# Determination of Partition Coefficients of Selected Model Migrants between Polyethylene and Polypropylene and Nanocomposite Polypropylene

Authors: Pablo Otero-Pazos; David A. Pereira de Abreu; Raquel Sendon; Ana Rodriguez Bernaldo de Quiros; Inmaculada Angulo; Jose M. Cruz; Perfecto Paseiro-Losada
Journal: Journal of Chemistry
 (2016)

---

## Abstract

Studies on nanoparticles have focused the attention of the researchers because they can produce nanocomposites that exhibit unexpected hybrid properties. Polymeric materials are commonly used in food packaging, but from the standpoint of food safety, one of the main concerns on the use of these materials is the potential migration of low molecular substances from the packaging into the food. The key parameters of this phenomenon are the diffusion and partition coefficients. Studies on migration from food packaging with nanomaterials are very scarce. This study is focused on the determination of partition coefficients of different model migrants between the low-density polyethylene (LDPE) and polypropylene (PP) and between LDPE and nanocomposite polypropylene (naPP). The results show that the incorporation of nanoparticles in polypropylene increases the mass transport of model migrants from LDPE to naPP. This quantity of migrants absorbed into PP and naPP depends partially on the nature of the polymer and slightly on the chemical features of the migrant. Relation (R
P
P
/
n
a
P
P) between partition coefficient K
L
D
P
E
/
P
P and partition coefficient K
L
D
P
E
/
n
a
P
P at 60°C and 80°C shows that only BHT at 60°C has a R
P
P
/
n
a
P
P less than 1. On the other hand, bisphenol A has the highest R
P
P
/
n
a
P
P with approximately 50 times more.


