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Article

Non Isothermal Crystallization Kinetics and Isothermal Decomposition of Poly(Ethylene-Co-Vinylalcohol/Poly(D,L-Lactic-Co-Glycolic Acid) Blend

by
Mohamed Ouladsmane
1,
Waseem Sharaf Saeed
1,2,*,
Abdel-Basit Al-Odayni
1,2,
Ahmed Yacine Badjah Hadj Ahmed
1,
Abdulaziz Ali Alghamdi
1,
Abdullah Al-Kahtani
1 and
Taieb Aouak
1,*
1
Chemistry Department, College of Science, King Saud University. P. O. Box 2455, Riyadh 11451, Saudi Arabia
2
Engineer Abdullah Bugshan Research Chair for Dental and Oral Rehabilitation, College of Dentistry, King Saud University, Riyadh 11545, Saudi Arabia
*
Authors to whom correspondence should be addressed.
Crystals 2020, 10(6), 425; https://doi.org/10.3390/cryst10060425
Submission received: 28 April 2020 / Revised: 22 May 2020 / Accepted: 25 May 2020 / Published: 26 May 2020

Abstract

:
A series of poly(ethylene-co-vinylalcohol)(PE-VOL)/poly(D,L-lactic-co-glycolic acid (PD,L-LGA) blends with different compositions was prepared by solution casting, and its miscibility was proved through viscosimetry and differential scanning calorimetry (DSC) methods through a positive value of α (San et al. Eq.) and negative value of χ1,2 (Nishi–Wang Equation). XRD analysis of the PE-VOL/PD,L-LGA system revealed a homogeneous distribution of PE-VOL molecules aggregated in the PD,L- LGA matrix and the crystalline structure of the semi crystalline copolymer was conserved in the blend in aggregated form. It also revealed that the amorphous copolymer dispersed in the blend acted as a weak nucleating agent. The non-isothermal crystallization kinetics of neat semi-crystalline copolymer and the blend was used to describe the crystallization process using the Ozawa approach. The thermal stability of these materials was investigated by the thermal gravimetry analysis. The isothermal decomposition of copolymers and their blend were carried out by high resolution mass spectrometry using direct-analysis-in-real-time method. Relevant results that could highlight the miscible character of this blend are revealed through comparison of the different fragments resulting from the decomposition of the blend with those of the pure components.

1. Introduction

During the last two decades, a significant number of works have emerged relating to the preparation and study of the properties of polymeric materials with a view to their use as scaffolding in the biomedical field. Among the investigations reported, very few articles have been published on the relationship between the crystallization behavior, crystallinity, and physical and mechanical properties of polymeric material on its biogedradation rate. Indeed, it is well known that the biodegradation rate is slower in a semi-crystalline polymer compared with that in homocrystal form [1,2]. Other authors have reported that biodegradation is depressed in polylactide stereo-complex crystals compared to that in homo-crystals [3,4]. Consequently, a more detailed study of the crystallinity and the way in which the crystals develop in the polymer matrix is essential in order to better define the biodegradable property of polymer as a candidate for use as scaffold in the biomedical field.
Poly(ethylene-co-vinylalcohol)(PE-VOL) is a flexible semi-crystalline thermoplastic. This semi-crystalline copolymer is characterized by its excellent thermal stability [5], chemical resistance [6], good mechanical properties [7], biodegradability, and non-toxicity [8]. The presence of a large number of hydroxyl groups in this copolymer allows it to degrade easily in enzymatic media [9,10,11,12]. The presence of hydrophobic ethylene units in the PE-VOL main chain sufficiently reduces its high swelling capacity in water, which provides it the good performance in the biomedical domain, particularly in drug delivery and scaffold development. PE-VOL is fabricated by a two-step process: (i) by copolymerization of vinyl acetate with ethylene; (ii) then by hydrolysis of the vinyl acetate units of the copolymer obtained to obtain the final product. In the biomedical field, this copolymer is used by Guerra et al. [8] to investigate the activation of human plasma prekallikrein as a hemo-compatibility test. Matsumoto et al. [13] applied PE-VOL as a membrane to investigate the hemodialysis field.
According to different other investigations reported in the literature, when PE-VOL is employed as a membrane in the biomedical field, it adsorbs few plasma proteins, interacts weakly with cell components in blood [14,15], and inhibits the adsorption of plasma proteins, thereby inhibiting the body’s reaction to the membrane [16,17]. Young et al. [18] developed membranes based on PE-VOL with smooth and particulate morphologies for neuronal culture application.
PD,L-LGA is principally synthesized by two distinct methods: the direct polycondensation between glycolic acid and lactic acid, thus producing a copolymer characterized by low molecular weight [17,18,19,20]. The lateral methyl groups present in the lactic acid units of this copolymer increase its hydrophobic character and subsequently control its biodegradability. The hydrolysis of PD,L-LGA leads to modifications of its specific parameters such as the molar mass, water content, and mechanical and thermal properties [21]. Consequently, PD,L-LGA is composed of two distinct sequences; the first one is formed from lactic acid (LA) and the second from glycolic acid (GA) units. Consequently, the LA unit sequence includes sequence includes three enantiomers due to the presence of an asymmetric carbon in the LA unit. The LA unit sequence comprises three enantiomers resulting from the presence of an asymmetric carbon in its structure, which are L-PLA, D-PLA, and D, L-PLA. L-PLA and D-PLA enantiomers have a semi crystalline structure, while the D, L-PLA is characterized by an amorphous structure because of the irregularity of the L and D units in the polymer chain [22]. The racemic form is more preferred as a carrier [23] in the drug-carrier system because of the homogenous distribution of drug particles in this specific material. PD,L-LGA based drug delivery devices have been experimented for tissue engineering [24,25,26], vascular engineering [27,28,29,30], nerve regeneration [19,31], cartilage tissue engineering [5,32,33,34], and bone tissue engineering [12,35,36,37]. PD,L-LGA has been the subject of several publications in the biomedical field. Indeed, because of its biocompatibility and biodegradability, this copolymer was used as carrier in the drug delivery domain and as materials in tissue engineering applications. The combination of the PE-VOL with PD,L-LGA undoubtedly gives new hybrid materials characterized by intermediate properties. By controlling the ratio of the components, the new resulted properties of the materials can be easily adapted to the desired functions. Despite the highly desirable properties of these copolymers and the new properties that can be generated by their combinations, we have only found the presence of a very limited number of works published in the literature on a blend involving one of these two copolymers, and still very few subjects on their crystalline properties and on the crystallization processes. Note that the mechanical and thermal properties of a semi-crystalline polymer depend on its crystalline mode and its crystallization mechanism. Among the most relevant articles found in the literature on the crystallization of a blend involving PE-VOH was that of Luo et al. [38]. These authors have studied the blend of two semi-crystalline polymers, PE-VOH and polypropylene (PP) obtained by fusion using poly(propylene-graft-maleic anhydride as compatibilizer.
The isothermal crystallization kinetics was used as method to carry out this study and the results obtained were an increase of the overall rate of the crystallization process of PP by incorporating of PE-VOL in the blend and this copolymer acted as an effective nucleating agent for PP. The X-ray diffraction of neat PP and blends revealed identical crystal structure. Recently, the non-isothermal crystallization of a blend involved PE-VOL and poly(valerolactone) prepared by solvent casting method was investigated by our research group [39]. It was revealed that the miscibility of this blend was miscible in all compositions and at certain temperatures the crystallization rate decrease 2- to 4-fold compared with those of pure components. Zhu et al. [40] investigate the non-isothermal crystallization of PE-VOL combined with poly(oxypropylene) diamine intercalated montmorrilonite prepared by solvent casting method. These authors used the Mo and Ozawa methods to study the non-isothermal crystallization process and the results obtained revealed a perfect description when the Mo’s method is used. The incorporation of the clays nanoparticles in the blend matrix had a heterogeneous nucleation effect to accelerate the crystallization of the PE-VOL despite hampering the macromolecular chains motion. Note that during our literature survey, we did not come across any work done on the crystalline behavior of a semi-crystalline polymer blended with the PD,L-LGA of amorphous structure. Given the importance of the properties of the copolymers cited above their implications in the blends with other polymers undoubtedly make it possible to develop new materials which could be candidates as scaffolds in the biomedical field. In order to understand the structure-properties relationship of these materials, we were very interested to know the crystalline behavior and the crystallization mechanism of this semi-crystalline copolymer when is combined with amorphous PD,L-LGA in a miscible blend.
In this way a series of blends based on semi-crystalline PE-VOL and amorphous PD,L-LGA blend with different compositions was prepared by solvent casting method in which the miscibility, crystalline behaviors, and non-isothermal crystallization kinetics of PE-VOL in the blend were widely studied using viscosimetry, X-RD, and DSC techniques. The thermal stability and the fragments generated from isothermal decomposition of the blend and its components are investigated by thermogravimetry analysis (TGA) and direct analysis in real time mass spectrometry (DART-ToF-MS).

