Find the area required for a shell-and-tube heat exchanger

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Reference no: EM131234847

A small steam condenser is to be designed to condense 0.8 kg/min steam at 80 kN/m² with cooling water at 290 K. If the exit temperature of the water is not to exceed 320 K, calculate the area required for a shell-and-tube heat exchanger with the steam making one shell pass and the water making two tube passes. The overall heat-transfer coefficient is 3000 W/m² ·K.

Reference no: EM131234847

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