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Conference Proceedings
In Line Compounding/Injection Molding with a Discontinuously Operating Twin Screw Extruder
Johan Billiet, Thomas Leng, Klaus Kapfer, Daniel Schwendemann, May 2001
For standard injection molding a granule length of 10 - 12 mm is used in long glass fibers applications to achieve an optimum fiber length distribution in the part. The resulting fiber length in the part is limited to approximately 3 - 5 mm. To increase the fiber length in the molded part it is necessary to directly compound the glassfibers into the polymer on the injection molding machine. The presentation describes a very cost effective way to produce injection molded parts with long glass fibers on a system where a discontinuous running twin screw extruder fed with glass rovings is directly mounted on a two stage injection unit. The advantages of this configuration compared to a continuously running twin screw extruder and discontinuously running single screw extruder mounted on a two stage injection unit were evaluated and are described in depth.
Formulating Foamable Resins for Achieving a Given Volume Expansion Ratio in Rotational Foam Molding
Remon Pop-Iliev, Ghaus M. Rizvi, Chul B. Park, May 2001
The rotational foam molding process is suitable for fabricating rotational moldings intended for applications that require their internal volume to be entirely or partially occupied with a cellular structure. Whether the outcome of this process will result in articles having a fully foamed core or just a foamed layer with a given thickness depends on the volume expansion ratio for which the foamable resin has been formulated and the shot size the mold has been charged with. Although the amount of chemical blowing agent (CBA) that should be introduced into the polymer in order to prepare a foamable resin that would be suitable for satisfying the required expansion characteristics can be theoretically calculated, in practice, due to various reasons, a portion of the generated blowing gasses during the rotational foam molding cycle is often inevitably lost via the mold's vent(s). As a consequence of this unaccounted loss of blowing gas, a discrepancy exists between the theoretically calculated and the practically achievable volume expansion ratio of a particular foamable resin. Thus, in order to compensate for the loss of the blowing gas that takes place during the foaming stage, the amount of CBA introduced into the polymer while preparing the foamable resin should be greater than the theoretically calculated. This paper establishes the relationship between the theoretically calculated level of CBA concentration in the foamable resin formulation and the actual experimentally-obtained volume expansion ratio in order to predict the necessary CBA concentration correction factor for a given volume expansion ratio and polymer material-blowing agent combination.
Importance of Timely Polymer Sintering Versus Blowing Agent Decomposition in Rotational Foam Molding of Polypropylene
Remon Pop-Iliev, Ghaus M. Rizvi, Chul B. Park, May 2001
Producing polypropylene (PP) foams with satisfactory cell morphologies in rotational foam molding is feasible. However, the narrow interval between the melting temperature of PP and the onset decomposition temperature of the suitable chemical blowing agent (CBA), together with the low melt strength of PP at elevated temperatures, often represent the greatest obstacles in the foaming of PP. Experimental results revealed that the morphology of the foams obtained by processing PP pellets that have been pre-compounded with a CBA could be governed by either pellet sintering or cell coalescence. The viscosity of the basic PP resin and the processing temperature determine which of these two key factors will assume a predominating influence towards the foaming process. Desirable PP foam structures in compounding based rotational foam molding could be obtained only if pellet sintering takes place prior to the decomposition of the CBA and if the processing temperature during the foaming process is kept lower than the temperature of cell coalescence.
Load Oriented One-Step-TWINTEX®-Sandwich-Structure for Large Scale Production of Automotive Semi-Structural Components
Frank Henning, Stefan Troester, Peter Eyerer, Ingo Kuch, May 2001
In a joint project with the German automotive industry, the Fraunhofer Institute, material suppliers, component-and mold manufacturers, a thermoplastic sandwich material has been developed. The goal is to offer a cost-effective material with increased mechanical properties to combine the advantages of In-Line-Compounded long fiber reinforced thermoplastics (LFT-ILC) or well-established thermoplastic semi-finished products like GMT and advanced thermoplastic TWINTEX® woven fabrics. These requirements are fulfilled by a sandwich which consists of outer layers of woven fabrics and a core layer of recycled material mainly of shredded TWINTEX®, GMT or LFT components or production waste. The foot support for the smart vehicle has been selected to evaluate the sandwich system.
Phase Separation Behavior of Ethylene-Styrene Interpolymer Blends
H.Y. Chen, W. Cheung, M. Guest, S.P. Chum, A. Hiltner, E. Baer, May 2001
Blends of ethylene-styrene interpolymers (ESIs) are a model system for studying the miscibility of a-olefin copolymer blends. The phase behavior of partially miscible ESI blends, with styrene content difference 9-10 wt%, was characterized by phase diagrams. Blends were rapidly quenched from the melt to retain the phase morphology, and the volume fractions of the two phases were obtained from AFM phase images. Assuming monodisperse polymers, the phase composition was approximated by extrapolation of the relationship between blend composition and phase volume fraction. The blends exhibited an upper critical solution temperature (UCST). The UCST decreased with decreasing molecular weight and decreasing styrene content difference. Phase compositions were also obtained with an analysis that considered the molecular weight distribution. Calculated results indicated that phase compositions depended on the initial blend composition. The interaction parameter obtained with this approach was independent of molecular weight and was proportional to the square of the styrene content difference. The solubility parameter, extracted from the interaction parameter, agreed with literature values.
