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1. A steam pouwer plant operetes uing the ideal Rankine Cycle where 'steam initially enter the turkin ott 5.0 MPa and 400 c then condenses at 7kPa and enkonetham exits as saturated. liquid Daw the IS diagram f efticienay, and steam rode. after expandingi Find the thermal.

1. A steam pouwer plant operetes uing the ideal Rankine Cycle where 'steam initially enter the turkin ott 5.0 MPa and 400 c then condenses at 7kPa and enkonetham exits as saturated. liquid Daw the IS diagram f efticienay, and steam rode. after expandingi Find the thermal.

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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Saturation: Pressures Specifie Volume Sa Internal Energy Sal Ligule Entropy Set. Ligurd Enthalpy Pr Tegp Ligld 10, Sat. Vaper Sal. Liquid Sat Veper Sat. Vapor Erap Er 10 DO06113 .0007 COC3 .co09 01 1.0002 206 136 1.89 1.0001 181 255 3.77 1.0001 159 675 5.45- 1.0001 142 789 00 2.75.3 23753 7.90 23700 2377.9 15.81 2364.7 23806 22.88 23600 2382.9 · O1 25013 2501.4 7.91 24969 2504 8 15.81 2492.5 2508.3 22.89 2488 5 2511.4 0000 9.1562 9.1562 0288 9.0775 9,1064 0575 8.9999 9.0573 ON29 8.9312 9,0:42 .0010 0011 0012 0013 .0014 6.98 1.0002 129 208 8.37 1.0002 118 042 9.66 LO003 108 696 10.86 11.98 29.30 2355.7 2385.0 35.17 23518 2386.9 40.58 2348.1 2388.7 45.60 2344.7 23903 50.31 23416 2391.9 29.30 24849 2514.2 35.17 2481.6 2516.8 40.58 2478.6 2519.1 45.60 2475.7 25213 503I 2473.1 2523.4 1059.R8697 8.9756 1268 8.8140 8.9408 1460 8.7631 8.9091 1637 8.7162 8.8799 1802 8.6727 8.8529 1.0004 100 755 1.0005 93 922 54.71 2338.6 2393.3 58.87 2335.8 2394.7 62.80 2333.2 2396.0 66.53 2330.7 23972 70.09 2328.3 2398.4 54.71 2470.6 2525.3 58.87 2468.3 2527.1 62.80 2466.0 2528.8 66.54 2463.9 2530.5 70.10 2461.9 2532.0 .1957 8.6322 8.8279 2102 8.5943 8.8044 2238 85586 8.7825 2368 8.5250 8.7618 2491 8.4931 $.7422 1.0007 87980 1.0008 82 763 ,0015 .0016 .0017 0018 0019 13.03 14.02 14.95 1.0009 78 146 15.84 1.0010 14 030 16.69 -1.0012 70 337 .0050 0055 0060 0065 0070 32.88 1.0053 28 192 1.0058 25 769 1.0064 37.6) 1.0069 22014 10074 137.81 2282.7 24205 144.94 2277.9 24228 151.53 2273.4 2425.0 157.66 2269.J 2426.9 163.39 2265 4 2428.8 137.82 2423.7 2561.5 144.95 2419.6 2564.5 IS1.53 2415.9 2567.4 157.67 2412.4 2570.0 163.40 2409.I 2572.5 4764 7.9187 8.3951 4997 7.8616 8.3613 5210 7.8094 8.3304 5408 7,7613 8.3020 5592 1,7167 8 2758 34.58 36.16 23 739 39.00 20 530 5764 76750 8.2515 3926 7.6361 8.2287 6079 75994 8.2073 6224 7.5648 8.1872 .6362 7.5321 8.1682 40.29 1.0079- 19 238 41.51 1.0054 18 103 168,78 2261.7 2430.5 173.87 2258J 24322. 