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$?

A. 1200W/m².K
B. 894W/m².K
C. 333W/m².K
D. 287 W/m².K
Answer» D. 287 W/m¬¨‚â§.K


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