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Cyclic-olefinic copolymers (COC) are being used in flexible packaging as a blend component or as a discreet layer in multi-layer polyolefin films. They are typically used to enhance stiffness and heat resistance in food packaging. As a core layer in laminated or coextruded multilayer films, they provide high moisture barrier and exceptional clarity and stiffness.In place of commonly used organic slip additives, they can decrease film to film coefficient of friction (C.O.F.) to levels of commercial interest. Performance as a slip additive, however, is related to a number of variables, including viscosity of the matrix, type and add level of the COC and the film process melt temperature. Various microscopy techniques investigated support the findings.
Most decisions in business (and life) are made on the basis of incomplete or estimated information. A wide range of psychological studies conducted over the past thirty years have shown that when forced to deal with uncertainty people fall back on rules of thumb that more often than not violate basic rules of probability and lead to flawed results. By understanding the types of mistakes people typically make, one can avoid these traps and improve the quality of the decisions. This paper discusses several of these, including regression towards the mean, ignoring base rates, and linked events.
The strength of Polypropylene is influenced by the thermal history of the material and oxidation experienced during molding. As the material gains more thermal exposures and subject to more shear stress, the tensile strength of the material is going to be influenced. In this work, five trials of reground polypropylene will be compared to determine the effect of multiple processing on the strength of the material. The relationship between the elongation and tensile strength of the part will be compared.Five different trials will be compared in this paper with each gaining another cycle through the machine. What affect the thermal and physical processing parameters have on the material after five runs will be examined. All of the material being used has gone through the same number of cycles, and has been processed at the same parameters throughout the experiment.
Co-rotating twin screws are the prime choice of machinery in the field of polymer compounding. Additional applications beyond that are the mixing, blending and homogenizing of viscous materials in the chemical industry where a self-wiping and thus self-cleaning profile is of the utmost interest for best performance.A great number of these processes e.g. filling with high loading of fillers, does not require extremely high powered twin screws since energy input for these materials and processing tasks is relatively low when comparing it to polymer compounding tasks such as alloying and reinforcing.It was therefore the challenge for design and process engineers to design a deep-flighted twin screw coping with these processes. The two key characteristic dimensions of a co-rotating twin screw diameter ratio" and "power-volume factor" were adapted such to meet the requirements of the low energy compounding tasks. At the same time mechanical constraints such as shaft and element interface shaft strength and gear box design had to be considered too."
Rubber compounds used in tires usually contain blends of more than one rubber to synergistically combine the properties of these rubbers. These include styrene-butadiene (SBR) and butadiene (BR) rubber or blends of natural rubber (NR) and butadiene rubber.In this study we investigated the true-stress true-strain birefringence behavior of blend of SBR and BR with a new real time spectral birefringence system and obtained the stress optical constant for the SBR/BR blends covering 10-40% BR concentration. The stress optical constants were found to decrease with the increase of BR concentration.
To exploit fully the available software tools for Finite Element stress analysis of engineering polymers, there is a need for constitutive models that capture the complexity of material behaviour. Recent work has led to the development of such a model for glassy polymers, where glass structure evolves during deformation, causing strain-softening after yield. The new anisostructural model is an extension of the physically-based 3D Glass-Rubber" constitutive model proposed earlier by Buckley and Jones. To test the model further an experimental study has been made of plastic deformation in compression of a range of glassy atactic polystyrenes with varying molecular masses. The model gave good agreement with measured strain-softening in these polymers but in its present form over-predicted the dependence of yield stress on molecular mass."
The deformation of the dispersed phase in polystyrene / high density polyethylene (PS/HDPE) blends produced by ribbon extrusion was studied numerically and experimentally. The analysis of the ribbon extrusion showed that parameters such as draw ratio (DR) and film-water contact length (X) influenced significantly the ribbon dimensions. A model was developed which enabled us to calculate the extensional stress (?xx) and the stretching force (Fo) as functions of extrusion conditions. As expected Fo, and hence ?xx, increased with increasing DR values. Furthermore, Fo not only depends on X, but also on the extrusion velocity (Vo) and the matrix viscosity (?m). The deformation of the dispersed phase and the stretching force were correlated theoretically by an uniaxial deformation analysis of the ribbon and the equilibrium shape of the particles determined by a balance between interfacial tension and extensional stresses. The results suggest that Fo is the most important parameter which determines the final shape of the particles. A comparison between the model and the experimental morphology produced a good agreement.
