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.
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Evaluation of Thermoplastic Polyurethane Based Thermoplastic Vulcanizates for Interior Automotive Applications
Although thermoplastic polyolefins (TPOs) have been considered as costwise and environmentally attractive materials, they face the difficulty in being used as potential automotive applications because of poor scratch resistance and oil resistance. The new thermoplastic vulcanizates (TPVs) composed of thermoplastic polyurethane (TPU) / polypropylene (PP) /polystyrene-block-poly(ethylene-co-propylene)- block-polystyrene copolymer (SEPS) systems have been found out to have outstanding oil resistance and scratch resistance. Now they can be used for various kinds of automotive applications such as injection molded, blow molded, extruded, calendered and further, slush molded automotive parts, particularly for automotive interior skins without any coat. The essential issue is conceivably just prolonged weathering resistance and durability. In this paper, this new TPVs are evaluated from the standpoints of weathering stability, long term heat aging and fogging as well as the mechanical and physical properties.
Study of the Characteristics of Thermoplastic Vulcanizates of PP/SEPS/SBS Blends
Thermoplastic vulcanizates (TPVs) of polypropylene (PP)/polystyrene-block-poly(ethylene-co-propylene)- block-polystyrene copolymer (SEPS) are able to become much more fascinating for automotive and architecture industry by using polystyrene-polybutylene-polystyrene copolymer (SBS) together. While SBS decreases tensile strength in these systems , it does improve compression set and oil resistance greatly and furthermore, overall balance of properties improve in proportion to the amount of peroxide as coupling agent and acrylic ester as coupling coagent. The goal of this study is to investigate the interaction between SEPS and SBS, which are dynamically crosslinked and microdispersed in PP matrix from the point of mechanical behavior and morphology.
Characterization of Dual Crystalline Texture and Process-Structure-Property Relationships in HDPE Blown Films
The crystalline texture in selected high-density polyethylene (HDPE) blown films was studied using transmission electron microscopy, small-angle X-ray scattering and infrared dichroism. An orthogonally oriented dual crystalline texture was found. This structure appears to consist of two superimposed uniaxial crystalline textures. In one texture the lamellae are stacked along the machine direction, while in the other, the lamellae are stacked along the transverse direction. The lamellar populations in the two textures are affected greatly by the neck height of the film blowing process. The mechanical properties of the HDPE films can be well correlated with the dual crystalline texture observed.
Relationship between Local Residence Time and Distributive Mixing in Sections of a Twin Screw Extruder
Local residence time and distributive mixing were measured in conveying sections and kneading blocks of a twin screw extruder. The residence time measurements were completed using carbon black as the tracer and an infrared temperature probe to detect the temperature decrease caused by the changing surface emissivity. A mixing limited interfacial reaction between polymer tracers was used to directly measure the distributive mixing. Possible relationships between mixing and residence time in the sections of the twin screw extruder were investigated by combining these two measurements.
Rheology and Degradation Kinetics of Poly(ethylene terephthalate)/Poly(ethylene naphthalate) Blends
Blends and copolyesters of poly(ethylene terephthalate)/poly(ethylene naphthalate), PET/PEN, have shown promise in high performance container applications. Both rheology and degradation kinetics of these blends have been studied as a function of material composition. Melt viscosity loss was measured as a function of time and temperature. Activation energies for degradation were calculated from experimental data. Results show that blends containing a minimum of 10% PEN by weight are as stable as PEN. Addition of low amounts of PEN to PET causes a depression in melt viscosity. A critical composition of 10% PEN by weight is required before we observe an increase in blend viscosity.
A New Barrier Screw Design Utilizing Solid Bed Deformation with Forced Melt Removal
A new patent pending barrier screw geometry incorporating modifications to the solids channel of the barrier section of the screw was introduced to improve melting and mixing efficiency. The new design geometry repeatedly deforms the solid bed to improve melting and mixing. Cross channel pressure gradients and screw pull-outs obtained from crash cooling experiments were used to investigate the working principles of the new design. The results were compared to those obtained under similar conditions with a conventional barrier screw.
