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.
This paper addresses mixing, interfacial area generation and structure developement in Kenics static mixers. A statistical description of the microstructure development is obtained using the extended mapping method. This method is adopted to the special flow conditions in spatially periodic flows, of which a static mixer is an example. The efficiency of the interface generation for different mixer layouts is compared and additional attention is given to the distribution of the interfacial area across the mixer. It is shown that the extended mapping method enables us to find the blade configuration that optimizes the mixing performance, in accordance to the standard mapping method, but now including much more details concerning the microstructure development in this chaotic flow.
Nanocomposites with different clay dispersions were prepared via in-situ polymerization and melt intercalation, with and without CO2, and the structure was observed by X-ray diffraction (XRD) and transmission electron microscope (TEM). The effects of clay dispersion, concentration and processing conditions on nanocomposite morphology, fire resistance, and thermal stability were studied. The thermal stability of the surfactant and the dispersion of the clay affect the fire resistance of the nanocomposites. Dispersion of the clay also affects the thermal stability of the nanocomposite.
Hydrocarbon based oils can be used to plasticize styrenic block copolymers. At high levels (30%), the method of oil addition and the properties of the oils used will affect mixing time. This becomes very important in twin screw compounding processes where increased throughput reduces residence time (available mixing time). This paper describes the investigation of factors affecting mixing of several model polymer systems having a very low viscosity ratio (well below 0.001) using a batch internal mixer. Similar to the findings of Ratnagiri, Scott, Joung, Shih & Burch (1-5) on morphological development during mixing of immiscible and miscible polymers, we have observed Phase Inversion (PI) during mixing of miscible polymer systems of block copolymers with hydrocarbon oils (6). The time to reach high torque after addition of the hydrocarbon oil, i.e., the Phase Inversion (PI) time as defined by Ratnagiri and Scott (2), decreased with increasing viscosity and hydrocarbon oil molecular weight. It was shown that splitting of the oil addition could decrease total PI time. It was also shown that an unequal split, with the lowest amount first, led to the fastest PI times. This emphasized that a slight lowering of the major component viscosity with small additions of the plasticizing agent was the most advantageous process for decreasing total time for mixing. In addition, it was shown that part of a lower viscosity (or MW) oil could be substituted with a higher viscosity oil thereby reducing overall Phase Inversion time. Of course, it would be important that the substituted hydrocarbon oil be compatible in the final product.
Introduction Mixing is one of the important functions of a plasticating extruder. Other functions are solids conveying, melting (or plasticating), melt conveying, and, in vented extruders, degassing (or devolatilization). It is well recognized that mixing is important when different plastics are blended or when fillers are added to the plastic in an extruder. However, it is not widely understood that mixing is equally important when a single plastic is extruded. In this case mixing is necessary to achieve a thermally homogeneous melt at the end of the extruder. Plastics have very low thermal conductivity resulting in large differences in melt temperature in the absence efficient mixers along the extruder screw. When the extruder discharges a melt into the die with non-uniform temperatures the flow in the die and the extruded product quality will be adversely affected.
In the product development of plastic components, increasing use is made of laser-sintering (LS) processes [1, 2, 3, 4]. To improve properties of prototypes, the main goals of development are reproducible density, to maintain edge sharpness, and to prevent uncontrolled shrink-age. Today, R+D mainly focuses on laser-technology, development of scan strategies, and LS process optimization.Another approach to make LS even more effective for product development is to identify the most important material properties of possible raw materials (polymer powder). The knowledge of significant material proper-ties could be an important tool for the choice of the correct material as well as for the development of new raw materials (structure- and chemistry synthesis).Thus, the current research of our group summarized in this paper mainly focuses on formulating requirements for LS raw materials . Therefore, the theoretic model of isothermic laser-sintering was developed. Based upon this model it can be shown that the most important requirements for raw materials refer to crystallization and melting behavior as well as surface tension and melt viscosity.
