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Question
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
Options:
A .  1200W/m².K
B .  894W/m².K
C .  333W/m².K
D .  287 W/m².K
Answer: Option C

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