use of migration modelling for food contact materials · uvitex ob 0,6 0,05 431 5 pp (random or...
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![Page 1: Use of Migration Modelling for food contact materials · Uvitex OB 0,6 0,05 431 5 PP (random or homo/ isotactic, diff from 6) 68320 Benzenepropanoic acid 3,5-bis(1,1-dimethylethyl)-4-hydroxy-](https://reader036.vdocuments.us/reader036/viewer/2022071421/611a35f3ed0ff565345e933d/html5/thumbnails/1.jpg)
Use of Migration Modelling for food contact materials
Exercises
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► Introduction to AKTS SML Software
► Estimation of diffusion coefficients
► Specific migration from plastics
► Migration from multilayer packaging
► Exercises
Content
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► Introduction to AKTS SML Software and Migration Modelling
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Migration ~ Diffusion
Mass transfer
simplifying assumption
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Migration ~ Diffusion
Migration process (Mass transfer)
● Diffusion process is the rate determining step
● Diffusion process is determined by:- mobility of the polymer(AP, polymer specific constant)
- size of the migrant(Mr, molecular weight)
- temperature(T, temperatur)
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2
2
x
cD
t
c
∂∂
⋅=∂∂
Fick's 2nd law of diffusion(one dimensional):
c - concentrationt - time
x - distanceD - diffusion coefficient
D
P - polymeric material
M - contacting medium
P M
Mass transfer ~ diffusion
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Diffusion models
» monolayer materials(monolayer)
D/K
» multilayer materials(multilayer)
(D/K)n
D,K - mass transfer constants
P M
migrant
DP
KP,M
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general diffusion model:
D/K/.../DD/K - polymer/liquidD/K/D - polymer/solidD/K/D/K - polymer/coating/liquid...(D/K)n/D - general
Diffusion models
polymeric materials in contact with ...
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D - diffusion coefficient [cm²/s]
D0 - pre-exponential factor
EA - activation energy [J]
R - gas constant [8,314 J/mol K]
T - temperature [K]
RT
EA
eDD
−
⋅= 0D RT
EA
eDD
−
⋅= 0D
Diffusion coefficient (how fast is the migration)
P M
migrant
DP
KP,M
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K - partition coefficient
c - concentration
P - polymeric material
M - contacting medium
∞ - at equilibrium
Partition coefficient (how far goes the migration)
∞
∞=,
,
,
M
P
MPc
cK
P M
migrant
DP
KP,M
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Solution of the diffusion equation
» » analytical solution
- only monolayer- only mean concentration in the contacting medium and the polymeric material(no concentration profile available)- no exchange cycles can be simulated
→ see J. Crank("Mathematics of Diffusion")
D/K
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H.S.Carslaw &J.C.Jaeger: Conduction of heat in solid
J. Crank: The Mathematics of Diffusion
Solution of the diffusion equation
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(D/K)n
» » numerical solution
- for multilayer materials- concentration profile available- exchange cycles can be simulated
→ see standard textbooks for Numerical Mathematicse.g. Finite Elements und Finite Differences algorithms
Solution of the diffusion equation
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Estimation of mass transfer constants
» Diffusion coefficients (DP)
Arrhenius DP=f(D0,EA,T)
Piringer DP=f(AP',tau,Mr,T)
Brandsch DP=f(Tg,M,T) - new
» Partition coefficients (KP,M)
worst case K=1, (VP<<VM)
Piringer K=f(p, Ma, Wa, GF)
Brandsch K=f(SW)
K=f(PO/W) - new
DP - diffusion coefficient
D0 - pre-exponential factor(Arrhenius)
EA - activation energy (Arrhenius)
T - temperature [K]
AP' - polymer specific constant(Piringer)
tau - polymer specific temperatureconstant (Piringer)
M - molecular weight [g/mol]
Mr - relative molecular weight
Tg, - glass temperature of polymer
KP,M - partition coefficient
VP - volume of polymer
VW - volume of medium
p - vapour pressure of migrant
SW - water solubility of migrant
PO/W - octanol/water- partitioncoefficient of migrant
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► must solve the diffusion equation numerically (partial differential equation, PDE)
→ the analytical solution of the diffusion equations serves as reference for validation
→ validation required, i.e. experimental examples must be reproduced correctly
Software Tools
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EU legislation (FCM 2002/72/EC, Article 8)
FOOD CONTACT MATERIALS
PRACTICAL GUIDE
“A PRACTICAL GUIDE FOR USERS OF EUROPEAN DIRECTIVES ”
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► Estimation of diffusion coefficients
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Migration ~ Diffusion
Migration process (Mass transfer)
● Diffusion process is the rate determining step
● Diffusion process is determined by:- mobility of the polymer(AP, polymer specific constant)
- size of the migrant(Mr, molecular weight)
- temperature(T, temperatur)
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D - diffusion coefficient [cm²/s]
D0 - pre-exponential factor
EA - activation energy [J]
R - gas constant [8,314 J/mol K]
T - temperature [K]
RT
EA
eDD
−
⋅= 0D RT
EA
eDD
−
⋅= 0D
Diffusion coefficient
P M
migrant
DP
KP,M
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Estimation of mass transfer constants
» Diffusion coefficients (DP)
Arrhenius DP=f(D0,EA,T)
Piringer DP=f(AP',tau,Mr,T)
Brandsch DP=f(Tg,M,T) - new
» Partition coefficients (KP,M)
worst case K=1, (VP<<VM)
Piringer K=f(p, Ma, Wa, GF)
Brandsch K=f(SW)
K=f(PO/W) - new
DP - diffusion coefficient
D0 - pre-exponential factor(Arrhenius)
EA - activation energy (Arrhenius)
T - temperature [K]
AP' - polymer specific constant(Piringer)
tau - polymer specific temperatureconstant (Piringer)
M - molecular weight [g/mol]
Mr - relative molecular weight
Tg, - glass temperature of polymer
KP,M - partition coefficient
VP - volume of polymer
VW - volume of medium
p - vapour pressure of migrant
SW - water solubility of migrant
PO/W - octanol/water- partitioncoefficient of migrant
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DP - Diffusion coefficient (D0 = 104 cm²/s)
AP= AP‘-τ/T - material specific constant(τ - material specific temperature constant)
