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Question 1 (10 point) A 350000 L rigid tank is filled with saturated liquid-vapor mixture of water at 250 kPa . If 35 percent of the mass is liquid and 65 percent of the mass is vapor, what is the total mass in the tank? Question \( 2\left(20\right. \) point) Two air flows are combined to a single flow. One flow is \( 1 \mathrm{~m}^{3} / \mathrm{s} \mathrm{at} 200^{\circ} \mathrm{C} \), and the other is \( 2 \mathrm{~m}^{3} / \mathrm{s} \) at \( 200^{\circ} \mathrm{C} \), both at 100 kPa . They mix without any heat transfer to produce an exit flow at 100 kPa . Neglect kinetic energies and find the volume flow rate at the exit. Assuming constant specific heat

Ask by Powell Curry. in Turkey
Jan 13,2025

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**Question 1:** The total mass in the tank is approximately **4,200 kg**. **Question 2:** The exit volume flow rate is **3 m³/s**.

Solution

### **Question 1** **Given:** - **Volume of tank, \( V \)** = 350,000 L = 350 m³ - **Pressure, \( P \)** = 250 kPa (saturated mixture) - **Mass fractions:** 35% liquid (\( x_f = 0.35 \)) and 65% vapor (\( x_g = 0.65 \)) **Approach:** 1. **Determine Specific Volumes:** - From steam tables at **250 kPa**: - **Saturated Liquid Specific Volume (\( v_f \))** ≈ 0.001156 m³/kg - **Saturated Vapor Specific Volume (\( v_g \))** ≈ 0.1269 m³/kg 2. **Calculate Mixture Specific Volume (\( v \)):** \[ v = x_f \cdot v_f + x_g \cdot v_g = 0.35 \times 0.001156 + 0.65 \times 0.1269 \approx 0.08289 \, \text{m}³/\text{kg} \] 3. **Determine Total Mass (\( m \)):** \[ m = \frac{V}{v} = \frac{350 \, \text{m}³}{0.08289 \, \text{m}³/\text{kg}} \approx 4217 \, \text{kg} \] **Answer:** The total mass in the tank is approximately **4,200 kg**. --- ### **Question 2** **Given:** - **Flow 1:** \( V_1 = 1 \, \text{m}³/\text{s} \) at \( T_1 = 200°C \) and \( P_1 = 100 \, \text{kPa} \) - **Flow 2:** \( V_2 = 2 \, \text{m}³/\text{s} \) at \( T_2 = 200°C \) and \( P_2 = 100 \, \text{kPa} \) - **Exit Pressure:** \( P_{\text{exit}} = 100 \, \text{kPa} \) - **Assumptions:** Adiabatic mixing, no heat transfer, constant specific heats, and neglecting kinetic energies. **Approach:** 1. **Since both incoming air streams are at the same temperature and pressure:** - **Mass Flow Rates:** \[ m_1 = \frac{P V_1}{R T}, \quad m_2 = \frac{P V_2}{R T} \] - **Total Mass Flow Rate:** \[ m_{\text{exit}} = m_1 + m_2 = \frac{P (V_1 + V_2)}{R T} \] 2. **Determine Exit Volume:** - Since temperature and pressure remain unchanged, specific volume remains the same. - Therefore, **Volume Flow Rates Add Up:** \[ V_{\text{exit}} = V_1 + V_2 = 1 \, \text{m}³/\text{s} + 2 \, \text{m}³/\text{s} = 3 \, \text{m}³/\text{s} \] **Answer:** The exit volume flow rate is **3 m³/s**.

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To find the total mass in the tank, you can use the relationship between the volumes of saturated liquid and vapor at the given pressure. By consulting steam tables, you can determine the specific volumes (\(v_f\) and \(v_g\)) at \(250\) kPa, then apply the quality formula. For the mixture, multiply the tank volume by the mass fractions (35% liquid, 65% vapor) to establish individual masses and add them together for total mass. When mixing two air flows, you simply add the volumetric flow rates to find the exit flow rate. Since both flows are at \(200^\circ C\) and are at a consistent pressure of \(100\) kPa, the exit volume flow rate is the sum of the individual flow rates: \(1 \, \text{m}^3/\text{s} + 2 \, \text{m}^3/\text{s} = 3 \, \text{m}^3/\text{s}\). Thus, the exit flow rate is \(3 \, \text{m}^3/\text{s}\).

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