Act like a helpful tutor and exlain me : Give step-by-step solution with explanation and final answer:Saturated vapor water at 2 5 0 ° C is expanded to a lower pressure with constant temperature. Find the changes in u and s when the final pressure is : a . 1 0 0 kPa b . 5 0 kPa c . 1 0 kPa
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Act like a helpful tutor and exlain me : Give step-by-step solution with explanation and final answer:Saturated vapor water at 2 5 0 ° C is expanded to a lower pressure with constant temperature. Find the changes in u and s when the final pressure is : a . 1 0 0 kPa b . 5 0 kPa c . 1 0 kPa
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Asked by: manish kumar
Created at: 2025-10-15 22:29:06
Asked by: manish kumar
Created at: 2025-10-15 22:29:06
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# Step-by-Step Solution: Water Vapor Expansion at 250°C
Given:
- Initial state: Saturated vapor water at \(T = 250^\circ\text{C}\)
- Process: **Isothermal** (constant temperature) expansion to a lower pressure
- Find the changes in **internal energy (\(u\))** and **entropy (\(s\))** for each final pressure:
- (a) \(P = 100~\text{kPa}\)
- (b) \(P = 50~\text{kPa}\)
- (c) \(P = 10~\text{kPa}\)
We'll use **superheated steam tables** for water at \(250^\circ\text{C}\).
---
## 1. Identify Initial State (Saturated Vapor at \(250^\circ\text{C}\))
At \(T = 250^\circ\text{C}\):
- The **saturation pressure** \(P_\text{sat}\) is (from steam tables):
\(P_\text{sat} \approx 3975~\text{kPa}\)
- As *saturated vapor*, the initial state is at:
- \(T_1 = 250^\circ\text{C}\)
- \(P_1 = 3975~\text{kPa}\)
- **Initial specific internal energy** (\(u_1\)) = \(u_g\) at \(250^\circ\text{C}\)
- **Initial specific entropy** (\(s_1\)) = \(s_g\) at \(250^\circ\text{C}\)
From steam tables:
- \(u_1 = u_g(250^\circ\text{C}) \approx 2594.2~\text{kJ/kg}\)
- \(s_1 = s_g(250^\circ\text{C}) \approx 6.361~\text{kJ/(kg·K)}\)
---
## 2. Isothermal Expansion: Final States
When expanding **isothermally** to a lower pressure, the vapor becomes **superheated**.
For each final pressure, find the properties at \(T = 250^\circ\text{C}\) and the specified \(P\):
### (a) \(P_2 = 100~\text{kPa}\)
From superheated steam tables at \(T = 250^\circ\text{C}, P = 100~\text{kPa}\):
- \(u_2 \approx 2642.5~\text{kJ/kg}\)
- \(s_2 \approx 8.117~\text{kJ/(kg·K)}\)
**Changes:**
- \(\Delta u = u_2 - u_1 = 2642.5 - 2594.2 = \boxed{48.3~\text{kJ/kg}}\)
- \(\Delta s = s_2 - s_1 = 8.117 - 6.361 = \boxed{1.756~\text{kJ/(kg·K)}}\)
---
### (b) \(P_2 = 50~\text{kPa}\)
From superheated steam tables at \(T = 250^\circ\text{C}, P = 50~\text{kPa}\):
- \(u_2 \approx 2656.9~\text{kJ/kg}\)
- \(s_2 \approx 8.626~\text{kJ/(kg·K)}\)
**Changes:**
- \(\Delta u = 2656.9 - 2594.2 = \boxed{62.7~\text{kJ/kg}}\)
- \(\Delta s = 8.626 - 6.361 = \boxed{2.265~\text{kJ/(kg·K)}}\)
---
### (c) \(P_2 = 10~\text{kPa}\)
From superheated steam tables at \(T = 250^\circ\text{C}, P = 10~\text{kPa}\):
- \(u_2 \approx 2673.7~\text{kJ/kg}\)
- \(s_2 \approx 9.398~\text{kJ/(kg·K)}\)
**Changes:**
- \(\Delta u = 2673.7 - 2594.2 = \boxed{79.5~\text{kJ/kg}}\)
- \(\Delta s = 9.398 - 6.361 = \boxed{3.037~\text{kJ/(kg·K)}}\)
---
## 3. **Summary Table**
| Final \(P\) (kPa) | \(u_2\) (kJ/kg) | \(s_2\) (kJ/kg·K) | \(\Delta u\) (kJ/kg) | \(\Delta s\) (kJ/kg·K) |
|:-----------------:|:---------------:|:-----------------:|:--------------------:|:----------------------:|
| 100 | 2642.5 | 8.117 | 48.3 | 1.756 |
| 50 | 2656.9 | 8.626 | 62.7 | 2.265 |
| 10 | 2673.7 | 9.398 | 79.5 | 3.037 |
---
## 4. **Explanation**
- As the vapor expands **isothermally** (at constant \(T\)), its pressure decreases and it becomes more superheated.
- Both **internal energy (\(u\))** and **entropy (\(s\))** **increase** because the system absorbs heat to keep the temperature constant while the volume increases.
- The lower the final pressure, the greater the increase in both \(u\) and \(s\).
---
## 5. **Final Answers**
### (a) For \(P = 100~\text{kPa}\):
- \(\Delta u = \boxed{48.3~\text{kJ/kg}}\)
- \(\Delta s = \boxed{1.756~\text{kJ/(kg·K)}}\)
### (b) For \(P = 50~\text{kPa}\):
- \(\Delta u = \boxed{62.7~\text{kJ/kg}}\)
- \(\Delta s = \boxed{2.265~\text{kJ/(kg·K)}}\)
### (c) For \(P = 10~\text{kPa}\):
- \(\Delta u = \boxed{79.5~\text{kJ/kg}}\)
- \(\Delta s = \boxed{3.037~\text{kJ/(kg·K)}}\)
---
**Note:**
Values are taken from typical steam tables. If your tables have slightly different values, use those for precise answers.
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