Characterization and Lifetime Estimation of High Density Polyethylene Containing a Prodegradant Agent


High density polyethylene (HDPE) samples, containing different concentrations of prodegradant additive d2w®, were prepared. The properties of the samples were evaluated through differential scanning calorimetry (DSC), Fourier transform infrared spectroscopy (FTIR), rheometry, and scanning electron microscopy (SEM). The work contributes to decreasing the products made of non-biodegradable polymeric materials derived from fossil sources which are have become a problem due to their increasingly inappropriate disposal and long degradation time in the environment. The obtained results indicated that there was no degradation of the samples due to processing. No significant changes in melting temperature, crystallinity, viscoelastic behavior, molecular weight and chemical composition were observed. Images from SEM analysis showed particles on HDPE surface, attributed to prodegradant additive d2w®. Oxidation Onset Temperature (OOT) results showed that the additive d2w® accelerated the degradation of HDPE. The activation energy (Ea) was determined by Ozawa-Wall-Flynn method. The obtained values were used for lifetime estimation of the samples. At 25°C, HDPE with d2w® showed a lifetime 50% higher than that of HDPE without this additive. This fact is attributed to the presence of stabilizers in masterbatch d2w® and the absence of oxygen in thermogravimetric analysis.

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Erbetta, C. , Azevedo, R. , Andrade, K. , e Silva, M. , Freitas, R. and Sousa, R. (2017) Characterization and Lifetime Estimation of High Density Polyethylene Containing a Prodegradant Agent. Materials Sciences and Applications, 8, 979-991. doi: 10.4236/msa.2017.813072.

1. Introduction

Products made of non-biodegradable polymeric materials derived from fossil sources have become a problem due to their increasingly inappropriate disposal and long degradation time in the environment [1] . In Brazil, their consumption increased from 10 kg to 30 kg per person-year in a ten-year period. Such increase is due, basically, to the low production cost of these materials, their lightness, high mechanical resistance and ease of fabrication in various shapes, sizes and colors [2] . The widespread use of plastics, particularly polyethylene, has led to the accumulation of plastic waste, which has caused much criticism [3] .

Prodegradant additives have been used to reduce the degradation time of plastic bags. One of these additives is d2w®, produced by the British company Symphony and commercialized in Brazil by RES Brasil. They are added as concentrates or masterbatches during polyolefin resins film processing [4] . According to the literature, additive d2w® is composed by a metal stearate (typically manganese) and stabilizers. The stabilizers are added in order to protect the prodegradant additive during the melting process and to establish the elapsed time before the degradation process starts. The indicated additive concentration ranges from 1% to 3% (w/w) [5] [6] .

Some work has been conducted to understand the degradation of polyolefins, and the effect of using degradation-promoting additives in these polymers. However, there remains considerable controversy regarding the degradation of these polymers [4] [5] [7] [8] .

According to Santos et al. [9] , oxibiodegradable plastics are not supposed to be sent for either composting or anaerobic digestion or to degrade in sanitary landfills. They were designed to degrade and then biodegrade in the presence of oxygen, thus returning to the carbon biological cycle. Their specification assumes their complete digestion by microorganisms, but in a longer period than that required for composting, which is 180 days, and shorter than that of plastic waste disposed in the environment, which is many decades, even centuries.

Chelliah et al. [10] evaluated the effects of the addition of cobalt stearate (0.25%, 0.5%, 0.75% and 1.0%) in polyethylene terephthalate (PET) on the physical and mechanical properties, and thermo-oxidative degradation of PET based on FTIR and scanning emission microscopy (SEM) analysis, before and after thermal exposure. This study showed that the increased prodegradant additives loading does not contribute much to thermo oxidative degradation.

Thermal stability studies of polymers are of great interest due to their technical and commercial importance, with the kinetic analysis of thermal degradation being a central issue. Through such analyses, it’s possible to obtain the activation energy (Ea) values, which may be used to estimate the lifetime of the materials. Therefore, they are relevant to indicate the performance of the material while being used [11] .

Ea can be determined from non-isothermal thermogravimetric curves at different heating rates. In polymers, this parameter is usually determined by the Ozawa-Wall-Flynn method [12] [13] . This method considers that the activation energy of a material, for a given mass loss (conversion), is directly proportional to the dβ/d (1/T) coefficient, when the inverse of the absolute temperature (1/T), for a fixed mass loss percentage, is linearly dependent on the log of the heating rate (β) used [14] . By this method, the activation energy can be estimated from Equation (1).

