coefficient 𝐾𝑝  Assumptions • C0, food = 0 , migrant is homogenously distributed in Pkg • Good approximation for single layer packages • Overestimation ageing, long storage, low MW -> Overestimation • Absence of chemical reaction, loss (e.g. evaporation) © INSTITUTE OF FOOD TECHNOLOGISTS | ALL RIGHTS RESERVED5 𝜕𝐶𝐴 𝑃 𝜕𝑡 = 𝐷𝐴 𝑃 𝜕2 𝐶𝐴 𝑃 𝜕𝑥2 𝐾𝑝 = 𝐶𝐴 𝑃 (∞) 𝐶𝐴 𝐹 (∞) 𝛼 = 𝑀𝐴 𝐹 (∞) 𝑀𝐴 𝑃 (∞) = 𝐶𝐴 𝐹 (∞) 𝐶𝐴 𝑃 (∞) = 𝑉 𝐹 𝐾𝑝 𝑉 𝑃 If 𝛼>>1 & Kp < 1 -> 100% migration
  • 6. Created by: Migration Models: Deterministic 6 Bi>100 No Resistance h is not infinitive Diffusion coefficient Interaction effects Swelling of the packaging materials -> Swelling layer E.g. Olive oil into PP (Poças, Oliveira, Oliveira, & Hogg, 2008)
  • 7. Created by: Migration Models: Empirical  Disregarding underlying mechanism behind coefficients • Empirical equations for D: LDPE, HDPE, PP -> f(T, MW) (Arrhenius-like) • Partitioning, mass transfer, polymer morphology, shape/polarity of the migrant are not considered • Piringer Model to determine D with overestimated diffusion (50% of the results) • Underestimate the effect of temperature for high MW migrants • Limm and Hollifield model for additive diffusion in polyolefins (Arr. Type)  Weibull model © INSTITUTE OF FOOD TECHNOLOGISTS | ALL RIGHTS RESERVED7 Piringer model
  • 8. Created by: Migration Models: Probabilistic  Variability in migration model outputs as a result of the uncertainty in model inputs  Mixed effect models with deterministic models  Probability distribution of the diffusion coefficient using Molecular mass  Distribution of outputs  Monte Carlo sampling  Fourier Amplitude Sensitivity Test (FAST)  Latin hypercube sampling  Capturing lack of knowledge • Temperature fluctuations • Time of contact • Non-systematic errors  Uoverall Migration = 2 mg/dm2 or 12 mg/kg
  • 9. Created by: Migration Models: Plastics  Majority of the migration studies are polyolefins  Low partition coefficients with non-polar simulants/foods due to Tg  Lack of data on polymers glassy at their temperature of use  PET requires longer testing time • Recent studies: Virgin layer migration barrier  Adhesives, urethane polymers, repeated Pkg use © INSTITUTE OF FOOD TECHNOLOGISTS | ALL RIGHTS RESERVED9 Hexanal Olive oil migration (Gavriil, Kanavouras, & Coutelieris, 2018)
  • 10. Created by: Migration Models: Paper & Paperboard  Inhomogeneous medium: Heterogenous, porous, fiber- based  Solid products adsorption/desorption  Fickian diffusion seems to poorly estimate low porosity low thickness  Simulants: Tenax®, Propak®  Weibull model provides good fit  Phthalates  Migrant volatility, polarity, affinity impact © INSTITUTE OF FOOD TECHNOLOGISTS | ALL RIGHTS RESERVED10 (Poças, Oliveira, Pereira, Brandsch, & Hogg, 2011)
  • 11. Created by: Migration Models: Other materials  Ceramic and printing inks  Cadmium and lead migration from ceramic into acid food simulants was studied • Time-temperature influence • Fickian Diffusion • 600 h & 130 days • Ion exchange -> hydrolysis © INSTITUTE OF FOOD TECHNOLOGISTS | ALL RIGHTS RESERVED11 (Dong, Lu, & Liu, 2015)
  • 12. Created by: Simulation Software  MIGRATEST 2000/2001 Fabes GmbH, Germany  AKTS SML by Advanced Kinetics Technology Solution, Switzerland  SMEWISE (Simulation of Migration Experiments with Swelling Effect)  MULTITEMP, MULTIWISE by Safe Food Packaging Portal  SFPP3 France  FMECAengine  FACET (Flavors, Additives and Food Contact Materials Exposure Task) © INSTITUTE OF FOOD TECHNOLOGISTS | ALL RIGHTS RESERVED12
  • 13. Created by: Decision-making Based on Models  FDA Model, EU Piringer model -> Overestimation 95% • E.g. HDPE-food simulant, PET-water, AO-Tenax®, Photoinitiator-paper-Tenax®  Oversimplification and assumptions: Over- or under-estimated migration  Possibility of rejecting potentially safe materials and chemicals  Trained professionals  Only for known chemicals IAS  Target group: Converters and Chemical Industry  High-throughput models only suitable for multiple migrants © INSTITUTE OF FOOD TECHNOLOGISTS | ALL RIGHTS RESERVED13
