Specific VolumeInternal EnergyKrapuBasVap"₂u0611301 1.0002 206 1361.39 1,0001 181 2553.77 1.0001 159 6755.45 1.0001 142 76900 2.75.3 2375.37.90 2370.0 2377915.81 2364.7 2380.622.88 2360.0 2382900100011001229 30 2355.7 2385.035.17 2351 2386940.58 2348.1 2388.745.60 23447 2390 350.31 2341.6 2391.9001300146.98 1.0002 129 2088.37 1.0002 1180429.66 10003-108 69610.36 10004 100 75511.98 1.0005 93 9221.00071.00080017 14.95 1.0009 76 1461.0010 74 03016.69 1.0012 70 337001513.030016 14.028798082 76354.31 23386 2393358.87 23358 2394 762.80 2333 2 2396066.53 2330.7 2397 270.09 2328.3 2398.415.84001800190050 32.88 1.0053 28 1920055 34.58 10058 257690060 36.16 1.0064 237390005 37.63 1,0069 22-0140070 39.00 1.0014 203300075 40.29 1.0079 19 2380000 4151IN 10)100840085 42.67 1.0089 17.0990090 43.76 10094 16 2030095 44 M1 10098 15:399010 45.81 10102 146742011 47.69 10111 13415137.81 22827 24205144 94 22779 24228151 53 22734 24250157 66 22693 24269163 39 2265.4 24288168.78 2261.7 24305173.47-2258 3 2432 2178 69 2255.0 2433.718) 27 2251 9187.64 22489 2436.6011 49.42 10119 12 361013 51.04 10126 11445014 53.55 1.9134 10693191 82 2246.1 2437.9199 66 2240.8 2440.4206.91 22358 24427213.66 22312 2444,9219.98 2226.9 2446.9.565758155.48 1.0967 342.7156.17 10975 336.9156.86 1.0983331 3157.53 1.0991 325.9158.20 1.0999 320,7655 32 1909 2 25645658 32 1906.8 2565.1661.27 1904 4 2565.7664 18 1902 1 2566.3667.06 18998 2566.8596061158.85 1.10061.1014159.501.1021160.14315.7669.90 1897.5 25674310.8 672.70 1895 3 2568 0306.0 675.47 18930 2568.5301.3 678 20 1890.8 2569.0297.0 680.90 1888.7 2569663160 771.102964161.391.10364.0 (250.40)10' vu49.78 2602.3 2801.46.070148.602583.92780.36.02976.067240.00 2001 2200030.74 2615.5 2818 5 6.10266.136251.74 2629.4 2836.36.168352.71 2642.7 2853.52655.5 2870.1 6.199053.652667.9 2886.254.5755.46 2680.0 2901.856.33 2691.7 2917.057.18 2703.2 2931.958.02 2714.4 2946.46.22856.25686.28426.31086.33652725.3 2960.758.846.361560.44 2746.7 2988.5 6.409530154 6.455361.99 2767.42787.6 3041.663.516.499164.99 2807.3 3067.3 6.541366.45 2826.7 3092.5 6.582167.88 2845.7 3117,22864.6 3141.769.2970.68 2883.2 3165.96.62156.65986.697172.05 2901.6 3189,8 6.733512EnthalpyEntropySelDetLiEras30VaporLiquidhyKvaphy01 25013-20147.91 24969 250481581 24925 2508322.89 24885 251140000 9.1562 9.1562028 90775 9.10640575 9999 9.057)0829 89312 9014229.30 24849 2514.235.17 24816 2516340.58 24786 2519145.60 24757 2521.350.31 2473.1 252341059 8.8697 897561268 88140 894081460 87631 8.90911637 8.7162 887991802 K6727 352954.71 24706 2525)58.87 2468 3 2527162.80 2466.0 2528866.34 2463.9 2530 570.10 2461.9 253201953 6322 8827921025943 880442238 5585 878252368 3250 8.76182491 84931 87422137 82 2423.7 2561 5144.95 24196 25645151 53 24159 25674157 67 24124 25700163.40 24091 257254764 75187 839514997 73616 8.36135210 78094 8.33045408 7,7613 8.30203592 7.7167 82758168.79 24060 23748173 24031 25770178.70 2400 3 25790183 29 23977 25810187.65 23952 258293764 76150 8.25153926 76361 #22876079 75904 8.207)6224 7.3648 818726362 73321 8.16826493 7,50098.15026738 74430 8116819183 23928 25847199 67 23883 25840206.92 23841 25911213.67 23802 25919219.99 2376.6 2596,56963 7 1900 8.08633132 7 3412 8.05847366 72939 .0325655.93 20970 2753.0658.93 2094 8 2753 8661.90 2092.7 2754 5664 83 20905 2755.3667.71 20884 2756.118973 48920 6.78931.9043 4.8789 6.783719112 48661 -6.77731.9180 4.8535 6.77141.9246 48411 6.7657670.56 20863 2756.8673.37 2084 2 2757,5676.15 2082.1 2758.3678.89 20801 2759.0681 60 20780 2759.61.9312 4.8288 6.76001.9377 4.8168 6.75451.9441 4.5049 6.74901.9504 47932 674361.9566 4.7817 6.7383P (t Sat.)4.1 (251.87)10 vh48.53 2601.9 2800.9u6.0597Sat.24047.042380.72773.66.007424525025549.172611.1 2812.750.17 2625.2 2830.92638.8 2848.551.1452.076.04596.08226.11656.14932651.9 2865,4 6.180526026527052.986.21052664.5 2881.727553.86 2676.7 2897.62806.239354.72 2688.7 2913.0 6.2671 28555.56 2700.3 2928.12906.294056.39 2711.6 2942.8 6.3200 29557.20 2722.7 2957.258.77 2744.3 2985.33012.560.30 2765.261.79 2785.6 3038.963.25 2805.4 3064.86.3453 3006.3939 3106.4401 3206.4843 3306.526834064.68 2824.9 3090.166,082844.1 3115.06.56783506.607536067.47 2863.0 3139.6 6.6460 37068.833806.68342881.7 3163.970.18 2900.2 3188.0 6.7200390tSat.10010511011512012513013514014515016017018019020021022023024025026027028029030031023060 (158.85)uhS10 v10 v336.9 2565.1 2753.8h6.7832315.7 25674 275686.76006.37326:4127277.0 2453.6 2608.7282.9 2464.7 2623.1288.7 2475 4 2637.1294.3 2486.0 2650.8299.8 2496.2 2664.16.4203256.0 2448 2 2601 #6.45852617 2459.6 2616.76.49532673 2470 A 2631.16.5307 272.7 2481.6 2645 26.3649277.9 2492.2 2658.96:45076.48726.3224305.2 2506.3 2677.2310.5 2516.1 2690.0315.7 2525.8 2702.6320.8 25353 2715.0325.9 2544.7 2727.26.59806.63006.66106.69126.72056.35636.58906.62086.65156.6814283 1 2502 5 26723288 1 2512.6 26855293 12522.5 2698 32979 2532 2 27110302.7 2541.7 27234307 5 25511 2735.6316.7 2569.5 2759 5325.8 2587.4 27828334.7 2604.9 2805.7343.4 2622.0 2828.16.7105330 8 2553.9 2739 2 6.7490340.6 2571.9 2762 7 6.8040350.2 2589.6 2785.7 6.8564359.6 2606.8 2808.2 6.9067368.9 2623.8 2830.4 6.95516.76636.81956.87056.9194352.0 2638,9 2850.1360.5 2655.6 2871.9378.1 2640.5 2852.2 7.0018387.1 2657.1 2873.9 7.0470396.1 2673.4 2895.3 7.0909405.0 2689.7 2916.5 7.1335413.8 2705.9 2937.6 7.17506.96657.0121369.0 2672.1 2893.5 7.0562377.3 2688.5 2914.81 7.0991385.6 2704.7 2936.1 7.1409422.6 2721.9 2958.6 7.2155431.3 2738.0 2979.5 7.2551440.0 2753.9 3000,3 7.2939448.7 2769.9 3021.2 7.3318457.3 2785.8 3041.9 7,3690393.8 2720.9 2957.2402,0 2737.0 2978.21410.2 2753.0 2999.1418.3 2769.0 3020.0426.3 2785.0 3040.87.18167.22147,26037.29847.3357465.9 2801 8 3062.7474.4 2817.7 3083.47.40567.4415434.4 2801.0 3061.6442.4 2817.0 3082.57.37247.4084747674870 1872.7 2104 Read the questions carefully and answer with complete solutionand units. Use the steam tables provided and use 4 decimal placesfor solving. Final answers shown are in 2 decimal places. Drawthe T-S diagrams properly with respect to the saturation lineA steam power plant uses the ideal Regenerative Rankine cycle with singleopen feedwater heater where the steam enters the high-pressure turbine at 4MPa and 300C. It partially expands to 600 kPa then some steam is extracted atthis point. The remaining steam expands and enters the condenser at 10 kPa.Sketch the schematic diagram and the TS diagram with labeled points, andsolve for mass taken for feedwater heating, Qa, Qr, Wt, Wp, Wnet, thermalefficiency, and Steam rate. Neglect the condensate pump work.kg20.01%, 2286.401457.51,832.543.74,828.89, 36.25%, 4.34 kWh 1

