Act like a helpful tutor and exlain me :NOT FOR REDISTRIBUTION
MECH 315 ~ Thermodynamics with Lab.
Homework 2
21 For cach case, determine the specified property athe dicated sa. Locate te sae on a sketch
ofthe = » ingm
3 Vers 505.2, p= 3bar. determine Tin'c
+) Ammoniast p= 10 B47 = ~20°%. determine, in 5
0 Prope tp = 1Mpa.T 05°C, determine win Be
2:2 A clos, righ nk whose volume i 15m? comains Refigerank 34a, nly a two-phase
Tauid vapor mista t 10°. Th eigen is std 0 ina sae wher temperature s 50°C
and quality s 100% Locate he nil and ins sates on skechof he T — » diagram. Determine
{he mass of vapor present at he nil an fil tts sch i Ki.
2.3 A piso
Question:
Act like a helpful tutor and exlain me :NOT FOR REDISTRIBUTION
MECH 315 ~ Thermodynamics with Lab.
Homework 2
21 For cach case, determine the specified property athe dicated sa. Locate te sae on a sketch
ofthe = » ingm
3 Vers 505.2, p= 3bar. determine Tin'c
+) Ammoniast p= 10 B47 = ~20°%. determine, in 5
0 Prope tp = 1Mpa.T 05°C, determine win Be
2:2 A clos, righ nk whose volume i 15m? comains Refigerank 34a, nly a two-phase
Tauid vapor mista t 10°. Th eigen is std 0 ina sae wher temperature s 50°C
and quality s 100% Locate he nil and ins sates on skechof he T — » diagram. Determine
{he mass of vapor present at he nil an fil tts sch i Ki.
2.3 A piso
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# Explanation of MECH 315 – Thermodynamics with Lab Homework 2
Let’s break down each problem and discuss the key concepts you’ll need to solve them.
---
## **2.1 Property Determination and T-v Diagram**
For each subpart, you are given two properties of a substance (like **v** and **p** for water, or **p** and **T** for propane). Using the property tables (steam tables, refrigerant tables, etc.), you are to:
1. **Find the Required Property:**
- Use the given information to look up (or interpolate) the unknown property in the appropriate thermodynamic tables.
2. **Locate the State:**
- Sketch the state on a Temperature vs. specific volume (**T-v**) diagram.
### **Example:**
**a) Water at \( v = 0.5 \frac{m^3}{kg}, p = 3\, bar \):**
- Use the steam tables at \( p = 3\, bar \) to find the temperature corresponding to \( v = 0.5 \frac{m^3}{kg} \).
- Check if this value lies in the compressed liquid, saturated mixture, or superheated region.
---
## **2.2 Rigid Tank with Refrigerant 134a**
- **Closed, Rigid Tank:** Volume is constant.
- **Given:** Initial two-phase mixture, initial and final temperatures, and pressures.
- **Quality (x):** Percentage of vapor in the mixture.
- **Procedure:**
1. Find initial and final states using refrigerant tables.
2. Use quality and specific volumes to find the mass of vapor.
3. Sketch both states on the T-v diagram.
---
## **2.3 Piston-Cylinder, Ammonia Compression (pV = constant)**
- **Ammonia is compressed:** Temperature and pressure change.
- **pV = constant:** This is a **polytropic process** with n = -1.
- **Work and Heat Transfer:** Use first law of thermodynamics.
- **Procedure:**
1. Find properties at initial and final states using ammonia tables.
2. Use the relationship for work in polytropic processes.
3. Apply energy balance to find heat transfer.
---
## **2.4 Piston-Cylinder, H₂O Two-Phase Mixture, Expansion**
- **Two-phase mixture expands at constant pressure** until a final temperature is reached.
- **Given Quality:** Initial state is a mixture; use tables to find properties.
- **Procedure:**
1. Find initial state properties using quality and pressure.
2. Final state: use pressure and temperature to find final properties.
3. Use energy balance to determine work done.
---
## **2.5 Rigid, Closed Tank—Solar Heating**
- **Rigid Tank:** Volume is constant, so mass is constant.
- **Refrigerant is heated by the sun:** Temperature and pressure change.
- **Key Steps:**
1. Initial state: use mass and volume to find initial specific volume and look up properties.
2. Final state: use pressure to find properties at saturated vapor.
3. Use energy balance to find heat transfer.
---
## **Key Concepts and Tools**
- **Thermodynamic tables:** Steam tables, refrigerant tables, property charts.
- **First Law of Thermodynamics:**
\[
\Delta U = Q - W
\]
- **Quality (x) in Two-Phase Mixtures:**
\[
x = \frac{m_{vapor}}{m_{total}}
\]
- **Rigid Tank:** Volume does not change.
- **Constant Pressure/Volume Processes:** Know how to handle work and energy balance.
- **T-v Diagram:** A plot used to visualize states and phase changes.
---
## **Tips**
- Always identify the phase (compressed liquid, saturated mixture, superheated vapor) first.
- Use **interpolation** if your values are between table entries.
- Sketch T-v diagrams for visualization.
- Clearly state assumptions (e.g., negligible kinetic and potential energy changes).
---
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