Chemical Engineering - Process Equipment and Plant Design - Discussion

Discussion Forum : Process Equipment and Plant Design - Section 3 (Q.No. 3)
3.
Ratio of tube length to shell diameter for a shell and tube heat exchanger is
8 : 1 to 12 : 1 for both liquid-liquid and gas-gas heat exchangers.
4 : 1 to 8 : 1 for liquid-liquid exchanger.
< 4 : 1 for gas-gas exchangers.
both(b) & (c).
Answer: Option
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