Predicting Gas Transport Coefficients of Alternative Refrigerant Mixtures

2006 ◽  
Vol 45 (26) ◽  
pp. 9211-9223 ◽  
Author(s):  
J. Moghadasi ◽  
D. Mohammad-Aghaie ◽  
M. M. Papari
2016 ◽  
Vol 61 (4) ◽  
pp. 1825-1832 ◽  
Author(s):  
A. Rybak ◽  
Au. Rybak ◽  
W. Kaszuwara

Abstract In this paper magnetic organic-inorganic hybrid membranes based on EC, PPO polymer matrices and various magnetic powder microparticles were synthesized and studied. Constant pressure permeation technique and the Time Lag method were used to obtain the gas transport coefficients. The mechanical, rheological and magnetic parameters of magnetic hybrid membranes were examined. It was found that their separation and gas transport properties (D, P, S and α) were improved with the decrease in powder particle size and the increase of membrane’s remanence, saturation magnetization and magnetic particle filling. The increase of the magnetic powder addition and a decrease of its granulation improved also mechanical and rheological parameters of the tested membranes. This improvement also had a positive effect on their gas separation properties and their potential usage in the future.


1996 ◽  
Vol 41 (3) ◽  
pp. 116-128 ◽  
Author(s):  
J. H. Song ◽  
J. R. G. Evans ◽  
M. J. Edirisinghe ◽  
E. H. Twizell

2015 ◽  
Vol 48 (8) ◽  
pp. 2585-2592 ◽  
Author(s):  
Carolina García ◽  
Ángel E. Lozano ◽  
José G. de la Campa ◽  
Yakov Vygoskii ◽  
Mihail Zolotukhin ◽  
...  

2017 ◽  
Vol 21 (6 Part B) ◽  
pp. 2851-2858
Author(s):  
Bo Song ◽  
Xiaopo Wang ◽  
Zhigang Liu

In this work, the inversion scheme was used to determine the potential energy surfaces of five polar refrigerant mixtures. The systems studied here are R123-R134a, R123-R142b, R123-R152a, R142b-R134a, and R142b-R152a. The low density transport coefficients of the refrigerant mixtures were calculated from the new invert potentials by the classical kinetic theory. The viscosity coefficient, binary diffusion coefficient, and thermal diffusion factor were computed for the temperature range from 313.15-973.15 K. The agreement with the NIST viscosity data demonstrates that the present calculated values are accurate enough to supplement experimental data over an extended temperature range. Correlations of the transport properties were also provided for the refrigerant mixtures at equimolar ratios.


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