E a = ( R b ) × d ( log β ) d ( 1 T ) (1)

where Ea is the estimated activation energy, R is the universal gas constant, b is an iteration variable, β is the heating rate and T is the absolute temperature. The Ea estimated is calculated using Equation (1) and a set value of 0.457/K for b in the first iteration [12] [13] .

From this result the lifetime can be estimated, for a constant conversion degree, by using Equation (2).

L o g t f = E a 2.303 * R * T f + log [ E a R * β ] a (2)

where tf is the lifetime at a certain degradation temperature (Tf) and a is a parameter that can be found in tables as a function of the activation energy and temperature (Tf) [15] .

The Ozawa-Wall-Flynn method is based on the isoconversion method, that is, the reaction mechanism is the same for a given conversion, regardless of the temperature [16] .

Although polyethylene has been extensively studied, relatively few reports actually address the investigation of the characterization of this polymer containing a prodegradant agent [17] [18] [19] . Moreover, only Maryudi et al. [19] presented a study related to lifetime estimation of high density polyethylene with a pro-degradant agent. Therefore, the aim of this study was to evaluate and compare some thermal, chemical and rheological properties of HDPE with and without d2w®, as well as estimate their lifetimes by the Ozawa-Wall-Flynn method.

2. Materials and Methods

2.1. Materials

High density polyethylene (density: 0.957 g/cm3, MFI: 7 g/10 min) was used in granulated form, as supplied by Braskem. Prodegradant additive d2w® was provided by RES Brasil in masterbatch form with low density polyethylene (LDPE) as a base polymer.

Additive d2w® was incorporated into HDPE using a Poly Drive mixer from Thermo Haake at 30 rpm, at 140˚C, for 5 min. Three mixtures were prepared, by adding 2%, 5% and 10% (w/w) of d2w® to 50 g of HDPE.

2.2. Fourier Transform Infrared Spectroscopy (FTIR) Analysis

FTIR spectra, in the 4000 - 650 cm−1 range, were obtained with a FTIR spectrometer model Nicolet 6700 from Thermo Fisher SCIENTIFIC, using attenuated total reflection (ATR) mode, with 64 scans and resolution of 4 cm−1 (Ge crystal). This test was performed to identify changes in the chemical composition of samples containing the prodegradant additive.

2.3. Differential Scanning Calorimetry (DSC) Analysis

DSC analyses were employed to determine the melting temperature (Tm), crystallinity and oxidation onset temperature (OOT). A Shimadzu apparatus model DSC-60 was used with an aluminum sample holder. The analysis conditions for the determination of Tm and of the degree of crystallinity followed ASTM D3418-12 (Standard Test Method for Transition Temperatures and Enthalpies of Fusion and Crystallization of Polymers by Differential Scanning Calorimetry) [20] . For the OOT test, synthetic air was used as a flow gas and the analysis conditions followed ASTM E2009-08 (Test method C) (Standard Test Method for Oxidation Onset Temperature of Hydrocarbons by Differential Scanning Calorimetry) [21] .

2.4. Rheometry Analysis

Rheological tests were performed in a rotational rheometer, model AR-G2 (TA Instruments), using plate-plate geometry, at 140˚C (higher than the HDPE melting temperature). The linear viscoelasticity region was determined from storage (G') and loss (G'') moduli plots as a function of strain (%), in a strain sweep test. This test also allowed the identification of the elastic or viscous domain in the rheological behavior of the samples. The frequency sweep test was performed to determine the variation of the weight average molecular weight (Mw) of the samples. The frequency was varied from 0.8 to 400 rad/s, and, as a control variable (% strain), the value of 2.5% was used, which is within the linear viscoelasticity region.

2.5. Thermogravimetric Analysis (TG)

TG measurements were performed with heating rates of 2˚C/min, 4˚C/min, 6˚C/min, 8˚C/min and 10˚C/min, in nitrogen atmosphere. A Shimadzu apparatus, model TGA-50, was used. The analysis conditions for the determination of Ea followed ASTM E1641-07 (Standard Test Method for Decomposition Kinetics by Thermogravimetry Using the Ozawa/Flynn/Wall Method) [22] and for lifetime determination followed ASTM E1877-13 (Standard Practice for Calculating Thermal Endurance of Materials from Thermogravimetric Decomposition Data) [15] . A mass loss of 10% was considered for the calculation of the activation energy.

2.6. Scanning Electron Microscopy (SEM) Analysis

A scanning electron microscope model TM3000 tabletop microscope (Hitachi), at a voltage of 15.0 kV, was used for the SEM tests, and the obtained images were processed using the TM3000 software. All samples were analyzed at room temperature (20˚C). There was no need for sample coating with gold, as this analysis was conducted under low vacuum.

