I. Specify whether the substance is subcooled liquid, compressed liquid, saturated liquid, saturated liquid-vapor (wet mixture), saturated vapor or superheated for the following conditions using the table below: Saturated water-Temperature table Specific volume, Internal energy Enthalpy. kkg Entropy m/kg k/kg kkg - K Sat. Тermp., press. Pu kPa Sat. liquid, Sat. Sat. Sat. Sat. Sat. Sat. liquid, Sat. Evap., liquid, Evap. vapor. liquid, Evap. vapor, vapor, T°C vapor, V 0.6113 0.8721 0.0 20.97 0.01 0.001000 206.14 9.1562 9.1562 20.98 2489.6 2510.6 0.0761 8.9496 9.0257 42.01 2477.7 2519.8 0.1510 8.7498 8.9008 62.99 2465.9 2528.9 0.2245 8.5569 8.7814 83.96 2454.1 2538.1 0.2966 8.3706 8.6672 2304.9 2409.8 104.89 2442.3 2547.2 0.3674 8.1905 8.5580 2290.8 2416.6 125.79 2430.5 2556.3 0.4369 8.0164 8.4533 2276.7 2423.4 146.68 2418.6 2565.3 0.5053 7.8478 8.3531 2262.6 2430.1 167.57 2406.7 2574.3 0.5725 7.6845 8.2570 2248.4 2436.8 188.45 2394.8 2583.2 0.6387 7.5261 8.1648 2234.2 2443.5 209.33 2382.7 2592.1 0.7038 7.3725 8.0763 2219.9 2450.1 230.23 2370.7 2600.9 0.7679 7.2234 7.9913 2205.5 2456.6 251.13 2358.5 2609.6 0.8312 7.0784 7.9096 2191.1 2463.1 272.06 2346.2 2618.3 0.8935 6.9375 7.8310 2176.6 2469.6 292.98 2333.8 2626.8 0.9549 6.8004 7.7553 2162.0 2475.9 313.93 2321.4 2635.3 1.0155 6.6669 7.6824 2147.4 2482.2 334.91 2308.8 2643.7 10753 6.5369 7.6122 355.84 2132.6 2488.4 355.90 2296.0 2651.9 1.1343 6.4102 7.5445 2117.7 2494.5 376.92 2283.2 2660.1 1.1925 6.2866 7.4791 2375.3 2375.3 0.01 2501.3 2501.4 0.000 0.001000 147.12 2361.3 2382.3 10 1.2276 0.001000 106.38 42.00 2347.2 2389.2 1.7051 2.339 15 0.001001 0.001002 77.93 62.99 2333.1 2396.1 2319.0 2402.9 20 57.79 83.95 104.88 125.78 25 3.169 0.001003 43.36 30 4.246 0.001004 32.89 35 5.628 0.001006 146.67 25.22 19.52 40 7.384 0.001008 167.56 45 9.593 0.001010 15.26 188.44 50 12.349 15.758 0.001012 12.03 209.32 230.21 55 0.001015 9.568 60 19.940 0.001017 7.671 251.11 65 6.197 25.03 31.19 38.58 47.39 0.001020 272.02 70 0.001023 5.042 292.95 75 0.001026 4.131 313.90 80 0.001029 3.407 334.86 85 57.83 0.001033 2.828 70.14 84.55 Sat. press. MPa 90 0.001036 2.361 376.85 95 0.001040 1.982 397.88 2102.7 2500.6 397.96 2270.2 2668.1 1.2500 6.1659 7.4159 100 105 0.10135 0.001044 0.12082 0.001048 1.6729 418.94 2087.6 2506.5 419.04 2257.0 2676.1 1.3069 6.0480 7.3549 1.4194 440.02 2072.3 2512.4 440.15 2243.7 2683.8 1.3630 5.9328 7.2958 2057.0 2518.1 461.30 2230.2 2691.5 1.4185 5.8202 7.2387 2041.4 2523.7 482.48 2216.5 2699.0 1.4734 5.7100 7.1833 2025.8 2529.3 503.71 2202.6 2706.3 1.5276 5.6020 7.1296 2009.9 2534.6 524.99 2188.5 2713.5 1.5813 5.4962 7.0775 1993.9 2539.9 546.31 2174.2 2720.5 1.6344 5.3925 7.0269 1977.7 2545.0 567.69 2159.6 2727.3 1.6870 5.2907 6.9777 1961.3 2550.0 589.13 2144.7 2733.9 1.7391 5.19908 6.9299 110 115 120 125 0.14327 0.001052 1.2102 461.14 0.16906 0.001056 1.0366 0.8919 482.30 0.19853 0.001060 503.50 524.74 0.2321 0.001065 0.2701 0.001070 0.7706 130 0.6685 0.5822 546.02 135 0.3130 0.001075 567.35 140 0.3613 0.001080 0.5089 588.74 145 0.4154 0.001085 0.4463 610.18 0.3928 0.3468 0.3071 1944.7 2554.9 610.63 2129.6 2740.3 1.7907 5.0926 6.8833 1927.9 2559.5 632.20 2114.3 2746.5 1.8418 4.9960 6.8379 1910.8 2564.1 653.84 2098.6 2752.4 1.8925 4.9010 6.7935 1893.5 2568.4 675.55 2082.6 2758.1 1.9427 4.8075 6.7502 1876.0 2572.5 697.34 2066.2 2763.5 1.9925 4.7153 6.7078 150 0.4758 0.5431 0.6178 0.001091 631.68 155 0.001096 653.24 160 0.001102 674.87 165 0.7005 0.001108 0.2727 696.56
