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Title: Comparative study of gas-liquid mass transfer coefficients in stirred autoclaves, tubing bomb microreactors, and bubble columns

Journal Article · · Ind. Eng. Chem. Process Des. Dev.; (United States)
DOI:https://doi.org/10.1021/i200024a010· OSTI ID:6429630

The relative gas-liquid contacting coefficients were examined for three reactor types commonly used for direct coal liquefaction. These reactors were the tubing bomb microreactor (TBMR), the magnetically driven batch autoclave with gas-inducing impeller, and the bubble column. The same chemical system, sulfite oxidation in the presence of cobaltous ion catalyst, was used in comparing the performance of the various reactors. Experimental results were obtained in this work for the TBMR and the stirred autoclave, while literature values using sulfite oxidation were utilized for bubble column characterization. The effect of two particle sizes of inert solids on the gas-liquid mass transfer parameters also was determined. The TBMR was the most effective gas-liquid contacting device, with interfacial areas up to 28 cm/sup -1/ being realized. Using literature results obtained with the sulfite oxidation system, the bubble column was found to have comparatively low mass transfer coefficients. Generally, small particles had little effect up to 40 wt % loading, although significant increases were obtained in certain instances in the stirred autoclave reactor.

Research Organization:
Department of Chemical Engineering, Auburn University, Auburn, Alabama
OSTI ID:
6429630
Journal Information:
Ind. Eng. Chem. Process Des. Dev.; (United States), Vol. 23:1
Country of Publication:
United States
Language:
English