CIESC Journal ›› 2010, Vol. 61 ›› Issue (3): 635-641.
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ZHANG Haocui;YUE Jun;CHEN Guangwen;YUAN Quan
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Published:
张好翠;乐军;陈光文;袁权
Abstract:
Gas phase mass transfer in falling film microreactors (FFMRs) with the absorption of CO2 into aqueous solutions of NaOH was investigated. The overall gas-phase mass transfer coefficient increases with NaOH concentration, but decreases as the concentration of CO2 increases. There exists an entrance effect, hindering the mass transfer, which is caused by the dead volume for gas-phase flow in the gas chamber in FFMRs. The entrance effect has a larger impact in a shorter FFMR owing to the relatively large dead volume with respect to that of gas chamber. A decrease in the depth of gas chamber facilitates the mass transfer process. Therefore, the gas-phase entrance or geometry of the gas chamber should be designed appropriately to reduce the entrance effect and improve the mass transfer.
Key words: 降膜吸收, 气相传质系数, 微反应器, 微通道
降膜吸收,
关键词: 降膜吸收, 气相传质系数, 微反应器, 微通道
ZHANG Haocui, YUE Jun, CHEN Guangwen, YUAN Quan. Mass transfer behaviors in process of chemical absorption of CO2 in falling film microreactors[J]. CIESC Journal, 2010, 61(3): 635-641.
张好翠, 乐军, 陈光文, 袁权. 降膜微反应器中CO2化学吸收过程传质行为 [J]. 化工学报, 2010, 61(3): 635-641.
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https://hgxb.cip.com.cn/EN/Y2010/V61/I3/635
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