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$^{-1}$.
An ideal monoatomic gas is contained inside a cylinder-piston assembly connected to a Hookean spring as shown in the figure. The piston is frictionless and massless. The spring constant is 10 kN/m. At the initial equilibrium state (shown in the figure), the spring is unstretched. The gas is expanded reversibly by adding 362.5 J of heat. At the final equilibrium state, the piston presses against the stoppers. Neglecting the heat loss to the surroundings, the final equilibrium temperature of the gas is __________ K (rounded off to the nearest integer).
The residence-time distribution (RTD) function of a reactor (in min$^{-1}$) is 
The mean residence time of the reactor is __________ min (rounded off to 2 decimal places).}
Ideal nonreacting gases A and B are contained inside a perfectly insulated chamber, separated by a thin partition, as shown in the figure. The partition is removed, and the two gases mix till final equilibrium is reached. The change in total entropy for the process is _________J/K (rounded off to 1 decimal place).
Given: Universal gas constant \( R = 8.314 \) J/(mol K), \( T_A = T_B = 273 \) K, \( P_A = P_B = 1 \) atm, \( V_B = 22.4 \) L, \( V_A = 3V_B \).
The following data is given for a ternary \(ABC\) gas mixture at 12 MPa and 308 K:
\(y_i\): mole fraction of component \(i\) in the gas mixture
\(\hat{\phi}_i\): fugacity coefficient of component \(i\) in the gas mixture at 12 MPa and 308 K
The fugacity of the gas mixture is __________ MPa (rounded off to 3 decimal places).