Step 1: Calculate the Log Mean Temperature Difference (LMTD)
For a double pipe heat exchanger with steam condensing at constant temperature (100°C):
Temperature differences:
LMTD: $$\Delta T_{lm} = \frac{\Delta T_1 - \Delta T_2}{\ln(\Delta T_1/\Delta T_2)}$$
$$\Delta T_{lm} = \frac{25 - 5}{\ln(25/5)} = \frac{20}{\ln(5)} = \frac{20}{1.609} = 12.43°C$$
Step 2: Calculate Heat Transfer Rate
Using the overall heat transfer equation:
$$Q = U \cdot A \cdot \Delta T_{lm}$$
$$Q = 1000 \times 1 \times 12.43 = 12,430 \text{ W} = 12.43 \text{ kW}$$
Step 3: Calculate Cooling Water Flow Rate
The heat gained by cooling water equals the heat transferred:
$$Q = \dot{m}c \cdot c_p \cdot (T{c,out} - T_{c,in})$$
$$12,430 = \dot{m}_c \times 4200 \times (95 - 75)$$
$$12,430 = \dot{m}_c \times 4200 \times 20$$
$$12,430 = \dot{m}_c \times 84,000$$
$$\dot{m}_c = \frac{12,430}{84,000} = 0.148 \text{ kg/s}$$
For a shell-and-tube heat exchanger, the clean overall heat transfer coefficient is calculated as 250 W m$^{-2}$ K$^{-1}$ for a specific process condition. It is expected that the heat exchanger may be fouled during the operation, and a fouling resistance of 0.001 m$^{2}$ K W$^{-1}$ is prescribed. The dirt overall heat transfer coefficient is \(\underline{\hspace{2cm}}\) W m$^{-2}$ K$^{-1}$.