The studies on up-take of water and other fluids by dental composites have been important in the determining some of their properties and successful use in dentistry. Properties such as strength and adhesion using biaxial flexure strength (BFS) and shear bond strength (SBS) of one experimental and three commercial materials stored in different media, dry air, water, saline and artificial saliva were analyzed. Results subjected to one-way ANOVA (p< 0.05) showed that the strength of these materials increases in dry air but deteriorates significantly in wet conditions with time. Such observations are due to, water sorption, hydrolysis and degradation of bonds in the polymerized matrix.
The measurement of changes in polymer density during the heating and cooling cycles in rotational molding is important in terms of improved cycle times and improvement in product performance. This investigation uses Thermal Mechanical Analysis (TMA), to continuously measure density changes of a range of thermoplastic powders, during heating, curing and solidification during cooling. Small samples of a range of thermoplastic powders were carefully weighed into small aluminum pans of known dimensions, with the tip of the free moving, weightless TMA quartz probe positioned on the top surface of the pan. The probe displacement was continuously recorded during the various heating and cooling cycles. Compaction of the various powders during heating, followed by compaction of the melt at elevated temperatures were easily recorded for various heating rates, holding temperatures and cooling rates.
The compounding process gains importance in the plastic processing industry, due to the increasing demands on the quality and flexibility during the production. The planetary roller extruders (PREs) convinced in comparison with other compounding machines through the thermally careful compounding, the balanced ratio of shear and heat transfer and the narrow residence time distribution , . Experimental investigations to analyse the process behaviour of PREs were carried out for the first time. For the experiments, process and material parameters were varied and different materials were used. To model the process both the essential geometric dimensions and the kinematic conditions are presented. It is shown, that the transport mechanisms in the PREs consist of a combination of forced conveying through the gearing, a pressure- drag-flow in the meltbank and flows through head and flank gaps.
The key quality requirements of automotive blow moulded parts include weight distribution, geometric tolerance and mechanical performance. This work deals with the optimization of an automotive filler panel used in a sports utility vehicle. The part is moulded with an insulating material (carpet) on one side, which renders the design of the part complex, due primarily to the non-uniform solidification of the part and the tight tolerance requirements of automotive OEM's. The proposed optimization consists of the manipulation of the die gap programming points and the mould temperature in order to optimize the part thickness distribution and to minimize the part warpage.
This Project optimizes the design of a child's tricycle frame. This is done using a topology optimization software package. Using specified material properties, this software technique analyzes a simplified finite element model with assigned loads and boundary conditions and returns a model with maximum structural rigidity and a minimal amount of material. The software goes through an internal iterative process of removing material from the model and recalculates the model's structural characteristics until an optimized shape and material distribution are created. The suggested shape may require further refinement to address manufacturing feasibility for an intended process.
State of the art methods based on mathematical models allow full characterization of the flow behavior of a solid material [1,2]. These methods draw their parameters from shear cell measurements and offer detailed analysis of the flow of the material and its potential problem . Appropriate feeder design can then be implemented to avoid such problems.The following paper describes the use of a self-made shear cell for the measurement of critical flow properties of polymer stabilizers of various physical forms.This detailed analysis is then compared to Carr's empirical model previously employed , to characterize such materials.
Economical analysis software, created as an additional feature to commercially available extrusion simulation software, is presented. The software allows calculating the price of a flat film, coextruded, product based on the structure, material price, equipment price and other economical variables. The link to the simulation software allows getting some values, such as energy consumption from the calculation rather than as an estimate. The simulation software can also indicate that the structure that is the most beneficial from the cost point of view may not be possible to be manufactured.
