Variable-gas-density fluidized bed reactor model for catalytic processes

Author:

A. Abba I,R. Grace J,T. Bi H

Publisher

Elsevier BV

Subject

Applied Mathematics,Industrial and Manufacturing Engineering,General Chemical Engineering,General Chemistry

Reference16 articles.

1. Abba, I. A. (2001). A generalized fluidized bed reactor model across the flow regimes. Ph.D. thesis, University of British Columbia, Vancouver, Canada.

2. Abba, I. A., Grace, J. R., Bi, H. T., & Thompson, M. L. (2002). Spanning the flow regimes: A generic fluidized bed reactor model. AIChE Journal, in press.

3. Adris, A. M., Lim, C. J., & Grace, J. R. (1993). The effect of gas volume increase due to reaction on bed expansion, bubbling and overall conversion in a fluidized bed reactor. A.I.Ch.E. Annual Meeting, St. Louis, November.

4. Adris, A.M., Lim, C.J., & Grace, J.R. (1997). The fluidized bed membrane reactor for steam methane reforming: Model verification and parametric study. Chemical Engineering Science, 52 1609–1622.

5. A state-of-the-art review of gas–solid turbulent fluidization;Bi;Chemical Engineering Science,2000

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