The heat duty equation for a heat exchanger is: \[ Q = U \cdot A \cdot \Delta T_m, \] where:
- \( Q \) is the heat duty (given as \( 15 \times 10^5 \) BTU/hr),
- \( U \) is the overall heat transfer coefficient (100 BTU/hr-ft²),
- \( A \) is the surface area of the tubes,
- \( \Delta T_m \) is the log mean temperature difference.
The log mean temperature difference \( \Delta T_m \) is calculated as: \[ \Delta T_m = \frac{(T_1 - T_2) - (T_3 - T_4)}{\ln \left( \frac{T_1 - T_2}{T_3 - T_4} \right)}, \] where:
- \( {T_1 = 175 \, }^\circ \text{F} \) (hot fluid inlet),
- \( {T_2 = 100 \, }^\circ \text{F} \) (hot fluid outlet),
- \( {T_3 = 75 \, }^\circ \text{F} \) (cold fluid inlet),
- \( {T_4 = 85 \, }^\circ \text{F} \) (cold fluid outlet).
Substitute the values: \[ \Delta T_m = \frac{(175 - 100) - (75 - 85)}{\ln \left( \frac{175 - 100}{75 - 85} \right)} = \frac{75 + 10}{\ln \left( \frac{75}{-10} \right)} {\approx 70.6 \,}^\circ \text{F}. \] Now, calculate the heat transfer surface area required: \[ Q = U \cdot A \cdot \Delta T_m \Rightarrow A = \frac{Q}{U \cdot \Delta T_m} = \frac{15 \times 10^5}{100 \cdot 70.6} = 212.6 \, \text{ft}^2. \] The surface area per tube is given as 0.26 ft²/ft, and the tube length is 40 ft. The surface area per tube is: \[ A_{\text{tube}} = 0.26 \times 40 = 10.4 \, \text{ft}^2. \] Finally, the minimum number of tubes required is: \[ \frac{212.6}{10.4} \approx 20.5 \Rightarrow \text{round to nearest integer: } 21 \, \text{tubes}. \] Thus, the minimum number of tubes required is 21.