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
The Genealogy of Polymers
Barbara J. Gedeon, May 2004
The supply chain for polymeric materials is a drastically changing environment. This paper will focus on the types of trade names used. Changes of ownership along with historic trade names will be discussed. Predictions of future uses and types of trade names will be made.
Thermal Control of Melt Flow in Cylindrical Geometries
Gautam Balasubrahmanyan, David Kazmer, May 2004
The control of plastic freeze-off and melt flow through a cylindrical nozzle is studied. Analysis of the temperature distribution of a nozzle contacting the mold shows a significant temperature distribution as a function of the axial and radial position in the metal and plastic. The temperature of the plastic melt determines the viscosity and subsequent flow through the nozzle. Experimental investigation validates the analysis by characterizing the pressure needed to induce flow as a function of nozzle and mold temperature. Control of the polymer freeze-off and melt flow is necessary for fully automatic production, as well as development of advanced molding processes.
Concept and Preliminary Result of a Nozzle Pressure Virtual Sensor of Injection Molding Process
J.-W. John Cheng, Tzu-Ching Chao, Li-Hung Chang, May 2004
This paper proposes a new virtual sensing approach for on-line monitoring process variables of injection molding process. In particular, a nozzle pressure virtual sensor has been developed. Exploiting the dynamic interaction between the machine and process variables, the virtual sensor utilizes the screw velocity data (a machine variable) to predict behavior of the nozzle pressure (a process variable). The virtual sensor was designed based on nonlinear observer theory. Experiment evaluation on a commercial injection molding machine was carried out, confirming the effectiveness of the virtual sensor.
Water-Assist Injection Molding – An Innovative Process Technology for Productivity Improvement - Developments in Processing, Equipment and Materials
Rainer Protte, Hartmut Bangert, Chris Cooper, Peter Hoeck, May 2004
Although water-assist injection molding is still in its infancy, this enabling technology promises productivity improvements for applications that may otherwise be cost prohibitive with gas-assist injection molding. Cycle times are reduced through cooling time reductions and the utilization of water as a cost-effective cooling medium when compared to nitrogen. For example, automotive suppliers have the potential for a broad range of cost savings with the production of conduits like cooling pipes or oil pipes. Other parts with large cross sections may also be produced in a cost-effective manner with water-assist injection molding. In fact, production parts in Europe are now beginning.Compared to the gas-assist injection molding details of the process, equipment, and the special material developments will be examined in this paper.
Effect of Injection Speed on Gas Penetration Length, Residual Wall Thickness and the Melt Front Position during Gas-Assisted Injection Molding
Jin-woong Shin, A.I. Isayev, May 2004
Extensive experiments were conducted to study the effect of injection speed on gas penetration length, residual wall thickness, the melt front position and short-shot weight of gas-assisted injection molded part. Experiments were performed on polystyrene melts filling a spiral tube cavity at three different melt temperatures. Simultaneous measurements of the screw position and the evolution of gas pressure and melt pressure in the cavity were performed. At a constant shot size, the length of melt propagation and the weight of moldings were found to increase with an increase of injection speed. An implication of these finding for gas penetration in gas-assisted injection molding was discussed.
Transient Gas/Melt Interface and Gas Penetration during Gas-Assisted Injection Molding: Simulation and Experiment
C.T. Li, J.W. Shin, A.I. Isayev, H.S. Lee, May 2004
Theoretical and experimental studies have been carried out on the transient gas-liquid interface development and gas penetration behavior during the cavity filling and gas packing stage in the gas-assisted injection molding of a spiral tube cavity. The evolution of the gas/melt interface and as well as the distribution of the residual wall thickness of skin melt along with the advancement of gas/melt front have been investigated. The physical model for both the primary and secondary gas penetrations was developed based on the Hele-Shaw approximation combined with interface kinematics and dynamics. Numerical simulations were implemented on a fixed mesh covering the entire cavity. The residual thickness of a polymer layer and the length of gas penetration in moldings were calculated using a commercial software (C-Mold) and both the simulation and model developed in this study. Extensive molding experiments were performed on polystyrene at different processing conditions. The obtained results on the gas bubble dynamics and penetration behavior were compared with those predicted by the present simulation and C-Mold.
