Question: Problem 8 (4 points) - Steam tables : Complete Table 1 for H2O using Table A-4, Table A-5, and Table A-6: V Table 1: H2O

 Problem 8 (4 points) - Steam tables : Complete Table 1
for H2O using Table A-4, Table A-5, and Table A-6: V Table

Problem 8 (4 points) - Steam tables : Complete Table 1 for H2O using Table A-4, Table A-5, and Table A-6: V Table 1: H2O temperature, pressure, specific volume and phase table. TC P kPa Phase description 400 0.1347 220 Saturated vapor 190 2500 4000 0.08103 SOLUCIOWE TemperatureTTE Specific volume, m/kg Sat. Sat. Sat. Temp. press. liquid, vapor, TC . kPa Vi VE 0.01 0.6117 0.001000 206.00 5 0.8725 0.001000 147.03 10 1.2281 0.001000 106.32 15 1.7057 0.001001 77.885 20 2.3392 0.001002 57.762 25 3.1698 0.001003 43.340 30 4.2469 0.001004 32.879 35 5.6291 0.001006 25.205 40 7.3851 0.001008 19.515 45 9.5953 0.001010 15.251 50 12.352 0.001012 12.026 55 15.763 0.001015 9.5639 60 19.947 0.001017 7.6670 65 25.043 0.001020 6.1935 70 31.202 0.001023 5.0396 75 38.597 0.001026 4.1291 47.416 0.001029 3.4053 85 57.868 0.001032 2.8261 90 70.183 0.001036 2.3593 95 84.609 0.001040 1.9808 100 101.42 0.001043 1.6720 105 120.90 0.001047 1.4186 110 143.38 0.001052 1.2094 115 169.18 0.001056 1.0360 120 198.67 0.001060 0.89133 125 232.23 0.001065 0.77012 130 270.28 0.001070 0.66808 135 313.22 0.001075 0.58179 140 361.53 0.00 1080 0.50850 145 415.68 0.001085 0.44600 150 476.16 0.001091 0.39248 155 543 49 0.001096 0.34648 160 618.23 0.001102 0.30580 165 700.93 0.001108 0.27244 170 792.18 0.001114 0.24260 175 892.60 0.001121 0.21659 180 10028 0.001127 0.19384 185 1123.5 0.001134 0.17390 190 1255.2 0.001141 0.15636 195 1398.8 0.001149 0.14089 200 1554.9 0.001157 0.12721 80 Internal energy, kJ/kg Sat. Sat. liquid, Evap.. vapor, UF ute uz 0.000 2374.9 2374.9 21.019 2360.8 2381.8 42.020 2346.6 2388.7 62.980 2332.5 2395.5 83.913 2318.4 2402.3 104.83 2304.3 2409.1 125.73 2290.2 2415.9 146.63 2276.0 2422.7 167.53 2261.9 2429.4 188.43 22477 2436.1 209.33 2233.4 2442.7 230.24 2219.1 2449.3 251.16 2204.7 2455.9 272.09 2190.3 2462.4 293.04 2175.8 2468.9 313.99 2161.3 2475.3 334.97 2146.6 2481.6 355.96 2131.9 2487.8 376.97 2117.0 2494.0 398.00 2102.0 2500.1 419.06 2087.0 2506.0 440.15 2071.8 2511.9 461.27 2056.4 2517.7 482.42 2040.9 2523.3 503.60 2025,3 2528.9 524.83 2009,5 2534.3 546.10 1993,4 2539,5 567.41 1977.3 2544.7 588.77 1960.9 2549,6 610.19 19442 2554.4 631.66 1927.4 2559.1 653.19 1910.3 2563.5 674.79 1893.0 2567.8 696.46 1875.4 2571.9 718.20 1857.5 2575.7 740,02 1839.4 2579.4 761.92 1820,9 2582.8 783.91 18021 2586.0 806.00 1783.0 2589.0 828.18 1763.6 2591.7 850.46 1743.7 25942 Enthalpy: kJ/kg Sat. Sat. liquid, Evap.. vapor, hi hy he 0.001 2500.9 2500.9 21.020 2489.1 2510.1 42.022 2477.2 2519.2 62.982 2465.4 2528.3 83.915 2453.5 2537.4 104.83 2441.7 2546.5 125.74 2429,8 2555.6 146.64 2417.9 2564.6 167.53 2406.0 2573.5 188.44 2394.0 2582.4 209.34 2382.0 2591.3 230.26 2369.8 2600.1 251.18 2357.7 2608.8 272.12 2345.4 2617.5 293.07 2333.0 2626.1 314.03 2320.6 2634.6 335.02 23080 2643.0 356.02 2295.3 2651.4 377.04 2282.5 2659.6 398.09 2269.6 2667.6 419.17 2256.4 2675.6 440.28 2243.1 2683.4 461.42 2229.7 2691.1 482.59 2216.0 2698.6 503.81 2202.1 2706.0 525.07 2188.1 2713.1 546.38 2173.7 2720.1 567.75 2159.1 2726.9 589.16 21443 2733.5 610.64 2129.2 2739.8 632.18 2113.8 2745.9 653.79 2098.0 2751.8 67547 20820 2757.5 697.24 2065.6 27628 719.08 2048.8 2767.9 741.02 2031.7 2772.7 76305 2014.2 27772 785.19 1996.2 2781.4 807.43 1977.9 2785.3 829.78 1959.0 2788.8 852.26 1939.8 2792.0 Entropy kJ/kg-K Sat. Sat. liquid, Evap., vapor, SI Ste Sc 0.0000 9.1556 9.1556 0.0763 8.9487 9.0249 0.1511 8.7488 8.8999 0.2245 8.5559 8.7803 0.2965 8.3696 8.6661 0.3672 8.1895 8.5567 0.4368 8.0152 8.4520 0.5051 7.8466 8.3517 0.5724 7.6832 8.2556 0.6386 7.5247 8.1633 0.7038 7.3710 8.0748 0.7680 7.2218 7.9898 0.8313 7.0769 7.9082 0.8937 6.9360 7.8296 0.9551 6.7989 7.7540 1.0158 6.6655 7.6812 1.0756 6.5355 7.6111 1.1346 6.4089 7.5435 1.1929 6.2853 7.4782 1.2504 6.1647 7.4151 1.3072 6,0470 7.3542 1.3634 5.9319 7.2952 1.4188 5.8193 7.2382 1.4737 5.7092 7.1829 1.5279 5.6013 7.1292 1.5816 5.4956 7.0771 1.6346 5.3919 7.0265 1.6872 5.2901 6.9773 1.7392 5.1901 6.9294 1.7908 5.0919 6.8827 1.8418 4.9953 6.8371 1.8924 4.9002 6.7927 1.9426 4.8066 6.7492 1.9923 4.7143 6.7067 2.0417 4.6233 6.6650 2.0906 4.5335 6.6242 2.1392 4.4448 6.5841 2.1875 4.3572 6.5447 22355 4.2705 6.5059 2.2831 4.1847 6.4678 2.3305 4.0997 6.4302

Step by Step Solution

There are 3 Steps involved in it

1 Expert Approved Answer
Step: 1 Unlock blur-text-image
Question Has Been Solved by an Expert!

Get step-by-step solutions from verified subject matter experts

Step: 2 Unlock
Step: 3 Unlock

Students Have Also Explored These Related Chemical Engineering Questions!