A MODEL FOR THE MASS TRANSFER COEFFICIENT IN ROTATING PACKED BED

2000 ◽  
Vol 178 (1) ◽  
pp. 249-256 ◽  
Author(s):  
DING XINLIN ◽  
HU XIAOYONG ◽  
DING YIGANG ◽  
WU YUANXIN ◽  
LI DINGHUO
Keyword(s):  
Mass Transfer ◽  
Transfer Coefficient ◽  
Mass Transfer Coefficient ◽  
Packed Bed ◽  
Rotating Packed Bed

Influence of Gas-Liquid Distribution Inducer on Mass Transfer Coefficient in Rotating Packed Bed

2014 ◽  
Vol 908 ◽  
pp. 277-281
Author(s):  
Fei Wu ◽  
Jie Wu ◽  
Mei Jin ◽  
Fang Wang ◽  
Ping Lu
Keyword(s):  
Mass Transfer ◽  
Transfer Coefficient ◽  
Mass Transfer Coefficient ◽  
Flow Rate ◽  
Rotor Blade ◽  
Gas Flow ◽  
Packed Bed ◽  
Contact Length ◽  
Liquid Distribution ◽  
Rotating Packed Bed

Based on acetone-H2O system, the influence of the gas-liquid distribution inducer on the mass transfer coefficient in the rotating packed bed with the stainless steel packing was investigated. Furthermore, the absorption performance was also obtained under the experimental condition of the rotational speed of 630 rpm, the gas flow rate of 2 m3/h and the liquid flow rate of 100 L/h in the rotating packed bed with different types and different installation ways of the distribution inducer. The experimental results showed that the volumetric mass transfer coefficient Kyα per unit contact length of gas-liquid was increased by 8.6% for the forward-curved fixed blade, by 19.8% for the backward-curved rotor blade and by 33.2% with the combination of the straight radial rotor blade and the backward-curved fixed blade, respectively. Furthermore, when the gas flow rate was 2.5 m3/h, Kyα per unit contact length of gas-liquid was increased by 2.9% for the forward-curved fixed blade, by 25.3% for the backward-curved rotor blade, by 42.7% for the combination of the straight radial rotor blade and the backward-curved fixed blade, respectively. The results indicated that the distribution inducer play an important role on the improvement of the mass transfer coefficient in acetone-H2O system.

Absorption Performance of Rotating Packed Bed with Gas-Liquid Distribution Inducer

2014 ◽  
Vol 1010-1012 ◽  
pp. 913-916
Author(s):  
Mei Jin ◽  
Li Zhan ◽  
Li Yan Zhou ◽  
Guo Xian Yu ◽  
Ping Lu
Keyword(s):  
Mass Transfer ◽  
Transfer Coefficient ◽  
Mass Transfer Coefficient ◽  
Gas Phase ◽  
Packed Bed ◽  
Volumetric Mass Transfer Coefficient ◽  
Liquid Distribution ◽  
Rotating Packed Bed ◽  
Different Types ◽  
Absorption Performance

Based on CO2-NaOH system, the absorption performances and the mass transfer of the rotating packed bed with the three different types of the gas-liquid distribution inducer were investigated. The experimental results showed that the structure of the gas-liquid distribution inducer have an important effect on the volumetric mass transfer coefficient and the absorptivity of CO2. Due to the enhancement of the countercurrent contact between the liquid phase and the gas phase from the installation of the distribution inducer, an increasement of the volumetric mass transfer coefficient and a higher absorptivity of CO2 could be obtained than those of the experiment in PRB without any inducers. Among the distribution inducers, the combination of the liquid distribution inducer of Type-B and the gas distribution inducer of Type-A could give a better volumetric mass transfer coefficient and a higher absorptivity of CO2, which were 27.84×10-3 s-1 and 80.00%, respectively.

scholarly journals LIQUID-PHASE MASS TRANSFER COEFFICIENT AND GAS HOLDUP IN A PACKED-BED COCURRENT UP-FLOW COLUMN

1976 ◽  
Vol 9 (1) ◽  
pp. 29-34 ◽  
Author(s):  
SATOSHI OHSHIMA ◽  
TOSHIICHI TAKEMATSU ◽  
YASUNORI KURIKI ◽  
KAZUO SHIMADA ◽  
MORIO SUZUKI ◽  
...  
Keyword(s):  
Mass Transfer ◽  
Liquid Phase ◽  
Transfer Coefficient ◽  
Mass Transfer Coefficient ◽  
Packed Bed ◽  
Gas Holdup ◽  
Liquid Phase Mass Transfer

Mass and Heat Transfer in Multi-Pulverizing RPB

2011 ◽  
Vol 396-398 ◽  
pp. 311-314
Author(s):  
Hai Hui Chen ◽  
Xu Guang Min
Keyword(s):  
Heat Transfer ◽  
Mass Transfer ◽  
Transfer Coefficient ◽  
Packed Bed ◽  
Experimental Models ◽  
Transfer Model ◽  
Axial Fan ◽  
Transfer Property ◽  
Rotating Packed Bed ◽  
Mass And Heat Transfer

New typical cross-flow Rotating Packed Bed (RPB) called multi-pulverizing RPB was manufactured. Mass and heat transfer property of the new type PRB were studied by two experimental models. In the mass transfer model, the axial fan pumping gas press is only 100 Pa, mass transfer coefficient is similar to countercurrent RPB. In the heat transfer experiment, the axial fan pumping gas press is only 120 Pa; volumetric heat transfer coefficient is from 75 kW.m-3. K-1 to 100 kW.m-3. K-1.

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