Mr - relative molar mass of migrant in Dalton
T - temperature in K
EA - reference activation energy(= R·10454 = 86,9 kJ, R = 8,314 J/K·mol)
⋅⋅
−⋅+⋅−=TR
RMMADD rrPP
10454003.01351.0exp
3/2
0
Estimation of diffusion coefficients
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-14
-13
-12
-11
-10
-9
-8
-7
-6
0 20 40 60 80 100 120
Mr2/3
log
DP
1
23
AP‘=11,5 , ττττ=0
Estimation of diffusion coefficients (LDPE, RT)
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PE
-10,5
-10
-9,5
-9
-8,5
-8
-7,5
-7
150 200 250 300 350 400 450
Mr
log
Dp
log Dp ex LDPE
log Dp calc
AP‘=11,5, ττττ=0
Estimation of diffusion coefficients (LDPE, 40°C)
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PP
-10,5
-10
-9,5
-9
-8,5
-8
-7,5
-7
150 200 250 300 350 400 450
Mr
log
Dp
log Dp ex PP
log Dp calc
AP‘=13,1, ττττ=1577
Estimation of diffusion coefficients (PP, RT)
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real diffusions coefficient: DP <--> AP
„upper limit“ diffusion coefficient : DP* <--> AP*
- an „upper limit“ diffusions coefficient DP* gives a „worst case“ migration estimation
Legal requirements for AP-values
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0
5
10
15
20
25
30
35
40
4 5 6 7 8 9 10 11 12 13 14 15 16
AP'-valueno. values: 134mean value AP‘ = 11,29standard deviation = 1,76
confidence interval (95%) = 7,85 - 14,74 ( = MW ± 1,96*STABW)
AP‘* = 14,5
Upper limit AP*-values
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< 1
< 1
< 1
< 1
< 1
< 1
cP,0 [%]
< 100011.5PP(rubber)
< 120155713.1PP(random)
< 120155713.1PP(homo)
< 90157714.5HDPE
< 100011.5LLDPE
< 80011.5LDPE
T [°C]τAP´Polymer
FOOD CONTACT MATERIALS
PRACTICAL GUIDE
“A PRACTICAL GUIDE FOR USERS OF EUROPEAN DIRECTIVES ”
Upper limit AP*-values (polyolefines)
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< 1
< 1
< 1
< 1
< 1
cP,0 [%]
< 10002PA 6,6
< 17515575PEN
< 17515776PET
< 7001HIPS
< 7000PS
T [°C]τAP´Polymer
FOOD CONTACT MATERIALS
PRACTICAL GUIDE
“A PRACTICAL GUIDE FOR USERS OF EUROPEAN DIRECTIVES ”
Upper limit AP*-values (non-polyolefines)
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Polymer
AP’
s
AP’(max)
AP’(min)
N
t
AP’*
τ
LDPE 10.0 1.0 11 7.0 27 1.7 11.7 0
HDPE 10.0 1.9 12.6 5.0 49 1.68 13.2 1577
PP 9.4 1.8 12.9 6.2 53 1.68 12.4 1577
PET 2.2 2.5 7.2 -4.3 58 1.67 6.35 1577
PEN -0.34 2.4 3.8 -5.5 38 1.7 3.7 1577
PS -2.8 1.25 0.0 -6.5 32 1.7 -0.7 0
HIPS -2.7 1.67 0 -6.2 33 1.7 0.1 0
PA (6,6) -1.54 2.0 2.3 -7.7 31 1.7 1.9 0
Other Polymers (EU-Project Migration Modeling)
AP= AP'-ττττ/T Food Additives and Contaminants, 2005; 22(1): 73–90
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Diffusion properties of different
polymers can be compared
based on their AP-value,
i.e. mobility of the polymer
► high AP-values account for high mobility of the polymer (flexible polymers) and high diffusion coefficients respectively
► low AP-values account for low mobility of the polymer (rigid polymers) and low diffusion coefficients respectively
Migration process (Mass transfer)
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DP AP
[cm²/s]
gases ~ 10-1
liquids ~ 10-5 20
viscous liquids ~ 10-6 18
soft PVC ~ 10-7 16
Polymere T > Tg
LDPE ~ 10-9 11HDPE ~ 10-10 9PP ~ 10-11 7
Polymere T < Tg
PA ~ 10-13 2PS ~ 10-14 0PET ~ 10-15 -2rigid PVC ~ 10-16 -4(Tg - glas temperature)
Diffusion coefficients (at T=20°C, Mr=300 g/mol)
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► Specific migration from plastics
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PARTNERS :
Fraunhofer Gesellschaft D (IVV)Pira International UK (PIRA)MAFF-CSL UK (CSL)FABES Forschungs-GmbH D (FABES)BIT-FCA B/EU (FCA)
Certified Reference Materials for the specific migration testingof plastics for food packaging
PROJECT G6RD-CT-2000-00411
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List of candidate materials
No Polymer PM/REF
No
Additive/Monomer/Test Substance Brand name e.g. SML
(mg/kg)
proposed
level %
MW Proposed
film/plaque
thickness
(range µm)
thickness
of
materials
(µm)
Form Production
mode
Commercial
availability/
possiblity of
production
T max
°C
Simulant
(migration
test)
Time/Temp
(migration
test)
1 LDPE 68320 Benzenepropanoic acid 3,5-bis(1,1-
dimethylethyl)-4-hydroxy- octadecyl ester
Irganox 1076 6 0,15 531 300-500 300 Film flat film Ind., tailor
made
<100 olive oil 2 h / 100°C
74240 Tris(2,4-di-tert-butylphenyl)phosphit Irgaphos 168 0,1 647
2 LDPE Diphenylbutadiene 0,01 206 500 500 film flat film IVV <100 olive oil 24 h / 5°C
3 HDPE 68320 Benzenepropanoic acid 3,5-bis(1,1-
dimethylethyl)-4-hydroxy- octadecyl ester
Irganox 1076 6 0,15 531 300-500 film flat film Ind., tailor
made
<120 olive oil 10 d / 40°C
74240 Tris(2,4-di-tert-butylphenyl)phosphit Irgaphos 168 0,1 647
4 HDPE 61600 2-hydroxy-4-n-octyloxybenzophenone Chimassorb 81 6 0,1 326 300-500 350 film flat film Pira <120 olive oil 2 h / 100°C
38560 2,5-bis(5-tert-butyl-2-
benzoxazolyl)thiophene
Uvitex OB 0,6 0,05 431
5 PP (random or
homo/ isotactic,
diff from 6)
68320 Benzenepropanoic acid 3,5-bis(1,1-
dimethylethyl)-4-hydroxy- octadecyl ester
Irganox 1076 6 0,15 531 300-500 380 film flat film Pira <120 olive oil 1 h / 100 °C
74240 Tris(2,4-di-tert-butylphenyl)phosphit Irgaphos 168 0,1 647
6 PP 61600 2-hydroxy-4-n-octyloxybenzophenone Chimassorb 81 6 0,1 326 300-500 380 film flat film Pira <120 olive oil 2 h / 100°C
(random or
homo/isotactic,
diff from 5)
38560 2,5-bis(5-tert-butyl-2-
benzoxazolyl)thiophene
Uvitex OB 0,6 0,05 431
7 PP 52720 Erucamide 0,05 337 300-500 440 film flat film IVV <120 olive oil 1 h / 70°C
random 94960 Trimethylolpropane 6 0,05 134 300-500 <120 aqueous 1 h / 100°C
8 HIPS, 6-7 %
mineral oil
68320 Benzenepropanoic acid 3,5-bis(1,1-
dimethylethyl)-4-hydroxy- octadecyl ester
Irganox 1076 6 0,15 370 50-150 2000 plaque injection
mould
Ind., tailor
made
<70 olive oil 2 h / 70°C
9 HIPS 1 % mineral
oil
24610 Styrene 104 50-150 2000 plaque injection
mould
Ind., tailor
made
<70 olive oil 10 d / 20°C
10 GPPS 24610 Styrene 104 50-150 2000 plaque injection
mould
Ind., tailor
made
<70 olive oil 10 d / 20°C
11 PET 16990/
15760
Mono-/Diethyleneglycol 30 film Ind.,
industrial
product
<70 olive oil to be checked,
measurable
migration
PET trimer
12 PET 51700 2-(4,6-Diphenyl-1,3,5-triazin-2-yl)-5-
hexyloxy-phenol
Tinuvin 1577 0,05 0,1 425 50-150 20 film Ind.,
industrial
product
higher
temp after
pre-
condition?
