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complete and clear units/conversion factors. Box your final answer and round to the nearest 2 decimal places. Thank you

complete and clear units/conversion factors. Box your final answer and round to the nearest 2 decimal places. Thank you

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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1. A Rankine cycle is use turbine at 2·25 Mpa and 300 c then exits at 0.0 25 MPa. The puump receives For a steam powor plant . Liqud First enters the saturated liquid trom the condener bepore sending it to the boiler at the ariginal pressure . a. Draw the T-s diagram b. Find the dry ness at turbine exit C. Wp d. Qa e. Qr f. Wr h. EFFiciency ( l-) i: Steam rate ( kg/ kwn) Anewer choices ° lo0%, 3.12 ku/kg, 4.63 kg/kwh 3016.3 kJ/kg, 234 ce.3 kJ/kg, 5 2 2 . 3 ku/ kg, 3522 % 96:21* , 2.21 kJ/kg, 2809.6 ki/kg, 1875.21 k/kg, e15.33 kJ. 31 . 29°%, 3.5) kg/k Wh 83.73°, 2.21 ku/ kg, 2742.1 k/kg, 1964.48 kJ/ kq. 119.89 ku/kg 2P:36°%, 4.03kg/ kWh lo0 'l• , o k/kg, 3016.3 kJ/ kg, 21 -G a ku /kg, 2798 kJ/tg, lo0%, 1 kg/kwh
Transcribed Image Text:1. A Rankine cycle is use turbine at 2·25 Mpa and 300 c then exits at 0.0 25 MPa. The puump receives For a steam powor plant . Liqud First enters the saturated liquid trom the condener bepore sending it to the boiler at the ariginal pressure . a. Draw the T-s diagram b. Find the dry ness at turbine exit C. Wp d. Qa e. Qr f. Wr h. EFFiciency ( l-) i: Steam rate ( kg/ kwn) Anewer choices ° lo0%, 3.12 ku/kg, 4.63 kg/kwh 3016.3 kJ/kg, 234 ce.3 kJ/kg, 5 2 2 . 3 ku/ kg, 3522 % 96:21* , 2.21 kJ/kg, 2809.6 ki/kg, 1875.21 k/kg, e15.33 kJ. 31 . 29°%, 3.5) kg/k Wh 83.73°, 2.21 ku/ kg, 2742.1 k/kg, 1964.48 kJ/ kq. 119.89 ku/kg 2P:36°%, 4.03kg/ kWh lo0 'l• , o k/kg, 3016.3 kJ/ kg, 21 -G a ku /kg, 2798 kJ/tg, lo0%, 1 kg/kwh
2.30 (217.29) 225 (218.45) p(t Sat.) 10 v 10 90.73 2601.7 2801.3 6.3056 88.75 2602.0 2801.7 6.2972 Set. 86.71 25715 2762.2 6.2248 88.38 2584.I 2778.5 6.2587 90.01 2596.3 2794.3 6.2912 91.38 2608.1 2809.5 6.3223 200 205 86.06 25813 2774.9 6.2423 210 87.66 2593.7 2790.9 6.2753 215 89.23 2605.7 2806.4 6.3068 220 93.12 2619.5 2824.4 6.3523 94.63 2630.7 2838.9 6.3812 92.23 2628.6 2836.1 6.3664 96.10 2641.6 2853.0 6.4092 93.69 2639.6 2850.4 6.3947 97.54 2652.2 2866.8 6.4362 95.11 2650.4 2864.4 6.4220 98.96 2662.7 2880.4 6.4626 96.51 2660.9 2878.1 6.4486 90.75 2617.3 -2821.5 6,3372 225 230 235 240 245 100.35 2672.9 2893.7 6.4881 97.88 2671.3 2891.5 6.4744 250 103.08 2693.0 2919.7 6.5374 100.57 2691.4 2917.7 6.5240 260 105.74 2712.4 2945.0 6.5844 103.19 2711.0 