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Engineering, Technology & Applied Science Research Vol. 12, No. 6, 2022, 9546-9550 9546 
 

www.etasr.com Hellati & Boufassa: Evaluation of the Role of Ethylene Vinyl Acetate on the Thermo-Mechanical … 

 

Evaluation of the Role of Ethylene Vinyl Acetate on 

the Thermo-Mechanical Properties of PET/HDPE 

Blends 
 

Abdelhak Hellati 

Faculty of Science and Technology 

Mohamed Bachir El Ibrahimi University 

Bordj Bou Arreridj, Algeria 

abdelhak.hellati@univ-bba.dz 

Samia Boufassa 

Faculty of Science and Technology 

Mohamed Bachir El Ibrahimi University 

Bordj Bou Arreridj, Algeria 

samia.boufassa@univ-bba.dz
 

Received: 5 September 2022 | Revised: 15 September 2022 | Accepted: 17 September 2022 

 

Abstract-In this paper, blends of recycled polyethylene 

terephthalate (r-PET) and high-density polyethylene (HDPE) 

with and without a compatibilizer were prepared using a 

Brabender Haake Rheocord at 270°C and 32rpm. Ethylene vinyl 

acetate was chosen as the compatibilizer and its proportion was 

set to 5, 7, and 10 wt%. The thermal properties and 

crystallization behavior were determined by Differential 

Scanning Calorimetry (DSC). Micromechanical properties were 

also investigated using a Vickers microindentation tester. The 

DSC analysis indicates that the melting temperature of r-PET 

and HDPE in all the blends, compatibilized and 

uncompatibilized, remains constant and almost the same as those 

of the pure component. On the other hand, it is shown that the 

degree of crystallinity of HDPE in the blends calculated by DSC 

depends on the composition of the polymeric mixture. However, 

the Hardness (H) decreases with increasing r-PET content until 

50/50 composition of r-PET/HDPE is reached, whereas for larger 

r-PET content values, H increases. The same trend was obtained 

with the addition of the compatibilizer. 

Keywords-recycled polyethelene terephtalate; DSC; hardness; 

compatibilization 

I. INTRODUCTION  

Recycling plastic waste not only preserves energy and raw 
resources but also provides an option of plastic waste disposal 
[1-3]. For both economic and environmental reasons, the 
interest in recycling polymeric materials has significantly 
increased over the last few decades [4]. Recycled polymers, 
however, are subjected throughout thermal and mechanical 
processes that result in structural and morphological changes, 
which in turn have an impact on the material qualities. 
Blending recycled polymers with unmodified polymers could 
be an approach to enhance their properties. In practice, 
formulating polymer blends is a viable method for developing 
materials with relatively new combinations of specified 
features. An important portion of post-consumer waste is made 
up of high density polyethylene (HDPE) and polyethylene 
terephthalate (PET), which are widely utilized in the packaging 
of consumer and industrial items. 

Due to the unique combination of its physical and 
mechanical properties, which include great thermal resistance, 
strong fatigue resistance, and good solvent resistance, PET has 
revolutionized the globe with its use [5, 6]. On the other hand, 
HDPE, due to its wide use in the packaging industry, 
contributes greatly to environmental degradation [7], in the 
light of the structural considerations by the absence of specific 
interactions and according to [8-10] affirming the non-
compatibility of PET with polyolefins. Due to the poor 
mechanical characteristics of PET/PE blends, compatibilizers 
must be used in order to decrease interfacial tension, which in 
turn increases morphological stability and interfacial adhesion. 
The study of the binary PET/HDPE polymeric system with the 
use of compatibilizing agents has been the subject of several 
research works. Among the most commonly used 
compatibilizers in HDPE/PET blending systems are graft 
copolymers containing reactive Maleic Anhydride (MA), 
functional groups such as MA-grafted polyethylene (PE-g-MA) 
[11, 12], HDPE-g-MA [13], and Maleic Anhydride-grafted 
Styrene-Ethylene-Butene copolymer (SEBS-g-MA) [14]. 
Another group of compatibilizers often used in research are the 
random copolymers containing GMA, such as HDPE-g-GMA 
[15], ethylene-glycidyl methacrylate copolymer (E-GMA) [16], 
Ethylene Ethyl-Glycidyl Methacrylate (E-EA-GMA) [15], and 
Ethylene Butyl Acrylate-Glycidyl Methacrylate (EBA-GMA) 
[17]. Other possibilities that are also promising have been 
investigated, such as compatibilizing the PET/HDPE system 
with an epoxy chain extender [18]. 