olive oil to be checked,
measurable
migration
13 PVC rigid 94400 Tin-organic stabilizer (total tin + specific) 50-150 250 film Ind. product <60 aqueous 24 h / 40°C
14 PVC clingfilm 31920 Di-(2-ethylhexyl)-adipat DEHA 18 10-20 370 200-500 500 film flat film,
pressed
Ind., tailor
made
<25 olive oil 10 d / 5°C
15 PA nylon 14200 caprolactam 15 113 100-200 120 film Ind. product <150 aqueous 120 min /
100°C
16 PA 12 19490 laurolactam 197 100-200 200 film Ind. product <100 aqueous 120 min / 70°C
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Polymer matrix : HDPE
HDPE
type 1: ρ = 0,948
d = 1043 µm
migrants: Irganox 1076 (antioxidant)
Irgafos 168 (antioxidant)
type 2: ρ = 0,933
d = 356 µm
migrants: Chimassorb 81 (UV-absorber)
Uvitex OB (optical brightener)
![Page 36: Use of Migration Modelling for food contact materials · Uvitex OB 0,6 0,05 431 5 PP (random or homo/ isotactic, diff from 6) 68320 Benzenepropanoic acid 3,5-bis(1,1-dimethylethyl)-4-hydroxy-](https://reader036.vdocuments.us/reader036/viewer/2022071421/611a35f3ed0ff565345e933d/html5/thumbnails/36.jpg)
O OH
O
CH3
CH3
CH3
CH3
N
O N
O
S
CH3
CH3
CH3
P
O
O
O
CH3
CH3
CH3CH3
CH3
CH3
CH3
CH3
CH3
CH3
CH3
CH3
CH3CH3
CH3
CH3 CH3
CH3
Structure of migrants
CH3
CH3
CH3CH3
CH3
CH3
OOCH3
OH
UvitexOB
Irgafos 168
Irganox 1076
Chimassorb81
![Page 37: Use of Migration Modelling for food contact materials · Uvitex OB 0,6 0,05 431 5 PP (random or homo/ isotactic, diff from 6) 68320 Benzenepropanoic acid 3,5-bis(1,1-dimethylethyl)-4-hydroxy-](https://reader036.vdocuments.us/reader036/viewer/2022071421/611a35f3ed0ff565345e933d/html5/thumbnails/37.jpg)
Experimental considerations
migration cell (one sided)
area, A = 48 cm²volume, V = 10 ml
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Migration of Irganox 1076 into ethanol 95%
0
500
1000
1500
2000
2500
3000
3500
4000
0 2 4 6 8 10 12
time [days]
co
ncen
trati
on
[µg
/dm
²]
40°C (exp.A)
40°C (exp.B)
60°C (exp.A)
60°C (exp.B)
80°C (exp.A)
80°C (exp.B)
CH3
CH3
CH3CH3
CH3
CH3
OOCH3
OH
![Page 39: Use of Migration Modelling for food contact materials · Uvitex OB 0,6 0,05 431 5 PP (random or homo/ isotactic, diff from 6) 68320 Benzenepropanoic acid 3,5-bis(1,1-dimethylethyl)-4-hydroxy-](https://reader036.vdocuments.us/reader036/viewer/2022071421/611a35f3ed0ff565345e933d/html5/thumbnails/39.jpg)
Migration of Irgafos 168 into ethanol 95%
0
100
200
300
400
500
600
700
800
0 2 4 6 8 10 12
time [days]
co
ncen
trati
on
[µg
/dm
²]
40°C (exp.A)
40°C (exp.B)
60°C (exp.A)
60°C (exp.B)
80°C (exp.A)
80°C (exp.B)
P
O
O
O
CH3
CH3
CH3
CH3
CH3
CH3
CH3
CH3
CH3
CH3
CH3
CH3
CH3CH3
CH3
CH3 CH3
CH3
![Page 40: Use of Migration Modelling for food contact materials · Uvitex OB 0,6 0,05 431 5 PP (random or homo/ isotactic, diff from 6) 68320 Benzenepropanoic acid 3,5-bis(1,1-dimethylethyl)-4-hydroxy-](https://reader036.vdocuments.us/reader036/viewer/2022071421/611a35f3ed0ff565345e933d/html5/thumbnails/40.jpg)
Migration of Chimassorb 81 into ethanol 95%
0
500
1000
1500
2000
2500
3000
3500
0 2 4 6 8 10 12
time [days]
co
ncen
tra
tio
n [
µg
/dm
²]
40°C (exp.A)
40°C (exp.B)
60°C (exp.A)
60°C (exp.B)
80°C (exp.A)
80°C (exp.B)
O OH
O
CH3
![Page 41: Use of Migration Modelling for food contact materials · Uvitex OB 0,6 0,05 431 5 PP (random or homo/ isotactic, diff from 6) 68320 Benzenepropanoic acid 3,5-bis(1,1-dimethylethyl)-4-hydroxy-](https://reader036.vdocuments.us/reader036/viewer/2022071421/611a35f3ed0ff565345e933d/html5/thumbnails/41.jpg)
Migration of Uvitex OB into ethanol 95%
0
200
400
600
800
1000
1200
0 2 4 6 8 10 12
time [days]
co
ncen
trati
on
[µg
/dm
²]
40°C (exp.A)
40°C (exp.B)
60°C (exp.A)
60°C (exp.B)
80°C (exp.A)
80°C (exp.B)
CH3
CH3
CH3
N
O N
O
S
CH3
CH3
CH3
![Page 42: Use of Migration Modelling for food contact materials · Uvitex OB 0,6 0,05 431 5 PP (random or homo/ isotactic, diff from 6) 68320 Benzenepropanoic acid 3,5-bis(1,1-dimethylethyl)-4-hydroxy-](https://reader036.vdocuments.us/reader036/viewer/2022071421/611a35f3ed0ff565345e933d/html5/thumbnails/42.jpg)
- the migration process follows the laws of diffusion
- the liquid is a well mixed
- data set: dP [µm]
ρP [g/cm³]VF [cm³]
ρF [g/cm³]A [g/cm³]t [days]T [°C]
food
simulant
Migrant
HDPE
DP
KP,F
Migrationexperiment
Migration modelling
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Fundamental physical constants
Fitting procedure by variation of the diffusion
coefficient, DP and the partition coefficient, KP,F
( )
−
+++
−
+= ∑
∞
=12
2
220,
,exp
1
121
1 n P
nP
n
PPP
tL
d
qtD
qdc
A
m
αααα
αα
ρLP
PL
K
VV
,
/=α
![Page 44: Use of Migration Modelling for food contact materials · Uvitex OB 0,6 0,05 431 5 PP (random or homo/ isotactic, diff from 6) 68320 Benzenepropanoic acid 3,5-bis(1,1-dimethylethyl)-4-hydroxy-](https://reader036.vdocuments.us/reader036/viewer/2022071421/611a35f3ed0ff565345e933d/html5/thumbnails/44.jpg)
0
500
1000
1500
2000
2500
3000
3500
4000
0 2 4 6 8 10 12
time [days]
co
ncen
trati
on
[µg
/dm
²]
40°C (exp.A)
40°C (exp.B)
40°C (calc.)
