Steam undergoes an Isentropic process where it is initially at 1.05 MPaand 304C. The isentropic process causes its pressure to drop to 30 kPa. Findthe tsat2, dryness, and enthalpy change. (69.10C, 90.4%, -657.34 kJ/kg)1.05 (18204)(t Sat.)LO (179.91)10v10' v194.44 2583.6 2778.16.5865185.60 2585.I 2780.06.5696Sat.150155179.07 2332.0 2711.J 6.4342182.29 2542.9 2725.1 6.4669183.43 2553.4 2738.9 6.4984188.50 2563.8 2752.3172.60 2539.2 2720.4 6.4336175.66 2550.0 2734.5 6.4678178.64 2560.6 2748.2 6.49891601651706.3289191.33 2573.9 2765.4 6.5584194.50 2583.8 2778.3 6.5870197.42 2593.6 2791.0 6.6148200.30 2603.2 2803.5 6.6419203.15 2612.6 2815.8 6.66821751801851901956.5289181.36 2570.9 2761.6184.44 258LO 2774.7 6.5580187.26 2590.9 2787.5 6.5863190.04 2600.7 2800.2192.79 2610.2 2812.76.61376.6405206.0 2621.9 2827.9 6.6940211.5 2640.2 2851.7 6.7437216.9 2658.0 2874.9 6.7914222.2 2675.6 2897.8 6.8374227.5 2692.9 2920.45.6666195.49 2619.7 2824.9200.81 2638.1 2849.0 6.7169206.02 2656.2 2872.5 6.7651211.14 2673.9 2895.6216.18 2691.3 2918.32002102202302406.81146.85616.8817232.7 2709.9 2942.6 6.9247237.8 2726.8 2964.6 6.9664242.9 2743.6 2986.5 7.0069248.0 2760.2 3008.2 7.0465253.0 2776.7 3029.7 7.08516.89946.9414221.2 2708.5 2940.7226.1 2725.5 2962.9231.0 2742.3 2984.8 6.9822235.8 2759.1 3006.6 7.0219240.6 2775.7 3028.3 7.0607250260270280290257.9 2793.2 3051.2 7.1229262.9 2809.7 3072.6267.8 2826.1 3093.9272.7 2842.5 3115.2277.6 2858.8 3136.47.15997.19627.23187.2667245.3 2792.2 3049.8 7.0986250.1 2808.7 3071.3 7.1358254.8 2825.2 3092.7259.5 2841.6 3114.1 7.2079264.1 2858.0 3135.43003103203303407.17227.2429Specific VolumeInternal EnergyEnthalpyEntropyBelSet.VaparProSat.VaperSat.LiguidSatVapeSatLiidHel.VapomEvep.10'v,EvapEap10,h.64.9765AS02510199620459803772.5579.5398271.90 21912 2463.1271.93 2346.3 2618.2275.61 2344.1 2619.7279.17 2342 0 2621 2282 62 23400 26226285 98 23360 2624.08931 6.9383 183149040 69139 781799145 6.8904 7.80499246 68678 1,79249344 6.8459 7.7803LO204027279.14 2186 2 2465 3282.60 2183.8 2466 4285.95 2181 S 2467.466.70 1.020967.5310214A2968.331.02181.022370.60 1.023210241102491.0257289 23 2336.I 2625.3295.48 2332.4 2627.8301 40 23288 2630 2307.05 2325.5 2632.5312.43 2322.3 2634.769.1052294922.650.4403289.20 2179.2 2468.4295 45 2174.9 24703J01 37 2170.8 2412.1307.01 2166.8 2473 8312.39 2163.I 2475.59439 6.8247 7.76869622 6.7843 1.74659193 6.7463 1.72579956 6.7104 7.703472.0173.3674.644190.10111 6.6764 7.6876 An Isobaric process is done on steam where it is heated to 200 C at 1.1MPa. It was initially a kilogram of saturated liquid. Find the change involume, change in internal energy, change in enthalpy, and change inentropy. (0.1848 m3, 1837.31 kJ, 2040.66 kJ, 4.4609 kJ/k)Table 3. Vaporpt Sat.)1.10 (I4.09)1.15 (I6.07)10Set.177.53 2586.4 2781.76.5535170.13 2587.7 278336.53811751001851901954.4726172 50 2547.9 2757.6175.28 2572 27710178.02 25882 2784.0 6.3387180.71 2598.1 2796.9183.36 2607. 