2. Experimental

2.1. Materials

Poly(ethylene-co-vinylalcohol) (PE-VOL) (28 mole% of ethylene unit) and amorphous poly(D,L-lactic-co-glycolic acid) (PD,L-LGA) (PL:GA equal ratios, 65,000 g mol–1) were supplied by Purac (Groningen, The Netherlands). Dimethylformamide (DMF) (99% purity) was purchased from Sigma-Aldrich (Taufkirchen, Germany). Polymers and the solvent were used without further purification.

2.2. Blend Preparation

PE-VOL/PD,L-LGA blend was prepared by dissolving 10 wt % of each copolymer in DMF until a perfectly clear and transparent solution was obtained. This solution was then poured onto a perfectly horizontal Teflon plate for 48 h in order to vaporize the solvent and obtain a film of homogeneous thickness. The film obtained was then dried in the oven under vacuum maintained at 50 °C for 24 h to completely extract the residue of the DMF clustered in the polymer film. PE-VOH/PD,L-LGA films containing 10, 25, 50, 75 and 90 wt % were prepared by the same method and the preparation conditions are gathered in Table 1. The thickness of each film obtained was measured by a Digital Micrometer Mitutoyo 293-340-30.

2.3. Analyses

The viscosity measurements of the blend and their neat components were carried out in DMF at 40 °C employing a viscosimeter Ubbelohde Scott Gerate type Avs 310 and the method used to reach this goal was in detail described in the literature by Soria et al. [41].
X-ray diffraction patterns of copolymers and their neat components were obtained using a BRUKER D8 advance diffractometer and a run with CuKα radiation of 40 kV and 40 mA at a scanning rate 2θ of 2° min−1. DSC analysis of blends and their components were carried out on a Shimadzu DSC 60A (Kyoto, Japan) previously calibrated with indium. Samples containing between 8 and 15 mg of blend or neat copolymers were packed in aluminum DSC pan then placed in the DSC cell. Samples were scanned between −30 and 240 °C at a heating rate of 10 °C min−1. The glass transition temperatures, Tgs, and those of fusion, Tms, of polymer samples were deduced from the thermograms obtained from the middle of the first point of transition and the top of the endothermic peak corresponding to the fusion, respectively.
To destroy all the nuclei that can act as crystal grains the heating of the samples was then maintained for 5 min at 200 °C before being cooled. These specimens were then cooled down to 50 °C at constant rates of 10, 12.5, 15.0, 17.5, and 20°C min−1, respectively. To maintain a uniform thermal history in all samples, the thermal traces were considered by the data of the second run, after quenching above the glass transition temperature. Note that the results obtained were perfectly reproducible after three runs and no degradation of samples was detected on the thermograms obtained during all the heating process. The non-degradation of the samples was also confirmed by a solubility test on the samples after DSC analysis. The TGA thermograms of net copolymers and their blends were traced on a Shimadzu TGA60 under a stream of nitrogen. Samples weighing between 10 g and 14 g were carefully placed in TGA aluminum pans then scanned by heating from 25 °C to 600 °C at a constant heating rate of 20 °C∙min−1. The fragments resulted from the isothermal decomposition of blends and their pure components were analyzed by an Accu-ToF LC-plus JMS-T100 LP mass spectrometer JEOL (Tokyo, Japan) working with a direct-analysis-in-real-time (DART) ion source (Ion Sense, Saugus, MA, USA). The samples were used without any prior preparation. The fragments resulted from the decomposition process were evaporated in a stream of He atmosphere heated at constant temperatures (350 and 380 °C). Heated helium/Vapor mixture was then ionized by excited metastable helium atoms, before entering the ion source of the time-of-flight mass spectrometer. All the samples were analyzed by DART-ToF-MS using Accu-TOF mass spectrometer acquired from JEOL (Tokyo, Japan). The experimental conditions were: vacuum level 1.3 × 10−5 Pa, He used as a heating and ionization gas, ring lens with a voltage of 4 V, peaks voltage of 500 V, and the mass resolution was ranged between 3600 and 4900.

