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International Polymer Processing

International Polymer Processing

Volume 28 Issue 4

  • Contents
  • Journal Overview

Contents

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Contents

September 9, 2013 Page range: 353-353
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Regular Contributed Articles

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Effect of Nanoclay Surface Modifier Chemical Reactivity on Morphology and Rheological Properties of PP/PA6 Blend Nanocomposite

G. R. Pircheraghi, H. Nazockdast, M. M. Salehi September 9, 2013 Page range: 354-360
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Abstract

An attempt was made to explore the role of nanoclay surface modifier chemical reactivity on the morphology and the rheological properties of a polypropylene/polyamide6 (PP/PA6 75/25) nanocomposite blend. The Na-MMT surface was modified with two types of cations; a) diamine cation (D-Clay), and b) a combination of diamine and quaternary alkylammonium cations (A-Clay) via cation exchange reaction. The nanocomposites samples compatibilized with PP-g-MA were prepared by melt compounding in an internal mixer. The XRD patterns indicated the intercalated/exfoliated microstructure for both nanocomposite samples. The SEM results showed a significant decreases in the PA6 droplet size, from 3.2 μm of the simple blend to the 0.4 μm in the D-Clay containing sample. Moreover, in the sample containing A-Clay the average droplet size was found to be 1 μm. The D-Clay containing sample showed the rheological properties similar to a simple blend in high frequencies with a nonterminal behavior in low frequencies storage modulus. This was explained by locating of D-Clay layers in the interphase and hence, significantly reducing the effective interfacial tension, α/R. In contrast, the sample containing A-Clay showed an increased complex viscosity and storage modulus within a range of frequencies, which was attributed to presence of a large amount of A-Clay layers in the PP matrix. These types of nanoclay partitioning were explained by the possibility of chemical reaction between amine group of nanoclay surface modifier and maleic group of PP-g-MA compatibilizer or in-situ formed block copolymer. Consequently, the D-Clay layers bounded with PP-g-MA is preferentially located in the interphase, while, the non reactive nanoclay layers (containing alkylammonium cations) is dispersed in the PP matrix by assistance of PP-g-MA. These findings were also evidenced by TEM micrograph of both nanocomposite samples.
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Thermal Mold Design in Consideration of the Temperature Control Fluid Flow

C. Hopmann, P. Nikoleizig September 9, 2013 Page range: 361-367
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Abstract

The striving for injection molded parts with an increasing functional density leads to more complex molds, which are more and more designed with injection molding simulation. Nowadays, software allows the operator to analyse not only the filling stage, but also the thermal activity within both, the mold and the part during the whole process cycle. However, commercial simulation software for injection molding does not offer the visualisation of the flow of the temperature control medium to get a reliable determination of the pressure drop and the local heat transfer coefficients (HTC). For this reason the potential of an exact implementation of the local HTC towards the temperature control medium, for improving the prediction precision of the thermal design, has been analysed at the Institute of Plastics Processing (IKV), Aachen. In order to use prior calculated HTCs from Computational Fluids Dynamics (CFD) simulations inside injection molding simulations, the development of an analogous model was required. An isolation layer between cooling channel and mold was therefore introduced, which allows to set a local heat transfer by varying the geometric dimensions of the layer. Several cooling channel layouts, which differ in geometric aspects (e.g. bends, diameter or fragmentation/consolidation of parallel channels) were studied with this set-up.
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Experimental Assessment of Dispersion Failure of Glass Fiber Reinforced Plastics in a Twin Screw Extruder

K. Hirata, H. Ishida, M. Hiragohri, Y. Nakayama, T. Kajiwara September 9, 2013 Page range: 368-375
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Abstract

To investigate the conditions necessary for glass fiber bundle dispersion in the polymer compounding process, we developed a method for experimentally quantifying dispersion failure in this study. We employed a co-rotating twin-screw extruder in our experiment and investigated the dependence of frequency of occurrence of dispersion failure on screw configurations (a forward kneading disk (FKD) and a backward mixing screw (BMS) with different screw configurations), throughput (Q), and screw speed (Ns). From our experiments, we found that increasing the production rate promotes the occurrence of dispersion failure when a FKD is used. Dispersion failure is markedly suppressed when a BMS is used. We thus found that the production rate could be increased by using a BMS with a large length-to-diameter (L/D) ratio.
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Life-stage Analysis of Solvent Induced Fissures under Static Stress in PET Fibers

M. Ramisetty, A. Rodriguez, A. Aneja, Y. Wang September 9, 2013 Page range: 376-385
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Abstract