173.88 2403.1 2577.0 178.69 22550 2433.7 178.70 2400 3 2579.0 183.27 2251.9 2435.2: 183.29 2397.7 2581.0 187,64 2248.9 2436.6 168.79 2406.0 2574.8 0075 0080 0oss. 42.67 1.0089 47 099 .0090 0095 43.76 1.0094 16 203 44,81 1.0098 15 399 187.65 2395.2 2582.9 1694.0 1618.4 1549.5 14864 1428,4 417.36 2088.7 2506.1 423.13 2084.6 2507.7 428.68 20805 2509.2 434,03 2076.7 2510.7 439.20 2072.9 2512.1 41746 2258.0 2675.5 423.24 2254,4 2677.6 428.79 2250.9 2679.7 434.15 2247.5 2681.7 439 32 2244.2 2683.5 13608 5.9373 7.2981 13026 60568 7.3594 13181 6.0249 7.3430 13329 5.9944 7.3273 13471 59653 1J124 99.63 1.0432 J00 105 101.00 1.0443 .110 115 103.58 .120 104.80 1.0473 102.31 1.0453 1.0463 Table 3. Vapor 5.0 (263.99) P(t Sat.) U 261AS) 49 262.73) 10, . 39.44 2597.1 2794.3 5.9734 Sat. 41.18 2598.4 2796.0 5.9916 40.29 2597. 2795.2 5.9824 255 260 265 270 1919 2376.8 276J 10.00 21017 2700 0 190z IT5 26096 28104 6.018 42.75 2624.7 2829,9 6.0544 3.9394 38.67 2583 7 2777 19.63 2600.4 2798.6 5.9813 40.54 2616.2 2818.9 3.9411 19.77 2388 21 20.722605.12804.6 41.62 2620.5 2824.5 6.0367 5 0607 3.9999 6.0189 275 280 285 290 295 43.62 2639.1 28485 6.0885 44,46 2652.9 28663 6.1209 45.28 2666.2 2883.6 6.1519 46.07 2679.1 2900.2 6.1816 46.83 2691.6 2916.4 62102 42.45 2635.2 2843.4 6.0714 43.J3 2649.3 2861.6 6.1044 44,14 2662.8 2879.1 6.1359 44.92 2675.9 2896.0 6.1661 45.69 2688.6 2912.4 6.1951 41.41 2631. 2838.3 6.0544 42.24 2645.6 2856.8 6.0880 43,04 2659.4 2874.6 6.1201 43.82 2672.7 28918 6.1507 44.58 2685.5 2908.4 6.1801 300 310 320 330 340 47.58 2703.7 2932.1 6.2377 49.03 2727.0 2962.4 6.2902 50.43 2749.4 2991.5 6.3396 51.78 2771.0 3019.5 6.3865 53.09 2792.0 3046.8 6.4313 46.43 2700.8 2928.3 6.2230 47.86 2724.5 2959.0 6.2760 49.24 2747.1 2988.4 6.3260 50.57 2768.9 3016.7 51.87 2790.0 3044.1 45.32 2698.0 2924.5 6.2084 46.74 2721.9 2955.6 6.2621 48.10 2744,7 2985.3 6.3125 49.42 2766.7 3013.8 6.3603 50.70 2788.0 3041.5 6.4058 63733 6.4185 53.13 2810,5 3070.9 54.36 2830.7 3097.0 6.5034 55.57 2850.4 3122.7 6.5436 56.76 2869.8 3148.0 6.5825 57.93 2889.0 3172.9 51.94 2808.7 3068.4 6.4493 53.16 2828.9 3094.7 6.4912 54.35 2848.8 3120.5 6.5317 55.52 2868.3 3145.9 6.5708 56.68 2887.6 3171.0 6.6089 6.4617 350 360 370 380 390 54.37 2812.4 3073.3 6.4743 55.62 2832.4 3099.3 6.5157 56.84 2852.O 3124.8 6.5557 58.05 28713 3150.0 6.5944 59.24 2890.4 3174.8 6.6321 6.6204 60.41 2909.3 3199.3 6.6688 61.57 2928.0 3223.6 6.7046 62.72 2946.6 3247.7 6.7396 63,85 2965.1 3271.6 6.7739 64.98 2983.5 32954 403 410 59.09 2908.0 3197.5 6.6572 60.23 2926.8 3221.9 6.6932 61.35 2945.4 3246.0 6.7283 62.47 2963.9 3270.0 6.7627 63.57 2982.4 3293.9 6.7964 57.81 2906.6 3195,7 58.93 2925.5 3220.2 6.6820 60.04 2944.2 3244.4 6.7172 61.14 2962.8 3268.5 62.23 29813 3292.4 6.6459 435 443 6.7517 6.7855 6.8075 10.0 (311.06) 10.2 (312.52) P(t Sat.) 10', 10', 18.026 2544.4 2724.7 5.6141 17.588 2541.6 2721.0. 