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1. |
Coefficients of dynamic friction as a function of temperature, pressure, and velocity for several polyethylene resins |
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Polymer Engineering&Science,
Volume 35,
Issue 7,
1995,
Page 557-563
Mark A. Spalding,
Kun S. Hyun,
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摘要:
AbstractThe coefficient of dynamic friction is often the controlling factor for solids conveying, pressure generation, and thermal decomposition of a resin in the feed section of a single‐screw plasticating extruder. The coefficients of friction are, however, very poorly understood, and the interpretation of the measurements are complicated by the dissipation of frictional energy at the sliding interface. A new instrument was recently built to help understand dynamic friction, and a numerical technique was developed to estimate the interface temperture. Coefficients of dynamic friction for several polyethylene resins are presented in this paper as a function of the surface temperature, pressure, and velocity. The relationship of the data with respect to the extrusion process is discusse
ISSN:0032-3888
DOI:10.1002/pen.760350702
出版商:Society of Plastics Engineers
年代:1995
数据来源: WILEY
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2. |
Rubber modified epoxy resin. III: Reaction injection molding process |
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Polymer Engineering&Science,
Volume 35,
Issue 7,
1995,
Page 564-576
Dae Su Kim,
Sung Chul Kim,
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摘要:
AbstractReaction injection molding of amine terminated butadiene acrylonitrile copolymer (ATBN) modified epoxy resin was investigated through computer simulation and experiment. The epoxy system composed of diglycidyl ether of bisphenol A (DGEBA) and triethylene tetramine (TETA) was employed since this system indicated a relatively high reaction rate. The coupled balance equations of momentum, chemical species, and energy within the disc‐type mold cavity were solved using finite difference techniques. The predicted temperature and conversion profiles within the mold were compared to experimental results. The domain correlation length data calculated from the simulation model were compared with the results of SEM micrographs. A moldability analysis was performed to find the optimum molding conditions. The moldability window decreased as the mold thickness was increase
ISSN:0032-3888
DOI:10.1002/pen.760350703
出版商:Society of Plastics Engineers
年代:1995
数据来源: WILEY
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3. |
A flow model for non‐newtonian liquids inside a slot die |
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Polymer Engineering&Science,
Volume 35,
Issue 7,
1995,
Page 577-586
Sinh‐Luh Yuan,
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摘要:
AbstractA one‐dimensional flow model for non‐Newtonian liquids inside a dual‐cavity slot die is presented. The model is capable of analyzing slot dies of any cavity shape, cavity taper, slot‐length variations, and slot‐gap variations. The proposed model incorporates a truncated‐power‐law model for the viscosity of non‐Newtonian liquids. According to flow models with power‐law approximation for liquid viscosity, the distribution of non‐Newtonian liquid through a slot die depends on the slot Reynolds number only. With our model, we find that the zero shear viscosity and the relaxation time of a non‐Newtonian liquid have large effects on its distribution. For non‐Newtonian liquids which are expected to experience shear‐thinning over portion of a slot die, it is concluded that a flow model with a truncated‐power‐law approximation for liquid viscosity be used to predict the liq
ISSN:0032-3888
DOI:10.1002/pen.760350704
出版商:Society of Plastics Engineers
年代:1995
数据来源: WILEY
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4. |
The copolymerization of methacrylates in a counter‐rotating twin‐screw extruder |
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Polymer Engineering&Science,
Volume 35,
Issue 7,
1995,
Page 587-597
H. A. Jongbloed,
R. K. S. Mulder,
L. P. B. M. Janssen,
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摘要:
AbstractThe copolymerization of n‐butylmethacrylate with 2‐hydroxypropylmethacrylate was studied in a closely intermeshing counterrotating twin‐screw extruder. The average molecular weight of the product can be increased by increasing the screw rotation rate or the die resistance or by decreasing the throughput or the barrel temperature. The conversion can be improved by decreasing the throughput, increasing the die resistance, and (within limits) increasing the barrel temperature, as well as through post‐initiation. Compared with various classical polymerization processes, this situation requires that particular attention be paid to the occurrence of a gel effect, the existence of a thermodynamic ceiling temperature, and the reactivity ratio of the monome
ISSN:0032-3888
DOI:10.1002/pen.760350705
出版商:Society of Plastics Engineers
年代:1995
数据来源: WILEY
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5. |
Residence time distribution in non‐intermeshing counter‐rotating twin‐screw extruders |
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Polymer Engineering&Science,
Volume 35,
Issue 7,
1995,
Page 598-603
L. Chen,
G. H. Hu,
J. T. Lindt,
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摘要:
AbstractThis paper deals with the residence time distribution (RTD) in a non‐intermeshing counter rotating twin screw extruder.The RTDs were measured in three vent zones of the extruder sparately, and in the adjacent zones combined, using a soluble dye as the tracer. Assuming that the RTDs in the adjacent zones are independent of each other, the overall RTD was also calculated using a previously developed statistical theory. The theory has also confirmed the consistency of the present measurements.A predictive RTD model for the non‐intermeshing twin screw extruder, based on the flow analysis of the individual screw zones and their statistical superposition, was also developed. The predictions are in good agreement with experim
ISSN:0032-3888
DOI:10.1002/pen.760350706
出版商:Society of Plastics Engineers
年代:1995
数据来源: WILEY
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6. |
Numerical simulation of fiber orientation in injection molding of short‐fiber‐reinforced thermoplastics |
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Polymer Engineering&Science,
Volume 35,
Issue 7,
1995,
Page 604-618
S. T. Chung,
T. H. Kwon,
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摘要:
AbstractThe present study develops a numerical simulation program to predict the transient behavior of fiber orientations together with a mold filling simulation for short‐fiber‐reinforced thermoplastics in arbitrary three‐dimensional injection mold cavities. The Dinh‐Armstrong model including an additional stress due to the existence of fibers is incorporated into the Hele‐Shaw equation to result in a new pressure equation governing the filling process. The mold filling simulation is performed by solving the new pressure equation and energy equation via a finite element/finite difference method as well as evolution equations for the second‐order orientation tensor via the fourth‐order Runge‐Kutta method. The fiber orientation tensor is determined at every layer of each element across the thickness of molded parts with appropriate tensor transformations for arbitrary three‐dimensi
ISSN:0032-3888
DOI:10.1002/pen.760350707
出版商:Society of Plastics Engineers
年代:1995
数据来源: WILEY
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7. |
The flow‐induced phase morphology of fluoroelastomer and polycarbonate blends during extrusion |
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Polymer Engineering&Science,
Volume 35,
Issue 7,
1995,
Page 619-636
Hsien Yin Tsai,
Kyonsuku Min,
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摘要:
AbstractThe flow‐induced phase morphological development under different extrusion conditions was studied in terms of the rheological property and interfacial tension of various elastomers and thermoplstics. The interfacial tension for elastomers and thermoplastics was investigated by using a breaking thread method (1‐4). We found that the method is suitable for measuring interfacial tension without degradation. The droplet‐fibrillation transition phenomenon was observed in various extrudates of fluoroelastomer/polycarbonate blends. The criteria for the flow‐induced morphology, in particular the droplet‐fibrillation transition, are critically discussed in t
ISSN:0032-3888
DOI:10.1002/pen.760350708
出版商:Society of Plastics Engineers
年代:1995
数据来源: WILEY
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8. |
Masthead |
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Polymer Engineering&Science,
Volume 35,
Issue 7,
1995,
Page -
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PDF (81KB)
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ISSN:0032-3888
DOI:10.1002/pen.760350701
出版商:Society of Plastics Engineers
年代:1995
数据来源: WILEY
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