Study of volumetric liquid-phase mass transfer coefficient in high solid-holdup three-phase bubble column slurry reactor and the comparison of its using two types of gas distributor

Gao Xiao Hua Xue Gong Cheng Xue Bao/Journal of Chemical Engineering of Chinese Universities

Volumn 17, Issue 4, 2003, Pages 383-388

  Han, Hui ^a   Fang, Ding Ye ^a   Zhu, Bing Chen ^a  

^a UNIVERSITY OF SHANGHAI FOR SCIENCE AND TECHNOLOGY   (China)

Author keywords

Bubble column slurry reactor; Gas distributor; Gas liquid mass transfer; Oxygen meter; Solid holdup

Indexed keywords

BUBBLE COLUMNS; CHEMICAL REACTORS; GASES; LIQUIDS; MASS TRANSFER; OXYGEN; SOLIDS;

BUBBLE COLUMN SLURRY REACTOR; GAS DISTRIBUTOR; SOLID HOLDUP; THREE PHASE;

MULTIPHASE FLOW;

EID: 0346147131     PISSN: 10039015     EISSN: None     Source Type: Journal    
DOI: None     Document Type: Article

References (7)

1. WANG Cui-wen, ZHU Bing-chen, DING Bai-quan, FANG Ding-ye. Methanol synthesis in bubble column slurry reactor (I) mathematical model and verification [J]. J Chem Ind and Eng, 2001, 52(11): 1006-1011.
2. YAN Yong-jie, REN Zheng-wei. Gas-liquid mass transfer coefficient in draft tube three phase fluidized bed [J]. J Chem Eng of Chinese Univ, 1996, 10(1): 52-58.
3. Koide K, Hiroyuki SATO, Shinji Iwamoto. Gas holdup and volumetric liquid-phase mass transfer coefficient in bubble column with draught tube and with gas dispersion into annulus [J]. J Chem Eng Japan, 1983, 16(5): 407-413.
4. Koide K, Takazawa A, Komara M, Matsunaga H. Gas holdup and volumetric liquid-phase mass transfer coefficient in solid-suspended bubble column [J]. J Chem Eng Japan, 1984, 17(5): 459-466.
5. Akita K, Yoshida F. Gas holdup and volumetric mass transfer coefficient in bubble ceolumns [J]. Ind Eng Chem Process Des Develop, 1973, 12(1): 76-80.
6. SHI Jun, WANG Jia-ding, YU Guo-cong, CHEN Min-heng. Chemical Engineering Handbook [M]. Beijing: Chemical Industry Press, 1996.
7. QIN Hui-fang, WANG Shi-rong, ZHU Bing-chen. Liquid paraffin physical character test [J]. Natural Gas Chemical Industry, 1999, 24(3): 56-58.