Question 7.3: Problem: Find the specific enthalpy of a saturated water‐ste...
Problem: Find the specific enthalpy of a saturated water‐steam mixture with 40% quality at a temperature of 50 °C.
Find: Specific enthalpy h.
Known: The water‐steam mixture is at the saturation temperature T_{sat} = 50 °C, quality x = 0.4.
Governing Equation:
Mixture property (y) y=xy_g + (1-x)y_f
Properties: From Table 7.2 at T_{sat} = 50 °C, enthalpy of liquid h_f = 209.33 kJ / kg and vapour h_g = 2592.1 kJ / kg.
Table 7.2 Properties of saturated water as a function of temperature.
Temp. (°C) | Pressure (MPa) | Spec. Vol. (m³/kg) | Int. Energy (kJ/kg) | Enthalpy (kJ/kg) | Entropy (kJ/kgK) | ||||
T_{sat} | P | v_f | v_g | u_f | u_g | h_f | h_g | s_f | s_g |
0.01 | 0.000 611 3 | 0.001 000 | 206.14 | 0.00 | 2375.3 | 0.00 | 2501.4 | 0.0000 | 9.1562 |
5 | 0.000 872 1 | 0.001 000 | 147.12 | 20.97 | 2382.3 | 20.98 | 2510.6 | 0.0761 | 9.0257 |
10 | 0.001 227 6 | 0.001 000 | 106.38 | 42.00 | 2389.2 | 42.01 | 2519.8 | 0.1510 | 8.9008 |
15 | 0.001 705 1 | 0.001 001 | 77.93 | 62.99 | 2396.1 | 62.99 | 2528.9 | 0.2245 | 8.7814 |
20 | 0.002 339 | 0.001 002 | 57.79 | 83.95 | 2402.9 | 83.96 | 2538.1 | 0.2966 | 8.6672 |
25 | 0.003 169 | 0.001 003 | 43.36 | 104.88 | 2409.8 | 104.89 | 2547.2 | 0.3674 | 8.5580 |
30 | 0.004 246 | 0.001 004 | 32.89 | 125.78 | 2416.6 | 125.79 | 2556.3 | 0.4369 | 8.4533 |
35 | 0.005 628 | 0.001 006 | 25.22 | 146.67 | 2423.4 | 146.68 | 2565.3 | 0.5053 | 8.3531 |
40 | 0.007 384 | 0.001 008 | 19.52 | 167.56 | 2430.1 | 167.57 | 2574.3 | 0.5725 | 8.2570 |
45 | 0.009 593 | 0.001 010 | 15.26 | 188.44 | 2436.8 | 188.45 | 2583.2 | 0.6387 | 8.1648 |
50 | 0.012 349 | 0.001 012 | 12.03 | 209.32 | 2443.5 | 209.33 | 2592.1 | 0.7038 | 8.0763 |
55 | 0.015 758 | 0.001 015 | 9.568 | 230.21 | 2450.1 | 230.23 | 2600.9 | 0.7679 | 7.9913 |
60 | 0.019 940 | 0.001 017 | 7.671 | 251.11 | 2456.6 | 251.13 | 2609.6 | 0.8312 | 7.9096 |
65 | 0.025 03 | 0.001 020 | 6.197 | 272.02 | 2463.1 | 272.06 | 2618.3 | 0.8935 | 7.8310 |
70 | 0.031 19 | 0.001 023 | 5.042 | 292.95 | 2469.6 | 292.98 | 2626.8 | 0.9549 | 7.7553 |
75 | 0.038 58 | 0.001 026 | 4.131 | 313.90 | 2475.9 | 313.93 | 2643.7 | 1.0155 | 7.6824 |
80 | 0.047 39 | 0.001 029 | 3.407 | 334.86 | 2482.2 | 334.91 | 2635.3 | 1.0753 | 7.6122 |
85 | 0.057 83 | 0.001 033 | 2.828 | 355.84 | 2488.4 | 355.90 | 2651.9 | 1.1343 | 7.5445 |
90 | 0.070 14 | 0.001 036 | 2.361 | 376.85 | 2494.5 | 376.92 | 2660.1 | 1.1925 | 7.4791 |
95 | 0.084 55 | 0.001 040 | 1.982 | 397.88 | 2500.6 | 397.96 | 2668.1 | 1.2500 | 7.4159 |
100 | 0.101 35 | 0.001 044 | 1.6729 | 418.94 | 2506.5 | 419.04 | 2676.1 | 1.3069 | 7.3549 |
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h=xh_g+(1-x) h_f =0.4 \times 2592.1 \ kJ/kg + (1-0.4)\times 209.33 \ kJ/kg=1162.438 \ kJ/kg
Answer: The mixture enthalpy is 1162.4 kJ / kg.
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