The SPE Library contains thousands of papers, presentations, journal briefs and recorded webinars from the best minds in the Plastics Industry. Spanning almost two decades, this collection of published research and development work in polymer science and plastics technology is a wealth of knowledge and information for anyone involved in plastics.
Blend of poly(?-caprolactone) (PCL) and poly(styrene-co-acrylonitrile) (SAN) containing 27.5 wt% of acrylonitrile was studied. The PCL/SAN blend having LCST (lower critical solution temperature) phase boundary above the melting point Tm of PCL offered an excellent opportunity to investigate the competition of liquid-solid phase transition (crystallization) and liquid-liquid phase transition (phase dissolution). A blend with critical composition (80/20 PCL/SAN) underwent a temperature-jump above LCST to proceed spinodal decomposition, yielding a regularly phase-separated structure (SD structure). Then, it was quenched to the temperatures below Tm, at which both the crystallization and the phase dissolution could occur. By transmission electron microscopy it was found that during isothermal annealing after quenching to high temperatures close to Tm (e.g., 51°C), the SD structure gradually disappeared, and then the crystallization started from a single-phase mixture to yield normal crystalline structure similar to that from neat crystalline polymer. At lower temperatures (e.g., 40°C), crystallization quickly occurred and the SD structure was preserved, implying that the crystallization prevailed over the dissolution yielding a bicontinuos structure consisting of amorphous (SAN-rich) and crystalline (PCL-rich) regions. At intermediate temperatures (e.g., 45°C), the phase dissolution competed with the crystallization, resulting in a bicontinuos structure with longer periodic distance and broad boundary having a gradient in composition of amorphous region between PCL crystal lamellae. Light scattering analysis quantitatively revealed a competition of the crystallization and the phase dissolution in terms of the crystallization rate (from Hv scattering) and the apparent diffusion coefficient for dissolution (from Vv scattering).
The objective of this work is to evaluate the suitability of metallocene-catalyzed polyethylenes for rotational molding. The metallocene resins were LLDPE (copolymer of ethylene with hexene) and ethylene-based butene plastomers. The study compares resin properties of metallocene and Ziegler-Natta polyethylenes. Through parallel-plate rheometry, zero-shear viscosity, G' and G were determined. Melting point heat of fusion and degree of crystallinity were obtained by DSC experiments and rate of coalescence of the polymer particles by sintering experiments. Molding tests ran in uniaxial rotomolding machine produced parts for impact resistance and tensile strength measurements."
The thermal oxidative stability of a variety of ABS commercial formulations has been studied in a broad temperature interval by means of the chemiluminescence technique. The influence of antioxidants on stability varies widely and depends on how they affect both the oxidation induction period and the oxidation rate constant. Introduction of UV stabilizers diminishes the effectiveness of antioxidants primarily because of the decrease in the induction period values. In most cases durability of colored compositions is defined by the oxidation rate constants and addition of colorants lowers the thermal oxidative stability in both blends with and without antioxidants and UV stabilizers. At the same time, the level of stability reduction varies drastically in formulations containing different UV stabilizers. The activation energy of oxidation was evaluated in 120-180°C temperature interval. Larger activation energy was obtained for samples with superior durability while less stable samples exhibited somewhat lower activation energy. Nonetheless the summation of the data shows that the absolute activation energy values cannot be used for evaluation of materials' quality.
Injection molded parts from today's commercially available thermoplastic elastomers (TPEs) including thermoplastic vulcanizates (TPVs) can show surface defects such as halos, gloss variations, gate blemishes, flow lines, etc. Novel TPEs that overcome the above mentioned defects were developed for injection molded applications. These new materials, produced by dynamic vulcanization, showed significant improvements in reducing surface defects in molded parts and also showed greatly reduced fogging (i.e., low volatile release) as compared to existing commercial TPEs. The fogging, measured at 100°C for 16 hrs, for these new TPEs were remarkably low (0.7 - 1.3 mg) compared to standard commercial SEBS-based TPEs which were measured at 2.0 - 2.3 mg. Rheology studies indicated that these materials have a unique flow behavior which may be responsible for the improved surface appearance. The new TPEs are known as Santoprene® thermoplastic rubber M300. These are suitable for injection molding of automotive interior parts such as coin trays, mats, cup holders, etc., where aesthetics of the parts are important.
