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Give step-by-step solution with explanation and final answer:Question 2 (25 points)
A one-dimensional plane wall of thickness 2Z = 86 mm experiences uniform thermal energy
generation of q¢ = 1000 WW /mms3 and is convectively cooled at x = +40 mm by an ambient fluid
characterized by T.. = 30°C. If the steady-state temperature distribution within the wall is 7(x)
=a (L*- x? + b where a = 16°C/m? and b = 46°C, Determine the followings
(a) What is the thermal conductivity of the wall? (10 marks) [SO1:PI3]
(b) What is the value of the convection heat transfer coefficient, 42 (15 marks) [SO2:P11]
Question:
Act like a helpful tutor and exlain me :
Give step-by-step solution with explanation and final answer:Question 2 (25 points)
A one-dimensional plane wall of thickness 2Z = 86 mm experiences uniform thermal energy
generation of q¢ = 1000 WW /mms3 and is convectively cooled at x = +40 mm by an ambient fluid
characterized by T.. = 30°C. If the steady-state temperature distribution within the wall is 7(x)
=a (L*- x? + b where a = 16°C/m? and b = 46°C, Determine the followings
(a) What is the thermal conductivity of the wall? (10 marks) [SO1:PI3]
(b) What is the value of the convection heat transfer coefficient, 42 (15 marks) [SO2:P11]
This is AI generated Response.
Asked by: manish kumar
Created at: 2025-09-30 20:48:26
Final Answer:
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Let's break down **Question 2** step by step:
---
## **Given Data**
- Thickness of wall: \( 2L = 86\, \text{mm} \implies L = 43\, \text{mm} = .043\, \text{m} \)
- Uniform heat generation: \( \dot{q} = 100\, \text{W}/\text{mm}^3 = 1 \times 10^9\, \text{W}/\text{m}^3 \)
- Convective cooling at \( x = \pm 40\, \text{mm} = \pm .04\, \text{m} \)
- Ambient temperature: \( T_\infty = 30^\circ \text{C} \)
- Temperature distribution in wall: \( T(x) = a(L^2 - x^2) + b \), where \( a = 16\,^\circ\text{C}/\text{m}^2 \), \( b = 46^\circ\text{C} \)
---
# **(a) Thermal Conductivity of the Wall (\(k\))**
### **Step 1: General Heat Equation for Steady State with Internal Generation**
\[
\frac{d^2 T}{dx^2} + \frac{\dot{q}}{k} =
\]
### **Step 2: Compare with Given Temperature Profile**
Given:
\[
T(x) = a(L^2 - x^2) + b = aL^2 - a x^2 + b
\]
Take the second derivative:
\[
\frac{dT}{dx} = -2a x \\
\frac{d^2 T}{dx^2} = -2a
\]
### **Step 3: Plug into Heat Equation**
\[
-2a + \frac{\dot{q}}{k} = \implies k = \frac{\dot{q}}{2a}
\]
### **Step 4: Substitute Values**
- \( \dot{q} = 1 \times 10^9\, \text{W}/\text{m}^3 \)
- \( a = 16\,^\circ\text{C}/\text{m}^2 \)
\[
k = \frac{1 \times 10^9}{2 \times 16} = \frac{1 \times 10^9}{32}
\]
\[
k = 31,250,000\, \text{W}/(\text{m}\cdot ^\circ\text{C})
\]
---
### **Final Answer for (a):**
\[
\boxed{
k = 3.13 \times 10^7\, \text{W}/(\text{m}\cdot \text{C})
}
\]
---
# **(b) Value of the Convection Heat Transfer Coefficient (\( h \))**
### **Step 1: Boundary Condition at \( x = .04\, \text{m} \)**
At the surface (\( x = L_s = .04\, \text{m} \)), energy balance:
\[
- k \left. \frac{dT}{dx} \right|_{x=L_s} = h [T(L_s) - T_\infty]
\]
### **Step 2: Compute Needed Values**
#### 1. **\(\frac{dT}{dx}\) at \(x = .04\)**
\[
\frac{dT}{dx} = -2a x \Rightarrow \left. \frac{dT}{dx} \right|_{x=.04} = -2 \times 16 \times .04 = -1.28\, ^\circ\text{C}/\text{m}
\]
#### 2. **\(T(x)\) at \(x = .04\)**
\[
T(.04) = 16[(.043)^2 - (.04)^2] + 46
\]
\[
(.043)^2 = .001849,\quad (.04)^2 = .0016
\]
\[
T(.04) = 16(.001849 - .0016) + 46 = 16(.000249) + 46 = .003984 + 46 \approx 46.004^\circ\text{C}
\]
\[
T(.04) - T_\infty = 46.004 - 30 = 16.004^\circ\text{C}
\]
### **Step 3: Solve for \( h \)**
\[
- k \left( -1.28 \right) = h (16.004)
\]
\[
k \times 1.28 = h \times 16.004
\]
\[
h = \frac{k \times 1.28}{16.004}
\]
Recall \( k = 3.13 \times 10^7 \):
\[
h = \frac{3.13 \times 10^7 \times 1.28}{16.004}
\]
\[
h = \frac{4.0064 \times 10^7}{16.004}
\]
\[
h \approx 2.50 \times 10^6\, \text{W}/(\text{m}^2 \cdot ^\circ\text{C})
\]
---
### **Final Answer for (b):**
\[
\boxed{
h = 2.50 \times 10^6\, \text{W}/(\text{m}^2 \cdot \text{C})
}
\]
---
## **Summary**
- (a) \( k = 3.13 \times 10^7\, \text{W}/(\text{m}\cdot \text{C}) \)
- (b) \( h = 2.50 \times 10^6\, \text{W}/(\text{m}^2 \cdot \text{C}) \)
Let me know if you need further clarification on any step!
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