Effect of Adhesion on Structure and Properties of Blends of Polyethylene and Polypropylene
A. Chang, B. Poon, L. Tau, S. Chum, A. Hiltner, E. Baer, May 2001
The morphology and mechanical properties of PP/LLDPE melt blends were compared and related to differences in adhesion. Blends of conventional Ziegler-Natta and metallocene PE's with conventional and high melt strength PP's were examined in terms of phase morphology by SEM and mechanical properties by tensile stress-strain measurements. By comparing blends of similar morphology, differences in tensile properties could be correlated to adhesion. Interfacial structures of yielded specimens observed with SEM were consistent with yield stress and modulus analyses that suggested differences in interfacial adhesion among the blend systems.
Process Window Identification for a Very Tight-Tolerance Injection Molded Part with Multiple Performance Criteria
Hamdi H. Demirci, May 2001
The injection molded part is for a very critical radar application and therefore its parabolic form has to be maintained through stringent application and environment conditions, while satisfying a number of other functional and quality requirements. A D-Optimal Design Of Experiments (DOE) analysis was run to identify an optimal process window in the four parameter design space, within which, ten very critical and tight-tolerance performance criteria were satisfied simultaneously. Prediction models generated based on the DOE analyses were shown to accurately represent the actual molding process. These models were then coded in a program to be utilized by molding engineers in process sensitivity analyses.
Innovations in Pad Printing - New Process Controls
John Marshall, Mike Learmouth, May 2001
Recent technical breakthroughs in pad printing machinery; such as automatic ink viscosity control, automatic pad cleaning, and compact automation friendly designs will assure a place for modernized pad printing well into the future. Gone are the old-school open inkwell systems that had their share of problems in production. Many modern machines have also been designed with an approach that requires only one (or two) nesting fixtures, giving many molding facilities ultimate flexibility without massive tooling costs. With these new process control innovations having been developed, the pad printing process now allows easy integration into automated systems. To help further bring pad print systems into modern molding facilities, the ink systems utilized have also made many technical leaps forward.
Free Radical Grafting of Maleic Anhydride on Polypropylene in the Presence of Supercritical Carbon Dioxide
Beth Dorscht, Costas Tzoganakis, May 2001
The functionalization of polypropylene (PP) with maleic anhydride in the presence of supercritical carbon dioxide was studied. Supercritical carbon dioxide was used in this reactive extrusion system to reduce the viscosity of the polypropylene melt phase by forming a polymer-gas solution in order to promote better mixing of the reactants. For that purpose, a reactive extrusion system was developed to facilitate grafting of maleic anhydride onto PP under supercritical pressures in a section of a twin screw extruder. Subsequently, the effect of supercritical carbon dioxide on the level of grafting, product homogeneity and molecular weight was evaluated. Analysis of the products revealed that the use of supercritical carbon dioxide led to improved grafting when high levels of maleic anhydride were used. The experimental results showed no evidence of an improvement in the homogeneity of the product while melt index measurements showed a reduction in the degradation of polypropylene during the grafting reaction when low levels of maleic anhydride were employed.
Development of Hollow Strand Plastic Foam
Slava Grinshpun, Michael Schaller, May 2001
We have developed a novel extruded foam structure that appears to have many advantages over current structures. The concept is a unique extension of the technology used to produce The Dow Chemical Company's STRANDFOAM* brand extruded polypropylene (PP) foam products. STRANDFOAM brand PP foam products are produced by extruding a gel made up of polymer and dissolved blowing agent through a die consisting of an array of holes. As the gel exits the die, it expands to form individual solid cylinders that coalesce into a solid plank. Hollow strand foam is produced in a similar fashion, except that the polymer gel is extruded through an array of annuli instead of an array of holes. This process produces hollow strands or tubes that expand and coalesce into a plank. The hollow strand structure gives the foam a host of interesting properties. For example, the hollow strand foam has excellent compressibility and recoverability compared to solid foam planks of similar composition. In addition, the new structure allows easier production of foam products with a low bulk density. Perhaps most intriguingly, it is possible to combine the hollow strand foam with solid strand or plank foam to produce products having two sets of performance attributes. There are numerous extensions of, and applications for, this technology. Examples include: impact energy absorbers; high impact packaging with built in drainage; low density hard to blow" foams like PET PC; leveling insulating board for concrete surfaces; combined thermal and acoustical insulation."