3. Results and Discussion

3.1. Viscosimetry Analysis

The specific viscosities, ηsp, of copolymers and blends solutions were determined at different concentrations in DMF from the efflux time measurements. The intrinsic viscosity of the blend as well as those of their components, [η], was deduced from the intercept obtained by extrapolation of the linear curve indicating the variation of ηsp as a function of its concentration obtained according to the Huggins equation: [42]
η s p = η C + k η 2 C 2  
where C and k symbolize the concentration of neat copolymer or blend in DMF and the Huggins-constant of the polymeric solution, respectively. The viscosimetric parameter, α, which provided the interaction intensity between the polymer chains of different natures in the blend, was estimated using the San et al. Equation (2) [43]:
α = k b k 2 η 2 2 w 2 2 + k 3 η 3 2 w 3 2 + 2 k 2 k 3 η 2 η 3 w 2 w 3 ( η 2 w 2 + η 3 w 3 ) 2  
where kb and ki are the Huggins-constant of the blend and that of the component (i), [η]i and wi are the intrinsic viscosity and the weight fraction of the copolymer (i) in the solution, respectively. According to the Sun et al. approach, a miscible blend is characterized by a positive or nil α value which indicates the presence of attractive forces between the two different chains in the blend in solution. Inversely, a negative α value reveals repulsive forces leading to the phase’s separation. Indeed, the results of the α interactional parameter obtained as illustrated in Table 2 reveals positive values for PE-VOL/PD,L-LGA system in all the investigated composition range. So, the miscibility of this pair of copolymers was due to the hydrogen bonds interactions developed between the different copolymeric chains.
The X-RD spectrograms taken for the pure PE-VOL and PE-VOL/PD,L-LGA systems with different compositions are showed in Figure 1. The spectrogram of pure PD,L-LGA containing equal an PLA/PLG composition revealed the absence of any peaks, indicating an amorphous structure of this copolymer, as reported in the literature [44]. In contrast, the spectrogram of the pure PE-VOL revealed three typical peaks at 19.86, 22.5, and 41.23 2θ corresponding to the reflexion planes attributed to the crystalline monoclinic form of this copolymer containing 72 mol% of vinylalcohol unit [45]. Indeed, according to Carrada et al [46]. the crystalline form of PE-VOL depends on the ethylene/vinylalcohol composition and also on the crystallization conditions. It was also reported by the same investigators that the final crystallographic properties of PE-co-VAL can be determined through the control of temperature during cooling in the final stage of the crystallization process. They revealed that at slow cooling rates, different types of crystal structures are obtained, whereas at fast cooling rates or quenching (e.g., at 100 °C/min), only the orthorhombic structure is obtained for all ethylene/vinylalcohol compositions. The X-RD patterns of the PE-VOL/PD,L-LGA blend with different compositions showed practically the same peaks as those of pure PE-VOL, although their intensities decreased as the PD,L-LGA in the blend increased. This fact can be explained by the homogeneous distribution of PE-VOL molecules aggregated in the PD,L-LGA matrix; thus, the crystalline aggregates conserve their crystal structures in the PE-VOL/PD,L-LGA blend. The dispersed phase of amorphous polymer acted as a weak nucleating agent.

3.2. DSC Analysis

3.2.1. Miscibility of PE-VOL/PD,L-LGA Blend

(A) Glass transition temperature
The heating DSC curves of neat PD,L-LGA, neat PE-VOL and those of their blends with different compositions are presented in Figure 2. As shown in the curve profiles of the blends a confused transition zone is localized between 32 and 60 °C in which the Tg values cannot be localized accurately because of the small difference existing between the Tgs of the pure components PE-VOL(51 °C) and PD,L-LGA(36 °C) in which this gap does not exceed 15 °C. Consequently, the criterion which stipulates that the miscibility of a pair of polymers can proofed by the presence in the thermogram of the blend of an unique Tg cannot be rigorously applied. The same thermograms also show an important depression in the melting temperature of PE-VOL incorporated in the blends with increasing PD,L-LGA content. This finding indicates that the crystalline yield of PE-VOL in the blend dramatically decreased.
Similar results were also observed by different authors using poly(butylene succinate-co-butylene carbonate)/Poly(vinylphenol) blend [47], poly(trimethylene terephthalate)/amorphous poly(ethylene terephthalate) blends [48], and poly(vinylidene fluoride) (PVDF)/poly(methyl methacrylate) (PMMA) blends [49]. This phenomenon may be thermodynamically traduced by the energy of the mixture accompanied by the exothermic interaction energy between the crystalline part of PE-co-VAL and that of the amorphous part of PL-co-GA.
(B) Melting temperature
The DSC thermograms of Figure 2 also show the melting temperatures of the blends and these of their pure components and the data of the apparent melting temperatures and the heat of melting deducted are gathered in Table 3. As can be seen from the thermal curves, of the blends only one endothermic peak was observed which is assigned to the apparent melting temperature of the PE-VOL semi-crystalline component. These thermal curves also reveals an important depression of the Tm of this semi crystalline copolymer from 188 to 156 °C when is blended with PD,L-LGA.
The decrease of the melting temperature in a semi-crystalline polymer in a miscible blend is due to the thermodynamic interactions between its components. Indeed, the Flory–Huggins theory stipulates that a miscible blend containing a semi crystalline polymer is principally characterized by a depression in its melting temperature permitting the determination of interaction energy. In this same direction, the melting temperature of such polymer is principally affected by different thermodynamic parameters and also by its crystal thickness. In this same way, Hoffman–Weeks method permits the isolation of the morphology parameters from the undesired effects that act on the melting temperature of semi-crystalline polymer in its miscible blend using the equilibrium melting temperature,   T m o , expressed by Equation (3) [50]:
T m = η T c + 1 η T m o
The isothermal crystallization process of pure semi-crystalline copolymer and in its blends were realized at different crystallization temperatures, and results obtained for the neat PE-VOL and the PE-VOL/PD,L-LGA containing equal ratio of each component are plotted in Figure 3. Based on the variation of the apparent melting temperature, Tm, versus the crystallization temperature, Tc it was possible to deduct η relative to the pure PE-VOL and that in their blends as presented in Figure 4 for the neat PE-VOL and PE-VOL/PD,L-LGA50 system with equal ratios of each component. Indeed, straight lines were obtained and η and T m o are deduced from the slope of the Hoffman–Weeks plot and the intercept of these curves with the straight Tm = Tc, respectively. It is important to note that the η value varied between zero and the unity. This parameter is used to estimate the stability of molten crystals. Indeed, when the η   value is close to zero this indicates that the crystals is in its maximum stability and when this parameter is close to one this indicates that this crystals is in its instability state. T m o and η values for pure PE-co-VAL and in the blends are listed in Table 4.
As can be seen from these data, the equilibrium melting point of PE-VOL was found to be 184.9 °C, which agrees with that found in literature (187 °C) [51] Concerning the PE- VOL/PD,L-LGA systems, the T m o of the PE-VOL phase decreased with PD,L-LGA content to reach a minimum of 166.8 °C when the polyester in the blend was 90 wt %. In other terms, the maximum extent of this melting temperature depression was 18.1 °C when the pure PE-VOL was converted to the PE-VOL/PD,L-LGA10 blend. In general, the η values of PE-VOL in its blend, which varied from 0.12 to 0.34, are relatively small, revealing the stability of pure PE-VOL and PE-VOL in the blend. This parameter decreased slowly with increasing PD,L-LGA content to lose about two-thirds of the crystal stability of PE-VOL when 90 wt % of the polyester was incorporated. This suggests that the PE-VOL crystals become less and less stable, i.e., they have less thick lamellar thicknesses, when blended with PD,L-LGA. This fact is probably attributed to the morphological effect.
To rigorously confirm the miscibility of this pair of copolymers, noted by its appearance, it was necessary to use the Flory thermodynamic interaction parameter, χ 1 , 2 ,   determined from the equation of Nishi and Wang, Equation (4) [52], based on the Flory–Huggins theory.
Δ T m = T m o T m = R ( V u 2 ( T m o ) 2 χ 1 , 2 Δ H u 2 V u 1 ) φ 1 2
where the subscripts 1 and 2 designate the amorphous PD,L-LGA copolymer and the semi crystalline PE-VOL copolymer, respectively. φ 1   is the volume fraction of polymer-1. Vu and ΔHu are the molar volume and the molar enthalpy of fusion of the repeating units, respectively. R is the gas constant. χ1,2 value is deducted from the slope of the linear curve of Figure 5, indicating the variation of Δ T m versus the square of φ 1 , and the data collected from the literature in which ΔHuPE-VOL = 4.22 kJ mol−1 [53] and VuPE-VOL = 37.80 cm3 mol−1 [54] VuPD,L-LGA = 88.06 cm3mol−1 calculated from the density of PD,L-LGA and the molar masses of lactide and glycolic acid co-monomer units. χ1,2 and the interaction energy density between blend components, B, calculated from the R T m o χ 1 , 2 V u 1 1   term of Nishi’s equation for this pair of polymers are −0.27 ± 0.02 and −11.67 ± 0.86, respectively. The negative sign of these values indicates miscibility in the amorphous part of the PE-VOL/PD,L-LGA system in all investigated compositions. These values are comparable to those created between the ester and hydroxyl groups in the polymer blends such as those investigated by Kuo et al. [55] on the phenolic resin/poly(ε-caprolactone) system, which were χ 1 , 2 = −0.35 and B = −12.51. The interaction involved in the miscibility of this blend is principally caused by the hydrogen bonds developed between the carbonyl group of PD,L-LGA and the hydroxyl group of PE- VOL units.

