Abstract:Polyesters, such as poly (butylene terephthalate) (PBT), owe a rather low melt strength, which is considered as not beneficial for foaming. To overcome this issue, a typical attempt is the incorporation of chemical modifications—so‐called chain extenders (CE)—in the reactive extrusion process. In this study, the reaction kinetic variables are investigated depending on the material and process parameters. For this purpose, different series of experiments are performed with varying PBT with different molecular w… Show more
“…An Avrami-like eq (eq 1) was used to calculate the reaction rate constant. 34,35 n t n k ln ln( ) ln( ) ln( )…”
Section: Microcompoundermentioning
confidence: 99%
“…34−37 In this context, kinetic analyses are aiming to determine the reaction rate constant of the corresponding chain extension. 34,35 In reactive extrusion, the reaction rate, expressed by the rate constant "k", can be determined by the increasing viscosity, which is reflected in the increasing torque during processing. The temperature-dependent analysis of k is of particular interest in calculating the activation energy (EA), which is required to initiate the reaction.…”
Section: Introductionmentioning
confidence: 99%
“…FT-IR can be used to detect the transformation of a chain extender on the basis of changes in characteristic bands. 2,35 To detect the increase in molecular weight and changes in polydispersity, often occurring in chain extension reactions, size exclusion chromatography (SEC) may be a suitable method. 22,30,36,38 In addition to these chemical analysis methods, rheological investigations are particularly suitable for understanding reaction-induced changes in materials.…”
Section: Introductionmentioning
confidence: 99%
“…The temperature-dependent analysis of k is of particular interest in calculating the activation energy (EA), which is required to initiate the reaction . It is important to note that the reaction rate constant or activation energy always pertains to the entire process and not exclusively to the chemical reaction itself . Initial changes in the substance, which can already be observed during processing and allow conclusions to be drawn about the occurrence of a reaction, can also be verified with the aid of Fourier transform infrared spectroscopy (FT-IR).…”
Section: Introductionmentioning
confidence: 99%
“…Initial changes in the substance, which can already be observed during processing and allow conclusions to be drawn about the occurrence of a reaction, can also be verified with the aid of Fourier transform infrared spectroscopy (FT-IR). FT-IR can be used to detect the transformation of a chain extender on the basis of changes in characteristic bands. , To detect the increase in molecular weight and changes in polydispersity, often occurring in chain extension reactions, size exclusion chromatography (SEC) may be a suitable method. ,,, In addition to these chemical analysis methods, rheological investigations are particularly suitable for understanding reaction-induced changes in materials. Appropriate rheokinetic experiments can provide significant insights into chemical and structural transformations. , …”
With the simultaneous growth of plastic demand and the need for a circular economy, processes for recycling discarded and worn-out consumer goods are also becoming increasingly important. In this context, reactive processing of recycled poly(ethylene terephthalate) (rPET) with pyromellitic dianhydride (PMDA) offers a frequently studied modification approach to optimize the viscous and elastic material properties of degraded PET through mechanical recycling. However, the kinetics of the underlying chain extension reaction have not been investigated yet. In this study, the parametric parameters for reaction kinetics are investigated as a function of material and process parameters. For this purpose, three series of experiments were carried out with rPET and PMDA on a microcompounder. The screw force was recorded, and the data was analyzed using an Avrami and Arrhenius approach. In order to follow the rheological and chemical changes during reactive extrusion, the samples were examined using SEC, FT-IR, and small amplitude oscillatory shear (SAOS) rheological analysis. An activation energy of 70 kJ/mol was determined for the process studied. Furthermore, a linear increase in polydispersity was observed over the processing time. An analogous behavior could be determined by FT-IR spectroscopy.
