To determine the interface temperature of the rods at thermal equilibrium, the principle of thermal conduction is applied, requiring equal heat flow rates through both rods A and B.
Heat flow rate \((Q/t)\) for cylindrical rods is calculated as:
\[ \frac{Q}{t} = \frac{KA(T_{\text{hot}} - T_{\text{cold}})}{L} \]
At equilibrium, \( \frac{Q_A}{t} = \frac{Q_B}{t} \), leading to:
\[ \frac{K_A \pi r_A^2 (400 - T)}{L_A} = \frac{K_B \pi r_B^2 (T - 200)}{L_B} \]
Upon canceling \( \pi \) and substituting the given ratios:
\[ \frac{(1/2) \cdot (2r_B)^2 \cdot (400 - T)}{(1/2)L_B} = \frac{K_B \cdot r_B^2 \cdot (T - 200)}{L_B} \]
Simplifying the equation yields:
\[ (1/2) \cdot 4 \cdot (400 - T) = T - 200 \]
This simplifies further to:
\[ 2 \cdot (400 - T) = T - 200 \]
Expanding and solving for \( T \):
\[ 800 - 2T = T - 200 \]
\[ 1000 = 3T \]
\[ T = \frac{1000}{3} \]
The interface temperature \( T = 333.33 \, \text{K} \). As this value falls outside the expected range (360, 360), a review of the problem statement and input data is recommended to identify potential inconsistencies.
Identify the evaporator 