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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)

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)

Principles of Heat Transfer (Activate Learning with these NEW titles from Engineering!)
Principles of Heat Transfer (Activate Learning with these NEW titles from Engineering!)
8th Edition
ISBN:9781305387102
Author:Kreith, Frank; Manglik, Raj M.
Publisher:Kreith, Frank; Manglik, Raj M.
Chapter8: Natural Convection
Section: Chapter Questions
Problem 8.19P
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Read the instructions carefully and write your COMPLETE solution on a piece of paper. Use the Steam Tables provided.
 
Entropy Enthaipy Specifie Volume Sal Internal Energy Sat Vayur Sal. Sel Teme Ligued Evag Erp Ver Pres inde 10 209 47 2057.0 2766 4 711.85 2055.2 27670 2.0253 46549 6.6802 714.20 2053.4 27675 2.0306 4.6451 6.6758 716.52 2051 6 27681 20359 46355 6.6714 718.83 2049.8 2168.6 20411 46260 6.6670 20200 4.6647 6.6847 167.78 LIIS 168.32 L1121 168 86 L1128 169 39 11135 255.6 252 4 249.3 246.3 2433 708.64 1866.1 2574.7 711.00 1864 2 2575.2 713.34 18622 25756 715.66 18603 2576.0 717.95 1858.5 2576.4 75 76 169 91 142 170.43 LI148 170.95 1I155 171 46 1116I 171.97 11168 172.47 1.174 240 4 2376 234.9 2322 229.5 720.22 1856.6 25768 722.47 1854.7 25772 724.70 I8529 25776 72691 1851. 2578.0 729.10 1849 2 2578.3 721.11 2048.O 2769.1 20462 46166 6.6628 723, 38 2046.3 2769 7 2OS13 4.6073 6.6585 725.62 2044.5 27702 20563 45981 6.6544 727.83 2042.8 2770.7 2.0612 4.5890 6.6302 730.04 2041. 27712 2.0662 4.5800 6.6462 82 .84 731.27 1847.4 2578.7 733.42 I845.7 2579.1 734.38 2037.7 2772.1 207S8 45623 6.6381 735.55 1843.9 2579 4 736.52 2036.1 2772.6 2.0806 4.5536 66342 737.66 1842.1 2579 8 738.64 2034 4 2773.0 2.08S3 4.5450 6.6303 739.75 1840 4 2580.1 732.22 2039.4 2771.6 2.0710 45711 6.6421 172.96 11181 173 46 LII87 36 173.94 1.193 174.43 1.1200 174.90 1.1206 2270 2245 222.0 2196 2113 38 740.75 2032.8 2773.5 2.0900 4.1364 66264 741.83 1838.6 2580.5 743 89 1836.9 2580.8 745.93 1835 2 2581.1 747.95 1833.5 25815 749.96 18318 2581.8 742 83 2031.1 27739 2.0946 4.5280 6.6226 744.91 2029.5 2774.4 2.0992 43196 6.6188 746.96 20279 2774.8 2.1038 45113 66151 749.00 2026.3 2775.3 2.1083 45031 66114 751.02 2024,7 27757 2 1127 44950 6.6077 175 3R 1.1212 215.0 212.7 2105 208 4 2063 90 91 175 85 L.1218 92 17631 11225 93 94 177.24 11237 176.78 11231 1.1243 95 .96 97 .98 177.69 178.14 11249 178.59 1.1255 179.03 11261 179.47 11267 204 2 2022 200.2 198.2 196 3 751.95 1830 2 2582.1 753.93 1828.5 2582.4 755.89 18269 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 2776.5 756,98 2019.9 2716.9 758.94 2018 4 27773 760.88 2016.8 2777.7 2.1215 44789 6.6005 2.1259 4.4710 65969 2.1302 4.4632 6.5934 21345 4.4555 6.5899 