60°C (exp.A)
60°C (exp.B)
60°C (calc.)
80°C (exp.A)
80°C (exp.B)
80°C (calc.)
Modelling of Irganox 1076 migration
CH3
CH3
CH3CH3
CH3
CH3
OOCH3
OHcP,0 = 850 ppm (8404 µg/dm²)
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Modelling of Irgafos 168 migration
0
100
200
300
400
500
600
700
800
0 2 4 6 8 10 12
time [days]
co
ncen
trati
on
[µg
/dm
²]
40°C (exp.A)
40°C (exp.B)
40°C (calc.)
60°C (exp.A)
60°C (exp.B)
60°C (calc.)
80°C (exp.A)
80°C (exp.B)
80°C (calc.)
P
O
O
O
CH3
CH3
CH3
CH3
CH3
CH3
CH3
CH3
CH3
CH3
CH3
CH3
CH3CH3
CH3
CH3 CH3
CH3
cP,0 = 517 ppm (5112 µg/dm²)
![Page 46: Use of Migration Modelling for food contact materials · Uvitex OB 0,6 0,05 431 5 PP (random or homo/ isotactic, diff from 6) 68320 Benzenepropanoic acid 3,5-bis(1,1-dimethylethyl)-4-hydroxy-](https://reader036.vdocuments.us/reader036/viewer/2022071421/611a35f3ed0ff565345e933d/html5/thumbnails/46.jpg)
Modelling of Chimassorb 81 migration
0
500
1000
1500
2000
2500
3000
3500
0 2 4 6 8 10 12
time [days]
co
ncen
trati
on
[µg
/dm
²]
40°C (exp.A)
40°C (exp.B)
40°C (calc.)
60°C (exp.A)
60°C (exp.B)
60°C (calc.)
80°C (exp.A)
80°C (exp.B)
80°C (calc.)
O OH
O
CH3
cP,0 = 935 ppm (3106 µg/dm²)
![Page 47: Use of Migration Modelling for food contact materials · Uvitex OB 0,6 0,05 431 5 PP (random or homo/ isotactic, diff from 6) 68320 Benzenepropanoic acid 3,5-bis(1,1-dimethylethyl)-4-hydroxy-](https://reader036.vdocuments.us/reader036/viewer/2022071421/611a35f3ed0ff565345e933d/html5/thumbnails/47.jpg)
Modelling of Uvitex OB migration
0
200
400
600
800
1000
1200
0 2 4 6 8 10 12
time [days]
co
ncen
trati
on
[µg
/dm
²]
40°C (exp.A)
40°C (exp.B)
40°C (calc.)
60°C (exp.A)
60°C (exp.B)
60°C (calc.)
80°C (exp.A)
80°C (exp.B)
80°C (calc.)
CH3
CH3
CH3
N
O N
O
S
CH3
CH3
CH3
cP,0 = 471 ppm (1564 µg/dm²)
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Migrant
40°C 60°C 80°C 40°C 60°C 80°C
Irganox 1076 3,9E-11 4,3E-10 3,3E-09 15,0 3,0 0,1
Irgafos 168 2,1E-12 7,2E-11 4,5E-10 80,0 50,0 3,0
Chmiassorb 81 5,0E-10 2,7E-09 1,9E-08 0,1 0,1 0,1
Uvitex OB 4,5E-11 4,5E-10 4,7E-09 1,0 1,0 0,1
Diff.coef Part.coeff
Fundamental physical constants
Fitting procedure by variation of the diffusion coefficient, DP
and the partition coefficient, KP,F gives for the best fit:
![Page 49: Use of Migration Modelling for food contact materials · Uvitex OB 0,6 0,05 431 5 PP (random or homo/ isotactic, diff from 6) 68320 Benzenepropanoic acid 3,5-bis(1,1-dimethylethyl)-4-hydroxy-](https://reader036.vdocuments.us/reader036/viewer/2022071421/611a35f3ed0ff565345e933d/html5/thumbnails/49.jpg)
DP - Diffusion coefficient (D0 = 104 cm²/s)
AP= AP‘-τ/T - material specific constant(τ - material specific temperature constant)
Mr - relative molar mass of migrant in Dalton
T - temperature in K
EA - reference activation energy(= R·10454 = 86,9 kJ, R = 8,314 J/K·mol)
⋅⋅
−⋅+⋅−=TR
RMMADD rrPP
10454003.01351.0exp
3/2
0
Diffusion modelling
► estimation of diffusion coefficients
![Page 50: Use of Migration Modelling for food contact materials · Uvitex OB 0,6 0,05 431 5 PP (random or homo/ isotactic, diff from 6) 68320 Benzenepropanoic acid 3,5-bis(1,1-dimethylethyl)-4-hydroxy-](https://reader036.vdocuments.us/reader036/viewer/2022071421/611a35f3ed0ff565345e933d/html5/thumbnails/50.jpg)
Migrant τ 40°C 60°C 80°C 40°C 60°C 80°C
Irganox 1076 12,5 12,6 12,6 1577 1577 1577
Irgafos 168 10,5 11,7 11,5 1577 1577 1577
Chmiassorb 81 13,2 12,6 12,5 1577 1577 1577
Uvitex OB 11,8 11,8 12,1 1577 1577 1577
Ap'
Polymer specific constant, AP'
00,7standard deviation
157713,5upper limit values *)
157712,1mean value
τAP’
The influence of the migrant structure on the diffusion coefficient is within the standard deviation of ± 10%.
![Page 51: Use of Migration Modelling for food contact materials · Uvitex OB 0,6 0,05 431 5 PP (random or homo/ isotactic, diff from 6) 68320 Benzenepropanoic acid 3,5-bis(1,1-dimethylethyl)-4-hydroxy-](https://reader036.vdocuments.us/reader036/viewer/2022071421/611a35f3ed0ff565345e933d/html5/thumbnails/51.jpg)
0
5
10
15
20
25
30
35
40
4 5 6 7 8 9 10 11 12 13 14 15 16
AP'-value
no. values: 134mean value AP‘ = 11,29
standard deviation = 1,76confidence interval (95%) = 7,85 - 14,74 ( = MW ± 1,96*STABW)
AP‘* = 14,5
Upper limit AP-values
![Page 52: Use of Migration Modelling for food contact materials · Uvitex OB 0,6 0,05 431 5 PP (random or homo/ isotactic, diff from 6) 68320 Benzenepropanoic acid 3,5-bis(1,1-dimethylethyl)-4-hydroxy-](https://reader036.vdocuments.us/reader036/viewer/2022071421/611a35f3ed0ff565345e933d/html5/thumbnails/52.jpg)
► Migration from multilayer Packaging:
Invisible set-off &
Functional Barrier
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Tube technology
decorative
printing
protective coating
Al
authorized substancespermitted substances
![Page 54: Use of Migration Modelling for food contact materials · Uvitex OB 0,6 0,05 431 5 PP (random or homo/ isotactic, diff from 6) 68320 Benzenepropanoic acid 3,5-bis(1,1-dimethylethyl)-4-hydroxy-](https://reader036.vdocuments.us/reader036/viewer/2022071421/611a35f3ed0ff565345e933d/html5/thumbnails/54.jpg)
protective coating
Al
decorative
printing
Set-off during storage in the stack
authorised substancespermitted substances
sto
rag
e tim
e
production
set-off set-off
![Page 55: Use of Migration Modelling for food contact materials · Uvitex OB 0,6 0,05 431 5 PP (random or homo/ isotactic, diff from 6) 68320 Benzenepropanoic acid 3,5-bis(1,1-dimethylethyl)-4-hydroxy-](https://reader036.vdocuments.us/reader036/viewer/2022071421/611a35f3ed0ff565345e933d/html5/thumbnails/55.jpg)
Migration testing for compliance
migration experimentfoo
dsim
ula
nt
→→→→ food contact layer contamination depending on sample history
→→→→ detectable migration of authorised and permitted substances
→→→→ must comply with Article 3 of the framework regulation (EC) 1935/2004
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Functional barrier concept
Article 7a
» Only glass and some metals may ensure complete blockage of migration. (absolute barrier)
» Plastics may be partial functional barriers with properties and effectiveness to be assessed and may help reducing the migration of a substance below a SML or a limit of detection.