Lipases are now known to also function as polyester synthases. In a previous report, we showed the ability of Lipase B from Candida antartica (Novozyme-435) to catalyze transesterification reactions between preformed polymer chains. To further study the kinetics and mechanism of these reactions, model reactions were performed using benzyl alcohol as the nucleophile and various aliphatic polyesters as substrates. Effects of the reaction temperature, time, nucleophile concentration, and the structure of the polymeric substrates on the rate of transesterification are reported. We also report the extent that these transesterification reactions occur with selectivity with respect to the site on chains that is cleaved.
The thermoforming industry has achieved a good understanding of the process, which has been in large scale operation since the 1950's. Consequently, control of machine settings such as heater band temperatures, plug position, plug and mould temperatures is quite advanced. However, to date, little work has been done to address the control of state parameters describing material behaviour during processing, such as sheet temperature and material distribution in the part. Control of state parameters is essential as material property changes, environmental factors and machine operating drifts can significantly change the dynamic operating point of the machine.
The question of temperature in film coextrusion is an important issue for the quality of the product. Since a direct measure of the temperatures in the melt is difficult, the modeling gives the values of the local temperatures, and the velocity profile as well. Important is the determination of the temperature at the interfaces of the layers, since this allows to compute the viscosities and the stresses at the interfaces. The ratio of the stresses is important in order to predict if the flow is stable, and to avoid instabilities. The knowledge of the temperature makes possible to avoid local overheating. We present a software running on a PC, a good tool to predict local peaks of temperature.
By combining sol-gel analysis and curemeter testing with a Monte Carlo simulation, the 160°C dicumyl peroxide initiation efficiency and scission/crosslinking ratio of a metallocene catalyzed ethylene 1-octene elastomer was determined to be 48% and 0.24, respectively. Using a calibrated simulation analysis, the network structural evolution during crosslinking was determined. Commonly used methods of curemeter interpretation were found to be severely flawed due to the combined effects of nonlinear evolution of elastically active chains, trapped entanglements, and slowly relaxing chain structures. A framework for correct interpretation of cure behavior is described.
Based on a picture of a polymeric glass as a mosaic of nanoscale clusters of differing viscoelastic characteristics, we propose a new model for glassy polymers that accurately captures the stress-strain dependence at different rates and temperatures from small strain up to yield for polycarbonate. The model allows one to interpolate and extrapolate limited experimental data (it requires three stress-strain curves as input). The model also provides insight into the fundamental issue of glassformer fragility" in the glassy state and a practical means to assess dynamic inhomogeneities within polymeric glasses."
Intrinsic Viscosity measurements are usually analyzed using the empirical Mark-Howink-Sakurada equation, which gives a power-law dependence of the intrinsic viscosity to the molecular weight of the polymer. Variation of the scaling exponent, a" with temperature is only poorly understood necessitating individual measurements at each temperature for every polymer/solvent system. The temperature dependence of "a" is shown to fall on a single universal curve under appropriate rescaling of the temperature of the solution. A method to obtain "a" from the static exponent is also described."
By application of UV-VIS spectroscopy, chromatography and some other analytical techniques new global tests and specifications for major solvent dyes have been created and validated at GE Plastics. One specification currently covers 15 dyestuffs and any number of new dyes can be added.The new testing protocols considerably speed up the QC of incoming raw materials and allow informative feedback to the supplier in case of quality issues.Rapid screening results correlate very well with color/strength data obtained in plastic testing, often making the traditional extrude-mold-test sequence unnecessary
The recent advent and commercialization of technology using single site, constrained geometry catalyst has made possible the introduction of unique ethylene/a-olefin elastomers with novel molecular architecture. These advances in elastomer technology have resulted in differentiated materials capable of impact modifying polypropylene polymers thereby offering new TPO blends with enhanced properties. This paper will explore high flow polypropylene blends modified with this distinct class of elastomers and will discuss the influence of elastomer comonomer choice, molecular weight and crystallinity along with discussions on the effect of dispersion, morphology and rheology.
The solid-state polymerization of nylon-6,6 has been studied in the presence of supercritical (SC) carbon dioxide (CO2 ) in a small autoclave. Experiments have been carried out under varying pressure and temperature conditions at several reaction times. In addition, experiments have been performed in the presence of nitrogen (N2) which is commonly used in commercial solid-state polymerization processes. The results indicate that the samples produced in the presence of CO2 have higher molecular weight and viscosity compared to those produced in the presence of N2 under the same reaction conditions. Furthermore, the polyamides produced in SC-CO2 have higher end group differences.