Advances in Understanding the Performance of Multilayer Films for Packaging Applications
Barry A. Morris, May 2001
A food package is called upon to perform a number of functions, including • providing a hermetic seal, • protecting against the environment (e.g., controlled moisture or oxygen ingress or egress, puncture resistance, impact resistance), • safeguarding the flavor of the food, • allowing the product to be packaged on high speed filling lines, and • conveying information to the consumer (e.g., advertising and product contents). A single material often cannot provide these functions in an economical way. Hence, multilayer structures are prevalent in the packaging industry. A number of examples are illustrated. Several processes are used to make multilayer packaging films including extrusion coating, lamination, coextrusion and various combinations. This paper will deal primarily with coextrusion. Designing and manufacturing multilayer films present special challenges beyond those encountered when making single layer structures. In this paper we will review recent progress made in understanding four such challenges: interlayer adhesion, the effect the coextrusion process itself may have on properties, stiffness and curl.
Prediction of Residual Deformation in Clamped NORYL GTX Plates after Thermal Cycles
Ihor D. Skrypnyk, Jan L. Spoormaker, May 2001
This paper is aimed on the development of a constitutive model for NORYL GTX with the purpose of Finite Element (FE) prediction of the residual deformation, caused by thermo-mechanical cycling of structural elements. This material is a blend, produced by General Electric Plastics and widely used in automotive industry. Two brands of this thermoplastic: NORYL GTX 964 and NORYL GTX 974 are specially developed for automotive parts for in-line painting. The technology of in-line painting includes thermo-cycle with maximum temperature ~ 170°C. Therefore, the aim of this study is related to prediction of performance of thermoplastic parts during and after the thermo-mechanical cycles (of painting). For this purpose an earlier developed non-linear visco-elasticity model of relaxation type is employed. The model calibrated using the experimental data on sagging of single-side-clamped thermoplastic plates under thermal cycles. The ability of the model to predict independent events was validated basing on the data from the tests of double-sides-clamped plates, subjected to a thermo-mechanical loading. Difference between the model prediction and the results of controlling tests is less than 10% that confirms applicability of the model proposed.
A Closer Look at the Long-Chain Branch Formation in Ethylene Polymerization Using Metallocenes
Daryoosh Beigzadeh, João B.P. Soares, Thomas A. Duever, May 2001
Polymerization of ethylene using metallocene catalysts, particularly the constrained geometry catalysts (CGC), was studied. The main focus of the paper is on the control of chain microstructure in olefin polymerization using metallocene catalysts, particularly long chain branching in ethylene polymerization. Combined metallocene catalysts, consisting of CGC and a conventional metallocene catalyst, which only produces linear chains (linear catalyst), were used to manipulate long chain branching degree. The feasibility of this technique was verified using a mathematical model developed for the polymerization of ethylene in a semi-batch reactor using combined catalyst systems. Polymerization experiments were performed to verify the validity of the proposed technique and some of the modeling results. It was shown that by choosing a proper catalyst system and polymerization conditions chain microstructure could be tailor-made. Monte Carlo simulation was also used to study the structure and length of the branches in metallocene catalyzed ethylene polymerization. This information is essential for making any correlations between LCB degree and rheological properties.
Determination of Comonomer Distribution in Ethylene/?-Olefin Copolymers
Daryoosh Beigzadeh, João B.P. Soares, Thomas A. Duever, May 2001
Estimation of chemical composition distribution in ethylene/?-olefin copolymers using crystallization techniques is studied in this paper. Monte Carlo simulation was used to model the fractionation process in crystallization analysis fractionation (CRYSTAF). Five poly(ethylene/1-octene) samples synthesized with a single-site-type catalyst were used to verify the simulation results. It was proposed that the fractionation mechanism be controlled by the crystallization of the longest ethylene sequence in each chain. Good agreement between experimental and simulation results verified the validity of the proposed fractionation mechanism.
Evaluation of Thermal Environment in Plastic Injection Mold
Feng Gao, Hiroshi Koresawa, Hiroyuki Narahara, Hiroshi Suzuki, May 2001
Thermal deformation is one of the major problems that affects a product's quality in plastic injection molding. It is very important to have an accurate evaluation of the thermal environment surrounding the injection mold, especially in the case of high precision or large product molding. This paper proposes an evaluation method of thermal environment with a consideration of both the effect of the resin solidification process and the product's geometric shape. With this method, the validity of the thermal environment in different cooling designs is discussed using numerical analysis.