“…An Avrami-like eq (eq 1) was used to calculate the reaction rate constant. 34,35 n t n k ln ln( ) ln( ) ln( )…”
Section: Microcompoundermentioning
confidence: 99%
“…34−37 In this context, kinetic analyses are aiming to determine the reaction rate constant of the corresponding chain extension. 34,35 In reactive extrusion, the reaction rate, expressed by the rate constant "k", can be determined by the increasing viscosity, which is reflected in the increasing torque during processing. The temperature-dependent analysis of k is of particular interest in calculating the activation energy (EA), which is required to initiate the reaction.…”
Section: Introductionmentioning
confidence: 99%
“…FT-IR can be used to detect the transformation of a chain extender on the basis of changes in characteristic bands. 2,35 To detect the increase in molecular weight and changes in polydispersity, often occurring in chain extension reactions, size exclusion chromatography (SEC) may be a suitable method. 22,30,36,38 In addition to these chemical analysis methods, rheological investigations are particularly suitable for understanding reaction-induced changes in materials.…”
Section: Introductionmentioning
confidence: 99%
“…The temperature-dependent analysis of k is of particular interest in calculating the activation energy (EA), which is required to initiate the reaction . It is important to note that the reaction rate constant or activation energy always pertains to the entire process and not exclusively to the chemical reaction itself . Initial changes in the substance, which can already be observed during processing and allow conclusions to be drawn about the occurrence of a reaction, can also be verified with the aid of Fourier transform infrared spectroscopy (FT-IR).…”
Section: Introductionmentioning
confidence: 99%
“…Initial changes in the substance, which can already be observed during processing and allow conclusions to be drawn about the occurrence of a reaction, can also be verified with the aid of Fourier transform infrared spectroscopy (FT-IR). FT-IR can be used to detect the transformation of a chain extender on the basis of changes in characteristic bands. , To detect the increase in molecular weight and changes in polydispersity, often occurring in chain extension reactions, size exclusion chromatography (SEC) may be a suitable method. ,,, In addition to these chemical analysis methods, rheological investigations are particularly suitable for understanding reaction-induced changes in materials. Appropriate rheokinetic experiments can provide significant insights into chemical and structural transformations. , …”
With the simultaneous growth of plastic demand and the need for a circular economy, processes for recycling discarded and worn-out consumer goods are also becoming increasingly important. In this context, reactive processing of recycled poly(ethylene terephthalate) (rPET) with pyromellitic dianhydride (PMDA) offers a frequently studied modification approach to optimize the viscous and elastic material properties of degraded PET through mechanical recycling. However, the kinetics of the underlying chain extension reaction have not been investigated yet. In this study, the parametric parameters for reaction kinetics are investigated as a function of material and process parameters. For this purpose, three series of experiments were carried out with rPET and PMDA on a microcompounder. The screw force was recorded, and the data was analyzed using an Avrami and Arrhenius approach. In order to follow the rheological and chemical changes during reactive extrusion, the samples were examined using SEC, FT-IR, and small amplitude oscillatory shear (SAOS) rheological analysis. An activation energy of 70 kJ/mol was determined for the process studied. Furthermore, a linear increase in polydispersity was observed over the processing time. An analogous behavior could be determined by FT-IR spectroscopy.
A fundamental understanding of crystallization behavior is essential for the processing of both virgin and recycled polymers. This research delves into the crystallization characteristics and non‐isothermal crystallization kinetics of recycled polyethylene terephthalate (rPET) and its blends with poly butylene terephthalate (PBT), which have been modified using epoxy‐based multifunctional chain extenders (CE). The preparation of rPET/PBT blends involved a twin‐screw extruder, with varying weight ratios and different CE concentrations. Differential scanning calorimetry was employed to perform crystallization analysis on the samples. The results underscore the profound impact of blend composition on the thermal characteristics of the system, with CE exerting only a marginal influence. The glass transition temperatures (Tg) of the two polymers were measured at 49 and 79°C. During blending, the Tg values demonstrated variations relative to the proportions but did not adhere to the Fox equation. Furthermore, PBT was found to enhance the crystallization tendencies of rPET, resulting in an increase in relative crystallinity from 11% to 36%. Notably, the crystallization rate of PBT at 0.40 min−1 exceeded that of rPET at 0.36 min−1. PBT minimally affected the crystallization rate constant of rPET‐dominant blends, while rPET significantly reduced the crystallization rate in PBT‐dominant blends.
This study investigates the melt rheological properties and foamability of recycled polyethylene terephthalate (rPET) and its blends with polybutylene terephthalate (PBT) modified through an epoxy-based Joncryl ADR 4468 chain extender. A twinscrew extruder was used to prepare rPET/PBT blends at various weight ratios (i.e., 100/0, 75/25, 50/50, 25/75, and 0/100) and with varying Joncryl chain extender contents (i.e., 0.25, 0.5, 0.75, and 1.0 wt %). The small-amplitude oscillatory shear rheological experiments were conducted to analyze the melt viscoelastic behavior of the samples. The melt strength and strain-hardening behavior of the compounds were examined by measuring the extensional rheology and Rheotens tests. Crystallization analysis was conducted on the processed samples by using differential scanning calorimetry. The bead foaming behavior of the samples was investigated using a batch-based foaming reactor with supercritical CO 2 . Both compounding with PBT and Joncryl chain modification increased the complex viscosity, melt strength, and strain-hardening behavior of the blends, while their synergistic effect revealed a more noticeable enhancement. Although direct modification of rPET with Joncryl and its direct compounding with PBT could not generate a meaningful foam structure, a homogeneous microcellular foam structure could successfully be induced when 25 wt % rPET was incorporated in blends with PBT modified with 1.0 wt % Joncryl.
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