2943.2 6.5713 270 108.34 2731.4 2969.7 6.6294 105.74 2730.1 2968.0 6.6167 280 110.89 2750.0 2993.9 6.6728 108.25 2748.8 2992.3 6.6603 290 113.40 2768.2 3017.7 6.7147 110.71 2767.1 3016.3 6.7023 300 115.87 2786.3 3041.2 6.7553 113.14 2785.2 3039.8 6.7431 310 118.31 2804.1 3064.4 6.7947 115.54 2803.1 3063.1 6.7827 320 120.72 2821.7 3087.3 6.8331 117.90 2820.9 3086.1 6.8212 330 123.11 2839.3 3110.1 6.8706 120.25 2838.4 3109.0 6.8588 340 125.48 2856.7 3132.7 6.9071 122.57 2855.9 3131.7 6.8955 390 127.83 2874.0 3155.2 6.9429 124.87 2873.3 3154.2 6.9314 360 130.16 2891.3 3177.6 6.9780 132.47 2908.5 3199.9 7.0124 134.77 2925.6 3222.1 7.0462 127.15 2890.5 3176.6 6.9665 370 129.42 2907.8 3199.0 7.0010 380 131.68 2925.0 3221.3 7.0349 390 Specific Volume Sat. Vapor 10vg Internal Energy Sat. Liquid Enthalpy Sat. Liquid Entropy Sat. Press. MPа Temp Liquid Sat. Vapor Sat. Vapor Sat. Liquid Sat. Vapor Evap. Evap. Evap. 10°v Sg 271.90 2191:2 2463.1 275.58 2188.7 2464.2 279.14 2186.2 2465.3 282.60 2183.8 2466.4 285.95 2181.5 2467.4 271.93 2346.3 2618.2 275.61 2344.1 2619.7 279.17 2342.0 2621.2 282.62 2340.0 2622.6 285.98 2338.0 2624.0 8931 6.9383 7.8314 9040 6.9139 7.8179 9145 6.8904 7.8049 .9246 6.8678 7.7924 9344 6.8459 7.7803 1.0199 6204. 5980. 5772. 5579. 5398. 64.97 .025 .026 .027 .028 .029 1.0204 65.85 66.70 1.0209 67.53 1.0214 68.33 1.0218 289.23 2336.1 2625.3 295.48 2332.4 2627.8 9439 6.8247 7.7686 9622 6.7843 7.7465 5229. 4922. 650. 4408. 4190. 289.20 2179.2 2468.4 295.45 2174.9 2470.3 301.37 2170.8 2472.1 301.40 2328.8 2630.2 9793 6.7463 7.7257 307.01 2166.8 2473.8 307.05 2325.5 2632.5 312.39 2163.1 2475.5 312.43 2322.3 2634.7 69.10 1.0223 .030 .032 .034 .036 .038 70.60 1.0232 72.01 1.0241 9956 6.7104 7.7061 1.0111 6.6764 7.6876 73.36 1.0249 74.64 1.0257 1.0259 6.6441 7.6700 1.0400 6.6133 7.6534 1.0536 6.5839 7.6375 317.53 2159.5 2477.0 317.58 2319.2 2636.8 3993. 3815. 322.47 2156.0 2478.5 322.51 2316.2 2638.7 3652. 327.22 2152.7 2479.9 327.26 2313.4 2640.6 3503. 3367. 75.87 1.0265 77.05 .040 042 044 .046 048 1.0272 78.18 1.0279 79.27 1.0286 1.0293 331.78 2149.5 2481.3 331.83 2310.6 2642.5 1.0666 6.5558 7.6223 336.23 2308.0 2644.2 80.32 336.19 2146.4 2482.6 1.0790 6.5288 7.6078
Transcribed Image Text:2.30 (217.29) 225 (218.45) p(t Sat.) 10 v 10 90.73 2601.7 2801.3 6.3056 88.75 2602.0 2801.7 6.2972 Set. 86.71 25715 2762.2 6.2248 88.38 2584.I 2778.5 6.2587 90.01 2596.3 2794.3 6.2912 91.38 2608.1 2809.5 6.3223 200 205 86.06 25813 2774.9 6.2423 210 87.66 2593.7 2790.9 6.2753 215 89.23 2605.7 2806.4 6.3068 220 93.12 2619.5 2824.4 6.3523 94.63 2630.7 2838.9 6.3812 92.23 2628.6 2836.1 6.3664 96.10 