- Heat Transfer - Section 1
- Heat Transfer - Section 2
- Heat Transfer - Section 3
- Heat Transfer - Section 4
- Heat Transfer - Section 5
- Heat Transfer - Section 6
- Heat Transfer - Section 7
- Heat Transfer - Section 8
- Heat Transfer - Section 9
- Heat Transfer - Section 10
- Heat Transfer - Section 11


Heat Transfer - Engineering
Q1: 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 isA 1200W/m2.K
B 894W/m2.K
C 333W/m2.K
D 287 W/m2.K
ANS:C - 333W/m2.K To find the overall heat transfer coefficient (𝑈U) after one year of operation, we can use the concept of overall heat transfer resistance: 1𝑈=1𝑈0+1ℎ𝑑0U1=U01+hd01 Where:
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