1.00 102 1.04 L06 1.08 179.91 L1273 194.44 180.77 L1284 190.80 181.62 1.1296 187.30 182.46 11308 183.28 11319 180 67 761.68 1822.0 2583.6 765 47 1818.8 2584.2 769 21 1815.6 2584.8 770,38 2009 2 2779.6 772 89 1812.5 25854 776.52 1809 4 2585.9 76281 20153 2778.1 766.63 2012.2 2778.9 2.1387 44475 6.5865 21471 44326 65796 2.1553 44177 6.5729 2.1634 4 4030 6.5664 2.171) 43886 6.5599 183.92 774.08 2006 2 27803 777.74 2003 3 27810 1.10 L12 184.09 184.89 L1330 177.53 174.49 780.09 1806.3 2586.4 783.62 1803 3 25869 781.34 20004 27817 784.89 1997.5 2782 4 21792 43744 6.5536 2.1869 4.3605 65473 L1342
Transcribed Image Text:Entropy Enthaipy Specifie Volume Sal Internal Energy Sat Vayur Sal. Sel Teme Ligued Evag Erp Ver Pres inde 10 209 47 2057.0 2766 4 711.85 2055.2 27670 2.0253 46549 6.6802 714.20 2053.4 27675 2.0306 4.6451 6.6758 716.52 2051 6 27681 20359 46355 6.6714 718.83 2049.8 2168.6 20411 46260 6.6670 20200 4.6647 6.6847 167.78 LIIS 168.32 L1121 168 86 L1128 169 39 11135 255.6 252 4 249.3 246.3 2433 708.64 1866.1 2574.7 711.00 1864 2 2575.2 713.34 18622 25756 715.66 18603 2576.0 717.95 1858.5 2576.4 75 76 169 91 142 170.43 LI148 170.95 1I155 171 46 1116I 171.97 11168 172.47 1.174 240 4 2376 234.9 2322 229.5 720.22 1856.6 25768 722.47 1854.7 25772 724.70 I8529 25776 72691 1851. 2578.0 729.10 1849 2 2578.3 721.11 2048.O 2769.1 20462 46166 6.6628 723, 38 2046.3 2769 7 2OS13 4.6073 6.6585 725.62 2044.5 27702 20563 45981 6.6544 727.83 2042.8 2770.7 2.0612 4.5890 6.6302 730.04 2041. 27712 2.0662 4.5800 6.6462 82 .84 731.27 1847.4 2578.7 733.42 I845.7 2579.1 734.38 2037.7 2772.1 207S8 45623 6.6381 735.55 1843.9 2579 4 736.52 2036.1 2772.6 2.0806 4.5536 66342 737.66 1842.1 2579 8 738.64 2034 4 2773.0 2.08S3 4.5450 6.6303 739.75 1840 4 2580.1 732.22 2039.4 2771.6 2.0710 45711 6.6421 172.96 11181 173 46 LII87 36 173.94 1.193 174.43 1.1200 174.90 1.1206 2270 2245 222.0 2196 2113 38 740.75 2032.8 2773.5 2.0900 4.1364 66264 741.83 1838.6 2580.5 743 89 1836.9 2580.8 745.93 1835 2 2581.1 747.95 1833.5 25815 749.96 18318 2581.8 742 83 2031.1 27739 2.0946 4.5280 6.6226 744.91 2029.5 2774.4 2.0992 43196 6.6188 746.96 20279 2774.8 2.1038 45113 66151 749.00 2026.3 2775.3 2.1083 45031 66114 751.02 2024,7 27757 2 1127 44950 6.6077 175 3R 1.1212 215.0 212.7 2105 208 4 2063 90 91 175 85 L.1218 92 17631 11225 93 94 177.24 11237 176.78 11231 1.1243 95 .96 97 .98 177.69 178.14 11249 178.59 1.1255 179.03 11261 179.47 11267 204 2 2022 200.2 198.2 196 3 751.95 1830 2 2582.1 753.93 1828.5 2582.4 755.89 18269 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 2776.5 756,98 2019.9 2716.9 758.94 2018 4 27773 760.88 2016.8 2777.7 2.1215 44789 6.6005 2.1259 4.4710 65969 2.1302 4.4632 6.5934 21345 4.4555 6.5899 1.00 102 1.04 L06 1.08 179.91 L1273 194.44 180.77 L1284 190.80 181.62 