The indentation test is one of the easiest methods of 
determining a material's micromechanical characteristics [19, 
20]. This method has been successfully used in a wide range of 
systems and is extremely sensitive to changes in the 
morphology and microstructure of polymers. In one of our 
previous research works [21], we investigated how combining 
clay and a compatibilizer SEBS-MAH affected the 
microindentation hardness (H) of PET/HDPE.  

The objective of the current study is to investigate the 
rheological, thermal, and mechanical properties of recycled 

Corresponding author: Abdelhak Hellati



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PET (r-PET) and HDPE blends as a function of their 
composition, compatibilized with Ethylene Vinyl Acetate 
(EVA). 

II. MATERIALS AND METHODS 

The following materials were used in this investigation: 
recycled r-PET bottles from Bangkok Polyester Public Co., 
Bangkok (Thailand), commercial grade HDPE ALCUDIA 
6006 (REPSOL) with Melt Flow Index (MFI): 0.56g/10 Min. 
The EVA used is UL00218CCN from EXON CHEMICALS 
with an MFI of 1.5g/10 Min. Before blending, the r-PET pellets 
were dried in vacuum at 105°C for 16h. The dried r-PET 
pellets were dry-mixed with the HDPE pellets in the following 
weight ratios: 25/75, 50/50, and 75/25, The blends were 
prepared in a Brabender Haake Rheocord type M, at 270°C and 
32rpm in two steps. At first, the r-PET was fed into the 
chamber, and once it was melted, the HDPE and the EVA 
compatibilizer were added. From the preceding blends, films 
were prepared by compression molding in a 7102 Zwick 
machine (Ulm, Germany), at a pressure of 150kg/cm

2
. The 

compression was performed at 275°C for a duration of 6min 
(4min for preheating and 2min for compression). A Zwick 
Universal Testing Machine (UTM) was used to study the 
tensile properties of the blends as per ASTM D 638 standard. 
The crosshead speed was 50mm/min. 

The thermal study was performed with the help of a Perkin 
Elmer (Norwalk, Connecticut, USA) DSC-7 Differential 
Scanning Calorimetry (DSC) instrument in an inert N2 
atmosphere. The weights of the samples were 5–10mg. The 
studied temperature range was 50–300°C. The heating rate was 
10°C/min. The crystallinity measured by DSC ( ���� ) was 
derived from the melting enthalpy obtained by DSC with the 
following expression: 

���� =
∆��

∆�	

�     (1) 

where ∆��  and ∆�	

  are the experimental melting enthalpy 

and the melting enthalpy for an infinitely thick crystal, 
respectively. For PET, the ∆�	


 used was 140.1J/g [21] and for 
HDPE 293.86J/g [22]. 

Microhardness H was determined at room temperature with 
a Leitz (Wetzlar, Germany) microindentation tester with a 
square-based diamond indenter. The H value was derived from 
the residual projected area of indentation according to the 
following expression [23]: 

� = �
 ���     (2) 

where d is the length of the impression diagonal (m), P is the 
contact load applied (N), and k is a geometrical factor equal to 
1.854. Loads of 0.5 and 1N were applied. The loading cycle 
was 0.1min. Ten indentations were performed on the surface of 
each sample, and the results were averaged. 

III. RESULTS AND DISCUSSION 

Figure 1 shows the variation of the equilibrium torque as a 
function of the % r-PET in the blends. It was found that the 
torque of the blends without EVA decreases for up to a 50% 
increase of the amount of r-PET. Beyond this threshold, the 

torque values stabilize. The same trend was observed with the 
addition of EVA to the different blends. It was observed that 
the r-PET/HDPE (50/50) blends show the lowest torque values 
for all formulations with and without EVA. This can be 
explained by the large contact area at equivolume percentage 
between the two polymers, thus reducing the transformation 
energy of the blends. 