---

## Body

## 1. Introduction

At the present time, multilayer systems are commonly used as food packaging. Plastic food packages contain additives (antioxidants, dyes, pigments, antifogging agents, stabilizers, and plasticizers) used to minimize degradation during processing, to facilitate processing and to increase stability during storage [1, 2]. The contamination of foodstuffs with substances from the packaging material that can arise either from the packaging process itself (e.g., via overprinting labels) or from migration processes [3]. From the food safety point of view, it is important to remark that some substances (volatiles, additives, monomers, and oligomers) are able to migrate from packaging to foods. Migration includes two phenomena (partition and diffusion) that are important in determining the concentration of contaminants in a food system at any time. In the migration process, the kinetic (diffusion) and thermodynamic equilibrium (partition) can be defined as an exchange of mass and energy between the packaging and food [4, 5]. Moreover, if food packaging is made up of various layers then it is important to know the capacity of substances to pass through them.Measurement of the rate at which the diffusion process occurs is expressed in terms of diffusion coefficient (cm2s−1). The classical theory used to model the diffusion process is based on Fick’s laws. Diffusion (D) is based on the fact that the rate of transfer (R) of a migrant passing perpendicularly through unit area of a section is proportional to the concentration gradient between the two sides of the packaging: R
=
∂
C
/
∂
t
=
-
D
(
C
)
(
d
C
/
d
X
). In general, D is a function of the local diffusant concentration, C (mol m−3), t is the time (s), and X is the thickness of the material (m) [5, 6]. Amongst plastics, the highest diffusion rates occur in polyolefins, especially low-density polyethylene (LDPE) films. LDPE film was therefore chosen for the migration tests because it is widely used and provides a picture of the “worst case scenarios” [7]. Polypropylene (PP) is one of the most polyolefins used in food because it provides mechanical properties at low cost. Other vantages are their resistance to water vapor, acids, bases, grease, and solvents. The amount of package components that may migrate between layers of multilayer packaging material depends on the chemical and physical properties of them and the material itself. Different factors like partition coefficient, migrant concentration, time, temperature, packaging composition, molecular weight, solubility, diffusivity, and structures are the main controlling factors in migration [5, 8, 9]. In a multilayer packaging system, migrant transfer occurs to reach thermodynamic equilibrium. A partition coefficient (K) is defined as the ratio of migrant concentration in the packaging material C
p
1 and its concentration in another packaging material phase, C
p
2 at equilibrium. K is defined as K
=
C
p
1
/
C
p
2. When K
=
1, the migrant concentration in each packaging material is equal, at equilibrium. K is higher when more migrant quantity is absorbed into packaging material 1 than in packaging material 2. Molecular size and structure of migrant and structure of polymeric matrix are the main factors that affect the partition coefficient [5].The approach of the European Commission (EC) in controlling the safety of food packaging and other food-contact materials has been to assign specific migration limits (SML) to those substances with potential adverse toxicological properties. The SML restricts the quantity of the substance allowed to migrate into foods or food simulants. For instance, the SML established for some of the model substances evaluated in this study are 0.6 mg/kg for bisphenol A and Uvitex and 3 mg/kg for butylated hydroxyl toluene. Migration limits are based on the acceptable daily intake/tolerable daily intake established by the European Food Safety Authority for the substance in question and on the assumption that a person weighing 60 kg eats 1 kg of food each day, which has been packaged in the same material. One important consideration in the migration test condition is the ratio of the volume of the simulant to the area of the sample. The conventional value considered by the EC, 6 dm2/kg, is used in most cases. In some instances, where the additive is readily soluble in the simulant, it is considered acceptable to increase this ratio to improve the sensitivity of the analysis. Experimental studies of all these migrations are time consuming and highly expensive [10–13]. Through the mathematical model, experimental migration tests only will be carried out when the predicted migration values are higher than those established by legislation. For those reasons, it is interesting to get a mathematical model that allows predicting theses distribution processes.Moreover, nanotechnology is driving a long list of developments offering many alternatives. Organic-inorganic nanocomposites are compounds that exhibit hybrid properties derived from synergistic reactions between the two components. Nanocomposites based on organic polymers and inorganic clay minerals consisting of silicate layers are one of the most promising composite systems. Inside this system, a nanocompound can be intercalated or exfoliated, depending on the degree of dispersal of the nanoparticle between polymeric chains; however, a mixture of the two morphologies is often found. If the nanoparticles are completely dispersed between the polymeric chains, the nanocompound is exfoliated [14–17]; if they are not it is intercalated. Packages with exfoliated nanoparticles show better barrier properties than packages with intercalated nanoparticles. In general, the nanocomposites have been found to provide effective barriers to gaseous diffusion [16, 17]. Nevertheless, for its use in the field of food-contact materials in the European Union they should be specifically authorized, and at this moment only titanium nitride nanoparticles are approved for use as additives in polyethylene terephthalate (PET) intended to come into contact with foodstuffs (Commission Regulation (EU) number 10/2011 of 14 January 2011) [18].The present study is focused on the determination of partition coefficients of trans,trans-1,4-diphenyl-1,3-butadiene (DPBD), 5-chloro-2-(2,4-dichlorophenoxy)phenol (triclosan), Benzophenone, 2,5-bis(5-tert-butyl-2-benzoxazolyl) thiophene (Uvitex OB®), diphenyl phthalate (DPP), isopropyl-9H-thioxanthen-9-one (ITX), butylated hydroxyl toluene (BHT), and bisphenol A (BPA) between the LDPE and polypropylene (PP) and between LDPE and nanocomposite polypropylene (naPP). Benzophenone and ITX are photoinitiators in inks, employed to print food packaging surfaces; DPBD is a fluorescent whitening agent; triclosan is a broad-spectrum antimicrobial compound; DPP is a plasticizer that improves the performance of polyvinylpyrrolidone; BPA is used in the production of polycarbonate and epoxy resins, flame retardants, and other products; BHT is a small phenolic antioxidant, used in plastics at levels between hundreds of and a few thousand mg per kg as plastic stabilizer, and Uvitex OB is an optical brightening agent [3, 7, 13, 19–22]. Selection of these substances was made on the basis of their representativeness as potential migrants from food-contact materials so that the results can be extrapolated to other substances of similar characteristics. The results were discussed in terms of the parameters that may have the greatest effect on migration.


## 2. Materials and Methods

### 2.1. Materials

The nanoclay used is natural montmorillonites, modified with a quaternary ammonium salt to facilitate dispersal in the polymeric matrix. Cloisite 15 A nanoparticles were used (provided by Southern Clay Product, Texas, USA;http://www.byk.com). Cloisite 15 A has an average particle size of 6 μm and cationic exchange capacity of 125 meq/100 g of clay. Montmorillonite is suitable for incorporation in an apolar polymeric matrix such as polypropylene. The polypropylene selected was a copolymer of intermediate-high fluidity (ISPLEN PB 171 H1M), with MFI: 9.5 g/10 min, ISO 1133 (230°C; 2.16 kg).


### 2.2. Reagents and Standard Solutions

All reagents were of analytical grade. Ethanol, acetonitrile, and tetrahydrofuran were purchased from Merck (Darmstadt, Germany). Water used for all solutions was obtained from a Milli-Q water purification system (Millipore; Bedford, MA).Model migrants standards were obtained as follows: Benzophenone and DPBD (98%) were from Sigma-Aldrich (Steinheim, Germany); triclosan (97%), Uvitex OB (≥99.0%), and BHT (≥99.0%) were from Fluka (Steinheim, Germany); DPP (≥99.0%), BPA (≥99.0%) and ITX (97%) were from Aldrich-Chemie (Steinheim, Germany). Stock standard solutions were prepared in ethanol and stored in amber flasks at 4°C.