Formulation of droplet deformation and breakup in an extensional flow for viscoelastic fluid systems were carried out, and parametric study was performed. The interfacial tension, and both droplet viscosity and elasticity reduce the droplet deformation, while the matrix viscosity and droplet size increase the droplet deformation. The matrix elasticity affects the droplet deformation in a more complex manner. The viscoelastic properties of the matrix are more influential on the droplet deformation than that of the drop phase. For viscoelastic systems, the capillary number, viscosity ratio, and the elasticity of both phases all have effects on the broken drop size and the critical deformation, and the relations between all these parameters are very complicated. The formulation then was used to numerically simulate the deformation and breakup of a liquid crystal polymer droplet suspended in polypropylene matrix during a film casting process. Although the result was not quantitatively accurate, the trend in terms of the particle size and aspect ratio was correctly predicted.
Polypropylene (PP) of various molecular weights were mixed with a thermotropic liquid crystal polymer (LCP) and strands were prepared by extrusion and stretching. The strands were subsequently pelletized and then injection molded at temperature below the melting point of LCP. The mechanical properties and the morphology of the strands and injection-molded specimens were investigated as a function of draw ratio, LCP concentration, and PP molecular weight. The results for strands show that an increase in the draw ratio, LCP concentration and matrix molecular weight in general enhance the modulus and tensile strength. However, the tensile properties of injection-molded specimens are found to be reduced compared with those of the original strands, in particular at high LCP concentration. The morphology of LCP changes from spherical or ellipsoidal droplets to elongated fibrils in the strands as the draw ratio increases, but this aligned LCP fibrillar morphology was not transferred to the injection-molded specimens due to the disorientation of fibrils during injection molding. Compatibilization of PP/LCP blends was also studied by using various polymers. Maleic anhydride and acrylic acid modified PPs improved the tensile properties modestly, but maleic anhydride modified EPDM reduced the tensile properties.
The effect of shear modification and blending on the coating performance of a commercial LDPE resin was studied. Shear modification of the virgin resin as well as of its blends with another LDPE was performed in a single and in a twin screw extruder. The rheological properties of the modified materials were measured and no significant differences in their behavior under shear deformation were detected. On the other hand, changes in the entrance pressure drop and extensional viscosity were observed. These changes in extensional behavior were found to affect coating properties. Overall, neck-in improved through shear modification while it was not sensitive to blending with a higher molecular weight resin. On the other hand, blending had an effect on the draw-down speed and it may be used to achieve a balanced coating performance.
Executing a color change is a routine operation for plastic processors. With on-line coloring in extrusion, the polymeric melt continuously flows shaping the product and changing its color from one color (color A) to another color (color B). At the moment of initiating the color change, there is a period of time in which the product will yield acceptable color (in color A). After some amount of time elapses, the transition phase from color A to color B will yield off-color product until the color change for color B is fully established in the system. The amount of time it takes to make this change from color A to color B depends on a variety of factors including the extruder size and type, shaping die, resin that is extruded, coloring system, and the color to be changed, whether from light to dark or vice versa. In this report, an approach for minimizing both the color-change extrusion time and off-color rejected product is presented. An extrusion simulation is applied to determine temperature - residence time -shearing correlation and the correct let down ratio for a PVC compound/pigmentation system. A Brabender mixer was used as an instrument. The information obtained was then applied for studying color change kinetics in a production environment.
Vibration welding is a useful technique for joining thermoplastics. This vibration welding study examined the microstructure of joints made of 33% glass reinforced nylon 66. Joints were made under different vibration welding conditions. The microstructural analysis techniques were: optical microscopy of weld cross-sections under polarized light, scanning electron microscopy of both weld cross-sections and fracture surfaces, and thermal gravimetric analyses near the weld line. These tests provide information on the thickness of the heat-affected zone, glass fiber orientation and level respectively. The microstructural analyses reported in this study assist in the interpretation of experimental tensile weld strengths.