  • 14. Created by: Research Gaps  A more realistic estimation of diffusion coefficients are needed  Effects of swelling phenomenon  Environment-package-food systems should be considered  Data needed beyond regulatory compliance but a food quality perspective  Actual interactions should be considered E.g. Oxygen effects, Flavor desorption etc.  Models of migrants from multilayer materials with numerical methods  Industrial tools to assess the migration: Practical, Robust  Non-plastic materials: E.g. paper and paperboard  Nanomaterial migration assessment  Emerging modeling methods E.g. Molecular modeling, molecular thermodynamics, coupled models with human exposure © INSTITUTE OF FOOD TECHNOLOGISTS | ALL RIGHTS RESERVED14
  • 15. Created by: References  20130719applicability_of_mathematical_modelling_for_the_estimation_of_specific_migration_of_substances.pdf. (n.d.-a). Retrieved from https://www.plasticseurope.org/application/files/8115/1722/2186/20130719applicability_of_mathematical_modelling_for_the_estimation_of_specific_migration_of_substances.pdf  20130719applicability_of_mathematical_modelling_for_the_estimation_of_specific_migration_of_substances.pdf. (n.d.-b). Retrieved from https://www.plasticseurope.org/application/files/8115/1722/2186/20130719applicability_of_mathematical_modelling_for_the_estimation_of_specific_migration_of_substances.pdf  Aparicio, J. L., & Elizalde, M. (n.d.). Migration of Photoinitiators in Food Packaging: A Review. Packaging Technology and Science, 28(3), 181–203. https://doi.org/10.1002/pts.2099  ARVANITOYANNIS, I. S., & BOSNEA, L. (2004). Migration of Substances from Food Packaging Materials to Foods. Critical Reviews in Food Science and Nutrition, 44(2), 63–76. https://doi.org/10.1080/10408690490424621  Arvanitoyannis, I. S., & Kotsanopoulos, K. V. (2014). Migration Phenomenon in Food Packaging. Food–Package Interactions, Mechanisms, Types of Migrants, Testing and Relative Legislation—A Review. Food and Bioprocess Technology, 7(1), 21–36. https://doi.org/10.1007/s11947-013-1106-8  Ashby, R. (1988). Migration from polyethylene terephthalate under all conditions of use. Food Additives & Contaminants, 5(sup001), 485–492. https://doi.org/10.1080/02652038809373681  Begley, T., Castle, L., Feigenbaum, A., Franz, R., Hinrichs, K., Lickly, T., … Piringer, O. (2005). Evaluation of migration models that might be used in support of regulations for food-contact plastics. Food Additives & Contaminants, 22(1), 73–90. https://doi.org/10.1080/02652030400028035  Begley, T. H., White, K., Honigfort, P., Twaroski, M. L., Neches, R., & Walker, R. A. (2005). Perfluorochemicals: Potential sources of and migration from food packaging. Food Additives & Contaminants, 22(10), 1023–1031. https://doi.org/10.1080/02652030500183474  Bhunia, K., Sablani, S. S., Tang, J., & Rasco, B. (2013). Migration of Chemical Compounds from Packaging Polymers during Microwave, Conventional Heat Treatment, and Storage. Comprehensive Reviews in Food Science and Food Safety, 12(5), 523–545. https://doi.org/10.1111/1541-4337.12028  Biryol, D., Nicolas, C. I., Wambaugh, J., Phillips, K., & Isaacs, K. (2017). High-throughput dietary exposure predictions for chemical migrants from food contact substances for use in chemical prioritization. Environment International, 108, 185–194. https://doi.org/10.1016/j.envint.2017.08.004  Bodai, Z., Jakab, P. P., Novák, M., Nyiri, Z., Szabó, B. S., Rikker, T., & Eke, Z. (2016). Solubility determination as an alternative to migration measurements. Food Additives & Contaminants: Part A, 33(3), 574–581. https://doi.org/10.1080/19440049.2016.1142676  Bott, J., Störmer, A., & Franz, R. (2014). Migration of nanoparticles from plastic packaging materials containing carbon black into foodstuffs. Food Additives & Contaminants: Part A, 31(10), 1769–1782. https://doi.org/10.1080/19440049.2014.952786  Bradley, E. L., Castle, L., & Speck, D. R. (2014). Model studies of migration from paper and board into fruit and vegetables and into TenaxTM