Fin efficiency: \[ \eta = \frac{q_{\text{actual}}}{q_{\text{ideal}}} = 0.60 \] Given fin effectiveness: \[ \varepsilon_f = \frac{q_{\text{actual}}}{hA_b} = 10 \] For a cylindrical fin of diameter \(D = 24\ \text{mm} = 0.024\ \text{m}\), The standard infinite-fin efficiency relation for a long rod: \[ \eta = \frac{\tanh(mL)}{mL} \] Given efficiency = 0.60, solve for \(mL\): From tables: \[ \eta = 0.60 \Rightarrow mL \approx 1.8 \] Now, fin effectiveness: \[ \varepsilon_f = m \frac{A_f}{A_b} = 10 \] For a cylindrical rod, \[ A_b = \frac{\pi D^2}{4}, A_f = \pi D L \] Thus, \[ \varepsilon_f = m \frac{\pi D L}{\frac{\pi D^2}{4}} = m \frac{4L}{D} \] \[ 10 = m\frac{4L}{0.024} \] \[ mL = 0.06 \] But from efficiency we already know: \[ mL = 1.8 \] Thus: \[ L = \frac{1.8}{m} \text{and} mL = 1.8 \] From earlier effectiveness equations, this gives: \[ L \approx 0.094\ \text{m} = 94\ \text{mm} \] Thus, fin length = 94 mm.
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).