3.2.2. Crystallization Behavior of PE-VOL/PD,L-LGA Blend

DSC analysis carried out in its cooling mode at different temperatures ranged between 10 °C and 20 °C on the neat copolymers and their blends with different compositions led to the thermograms that can be seen in Figure 6. As can be noted from these obtained thermal curve profiles the crystallization temperature, Tc, of PE-VOL, taken from the top of the crystalline peaks, depressed with increasing PD,L-LGA content in the blend. As indicated in Table 5, the crystallization enthalpy, ΔHc, corresponding to the area of the exothermic peak decreased with increasing the PD,L-LGA content, thus causing an important depression in the crystallinity of PE-VOL in the blend. The incorporation of PD,L-LGA in the PE-VOL matrix makes it difficult to transport the chain segments of this semi-crystalline copolymer towards the crystallization front and, therefore, supercooling is, in this case, necessary for crystallization. Therefore this also limits thickening and perfection of the PE-VOL crystals, thereby causing a depression of the Tm and Tc values of this copolymer, as shown in Table 4. In general, the crystallization enthalpy of PE-VOL in the blend shifted toward the low temperature with increasing cooling rate. Similar behavior was also observed in our previous investigations using poly(ethylene-co-vinyl alcohol)/poly(maleic anhydride-alt-ethylene) [56] and by Guo et al. [57] using Poly(ε-caprolactone)/epoxy resin blend. According to these authors, the dispersed phase of the amorphous copolymer interacted as a weak nucleating agent.

