Step 1: Use Carnot's relation: \[ \frac{Q_C}{Q_H} = \frac{T_C}{T_H} \] Where: \( Q_C = 400\,\text{J} \), \( Q_H = 600\,\text{J} \), \( T_H = 127^\circ\text{C} = 127 + 273 = 400\,\text{K} \)
Step 2: Plug values into the equation: \[ \frac{400}{600} = \frac{T_C}{400} \Rightarrow \frac{2}{3} = \frac{T_C}{400} \Rightarrow T_C = \frac{2}{3} \times 400 = 266.7\,\text{K} \]
A hot plate is placed in contact with a cold plate of a different thermal conductivity as shown in the figure. The initial temperature (at time $t = 0$) of the hot plate and cold plate are $T_h$ and $T_c$, respectively. Assume perfect contact between the plates. Which one of the following is an appropriate boundary condition at the surface $S$ for solving the unsteady state, one-dimensional heat conduction equations for the hot plate and cold plate for $t>0$?

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).
The internal energy of air in $ 4 \, \text{m} \times 4 \, \text{m} \times 3 \, \text{m} $ sized room at 1 atmospheric pressure will be $ \times 10^6 \, \text{J} $. (Consider air as a diatomic molecule)