- 2071 Magh · 8 marks
Rigid container of steam 1500 kPa cooled to 100°C
Short answer
For rigid container volume 0.170 m³, initial superheated steam at 1500 kPa, 200°C, v1=0.1324 m³/kg, mass m = V/v1 = 1.284 kg. Cooled to 100°C at constant volume, state becomes wet at saturation pressure 101.4 kPa; with v2=v1, quality x=0.0786, so liquid mass fraction = 1-x = 0.921.
A rigid container with a volume of 0.170 m³ is initially filled with steam at 1500 kPa, 200°C. It is cooled to 100°C. Determine a) Total mass of the system b) Final pressure c) Mass fraction of the liquid in the final state Also sketch the process on P-v and T-v diagrams. [Refer the attached table for properties of steam]
Given: V = 0.170 m³ (rigid); state 1: 1500 kPa, 200 °C; cooled to 100 °C.
State 1: T_sat(1500 kPa) = 198.3 °C, so steam at 200 °C is slightly superheated. Superheated table: v₁ = 0.1324 m³/kg.
a) Total mass
m = V/v₁ = 0.170/0.1324 = 1.284 kg
b) Final pressure
v₂ = v₁ = 0.1324 (constant volume). At 100 °C: v_f = 0.001043, v_g = 1.6719 m³/kg; since v_f < v₂ < v_g, it is a wet mixture.
P₂ = P_sat(100 °C) = 101.4 kPa (≈ 0.1 MPa)
c) Mass fraction of liquid
x₂ = (0.1324 − 0.001043)/(1.6719 − 0.001043) = 0.0786
Liquid fraction = 1 − x₂ = 0.921 (m_f = 1.183 kg; m_g = 0.101 kg)
P|
| 1 (1500 kPa, 200 C)
| |
| | const v = 0.1324
| |
| 2 (101.4 kPa, wet)
+----------- v
T|
| 1 (200 C)
| * (≈ 198 C, meets sat. vapour line)
| |
| 2 (100 C, wet)
+----------- v
On both diagrams, process 1-2 is a vertical line going down from state 1 (superheated vapour) into the dome, crossing the saturated vapour line at about 198 °C and ending at 2 inside the dome.
Answer: m = 1.284 kg; P₂ = 101.4 kPa; liquid mass fraction = 0.921.
✓ Answer checked by Claude Opus 5.5 (high effort)
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