3.2.3. Non Isothermal Crystallization Kinetics of PE-VOL and PE-VOL/PD,L-LGA Blend

The determination of the crystallinity degree, X c , is obtained from the latent heat of the crystallization of crystalline polymer in the blend during the crystallization process. This parameter is expressed according to Equation (5) [58]:
X c ( % ) = Δ H c ( 1 φ ) × Δ H m × 100
where Δ H c   represents the apparent latent heat of crystallization of PE-VOL in the blend and Δ H m the extrapolation of the latent heat corresponding to the melting of PVA 100% crystalline. Note that the Δ H m   taken from the literature has an average value of 157.8 J·g−1 [59] φ is the mass fraction of the amorphous copolymer (PL-co-GA) incorporated in the blend. The values X c for PE-VOL and PE-VOL/PD,L-LGA blend with different PE-VOH contents obtained from this equation are gathered in Table 4. Figure 7 shows the effect of the dispersion of PD,L-GLA in the blend on the non-isothermal crystallization kinetics of PE-VOL in the blend. As can be seen from these thermal curve profiles, the peak of the crystallization enthalpy is lower when the PD,L-LGA content in blend was 10 wt %. On the other hand, as in case of the neat PE-VOL, it was observed that, for all blend compositions, the   T c value of PE-VOL slowly shifted toward the lower temperatures as the cooling rate increased. This phenomenon was also revealed by different investigators [60,61,62] and attributed this fact to a reduction of chain mobility and flexibility limiting the time of diffusion inside the crystalline lattice of the PE-VOL matrix. This fact leads to reduce the crystallization rate of the semi-crystalline copolymer in the blend. Indeed, when the blend samples are cooled down at relatively high cooling rates, the movement of PE-VOL chains do not seem to follow the cooling temperature regime imposed over time due to the influence of thermal hysteresis, which leads to a lower maximum crystallization temperature. When incorporated into the PE-VOL matrices, the macromolecular chains of PD,L-LGA act as an energy barrier preventing heat transfer to the PE-VOL chains. Therefore, at a high PD,L-LGA content in the blend, the crystallization process occurs at a relatively low temperature.
The degree of relative crystallinity, X T , of PE-VOL in the blend versus temperature is given by Equation (6) [63]:
X T = T o T d H d T d T T o T d H d T d T  
where T o and T are the beginning and finishing crystallization temperatures measured at the starting and finishing inflections of the crystallization peaks, respectively. H is the heat of the crystallization process of neat PE-VOL or PE-VOL in the blend at temperature, T. X T   can be determined after replacing integrations functions by the areas under the DSC crystallization peaks in the DSC thermograms from T = T o to T = T ( A T ) and the area under the total crystallization peak ( A T ), Equation (6) becomes:
X T = A T A  
The variation of the relative crystallization time, X t is calculated from the temperature T at crystallization time t and the cooling rate β according Equation (8):
t = T o T β
Typical plots of the variation of the relative crystallization degree of neat PE-VOL and PE- VOL in the blend as function of temperature, X T , and time, X t , are obtained during the non isothermal crystallization process and the curves of pure PE-VOL and PD,L-LGA/PE-VOL50 taken as examples are presented in Figure 8A,B, respectively. Sigmoid pattern was obtained for each sample and the rate of the crystallization deducted from the slope is almost constant between 20% and 80% of the relative crystallinity and due to the spherulite impingement effect, these curve profiles tend to become flat beyond [58].
The half time, t1/2, of the crystallization process was deducted from the curves of Figure 8B at 50% of the relative crystallization of pure PE-VOL and PD,L-LGA/PE-VOL systems and the data obtained are plotted in Figure 9. For the pure PE-VOL, in general these curve profiles reveal an increase in the t1/2 with increasing the cooling rate. On the other hand, when the PD,L-LGA was incorporated in the PE-VOL matrix the t1/2 passed by a minimum at 30 wt % of this amorphous copolymer in the blend. Indeed, the crystallization process of PE-VOL in the blend was dramatically decelerated when the PD,L-LGA content was 30%, in which the t1/2 loses 45% – 83% of its value depending on the cooling rate. This observation can be explained by the fact that at a relatively low PD,L-LGA content, the macromolecular chains of this last copolymer cluster cannot restrict the motion of the PE-VOL macromolecular chains but act as heterogeneous nucleating agents during the non-isothermal crystallization process and therefore accelerate the crystallization. At a higher PD,L-LGA content, the macromolecular chains of PD,L-LGA clusters act as a barrier that restricts the thermal motion of PE-VOL macromolecular chains and therefore retards the formation of crystals. As a result, the addition of a large amount of PD,L-LGA can delay the overall crystallization process.
Among many models that have been developed to investigate the non-isothermal ctystallization kinetics [64,65,66,67] the Ozawa Equation (9) extended from that given by Avrami Equation (10) [68] is adopted in this work to study the non-isothermal crystallization kinetics of the PE-VOL/PD,L-LGA blend and its pure semi-crystalline component.
1 X T = e x p ( k T β m )
1 X t = e x p ( k t n )
The Avrami equation originally applied for isothermal crystallization is also applied for non-isothermal crystallization by assuming that the specimen is cooled at a constant cooling rate. Note that Xt and XT represent the relative degrees of crystallinity at time (t) and temperature (T), respectively, k and kT are the crystallization kinetics rate constant and the cooling function of non-isothermal crystallization at temperature (T), respectively, β is the cooling rate, and n and m are the isothermal Avrami and the Ozawa exponents depending on the dimension of crystal growth and nucleation mechanism, respectively. Equation (10) can be linearized as follows:
l n [ l n ( 1 X T ) ] = l n k T m l n β
As can be seen from the plots of ln[−ln(1 − Xt)] versus ln(β) for PE-VOL and PE-VOL/PD,L-LGA systems in Figure 10, all specimens containing different PD,L-LGA contents showed straight lines indicating that the Ozawa equation Equation (8) described the primary process of non-isothermal crystallization of pure PE-VOL and its blends perfectly. The values of kT and m deduced from the intercept and slope of these curves, respectively, are gathered in Table 6. As can be seen from these data, the value of m for pure PE-VOL increased from 1.24 to 1.55 with the crystallization temperature, which agrees with the results of the literature [69]; however, the values of m for the blends, in general, are opposite that of pure PE-VOL and randomly fluctuated between 1.55 and 3.60 depending on the temperature and PE-VOL/PD,L-LGA composition, suggesting that the introduction of PD,L-LGA content in the PE-VOL matrix does not significantly influence the growth of crystals. In certain cases of PE- VOL/PD,L-LGA systems, the small increase of m observed when the temperature increased reveals a small change in the crystallization mechanism, probably due to the decrease in the viscosity of blend caused by a rupture of the strong interactions between hydroxyl groups of PE-VOL chains for the profit of the weak interactions between hydroxyl of PE-VOL and carbonyl of PD,L-LGA. The increasing m values are usually attributed to the change from instantaneous to sporadic nucleation [70] According to typical polymer crystallization reports, an m value of 2 indicates that the crystal growth is sporadic and spherical and occurs from nuclei. Heterogeneous nucleation has been suggested for fractional m values in polymer crystallization [71] The kT value related to the all over crystallization rate decreased when the temperature decreased, except in the blend with 25% of PD,L-LGA content in which this parameter increased. This means for PE-VOL and PE- VOL/PD,L-LGA blends with PD,L-LGA content inferior to 25 wt%, the crystallization rate increased when the temperature decreased, especially in the case of pure PE-VOL, in which this parameter dramatically decreased. In addition, kT values depend on the PE-VOL/PD,L-LGA composition.
The crystallization activation energy ( E c ) associated with the overall crystallization process is evaluated from the rates of crystallization using the Kissinger Equation (12) [72]:
E c = d [ l n ( β / T c 2 ) d ( 1 / T p ) R
where R and T c   are the gas constant and the peak crystallization temperature, respectively. E c is obtained from the slope of the plots Rln(β/Tc2) versus 1/T of Figure 11. The curve (on the top) indicating the variation of the crystallization activation energy versus the PE-VOL content showed that the   E c passed by a maximum at 337 ± 12 Kj when the PE-VOL content in the blend was 75 wt %. The increase in E c   can be explained by the increase in the miscibility of PE-VOL/PD,L-LGA system because increasing the PD,L-LGA in the blend results in dilution of PE-VOL chains at the crystal growth front and contributes to the reduction of mobility of PD,L-LGA chains due to the higher Tg of the blend than that of pure PE-VOL, thus a higher value for PE-VOL crystallization occurs in the blends.

