To solve this problem, we will use the concept of heat conduction through a wall and convective heat transfer from the wall to the surrounding air.
1. Thermal Conductivity Equation (Heat Conduction):
The steady-state heat conduction through the wall can be expressed as:
\[
Q = \frac{kA(T_1 - T_2)}{L}
\]
Where:
- \( Q \) is the heat transfer rate,
- \( k \) is the thermal conductivity of the wall,
- \( A \) is the cross-sectional area of the wall,
- \( T_1 \) and \( T_2 \) are the temperatures at the two sides of the wall,
- \( L \) is the thickness of the wall.
2. Convective Heat Transfer Equation:
The heat lost from the wall to the air is governed by convection, which can be written as:
\[
Q = hA(T_{{wall}} - T_{\infty})
\]
Where:
- \( h \) is the convective heat transfer coefficient,
- \( A \) is the surface area,
- \( T_{{wall}} \) is the temperature of the wall surface,
- \( T_{\infty} \) is the temperature of the air.
3. Setting the Heat Transfer Rates Equal:
Since there is no heat generation inside the wall, the heat conducted through the wall must equal the heat lost to the surrounding air:
\[
\frac{kA(T_1 - T_2)}{L} = hA(T_{{wall}} - T_{\infty})
\]
Simplifying, we get:
\[
\frac{k(T_1 - T_2)}{L} = h(T_{{wall}} - T_{\infty})
\]
4. Substituting Known Values:
- \( k = 100 \, {W/m·K} \),
- \( T_1 = 25^\circ C \),
- \( T_2 = 50^\circ C \),
- \( L = 0.2 \, {m} \),
- \( h = 50 \, {W/m²·K} \),
- \( T_{\infty} = 50^\circ C \).
Substitute these values into the equation:
\[
\frac{100(25 - T_{{wall}})}{0.2} = 50(T_{{wall}} - 50)
\]
5. Solve for \( T_{{wall}} \):
Expanding and solving the equation gives:
\[
500(25 - T_{{wall}}) = 50(T_{{wall}} - 50)
\]
\[
12500 - 500T_{{wall}} = 50T_{{wall}} - 2500
\]
\[
15000 = 550T_{{wall}}
\]
\[
T_{{wall}} = \frac{15000}{550} = 27.27^\circ C
\]
Thus, the temperature of the right-hand side surface of the wall is approximately \( 27.3^\circ C \).