3. Results and Discussion

The spectra of all the analyzed samples are presented in Figure 1. The FTIR analysis did not allow the identification of significant spectral changes between the HDPE samples with and without additive. All the bands identified in the spectra are characteristic of polyethylene, that is, stretching between 2950 cm−1 and 2850 cm−1, bending between 1470 cm−1 and 1350 cm−1 and rocking close to 700 cm−1 [23] . None of the analyzed spectra presented band close to 1700 cm−1, assigned to carbonyl group (C=O) [24] , suggesting that there was no HDPE degradation during processing.

Figure 2 shows the second-run DSC curves of HDPE, d2w® and HDPE with 2%, 5% and 10% d2w® samples. An endothermic event (melting) of similar profile was observed for HDPE samples with and without additive, contrasting to that of the d2w® sample.

Table 1 summarizes DSC obtained data of the analyzed samples. Crystallinity was calculated using Equation (3) [25] .

Crystallinity ( % ) = ( Δ H m Δ H m c ) × 100 (3)

where ΔHmc is the melting enthalpy of 100% crystalline HDPE (289 J/g) and ΔHm is the melting enthalpy of the sample.

DSC results presented in Table 1 show greater thermo-oxidative stability for

Figure 1. FTIR spectra for HDPE, d2w® and HDPE with 2%, 5% and 10% d2w® samples.

Figure 2. DSC curves for HDPE, d2w® and HDPE with 2%, 5% and 10% d2w® samples.

Table 1. DSC results.

the d2w® sample (highest OOT), which is attributed to the presence of stabilizers in the masterbatch. The OOT values of the samples of HDPE with d2w® are 8˚C to 13˚C lower than that of HDPE without additive.

The crystallinity and melting temperature of all samples were determined after removing their thermal history (second-run tests). It’s observed that the melting temperature and the crystallinity of the d2w® sample are lower than those of the other samples. Such result can be understood as far as the masterbatch base polymer is LDPE. It’s also observed that the crystallinity and the melting temperature of the HDPE with additive samples, in all concentrations, are, basically, the same of the HDPE without additive sample, due, certainly, to the small amount of d2w® added.

Through the strain sweep test, the linear viscoelasticity region could be determined as being between 0.1% and 10% of strain. The strain value chosen for the frequency sweep test was 2.5%. The obtained results from the frequency sweep test, for HDPE, d2w® and HDPE with 2% d2w® are presented in Figure 3. In this figure, the storage or elastic modulus (G’, in red) and the loss or viscous modulus (G”, in blue) are shown as functions of angular frequency. The curves (G’or G” versus angular frequency), obtained for the HDPE with 5% and 10% d2w® samples, are similar to those presented in Figure 3.

From the rheological tests, at 140˚C, it was observed that, for all samples, the viscous effect predominated over the elastic effect (G” > G’). These results suggest that the rheological behavior of HDPE was preserved in the additivated samples. The results, for the weight average molecular weight (Mw) of HDPE and HDPE with 2%, 5% and 10% d2w® samples, obtained from the frequency sweep tests (relative results, just for comparison purposes), are presented in Table 2. It can be observed that the values of Mw are in the same order of magnitude (105 g/mol), with no significant change.

SEM images of all samples are shown in Figure 4. The micrograph of HDPE is shown in Figure 4(a). It can be noted that the surface presents integrity and a non-porous appearance. In Figure 4(b), it’s shown the micrograph obtained for the prodegradant additive d2w®, where it can be observed clusters in the surface. The micrographs shown in Figures 4(c)-(e) are for the samples of HDPE with 2%, 5% and 10% d2w®, respectively. It’s possible to observe that the aspect of the samples is similar (integral and non-porous), but small particles can be seen in the surface, related to the presence of d2w®. Also, the number of particles increases as d2w® concentration increases.

Figure 3. Curves from frequency sweep test for HDPE, d2w® and HDPE with 2% d2w® samples.

Table 2. Results for the weight average molecular weight (Mw), from the frequency sweep test.

Figure 4. Micrographs for HDPE (a), additive d2w® (b) and HDPE with 2% (c), 5% (d) and 10% (e) additive d2w® samples.

For the study of the lifetime of additivated HDPE, the sample with 2% d2w® was chosen, considering the amount normally recommended, by the manufacturer, for commercial use [6] . In Figure 5 and Figure 6, TG curves, at different heating rates, for HDPE and HDPE with 2% d2w®, are presented. Both samples exhibited thermal degradation in a single step related to the complete degradation of polymer chains. Since thermal degradation occurred in a single step, at all heating rates, the Ozawa-Wall-Flynn method can be applied, in order to calculate the activation energy. A linear correlation between the logarithm of the conversion rate and the inverse of the absolute temperature, at conversion rates of 5%, 10% and 20%, indicates that the thermal degradation of both pure and additivated HDPE (2% d2w®) samples is of a 1st order reaction type.