Flame retardant polyethylene compounds fabricated from rotational moulding technique are finding widespread applications for Industrial applications, stadium seats, children`s toys in parks etc. In the present work , the objective was to assess rotational moulding characteristics of flame retardant -LLDPE. The end application identified for the purpose was a hollow box for packaging of explosive materials. The material currently used is wood. With increasing pressure to conserve natural resources, the present work acquires significance and provides impetus in that direction. Compounds were designed to meet V0, V1, and V2 Flammability rating as per UL 94 test protocol. FR-LLDPE compounds were prepared on Berstoff ZE-25 twin-screw extruder. Mechanical properties are determined on the injection moulded ASTM test specimens and cut specimens from rotational moulded boxes. The flammability test on rotational moulded hollow containers has been captured in a compact disk.
N-isopropylacrylamide (NIPA) was copolymerized with different concentrations of N, N'-methylenebisacrylamide (MBA) to obtain networks of different crosslinking densities. Semiinterpenetrating networks of the same crosslinking densities were obtained by copolymerization of NIPA and MBA in the presence of linear polyacrylamide (5 wt.%). The equilibrium swelling degree in water at 25°C varied from 7.61 to 16.8 times the original volume when the molar ratio NIPA/MBA increased from 10:1 to 100:1. The transition temperature determined by DSC was largely unaffected by the crosslinking conditions in this work. Crosslinking density obtained from dynamic shear measurements was much lower than predicted from the molar ratio of the monomer and crosslinker, which was explained by the incomplete reaction. The sol fraction varied from 12% to 30%. Thermomechanical analysis showed contraction followed by the expansion of the gels during transition. The broadening of the temperature range of the gel collapse was observed as the crosslinking density increased. Tensile strength of the 10% swollen semiinterpenetrating NIPA networks was higher (15-23 kPa) than that of the 10% swollen single NIPA networks (9-13 kPa). Elongations at break were significantly higher for semi IPN gels compared to the single ones, especially at lower crosslinking densities.
The apparent extensional properties of three injection molding grade, high density polyethylenes (PE) and their composites containing 20vol% hydroxyapatite (HA) were studied using orifice pressure drop data from a capillary rheometer followed by Cogswell's analysis. The effects of temperature, molecular weight and filler have been investigated. For unfilled PE extensional viscosity was found to decrease as the molecular weight decreased or the temperature increased. The addition of HA appears to increase the extensional viscosity at low strain rates and decreases due to extension thickening at high strain rates. HA addition tended to decrease the Trouton ratios of PE at moderate to high strain rates.
The objective of this work was to compare simulation and experimental results for a flat specimen injection mold. The study was made using standard and film" gates. The results were obtained through a simulation program for the injection process C-MOLD for theoretical data and for the experimental data results were obtained in an injection molding machine. In both cases the injection molding conditions were the same. Differences between the gates and also between experimental and theoretical results mainly in the injection pressure and pattern flow were found."
The tolerances on injection molded thermoplastic parts have grown tighter over the past several decades, and concomitantly the range of applications for thermoplastic injection molded parts have grown dramatically. Now, tolerances of one micron can be achieved, expanding the range of applications for injection molded thermoplastics even more. The tolerances on the injection molded thermoplastic parts are precipitated by the combination of the tolerances from the feedstock, the injection mold, the injection molding machine, the peripherals, the control system and the part measurement devices. So, in simple terms, each of these contributing tolerances must be minimized in order to minimize the tolerances on the injection molded part. In the specific applications herein described, which is a single part fabricated in a multi cavity mold the tolerances on the injection mold are found to be the primary contributing tolerances, the tolerances on the control system are found to be the secondary contributing tolerances, and the tolerances on the injection molding machine and the feedstock are less significant.
Weldlines, which are a common feature in many injection molded parts, are known to be inherently weak. The present experimental study focused on improving weldline strength through the addition of oscillatory vibrational energy during molding processes. Both filled and unfilled polymers were studied, and comparisons between the tensile strength of ASTM specimens made with and without vibration were made. It was found that minimal product strength increases were realized when optimized vibration-assisted molding conditions were applied. Details related to the critical vibration-assistance parameters studied and optimization processes utilized will be presented and discussed.
