SPE Library

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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Conference Proceedings
Effects of Processing Conditions on Extruded Polystyrene Sheet Feedstock Quality
Kolapo P. Adewale, Robert Roberts, May 2000
This work investigates the influence of various extrusion parameters on the physical properties of rubber modified polystyrene sheets. The extrusion parameters under consideration are melt temperature, chill-roll temperature, line speed and sheet thickness. Optimum extrusion conditions for producing polystyrene sheet feedstock are discussed.
Viscoelastic Stress Calculation in Multilayer Coextrusion Dies
C. Tzoganakis, M. Zatloukal, J. Perdikoulias, P. Saha, May 2000
Calculation of transient viscoelastic stresses in a coextrusion die is performed using the modified Leonov constitutive equation and the deformation rate field from finite element simulations. It is shown that a heuristic criterion based on the difference of normal stress differences across the layer interfaces may be used to potentially detect the onset of interfacial instabilities. Finally, it is shown how this criterion may be incorporated into current design practices to optimize resin selection and die design in order to eliminate interfacial instabilities.
Dynamic Vulcanization of Elastomers in Polypropylene Blends
Miguel A. López, José M. Kenny, May 2000
The use of innovative crosslinking agents for the preparation of thermoplastic vulcanizates (TPVs) is investigated. In this preliminary study, the most common TPVs systems, based on polypropylene (iPP) and rubber ethylene-propylene-diene terpolymer (EPDM) blends, are studied. Typical vulcanization agents, such as sulfur, phenolic resins and peroxides do not permit to crosslink saturated elastomers and, furthermore, give rise to dynamic vulcanization of the polyolefins. For this reason, the main goal of the present study is to investigate a new vulcanization agent for elastomeric matrices. This agent is based on azide derivative, 1,3-bis sulphonyl azide benzene that, for the specific behavior of the sulphonyl azide group, allows its interaction with the C-H bonds of the elastomeric phase and of the polyolefin. The study includes the dynamic vulcanization of PP-EPDM blends and their rheological, mechanical and thermal characterization. A comparison with traditional blends prepared with sulfur as vulcanization agent is also presented.
Effects of Fibers on the Crystallization of Polypropylene in Binary and Ternary Composites
Miguel A. López, Jerico Biagiotti, Luigi Torre, José M. Kenny, May 2000
The simultaneous effects of the incorporation of different types of fibers and of the presence of EPDM on the crystallization kinetics and thermodynamics of isotactic polypropylene are presented. The study is applied to the behavior of polypropylene matrix composites reinforced with glass, PET, aramidic and sisal fibers. The results obtained show that in all cases, either the fibers and the EPDM rubber behave as effective nucleant agents for the crystallization of polypropylene. A dramatic decrease of the half time of crystallization, t1/2, and an increase of the overall crystallization rate, Kn, are observed being the aramidic fibers the most effective. It is also reported that transcrystallinity takes places in all fibers being more evident with aramidic fibers in the neat PP matrix. Only a slight transcristallinity effect is detected when fibers were incorporated in the PP-EPDM matrix.
Best Practices: Looking beyond Benchmarking to Develop Your Business Strategy
Margaret Baumann, May 2000
Real breakthroughs in strategy and business development come from looking beyond your in-kind competitors for a process view of customer-focused solutions. A company's basic operations are first level processes and cross over industry type. Best practices is the study of identifying the companies which have developed superior processes in product development, manufacturing, customer service and market segmentation regardless of the industry they are in. This paper discusses the benefits of the study of Best Practices in addition to competitive intelligence and benchmarking in business planning. Examples of companies in the plastic industry who have distinguished themselves by their best practices will be presented.
Effects of Twin Screw Compounding Conditions on the Mechanical Properties of Nylon-6/Glass Fiber Composites
Murat Cansever, Ulku Yilmazer, May 2000
The effect of processing conditions on fiber length degradation was investigated in order to produce higher performance composites. For this aim, Nylon-6 was compounded with glass fibers in a twin screw extruder for various combinations of screw speed and feed rate. Collected samples were injection molded and izod impact and tensile strength tests were performed in order to observe the effects of fiber length on mechanical properties. Also, by using the extruded and injection molded samples, fiber length distribution curves for all experimental runs were obtained. Results show that when the shear rate is increased through the alteration of screw speed and feed rate the average fiber length decreases.
