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An Isobaric process is done on steam where it is heated to 200 C at 1.1 MPa. It was initially a kilogram of saturated liquid. Find the change in volume, change in internal energy, change in enthalpy, and change in entropy. (0.1848 m3, 1837.31 kJ, 2040.66 kJ, 4.4609 kJ/k) Table 3. Vapor 1.15 (186.07) p(t Sat.) 1.10 (184.09) 10v 10 . 6.5381 177.53 2586.4 2781.7 170.13 2587.7 2783.3 Sat. 6.5535 175 180 185 190 195 172.50 2567.9 2757.6 175.28 2578 2 27710 6.5300 178.02 2588.2 2784.0 6.3587 180.71 2598.I 2796.9 6.5866 183.36 2607.8 2809.5 6.6137 164.20 25648 2753.6 166.91 2573.2 2767.2 169.37 258S.5 2780.5 172.18 2595.3 2793.5 6.5603 174.75 2605.4 2806.4 6.4726 6.3028 6.3320 6.5004 6.5878 177.28 2615.1 2819.0 6.6146 179.77 2624.6 2831.4 200 205 210 215 220 185.97 2617.4 2822.0 6.6401 188.56 2626.8 2834.2 6.6659 191.11 2636.1 2846.3 6.6911 182.24 2634.0 2843.6 6.6661 193.63 2645.3 2858.3 6.7157 196.13 2654.3 2870.1 6.7398 6.6407 184.68 2643.3 2855.7 187.09 2652.5 2867.6 6.7154 6.6910 225 230 235 240 245 198.60 2663.3 2881.8 6.7634 201.05 2672.2 2893.4 6.7865 203.49 2681.0 2904.9 6.8093 205.90 2689.8 2916.3 208.30 2698.5 2927.6 189.47 2661.5 2879.4 6.7392 191.84 2670.5 2891.1 194.19 2679.4 2902.7 196.51 2688.2 2914.2 198.82 2697.0 2925.6 6.7625 6.7855 6.8080 6.8301 6.8316 6.8535 250 260 270 280 290 210.7 2707.1 2938.8 6.8751 215.4 2724.2 2961.1 220.1 2741.1 2983.2 6.9584 224.7 2757.9 3005.1 229.3 2774.6 3026.9 201.1 2705.7 2936.9 205.7 2722.9 2959.4 210.2 2739.9 2981.6 214.6 2756.8 3003. 219.0 2773.6 3025.4 6.8518 6.8943 6.9356 6.9757 7.0149 6.9174 6.9984 7.0373

An Isobaric process is done on steam where it is heated to 200 C at 1.1 MPa. It was initially a kilogram of saturated liquid. Find the change in volume, change in internal energy, change in enthalpy, and change in entropy. (0.1848 m3, 1837.31 kJ, 2040.66 kJ, 4.4609 kJ/k) Table 3. Vapor 1.15 (186.07) p(t Sat.) 1.10 (184.09) 10v 10 . 6.5381 177.53 2586.4 2781.7 170.13 2587.7 2783.3 Sat. 6.5535 175 180 185 190 195 172.50 2567.9 2757.6 175.28 2578 2 27710 6.5300 178.02 2588.2 2784.0 6.3587 180.71 2598.I 2796.9 6.5866 183.36 2607.8 2809.5 6.6137 164.20 25648 2753.6 166.91 2573.2 2767.2 169.37 258S.5 2780.5 172.18 2595.3 2793.5 6.5603 174.75 2605.4 2806.4 6.4726 6.3028 6.3320 6.5004 6.5878 177.28 2615.1 2819.0 6.6146 179.77 2624.6 2831.4 200 205 210 215 220 185.97 2617.4 2822.0 6.6401 188.56 2626.8 2834.2 6.6659 191.11 2636.1 2846.3 6.6911 182.24 2634.0 2843.6 6.6661 193.63 2645.3 2858.3 6.7157 196.13 2654.3 2870.1 6.7398 6.6407 184.68 2643.3 2855.7 187.09 2652.5 2867.6 6.7154 6.6910 225 230 235 240 245 198.60 2663.3 2881.8 6.7634 201.05 2672.2 2893.4 6.7865 203.49 2681.0 2904.9 6.8093 205.90 2689.8 2916.3 208.30 2698.5 2927.6 189.47 2661.5 2879.4 6.7392 191.84 2670.5 2891.1 194.19 2679.4 2902.7 196.51 2688.2 2914.2 198.82 2697.0 2925.6 6.7625 6.7855 6.8080 6.8301 6.8316 6.8535 250 260 270 280 290 210.7 2707.1 2938.8 6.8751 215.4 2724.2 2961.1 220.1 2741.1 2983.2 6.9584 224.7 2757.9 3005.1 229.3 2774.6 3026.9 201.1 2705.7 2936.9 205.7 2722.9 2959.4 210.2 2739.9 2981.6 214.6 2756.8 3003. 219.0 2773.6 3025.4 6.8518 6.8943 6.9356 6.9757 7.0149 6.9174 6.9984 7.0373

Elements Of Electromagnetics
Elements Of Electromagnetics
7th Edition
ISBN:9780190698614
Author:Sadiku, Matthew N. O.
