Abstract
An experimental rectangular airlift reactor having mesh baffle-plates has been fabricated out of Perspex and compared with conventional airlift and bubble column in terms of gas holdup, volumetric mass transfer coefficient and mixing time. Mesh baffle-plates improved mass transfer and mixing with the mass transfer coefficient of the proposed reactor being up to 12% higher than that in a conventional airlift reactor under the same operating condition. The mixing time of the proposed reactor can be 95% lower than that of the airlift reactor.
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References
Botton, R. and Cosserat, D. (1978). Chem. Eng. J., 16, 107–115.
Gasner, L.L. (1974). Biotechnol. Bioeng., 16, 1179–1195.
Kamp, F., Wase, D.A.J., McMannamey, W.J., Mendoza, O. and Thayanithy, K. (1987). Biotechnol. Bioeng., 30, 179–186.
Pandit, A.B. and Joshi, J.B. (1983). Chem. Eng. Sci., 38, 1189–1215.
Siegel, M.H., Merchuk, J.C. and Schugerl, K. (1986). AICHE J., 32, 1585–1596.
Siegel, M.H. and Merchuk, J.C. (1988). Biotechnol. Bioeng., 32, 1128–1137.
Siegel, M.H. and Merchuk, J.C. (1991). Can. J. Chem. Eng., 69, 465–473.
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Chen, CP., Yang, SJ. & Wu, WT. A novel rectangular airlift reactor with mesh baffle-plates. Biotechnology Techniques 11, 439–441 (1997). https://doi.org/10.1023/A:1018433209929
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DOI: https://doi.org/10.1023/A:1018433209929