Polymer Raw Material, Process and Production Fingerprints in Injection Moulding
A.J. Dawson, A. Key, P.D. Coates, May 2000
In-process monitoring of polymer melts is found to provide a fingerprint of the: • polymer (process-relevant polymer rheometry); • the process (injection pressure-time curves which reflect the material-machine-mould combination, including polymer batch to batch variation and machine dynamic repeatability); and • production trends, with 'process indices' offering an efficient basis for 100% automatic inspection, Statistical Process Control, and even insight into factory housekeeping. Specific pressure indices in an indentified low noise region of the primary injection stage of injection moulding have been found to provide a sensitive indicator of changes in a polymer, including batch to batch changes and process-induced changes, as such measurements are closely related to the rheology of the polymer melt. The same information has also been found to provide sensitive indications of variation in the processing operation for a given polymer-mould combination, and also consequently to allow meaningful statistical analysis of trends in the injection moulding process. Laboratory and factory data for raw material, process and production trend analysis (the latter involving data from substantial production runs) are presented.
A Three-Dimensional Analysis of Coextrusion in a Single Manifold Flat Die
W.A. Gifford, May 2000
The coextrusion of two polymers through a single manifold flat die is examined. The three components of velocity and the pressure are determined in each layer along with the interface between the layers. It is shown that even when the viscosity ratio is one (i.e., single layer), flat layers" entering the die will not remain flat but will be distorted by the die. For coextrusion of two polymers the distortion of the interface profile at the exit of the die and thus the uniformity of the layers depends upon the viscosity and flow rate ratios of the two polymers as well as the geometry of the die."
Design for Rotational Molding
Jordan I. Rotheiser, May 2000
This paper will cover the details of piece part design particular to the rotational molding process. Ribs, bosses, wall thicknesses, parallel walls, internal and external corners, openings, draft angles and undercuts will be discussed. Joining features, such as inserts, hinges and molded-in threads, will also be reviewed.
Designing for the Process? (Design Details to Avoid)
Kenneth Bather, May 2000
At first glance the Rotomold process is a fairly simple one. Its capabilities are exiting and have opened new avenues for creative industrial designs including complex shapes and rugged structural parts. Successful Rotomolded designs can be obtained by keeping a few guidelines in mind from concept through to product generation. This portion of the program will cover the areas that need to be considered during the design process. Items to be highlighted are basic design guidelines, features that can compromise, complicate and delay a project and what to ask a molder about specific designs.
Novel Small and Large Scale Flow Visualisation of Polymer Melts
P.D. Coates, M.T. Martyn, M. Kamala, C. Parminter, May 2000
A novel small scale (<30g of polymer) recirculating flow visualisation cell has been designed and built. The unit comprises a single screw extruder, gear pump and variable geometry inserts making a flow recirculation loop. The recirculation flow cell is capable of being used with a range of entry geometries, including abrupt entry and hyperbolic, with a polariscope for stress birefringence, and a CCD camera and image processing system for particle streak velocimetry. This new facility complements existing larger scale flow visualisation cells in our laboratory, fitted to a single screw extruder. Information from flows in both scales of flow cell are presented for an LDPE melt.
Viscoleastic Properties of Reactive and Non-Reactive Styrene-Maleic Anhydride / Olefinic Blends
G. Bayram, U. Yilmazer, M. Xanthos, May 2000
Reactive blends of styrene-maleic anhydride (SMAH) with polyethylene/methyl acrylate/glycidyl methacrylate (PE-F) and non-reactive blends of SMAH with polyethylene/methyl acrylate (PE-NF) were produced and characterized in terms of morphology and viscoelastic properties in order to understand the reaction characteristics between anhydride/epoxy functional groups. Storage modulus, G', loss modulus, G and complex viscosity ?* of reactive blends at 25 % and 50 % PE-F were higher than those of non-reactive ones. At 25 % PE-F a maximum in complex viscosity was obtained for the reactive blends. In morphological analysis the reactive blends showed finer morphology than the non-reactive ones."
Simultaneous Measurement of Torque, Axial Normal Force and Volume Change in the NIST Torsional Dilatometer-Experiments and Analysis
Carl R. Schultheisz, Gregory B. McKenna, May 2000
The NIST Torsional Dilatometer measures simultaneously the torque, axial normal force and volume change in response to a torsional deformation. While the torque is a linear function of the angle of twist per unit of length, the normal force and volume change are effects of geometrical nonlinearities. In stress-relaxation experiments with an epoxy cylinder near its glass transition temperature, the torque and normal force decay monotonically, but the volume change associated with the torsion shows a significant non-monotonic decay at lower temperatures. The measurements are investigated with a series solution for torsion of an elastic, compressible material [Murnaghan, F.D. (1951) Finite Deformation of an Elastic Solid. Wiley, New York.].
