Effect of interfacial transport on the diffusivity of highly filled polymers

2021 ◽  
Vol 42 ◽  
pp. 100405
Author(s):  
M. van Soestbergen ◽  
A. Herrmann ◽  
S.J.F. Erich ◽  
O.C.G. Adan
1991 ◽  
Author(s):  
Zheng-You Ding ◽  
Shenmin Ma ◽  
Dennis Kriz ◽  
J. J. Aklonis ◽  
R. Salovey

1986 ◽  
Vol 51 (6) ◽  
pp. 1222-1239 ◽  
Author(s):  
Pavel Moravec ◽  
Vladimír Staněk

Expression have been derived in the paper for all four possible transfer functions between the inlet and the outlet gas and liquid steams under the counter-current absorption of a poorly soluble gas in a packed bed column. The transfer functions have been derived for the axially dispersed model with stagnant zone in the liquid phase and the axially dispersed model for the gas phase with interfacial transport of a gaseous component (PDE - AD). calculations with practical values of parameters suggest that only two of these transfer functions are applicable for experimental data evaluation.


1982 ◽  
Vol 47 (10) ◽  
pp. 2639-2653 ◽  
Author(s):  
Pavel Moravec ◽  
Vladimír Staněk

Expressions have been derived for four possible transfer functions of a model of physical absorption of a poorly soluble gas in a packed bed column. The model has been based on axially dispersed flow of gas, plug flow of liquid through stagnant and dynamic regions and interfacial transport of the absorbed component. The obtained transfer functions have been transformed into the frequency domain and their amplitude ratios and phase lags have been evaluated using the complex arithmetic feature of the EC-1033 computer. Two of the derived transfer functions have been found directly applicable for processing of experimental data. Of the remaining two one is useable with the limitations to absorption on a shallow layer of packing, the other is entirely worthless for the case of poorly soluble gases.


Langmuir ◽  
2015 ◽  
Vol 31 (7) ◽  
pp. 2167-2179 ◽  
Author(s):  
Shaina Kelly ◽  
Matthew T. Balhoff ◽  
Carlos Torres-Verdín

1988 ◽  
Vol 24 (2) ◽  
pp. 223-230
Author(s):  
M. I. Gandel'sman ◽  
R. V. Matveenko ◽  
V. P. Budtov
Keyword(s):  

Author(s):  
Lisa Mondy ◽  
Rekha Rao ◽  
Eric Lindgren ◽  
Amy Sun ◽  
Robert Lagasse ◽  
...  

Manufacturing applications for filled polymers include encapsulation of microelectronics and injection molding of composite parts. Predictive tools for simulating these manufacturing processes require knowledge of time- and temperature-dependent rheology of the polymer as well as information about local particle concentration. The overall system rheology is highly dependent on the particle concentration. The local particle concentration can change due to gravity, convection and shear-induced migration. For the epoxy systems of interest, an extent of reaction can be used to track the degree of cure. We couple the curing model with a diffusive flux suspension model [Zhang and Acrivos 1994] to determine the particle migration. This results in a generalized Newtonian model that has viscosity as a function of temperature, cure and concentration. Using this model, we examine settling of the particulate phase in both flowing and quiescent curing systems. We focus on settling in molds and flow in wide-gap counter-rotating cylinders. The heat transfer, including the exothermic polymerization reaction, must be modeled to achieve accurate results. The model is validated with temperature measurements and post-test microscopy data. Particle concentration is determined with x-ray microfocus visualization or confocal microscopy. Agreement between the simulations and experimental results is fair.


2010 ◽  
Vol 14 (1) ◽  
pp. 21-33 ◽  
Author(s):  
John C. Duda ◽  
Patrick E. Hopkins ◽  
Justin L. Smoyer ◽  
Matthew L. Bauer ◽  
Timothy S. English ◽  
...  

1975 ◽  
Vol 9 (1) ◽  
pp. 76-81 ◽  
Author(s):  
V. P. Stavrov ◽  
A. P. Velichko

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