2809.514.20 2564 27336164.91 25732 2767.2 3028L69.37 23835 274056.50046.58666.6137636036.5878174.75 2605.4 2806.4200205210215220185.97 2617.4 2822.0 6.6401188.56 2626.8 2834.2 6.6659191.11 2636.1 2846.3193.63 2645 3 28583196.13 2654.3 2870.16.69116.71576.7398177.28 2615.1 2819.0 6.6146179.77 2624.6 28314 6.6407182.24 2634.0 2843.6 6.6661184.68 2643.3 2855.7 6.6910187.09 2652.5 2867.6 6.7154225230235240245198.60 2663.3 28818 6.7634201.05 2672.2 2893.4 6.7865203.49 2681.0 2904.9 6.8093 194.19 2679.4 2902.7205.90 2689.8 2916.3 6.8316208.30 2698.5 2927.6 6.8535189.47 2661.5 2879.4 6.7392191 84 2670.5 2891.1196.51 2688.2 2914.2198 82 2697.0 2925.66.76256.78556.80806.8301250260270280290210.7 2707.1 2938.8 6.8751215.4 2724.2 2961.1 6.9174220.1 2741.1 2983.2 6.9584224.7 2757.9 3005.1 6.9984201.1 2705.7 2936.9205.7 2722.9 2959 4 6.8943210.2 2739.9 2981.6 6.9356214.6 2756.8 3003.6 6.9757219.0 2773.6 3025.4 7.014968518229.3 2774.6 3026.9 7.0373Specifie VelumeInternal KnergyEnthalpyEMrepyLindVapEpLigdT08 64 IB66I 25747T 00 I842 2575 21134 18622 2575671366 I860.3 2576.071795 1858S 25744J09 47 20570 2766 4T1I85 20552 21670T14.20 2053.4 27675716.52 20516 27681718 2049 216862.0200 46647 6.68472.0253 46549 648022010 4.45I 6.67582.0159 46155 6.67142.0411 4.626e 6 6670LISL121167758.321.56251.6212 42493246.3243.375LI135142721 11 2048 O 27691123.38 2046.3 27693725.62 2044S 2770.2727.6) 20428 2770.7730 04 2041I 277122.0462 46166 6.66282.0513 4.6073 665852.0563 45I 665442.0612 4.5890 645022.0662 45800 66462LI148I043170.95171 45171.9717247 1.1I1424042376234.92322229.5120.22 18566 25768722 47 1854,7 25772724.70 1852.9 25776726 91 1851I 2578.0729.10 18492 257834.116114172 96173.46 1.1187173.942270224.52220731.27 1843.4 25787733.42 1845.7 2579.1735.55 18439 2379.4737.64 18421 2519.8739.75 1840.4 2580.1732.22 2039.4 27714734.38 2037.7 2772.1136.52 2036.1 2772.6138.64 2034.4 2773.0740.75 2032 8 2773.520710 45711 6642120758 45423 6.63812.0806 4.5536 6.63422.0853 4.5450 6.630)2.0900 4.5344 66264L19)L.1200174 432196211.3174.90L.1206175.3817585 11218L1225213.0212.72105208 4206.374283 2031.1 27739744.91 2029.5 2774.4746.96 2027 9 2774.8749.00 2026.3 2775.3751.02 2024.T 2775.72.0946 4.5280 662262.0992 45196 6.61882.1038 43113 661512.108) 4.5031 6611421127 4.4950 6.6077.9091L121214183 18386 25805743.89 1836.9 25808745.93 1835.2 2581.1747.95 1833.5 2581.5749.96 1831A 2581.8176 3111231.9394176. 