The mechanical, thermal and rheological behavior and the morphology of a Polypropylene (PP)/high density polyethylene (HDPE) blend and of the PP/HDPE/Woodflour composite, both modified with peroxide, were evaluated. A decrease in the apparent viscosity of the blends with the increase in the content of peroxide was found. None of the peroxide modified samples showed significant variations in the melt and crystallization temperatures. The blend modified with 0.04 phr of peroxide showed the highest Young's modulus of all. The woodflour produced a significant increase in the viscosity and the Young's modulus of the composite.
Relationships between the density of foamed rigid PVC/wood-flour composites and the moisture content of the wood flour, the chemical foaming agent (CFA) content, the content of all-acrylic foam modifier, and the extruder die temperature were determined using a response surface model (RSM) based on a four factor central composite design (CCD). The experimental results indicated that there is no synergistic effect between the CFA content and the moisture content of the wood flour. Wood flour moisture could be used effectively as foaming agent in the production of rigid PVC/wood-flour composite foams. Foam density as low as 0.4 g/cm3 was produced without the use of chemical foaming agents. However, successful foaming of rigid PVC/wood-flour composite with moisture contained in wood flour strongly depends upon the presence of all-acrylic foam modifier in the formulation and the extrusion die temperature. The lowest densities were achieved when the all-acrylic foam modifier concentration was between 7-phr and 10-phr and extruder die temperature was as low as 170°C.
The Portuguese mouldmaking industry has a driving force for competency and innovation. This attitude relies on the embodiment of the latest developments in science and technology. In 1999 the University of Minho was challenged to design a course to materialize that purpose.This idea sprung from one of the regular meetings of the Advisory Council to the Department of Polymer Engineering involving representatives of the Plastics and Moldmaking Industries and the University of Minho. As a result an MSc course is now running in cooperation with the industry.This initiative deserved the interest of the Agency for Innovation within the Ministry for Science and Technology, who meant it to be a stimulus and commitment to the joint initiatives towards the improvement of the know-how in the fields of molds and plastics, involving the government, the industry and the university.The course includes core subjects as Injection Molding or Manufacturing, and options as Communications Networks or Rapid Tooling Prototyping.The globalization of science and technology suggests this experience being open to other countries, for example developing an English version of the course with international cooperation of specialists.
The molecular orientation at the surface of injection-blow- molded bottles made from poly(ethylene terephthalate) (PET) and high density polyethylene (HDPE) was characterized by means of front-surface reflection infrared spectroscopy. For PET, the analysis was based on a method developed previously (1), while for HDPE a new approach was developed based on the C-H stretching band at 2915 cm-1 . Results obtained for two different bottle shapes and different injection mold temperatures are interpreted in terms of the process conditions.
Essential to 'intelligent manufacturing' and 'smart materials' is the ability to monitor the state of a polymer resin as it is synthesized in a reactor, as it cures during fabrication and as it ages during uses in the field. Important aspects of this sensor monitoring capability are: in situ, on-line measurement; that the signal output be related to the relevant processing and use properties; sensitivity with long-term reliability in a manufacturing and field environment. This paper addresses how to successfully use in situ dielectric sensor measurements to monitor the changing state of a polymer resin during fabrication and/or use both in the laboratory, in an industrial plant, and during use in the field. The talk will address thermoset and thermoplastic materials as neat resins, composites and coatings.
Flow simulation is one of the most important CAE tools used in concurrent engineering for injection molding process. However, it is not a panacea. Users need to understand its capability limitation and use it in a correct way before it can become a useful and powerful tool. In this paper, a two and half dimensional flow simulation (three dimensional temperature analysis and two dimensional pressure analysis) is focused. A few insides regarding modeling, numerical method, molding dynamics, material property modeling, and heat transfer effects will be discussed. This understanding can help us analyze simulation results and make an engineering decision wisely.
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ANTEC 2016 - Indianapolis, Indiana, USA May 23-25, 2016. [On-line].
Society of Plastics Engineers
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