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► FB consists of one or several layers,
► FB assures that the migration of positively listed
substances does mot exceed the specific migration limit
► FB assures that the migration of substances not listed
does not exceed the limit of 0,01 mg/kg food (including
set-off)
► not allowed are substances classified as proved or
suspect "carcinogenic", “mutagenic” or “toxic to
reproduction”, substances in Annex I to Council Directive
67/548/EEC
► FB prevents the migration of "not intentionally added
substances" (NIAS = impurities, decomposition products,
etc.), i.e. keeps their migration not detectable (detection
limit 0,01 mg/kg food).
Functional barrier concept
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contact medium
Direct and indirect contact
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t
A
m tF ,
2d 10d
concave
I > 0
Food contact layer
two data points:
2d@60°C10d@60°C
Functional barrier concept
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t
θθθθ
A
m tF ,
2d 10d
convex
concave
I > 0
I < 0
two data points:
2d@60°C10d@60°C
printing ink
Functional barrier concept
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FB
FB
D
d 2
6
1⋅=θ
dFB - thickness
DFB - diffusions coefficient
θθθθ - "lag time"
Simulanz /Lebensmittel
Migrant
Kunststoff
DP
KFB,F
FBSimulanz /
Lebensmittel
Migrant
Kunststoff
DP
KFB,F
FBSimulanz /
Lebensmittel
Migrant
Kunststoff
DP
KFB,F
FBSimulanz /
Lebensmittel
Migrant
Kunststoff
DP
KFB,F
FBSimulanz /
Lebensmittel
Migrant
Kunststoff
DP
KFB,F
FBSimulanz /
Lebensmittel
Migrant
Kunststoff
DP
KFB,F
FB
KP,FB
DFB
"lag time"
Theoretical understanding
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DEHA, Verbund 1 (NC/20µmOPP/Adh/30µmOPP)
21Tage bei 20°C, Ethanol95%
0
100
200
300
400
500
600
700
0 5 10 15 20 25 30 35 40
Zeit [Tage]
Mig
rati
on
[µ
g/d
m²]
exp.
calc. N
Functional barrier
multilayer structure:(from left to right)
ink(1µm)
OPP(20µm)adh.(2,5µm)
OPP(30µm)
time [days]
one sided migration testfood simulant (D) substitute: 95% ethanoltemperature: 20°Cmigrant: DEHA
migration kinetic
O
O
O
O
CH3
CH3
CH3 CH3
![Page 63: Use of Migration Modelling for food contact materials · Uvitex OB 0,6 0,05 431 5 PP (random or homo/ isotactic, diff from 6) 68320 Benzenepropanoic acid 3,5-bis(1,1-dimethylethyl)-4-hydroxy-](https://reader036.vdocuments.us/reader036/viewer/2022071421/611a35f3ed0ff565345e933d/html5/thumbnails/63.jpg)
DEHA, Verbund 1 (NC/20µmOPP/Adh/30µmOPP)
10 Tage bei 40°C, Ethanol95%
0
500
1000
1500
2000
2500
0 5 10 15 20 25 30 35 40 45
Zeit [Tage]
Mig
rati
on
[µ
g/d
m²]
calc. N
exp.
time [days]
one sided migration testfood simulant (D) substitute: 95% ethanoltemperature: 40°Cmigrant: DEHA
multilayer structure:(from left to right)
ink(1µm)
OPP(20µm)adh.(2,5µm)
OPP(30µm)
Functional barrier
migration kinetic
O
O
O
O
CH3
CH3
CH3 CH3
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DEHA, Verbund 1 (NC/20µmOPP/Adh/30µmOPP)
7 Tage bei 60°C, Ethanol95%
0
500
1000
1500
2000
2500
0 1 2 3 4 5 6 7 8
Zeit [Tage]
Mig
rati
on
[µ
g/d
m²]
exp.
calc. N
time [days]
one sided migration testfood simulant (D) substitute: 95% ethanoltemperature: 60°Cmigrant: DEHA
multilayer structure:(from left to right)
ink(1µm)
OPP(20µm)adh.(2,5µm)
OPP(30µm)
Functional barrier
migration kinetic
O
O
O
O
CH3
CH3
CH3 CH3
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Simulation of Migration (set-off)
PE/Druck/Karton/PE/Al/PE
Fachverband Kartonverpackungen für flüssige Nahrungsmittel e.V. (FKN)
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2-Isopropyl thioxanthone
(ITX)
Simulation of Migration (set-off)
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104 µg/kg Lebensmittel
Simulation of Migration (set-off)
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Validation of Simulation
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Validation of Simulation
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► Compliance Flow Chart
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material
specifications
initial
concentrations
of migrants
packaging application
(type of food,
temperatures, times)
Determination of
migration potential
migration scenario
via mathematical modelling
compare M vs SML
Quick test
(worse case)
kinetical migration test
(also for black
box approach)
M < SML?
compliance
yes
compliance
no
estimation of migration M
Functional
Barrier
M = ca. SMLM << SMLM = 0
M < SML?
yes
no
ja no
direct evaluation:
however, further
validation needed
today:
future:
no
set-off
effect
set-off
Effect
yes
flow diagram:
information’s
modelling migration
(complete transfer)
experimental testing
assessment
Compliance assessment concept
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material
specifications
initial
concentrations
of migrants
packaging application
(type of food,
temperatures, times)
Determination of
migration potential
migration scenario
via mathematical modelling
information’s:
materials specifications(identity and thickness of
layers)
initial concentration of
migrants
packaging applications (food type, storage
temperature and time)
(exp. determination of initial concentration)
migration modelling:
Compliance assessment concept
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migration scenario
via mathematical modelling
compare M vs SML
Quick test
(worse case)
kinetical migration test
(also for black
box approach)
M < SML?
compliance
yes
compliance
no
estimation of migration M
Functional
Barrier
M = ca. SMLM << SMLM = 0
M < SML?
yes
no
ja no
direct evaluation:
however, further
validation needed
today:
future:
no
set-off
effect
set-off
Effect
yes
migration modelling:
no set-offwith set-offcomplete transferquick test
migration kinetic
assessment:
compliant YES/NO
Compliance assessment concept
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► Exercises
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Ex. 1 - Monolayer Plastic Food Contact Material
A film of LDPE with a thickness of 100 µm is used for packing sandwiches with fatty substances on the surface with an area to volume ratio of A/V = 6 dm-1.