### 2.3. Film Samples

Films of LDPE were spiked with the migrants by extrusion process:(i)
LDPE film (thickness:397.7
±
13.9 μm; C
B
e
n
z
o
p
h
e
n
o
n
e
=
417.7
±
67.4 μg·g−1; C
D
P
B
D
=
755.0
±
31.6 μg·g−1; C
U
v
i
t
e
x
=
900.3
±
55.2 μg·g−1) was spiked with Benzophenone, DPBD, and Uvitex OB.
(ii)
LDPE film (thickness:410.6
±
16.7 μm; C
D
P
P
=
457.3
±
113.2 μg·g−1; C
I
T
X
=
1138.0
±
206.9 μg·g−1; C
B
H
T
=
839.8
±
170.3 μg·g−1) was spiked with DPP, ITX, and BHT.
(iii)
LDPE film (thickness:394.8
±
17.6 μm; C
B
P
A
=
933.7
±
57.5 μg·g−1; C
T
r
i
c
l
o
s
a
n
=
1233.1
±
85.1 μg·g−1) was spiked with BPA and triclosan.The obtaining of the exfoliated film was previously described by Pereira de Abreu et al. [16].A polypropylene masterbatch was used to elaborate that the nanocomposite polypropylene (naPP) film contained equal percentages of polypropylene and polypropylene modified with maleic anhydride and Cloisite 15 A (C15A). This masterbatch was prepared in the rollers at temperature of 160°C. The resulting mixture was then crushed and diluted in the PP matrix by compounding in a double screw extruder (MIKE 27 GL-36 D LEISTRITZ) (screw diameter: 27 mm, screw length:36
×
D, and screw speed range: 10–400 rpm).For both the PP and its nanocompound, the following conditions were used in the extruder: barrel was set to 160–170°C; Zones I and II were at 160°C, Zones III, IV, and V were at 163°C, Zones VI, VII, and VIII were at 165°C, and Zone IX was at 170°C. The inorganic content of the samples was determined by measuring the weight before and after burning the organic component. Screw speed was set to 300 rpm with a maximum temperature of 170°C for the PP. The obtained pellet was passed through the double screw extruder twice to homogenize the mixture thoroughly.


### 2.4. Analytical Procedure

To carry out partition coefficients calculation, LDPE, PP, and naPP were cut in pieces of4
×
4 cm2. The thickness along the film was measured to obtain an average value. LDPE film was put into contact with one face of PP or naPP. Samples were then wrapped with aluminum foil to protect them from the light and were placed inside a plastic bag and incubated in the oven at 60 and 80°C. The incubation times used at 60°C were 40, 55, and 70 days and at 80°C were 25, 40, and 60 days, respectively. Then, at selected times, the set was withdrawn of the oven and the spiked LDPE film and the other plastic (PP or naPP) were separated. After this, an extraction of the selected migrants from spiked LDPE, PP, and naPP films was made. The films were extracted in a 60 mL amber flask with 50 mL of ethanol for 6 hours at 70°C. After this time, the flask was removed from the oven and the film was separated from the liquid phase. Then an aliquot of this liquid phase was filtered by a 0.50 μm filter and analyzed by HPLC.


### 2.5. High-Performance Liquid Chromatography Analysis

The HPLC-DAD-FLD system (Hewlett-Packard, Waldbronn, Germany) was fitted with a HP1100 quaternary pump, a degassing device, an autosampler, a column thermostatting system, a diode array UV detector, and a fluorescence array detector. HP ChemStation chromatographic software was used for data acquisition. Chromatographic separation was performed on a Kromasil ODS C18 column (25 × 0.32 cm ID, 5μm particle size) at 30°C and a flow rate of 0.5 mL·min−1; detailed analytical conditions are shown in Tables 1, 2, and 3.Table 1
High performance liquid chromatography parameters employed in the analysis of Benzophenone, diphenylbutadiene (DPBD), and Uvitex.
Injection volume
20µL
Eluents
A: Milli-Q water
B: THF 30% methanolic solution (v/v)
Time (min)
%  Eluent A
% Eluent B
Eluent gradient
0
30
70
4
30
70
10
0
100
17
0
100
Posttime: 3 minutes
Substance
UV (nm)
Detection
Benzophenone
256
DPBD
330
Uvitex OB
372Table 2
High performance liquid chromatography parameters employed in the analysis of diphenyl phthalate (DPP), 2-isopropylthioxanthone (ITX), and butylated hydroxyl toluene (BHT).
Injection volume
10µL
Eluents
A: Milli-Q water
B: Acetonitrile
Time (min)
% Eluent A
% Eluent B
Eluent gradient
0
40
60
1
40
60
17
0
100
20
0
100
Posttime: 5 minutes
Substance
DAD (nm)
FLD (nm)
Detection
DPP
205
—
ITX
—
Ex 250; Em 410
BHT
205
—Table 3
High performance liquid chromatography parameters employed in the analysis of bisphenol A (BPA) and triclosan.
Injection volume
10µL
Eluents
A: Milli-Q water
B: Acetonitrile
Time (min)
% Eluent A
% Eluent B
Eluent gradient
0
40
60
3
40
60
9
0
100
17
0
100
Posttime: 5 minutes
Substance
DAD (nm)
FLD (nm)
Detection
Triclosan
205
—
BPA
—
Ex 225; Em 305