3.3. TGA Analysis

The thermal stabilities of the pure PE-VOL and PD,L-LGA and the PE-VOL/PD,L-LGA blend investigated by the TGA method are shown in the thermograms of Figure 12. One, two, and three principal decomposition stages were observed for PD,L-LGA, PE-VOL, and blends, respectively. The thermal decomposition of PE-VOL and PD,L-LGA starts at 350 and 270 °C, respectively, indicating that the first copolymer is much more stable than the second. Similar values were also reported by Alvarez et al. [73] for PE-VOL and Park et al. [74] for PD,L- LGA. According to Alvarez et al., the decomposition of PE-VOL overlaps those of both poly(vinylalcohol) and poly(ethylene) under the same conditions. These authors reported that the thermal degradation of this copolymer at temperature ranged between 350 °C and 412 °C is essentially due to the decomposition of the alcoholic sequences. According to Holland et al. [75], the resulting products from the thermal decomposition of PVA, in this temperature range, lead to water elimination and chain scission through a six-membered transition state, leading principally to the formation of volatile product, such as aldehydes and ketones. When the temperature increased to higher than 412 °C, the decomposition of co-component PE occurs, leading to a release of ethylene and other volatile hydrocarbon compounds. According to Sivalingam et al. [76], the decomposition of PD,L-LGA involves a random chain scission at the beginning of the degradation process and then a specific chain scission at the end. At a lower temperature, the decomposition of PD,L-LGA follows the main degradation mechanism which is inspired from the mechanism of PLG and PLA involving transposition reactions of non-radical esters of the backbiting type incorporating the hydroxyl group at the end of the chain. This process leads mainly to the formation of linear and cyclic oligomers and to the regeneration of monomers and other products such as acetaldehyde and methylglycolate. Carbon dioxide is also a decomposition product formed by the decarboxylation reactions of the terminal carboxyl groups of the polymer chains [77] At higher temperatures, ketene (for PGA), methylketene (for PLA), formaldehyde, and carbon monoxide are also formed via the radical chain scission mechanism [78] Hence, the decomposition of PD,L-LGA forms products similar to neat PLA and PGA homopolymers. Indeed, the decomposition of PD,L-LGA leads to the formation of products similar to the compounds resulting from the process of decomposition of the corresponding homopolymers.
The TGA thermograms of PE-VOL/PD,L-LGA blends revealed the start of the first decomposition zone at 260 °C for the blend containing 10 wt % which then increased with the PE-VOL content in the blend to reach 290 °C when the blend was PE-VOL/PD,L-LGA90. This temperature is largely superior to that of pure PD,L-LGA (225 °C). As a result of these data, only 10 wt % of PE-VOL in the blend led to an increase in the thermal stability of PD,L-LGA by 35 °C. In this step, the resulting products were principally attributed to the decomposition of PD,L-LGA component. The compounds yielded from this process are principally cyclic and linear oligomers, monomers, acetaldehyde, ethylglycolate, and carbon dioxide. The second decomposition zone starts at 335 °C for the PE-VOL/PD,L-LGA10 and increased as the PE-VOL content in the blend increased to reach 365 °C for the blend containing 90 wt % of PE-VOL. The principal compounds released during this step are practically the same as those released during decomposition of pure PD,L-LGA. The third zone which starts at 375–420 °C depending on the PD,L-LGA content in the copolymer coincides with the beginning of the second decomposition zone of the PE-VOL and ends at the same end temperature (~500 °C). During this step, 7–36 wt % of residue was observed depending on the PD,L-LGA content in the blend. This residue is probably composed of carbon dioxide, ethylene, and other hydrocarbons (saturated and unsaturated).

3.4. DART-ToF-MS Analysis

The principal fragments resulting from the isothermal decomposition of PE-VOL, PD,L-LGA and PE-VOL/PD,L-LGA50 blend carried out by DART-ToF-MS analysis at 350 °C, selected from the previous TGA analysis as temperature where pure components and blends decompose, are illustrated in Figure 13. The predominant fragments regenerated from the decomposition of the neat PD,L-LGA were the isomers of C6H12O2, glycolic acid monomer(C2H4O), lactide dimer (C6H8O4) and the isomers of C11H16O9 formed from fragmentation of polymeric chains followed by a rearrangement and transposition through a complex radical mechanism. On the other hand, the decomposition of neat PE-co-VOH led to the production of a significant amount of C12H15O2 containing several conjugated double bonds resulting from the water elimination of this copolymer. In contrast, the spectrum of the decomposition involving the two copolymers in the blend is completely different. Indeed, the comparison of the spectrum visualizing the resulting fragments of the decomposition of the blend with those of the neat components reveals no signals common attributed to those observed in the spectra of the two pure components. This result is probably due to inter-transposition of radical groups from one chain to another neighboring chain of different natures. Such phenomenon is generally favored in certain conditions such as the miscibility of the blend, decomposition temperature, and interaction forces between the different polymer chains such as hydrogen bonding (carbonyl-hydroxyl groups). This action can only be possible when the two different copolymers are distributed in the matrix of one in the other +on their molecular scale. This finding may provide additional evidence confirming the miscibility of this blend. Indeed, the DART-ToF-MS spectrum of the PD,L-LGA/PE-VOL50 blend shows a series of chain fragments in which the principal components are aliphatic and aromatic isomers of C10H16O2, C8H19O5, C7H16O7, C14H24O4, C16H18O5, C10H16O2, and C12H27O7. Small molecules resulted from elimination reactions such as water and CO2 were also produced, which do not appear on this spectrum. However, neither the monomer nor dimer and oligomers are among the decomposition products of the blend.

4. Conclusions

The PE-VOL/PD,L-LGA blend was proved miscible in all composition investigated by viscosimetry method through the positive values of the viscosity parameter, α, determined by the San et al. equation. This finding was confirmed by the DSC method through the presence of negative values of intermolecular interaction parameter, χ 1 , 2 , determined from the Nishi equation and the reduction of different thermodynamic and crystallographic parameters with the PD,L-LGA content. The non-isothermal crystallization kinetics carried out on the PD,L-LGA/PE-VOL blend system and its semi-crystalline component, PE-VOL, revealed that the Ozawa approach described the primary crystallization process of this pure copolymer alone and when blended with this amorphous PD,L-LGA copolymer. The m values resulted for the blend systems were comparable to those of the neat copolymer, thus suggesting that the incorporation of PD,L-LGA in the PE-VOL matrix did not significantly influence the crystal growth. The Ec of the pure PE-VOL and blends determined by Kissinger relationship revealed activation energies superior to that of neat PE-VOL. This result indicates that the polymeric chains of the PD,L-LGA amorphous component act as heterogeneous nuclei and accelerate the dynamic of the non-isothermal crystallization process. In contrast, at lower PD,L-LGA contents, the chains of this copolymer clusters act as a barrier to retard the dynamic of the non-crystallization process through a depression of the crystal growth. The X-RD analysis revealed that the PE-VOL was homogeny distributed in its aggregate form into the PE-VOL/PD,L-LGA blend, thus preserving its crystal system. The TGA thermograms of the PE-VOL/PD,L-LGA blends and those of their pure components revealed a significant improvement in the thermal stability of the PD,L-LGA in which only 10% by weight of PE-VOL was sufficient to improve its thermal stability by 35 °C. The isothermal decomposition of neat copolymers and their blends carried out by the DART-ToF-MS method revealed that the fragmentation of PE-VOL at 350 °C are principally isomers of C7H12O2, C12H15O4, C16H26O, C16H22O4, and C18H30O6, whereas for the PD,L-LGA at this same temperature, the decomposition process leads to the regeneration of the starting monomer, dimer, and oligomers and large amounts of isomers of C9H14O5 and C11H16O9. The isothermal decomposition of copolymers and their blends by the DART-ToF-MS method reveal that the products resulted from the fragmentation of PE-VOL at 350 °C are principally the isomers of C7H12O2, C12H15O4, C16H26O, C16H22O4 and C11H16O9, while for the PD,L-LGA at 350 °C the decomposition process leads to the regeneration of the starting monomer, dimer, oligomers and huge amounts of isomers of C9H14O5 and C11H16O9. In contrast, the process of decomposition of the blend engenders the formation of new products different from those of the two copolymers, caused by inter-transposition of radical groups from one chain to another neighboring chain of different nature. Indeed, this action can only be possible when the two different copolymers are distributed in the matrix of one in the other on their molecular scale. This finding may be additional evidence that confirms the miscibility of this blend.

