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    Please use this identifier to cite or link to this item: https://ir.fy.edu.tw:8080/ir/handle/987654321/10277

    Title: Characteristics of Rotating Packed Bed
    Authors: Liu,Hwai-Shen;Lin,Chia-Chang;Wu,Sheng-Chi;Hsu, Hsien-Wen
    Contributors: 輔英科技大學 生物科技系
    Date: 1996
    Issue Date: 2010-11-19 14:09:19 (UTC+8)
    Abstract: The mass transfer (stripping of ethanol) and pressure drop (water−air) of a rotating packed bed were investigated under 13−273 equiv of gravitational force with two packings. The results indicated that the mass-transfer coefficient (KGa) was enhanced due to the centrifugal force as compared to a conventional packed bed. An empirical correlation was also proposed, suggesting that the KGa value depends on the GrG number to the power of 0.25. As to pressure drop, the gas rate seems to be a more important factor than the liquid rate because of less liquid holdup under centrifugal force. A semiempirical equation was also developed to correlate the pressure drop data with good agreement.
    Relation: Industrial & Engineering Chemistry Research 35(10), pp 3590–3596
    Appears in Collections:[生物科技系] 期刊論文

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