## 2.1. Materials

The nanoclay used is natural montmorillonites, modified with a quaternary ammonium salt to facilitate dispersal in the polymeric matrix. Cloisite 15 A nanoparticles were used (provided by Southern Clay Product, Texas, USA;http://www.byk.com). Cloisite 15 A has an average particle size of 6 μm and cationic exchange capacity of 125 meq/100 g of clay. Montmorillonite is suitable for incorporation in an apolar polymeric matrix such as polypropylene. The polypropylene selected was a copolymer of intermediate-high fluidity (ISPLEN PB 171 H1M), with MFI: 9.5 g/10 min, ISO 1133 (230°C; 2.16 kg).


## 2.2. Reagents and Standard Solutions

All reagents were of analytical grade. Ethanol, acetonitrile, and tetrahydrofuran were purchased from Merck (Darmstadt, Germany). Water used for all solutions was obtained from a Milli-Q water purification system (Millipore; Bedford, MA).Model migrants standards were obtained as follows: Benzophenone and DPBD (98%) were from Sigma-Aldrich (Steinheim, Germany); triclosan (97%), Uvitex OB (≥99.0%), and BHT (≥99.0%) were from Fluka (Steinheim, Germany); DPP (≥99.0%), BPA (≥99.0%) and ITX (97%) were from Aldrich-Chemie (Steinheim, Germany). Stock standard solutions were prepared in ethanol and stored in amber flasks at 4°C.


## 2.3. Film Samples

Films of LDPE were spiked with the migrants by extrusion process:(i)
LDPE film (thickness:397.7
±
13.9 μm; C
B
e
n
z
o
p
h
e
n
o
n
e
=
417.7
±
67.4 μg·g−1; C
D
P
B
D
=
755.0
±
31.6 μg·g−1; C
U
v
i
t
e
x
=
900.3
±
55.2 μg·g−1) was spiked with Benzophenone, DPBD, and Uvitex OB.
(ii)
LDPE film (thickness:410.6
±
16.7 μm; C
D
P
P
=
457.3
±
113.2 μg·g−1; C
I
T
X
=
1138.0
±
206.9 μg·g−1; C
B
H
T
=
839.8
±
170.3 μg·g−1) was spiked with DPP, ITX, and BHT.
(iii)
LDPE film (thickness:394.8
±
17.6 μm; C
B
P
A
=
933.7
±
57.5 μg·g−1; C
T
r
i
c
l
o
s
a
n
=
1233.1
±
85.1 μg·g−1) was spiked with BPA and triclosan.The obtaining of the exfoliated film was previously described by Pereira de Abreu et al. [16].A polypropylene masterbatch was used to elaborate that the nanocomposite polypropylene (naPP) film contained equal percentages of polypropylene and polypropylene modified with maleic anhydride and Cloisite 15 A (C15A). This masterbatch was prepared in the rollers at temperature of 160°C. The resulting mixture was then crushed and diluted in the PP matrix by compounding in a double screw extruder (MIKE 27 GL-36 D LEISTRITZ) (screw diameter: 27 mm, screw length:36
×
D, and screw speed range: 10–400 rpm).For both the PP and its nanocompound, the following conditions were used in the extruder: barrel was set to 160–170°C; Zones I and II were at 160°C, Zones III, IV, and V were at 163°C, Zones VI, VII, and VIII were at 165°C, and Zone IX was at 170°C. The inorganic content of the samples was determined by measuring the weight before and after burning the organic component. Screw speed was set to 300 rpm with a maximum temperature of 170°C for the PP. The obtained pellet was passed through the double screw extruder twice to homogenize the mixture thoroughly.


## 2.4. Analytical Procedure

To carry out partition coefficients calculation, LDPE, PP, and naPP were cut in pieces of4
×
4 cm2. The thickness along the film was measured to obtain an average value. LDPE film was put into contact with one face of PP or naPP. Samples were then wrapped with aluminum foil to protect them from the light and were placed inside a plastic bag and incubated in the oven at 60 and 80°C. The incubation times used at 60°C were 40, 55, and 70 days and at 80°C were 25, 40, and 60 days, respectively. Then, at selected times, the set was withdrawn of the oven and the spiked LDPE film and the other plastic (PP or naPP) were separated. After this, an extraction of the selected migrants from spiked LDPE, PP, and naPP films was made. The films were extracted in a 60 mL amber flask with 50 mL of ethanol for 6 hours at 70°C. After this time, the flask was removed from the oven and the film was separated from the liquid phase. Then an aliquot of this liquid phase was filtered by a 0.50 μm filter and analyzed by HPLC.


