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Liquid-solid mass transfer in a three-phase stationary catalytic basket reactor
被引:8
|作者:
Mitrovic, M
Pitault, I
Forissier, M
Simoens, S
Ronze, D
机构:
[1] CNRS, CPE, Lab Genie Procedes Catalyt, F-69616 Villeurbanne, France
[2] CNRS, ECL, Lab Mecan Fluides & Acoust, F-69134 Ecully, France
[3] Univ Lyon 1, IUT A, Dept Genie Chim Genie Procedes, F-69622 Villeurbanne, France
关键词:
Robinson-Mahoney reactor;
mass transfer;
liquid-solid transfer;
catalytic basket;
particle image velocimetry (PIV);
D O I:
10.1002/aic.10436
中图分类号:
TQ [化学工业];
学科分类号:
0817 ;
摘要:
Measurements of the liquid-solid mass transfer coefficient k(S) were performed in a three-phase multiple impeller and stationary catalytic basket reactor, called a Robinson-Mahoney reactor. Local coefficients were determined using naphtol particle dissolution in water and n-heptane with or without gas flow. Experiments have shown that local coefficients k(S) (loc) depend on the particle position in the basket, agitation speed, and liquid properties. A correlation linking k(S) to liquid velocity was established in a reactor simulating hydrodynamics in a piece of catalytic basket. Liquid velocity values were validated using a particle image velocimetry technique in a Robinson-Mahoney reactor, using water. (c) 2005 American Institute of Chemical Engineers.
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页码:1747 / 1757
页数:11
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