5.6017 Sat. 305 17.864 2338.3 2717.1 3.6011 18.593 2565.1 27510 5.6589 19.253 2588.8 2781.3 5.7103 17.197 25269 27023 S 5697 310 T7.950 2555.T 2738.2 5.6309 315 5.6848 18.626 2580.0 2770.0 320 19.861 2610.4 2809.1 20.429 2630.4 2834.7 5.7996 20.964 2649.1 2858.7 5.8392 21.472 2666.6 2881.4 5.8763 21.957 2683.3 2902.9 5.9112 19.244 2602.5 2798,8 19.819 2623.2.2825.4 5.7174 330 20.358 2642.5 2850.1 5.8183 335 20.869 2660.6 2873.4 5.8564 340 21.355 2677.5 2895.5 5.3922 5.7568 5.7332 325 345 21.82 2693.9 2916.5 5.9261 22.70 2724.4 2955.9 5.9889 22.42 2699.2 2923.4 5.9443 23.31 2729.1 2962.1 6.0060 24.14 2756.9 2998.3 6.0626 24.93 2783.2 3032.5 6.1154 25.68 2808.3 3065.1 6.1650 350 360 23.53 2752.7 2992.7 6.0465 24.31 2779.4 3027.4 6.1000 25.06 2804.8 3060.4 6.1503 370 380 390 26.41 2832.4 3096.5 5.2120 27.11 2855.7 3126.8 6.2567 27.80 2878.4 3156.3 6.2995 28.46 2900,4 3185.1 6.3407 29.11 2922.1 3213.2 6.3805 25.78 2829.1 3092.1 6.1977 26.48 2852.7 3122.8 6.2429 27.16 2875.5 3152.5 6.2861 400 410 420 430 6.3677. 440 28.46 2919.6 3209.9
Transcribed Image Text:Saturation: Pressures Specifie Volume Sa Internal Energy Sal Ligule Entropy Set. Ligurd Enthalpy Pr Tegp Ligld 10, Sat. Vaper Sal. Liquid Sat Veper Sat. Vapor Erap Er 10 DO06113 .0007 COC3 .co09 01 1.0002 206 136 1.89 1.0001 181 255 3.77 1.0001 159 675 5.45- 1.0001 142 789 00 2.75.3 23753 7.90 23700 2377.9 15.81 2364.7 23806 22.88 23600 2382.9 · O1 25013 2501.4 7.91 24969 2504 8 15.81 2492.5 2508.3 22.89 2488 5 2511.4 0000 9.1562 9.1562 0288 9.0775 9,1064 0575 8.9999 9.0573 ON29 8.9312 9,0:42 .0010 0011 0012 0013 .0014 6.98 1.0002 129 208 8.37 1.0002 118 042 9.66 LO003 108 696 10.86 11.98 29.30 2355.7 2385.0 35.17 23518 2386.9 40.58 2348.1 2388.7 45.60 2344.7 23903 50.31 23416 2391.9 29.30 24849 2514.2 35.17 2481.6 2516.8 40.58 2478.6 2519.1 45.60 2475.7 25213 503I 2473.1 2523.4 1059.R8697 8.9756 1268 8.8140 8.9408 1460 8.7631 8.9091 1637 8.7162 8.8799 1802 8.6727 8.8529 1.0004 100 755 1.0005 93 922 54.71 2338.6 2393.3 58.87 2335.8 2394.7 62.80 2333.2 2396.0 66.53 2330.7 23972 70.09 2328.3 2398.4 54.71 2470.6 2525.3 58.87 2468.3 2527.1 62.80 2466.0 2528.8 66.54 2463.9 2530.5 70.10 2461.9 2532.0 .1957 8.6322 8.8279 2102 8.5943 8.8044 2238 85586 8.7825 2368 8.5250 8.7618 2491 8.4931 $.7422 1.0007 87980 1.0008 82 763 ,0015 .0016 .0017 