2641.6 2853.0 6.4092 93.69 2639.6 2850.4 6.3947 97.54 2652.2 2866.8 6.4362 95.11 2650.4 2864.4 6.4220 98.96 2662.7 2880.4 6.4626 96.51 2660.9 2878.1 6.4486 90.75 2617.3 -2821.5 6,3372 225 230 235 240 245 100.35 2672.9 2893.7 6.4881 97.88 2671.3 2891.5 6.4744 250 103.08 2693.0 2919.7 6.5374 100.57 2691.4 2917.7 6.5240 260 105.74 2712.4 2945.0 6.5844 103.19 2711.0 2943.2 6.5713 270 108.34 2731.4 2969.7 6.6294 105.74 2730.1 2968.0 6.6167 280 110.89 2750.0 2993.9 6.6728 108.25 2748.8 2992.3 6.6603 290 113.40 2768.2 3017.7 6.7147 110.71 2767.1 3016.3 6.7023 300 115.87 2786.3 3041.2 6.7553 113.14 2785.2 3039.8 6.7431 310 118.31 2804.1 3064.4 6.7947 115.54 2803.1 3063.1 6.7827 320 120.72 2821.7 3087.3 6.8331 117.90 2820.9 3086.1 6.8212 330 123.11 2839.3 3110.1 6.8706 120.25 2838.4 3109.0 6.8588 340 125.48 2856.7 3132.7 6.9071 122.57 2855.9 3131.7 6.8955 390 127.83 2874.0 3155.2 6.9429 124.87 2873.3 3154.2 6.9314 360 130.16 2891.3 3177.6 6.9780 132.47 2908.5 3199.9 7.0124 134.77 2925.6 3222.1 7.0462 127.15 2890.5 3176.6 6.9665 370 129.42 2907.8 3199.0 7.0010 380 131.68 2925.0 3221.3 7.0349 390 Specific Volume Sat. Vapor 10vg Internal Energy Sat. Liquid Enthalpy Sat. Liquid Entropy Sat. Press. MPа Temp Liquid Sat. Vapor Sat. Vapor Sat. Liquid Sat. Vapor Evap. Evap. Evap. 10°v Sg 271.90 2191:2 2463.1 275.58 2188.7 2464.2 279.14 2186.2 2465.3 282.60 2183.8 2466.4 285.95 2181.5 2467.4 271.93 2346.3 2618.2 275.61 2344.1 2619.7 279.17 2342.0 2621.2 282.62 2340.0 2622.6 285.98 2338.0 2624.0 8931 6.9383 7.8314 9040 6.9139 7.8179 9145 6.8904 7.8049 .9246 6.8678 7.7924 9344 6.8459 7.7803 1.0199 6204. 5980. 5772. 5579. 5398. 64.97 .025 .026 .027 .028 .029 1.0204 65.85 66.70 1.0209 67.53 1.0214 68.33 1.0218 289.23 2336.1 2625.3 295.48 2332.4 2627.8 9439 6.8247 7.7686 9622 6.7843 7.7465 5229. 4922. 650. 4408. 4190. 289.20 2179.2 2468.4 295.45 2174.9 2470.3 301.37 2170.8 2472.1 301.40 2328.8 2630.2 9793 6.7463 7.7257 307.01 2166.8 2473.8 307.05 2325.5 2632.5 312.39 2163.1 2475.5 312.43 2322.3 2634.7 69.10 1.0223 .030 .032 .034 .036 .038 70.60 1.0232 72.01 1.0241 9956 6.7104 7.7061 1.0111 6.6764 7.6876 73.36 1.0249 74.64 1.0257 1.0259 6.6441 7.6700 1.0400 6.6133 7.6534 1.0536 6.5839 7.6375 317.53 2159.5 2477.0 317.58 2319.2 2636.8 3993. 3815. 322.47 2156.0 2478.5 322.51 2316.2 2638.7 3652. 327.22 2152.7 2479.9 327.26 2313.4 2640.6 3503. 3367. 75.87 1.0265 77.05 .040 042 044 .046 048 1.0272 78.18 1.0279 79.27 1.0286 1.0293 331.78 2149.5 2481.3 331.83 2310.6 2642.5 1.0666 6.5558 7.6223 336.23 2308.0 2644.2 80.32 336.19 2146.4 2482.6 1.0790 6.5288 7.6078
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