Modeling and experimental studies of mass transfer in the cavity zone of a rotating packed bed

2017 ◽  
Vol 170 ◽  
pp. 355-364 ◽  
Author(s):  
Le Sang ◽  
Yong Luo ◽  
Guang-Wen Chu ◽  
Ya-Zhao Liu ◽  
Xing-Zheng Liu ◽  
...  
Keyword(s):  
Mass Transfer ◽  
Experimental Studies ◽  
Packed Bed ◽  
Rotating Packed Bed

Mass transfer in a rotating packed bed reactor with a mesh-pin rotor: Modeling and experimental studies

2019 ◽  
Vol 369 ◽  
pp. 600-610 ◽  
Author(s):  
Wei Liu ◽  
Guang-Wen Chu ◽  
Yong Luo ◽  
Ya-Zhao Liu ◽  
Fan-Yong Meng ◽  
...  
Keyword(s):  
Mass Transfer ◽  
Experimental Studies ◽  
Packed Bed ◽  
Packed Bed Reactor ◽  
Rotating Packed Bed

Multilevel cross flow rotating packed bed to enhance gas film control mass transfer process

2021 ◽  
Vol 161 ◽  
pp. 108321
Author(s):  
Qing-Qing Duan ◽  
Zhi-Guo Yuan ◽  
You-Zhi Liu ◽  
Shan-Shan Duan ◽  
Xi-Fan Duan
Keyword(s):  
Mass Transfer ◽  
Transfer Process ◽  
Cross Flow ◽  
Mass Transfer Process ◽  
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.

scholarly journals Mass Transfer in a Rotating Packed Bed with Viscous Newtonian and Non-Newtonian Fluids

2005 ◽  
Vol 44 (4) ◽  
pp. 1043-1051 ◽  
Author(s):  
Yu-Shao Chen ◽  
Chia-Chang Lin ◽  
Hwai-Shen Liu
Keyword(s):  
Mass Transfer ◽  
Packed Bed ◽  
Newtonian Fluids ◽  
Rotating Packed Bed

Polytetrafluoroethylene Wire Mesh Packing in a Rotating Packed Bed: Mass-Transfer Studies

2016 ◽  
Vol 55 (44) ◽  
pp. 11606-11613 ◽  
Author(s):  
Qiu-Yun Chen ◽  
Guang-Wen Chu ◽  
Yong Luo ◽  
Le Sang ◽  
Li−Li Zhang ◽  
...  
Keyword(s):  
Mass Transfer ◽  
Packed Bed ◽  
Wire Mesh ◽  
Rotating Packed Bed ◽  
Mass Transfer Studies

Modeling and Experimental Studies on Ozone Absorption into Phenolic Solution in a Rotating Packed Bed

2019 ◽  
Vol 58 (17) ◽  
pp. 7052-7062
Author(s):  
Dan Wang ◽  
Taoran Liu ◽  
Lei Ma ◽  
Feng Wang ◽  
Lei Shao
Keyword(s):  
Experimental Studies ◽  
Packed Bed ◽  
Ozone Absorption ◽  
Rotating Packed Bed
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