0018 0019 13.03 14.02 14.95 1.0009 78 146 15.84 1.0010 14 030 16.69 -1.0012 70 337 .0050 0055 0060 0065 0070 32.88 1.0053 28 192 1.0058 25 769 1.0064 37.6) 1.0069 22014 10074 137.81 2282.7 24205 144.94 2277.9 24228 151.53 2273.4 2425.0 157.66 2269.J 2426.9 163.39 2265 4 2428.8 137.82 2423.7 2561.5 144.95 2419.6 2564.5 IS1.53 2415.9 2567.4 157.67 2412.4 2570.0 163.40 2409.I 2572.5 4764 7.9187 8.3951 4997 7.8616 8.3613 5210 7.8094 8.3304 5408 7,7613 8.3020 5592 1,7167 8 2758 34.58 36.16 23 739 39.00 20 530 5764 76750 8.2515 3926 7.6361 8.2287 6079 75994 8.2073 6224 7.5648 8.1872 .6362 7.5321 8.1682 40.29 1.0079- 19 238 41.51 1.0054 18 103 168,78 2261.7 2430.5 173.87 2258J 24322. 173.88 2403.1 2577.0 178.69 22550 2433.7 178.70 2400 3 2579.0 183.27 2251.9 2435.2: 183.29 2397.7 2581.0 187,64 2248.9 2436.6 168.79 2406.0 2574.8 0075 0080 0oss. 42.67 1.0089 47 099 .0090 0095 43.76 1.0094 16 203 44,81 1.0098 15 399 187.65 2395.2 2582.9 1694.0 1618.4 1549.5 14864 1428,4 417.36 2088.7 2506.1 423.13 2084.6 2507.7 428.68 20805 2509.2 434,03 2076.7 2510.7 439.20 2072.9 2512.1 41746 2258.0 2675.5 423.24 2254,4 2677.6 428.79 2250.9 2679.7 434.15 2247.5 2681.7 439 32 2244.2 2683.5 13608 5.9373 7.2981 13026 60568 7.3594 13181 6.0249 7.3430 13329 5.9944 7.3273 13471 59653 1J124 99.63 1.0432 J00 105 101.00 1.0443 .110 115 103.58 .120 104.80 1.0473 102.31 1.0453 1.0463 Table 3. Vapor 5.0 (263.99) P(t Sat.) U 261AS) 49 262.73) 10, . 39.44 2597.1 2794.3 5.9734 Sat. 41.18 2598.4 2796.0 5.9916 40.29 2597. 2795.2 5.9824 255 260 265 270 1919 2376.8 276J 10.00 21017 2700 0 190z IT5 26096 28104 6.018 42.75 2624.7 2829,9 6.0544 3.9394 38.67 2583 7 2777 19.63 2600.4 2798.6 5.9813 40.54 2616.2 2818.9 3.9411 19.77 2388 21 20.722605.12804.6 41.62 2620.5 2824.5 6.0367 5 0607 3.9999 6.0189 275 280 285 290 295 43.62 2639.1 28485 6.0885 44,46 2652.9 28663 6.1209 45.28 2666.2 2883.6 6.1519 46.07 2679.1 2900.2 6.1816 46.83 2691.6 2916.4 62102 42.45 2635.2 2843.4 6.0714 43.J3 2649.3 2861.6 6.1044 44,14 2662.8 2879.1 6.1359 44.92 2675.9 2896.0 6.1661 45.69 2688.6 2912.4 6.1951 41.41 2631. 2838.3 6.0544 42.24 2645.6 2856.8 6.0880 43,04 2659.4 2874.6 6.1201 43.82 2672.7 28918 6.1507 44.58 2685.5 2908.4 6.1801 300 310 320 330 340 47.58 2703.7 2932.1 6.2377 49.03 2727.0 2962.4 6.2902 50.43 2749.4 2991.5 6.3396 51.78 2771.0 3019.5 6.3865 53.09 2792.0 3046.8 6.4313 46.43 2700.8 2928.3 6.2230 47.86 2724.5 2959.0 6.2760 49.24 2747.1 2988.4 6.3260 50.57 2768.9 3016.7 51.87 2790.0 3044.1 45.32 2698.0 2924.5 6.2084 46.74 2721.9 2955.6 6.2621 48.10 2744,7 2985.3 6.3125 49.42 2766.7 3013.8 6.3603 50.70 2788.0 3041.5 6.4058 