On the Breakup of a Non-Newtonian Drop in an Extensional Flow
Moshe Favelukis, Olga M. Lavrenteva, Avinoam Nir, May 2004
The condition for the breakup, of a power-law non-Newtonian slender drop in a Newtonian liquid in an axisymmetric extensional flow, has been theoretically studied. The problem is governed by four dimensionless numbers: The capillary number, the Reynolds number, the viscosity ratio and the power-law index. The results suggest that the critical capillary number for drop breakup increases as the Reynolds number, the viscosity ratio and the power-law index decrease.
Molecular Dynamics Simulation of Nano-Scale Polymeric Rheological Properties and Extrusion Flows
Rong-Yeu Chang, Jenn-Jye Wang, May 2004
In this work the rheological properties of polymer have been studied by molecular dynamics simulation. Couette flow with various shear rates are used to investigate the degree of slip, shear viscosity and normal stress difference. The fluid consists of chains of n-hexadecane and is confined between two structured gold atomic walls. Isothermal simulations (350K) of 4 to 1 unsteady extrusion flow with various extrusion rates are conducted.
Optimization of a Flat Die Geometry
Y. Sun, M. Gupta, May 2004
Geometry of a flat die for polymer sheet extrusion is optimized to obtain a uniform velocity distribution across the exit of the die. While optimizing the exit velocity distribution, the constraint optimization algorithm used in this work enforced a limit on the maximum allowable pressure drop in the die. Effect of the shear as well as elongational viscosity of the polymer on the flow in the flat die is taken into account.
The Effect of Stabiliser Type and TiO2 Concentration on the Rheology of uPVC Profile Formulations
W.C. Yap, A.C. Ruddy, K. Halliwell, G.M. McNally, W.R. Murphy, May 2004
A range of unplasticised polyvinylchloride (uPVC) profile extrusion grade formulations, containing calcium/zinc, organotin and lead based stabiliser systems were blended with different concentrations of TiO2. Rheological analysis showed that the concentration of TiO2 (2phr - 8phr) had little effect on viscosity over the shear rate (200-1000s-1) and temperature range (170 – 190°C) studied. Mechanical analysis showed higher tensile and flexural modulii for the organotin stabilised formulations.
Setup and Optimisation of the Gas Assisted Injection Moulding Process Using an Expert System
L. Mulvaney-Johnson, P.D. Coates, R.G. Speight, P.A. Brincat, A.S. Bakharev, May 2004
An expert system has been developed here to assist the machine setter eliminate common defects from a gas assisted injection moulded product. The system breaks down the range of possible mould tool configurations into four main modes of operation. A process starting point is determined by an initialisation routine. The process is changed according to specified product defects to provide acceptable products. A further routine optimises the process by ensuring the process envelope, defined by natural random variation, does not move outside the moulding window. A multicavity mould tool has been used to validate the routines.
Three-Dimensional Simulation of Gas-Assisted Injection Molding Process
K.C. Shih, T.M. Liou, S.W. Chau, S.C. Chen, Y.W. Lin, N.T. Cheng, May 2004
In this study, the application of a finite volume discretization and volume-of-fluid method has been demonstrated to simulate three-dimensional gas-assisted injection molding processes. An effective fluid concept is employed to compute segregated multi-fluid flows. The modified Cross model and Arrhenius temperature equation are implemented in the numerical scheme in order to calculate the rheological properties of polymer flows. The numerical results successfully depict some important three-dimensional phenomena, such as the jetting effect, race-tracking effect, corner effect, and the flow asymmetry after the gas is injected, which could not be described by any two-and-half dimensional model commonly used in the current commercial CAE applications.
Comparative Performance of a H13 and Beryllium-Copper Core Caps in a Thin-Wall Injection Molding Application
Vincent Barre, Layne Lumus, Likuo Sun, May 2004
As a result of heat transfer properties superior to that of standard tool steel, copper-beryllium alloy inserts are expected to provide cycle time improvements in some injection molds. However, issues such as manufacturing cost can limit the benefits of using such inserts. A thin-wall single cavity container mold with inter-changeable H13 and Copper Beryllium core caps was used to quantify the possible differences between these materials. Under optimized single cavity process conditions (cycle time below 3 seconds), the cycle time could be significantly reduced by using the copper beryllium core cap. However, the impact properties of the resulting cups were reduced for some of the materials under investigation. No such disparity either in the process or in the mechanical properties could be observed when a stack mold process (cycle time around 5 seconds) was simulated. There is evidence that the container’ impact behavior is mostly determined by the local internal stresses near the injection gate.
