Absorption of CO with reaction in a biphasic medium (aqueous NaOH-n-hexane): rate enhancement due to dispersed organic phase and phase-transfer catalysis

Chaudhari, R. V. ; Jayasree, P. ; Gupte, S. P. ; Delmas, H. (1997) Absorption of CO with reaction in a biphasic medium (aqueous NaOH-n-hexane): rate enhancement due to dispersed organic phase and phase-transfer catalysis Chemical Engineering Science, 52 (21-22). pp. 4197-4203. ISSN 0009-2509

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Official URL: http://linkinghub.elsevier.com/retrieve/pii/S00092...

Related URL: http://dx.doi.org/10.1016/S0009-2509(97)88934-8

Abstract

The absorption of CO in aqueous NaOH-n-hexane dispersions has been investigated in an agitated reactor over a temperature range of 353-433 K. The rate of absorption was found to be significantly enhanced in the presence of organic droplets and an emulsifier. Also, the addition of a phase-transfer catalyst and a Co complex catalyst resulted in further enhancement of CO absorption rates. The effect of agitation speed, NaOH concentration and CO pressure was studied at 353-433 K for different organic-phase hold-ups and the experimental data were found to be in good agreement with a theoretical model incorporating the variation of the gas-liquid interfacial area with hold-up.

Item Type:Article
Source:Copyright of this article belongs to Elsevier Science.
Keywords:Absorption; Biphasic; Dispersion; Mass Transfer; Emulsifier
ID Code:7881
Deposited On:25 Oct 2010 09:48
Last Modified:30 May 2011 04:20

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