## 2.5. High-Performance Liquid Chromatography Analysis

The HPLC-DAD-FLD system (Hewlett-Packard, Waldbronn, Germany) was fitted with a HP1100 quaternary pump, a degassing device, an autosampler, a column thermostatting system, a diode array UV detector, and a fluorescence array detector. HP ChemStation chromatographic software was used for data acquisition. Chromatographic separation was performed on a Kromasil ODS C18 column (25 × 0.32 cm ID, 5μm particle size) at 30°C and a flow rate of 0.5 mL·min−1; detailed analytical conditions are shown in Tables 1, 2, and 3.Table 1
High performance liquid chromatography parameters employed in the analysis of Benzophenone, diphenylbutadiene (DPBD), and Uvitex.
Injection volume
20µL
Eluents
A: Milli-Q water
B: THF 30% methanolic solution (v/v)
Time (min)
%  Eluent A
% Eluent B
Eluent gradient
0
30
70
4
30
70
10
0
100
17
0
100
Posttime: 3 minutes
Substance
UV (nm)
Detection
Benzophenone
256
DPBD
330
Uvitex OB
372Table 2
High performance liquid chromatography parameters employed in the analysis of diphenyl phthalate (DPP), 2-isopropylthioxanthone (ITX), and butylated hydroxyl toluene (BHT).
Injection volume
10µL
Eluents
A: Milli-Q water
B: Acetonitrile
Time (min)
% Eluent A
% Eluent B
Eluent gradient
0
40
60
1
40
60
17
0
100
20
0
100
Posttime: 5 minutes
Substance
DAD (nm)
FLD (nm)
Detection
DPP
205
—
ITX
—
Ex 250; Em 410
BHT
205
—Table 3
High performance liquid chromatography parameters employed in the analysis of bisphenol A (BPA) and triclosan.
Injection volume
10µL
Eluents
A: Milli-Q water
B: Acetonitrile
Time (min)
% Eluent A
% Eluent B
Eluent gradient
0
40
60
3
40
60
9
0
100
17
0
100
Posttime: 5 minutes
Substance
DAD (nm)
FLD (nm)
Detection
Triclosan
205
—
BPA
—
Ex 225; Em 305