I. Specify whether the substance is subcooled liquid, compressed liquid, saturated liquid, saturated liquid-vapor (wet mixture), saturated vapor or superheated for the following conditions using the table below: Saturated water-Temperature table Specific volume, Internal energy Enthalpy. kkg Entropy m/kg k/kg kkg - K Sat. Тermp., press. Pu kPa Sat. liquid, Sat. Sat. Sat. Sat. Sat. Sat. liquid, Sat. Evap., liquid, Evap. vapor. liquid, Evap. vapor, vapor, T°C vapor, V 0.6113 0.8721 0.0 20.97 0.01 0.001000 206.14 9.1562 9.1562 20.98 2489.6 2510.6 0.0761 8.9496 9.0257 42.01 2477.7 2519.8 0.1510 8.7498 8.9008 62.99 2465.9 2528.9 0.2245 8.5569 8.7814 83.96 2454.1 2538.1 0.2966 8.3706 8.6672 2304.9 2409.8 104.89 2442.3 2547.2 0.3674 8.1905 8.5580 2290.8 2416.6 125.79 2430.5 2556.3 0.4369 8.0164 8.4533 2276.7 2423.4 146.68 2418.6 2565.3 0.5053 7.8478 8.3531 2262.6 2430.1 167.57 2406.7 2574.3 0.5725 7.6845 8.2570 2248.4 2436.8 188.45 2394.8 2583.2 0.6387 7.5261 8.1648 2234.2 2443.5 209.33 2382.7 2592.1 0.7038 7.3725 8.0763 2219.9 2450.1 230.23 2370.7 2600.9 0.7679 7.2234 7.9913 2205.5 2456.6 251.13 2358.5 2609.6 0.8312 7.0784 7.9096 2191.1 2463.1 272.06 2346.2 2618.3 0.8935 6.9375 7.8310 2176.6 2469.6 292.98 2333.8 2626.8 0.9549 6.8004 7.7553 2162.0 2475.9 313.93 2321.4 2635.3 1.0155 6.6669 7.6824 2147.4 2482.2 334.91 2308.8 2643.7 10753 6.5369 7.6122 355.84 2132.6 2488.4 355.90 2296.0 2651.9 1.1343 6.4102 7.5445 2117.7 2494.5 376.92 2283.2 2660.1 1.1925 6.2866 7.4791 2375.3 2375.3 0.01 2501.3 2501.4 0.000 0.001000 147.12 2361.3 2382.3 10 1.2276 0.001000 106.38 42.00 2347.2 2389.2 1.7051 2.339 15 0.001001 0.001002 77.93 62.99 2333.1 2396.1 2319.0 2402.9 20 57.79 83.95 104.88 125.78 25 3.169 0.001003 43.36 30 4.246 0.001004 32.89 35 5.628 0.001006 146.67 25.22 19.52 40 7.384 0.001008 167.56 45 9.593 0.001010 15.26 188.44 50 12.349 15.758 0.001012 12.03 209.32 230.21 55 0.001015 9.568 60 19.940 0.001017 7.671 251.11 65 6.197 25.03 31.19 38.58 47.39 0.001020 272.02 70 0.001023 5.042 292.95 75 0.001026 4.131 313.90 80 0.001029 3.407 334.86 85 57.83 0.001033 2.828 70.14 84.55 Sat. press. MPa 90 0.001036 2.361 376.85 95 0.001040 1.982 397.88 2102.7 2500.6 397.96 2270.2 2668.1 1.2500 6.1659 7.4159 100 105 0.10135 0.001044 0.12082 0.001048 1.6729 418.94 2087.6 2506.5 419.04 2257.0 2676.1 1.3069 6.0480 7.3549 1.4194 440.02 2072.3 2512.4 440.15 2243.7 2683.8 1.3630 5.9328 7.2958 2057.0 2518.1 461.30 2230.2 2691.5 1.4185 5.8202 7.2387 2041.4 2523.7 482.48 2216.5 2699.0 1.4734 5.7100 7.1833 2025.8 2529.3 503.71 2202.6 2706.3 1.5276 5.6020 7.1296 2009.9 2534.6 524.99 2188.5 2713.5 1.5813 5.4962 7.0775 1993.9 2539.9 546.31 2174.2 2720.5 1.6344 5.3925 7.0269 1977.7 2545.0 567.69 2159.6 2727.3 1.6870 5.2907 6.9777 1961.3 2550.0 589.13 2144.7 2733.9 1.7391 5.19908 6.9299 110 115 120 125 0.14327 0.001052 1.2102 461.14 0.16906 0.001056 1.0366 0.8919 482.30 0.19853 0.001060 503.50 524.74 0.2321 0.001065 0.2701 0.001070 0.7706 130 0.6685 0.5822 546.02 135 0.3130 0.001075 567.35 140 0.3613 0.001080 0.5089 588.74 145 0.4154 0.001085 0.4463 610.18 0.3928 0.3468 0.3071 1944.7 2554.9 610.63 2129.6 2740.3 1.7907 5.0926 6.8833 1927.9 2559.5 632.20 2114.3 2746.5 1.8418 4.9960 6.8379 1910.8 2564.1 653.84 2098.6 2752.4 1.8925 4.9010 6.7935 1893.5 2568.4 675.55 2082.6 2758.1 1.9427 4.8075 6.7502 1876.0 2572.5 697.34 2066.2 2763.5 1.9925 4.7153 6.7078 150 0.4758 0.5431 0.6178 0.001091 631.68 155 0.001096 653.24 160 0.001102 674.87 165 0.7005 0.001108 0.2727 696.56
Introduction to Chemical Engineering Thermodynamics
8th Edition
ISBN:9781259696527
Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Publisher:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Chapter1: Introduction
Section: Chapter Questions
Problem 1.1P
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