 

 

Fig. 1.  Variation of the equilibrium torque as a function r-PET percentage. 

 

Fig. 2.  Effect of % EVA on the equilibrium torque. 

The change in equilibrium torque was displayed as a 
function of % EVA in order to visualize the impact of the 
addition of EVA on the r-PET/HDPE (50/50) blends (see 
Figure 2). It was found that the torque increases with the 
addition of EVA up to 5% indicating that there may have been 
interactions between the polymers, which increase the flow 
resistance. Further, the torque decreases with increasing EVA 
content, which is probably due to the increase in the free 
volume created by the EVA. It was also noted from the results 
of the MFI (not shown here) that the MFI increases with the 
increasing percentage of the r-PET in the blends. This increase 
is not too significant at low concentrations of r-PET, but it is 
noticeable at high concentrations. It was also noted that the 
addition of EVA affects both polymers in a significant degree, 
slightly decreasing the MFI of HDPE and acting as a plasticizer 
for r-PET, while the blend values remain very complex. 
However, the values of the blends of r-PET/HDPE 50/50 
concentration are the lowest for all formulations with EVA 
compared to the MFI values without EVA, showing a 
resistance to flow, confirming the equilibrium torque results. 
Figure 3 shows the variation of stress at break as a function of 
the incorporation rate of R-PET with and without the addition 
of EVA.  



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The stress at break values of r-PET are higher than that of 
HDPE while their blends show lower values than those of 
homopolymers. This can be explained by the dimixture 
between these two polymeric phases due to their 
incompatibility. It should be also noted that the stress values of 
the r-PET/HDPE 75/25 blends are very close to those of the 
greater amount of component, i.e. r-PET, while the r-
PET/HDPE 25/75 blend has a stress value close to that of 
HDPE. Thus, the minor component has a dispersed spherical 
morphology in the major part and therefore the properties of 
the blends are those of the high concentration polymer as it 
absorbs all the stresses when subjected to a load or force. With 
the addition of EVA, the results are better. An addition of 5% 
EVA improves the stress at break of the blends up to 10%. This 
rise is caused by a decrease in interfacial tension, which in turn 
improves the adhesion between the two phases of the 
individual polymers. As a result, EVA has reduced the phase 
border energy, increasing the phase boundary area. The greater 
the phase boundary area, the more effectively energy can be 
transferred from one phase to another, improving the 
mechanical characteristics. 

 

 
Fig. 3.  Effect of the concentration of the EVA on the stress at break of the 
r-PET/HDPE blends. 

 
Fig. 4.  Effect of the concentration of the EVA on the elongation at break 
of the r-PET/HDPE blends. 

The incompatibility of the r-PET blends with the HDPE of 
the binary blends without EVA is reflected much more in the 
elongation at break (Figure 4), where the values obtained are 
significantly lower than those of the homopolymers for all 
compositions. The calorimeters limit such resolutions and the 
Tg of one of the components of the mixture (HDPE) is below 

0°C. On the other hand, the glass transition temperature of r-
PET, which is around 70-80°C, was not detected in some 
thermograms, perhaps due to the presence of HDPE in the 
compositions and the melting temperature Tm of the HDPE. 
Authors in [24] were able to detect the Tg of r-PET in r-
PET/PP blends of 75/25 composition and this temperature was 
almost the same as that of pure r-PET. Therefore, we limited 
ourselves to the study of the melting temperature and the 
determination of the crystallinity. The thermograms in Figures 
5, 6 reveal that the Tm values of both components were nearly 
constant throughout all of the compositions and were the same 
as those of the pure polymers. Tm = 122–131°C for HDPE and 
241–249°C for PET. As a result, the blending method had little 
effect on the cristal thikness (lc) of the components.  

 

 
Fig. 5.  DSC thermograms of neat polymers. 

 
Fig. 6.  DSC thermograms of the r-PET/HDPE (50/50) blends with and 
without EVA. 

