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Discussion :: Heat Transfer

  1. The overall heat transfer co-efficient for a shell and tube heat exchanger for clean surfaces is U0 = 400 W/m2.K. The fouling factor after one year of operation is found to be hd0 = 2000 W/m2.K. The overall heat transfer co-efficient at this time is

    2. A.
    1200W/m2.K
    B.
    894W/m2.K
    C.
    333W/m2.K
    D.
    287 W/m2.K

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    Workspace

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    Answer : Option C

    Explanation :

    No answer description available for this question.

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