ENZYME MASS TRANSFER COEFFICIENT IN AQUEOUS TWO PHASE SYSTEMS: SPRAY EXTRACTION COLUMNS

1993 ◽  
Vol 122 (1) ◽  
pp. 151-169 ◽  
Author(s):  
P.A. PA WAR ◽  
K. ROSTAMI JAFARABAD ◽  
S.B. SAWANT ◽  
J.B. JOSHI
2011 ◽  
Vol 347-353 ◽  
pp. 1797-1800
Author(s):  
Yan Chao Li ◽  
Zhi Wu Hao ◽  
Xian Ping Zeng ◽  
Fang Qin Li ◽  
Jian Xing Ren

In this paper, membrane absorption method was introduced. Analyzed and studied flue gases passing in the shell side (hollow fiber membrane) and in the pipe side (membrane lumen) respectively. Total mass transfer coefficient and de CO2 efficiency were calculated. For flue gases passing in the pipe side, total mass transfer coefficient was 1.1191×10-4m/s and de CO2 efficiency was 73.8%; while for flue gases passing in the shell side, total mass transfer coefficient was 3.4701×10-4m/s and de CO2 efficiency was 98.0%. The results showed that the flow of flue gas flowing in the lumen is better than the flow of flue gas flowing out of the hollow fiber membrane from the point of views of removal rate and mass transfer. To build de CO2 experimental devices, flow of flue gas flowing in the pipe side was proposed.


1984 ◽  
Vol 49 (12) ◽  
pp. 2756-2762
Author(s):  
Jan Červenka ◽  
Václav Kolář

A theoretically derived relationship has been applied for the gas-side mass transfer coefficient to experimental values of kG. The experimental data have been obtained under the two-phase flow of gas and liquid in a plane vertical packing manufactured of the expanded metal sheet. This packing exhibits a significant dependence of the extent of interfacial area, and hence the geometry of the channel available for gas flow, on the density of irrigation.


Author(s):  
Takayuki YAMAGATA ◽  
Hidefumi TSURUTA ◽  
Yuhei NISHII ◽  
Nobuyuki Fujisawa ◽  
Fumio INADA

2004 ◽  
Vol 99 (3) ◽  
pp. 273-277 ◽  
Author(s):  
Yanhui Yuan ◽  
Minghan Han ◽  
Lunwei Wang ◽  
Dezheng Wang ◽  
Yong Jin

Sign in / Sign up

Export Citation Format

Share Document