This kind of food is stored at 4°C for maximum 7 days.
It is known that the film contains two additives:PM-ref. No 68320 / SML = 6 mg/kg foodPM-ref. No 74240 / SML = 60 mg/kg food)
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plastic material (P): LDPE
density of P: roP = 0.945
AP*-value: AP'* = 11.5 (polymer specific constant)
tau = 0 (polymer specific temperature constant)
thickness: d = 0.01 cm (= 100 µm)
migrants: (a) PM-ref. No 68320 (molecular weight M=531)(Octadecyl-3-(3,5-di-tertbutyl-4-hydroxyphenyl)propionate)
(b) PM-ref. No 74240 (molecular weight M=647)(Phosphorous acid, tris(2,4-di-tertbutylphenyl)ester)
initial concentration: cP,0 = 5000 mg/kg (= ppm)
contact area: A = 6 dm²
volume of food (F): V = 1 l (food or food simulant)
density of F: roF = 1.0 (by definition in regulation)
KP,F*: K = 1 for olive oil
K = 1000 for water, ethanol 10%, acetic acid 3%
Ex. 1 - Information & Inputs
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Q1: Determine conventional test conditions (time, temperature, simulant) according to the testing directives (82/711 and 85/572 including amendments).
Q2: Estimate the diffusion coefficients of the two additives at the temperature (from Q1) based on the polymer specific constant of the plastic material.
Q3: Estimate the specific migration of the two additives into one fatty and one aqueous food simulant.
Q4: Make the compliance evaluation.
Q5: Estimate time (and cost) savings compared to the experimental approach.
Ex. 1 - Questions
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Q1: Determine conventional test conditions (time, temperature, simulant) according to the testing directives (82/711 and 85/572 including amendments).
A1: time - 10 daystemperature - 5°C
Ex. 1 - Q1 Answers
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Q2: Estimate the diffusion coefficients of the two additives at the temperature (from Q1) based on the polymer specific constant of the plastic material.
A2: - start software and select "start"- select "new project"- select number of layers = 1- select "layer properties"- select diffusion coefficient "AP"- select LDPE- type in temperature- type in molecular weight of additive- select "OK"
Ex. 1 - Q2 Answers
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Ex. 1 - Q2 Answers
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Ex. 1 - Q2 Answers
FO
OD
monolayerPACKAGING
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Ex. 1 - Q2 Answers
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Ex. 1 - Q2 Answers
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Q2: Estimate the diffusion coefficients of the two additives at the temperature (from Q1) based on the polymer specific constant of the plastic material.
R2: PM-ref. No 68320 - DP = 3.30e-11 cm²/sPM-ref. No 74240 - DP = 1.35e-11 cm²/s
Ex. 1 - Q2 Results
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Q3: Estimate the specific migration of the two additives into one fatty and one aqueous food simulant.
A3: - select "layer properties"- type in thickness, d = 100 µm- type in density of plastic, roP = 0.945- type in initial concentration of additive, cP,0=5000 ppm- type in partition coefficient, KP,F = 1- select "OK"
- select "packaging geometry"- check "Rectangular"- select "OK"- type in length, width and height- select "NEXT"
Ex. 1 - Q3 Answers
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Q3: continued
A3: - change to "Calculate"- check "T-iso"- type in temperature = 5°C- select time unit -days-- type in time = 10- select "Run Finite Element Analysis"
Ex. 1 - Q3 Answers
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Ex. 1 - Q3 Answers
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Ex. 1 - Q3 Answers
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Ex. 1 - Q3 Answers
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Ex. 1 - Q3 Answers
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Ex. 1 - Q3 Answers
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Ex. 1 - Q3 Answers
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concentration
profile
Ex. 1 - Q3 Answers
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time
dependentmigration
Ex. 1 - Q3 Answers
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Ex. 1 - Q3 Answers
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concentration
profile
Ex. 1 - Q3 Answers
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time
dependentmigration
Ex. 1 - Q3 Answers
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Ex. 1 - Q3 Results
Q3: Estimate the specific migration of the two additives into one fatty and one aqueous food simulant.
R3: KP,F = 1PM-ref. No 68320 - mF,t = 2.82 mg/dm²PM-ref. No 74240 - mF,t = 1.81 mg/dm²
KP,F = 1000PM-ref. No 68320 - mF,t = 0.651 mg/dm²PM-ref. No 74240 - mF,t = 0.589 mg/dm²
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Ex. 1 - Answers
Q4: Make the compliance evaluation.
A4:
Q5: Estimate time (and cost) savings compared to the experimental approach.
A5: Estimated time savings 99%Estimated costs savings 50%
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Ex. 2 - Monolayer Plastic Food Contact Material
An empty baker made of PS is to be evaluated with respect to its
compliance when intended for being in contact with milk products
(yoghurt, and such products in association with fruit and fruit
products) as categorized with the reference number 07.02 in the
Directive 85/572/EEC. The product must be stored at 8°C. The baker with a volume of 500 ml has a conic geometry and a wall
thickness of 1 mm.
The test conditions in conformity with the EU Directives are:
10 days at 20°C with simulant B (acetic acid 3%) and simulant D (ethanol 50%).
Which information can mathematical modeling provide with
respect to specific migration of an additive like Tinuvin P, PM-Ref No 61440, (2-(2;-Hydroxy-5-methylphenyl)benzotriazole) with the
smallest molecular weight (M = 225 g/mol) for which it can be
assumed that it migrates with the highest rate.
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plastic material (P): PS
density of P: roP = 1.1
AP*-value: AP'* = 0 (polymer specific constant)
tau = 0 (polymer specific temperature constant)
thickness: d = 0.1 cm (= 1000 µm)
migrants: (a) PM-ref. No 61440 (molecular weight M = 225)(2-(2;-Hydroxy-5-methylphenyl)benzotriazole)
initial concentration: cP,0 = 5000 mg/kg (= ppm)
contact area: A = to be calculated - conic trunk packaging:
(d = 6.8 cm; D = 8.8 cm; h = 10.5 cm)
volume of food (F): V = to be calculated - conic trunk packaging:(d = 6.8 cm; D = 8.8 cm; h = 10.5 cm)
density of F: roF = 1.0 (by definition in regulation)
diffusion coefficient in F: DF = 1e-4 for food simulants (liquid)DF = 1e-6 for yoghurt (high viscous food)
partition coefficient (KP,F*): K = 1 yoghurt and ethanol 50%
K = 1000 for acetic acid 3%
Ex. 2 - Information & Inputs
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Ex. 2 - Questions
Q1: Estimate the diffusion coefficients of the additive at the temperature (T = 20°C) based on the polymer specific constant of the plastic material. Make use of the additives list available in the software.
Q2: Estimate the specific migration of the additive into the food simulants (acetic acid 3% and ethanol 50%).
Q3: Estimate the specific migration of the additive into the food (yoghurt).
Q4: Discuss the results.
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Q1: Estimate the diffusion coefficients of the additive at the temperature (T = 20°C) based on the polymer specific constant of the plastic material. Make use of the additives list available in the software.