The paper discusses the impact of drawing poly(ethylene terephthalate) (PET) fibers in the presence of solvents, which consist of the first five homologues of aliphatic primary alcohols, namely methanol to amyl alcohol. The solvent induced deformation under tensile load leads to surface fissures characterized by four stages: fissure formation (birth), incipient draw (neck formation), partial draw, and full draw. This process results in internal void formation in the presence of a propagating neck. A design of experiment (DOE) was performed to screen out the process parameters critical for understanding surface fissure formation. Four process parameters were investigated: initial material properties (orientation); environment of draw (i.e. type of alcohols used as solvent); rate of extension; and amount of extension. The response of solvent induced deformation were characterized by the natural draw force reduction; number of fissures formed at time of birth, fissure width at time of formation, and neck angle. Of all the four process parameters involved, the analysis indicates that the material properties and amount of extension were the best predictors of solvent induced fissure formation. Organic solvents reduce the tension required for draw and create internal voids, a porous network, with possibly the penetrant being “sucked” into the interior of PET fibers drawn in the presence of alcohols.
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The Effect of TMPTMA Addition on Electron-beam Irradiated LDPE, EVA and Blend Properties

M. Sabet, R. M. Savory, A. Hassan, C. T. Ratnam September 9, 2013 Page range: 386-392
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Abstract

In this work low density polyethylene (LDPE) and ethylene vinyl acetate (EVA) were blended in the presence of trimethylol propane trimethylacrylate (TMPTMA) (0 to 6 phr). The resultant blends were irradiated with a 3 MeV electron-beam resulting in dosages of 0 to 240 kGy using a rhodotron accelerator system. The effect of radiation exposure on the LDPE/EVA/TMPTMA blend properties were investigated with respect to gel content, tensile strength and elongation up to breakage of the blends. The findings indicate that increasing EVA and TMPTMA content yield tighter network structures through enhanced blend crosslinking, which is a direct consequence of irradiation. For pure EVA significant tensile strength improvements are evident as irradiation increases up to 210 kGy. Irradiated blends exhibit improved tensile strength and elongation at breakage with respect to pure LDPE and EVA. Volume resistivity (VR) and dielectric constant (DC) of the blends were also studied as a function of EVA content, TMPTMA content and radiation dosage. Increasing EVA and TMPTMA content enhances DC and VR values, whereas, increasing irradiation dosage only effects VR values of the blends. The maximum VR value attained in this work corresponds to a radiation dosage of 170 kGy and a blend comprising of 30 wt% of EVA.
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Flammability and Thermal Characterization of Aluminum Hydroxide Filled with LDPE

M. Sabet, A. Hassan, C. T. Ratnam September 9, 2013 Page range: 393-397
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Abstract

Aluminum hydroxide (ATH), a non-toxic and environmentally friendly flame retardant, was characterized using thermogravimetric analysis (TGA) and differential thermal analysis (DTA). The effect of ATH content on flammability properties of LDPE was also determined using limiting oxygen index (LOI) and smoke density test. The thermal characterization studies showed that the effective temperature range for ATH as a flame retardant is 200 to 350°C. In water release test, it was determined that the release of the water by ATH degradation in ATH increased with increasing temperature. The LOI test showed that the flame retardancy of LDPE increased with increasing ATH content and decreasing ATH particle size. The smoke density test proved that addition of ATH reduced effectively the smoke density of a burning LDPE. It was studied in this paper the effect of ATH particle size on thermal, flammability and viscosity of ATH filled with LDPE.
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The Influence of Vulcanization Agents on Vulcanization Kinetics of Chloride Butyl Rubber

X. R. He, H. Yu, X. Wang, Y. Q. Rong, R. Zhang September 9, 2013 Page range: 398-414
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Abstract

BPR (brominated tert octyl phenolic resin) vulcanization system is one of the commonly used systems for CIIR (chloride butyl rubber). In the vulcanization process, there are two competitive reactions, the cross-linking reaction and the self-poly-condensation reaction of BPR. In this vulcanization system, the metal oxide, as vulcanization active agent, have a greater impact on the kinetics of these two competing reaction. The kinetics equation of overall reaction (including the two competitive reactions) and the BPR self-poly-condensation reaction with different amount of ZnO or MgO were obtained by non-isothermal DSC method. The results showed that ZnO would promote the overall reaction and the BPR self-poly-condensation reaction at lower dosage, the rate constant of overall reaction increased faster than BPR self-poly-condensation reaction rate constant with the increasing of the ZnO content, and when the ZnO content exceeded 7.5 phr, the rate constant of BPR self-poly-condensation reaction decreased; With the increasing of the MgO content, the rate constant of overall reaction and BPR self-poly-condensation reaction reduced, and the rate constant of self-poly-condensation reaction reduced much faster than the rate constant of the overall reaction when the content of MgO changed from 0.5 to 0.75. The cross-linking density was measured by the equilibrium swelling method. The results showed that with the increasing of ZnO content, the cross-linking density increased when it was less than 10 phr, and decreased when the ZnO content exceeded 10 phr. With the increasing of MgO content, the cross-linking density increased when it was less than 0.75 phr, and decreased when the MgO content exceeded 0.75 phr. The mechanical properties and the dynamic mechanical properties were investigated by the universal testing machine and the dynamic mechanical performance analysis (DMA), respectively. The results showed that the ZnO and MgO content had a great impact on the mechanical properties and the dynamic mechanical properties, and the variation trend of the cross-linking density was further confirmed by the corresponding variation of the properties.
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Adhesion Tendency of Polymers to Hard Coatings