## 3. Results and Discussion

Model migrants were selected based on their structure and chemical properties, trying to cover the maximum area in terms of molecular size and polarity.Ranges of temperature and time exposition were selected seeking a compromise between the speed of the assay and the stability of the molecules. Thus, 60°C and 80°C were chosen, with exposure times of 40, 55, and 70 days and 25, 40, and 60 days, respectively.Effectiveness of extraction procedure was tested in films spiked with the selected substances. These films were extracted several times. Subsequent extractions of the film resulted in quantities of substances that were undetectable.Quantification was obtained using a series of standards of selected substances solutions of known concentration. Calibration curves were constructed using five concentration levels and they were fitted to linear equations within the 0.25–5μg mL−1 range. The equations are shown in Table 4.Table 4
Calibration curves and retention times of analyzed substances.
Substance
R
t (min)
R
2
Equation
Benzophenone
5.3
0.99998
y
=
216.28
x
-
5.6776
DPBD
12.7
0.99988
y
=
567.67
x
-
22.856
Uvitex
14.8
0.99998
y
=
260.44
x
+
5.4778
DPP
11.7
0.99999
y
=
174.88
x
+
0.5316
ITX
16.8
0.99997
y
=
262.77
x
+
1.5187
BHT
17.8
0.99950
y
=
161.96
x
+
74.026
Bisphenol A
4.1
0.99999
y
=
662.48
x
-
1.731
Triclosan
11.0
0.99999
y
=
239.82
x
+
2.327Partition coefficient LDPE/PP or naPP for each model substance was calculated using the following equation:(1)
K
L
D
P
E
/
P
P
=
C
L
D
P
E
e
q
C
P
P
e
q
,
K
L
D
P
E
/
n
a
P
P
=
C
L
D
P
E
e
q
C
n
a
P
P
e
q
,where K
L
D
P
E
/
P
P is the partition coefficient between LDPE and PP; K
L
D
P
E
/
n
a
P
P is the partition coefficient between LDPE and naPP; C
P
P
e
q is the concentration of substance in PP at equilibrium, in μg g−1; C
n
a
P
P
e
q is the concentration of substance in naPP at equilibrium, in μg g−1; C
L
D
P
E
e
q is the concentration of substance in the LDPE at equilibrium, in μg g−1.The partition coefficient of low-density polyethylene/polypropylene (K
L
D
P
E
/
P
P) and low-density polyethylene/nanocomposite polypropylene (K
L
D
P
E
/
n
a
P
P), that is, the relative solubility of the migrants at equilibrium between the polyethylene and the polypropylene or nanocomposite polypropylene, is shown in Tables 5 and 6, respectively.Table 5
Partition coefficient of polyethylene/polypropylene (K
L
D
P
E
/
P
P) at 60°C and 80°C for all substances studied.
Model migrant
Temperature
Time
K
L
D
P
E
/
P
P
Model migrant
Temperature
Time
K
L
D
P
E
/
P
P
Benzophenone
40 days
0.86
DPP
40 days
0.86
60°C
55 days
0.84
60°C
55 days
1.02
70 days
0.86
70 days
0.89
25 days
1.08
25 days
1.21
80°C
40 days
1.04
80°C
40 days
1.04
60 days
1.03
60 days
1.16
DPBD
40 days
1.16
BHT
40 days
0.62
60°C
55 days
1.15
60°C
55 days
0.66
70 days
1.09
70 days
0.56
25 days
1.36
25 days
0.90
80°C
40 days
1.31
80°C
40 days
0.67
60 days
1.36
60 days
0.86
Uvitex OB
40 days
41.35
Bisphenol A
40 days
14.23
60°C
55 days
16.43
60°C
55 days
14.13
70 days
9.42
70 days
12.05
25 days
6.26
25 days
8.19
80°C
40 days
4.50
80°C
40 days
7.17
60 days
3.61
60 days
5.70
ITX
40 days
0.99
Triclosan
40 days
0.88
60°C
55 days
1.05
60°C
55 days
0.93
70 days
0.99
70 days
0.91
25 days
1.26
25 days
1.13
80°C
40 days
1.07
80°C
40 days
1.12
60 days
1.23
60 days
1.15Table 6
Partition coefficient of polyethylene/nanocomposite polypropylene (K
L
D
P
E
/
n
a
P
P) at 60°C and 80°C for all substances studied.
Model migrant
Temperature
Time
K
L
D
P
E
/
n
a
P
P
Model migrant
Temperature
Time
K
L
D
P
E
/
n
a
P
P
Benzophenone
40 days
0.35
DPP
40 days
0.13
60°C
55 days
0.33
60°C
55 days
0.07
70 days
0.34
70 days
0.10
25 days
—
25 days
0.10
80°C
40 days
0.48
80°C
40 days
0.09
60 days
0.45
60 days
0.12
DPBD
40 days
0.20
BHT
40 days
0.67
60°C
55 days
0.18
60°C
55 days
0.55
70 days
0.20
70 days
0.55
25 days
—
25 days
0.84
80°C
40 days
0.27
80°C
40 days
0.79
60 days
0.32
60 days
0.97
Uvitex OB
40 days
11.57
Bisphenol A
40 days
0.87
60°C
55 days
12.58
60°C
55 days
0.91
70 days
4.67
70 days
0.60
25 days
—
25 days
—
80°C
40 days
1.35
80°C
40 days
0.15
60 days
1.73
60 days
0.11
ITX
40 days
0.41
Triclosan
40 days
0.05
60°C
55 days
0.37
60°C
55 days
0.05
70 days
0.41
70 days
0.04
25 days
0.57
25 days
—
80°C
40 days
0.60
80°C
40 days
0.06
60 days
0.60
60 days
0.06The partition coefficient values correspond to the relative solubility of the migrant at equilibrium between the polyethylene and the polypropylene or nanocomposite polypropylene [23]. Benzophenone, DPP, DPBD, BHT, ITX, and triclosan show a K
L
D
P
E
/
P
P near to 1. Because of the composition of polyethylene -[-CH2-CH2-]n- and polypropylene -[-CH2-CH(CH2)-]n-, with a similar structural base, these results were expected, whereas in the cases of Uvitex and bisphenol A the equilibrium was not reached at the end of the assay (i.e., at 60°C, 70 days or at 80°C, 60 days). The molecular size, chemical structure, and physicochemical properties (polarity, solubility, and hydrogen bonding) of migrants and type of packaging are important parameters affecting partition coefficient. Due to the large sizes of the polymer molecules, the secondary bond forces (van der Waals forces and hydrogen bonding) assume much greater roles in influencing physical properties than they do in small organic molecules [24]. Smaller molecules are absorbed more rapidly because they have a greater diffusivity than larger molecules. In fact, the partition coefficient of a series of compounds with the same functional group (i.e., esters or aldehydes) increased with increasing carbon chain length [5, 25–30]. The alcohols in aqueous solutions increase its partition coefficients to increase its molecular weight.The differences in polarity of migrant and polymer are another important factor in the absorption process [5]. Alcohols and short-chained esters (polar substances) have higher partition coefficients in the oil/polymer system than in the water/polymer system, while aldehydes (long carbon nonpolar chains) have lower partition coefficients in the oil/polymer than in the water/polymer [29]. In mixtures, some compounds exhibit a lower absorption rate than systems containing the individual compounds. This effect could be due to the fact that the absorbed components change the properties of polymer and/or the compounds compete for a limited number of active sorption sites [29, 30]. When more than one type of solids is present, alcohols preferentially are adsorbed to the solid with higher affinity for alcohols, until all binding sites on the solid have been occupied. Silica and soy protein increase solubility of alcohols in water by adsorbing them through hydrophobic association and/or hydrogen bonds [31].Some of these factors could be the reasons because the diffusion for Uvitex and bisphenol A was lower than the rest of compounds and the equilibrium was not achieved. However, theK