Equation (1) and the obtained data from the curves shown in Figure 5 and

Figure 5. TG curves for HDPE, at different heating rates.

Figure 6. TG curves for HDPE with 2% d2w®, at different heating rates.

Figure 6, at 10% conversion, were used to calculate the activation energy of pure and additivated HDPE (2% d2w®) samples. The results are presented in Table 3.

From the results shown in Table 3, a higher value for the activation energy of HDPE additivated sample is observed. It means that it has a greater thermal stability in comparison to the non-additivated HDPE, probably due to the presence of stabilizers in prodegradant agent masterbatch. The opposite behavior was observed in OOT and DSC analyses, where pure HDPE showed greater stability.

Table 3. Activation Energies for pure and additivated HDPE samples (10% conversion).

Figure 7. Lifetime versus temperature for HDPE and HDPE 2% d2w® samples.

This fact could be related to the type of atmosphere used in each analysis, nitrogen in TG and synthetic air in DSC. Oxygen may induce degradation reactions of polymer chains, probably catalyzed by d2w®.

A similar behavior was observed for d2w®-additivated polypropylene in a study by Carvalho et al. [17] , using OIT (oxidation induction time), MFI (melt flow index), FTIR and mechanical tests and TG techniques to determine Ea.

The estimated lifetime of the polymers was taken as the one in which the mass loss was 10%, at different temperatures, as shown in Figure 7. The lifetime was calculated using Equation (2). From the results shown in this figure, it’s observed that the lifetime of both the additivated and non-additivated HDPE is quite high, at 25˚C, with higher values for the additivated HDPE (45 × 107 years) compared to the non-additivated HDPE (6 × 107 years). Therefore, as temperature being the only effect, in an inert atmosphere, and for a prodegradant agent concentration of 2% (w/w), the lifetime of HDPE showed an increase of 7.5 times. By zooming the curves of Figure 7 (time in min.), for a better visualization of the correlation between lifetime and temperature of the samples, one obtains the curves in the top right of this Figure. From 390˚C, a similar behavior of the samples was observed, that is, the lifetime of the additivated HDPE sample is the same that of the non-additivated one.

Roy et al. [17] determined the lifetime of LDPE (taken as the time for 5% mass loss) additivated with cobalt stearate as a prodegradant agent. The additive was directly incorporated into LDPE during extrusion, without a masterbatch, that is, without the influence of the stabilizer load, which are normally used in masterbatches. As a result, the lifetime of additivated LDPE was significantly reduced in both an inert and an oxidizing atmosphere. Maryudi et al. [19] evaluated the effect of the addition of 1% manganese laurate on HDPE. This prodegradant agent was synthesized by the authors and mixed directly to the polymer during extrusion, in a way similar to that used by Roy et al. [18] . They reported an accelerated degradation of the additivated HDPE.

These results corroborate the hypothesis that stabilizers present in the prodegradant agent masterbatch may be responsible for the increased thermal stability of additivated HDPE, when considering only the effect of the temperature under inert atmosphere.

4. Conclusions

The results presented in this study indicate that the addition of prodegradant agent d2w® to HDPE practically did not affect polymer properties: melting temperature and crystallinity, viscoelastic behavior, molecular weight and chemical composition.

Considering only the effect of temperature under inert atmosphere, the additivated polymer presented greater thermal stability (higher activation energy values), and, as a consequence, an increased lifetime. This behavior may be related to the presence of stabilizers in the masterbatch additionally to the absence of oxygen in the medium, since additivated samples were less thermally stable in an oxidizing atmosphere, as demonstrated by OOT analysis. In conclusion, the prodegradant agent became effective, that is, it really started its activity, only after the thermal degradation of the polymer had begun, when in the absence of oxygen. In presence of oxygen in the medium, the activation energy values should be much smaller than those found in inert atmosphere. Its efficiency is directly related to the presence of oxygen in the medium. The temperature, alone, does not play a fundamental role in the action of the prodegradant additive evaluated in these studies.


The authors thank the Polymer Engineering Laboratory and Composites― LEPCom UFMG, for the important collaboration in the preparation of the samples, RES Brasil Company for providing the additive, Braskem Company for supplying HDPE samples, CEMIG, PETROBRAS, FAPEMIG, CAPES and CNPq for all financial support for this research.

Conflicts of Interest

The authors declare no conflicts of interest.


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