Polypropylene (PP) nano-composites are prepared by melt intercalation in this study. Nano-clay is mixed with PP by twin screw extrusion. Maleic anhydride modified polypropylene (PP-MA) is added to enhance the dispersion of the clay in PP. Nylon 6 is also added to this PP/PP-MA/clay composite to partially replace the content of PP-MA in order to decrease the material cost. The basal spacing of the clay in the composites is measured by X-ray Diffraction (XRD). The morphology of the composites is observed by SEM. The mechanical properties of the composites are also measured. It was found that the molecular weight and MA content strongly affect the nano-structure and the properties of PP nano-composites. PP-MA with a lower molecular weight (LMW) and a high MA content can lead to good clay dispersion in PP-MA. However, it causes a decrease in the mechanical properties of PP/PP-MA/clay composites. It was also found that the addition of nylon 6 further expands the basal spacing of the clay in PP composites. However, the mechanical strength decreases by adding nylon 6 to the nano-composites.
In this paper, design and fabrication of a CD platform, where different fluidic structures are micromachined into a plastic CD, are presented. Various ways to fabricate mold inserts (traditional CNC-machining of tool steel vs. photolithography/electroplating) and microfluidic platforms (micro-embossing, thin wall injection molding, and reactive molding) based on optically clear thermoplastic and thermoset polymers (e.g. optical quality polycarbonate, PMMA, PDMS) are introduced. The effects of mold inserts, molding methods, and feature size on replication accuracy and 'molded-in' stresses are also discussed.
The presence of low profile additives (LPAs) can reduce the shrinkage of unsaturated polyester (UP)/styrene (St) resins cured at low temperatures, but the final shrinkage is still quite high. In this study, secondary monomers (e.g. divinylbenzene (DVB) and trimethylopropane trimethacrylate (TMPTMA)) and co-promoter 2,4-Pentandione (2,4-P) were added into the UP/St/LPA system to investigate their effect on shrinkage control of resins cured at low temperatures. Dilatometery results showed that the addition of both TMPTMA and 2,4-P resulted in earlier volume expansion during curing and in turn; better shrinkage control. The phase separation, reaction kinetics and viscosity changes in the LPA-rich and UP-rich phase during curing were investigated. Results revealed that the increased reaction rate in the LPA-rich phase led to an earlier formation of microvoids and, consequently, less volume shrinkage of the cured resin.
Unsaturated polyester and vinylester resins are the two major thermoset resins used in low temperature composite manufacturing processes, such as the Seemann Composite Resin Infusion Molding Process (SCRIMP). Understanding the reaction kinetics and network formation can be critical to SCRIMP. A series of well-defined polyester resins are used to study the effect of resin chemistry on the reaction kinetics. The effects of styrene concentration and temperature on the cure kinetics of styrene/vinylester systems are also studied. The glass transition temperature of polyester/vinylester resins cured at different temperatures is measured and used to monitor the final conversion change. A mechanistic kinetic model is proposed to simulate both the reaction kinetics and the final conversions of various resins in low temperature copolymerization. The results may shed light on resin modification and process innovation.
Supercritical carbon dioxide (scCO2) was added during compounding of polystyrene (PS)/poly(ethylene-methyl acrylate) copolymer (SP 2207) and poly(methyl methacrylate) (PMMA)/SP 2207 blends and the resulting phase inversion, morphology, and mechanical properties were studied. SP 2207 is a 80 wt.% ethylene-20% methyl acrylate copolymer used to increase the toughness of polystyrene and PMMA. Carbon dioxide was added at 2.0 wt.% based on polymer melt flow rates. Carbon dioxide injected into the extruder sped up the phase inversion of the two components by reducing the glass transition temperature of PMMA and PS. This allowed for an enhanced dispersion of the rubber phase after phase inversion. An earlier extruder location at which phase inversion occurred along with a reduced viscosity ratio greatly improved the dispersion of the rubber copolymer in the polystyrene and PMMA matrix. An increase in impact strength and a reduction in the flexural modulus of blends prepared with CO2 were measured, indicating that CO2 aided in dispersing the rubber into the brittle matrices of polystyrene and PMMA. Reprocessing did not result in a loss of morphology for PMMA/SP 2207 blends.
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