1.1296 187.30 182.46 11308 183.28 11319 180 67 761.68 1822.0 2583.6 765 47 1818.8 2584.2 769 21 1815.6 2584.8 770,38 2009 2 2779.6 772 89 1812.5 25854 776.52 1809 4 2585.9 76281 20153 2778.1 766.63 2012.2 2778.9 2.1387 44475 6.5865 21471 44326 65796 2.1553 44177 6.5729 2.1634 4 4030 6.5664 2.171) 43886 6.5599 183.92 774.08 2006 2 27803 777.74 2003 3 27810 1.10 L12 184.09 184.89 L1330 177.53 174.49 780.09 1806.3 2586.4 783.62 1803 3 25869 781.34 20004 27817 784.89 1997.5 2782 4 21792 43744 6.5536 2.1869 4.3605 65473 L1342
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 pt 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 175 180 185 190 195 164 20 2364 27536 166 91 25752 2767.2 169.372585S 27403 172.18 2595.3 2793.5 174.75 2605.4 2806.4 172 30 2567.9 2737.6 6.5004 4.4726 178.02 2588.2 2784.0 180.71 2598.I 2796.9 183.36 2607.8 2809.5 O300 6.5387 6.5866 6.6137 6.3028 63320 6.5603 6.5878 200 205 210 215 220 185.97 2617.4 2822.0 6.6401 188.56 2626.8 2834.2 6.6659 191.11 2636.I 2846.3 6.6911 193.63 2645.3 2858.3 6.7157 196.13 2654.3 2870.1 177.28 2615.1 2819.0 179.77 2624.6 2831 4 6.6407 182.24 2634.0 2843.6 6.6661 184.68 2643.3 2855.7 6.6910 187.09 2652.5 2867.6 6.6146 6.7398 6.7154 225 230 235 240 245 198.60 2663.3 2881.8 201.05 26722 2893.4 203.49 2681.0 2904.9 205.90 2689.8 2916.3 208.30 2698.5 2927.6 6.7634 6.7865 6.8093 6.8316 6.8535 6.7392 6.7625 189.47 2661.5 2879.4 191.84 2670.5 2891.1 194.19 2679.4 2902.7 6.7855 196.51 2688.2 2914.2 198.82 2697.0 2925.6 6.8080 6.8301 250 260 270 280 290 210.7 2707.1 2938.8 215.4 2724.2 2961.1 220.1 2741.1I 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
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 pt 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 175 180 185 190 195 164 20 2364 27536 166 91 25752 2767.2 169.372585S 27403 172.18 2595.3 2793.5 174.75 2605.4 2806.4 172 30 2567.9 2737.6 6.5004 4.4726 178.02 2588.2 2784.0 180.71 2598.I 2796.9 183.36 2607.8 2809.5 O300 6.5387 6.5866 6.6137 6.3028 63320 6.5603 6.5878 200 205 210 215 220 185.97 2617.4 2822.0 6.6401 188.56 2626.8 2834.2 6.6659 191.11 2636.I 2846.3 6.6911 193.63 2645.3 2858.3 6.7157 196.13 2654.3 2870.1 177.28 2615.1 2819.0 179.77 2624.6 2831 4 6.6407 182.24 2634.0 2843.6 6.6661 184.68 2643.3 2855.7 6.6910 187.09 2652.5 2867.6 6.6146 6.7398 6.7154 225 230 235 240 245 198.60 2663.3 2881.8 201.05 26722 2893.4 203.49 2681.0 2904.9 205.90 2689.8 2916.3 208.30 2698.5 2927.6 6.7634 6.7865 6.8093 6.8316 6.8535 6.7392 6.7625 189.47 2661.5 2879.4 191.84 2670.5 2891.1 194.19 2679.4 2902.7 6.7855 196.51 2688.2 2914.2 198.82 2697.0 2925.6 6.8080 6.8301 250 260 270 280 290 210.7 2707.1 2938.8 215.4 2724.2 2961.1 220.1 2741.1I 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
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