Publisher:Sadiku, Matthew N. O.
ChapterMA: Math Assessment
Section: Chapter Questions
Problem 1.1MA
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An Isobaric process is done on steam where it is heated to 200 C at 1.1 MPa. It was initially a kilogram of saturated liquid. Find the change in volume, change in internal energy, change in enthalpy, and change in entropy. (0.1848 m3, 1837.31 kJ, 2040.66 kJ, 4.4609 kJ/k) Table 3. Vapor p(t Sat.) 1.10 (184.09) 1.15 (186.07) 10 10 . Sat. 177.53 2586.4 2781.7 6.5535 170.13 2587.7 27833 6.5381 175 180 185 190 195 172.50 2567.9 2737.6 L75.28 25782 2771.0 178.02 2588.2 2784.0 180.71 2598.1 2796.9 183.36 2607.8 2809.5 6.6137 164.20 25648 2753.6 166.91 2573.2 2767.2 169 37 258SS 2780.5 172.18 2595.5 2793.5 174.75 2605.4 2806.4 6.4726 6.3028 63320 6.5603 6.5878 6.5004 63300 6.5587 6.5866 200 205 210 215 220 185.97 2617.4 2822.0 6.6401 188.56 2626.8 2834.2 6.6659 191.11 2636.1 2846.3 6.6911 193.63 2645.3 2858.3 6.7157 196.13 2654.3 2870.1 6.7398 177.28 2615.1 2819.0 179.77 2624.6 2831.4 182.24 2634.0 2843.6 184.68 2643.3 2855.7 187.09 2652.5 2867.6 6.7154 6.6146 6.6407 6.6661 6.6910 225 230 235 240 245 198.60 2663.3 2881.8 6.7634 201.05 2672.2 2893.4 6.7865 203.49 2681.0 2904.9 6.8093 205.90 2689.8 2916.3 208.30 2698.5 2927.6 189.47 2661.5 2879.4 6.7392 191.84 2670.5 2891.1 194.19 2679.4 2902.7 196.51 2688.2 2914.2 198.82 2697.0 2925.6 6.7625 6.7855 6.8080 6.8301 6.8316 6.8535 250 260 270 280 290 210.7 2707.1 2938.8 215.4 2724.2 2961.1 220.1 2741.1 2983.2 224.7 2757.9 3005.1 229.3 2774.6 3026.9 6.8751 6.9174 6.9584 6.9984 7.0373 201.1 2705.7 2936.9 205.7 2722.9 2959.4 210.2 2739.9 2981.6 214.6 2756.8 3003.6 219.0 2773.6 3025.4 6.8518 6.8943 6.9356 6.9757 7.0149 Enthalpy Entropy Specific Volume Sat, Sat. Liquid Vapor 10v 10, Internal Energy Sat, Liquid Tep Sat. Vapor Sat. Liquid Sat. Vapor Sat. 1Jquid Sat. Vapor Evap. Evap. Evap. Press MP h/ h h, u u, s, 708.64 1866.1 2574.7 109.47 2057.0 2766.4 2.0200 4.6647 6.6847 255.6 252.4 711.00 1864.2 2575.2 711.85 2055.2 2767.0 2.0253 4.6549 6.6802 249.3 713.34 1862.2 25S75.6 714.20 2053.4 2767.5 2.0306 4.6451 6.6758 246.3 715.66 1860.3 25576.0 716.52 2051.6 2768.1 2.0359 4.6355 6.6714 243.3 167.78 1.115 .75 .76 .77 .78 .79 168.32 L1121 168.86 1.1128 169.39 1.1135 169.91 11142 717.95 1858.5 2576.4 718.83 2049.8 2768.6 