A General Method of Designing Injection Molds by Straightforward Solution Procedures
Natti S. Rao, Günter Schumacher, Nick R. Schott, May 2004
The design of injection molds can be accomplished by the state-of-the-art software available on the market. However, in daily practice where quick estimates of the parameters involved are needed, the application of sophisticated software can be time consuming and costly. This paper deals with straightforward solution procedures for optimizing the mold design by taking thermal, mechanical and rheological design criteria into account. Easily applicable analytical methods are given for calculating the heat transfer between the melt and the coolant. It is shown in these calculations how the geometrical layout of the cooling channels is related to the mechanical strength of the mold material. Furthermore, explicit relationships based on resin rheology are presented for balancing the melt flow in runner systems. These proven equations are illustrated by numerous worked-out examples.
Thermal Performance of Hybrid Injection Moulds with Epoxy Inserts
P.S. Lima, João Ramos, A.S. Pouzada, May 2004
Hybrid injection molds with non-metallic components in the molding zone are being considered for short runs or pre-series. Cast resin tooling is one of the techniques for making the molding inserts. The nonmetallic materials being used have poor thermal properties that tend to increase substantially the molding cycle. In this study, the dependence of the thermal performance of hybrid molds with respect to the cooling layout was studied using epoxy inserts. Experimental data was gathered in terms of temperature at the polymer/mold interface and compared with simulation using the software C-MOLD. The thermal performance is discussed for different cooling layouts.
Medical Grade Copolyesters for Profile Extrusion
Daniel C. Cobb, Thomas J. Pecorini, Marc A. Strand, Eric J. Moskala, May 2004
Resins used in profile extrusion require high viscosity at low shear rates to improve melt strength and low viscosity at high shear rates to prevent melt fracture. This paper discusses the development of copolyester resins with the desirable rheological properties, as well as good optical and physical properties. The processing, biocompatibility, and sterilization of these resins will also be discussed.
Modeling Polymer Balloons for Angioplasty: From Fabrication to Deployment
Sébastien Delorme, Denis Laroche, Robert DiRaddo, Jean Buithieu, May 2004
Postulating that arterial injury resulting from the angioplasty intervention is a possible predictor of restenosis, a three-dimensional finite element model is proposed to predict stresses during balloon angioplasty. The model simulates balloon folding, insertion and deployment into a diseased artery. This work focuses on the balloon material model and properties, using experimental characterization and inverse modelling. A numerical example, including balloon folding and deployment inside a stenosed artery is also presented.
The Design of the Small Punch Test and its Application to Testing Medical Polymers
C. Daly, D. Leonard, F. Buchanan, J. Orr, N. Dunne, May 2004
The small punch test is a useful technique in the mechanical testing of polymers where limited material is available. This investigation focuses on the latest developments in the small punch test design, including integrated temperature control and environmental conditioning and its use in analysis of polymethyl methacrylate (PMMA) bone cement.
Plastic Medical Enclosures Made without Molds
Jim Fowler, Jack Hill, May 2004
It has never been easy, in the Medical Products Industry to design and build a custom plastic enclosure when the initial or lifetime quantities do not justify molds or tooling. In the last few years, a toolless technology has been commercialized to allow the manufacture of such enclosures, with minimal up front costs and broad design flexibility. This paper describes the technology, its application, strengths and limitations and provides an economic comparison to the other enclosure technologies used in the industry.
Sequential Injection Molding Using Fast-Response Valve Gate System
Shia-Chung Chen, Radium L.T. Huang, Pao-Lin Su, May 2004
Due to the complication in operation mechanisms, commercial valve gate usually delays for about 0.3 to 0.5 seconds once the valve-opening command is given. This signal to operation delay limits its application to 3C thin-wall injection molded parts. In this study, a fast-response gas-driven unit developed for thin-wall gas-assisted injection molding was adopted to perform valve gate control. Verifications of valve-gate opening were monitored using CCD camera, cavity pressure transducers and accelerometer, respectively. All design parameters including gas-valve response characteristics, tolerance between inner piston and cylinder, gas pressure, melt temperature, etc., that would affect valve-gate opening were investigated. The delay time for vale-gate shaft movement in a non-melt environment can be reduced to about 50 milliseconds whereas it increases to about 80 milliseconds in a melt-filled environment. The improved system results in injection molded parts without weld line and good cosmetic quality.

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"Insert title of paper here in quotes,"
ANTEC 2016 - Indianapolis, Indiana, USA May 23-25, 2016. [On-line].
Society of Plastics Engineers
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