L
D
P
E
/
P
P should be close to 1 when the equilibrium will be reached.PP has no polar groups in its backbone and the homogeneous dispersion of the silicate layers in PP is problematic without the utilization of a functional oligomer (maleic anhydride (MA) modified PP oligomer). There are two important factors in terms of the structures of the oligomers in order to obtain the complete homogeneous dispersion of the silicate layers. The oligomers should include a certain amount of polar groups to be intercalated between silicate layers through hydrogen bonding and the oligomers should be well miscible with PP. Functional oligomer is intercalated into the silicate layers at the first stage of the mixing process because the driving force of the intercalation originated from the strong hydrogen bonding between the maleic anhydride group (or COOH group generated from the hydrolysis of the maleic anhydride group) and the oxygen groups of the silicates. The interlayer spacing of the clay is increased and the interactions of the layers are decreased. Then, intercalated clays with the oligomers can enter in contact with PP under a strong shear field. If the miscibility of PP-MA with PP is good enough to disperse at the molecular level, the exfoliation of the intercalated clay should take place smoothly [32, 33]. Polymer/silicate nanocomposites have better properties that include high barrier properties, improved tensile characteristics, higher heat deflection temperature, better scratch resistance, and increased flame retardancy [13, 16, 17, 34]. Observing results obtained, only in the cases of the Uvitex and bisphenol A at 60°C (70 days) it was not possible to reach equilibrium in the LDPE/naPP system. Triclosan, bisphenol (80°C), and DPP show the smallest partition coefficient of low-density polyethylene/nanocomposite polypropylene (K
L
D
P
E
/
n
a
P
P), while Uvitex (80°C) has the biggest K
L
D
P
E
/
n
a
P
P. Table 7 shows the properties of the substances used in this study. The molecular size, chemical structure, and physicochemical properties of migrants and naPP characteristics could explain these results. These substances have the capacity to form secondary bond forces, only DPBD has no polar surface area. The polar surface area of a molecule is defined as the area of its van der Waals surface that arises from oxygen or nitrogen atoms or hydrogen atoms attached to oxygen or nitrogen atoms. As such, it is clearly related to the capacity of a compound to form hydrogen bonds [35]. But DPBD can form secondary bond forces (van der Waals forces). naPP has polar zones where the exfoliated nanoparticles and maleic anhydride group are staying. Maleic anhydride group can also be found distributed in the PP without being attached to the nanoparticles. These areas could attract and form hydrogen bonds and van der Waals forces bonds with migrants from the polyethylene. This ability to form secondary bond forces could explain the decrease in the values of K
L
D
P
E
/
n
a
P
P found for all these molecules.Table 7
Chemical information of selected migrants.
Migrant
Chemical name
CAS number
MW
Polar surface area (Å2)
Molar volume (cm3·mol−1)
H bond donor
H bond acceptor
Structure
Benzophenone
Methanone diphenyl
119-61-9
182.22
17.07
167.50
0
1
Bisphenol A
4,4′-Dihydroxy-2,2-diphenylpropane
80-05-7
228.29
40.46
199.56
2
2
Triclosan
5-Chloro-2-(2,4-dichlorophenoxy)phenol
3380-34-5
289.54
29.46
194.30
1
2
DPBD
trans,trans-1,4-Diphenyl-1,3-butadiene
538-81-8
206.28
0.00
199.20
0
0
Uvitex
2,5-Bis(5-tert-butyl-2-benzoxazolyl) thiophene
7128-64-5
430.56
80.30
363.10
0
4
DPP
Diphenyl phthalate
84-62-8
318.32
52.60
256.20
0
4
ITX
Isopropyl-9H-thioxanthen-9-one
75081-21-9
254.35
42.37
212.12
1
1
BHT
Butylated hydroxyl  toluene
128-37-0
220.35
20.23
237.50
1
1R
P
P
/
n
a
P
P is a measure of the relative solubility of a substance in PP compared to its solubility in naPP. Relation (R
P
P
/
n
a
P
P) between K
L
D
P
E
/
P
P and K
L
D
P
E
/
n
a
P
P at 60°C and 80°C for all substances studied is shown in Table 8. R
P
P
/
n
a
P
P is defined as(2)
R
P
P
/
n
a
P
P
=
K
L
D
P
E
/
P
P
K
L
D
P
E
/
n
a
P
P
.Table 8
Relation (R
P
P
/
n
a
P
P) K
L
D
P
E
/
P
P/K
L
D
P
E
/
n
a
P
P at 60°C and 80°C for all substances studied.
Model migrant
Temperature
Time
R
P
P
/
n
a
P
P
Model migrant
Temperature
Time
R
P
P
/
n
a
P
P
Benzophenone
40 days
2.47
DPP
40 days
6.70
60°C
55 days
2.54
60°C
55 days
13.84
70 days
2.55
70 days
8.53
25 days
—
25 days
11.92
80°C
40 days
2.15
80°C
40 days
11.35
60 days
2.30
60 days
10.02
DPBD
40 days
5.69
BHT
40 days
0.93
60°C
55 days
6.33
60°C
55 days
1.20
70 days
5.50
70 days
1.02
25 days
—
25 days
1.07
80°C
40 days
4.82
80°C
40 days
0.85
60 days
4.27
60 days
0.89
Uvitex OB
40 days
3.57
Bisphenol A
40 days
16.30
60°C
55 days
1.31
60°C
55 days
15.54
70 days
2.02
70 days
20.19
25 days
—
25 days
—
80°C
40 days
3.34
80°C
40 days
48.41
60 days
2.09
60 days
54.19
ITX
40 days
2.42
Triclosan
40 days
16.41
60°C
55 days
2.84
60°C
55 days
16.98
70 days
2.44
70 days
23.01
25 days
2.22
25 days
—
80°C
40 days
1.77
80°C
40 days
18.28
60 days
2.03
60 days
18.60WhenR
=
1, the migrant concentration in naPP at equilibrium equals the concentration in PP at equilibrium. R is higher than 1 when more migrant is present into the naPP than in the PP. Only BHT at 60°C has an R
P
P
/
n
a
P
P less than 1 but is very near to one. On the other hand, BPA has the highest R
P
P
/
n
a
P
P (approximately 50 times more). These results show that all substances employed in this study have more preference for naPP than for PP. At 60°C (70 days) the affinity in decreasing order for naPP is triclosan > BPA > DPP > DPBD > Benzophenone > ITX > Uvitex > BHT. At 80°C (60 days) the preference in decreasing order for naPP is BPA > triclosan > DPP > DPBD > Benzophenone > Uvitex > ITX > BHT. Generally, the incorporation of Cloisite to PP increased the affinity of the selected substances compared to PP and LDPE.These substances used in the preparation of food packaging could migrate into food. It is interesting to remark that the solubility of these substances has increased in the material with nanoparticles respect with the polypropylene alone. With this information, we can speculate about the behaviour of these kinds of plastics in contact with another element, for example, foodstuff. In this case, the increased solubility in nanoparticle polymer could represent a less quantity of substances that would pass away across the naPP and could be a good option to increase the safety and security in food packaging. More investigation about this approach must be carried out.