2.0411 4.6260 6.6670 240.4 720.22 1856.6 2576.8 721.11 2048.0 2769.1 2.0462 4.6166 6.6628 237.6 722.47 1854.7 2577.2 723,38 2046.3 2769,7 2.0513 4.6073 6.6585 82 171.46 LI161 234.9 724.70 1852.9 2577.6 725.62 2044,5 2770.2 2.0563 45981 6.6544 232.2 726.91 1851.1 2578.0 727.83 2042.8 2770.7 2.0612 4.5890 6.6502 730.04 20411 2771.2 2.0662 4.5800 6.6462 170.43 1.1148 170.95 1.1155 .80 .83 171.97 1.1168 .84 172.47 1.1174 229.5 729.10 1849.2 2578.3 732.22 2039.4 2771.6 2.0710 4.5711 6.6421 734.38 2037.7 2772.1 2.0758 4.5623 6.6381 736.52 2036.1 2772.6 2.0806 4.5536 6.6342 738.64 2034.4 2773.0 2.0853 4.5450 6.6303 2.0900 4.5364 6.6264 227.0 731.27 1847.4 2578.7 83 .86 .87 88 89 172.96 1,1181 173.46 1.1187 224.5 733.42 1845.7 2579.1 173.94 1.1193 222.0 735.55 1843.9 2579.4 174.43 1.1200 174.90 1.1206 219.6 217.3 739.75 1840.4 2580.1 740.75 2032.8 2773.5 737.66 1842.1 2579.8 215.0 175.38 1.1212 175.85 1.1218 212.7 176.31 1.1225 176.78 1:1231 177.24 1.1237 741.83 1838.6 2580.5 743.89 1836.9 2580.8 745.93 1835.2 2581.1 747.95 1833.5 2581.5 749.96 1831.8 2581.8 742.83 2031.1 2773.9 744.91 2029.5 2774.4 2.0992 4.5196 6.6188 746.96 2027.9 2774.8 2.1038 4.5113 6.6151 749.00 2026.3 2775.3 751.02 2024.7 2775.7 2.0946 4.5280 6.6226 .90 ,91 .92 .93 .94 210.5 208.4 206.3 2.1083 4.5031 6.6114 2.1127 4.4950 6.6077 177.69 1.1243 178.14 1.1249 178.59 1.1255 179.03 1.1261 179.47 1.1267 204 2 202.2 753.93 1828.5 2582.4 200.2 198.2 196.3 751.95 1830.2 2582.1 .95 ,96 97 .98 .99 755.89 1826.9 2582,7 757.84 1825.2 2583.1 759.77 1823.6 2583.4 753.02 2023.1 2776.1 2.1172 4.4869 6.6041 755.01 2021.5 2776.5 2.1215 4.4789 6.6005 756.98 2019.9 2776.9 2.1259 4.4710 6.5969 758.94 2018.4 2777.3 2.1302 4.4632 6.5934 760.88 2016.8 2777.7 2.1345 4.4555 6.5899 1.00 1.02 1.04 1.06 1,08 179.91 1.1273 194.44 180.77 1.1284 190.80 181.62 1.1296 187.30 182,46 183.28 761.68 1822.0 2583.6 765.47 1818.8 2584.2 766.63 2012.2 2778.9 769.21 1815.6 2584.8 772.89 1812.5 2585.4 776.52 1809.4 2585.9 762.81 2015.3 2778.1 770.38 2009.2 2779.6 774.08 2006.2 2780.3 777.74 2003.3 2781.0 2.1387 4.4478 6.5865 2.1471 4.4326 6.5796 2.1553 4.4177 6.5729 2.1634 4.4030 6.5664 2.1713 4.3886 6.5599 1.1308 1.1319 183.92 180.67 1.10 1.12 184.09 184.89 1.1330 1.1342 177.53 174.49 780.09 1806.3 2586.4 783.62 1803.3 2586.9 781.34 2000.4 2781.7 784.89 1997.5 2782.4 2.1792 4.3744 6.5536 2.1869 4.3605 6.5473