Towards Design Guidelines for Injection Molded Biodegradable Plastics Products
Specimens of two semicrystalline biodegradable thermoplastics, polyester-amide and polyhydroxybutyrate, injection molded at various settings, have been tensile tested. Upper limits to wall thicknesses with respect to surface appearance were found less severe than for traditional plastics. Molding settings appeared important for mechanical behavior. A higher degree of crystallization was obtained for polyhydroxybutyrate when the cooling rate was decreased. The lowest possible mold fill pressures appeared preferable, increasing ductility for both materials.
A Novel Gas Driven Dual Barrel Capillary Rheometer
A new capillary rheometer has been developed which is gas driven using a high-precision pressure controller. The flow rate is determined on-line. A precision pressure transducer controls the applied pressure to a maximum 21 MPa with an accuracy of better than 0.1%. The rheometer described here has a twin barrel system. Due to the equilibrium N2-pressure control in both barrels, creep tests can be performed, applying constant pressure irrespective of the installed die geometry. The flow rate from each barrel is independently measured.
Flow Surging in Single-Screw, Plasticating Extruders
Flow surging in single-screw, plasticating extruders is the variation of the machine's rate with time, and it generally leads to higher production costs, lost production, and often higher scrap rates. Flow surging can originate from many different sources including machine controls, resin feedstock variation, screw geometry, and machine temperature. This paper will focus on flow surging that originates from improper solids conveying, and it will present experimental data and corrective action to eliminate or minimize surging.
The Heating/Melting Mechanism of Plastic Energy Dissipation
The Paper discusses the bulkwise heat source melting mechanism, we have termed Plastic Energy Dissipation (PED). When solid particulates are deformed in the melting section of polymer processing equipment, where melting occurs in a dissipative mix melting mode, part of the applied mechanical energy to deform solid particulates dissipates into heat. The amount of heat dissipation is quite large for both amorphous and semicrystalline polymers. A number of PED experiments were conducted as functions of strain rate, strain and temperature and the iso-temperature rise plots were obtained in temperature-strain space for commercial amorphous and semicrystalline polymers. A method to estimate melting length for Co-TSE was also developed.
Transesterification Reaction Kinetics of Blends of Poly(ethylene terephthalate) and Poly(ethylene naphthalate)
Blends of poly(ethylene terephthalate)/poly(ethylene naphthalate), PET/PEN, have exhibited properties that are of commercial interest to the packaging industry. Melt processing of PET with PEN results in transesterification reactions. The blend properties are controlled by the kinetics of these reactions and these have been widely studied. Modifications to the chemical kinetic equations have been made to predict a theoretical processing temperature for different compositions of the blends to achieve critical transesterification. These values were found to be in close agreement with the experimentally observed values when blends were processed in a twin screw extruder.
The Influence of Morphology on the Impact Performance of an Impact Modified PP/PS Alloy
Brittle impact failures were observed at low temperature on blow molded parts made from a PP/PS alloy that is normally ductile for injection molded parts tested at same temperature. An investigation was launched to determine the cause of these failures. SEM analysis on the inside surface of the blowmolded part revealed the presence of micro-voids and large spherulites. Additionally, cross-sectional analysis of the inside surface showed coalescence of the impact modifier. These factors are believed to have contributed to the brittle failures. A test method was developed in an attempt to confirm these findings.
Shrinkage Behavior of Oriented Poly(ethylene terephthalate)
The kinetics of thermal shrinkage of poly(ethylene terephthalate) films have been characterized and related to various parameters of the stretching process. Amorphous orientation functions and levels of crystallinity have been found to be of major importance to the shrinkage process. As film extension ratios increase, shrinkage behavior passes through five different regions. Shrinkage first increases with extension ratio, decreases with further extension to reach a minimum, and then increases again as extension is continued to higher levels. A schematic model has been proposed to describe molecular changes in polymer chain structures, within each of the shrinkage regions. Activation energies of shrinkage have been determined in addition to equilibrium shrinkage and shrinkage rate constants.