The Thomson-Gibbs equation was employed to determine 
the lc value of each component. Consequently, the lc value 
calculated was 25nm and 14nm for PET and HDPE 
respectively. The crystallization temperatures for the r-PET 
component were found to have somewhat decreased values. 
The crystallinity decreased as the r-PET level increased for all 
compositions (pure blends and blends with compatibilizer). 



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Figure 7 shows the H of the various blends as a function of 
the r-PET content. The H's additivity behavior is depicted as a 
straight line. It is evident from the plot that neither the 
uncompatibilized nor compatibilized blends with EVA respect 
the additivity law of a binary blend as a function of 
composition. With increasing PET content, the blends became 
harder and deviated from linearity. EVA caused a reduction in 
H, which was more evident as the compatibilizer concentration 
increased. According to the two-phase model, the H of a 
semicrystalline polymer can be described by [22]: 

� = ������ ∅� + ���
����  ����� +  ��

���� �1 − � !�1 − ∅     (3) 

Equation (3) considers the compositions of the blends as 
well as the crystalline Hc and amorphous Ha hardness of each 
individual component. The H values for the blends with EVA 
were noticeably lower than those obtained from the additivity 
law in accordance with (3). It is evident that the 
compatibilizer's two primary effects on these blends were a 
decrease in their crystallinity and a concurrent decrease in their 
hardness. 

TABLE I.  PURE r-PET/HDPE BLENDS AND BLENDS WITH EVA  

Composition 
HDPE 

crystallinity (%) 

Tm (°C) 

r-PET 

Tm (°C) 

HDPE 

r-PET.HDPE (100/0) 0 249 129 

r-PET.HDPE (75/25) 0.15 248 130 

r-PET.HDPE (50/50) 0.23 249 127 

r-PET.HDPE (25/75) 0.49 247 130 

r-PET.HDPE (0/100) 0.53 247 129 

r-PET.HDPE/EVA(100/0/5) 0 248 126 

r-PET.HDPE/EVA (75/25/5) 0.09 249 128 

r-PET.HDPE/EVA (50/50/5) 0.08 248 129 

r-PET.HDPE/EVA (25/75/5) 0.12 246 129 

r-PET.HDPE/EVA (0/100/5) 0.23 249 130 

r-PET.HDPE/EVA(100/0/7) 0 248 129 

r-PET.HDPE/EVA(75/25/7) 0.09 248 127 

r-PET.HDPE/EVA (50/50/7) 0.03 249 128 

r-PET.HDPE/EVA (25/75/7) 0.09 246 130 

r-PET.HDPE/EVA (0/100/7) 0.10 248 129 

r-PET.HDPE/EVA(100/0/10) 0 246 127 

r-PET.HDPE/EVA(75/25/10) 0.10 249 129 

r-PET.HDPE/EVA (50/50/10) 0.18 248 127 

r-PET.HDPE/EVA (25/75/10) 0.10 247 129 

r-PET.HDPE/EVA (0/100/10) 0.12 249 128 

 

 

Fig. 7.  Hardness dependance on the r-PET content with and without EVA. 

IV. CONCLUSION 

It is evident from the obtained results that PET was 
incompatible with HDPE, but the presence of EVA as a 
compatibilizer allowed combinations of these polymers. The 
compatibilization of blends with additional small quantities of 
EVA in one processing step is an interesting proposal, 
particularly for recycled blends, because it does not require 
prior expensive synthesis and leads to better results. The r-
PET/HDPE 50/50 blends show the lowest torque values for all 
formulations with and without EVA caused by the large contact 
area at equivolume percentage between the two polymers. The 
Tm values of both components were nearly constant for all 
compositions and were the same as those of the pure polymers. 
The composition was the only factor influencing the 
crystallinity of the r-PET/HDPE blends (pure blends and 
blends with compatibilizer), whereas the PET affects the 
crystallizability of the HDPE component. The blending method 
had little effect on the cristal thikness of the components and 
the calculated values for PET and HDPE were 25nm and 14nm 
respectively. Moreover, the presence of the EVA strongly 
induced a hardness decrease in the blends. 

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