M. Rebelo de Figueiredo, C. Bergmann, C. Ganser, C. Teichert, C. Kukla, C. Mitterer September 9, 2013 Page range: 415-420
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Abstract

The adhesion tendency of the polymers polyoxymethylene, polyamide 6.6 and polyether ether ketone against hard coatings to protect molds in polymer processing was evaluated by a combination of tribological tests, investigations of wear tracks and measurements of the coatings' surface energies. It was found that a low surface roughness and a low surface energy of the coating are beneficial to reduce friction and adhesion tendency. Among the coating materials investigated, CrN seems to be the most promising candidate for the protection of molds for polymer processing.
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Barrier Screw Compounding and Mechanical Properties of EAA Copolymer and Cellulose Fiber Composite

R. Ariño, A. Boldizar September 9, 2013 Page range: 421-428
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Abstract

The difficulty of feeding cellulose fibers and thermoplastics into the extruder or injection molding machine is addressed, this being a serious problem in the production of cellulose fiber composites for industrial applications. Agglomerates consisting in cellulose fibers and ethylene-acrylic acid copolymer (EAA) with different cellulose contents and different fiber lengths were processed with two different screws in order to better understand how the dispersion of the fibers can be improved by melt extrusion. A conventional screw with a compression ratio of 4:1 and a screw with barrier flights were used at different screw rotation speeds. The fiber length and fiber content were measured and microscopic analyses were performed in order to estimate the number and size of the cellulose fiber aggregates in the final composites. It was concluded that the barrier screw was more effective than the conventional screw in breaking up the fiber aggregates and dispersing the fibers. More but smaller cellulose aggregates were observed when the barrier screw was used, and the reduction of length was significantly greater for long than for short fibers. In contrast to that was expected, the samples containing the shorter fibers had better mechanical properties, probably due to a better dispersion of the fibers.
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Melt Processing of Wood Cellulose Tissue and Ethylene-Acrylic Acid Copolymer Composites

R. Ariño, A. Boldizar September 9, 2013 Page range: 429-436
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Abstract

The difficulty of feeding cellulose fibers together with the polymer into the melt processing equipment is a serious disadvantage for the production of cellulose-containing composites on a large scale. In the present work, a continuous method of feeding cellulose in the form of a tissue into a twin-screw extruder through an opening downstream of the extruder cylinder was studied. With this method, composites with different fiber contents were obtained. The tissues used were one made mainly of softwood fibers and another mainly of hardwood fibers. In order to better understand how to improve the fiber dispersion by melt mixing, a second extrusion was performed with a single screw extruder with a barrier-flighted screw and also with the twin-screw used to compound the tissue with the polymer. The compounds produced were then injection molded into test bars. The test bars containing the softwood tissue exhibited some fiber aggregates also after a second extrusion, whereas no fiber aggregates were observed in samples made with the tissue containing hardwood fibers and two passes through the twin screw. The fiber length was in general reduced by each melt processing stage and the shortest fiber length was observed after two extrusions with the twin-screw and injection molding. The tensile modulus increased with increasing fiber content. A higher stiffness was obtained with more softwood fibers in the tissue whereas more hardwood fibers gave a higher tensile strength and greater elongation at break.
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Experiments and Modelling of Calender Processing for Shear Thinning Thermoplastics between Counter Rotating Rolls with Differential Velocities

R. Magnier, J.-F. Agassant, P. Bastin September 9, 2013 Page range: 437-446
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Abstract

This paper is concerned with a floor application calendering processing using both a PVC and a Polyolefin formulation within a two roll calender. The rheology of both formulations was measured using the Rheoplast, a specific capillary rheometer. Experiments with various velocity differentials were performed and the roll separating force and the sheet exit temperature were measured for each case. An isothermal model based on the lubrication approximations hypothesis together with a power-law behavior for the molten polymer has been developed. Due to the difference between the rotation velocities of the two cylinders, the problem is no longer symmetric and the integration of the generalized Reynolds equation requires taking into account various velocity profiles. The resulting pressure profile enables computation of the roll separating force. The agreement between the model and experiments performed with the PVC formulation at various velocity differentials is fair; however for the Polyolefin formulation there is a significant difference which means that the model for this new formulation needs to be improved.

PPS News

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PPS News

September 9, 2013 Page range: 447-447
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Seikei Kakou Abstracts

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Seikei Kakou Abstracts

September 9, 2013 Page range: 448-448
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About this journal

International Polymer Processing offers original research contributions, invited review papers and recent technological developments in processing thermoplastics, thermosets, elastomers and fibers as well as polymer reaction engineering. For more than 25 years International Polymer Processing, the journal of the Polymer Processing Society, provides strictly peer-reviewed, high-quality articles and rapid communications from the leading experts around the world.
All articles are subject to thorough, independent peer review.
Editor: Polymer Processing Society
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