as a food simulant. Food Additives & Contaminants: Part A, 31(7), 1301–1309. https://doi.org/10.1080/19440049.2014.914633  Brandsch, R. (2017). Probabilistic migration modelling focused on functional barrier efficiency and low migration concepts in support of risk assessment. Food Additives & Contaminants: Part A, 34(10), 1743–1766. https://doi.org/10.1080/19440049.2017.1339235  Cai, H., Ji, S., Zhang, J., Tao, G., Peng, C., Hou, R., … Wan, X. (2017). Migration kinetics of four photo-initiators from paper food packaging to solid food simulants. Food Additives & Contaminants: Part A, 34(9), 1632–1642. https://doi.org/10.1080/19440049.2017.1331470  Chung, D., Papadakis, S. E., & Yam, K. L. (2002). Simple models for assessing migration from food-packaging films. Food Additives & Contaminants, 19(6), 611–617. https://doi.org/10.1080/02652030210126389  Dong, Z., Lu, L., & Liu, Z. (2015). Migration Model of Toxic Metals from Ceramic Food Contact Materials into Acid Food. Packaging Technology and Science, 28(6), 545–556. https://doi.org/10.1002/pts.2122  Ernstoff, A. S., Fantke, P., Huang, L., & Jolliet, O. (2017a). High-throughput migration modelling for estimating exposure to chemicals in food packaging in screening and prioritization tools. Food and Chemical Toxicology, 109, 428–438. https://doi.org/10.1016/j.fct.2017.09.024  Ernstoff, A. S., Fantke, P., Huang, L., & Jolliet, O. (2017b). High-throughput migration modelling for estimating exposure to chemicals in food packaging in screening and prioritization tools. Food and Chemical Toxicology, 109, 428–438. https://doi.org/10.1016/j.fct.2017.09.024 © INSTITUTE OF FOOD TECHNOLOGISTS | ALL RIGHTS RESERVED15
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  • 19. Created by: Thank you! Let’s Connect www.PackagingTechnologyAndResearch.com Ziynet@PackagingTechnologyAndResearch.com

Editor's Notes

  1. Chemical partitioning from packaging material into the food systems : Migration
  2. Worst case scenario: 100% migration Models can at least partially replace experiments Functional barrier (virgin polymer) effectiveness in laminated or coextruded structures
  3. SML = specific migration limits
  4. Therefore, the majority of the scientific literature on migration modeling is dedicated to the deterministic approach. In many cases, migration is governed by a mass transfer process called diffusion that can be described by FICK’s LAW Two constants partition coefficient and alpha at equilibrium Low Mw no longer homogenously distributed at the interface No transfer at the outer surface if migrant has lower volatility
  5. 2-3 orders of magnitude difference, this is explained by molecular size and shape. The higher, the lower the D Both of these models can be applied accurately to polyolefins
  6. Monte Carlo sampling based on random sampling Model output is the distribution of values
  7. PET, PEN, PS, PA are lower than polyolefins Polyolefins modeling more sensitive and faster results due to high migration rates : E.g. antioxidants modeling in polyolefins
  8. Paper migration is higher / faster To food and to atmosphere The retention behaviour of the substance in the paper matrix depends also on its interaction with fibres surface and, as mentioned before, the cellulose fibres have an overall negative charge due to carboxyl groups from the carbohydrates and the hydroxyl groups of the lignins. Thus, substances rich in electrons, such as naphthalene, tend to be repelled and are not retained by the fibre. As a consequence, these substances are less absorbed by the paper Tau system time parameter, Beta shape parameters Weibull model: Simple and flexible in determining mass transfer ptocessess where diffusion theories cannot explain.
  9. Migratest :Piringer’s model -> Designed to overestimate AKTS: Monolayers (freeware version), Up to 10 layers (licensed version) SMEWISE: Freeware
  10. Several orders of magnitude overestimation Values had a large margin of uncertainty Photoinitiator study has 20% m ore than actual values