Standard Reference Materials: Non-Newtonian Fluids for Rheological Measurements
Carl R. Schultheisz, Gregory B. McKenna, May 2000
NIST develops Standard Reference Materials for calibration, quality assurance and research into improved measurements. Two fluid standards are being developed to exhibit shear thinning and normal stresses typical of polymeric fluids. SRM 2490 is a solution of polyisobutylene dissolved in 2,6,10,14-tetramethylpentadecane. At this time, SRM 2491 is expected to be a poly(dimethylsiloxane) melt, giving less temperature dependence than SRM 2490. NIST will certify linear viscoelastic behavior and the shear-rate dependence of the viscosity and first normal stress difference at 0 °C, 25 °C and 50 °C. A round robin with the fluids will investigate variability in rheological measurements. We report progress on the project.
Comparing the Long Term Behaviour of Tough Polyethylenes by Craze Testing
K.C. Pandya, J.G. Williams, May 2000
The initiation, growth and final failure of a craze at the site of a flaw is known to precede slow crack growth under low constant load in polyethylene pipe. Most established slow crack growth tests rely on being able to generate high constraint at the crack tip in order to promote damage and micro-voiding. However, for recently developed PE80 and PE100 type grades of polyethylene, such methods cannot achieve constrained brittle fracture due to extensive crack tip blunting and the formation of large crack tip craze zones, thus invalidating the use of a conventional fracture mechanics analysis. An experimental method is described here wherein deep notched tensile specimens are used to analyse craze behaviour in tough polyethylenes under plane strain conditions. Under constant load conditions, stress - time characteristics of the craze provide good discrimination between various grades within acceptable times. Under constant speed conditions, traction - separation properties of the craze have been measured directly, yielding a rate and temperature dependent work of separation(?) which may be thought of as equivalent to Gc. Rate dependent trends in ? distinguish well between the grades allowing assessment of long term properties. The intrinsic physical justification of the method lies in the measurement and analysis of separation properties locally at the craze interface. A cohesive zone modelling technique using the 'Finite Volume' method is introduced indicating how the results may be applied to the prediction of slow crack growth in other geometries.
Aesthetics, Industrial Designers, and Designing for Rotational Molding
Gene Bothun, May 2000
Roto-mold is a versatile process which accomplishes many objectives which are difficult or impossible in other processes. It also has some special problems which complicate the aesthetic aspects of a design. Industrial designers working with engineers are uniquely qualified to design for this process.
The What, How and Why of Rotational Molding
Glenn L. Beall, May 2000
Rotational molding is a plastics molding process that is noted for producing seamless, hollow parts. The process is capable of molding complex, thin-walled, hollow parts in small and extremely large sizes. This paper will explain what the process is, how it works, and why the manufacturers of durable plastic products should be aware of this process's impressive capabilities.
Nylon and Moisture: The Real Story behind the Effects of Drying Resin and Conditioning Molded Parts on Final Properties
Michael P. Sepe, May 2000
The influence of absorbed moisture on the performance of nylon products is well documented. Similarly, the effects of excess moisture on the processing of nylon are well established. But confusion often arises in the processing community regarding the reasons for the brittle behavior of nylon parts. This paper is designed to follow the role of moisture from the pellet through to the conditioned part and separate the fact from the fiction regarding the effects of moisture on nylon properties.
Degradation of an Acetal Plumbing Fitting by Chlorine
P.R. Lewis, May 2000
It has been known for many years that both types of acetal plastic are susceptible to oxidative attack, or stress corrosion cracking (SCC) when in contact with chlorine. It was thought that high levels (>30ppm) of free chlorine in cold water are needed to initiate attack, so that acetal injection moulded fittings could be used quite safely in potable water supplies where free chlorine levels are very much lower (<1 ppm). The case study to be described here of a fracture in a water supply which caused substantial damage, indicates that attack probably can occur at such levels, especially if the fittings exhibit extensive weld lines near stressed zones. High chlorine concentrations can arise due to chlorine surges in the water supply, especially when the water company overdoses the supply after a major leak.
3D Numerical Simulation of Gas-Assisted Injection Molding Process
Florin Ilinca, Jean-François Hétu, May 2000
This paper presents a finite element algorithm for solving gas-assisted injection molding problems. The solution of the three-dimensional (3D) equations modeling the momentum, mass and energy conservation is coupled with two front-tracking equations, which are solved for the polymer/air and gas/polymer interfaces. The performances of the proposed procedure are quantified by solving the gas-assisted injection problem on a thin plate with a rib. Solutions are shown for different ratios polymer/gas injected. The effect of the melt temperature, gas pressure and gas injection delay, on the solution behavior is also investigated. The approach is then applied to a thick 3D part.

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ANTEC 2016 - Indianapolis, Indiana, USA May 23-25, 2016. [On-line].
Society of Plastics Engineers
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