A1: - start software and select "start"- select "new project"- select number of layers = 1- select "layer properties"- select diffusion coefficient "AP"- select PS- type in temperature- select "EU-list"- check "by reference number"- type in PM ref No = 61440
Ex. 2 - Q1 Answers
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Q1: continued
A1: - select "OK"- select "OK"- select "OK"- type in thickness, d = 1000 µm- type in density of plastic, roP = 1.1- type in initial concentration of additive, cP,0=5000 ppm- type in partition coefficient, K = 1- select "OK"- select "packaging geometry"- check "Truncated cone"- select "OK"- type in small diameter, d; big diameter, D; and height, h- select "NEXT"
Ex. 2 - Q1 Answers
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Q1: continued
A1: - change to "Calculate"- check "T-iso"- type in temperature = 20°C- select time unit -days-- type in time = 10- select "Run Finite Element Analysis"
Ex. 2 - Q1 Answers
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Ex. 2 - Q1 Answers
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Ex. 2 - Q1 Answers
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Ex. 2 - Q1 Answers
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Ex. 2 - Q1 Answers
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Ex. 2 - Q1 Results
Q1: Estimate the diffusion coefficients of the additive at the temperature (T = 20°C) based on the polymer specific constant of the plastic material. Make use of the additives list available in the software.
R1: PM-ref. No 61440 - DP = 4.32e-14 cm²/s
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Ex. 2 – Q2 Answers
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Ex. 2 – Q2 Answers
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Ex. 2 – Q2 Answers
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Ex. 2 – Q2 Answers
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Ex. 2 – Q2 Answers – ethanol 50%
concentration
profile
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Ex. 2 – Q2 Answers – ethanol 50%
time
dependentmigration
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Ex. 2 – Q2 Answers – acetic acid 3%
concentration
profile
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Ex. 2 – Q2 Answers – acetic acid 3%
time
dependentmigration
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Ex. 2 - Q2 Results
Q2: Estimate the specific migration of the two additives into one fatty and one aqueous food simulant.
R2: ethanol 50%, KP,F = 1, DF = 1e-4 cm²/sPM-ref. No 61440 - mF,t = 0,847 mg/kg
acetic acid 3%, KP,F = 1000, DF = 1e-4 cm²/s PM-ref. No 61440 - mF,t = 0,754 mg/kg
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Ex. 2 – Q3 Answers – yoghurt
concentration
profile
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Ex. 2 – Q3 Answers – yoghurt
time
dependentmigration
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Ex. 2 – Q3 Results
Q3: Estimate the specific migration of the additive into the food (yoghurt).
R3: yoghurt, KP,F = 1, DF = 1e-6 cm²/sPM-ref. No 61440 - mF,t = 0,847 mg/kg
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Ex. 2 – Q4 Results
Q4: Discuss the results
R4: yoghurt, KP,F = 1, DF = 1e-6 cm²/sPM-ref. No 61440 - mF,t = 0,847 mg/kg
ethanol 50%, KP,F = 1, DF = 1e-4 cm²/sPM-ref. No 61440 - mF,t = 0,847 mg/kg
acetic acid 3%, KP,F = 1000, DF = 1e-4 cm²/s PM-ref. No 61440 - mF,t = 0,754 mg/kg
The migration into acetic acid 3% is approximate 10% lower compared to ethanol 50% due to the higher partition coefficient (lower solubility) of the additive.
The migration into ethanol 50% is equal to the food yoghurt because the slightly lower diffusion coefficient in the yoghurt has no significant influence on the migration of the additive.
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Ex. 3 - Monolayer Plastic Food Contact Material
A steam sterilizable container with a capacity of 500 ml and a
cylindrical form, with a maximum wall thickness of 2 mm is used
for liquid or paste with fatty substances on the surface, according
to reference number 08.03 in the Directive 85/572/EEC. The
container has a PP label. The additives used are Irganox 1076 (0.06 %) and Irgafos 168 (0.1 %).
This information was obtained from the producer of the article.
Compliance testing of the above article according to Directive
97/48/EEC requires test conditions of 2 h at 121°C followed by
10 days at 40°C using simulant D, olive oil.
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plastic material (P): PP
density of P: roP = 0.91
AP*-value: AP'* = 13.1 (polymer specific constant)
tau = 1577 (polymer specific temperature constant)
thickness: d = 0.2 cm (= 2000 µm)
migrants: (a) PM-ref. No 68320 (molecular weight M=531)(Octadecyl-3-(3,5-di-tertbutyl-4-hydroxyphenyl)propionate)
(b) PM-ref. No 74240 (molecular weight M=647)(Phosphorous acid, tris(2,4-di-tertbutylphenyl)ester)
initial concentration: cP,0 = 600 mg/kg (= ppm)cP,0 = 1000 mg/kg (= ppm)
contact area: A = to be calculated - cylindrical packaging:(d = 10 cm; h = 6.5 cm)
volume of food (F): V = to be calculated - cylindrical packaging:(d = 10 cm; h = 6.5 cm)
density of F: roF = 1.0 (by definition in regulation)
diffusion coefficient in F: DF = 1e-4 for food simulants (liquid)partition coefficient (KP,F
*): K = 1 simulant D (olive oil)
Ex. 3 - Information & Inputs
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Ex. 3 - Questions
Q1: Estimate the diffusion coefficients of the additives at the temperatures (T = 121°C and 40°C) based on the polymer specific constant of the plastic material. Make use of the additives list available in the software.
Q2: Estimate the specific migration of the additives into the food simulant (olive oil) for each time/temperature condition.
Q3: Estimate the specific migration of the additives into the food simulant (olive oil) with consecutive time/temperature conditions (T-step).
Q4: Discuss the results.
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Ex. 3 - Q1 Answers
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Ex. 3 - Q1 Answers
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Ex. 3 - Q1 Answers
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Ex. 3 - Q1 Answers
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Ex. 3 - Q1 Answers
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Ex. 3 - Q1 Answers
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Q1: Estimate the diffusion coefficients of the additives at the temperatures (T = 121°C and 40°C) based on the polymer specific constant of the plastic material. Make use of the additives list available in the software.
R1: PM-ref. No 68320 40°C: DP = 7.11e-11 cm²/s121°C: DP = 1.91e-7 cm²/s
PM-ref. No 74240 40°C: DP = 2.89e-11 cm²/s121°C: DP = 7.77e-8 cm²/s
Ex.3 – Q1 Results
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Ex. 3 – Q2 Answers
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Ex. 3 – Q2 Answers (68320)
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Ex. 3 – Q2 Answers (68320)
concentration
profile
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Ex. 3 – Q2 Answers (68320)
time
dependentmigration
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Ex. 3 – Q2 Answers (68320)
concentration
profile
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Ex. 3 – Q2 Answers (68320)
time
dependentmigration
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Ex. 3 – Q2 Answers (74240)
concentration
profile
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Ex. 3 – Q2 Answers (74240)
time
dependentmigration
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Ex. 3 – Q2 Answers (74240)
concentration
profile
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Ex. 3 – Q2 Answers (74240)
time
dependentmigration
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Ex. 3 - Q2 Results
Q2: Estimate the specific migration of the additives into the food simulant (olive oil) for each time/temperature condition.