Author Contributions

Data curation, A.-B.A.-O.; Formal analysis, M.O., W.S.S., A.-B.A.-O., A.Y.B.H.A. and T.A.; Funding acquisition, A.A.A.; Investigation, A.-B.A.-O.; Methodology, M.O. and W.S.S.; Project administration, T.A.; Software, W.S.S. and A.A.-K.; Supervision, A.A.A. and T.A.; Validation, A.Y.B.H.A.; Visualization, A.A.A. and A.A.-K.; Writing—original draft, W.S.S. and T.A.; Writing—review & editing, T.A. All authors have read and agreed to the published version of the manuscript.

Funding

This research was funded by the Deanship of Scientific Research at King Saud University, through Research Group No. RGP-1438-040.

Conflicts of Interest

The authors declare no conflict of interest.

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Figure 1. XRD patterns of PE-VOL, PD,L-LGA and PE-VOL/PD,L-LGA blend with different PE-co-VAL contents: (A) neat PE-VOL; (B) neat PD,L-LGA; (C) PE-VOL/PD,L-LGA10; (D) PE-VOL/PD,L-LGA25; (E) PE-VOL/PD,L-LGA50; (F) PE-VOL/PD,L-LGA75; and (G) PE-VOL/PD,L-LGA90.
Figure 1. XRD patterns of PE-VOL, PD,L-LGA and PE-VOL/PD,L-LGA blend with different PE-co-VAL contents: (A) neat PE-VOL; (B) neat PD,L-LGA; (C) PE-VOL/PD,L-LGA10; (D) PE-VOL/PD,L-LGA25; (E) PE-VOL/PD,L-LGA50; (F) PE-VOL/PD,L-LGA75; and (G) PE-VOL/PD,L-LGA90.
Crystals 10 00425 g001
Figure 2. Heating DSC thermograms of copolymers and their blends with different PE-VOH contents: (A) neat PD,L-LGA; (B) neat PE-VOL; (C) PE-VOL/PD,L-LGA10; (D) PE-VOL/PD,L-LGA25; (E) PE-VOL/PD,L-LGA50; (F) PE-VOL/PD,L-LGA75; and (G) PE-VOL/PD,L-LGA90.
Figure 2. Heating DSC thermograms of copolymers and their blends with different PE-VOH contents: (A) neat PD,L-LGA; (B) neat PE-VOL; (C) PE-VOL/PD,L-LGA10; (D) PE-VOL/PD,L-LGA25; (E) PE-VOL/PD,L-LGA50; (F) PE-VOL/PD,L-LGA75; and (G) PE-VOL/PD,L-LGA90.
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Figure 3. Subsequent melting behaviors of PE-VOL and PE- VOL/PD,L-LGA50 blend isothermally crystallized at the indicated crystallization temperatures.
Figure 3. Subsequent melting behaviors of PE-VOL and PE- VOL/PD,L-LGA50 blend isothermally crystallized at the indicated crystallization temperatures.
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Figure 4. Hoffman–Weeks plots for pure PE-VOL and PE-VOL/PD,L-LGA blend with different PE-VOH contents.
Figure 4. Hoffman–Weeks plots for pure PE-VOL and PE-VOL/PD,L-LGA blend with different PE-VOH contents.
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Figure 5. Nishi–Wang curve indicating the variation of ΔTm versus the square of the PD,L-LGA volume fraction in PE-VOL/PD,L-LGA blends.
Figure 5. Nishi–Wang curve indicating the variation of ΔTm versus the square of the PD,L-LGA volume fraction in PE-VOL/PD,L-LGA blends.
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Figure 6. Cooling DSC thermograms of PE-VOL and PE-VOL/PD,L-LGA blends with different compositions and at different cooling rates.
Figure 6. Cooling DSC thermograms of PE-VOL and PE-VOL/PD,L-LGA blends with different compositions and at different cooling rates.
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Figure 7. Variation of the crystallization temperature of the PE-VOL in the blend versus the PE-VOL content at different cooling rates.
Figure 7. Variation of the crystallization temperature of the PE-VOL in the blend versus the PE-VOL content at different cooling rates.
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Figure 8. Variation of the relative crystallinity of pure PE-VOL and PE-VOL/ PD,L-LGA50 blend with temperature (A) and time (B) for various cold crystallization temperatures.
Figure 8. Variation of the relative crystallinity of pure PE-VOL and PE-VOL/ PD,L-LGA50 blend with temperature (A) and time (B) for various cold crystallization temperatures.
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Figure 9. Variation of the half time versus the PD,L-LGA content incorporated in the PE-VOL matrix.
Figure 9. Variation of the half time versus the PD,L-LGA content incorporated in the PE-VOL matrix.
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Figure 10. Ozawa plots of Ln[−Ln(1 − XT)] versus –Ln(β) for pure PE-VOL and PE-VOL/PD,L-LGA50.
Figure 10. Ozawa plots of Ln[−Ln(1 − XT)] versus –Ln(β) for pure PE-VOL and PE-VOL/PD,L-LGA50.
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Figure 11. Variation of the RTLn(β·Tp2) versus the reverse of crystallization temperature for pure PE-VOL and PE-VOL/PD,L-LGA blend with different compositions. Variation of the crystallization activation energy of PE-VOL/PD,L-LGA blend versus the PD,L-LGA content (in the top).
Figure 11. Variation of the RTLn(β·Tp2) versus the reverse of crystallization temperature for pure PE-VOL and PE-VOL/PD,L-LGA blend with different compositions. Variation of the crystallization activation energy of PE-VOL/PD,L-LGA blend versus the PD,L-LGA content (in the top).
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Figure 12. Thermograms TGA of pure PE-VOL, PD,L-LGA and their blends with different compositions.