Gas-assisted injection molding is an increasingly used manufacturing process that allows production of parts with more uniform properties, reduced shrinkage, warpage and residual stresses. Getting the proper combination of different process parameters such as gas pressure, gas injection delay and melt temperature, makes gas-assisted injection molding more intricate than the traditional injection. Very often a successful design in gas-assisted injection comes at the end of a long trial and error process. Design Sensitivity Analysis (DSA) can help the processors improve the design and can produce substantial investment savings in both time and money. This paper compares two approaches to perform sensitivity analysis for the filling stage of the gas-assisted injection molding process. Solution of the gas-assisted process and the sensitivity of the solution with respect to different design parameters are computed in three-dimensions using a finite element method.
The design and processing of appropriate porous 3-D scaffolds is one of the most important steps towards the regeneration of damaged tissues/organs using a tissue engineering approach. Work has been going on designing scaffolds from a range of starch based polymers that combine an appropriate degradation rate, with controlled porosity and adequate pore sizes, as well as tissue matching mechanical properties.Several processing techniques have been specially developed for producing the scaffolds. The developed methods include melt based processing technologies (based on injection moulding and extrusion using blowing agents), combined techniques based on solvent casting and on compression moulding associated to particle leaching, and other innovative techniques such as in-situ polymerization. It has been possible to produce scaffolds with adequate properties and structure. Some of them can be eventually used on minimally invasive surgical techniques. Furthermore, the developed methods have no negative effect on the biocompatible behavior of the starch based polymers.
This paper presents a study about the ways in which shear, developed in the perimeter of the runner, affects the distribution of gas in gas-assisted injection molding. High-shear regions in the perimeter of the runner can be traced and followed into a part-forming cavity. The high-shear regions create variations in the melt viscosity within the cavity. Once gas is injected, the gas flow is significantly influenced by these viscosity variations. A method is investigated which controls the position of these high-shear laminates and thereby the distribution of gas within the mold.
In various extrusion processes, particularly those involving resin blends containing fillers and additives, it is often necessary to increase the melt pressure, in order to create more back mixing of the melt in the screw channel of the extruder. This can be achieved by using screen packs of different mesh sizes. They can also be used to increase the melt temperature to attain better plastication of the resin. Another application of screens concerns melt filtration, in which undesirable material is removed from the melt. In all these operations it is necessary to be able to predict the pressure drop in the screen packs as accurately as possible, as the melt pressure is closely related to the extruder output. Based on recent developments in rheology this paper presents an easy and quick method of calculating the pressure drop in a screen pack as a function of the resin viscosity, extruder throughput and the geometry of the screen. The effect of screen blocking is also taken into account. The predictions agree well with the experiments. Practical worked-out examples illustrate the design principles involved.
Growing concern for ecological issues, including international standards agreements such as ISO14001, demonstrate a clear requirement to conserve energy for both environmental and cost issues. Energy measurements on injection moulding machines both in the laboratory and in industry demonstrate the potential of process energy measurements in the development of a systematic management approach to the environmental concerns of an organization. The data gathered can also provide useful information to both the processor regarding the performance of the machine in question, and the power companies regarding the specification of supply equipment.Detailed energy measurements during the injection moulding cycle provide data regarding the energy consumption of specific machine components and/or phases of the injection moulding cycle, providing valuable data for machinery manufacturers and processors.
Four polypropylenes of different grades were used in this study to test the reliability of the use of rheological measurements in the determination of the curve of the molecular weight distribution, MWD. For this purpose, it was used the mixing rule theory based on the double reptation. A commercial software (Rheometric Scientific Orchestrator®) and another one developed in our laboratories were used for this purpose. The final data were compared with curves obtained by gel permeation chromatography, GPC. It was found that curves obtained from the rheological tests had weak agreement with the curves of GPC. However the method showed to be reliable for a comparative study among materials.
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ANTEC 2016 - Indianapolis, Indiana, USA May 23-25, 2016. [On-line].
Society of Plastics Engineers
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