Step 1: Understanding the Concept:
One-dimensional steady-state heat conduction in series composite walls: according to Fourier's law and electrical analogy, the total conductive thermal resistance of multilayer walls in series per unit area is the arithmetic sum of individual layer resistances ($R_t = \sum
rac{x_i}{k_i}$).
Key Formula or Approach:
\[ R_{\text{cond}} = \frac{x}{k \cdot A} \quad \xrightarrow{A = 1\text{ m}^2} \quad \mathbf{R_t} = R_1 + R_2 + R_3 = \mathbf{\left[ \left(\frac{x_1}{k_1}\right) + \left(\frac{x_2}{k_2}\right) + \left(\frac{x_3}{k_3}\right) \right]} \]
Step 2: Detailed Explanation:
In thermal engineering and heat transfer calculations for dairy cold storage walls:
- By Fourier's law of 1D steady-state heat conduction, heat flow through a layer of thickness $x$, thermal conductivity $k$, and cross-sectional area $A$ is:
\[ q = \frac{k \cdot A \cdot \Delta T}{x} = \frac{\Delta T}{R_{\text{cond}}} \quad \text{where } R_{\text{cond}} = \frac{x}{k \cdot A} \]
- For a 3-layer composite wall in series with unit area ($A = 1\text{ m}^2$):
1. Thermal resistance of layer 1: $R_1 = \frac{x_1}{k_1}$.
2. Thermal resistance of layer 2: $R_2 = \frac{x_2}{k_2}$.
3. Thermal resistance of layer 3: $R_3 = \frac{x_3}{k_3}$.
- The total equivalent thermal resistance ($R_t$) is the direct sum of series resistances:
\[ \mathbf{R_t = \left[ \left(\frac{x_1}{k_1}\right) + \left(\frac{x_2}{k_2}\right) + \left(\frac{x_3}{k_3}\right) \right]} \]
Step 3: Final Answer:
Therefore, total thermal resistance is \(R_t = [(x_1/k_1) + (x_2/k_2) + (x_3/k_3)]\), corresponding to option (A).