Transcribed Image Text:An Isobaric process is done on steam where it is heated to 200 C at 1.1 MPa. It was initially a kilogram of saturated liquid. Find the change in volume, change in internal energy, change in enthalpy, and change in entropy. (0.1848 m3, 1837.31 kJ, 2040.66 kJ, 4.4609 kJ/k) Table 3. Vapor p(t Sat.) 1.10 (184.09) 1.15 (186.07) 10 10 . Sat. 177.53 2586.4 2781.7 6.5535 170.13 2587.7 27833 6.5381 175 180 185 190 195 172.50 2567.9 2737.6 L75.28 25782 2771.0 178.02 2588.2 2784.0 180.71 2598.1 2796.9 183.36 2607.8 2809.5 6.6137 164.20 25648 2753.6 166.91 2573.2 2767.2 169 37 258SS 2780.5 172.18 2595.5 2793.5 174.75 2605.4 2806.4 6.4726 6.3028 63320 6.5603 6.5878 6.5004 63300 6.5587 6.5866 200 205 210 215 220 185.97 2617.4 2822.0 6.6401 188.56 2626.8 2834.2 6.6659 191.11 2636.1 2846.3 6.6911 193.63 2645.3 2858.3 6.7157 196.13 2654.3 2870.1 6.7398 177.28 2615.1 2819.0 179.77 2624.6 2831.4 182.24 2634.0 2843.6 184.68 2643.3 2855.7 187.09 2652.5 2867.6 6.7154 6.6146 6.6407 6.6661 6.6910 225 230 235 240 245 198.60 2663.3 2881.8 6.7634 201.05 2672.2 2893.4 6.7865 203.49 2681.0 2904.9 6.8093 205.90 2689.8 2916.3 208.30 2698.5 2927.6 189.47 2661.5 2879.4 6.7392 191.84 2670.5 2891.1 194.19 2679.4 2902.7 196.51 2688.2 2914.2 198.82 2697.0 2925.6 6.7625 6.7855 6.8080 6.8301 6.8316 6.8535 250 260 270 280 290 210.7 2707.1 2938.8 215.4 2724.2 2961.1 220.1 2741.1 2983.2 224.7 2757.9 3005.1 229.3 2774.6 3026.9 6.8751 6.9174 6.9584 6.9984 7.0373 201.1 2705.7 2936.9 205.7 2722.9 2959.4 210.2 2739.9 2981.6 214.6 2756.8 3003.6 219.0 2773.6 3025.4 6.8518 6.8943 6.9356 6.9757 7.0149 Enthalpy Entropy Specific Volume Sat, Sat. Liquid Vapor 10v 10, Internal Energy Sat, Liquid Tep Sat. Vapor Sat. Liquid Sat. Vapor Sat. 1Jquid Sat. Vapor Evap. Evap. Evap. Press MP h/ h h, u u, s, 708.64 1866.1 2574.7 109.47 2057.0 2766.4 2.0200 4.6647 6.6847 255.6 252.4 711.00 1864.2 2575.2 711.85 2055.2 2767.0 2.0253 4.6549 6.6802 249.3 713.34 1862.2 25S75.6 714.20 2053.4 2767.5 2.0306 4.6451 6.6758 246.3 715.66 1860.3 25576.0 716.52 2051.6 2768.1 2.0359 4.6355 6.6714 243.3 167.78 1.115 .75 .76 .77 .78 .79 168.32 L1121 168.86 1.1128 169.39 1.1135 169.91 11142 717.95 1858.5 2576.4 718.83 2049.8 2768.6 2.0411 4.6260 6.6670 240.4 720.22 1856.6 2576.8 721.11 2048.0 2769.1 2.0462 4.6166 6.6628 