74177.24 1.1237.95969717769178.14178 5917903179 47L1243L124911255L12611 12672042202.2200.2198.2751.95 1830.2 2582.1753.93 1828.5 25824755.89 1826.9 2582.7157.84 I825.2 25831759.13 I823.6 25834753.02 2023.1 2776.1755.01 2021 5 2776.5756.98 2019.9 27769758.94 2018 4 2177.3760.88 2016.8 2777.72.1172 4.4869 6.60412.1215 44789 6.60052.1259 4.4710 6.5969632 6 59342.1345 4.4555 6.58999919631.00179.911.1273761.68 1822.0 2583.6765,47 1818.8 2584.2769.21 18156 2584 8772.89 1812 5 25854776.52 1B09 4 2585.9194.44LI28418162 1.1296182.4676281 2015.3 2778.1766.63 2012.2 2778.9770.38 2009 2 27796774.08 2006 2 2780.3771.14 2003. 278102.1387 4447S 6.58652.1471 44326 6.57962.1553 4.4177 657292.1634 4.4030 6.56642.1713 4.3886 6.5599180.77190 80187.30183.92180.67L04113081.8183.24L1319184 09184.89L.133011342177.53174.49780.09 1806.) 2586.4783.62 I8033 2586.9781.34 20004 27817784 89 1991 5 2782.42.1792 4.3144 6.55162.1869 4.3605 6.54731.12

Given:P1=1.05 MPaT1=304°CP2=30 KPa

Steam undergoes an Isentropic process where it is initially at 1.05 MPa and 304C. The isentropic process causes its pressure to drop to 30 kPa. Find the tsat2, dryness, and enthalpy change. (69.10C, 90.4%, -657.34 kJ/kg) LO (179.91) 1.05 (182.04) (L Sat.) 10 v 10 194.44 2583.6 2778.1 6.5865 185.60 2585.I 2780.0 6.5696 Sat. 150 179.07 2532.0 2711 6.4342 182 29 2542.9 2725.1 6.4669 183.43 2553.4 2738.9 6.4984 188 50 25638 2752.3 6.3289 155 160 175.66 2550 0 2734.5 6.4678 165 178.64 2560.6 2748 2 6.4989 170 172.60 2539.2 2720.4 6.4356 19153 2573.9 27654 194 50 2583.8 2778.3 6.5870 197.42 2593.6 2791.0 200.30 2603.2 2803.5 6.5584 181.36 2570.9 2761.6 65289 175 180 185 184.44 2581O 2774.7 6.6148 6.6419 6.3380 187.26 2590.9 2787.5 6.5863 190.04 2600.7 2800.2 6.6137 6405 190 194

Steam undergoes an Isentropic process where it is initially at 1.05 MPa and 304C. The isentropic process causes its pressure to drop to 30 kPa. Find the tsat2, dryness, and enthalpy change. (69.10C, 90.4%, -657.34 kJ/kg) LO (179.91) 1.05 (182.04) (L Sat.) 10 v 10 194.44 2583.6 2778.1 6.5865 185.60 2585.I 2780.0 6.5696 Sat. 150 179.07 2532.0 2711 6.4342 182 29 2542.9 2725.1 6.4669 183.43 2553.4 2738.9 6.4984 188 50 25638 2752.3 6.3289 155 160 175.66 2550 0 2734.5 6.4678 165 178.64 2560.6 2748 2 6.4989 170 172.60 2539.2 2720.4 6.4356 19153 2573.9 27654 194 50 2583.8 2778.3 6.5870 197.42 2593.6 2791.0 200.30 2603.2 2803.5 6.5584 181.36 2570.9 2761.6 65289 175 180 185 184.44 2581O 2774.7 6.6148 6.6419 6.3380 187.26 2590.9 2787.5 6.5863 190.04 2600.7 2800.2 6.6137 6405 190 194

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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