Solve correct option= Comatrer a fave of water in a Eyer Maintained at constant temperature, of 190" C: the. : og » Es LE cere cre cman 50 mm an ne enn of th ie Toe i ad th TY / tos mperetire of the water fs
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Solve correct option
= Comatrer a fave of water in a Eyer Maintained at constant temperature, of 190" C: the. : og
» Es
LE cere cre cman 50 mm an ne enn of th ie Toe i ad th TY
/ tos mperetire of the water fs
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Asked by: Santosh Pujari
Created at: 2025-10-28 12:46:48
Asked by: Santosh Pujari
Created at: 2025-10-28 12:46:48
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---
### **Problem (from image):**
- **Flow in a cylinder:** Water at a constant temperature of 100°C.
- **Cylinder diameter (D):** 50 mm = .05 m
- **Length of tube (L):** 6 m
- **Inlet temperature of water (T₁):** 15°C
- **Outlet temperature of water (T₂):** 57°C
- **Mass flow rate (ṁ):** .25 kg/s
- **Specific heat (cₚ):** 4.18 kJ/kg·K = 418 J/kg·K
**Asked:** Find the average heat transfer coefficient (h).
---
## **Step 1: Find Heat Transfer Rate (Q)**
\[
Q = \dot{m} c_p (T_2 - T_1)
\]
\[
Q = .25 \times 418 \times (57 - 15)
\]
\[
Q = .25 \times 418 \times 42
\]
\[
Q = .25 \times 175560
\]
\[
Q = 43890 \text{ W}
\]
---
## **Step 2: Log Mean Temperature Difference (LMTD)**
The surface temperature is constant at 100°C, so:
\[
\Delta T_1 = 100 - 15 = 85^\circ C
\]
\[
\Delta T_2 = 100 - 57 = 43^\circ C
\]
\[
\Delta T_m = \frac{\Delta T_1 - \Delta T_2}{\ln(\Delta T_1 / \Delta T_2)}
\]
\[
\Delta T_m = \frac{85 - 43}{\ln(85/43)}
\]
\[
\Delta T_m = \frac{42}{\ln(1.9767)}
\]
\[
\ln(1.9767) \approx .681
\]
\[
\Delta T_m = \frac{42}{.681} \approx 61.7^\circ C
\]
---
## **Step 3: Surface Area (A)**
\[
A = \pi D L
\]
\[
A = \pi \times .05 \times 6
\]
\[
A \approx .942 \text{ m}^2
\]
---
## **Step 4: Heat Transfer Coefficient (h)**
\[
Q = h A \Delta T_m
\]
\[
h = \frac{Q}{A \Delta T_m}
\]
\[
h = \frac{43890}{.942 \times 61.7}
\]
\[
h = \frac{43890}{58.11}
\]
\[
h \approx 755 \text{ W/m}^2 \cdot \text{K}
\]
---
## **Step 5: Correct Option**
**The correct answer is:**
**755 W/m²·K**
---
### **Mark:**
- [x] 755 W/m²·K
---
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