237.6 722.47 1854.7 2577.2 723,38 2046.3 2769,7 2.0513 4.6073 6.6585 82 171.46 LI161 234.9 724.70 1852.9 2577.6 725.62 2044,5 2770.2 2.0563 45981 6.6544 232.2 726.91 1851.1 2578.0 727.83 2042.8 2770.7 2.0612 4.5890 6.6502 730.04 20411 2771.2 2.0662 4.5800 6.6462 170.43 1.1148 170.95 1.1155 .80 .83 171.97 1.1168 .84 172.47 1.1174 229.5 729.10 1849.2 2578.3 732.22 2039.4 2771.6 2.0710 4.5711 6.6421 734.38 2037.7 2772.1 2.0758 4.5623 6.6381 736.52 2036.1 2772.6 2.0806 4.5536 6.6342 738.64 2034.4 2773.0 2.0853 4.5450 6.6303 2.0900 4.5364 6.6264 227.0 731.27 1847.4 2578.7 83 .86 .87 88 89 172.96 1,1181 173.46 1.1187 224.5 733.42 1845.7 2579.1 173.94 1.1193 222.0 735.55 1843.9 2579.4 174.43 1.1200 174.90 1.1206 219.6 217.3 739.75 1840.4 2580.1 740.75 2032.8 2773.5 737.66 1842.1 2579.8 215.0 175.38 1.1212 175.85 1.1218 212.7 176.31 1.1225 176.78 1:1231 177.24 1.1237 741.83 1838.6 2580.5 743.89 1836.9 2580.8 745.93 1835.2 2581.1 747.95 1833.5 2581.5 749.96 1831.8 2581.8 742.83 2031.1 2773.9 744.91 2029.5 2774.4 2.0992 4.5196 6.6188 746.96 2027.9 2774.8 2.1038 4.5113 6.6151 749.00 2026.3 2775.3 751.02 2024.7 2775.7 2.0946 4.5280 6.6226 .90 ,91 .92 .93 .94 210.5 208.4 206.3 2.1083 4.5031 6.6114 2.1127 4.4950 6.6077 177.69 1.1243 178.14 1.1249 178.59 1.1255 179.03 1.1261 179.47 1.1267 204 2 202.2 753.93 1828.5 2582.4 200.2 198.2 196.3 751.95 1830.2 2582.1 .95 ,96 97 .98 .99 755.89 1826.9 2582,7 757.84 1825.2 2583.1 759.77 1823.6 2583.4 753.02 2023.1 2776.1 2.1172 4.4869 6.6041 755.01 2021.5 2776.5 2.1215 4.4789 6.6005 756.98 2019.9 2776.9 2.1259 4.4710 6.5969 758.94 2018.4 2777.3 2.1302 4.4632 6.5934 760.88 2016.8 2777.7 2.1345 4.4555 6.5899 1.00 1.02 1.04 1.06 1,08 179.91 1.1273 194.44 180.77 1.1284 190.80 181.62 1.1296 187.30 182,46 183.28 761.68 1822.0 2583.6 765.47 1818.8 2584.2 766.63 2012.2 2778.9 769.21 1815.6 2584.8 772.89 1812.5 2585.4 776.52 1809.4 2585.9 762.81 2015.3 2778.1 770.38 2009.2 2779.6 774.08 2006.2 2780.3 777.74 2003.3 2781.0 2.1387 4.4478 6.5865 2.1471 4.4326 6.5796 2.1553 4.4177 6.5729 2.1634 4.4030 6.5664 2.1713 4.3886 6.5599 1.1308 1.1319 183.92 180.67 1.10 1.12 184.09 184.89 1.1330 1.1342 177.53 174.49 780.09 1806.3 2586.4 783.62 1803.3 2586.9 781.34 2000.4 2781.7 784.89 1997.5 2782.4 2.1792 4.3744 6.5536 2.1869 4.3605 6.5473
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