Effect of impeller geometry on gas-liquid mass transfer coefficients in filamentous suspensions
- Univ. of Louisville, KY (United States)
Volumetric gas-liquid mass transfer coefficients were measured in suspensions of cellulose fibers with concentrations ranging from 0 to 20 g/L. The mass transfer coefficients were measured using the dynamic method. Results are presented for three different combinations of impellers at a variety of gassing rates and agitation speeds. Rheological properties of the cellulose fibers were also measured using the impeller viscometer method. Tests were conducted in a 20 L stirred-tank fermentor and in 65 L tank with a height to diameter ratio of 3:1. Power consumption was measured in both vessels. At low agitation rates, two Rushton turbines gave 20% better performance than the Rushton and hydrofoil combination and 40% better performance than the Rushton and propeller combination for oxygen transfer. At higher agitation rates, the Rushton and hydrofoil combination gave 14 and 25% better performance for oxygen transfer than two Rushton turbines and the Rushton and hydrofoil combination, respectively. 8 refs., 11 figs., 1 tab.
- Sponsoring Organization:
- USDOE
- OSTI ID:
- 576243
- Report Number(s):
- CONF-960539--
- Journal Information:
- Applied Biochemistry and Biotechnology, Journal Name: Applied Biochemistry and Biotechnology Vol. 63-65; ISSN ABIBDL; ISSN 0273-2289
- Country of Publication:
- United States
- Language:
- English
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