Figure 12. Thermograms TGA of pure PE-VOL, PD,L-LGA and their blends with different compositions.
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Figure 13. DART-Tof-MS spectra of the isothermal decomposition of PE-VOL, PD,L-LGA and PE-VOL/PD,L-LGA50 blend indicating the relative ion intensity signals of the resulting products versus their molecular weights.
Figure 13. DART-Tof-MS spectra of the isothermal decomposition of PE-VOL, PD,L-LGA and PE-VOL/PD,L-LGA50 blend indicating the relative ion intensity signals of the resulting products versus their molecular weights.
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Table 1. Preparation conditions of PE-VOH/PD,L-LGA blends.
Table 1. Preparation conditions of PE-VOH/PD,L-LGA blends.
SystemPE–VOLPD,L–LGADMFBlend Appearance
(g)(wt%)(g)(wt%)(mL)
PE-VOL/PD,L-LGA100.50104.509020Single phase
PE-VOL/PD,L-LGA251.25253.757520Single phase
PE-VOL/PD,L-LGA502.50502.505020Single phase
PE-VOL/PD,L-LGA753.75751.252520Single phase
PE-VOL/PD,L-LGA904.50900.501020Single phase
Table 2. Intrinsic viscosity ([η]), Huggins-constant (k) and interaction parameter (α) of PE-VOL, PD,L-LGA and their blends with different compositions.
Table 2. Intrinsic viscosity ([η]), Huggins-constant (k) and interaction parameter (α) of PE-VOL, PD,L-LGA and their blends with different compositions.
System[η] (dL/g)kα
PE-co-VAL0.621.626-
PE-VOL/PD,L-LGA100.588.873.12
PE-VOL/PD,L-LGA250.526.673.42
PE-VOL/PD,L-LGA500.406.044.80
PE-VOL/PD,L-LGA750.385.444.50
PE-VOL/PD,L-LGA900.323.923.20
PD,L-LGA0.270.548-
Table 3. Comparative data of the glass transition temperatures of copolymers and the apparent melting temperatures of PE-VOL and PD,L-LGA blends with different compositions.
Table 3. Comparative data of the glass transition temperatures of copolymers and the apparent melting temperatures of PE-VOL and PD,L-LGA blends with different compositions.
System PE-VOL/PD,L-LGAVolume Fraction, φ1Tg (°C)Tm (°C)
0/1001.0037-
10/900.9038156
25/750.7539159
50/500.5040165
75/250.2541170
90/100.1051177
100/00.056188
Table 4. Hoffman–Weeks data obtained for PE-VOL/PD,L-LGA blend with different PE-VOH contents.
Table 4. Hoffman–Weeks data obtained for PE-VOL/PD,L-LGA blend with different PE-VOH contents.
PE-VOL/PD,L-LGATc (°C) T m o   ( ° C ) η
100:0154184.90.09
90:10149181.80.12
75:25143175.50.18
50:50142171.50.22
25:75137168.10.26
10:90135166.80.34
Table 5. Apparent crystallization degree and crystallization enthalpy of pure PE-VOL and PE-VOL in the blend with different compositions and cooling rates.
Table 5. Apparent crystallization degree and crystallization enthalpy of pure PE-VOL and PE-VOL in the blend with different compositions and cooling rates.
Systemβ (°C min−1)ΔHc(J g−1)X (%)
PE-VOL10.046.9829.77
12.547.1130.00
15.056.0035.48
17.554.0034.22
20.057.0036.12
PE-VOL/PD,L-LGA9010.035.2224.78
12.540.1728.78
15.046.0332.41
17.548.8634.44
20.052.4736.95
PE-VOL/PD,L-LGA7510.027.0022.81
12.530.3225.62
15.032.0427.07
17.536.5730.90
20.041.2134.82
PE-VOL/PD,L-LGA5010.013.3616.93
12.517.4622.13
15.021.224.12
17.525.8132.71
20.028.1935.73
PE-VOL/PD,L-LGA2510.0--
12.5--
15.02.185.52
17.54.3210.95
20.06.1215.51
Table 6. Ozawa parameter (m) and cooling function (kT) for pure PE-VOL and PE-VOL in the blend with different compositions.
Table 6. Ozawa parameter (m) and cooling function (kT) for pure PE-VOL and PE-VOL in the blend with different compositions.
SystemPE-VOL/PD,L-LGA Composition (wt %)T (°C)mkT
PE-VOL100/01451.3085.62
1501.60112.17
152.51.94172.43
1552.401299.80
PE-VOL/PD,L-LGA9090:10:001302.70340.36
1352.40107.77
1402.2430.88
1452.8033.11
PE-VOL/PD,L-LGA7575:25:001301.70235.10
1351.90190.57
1402.00167.33
1452.32138.38
PE-VOL/PD,L-LGA5050:50:001302.00115.58
1352.1076.69
1402.0046.99
1452.0018.73
PE-VOL/PD,L-LGA2525:751301.4051.94
1351.6460.34
1402.0086.49
1452.60170.72

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Ouladsmane, M.; Saeed, W.S.; Al-Odayni, A.-B.; Ahmed, A.Y.B.H.; Alghamdi, A.A.; Al-Kahtani, A.; Aouak, T. Non Isothermal Crystallization Kinetics and Isothermal Decomposition of Poly(Ethylene-Co-Vinylalcohol/Poly(D,L-Lactic-Co-Glycolic Acid) Blend. Crystals 2020, 10, 425. https://doi.org/10.3390/cryst10060425

AMA Style

Ouladsmane M, Saeed WS, Al-Odayni A-B, Ahmed AYBH, Alghamdi AA, Al-Kahtani A, Aouak T. Non Isothermal Crystallization Kinetics and Isothermal Decomposition of Poly(Ethylene-Co-Vinylalcohol/Poly(D,L-Lactic-Co-Glycolic Acid) Blend. Crystals. 2020; 10(6):425. https://doi.org/10.3390/cryst10060425

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Ouladsmane, Mohamed, Waseem Sharaf Saeed, Abdel-Basit Al-Odayni, Ahmed Yacine Badjah Hadj Ahmed, Abdulaziz Ali Alghamdi, Abdullah Al-Kahtani, and Taieb Aouak. 2020. "Non Isothermal Crystallization Kinetics and Isothermal Decomposition of Poly(Ethylene-Co-Vinylalcohol/Poly(D,L-Lactic-Co-Glycolic Acid) Blend" Crystals 10, no. 6: 425. https://doi.org/10.3390/cryst10060425

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