Vibration Welding of Dissimilar Nylons
Valerie LeBlanc, Bobbye Baylis, Liying Qi, Dan Watt, May 2001
Tensile strengths of linear vibration welds of nylons with different melting temperatures and glass contents were determined. Two different geometries were investigated: T-welds and a cylinder welded to a plaque. The study involved weld strengths for both homogeneous" welds where both components being welded were the same and for "heterogeneous" welds where the two components were made of nylons of different melt temperatures. It was determined based on the T-weld and the cylindrical-weld analysis that there is potential for dissimilar material weld combinations using vibration welding as the joining process. Relatively high weld strengths were obtained when PA 6 (and PA 66) was welded to the 3 different PPA's. For the short-glass-fiber materials one of the factors influencing weld strength was the difference in melt temperature between the two resins: greater difference in melt temperature resulting in lower weld strength. The long glass-fiber reinforced material which is predominantly PA 66 exhibited approximately the same weld strength regardless of the difference in melt temperature between it and the other nylon to which it was welded."
Development of an Extrusion System for Fine-Celled Foaming of Wood-Fiber Composites Using a Physical Blowing Agent
H. Zhang, G.M. Rizvi, W.S. Lin, G. Guo, C.B. Park, May 2001
This paper presents an innovative design of a tandem extrusion system for fine-celled foaming of plastic/wood-fiber composites using a physical blowing agent (PBA). The plastic/wood-fiber composites utilize wood-fibers as reinforcing filler in the plastic matrix and are known to be advantageous over the neat plastics in terms of the materials cost and some improved mechanical properties such as stiffness and strength. However, these improvements are usually accompanied by sacrifices in the ductility and impact resistance. These shortcomings can be reduced by inducing fine-celled or microcellular foaming in these composites, thereby creating a new class of materials with unique properties. An innovative tandem extrusion system with continuous on-line moisture removal and PBA injection was successfully developed. The foamed composites, produced on the tandem extrusion system, were compared with those produced on a single extruder system, and demonstrated significant improvement in cell morphology, resulting from uniform mixing and effective moisture removal. The effects of both wood-fiber and PBA (CO2) content on the cell morphology and foam properties were studied. Increasing the CO2 content marginally improved the cell structure, whereas, increasing the wood-fiber content had an adverse affect. The effectiveness of a coupling agent was also evaluated. The cell morphology and foam properties showed improvement when the coupling agent was added.
An Experimental Investigation of the Plug Assist Thermoforming Process
G.W. Harron, E.M.A. Harkin-Jones, P.J. Martin, May 2001
This work investigates the influence of processing parameters on the properties of thermoformed polypropylene pots. Fourteen parameters were studied using a Design of Experiments methodology encompassing the polypropylene resin, extrusion parameters (Chill Roll Temperature and Line Speed) and thermoforming parameters including Plug Geometry, Plug Speed, Air Pressure and Sheet Temperature. The thermoformed pots were measured for wall thickness distribution, weight, and compression resistance. The force exerted on the plug during the forming cycle was also recorded, with a long-term goal of incorporating this data into a process control system for Plug Assist Thermoforming. Results show that the parameters associated with the plug have the greatest effect on the final pot quality.
Nonlinear Rheological Behavior of LDPE Melt during Capillary Extrusion under Vibration Force Field
Xiangfang Peng, Jinping Qu, Hui Zeng, May 2001
In order to study the rheological behavior of polymer on vibration force field, a new capillary dynamic rheometer has been successfully developed by us for the vibration extrusion experiments of polymer melts. In this paper the measuring principles for the capillary rheological behavior of polymer melts under vibration force field will be introduced. By the experiment study of low-density polyethylene (LDPE), it has been discovered that melt viscosity and extrusion swelling ratio nonlinearly changed with the frequency and amplitude of vibration sources. The viscosity of the LDPE melt, the swelling ratio and unstable flow of LDPE decreased during capillary extrusion under vibration force field, and had a minimum with vibration frequency's change. It has great significance to the researches on dynamic extrusion and injection processing of polymer materials.
Rapid Prototype Tooling for Injection Molding Microfluidic Components Using Photodefinable SU-8 Epoxy
Thayne L. Edwards, Swomitra K. Mohanty, A. Bruno Frazier, Russell K. Edwards, Charles L. Thomas, May 2001
A rapid method for fabricating an injection molding tool using current MEMS processing is presented. The process was used to fabricate micro fluidic channels in a plastic substrate with depths of 27 µm. The tool was made using a photosensitive SU-8 epoxy on silicon. Two polymers were successfully used for injection molding the channels, clear rigid polycarbonate and opaque flexible polypropylene. Tool fabrication time was approximately 30 minutes and survived, 22 shots for polypropylene and 8 shots for polycarbonate. Deformities of the channels were observed in both plastics. Channel height was increased by 2-3 µm due to a ridge that was formed from shear forces generated between the walls. The channel width shrunk approximately 7.9% maximum for polypropylene.


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