## 4. Conclusions

Partition coefficient of eight model substances between LDPE and PP and naPP was determined from their concentration in each polymer analysed. These concentrations were determined by using High-Performance Liquid Chromatography. The additives were of different chemical types, molecular weights and used for different functions.The obtaining of partition coefficients lower than 1 indicates that affinity of additives is greater for naPP than PP, even when substances with less tendency to migrate are present. Relation (R
P
P
/
n
a
P
P) between K
L
D
P
E
/
P
P and K
L
D
P
E
/
n
a
P
P at 60°C and 80°C shows that only BHT at 60°C has a R
P
P
/
n
a
P
P lower than 1 but is very near to 1. On the other hand, BPA has the highest R
P
P
/
n
a
P
P (approximately 50 times more). The amount of migrants absorbed into PP and naPP depends partially on the nature of the polymer and slightly on the chemical features of the model migrant. Factors that affected absorption include molecular size of migrants, polarity, and solubility properties of both the polymers and the migrants. The results obtained could prove the presence of interactions between the model migrants and the naPP. As far as we know there are no published studies over the partition coefficient of model migrants into nanocomposite polypropylene films. For that reason, the results obtained in the present study contribute to a better understanding of mass transport processes of migrants to nanocomposite film.



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*Source: 3952631-2016-01-28.xml*