Filament Winding of Bicomponent Fibers Consisting of Polypropylene and a Liquid Crystalline Polymer
Bicomponent fibers consisting of a sheath of polypropylene (PP) and a core of thermotropic liquid crystalline polymer (TLCP) were used in filament winding to form tubes suitable for transporting liquid oxygen. As the first step, the TLCP/PP bicomponent fiber was spun and the mechanical properties of the fibers were determined as a function of temperature to establish the conditions suitable for filament winding. Under these conditions the tensile modulus and strength of the filaments can be maintained in the filament wound products.
Heat Transfer in Extruder Screws
In the study and modeling of the resin temperature in extruder channels, the screw is commonly assumed adiabatic. However, the resin begins as a cold solid and is melted and heated as it flows, which requires that the screw also be cold at the entrance and hot at the exit. Heat must, therefore, be conducted in the screw metal from the hot end of the screw to the cold end, which requires heat transfer with the melt. Also, the heat capacity, especially of larger extruders, can require significant time to attain steady-state operation. A model of transient heat conduction in the screw coupled to heat transfer with the resin feed, melting, and pumping is used to investigate these two phenomena.
Electrospun Nanofibers of Electronic and Photonic Polymer Systems
Electrospinning employs strong electric fields to create nanometer scale fibers. The fibers are collected as a non-woven fiber membrane with a very large surface area to volume ratio. Sulfonated polystyrene, enzymatically synthesized polyaniline and blends thereof, and dye-sensitized composite polymeric systems were electrospun and studied to optimize fiber formation. It is expected that these types of electrospun materials will find potential use as new lightweight electronic and photonic materials in numerous device applications.
A Fast Approach to Automotic Runner Balance
Runner balance is one of the most important issues to be addressed for multi-cavity mold in the mold design phase. Poor runner sizing will lead to Christmas tree filling pattern and hence different residence time of plastic melt on each cavity. This leads to excessive packing pressure on small cavity and part weight variation. This problem becomes more crucial for the so-called family mold. In this work, the concept of flow balance index (FBI) is proposed to address this problem. Real industrial cases are studied by this new approach and are verified by molding trial results.
CAE Approach to Relieve Notebook Connector Air-Trap Problems
Air trap problem is crucial to notebook connectors that have complicated rib-hole structure and thickness variation. Engineering experience is usually not enough to provide a suitable gate-runner system design for these intricate parts. In this work, various design proposals are examined via mold filling simulation in order to avoid potential air-trap and void problems. This approach is proved to be effective to notebook connector mold designer for verifying design on computer before mold is constructed.
Preventing Sink Marks of Injection Molded Parts Using CAE Analysis
Sink marks on injection molded parts were caused mainly by part geometric design, mold design, and molding process conditions. This paper describes the dominant factors causing sink marks on injection molded part that can be predicted using CAE injection molding simulation programs. Sink marks on injection molded parts should be prevented for a new part design or solved for an existing one based on simulation results. In this study, a Bearing Bur, Laser printer part was chosen to illustrate how sink mark problems were solved using a commercial available C-MOLD® simulation program. The predicted sink marks of the Bearing Bur were compared to the measurements of an actual production part. Predictions were in good agreement with the actual injection molded part.
Apparent Viscosity Measurements for Determining Injection Molding Dimensional Variations
Injection molders presently use the Apparent Viscosity Curve" to determine the optimum fill time for a particular mold. Once the fill time has been determined the Viscosity Curve is set aside and the goal of the molder is to maintain the fill time. The motivation for my work is not only to determine fill time but also to quantify the melt viscosity using an injection molding machine/mold combination. The ability to determine the melt viscosity would assist the molder with "root cause" analysis when evaluating small dimensional shifts. The study will focus on determining if the derived viscosity using traditional rheological equations is of value when compared to dimensional or cosmetic changes."
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