Consider a 1-2, shell-and-tube heat exchanger:

The cold stream has a heat-capacity flow rate \(C=40,000 \mathrm{Btu} / \mathrm{hr}-{ }^{\circ} \mathrm{F}\). Its heat-transfer coefficients are \(h_{i}=h_{0}=50 \mathrm{Btu} /\left(\mathrm{ft}-\mathrm{hr}-{ }^{\circ} \mathrm{F}\right)\). For a stainless steel heat exchanger with a floating head built to withstand pressures up to 100 barg, estimate the bare-module cost. Use a CE cost index \(=600\).

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16.11 Consider a 1-2, shell-and-tube heat exchanger: 80F 170F 90F 140F