Step 1: Use the first law of thermodynamics.
For the steady-state process, the energy balance equation can be written as:
\[
\dot{m_1} h_1 + \dot{m_2} h_2 - \dot{Q} = (\dot{m_1} + \dot{m_2}) h_3
\]
where \( h_1 \), \( h_2 \), and \( h_3 \) are the specific enthalpies of the air streams at inlet and exit, respectively.
Step 2: Express specific enthalpy in terms of temperature.
For an ideal gas, specific enthalpy is related to temperature by:
\[
h = c_p T
\]
Thus, the energy balance equation becomes:
\[
\dot{m_1} c_p T_1 + \dot{m_2} c_p T_2 - \dot{Q} = (\dot{m_1} + \dot{m_2}) c_p T_3
\]
Step 3: Solve for the final temperature \( T_3 \).
Rearranging the equation to solve for \( T_3 \), we get:
\[
T_3 = \frac{\dot{m_1} T_1 + \dot{m_2} T_2}{\dot{m_1} + \dot{m_2}} - \frac{\dot{Q}}{c_p (\dot{m_1} + \dot{m_2})}
\]
Step 4: Conclusion.
Thus, the correct expression for the final temperature \( T_3 \) after mixing is option (C).
Final Answer: (C) \( T_3 = \frac{\dot{m_1} T_1 + \dot{m_2} T_2}{\dot{m_1} + \dot{m_2}} - \frac{\dot{Q}}{c_p(\dot{m_1} + \dot{m_2})} \)
Air having a mass flow rate of 2 kg/s enters a diffuser at 100 kPa and 30°C, with a velocity of 200 m/s. Exit area of the diffuser is 400 cm2 while the exit temperature of the air is 45°C. The rate of heat loss from the diffuser to the surrounding is 8 kJ/s. The pressure at the diffuser exit is \(\underline{\hspace{2cm}}\) kPa (2 decimal places).
Air at a pressure of 1 MPa and 300 K is flowing in a pipe. An insulated evacuated rigid tank is connected to this pipe through an insulated valve. The volume of the tank is 1 m3. The valve is opened and the tank is filled with air until the pressure in the tank is 1 MPa. Subsequently, the valve is closed. Consider air to be an ideal gas and neglect bulk kinetic and potential energy. The final temperature of air in the tank is \(\underline{\hspace{2cm}}\) K (1 decimal place).
Potato slices weighing 50 kg is dried from 60% moisture content (wet basis) to 5% moisture content (dry basis). The amount of dried potato slices obtained (in kg) is ............ (Answer in integer)
Two Carnot heat engines (E1 and E2) are operating in series as shown in the figure. Engine E1 receives heat from a reservoir at \(T_H = 1600 \, {K}\) and does work \(W_1\). Engine E2 receives heat from an intermediate reservoir at \(T\), does work \(W_2\), and rejects heat to a reservoir at \(T_L = 400 \, {K}\). Both the engines have identical thermal efficiencies. The temperature \(T\) (in K) of the intermediate reservoir is ........ (answer in integer). 
A bar of length \( L = 1 \, {m} \) is fixed at one end. Before heating its free end has a gap of \( \delta = 0.1 \, {mm} \) from a rigid wall as shown in the figure. Now the bar is heated resulting in a uniform temperature rise of \( 10^\circ {C} \). The coefficient of linear thermal expansion of the material is \( 20 \times 10^{-6} / \degree C \) and the Young’s modulus of elasticity is 100 GPa. Assume that the material properties do not change with temperature.
The magnitude of the resulting axial stress on the bar is .......... MPa (in integer). 
A massless cantilever beam, with a tip mass \( m \) of 10 kg, is modeled as an equivalent spring-mass system as shown in the figure. The beam is of length \( L = 1 \, {m} \), with a circular cross-section of diameter \( d = 20 \, {mm} \). The Young’s modulus of the beam material is 200 GPa.
The natural frequency of the spring-mass system is ............ Hz (rounded off to two decimal places).
A simply-supported beam has a circular cross-section with a diameter of 20 mm, area of 314.2 mm\(^2\), area moment of inertia of 7854 mm\(^4\), and a length \( L \) of 4 m. A point load \( P = 100 \, {N} \) acts at the center and an axial load \( Q = 20 \, {kN} \) acts through the centroidal axis as shown in the figure.
The magnitude of the offset between the neutral axis and the centroidal axis, at \( L/2 \) from the left, is ............ mm (rounded off to one decimal place).