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Information Journal Paper

Title

THE STUDY OF THE EFFECT OF BED HEIGHT ON BUBBLE DIAMETER AND MASS TRANSFER AREA IN A FLUIDIZED BED REACTOR

Pages

  0-0

Abstract

 Design, modeling and simulation of fluidized bed risers and reactors depend strongly on the knowledge, operational and hydrodynamic characteristics. In this study effort has been made to describe fluidization phenomenon and its application in fluidized beds is briefly explained. The bubble FLUIDIZED BED REACTORs will be introduced and the computerized calculation needed for simulating of a fluidized bed riser with 0.3m diameter and 5m height will be given. The effect of bed height on the bubble diameter and MASS TRANSFER AREA is calculated and the results are discussed. Operational conditions of the bed, type and characteristics of the catalyst, has been selected so as to suit the production of Maleic Anhydride from the n-Butane oxidation.

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    APA: Copy

    GHORBANPOUR, A.A., & GHANNADI, M.. (2003). THE STUDY OF THE EFFECT OF BED HEIGHT ON BUBBLE DIAMETER AND MASS TRANSFER AREA IN A FLUIDIZED BED REACTOR. JOURNAL OF NUCLEAR SCIENCE AND TECHNOLOGY, -(28), 0-0. SID. https://sid.ir/paper/371301/en

    Vancouver: Copy

    GHORBANPOUR A.A., GHANNADI M.. THE STUDY OF THE EFFECT OF BED HEIGHT ON BUBBLE DIAMETER AND MASS TRANSFER AREA IN A FLUIDIZED BED REACTOR. JOURNAL OF NUCLEAR SCIENCE AND TECHNOLOGY[Internet]. 2003;-(28):0-0. Available from: https://sid.ir/paper/371301/en

    IEEE: Copy

    A.A. GHORBANPOUR, and M. GHANNADI, “THE STUDY OF THE EFFECT OF BED HEIGHT ON BUBBLE DIAMETER AND MASS TRANSFER AREA IN A FLUIDIZED BED REACTOR,” JOURNAL OF NUCLEAR SCIENCE AND TECHNOLOGY, vol. -, no. 28, pp. 0–0, 2003, [Online]. Available: https://sid.ir/paper/371301/en

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