63733 6.4185 53.13 2810,5 3070.9 54.36 2830.7 3097.0 6.5034 55.57 2850.4 3122.7 6.5436 56.76 2869.8 3148.0 6.5825 57.93 2889.0 3172.9 51.94 2808.7 3068.4 6.4493 53.16 2828.9 3094.7 6.4912 54.35 2848.8 3120.5 6.5317 55.52 2868.3 3145.9 6.5708 56.68 2887.6 3171.0 6.6089 6.4617 350 360 370 380 390 54.37 2812.4 3073.3 6.4743 55.62 2832.4 3099.3 6.5157 56.84 2852.O 3124.8 6.5557 58.05 28713 3150.0 6.5944 59.24 2890.4 3174.8 6.6321 6.6204 60.41 2909.3 3199.3 6.6688 61.57 2928.0 3223.6 6.7046 62.72 2946.6 3247.7 6.7396 63,85 2965.1 3271.6 6.7739 64.98 2983.5 32954 403 410 59.09 2908.0 3197.5 6.6572 60.23 2926.8 3221.9 6.6932 61.35 2945.4 3246.0 6.7283 62.47 2963.9 3270.0 6.7627 63.57 2982.4 3293.9 6.7964 57.81 2906.6 3195,7 58.93 2925.5 3220.2 6.6820 60.04 2944.2 3244.4 6.7172 61.14 2962.8 3268.5 62.23 29813 3292.4 6.6459 435 443 6.7517 6.7855 6.8075 10.0 (311.06) 10.2 (312.52) P(t Sat.) 10', 10', 18.026 2544.4 2724.7 5.6141 17.588 2541.6 2721.0. 5.6017 Sat. 305 17.864 2338.3 2717.1 3.6011 18.593 2565.1 27510 5.6589 19.253 2588.8 2781.3 5.7103 17.197 25269 27023 S 5697 310 T7.950 2555.T 2738.2 5.6309 315 5.6848 18.626 2580.0 2770.0 320 19.861 2610.4 2809.1 20.429 2630.4 2834.7 5.7996 20.964 2649.1 2858.7 5.8392 21.472 2666.6 2881.4 5.8763 21.957 2683.3 2902.9 5.9112 19.244 2602.5 2798,8 19.819 2623.2.2825.4 5.7174 330 20.358 2642.5 2850.1 5.8183 335 20.869 2660.6 2873.4 5.8564 340 21.355 2677.5 2895.5 5.3922 5.7568 5.7332 325 345 21.82 2693.9 2916.5 5.9261 22.70 2724.4 2955.9 5.9889 22.42 2699.2 2923.4 5.9443 23.31 2729.1 2962.1 6.0060 24.14 2756.9 2998.3 6.0626 24.93 2783.2 3032.5 6.1154 25.68 2808.3 3065.1 6.1650 350 360 23.53 2752.7 2992.7 6.0465 24.31 2779.4 3027.4 6.1000 25.06 2804.8 3060.4 6.1503 370 380 390 26.41 2832.4 3096.5 5.2120 27.11 2855.7 3126.8 6.2567 27.80 2878.4 3156.3 6.2995 28.46 2900,4 3185.1 6.3407 29.11 2922.1 3213.2 6.3805 25.78 2829.1 3092.1 6.1977 26.48 2852.7 3122.8 6.2429 27.16 2875.5 3152.5 6.2861 400 410 420 430 6.3677. 440 28.46 2919.6 3209.9
1. A steam power plant Dperates uing The ideal Rankine Cycle where 'steam initially enteo the turking ott 5.0 uPa and 400 c then condenses at 7kPa and enteradhi exits as saturated liquid- Draw the IS diagram find the thermal efticienay, and steam rate. after expanding t
Transcribed Image Text:1. A steam power plant Dperates uing The ideal Rankine Cycle where 'steam initially enteo the turking ott 5.0 uPa and 400 c then condenses at 7kPa and enteradhi exits as saturated liquid- Draw the IS diagram find the thermal efticienay, and steam rate. after expanding t
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