R2: PM-ref. No 68320, olive oil, KP,F = 1, DF = 1e-4 cm²/s40°C mF,t = 3.4 mg/kg121°C mF,t = 15.5 mg/kg
PM-ref. No 74240, olive oil, KP,F = 1, DF = 1e-4 cm²/s 40°C mF,t = 3,62 mg/kg121°C mF,t = 16,7 mg/kg
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concentration
profile
Ex. 3 – Q3 Answers (68320)
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time
dependentmigration
Ex. 3 – Q3 Answers (68320)
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Ex. 3 – Q3 Answers (74240)
concentration
profile
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Ex. 3 – Q3 Answers (74240)
time
dependentmigration
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Ex. 3 – Q3 Results
Q3: Estimate the specific migration of the additives into the food simulant (olive oil) with consecutive time/temperature conditions (T-step).
R3: PM-ref. No 68320, olive oil, KP,F = 1, DF = 1e-4 cm²/s40°C + 121°C mF,t = 16.7 mg/kg
PM-ref. No 74240, olive oil, KP,F = 1, DF = 1e-4 cm²/s 40°C + 121°C mF,t = 18,0 mg/kg
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Q4: Discuss the results
The addition of individual migration at two time/temperature conditions (68320: 3.4 + 15.5 = 18.9 mg/kg) is higher compared to the consecutive T-step (68320: 16.7 mg/kg).
Ex. 3 – Q4 Results
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Ex. 4 - Monolayer Plastic Food Contact Material
A kitchen utensil (spatula) for high temperature cooking
application with circular form (diameter 8 cm, thickness 2 mm).
Label on the spatula: PA, 200°C.
Compliance testing of the above article according to Directive
97/48/EEC.
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plastic material (P): PA6
density of P: roP = 1.15
AP*-value: AP'* = 2.0 (polymer specific constant)
tau = 0 (polymer specific temperature constant)
thickness: d = 0.2 cm (= 2000 µm)
migrants: PM-ref. No 14200 (molecular weight M=113)(Caprolactam)
initial concentration: cP,0 = 2000 mg/kg (= ppm)
contact area: A = to be calculated – circular shape:(d = 8 cm)
volume of food (F): V = 1 kg
density of F: roF = 1.0 (by definition in regulation)
diffusion coefficient in F: DF = 1e-1 for food simulants (liquid)partition coefficient (KP,F
*): K = 1 simulant D (olive oil)
K = 1 simulant A & B (water & acetic acid 3%)
Ex. 4 - Information & Inputs
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Q1: Determine conventional test conditions (time, temperature, simulant) according to the testing directives (82/711 and 85/572 including amendments).
Q2: Estimate the diffusion coefficients of the monomer (caprolactam) at the temperature (from Q1) based on the polymer specific constant of the plastic material.
Q3: Estimate the specific migration of the monomer (caprolactam) into one fatty and one aqueous food simulant.
Q4: Make the compliance evaluation.
Ex. 4 - Questions
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Q1: Determine conventional test conditions (time, temperature, simulant) according to the testing directives (82/711 and 85/572 including amendments).
R1: time: 30 minutestemperature: 200°Csimulant: fatty & aqueous
full immersion => migration from the center of thespatula in "both" directions
=> both sides of spatula consideredas contact area
=> half thickness of spatula consideredas thickness
Ex. 4 – Answer Q1
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Ex. 4 – Answer Q2
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Ex. 4 – Answer Q2
Both sides of the spatula considered.
(circular, diameter 8 cm)A = 2 x 50 cm²
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Ex. 4 – Answer Q2
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Ex. 4 – Answer Q2
► half thickness !
- because offull immersion
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Ex. 4 – Answer Q2
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Q2: Estimate the diffusion coefficients of the monomer (caprolactam) at the temperature (from Q1) based on the polymer specific constant of the plastic material.
R2: Caprolactam, PA6, 200°C: DP = 1.12e-6 cm²/s
Ex. 4 – Answer Q2
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Ex. 4 – Answer Q3
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Ex. 4 – Answer Q3
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concentration
profile
Ex. 4 – Answer Q3
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time
dependent migration
Ex. 4 – Answer Q3
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Q3: Estimate the specific migration of the monomer (caprolactam) into one fatty and one aqueous food simulant.
R3: SM = 11.6 mg/dm²SM = 11.6 mg/kg
Ex. 4 – Answer Q3
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Q4: Make the compliance evaluation.
R4: caprolactam SML = 15 mg/kg
=> spatula is compliant with respect to caprolactam migration
Ex. 4 – Answer Q4
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Exercise 5 - Multilayer Packaging (real food)
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fill good: yoghurt
shelf live: 30 days
storage temperature: 5°C
packaging material:
(a) inmould label
(b) beaker
(c) lid
Exercise 5 - Information & Inputs (a)
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packaging material (from outer to inner layers):
(a) inmould label - 20 µm OPP-film- 3 µm UV printing ink- 20 µm OPP-film
(b) beaker - 800 µm PP
(c) lid - 3 µm UV printing ink- 1 µm Primer- 37 µm Aluminum foil- 6 µm SBS HS-lacquer
Exercise 5 - Information & Inputs (b)
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Densities [g/cm³]:
(a) inmould label - OPP-film 0.910- UV printing ink 1.200- OPP-film 0.910
(b) beaker - PP 0.910
(c) lid - UV printing ink 1.200- Primer 1.000- Aluminum foil 2.700- SBS HS-lacquer 0.980
(d) yoghurt 1.000
Exercise 5 - Information & Inputs (c)
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Migrants (identity):
Irganox 1076 CAS No. 2082-79-3Octadecyl-3-(3,5-di-tert.butyl-4-hydroxyphenyl)-propionate
Irgafos 168 CAS No. 31570-04-4Phosphorous acid, tris(2,4-di-tert-butylphenyl)ester
Benzophenone CAS No. 119-61-9
P
O
O
O
CH3
CH3
CH3CH3
CH3
CH3
CH3
CH3
CH3
CH3
CH3
CH3
CH3CH3
CH3
CH3 CH3
CH3
CH3
CH3
CH3CH3
CH3
CH3
OOCH3
OH
O
Exercise 5 - Information & Inputs (d)
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Migrants [mg/kg]:
(a) - OPP-film Irganox 1076 200Irgafos 168 500
- UV printing ink Benzophenone 2000- OPP-film Irganox 1076 200
Irgafos 168 500
(b) - PP Irganox 1076 200Irgafos 168 500
(c) - UV printing ink Benzophenone 2000- Primer none ---- Aluminum foil none absolute barrier- SBS HS-lacquer Irganox 1076 300
Exercise 5 - Information & Inputs (c)
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Q1: Calculate the migration of the two additives from the container into food at the and of the shelf live
Q2: Calculate the migration of the two additives from the lid into food at the and of the shelf live(Aluminum =absolute barrier - DP = 1e-20 cm²/s)(SBS - diffusion properties similar to LDPE)(UV -printing ink and Primer - AP' = -2, tau = 0)
Q3: Calculate the migration of the three additives from the in-mould label into food at the and of the shelf live (UV -printing ink and Primer - AP' = -2, tau = 0)
Ex. 4 – Questions
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A3 = 50 cm²
A2 = 50 cm²
A1 = 150 cm²
Ex. 5 – Answer Q1, Q2, Q3
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A2: Irganox 1076 0,0417 mg/kgIrgafos 168 0,0663 mg/kg
A3: Irganox 1076 0,0294 mg/kgBenzophenon 0 mg/kg
A1: Irganox 1076 0,125 mg/kgIrgafos 168 0,199 mg/kgBenzophenon 0 mg/kg
Ex. 5 – Answer Q1, Q2, Q3