Answered: Image /qna-images/answer/e9065702-17b5-472d-a244-46a7ffd890e1.jpg

Read the questions carefully and answer with complete solution and units. Use the steam tables provided and use 4 decimal places for solving. Final answers shown are in 2 decimal places. Draw the T-S diagrams properly with respect to the saturation line A steam power plant uses the ideal Regenerative Rankine cycle with single open feedwater heater where the steam enters the high-pressure turbine at 4 MPa and 300C. It partially expands to 600 kPa then some steam is extracted at this point. The remaining steam expands and enters the condenser at 10 kPa. Sketch the schematic diagram and the TS diagram with labeled points, and solve for mass taken for feedwater heating, Qa, Qr, Wt, Wp, Wnet, thermal efficiency, and Steam rate. Neglect the condensate pump work. kg 20.01%, 2286.401457.51,832.54 3.74,828.8936.25%, 4.34 kWh 1

Read the questions carefully and answer with complete solution and units. Use the steam tables provided and use 4 decimal places for solving. Final answers shown are in 2 decimal places. Draw the T-S diagrams properly with respect to the saturation line A steam power plant uses the ideal Regenerative Rankine cycle with single open feedwater heater where the steam enters the high-pressure turbine at 4 MPa and 300C. It partially expands to 600 kPa then some steam is extracted at this point. The remaining steam expands and enters the condenser at 10 kPa. Sketch the schematic diagram and the TS diagram with labeled points, and solve for mass taken for feedwater heating, Qa, Qr, Wt, Wp, Wnet, thermal efficiency, and Steam rate. Neglect the condensate pump work. kg 20.01%, 2286.401457.51,832.54 3.74,828.8936.25%, 4.34 kWh 1

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

See similar textbooks

Similar questions

B) A heat pump that operates on the ideal vapor compression cycle with refrigerant-134a is used to heat a house and maintain it at 25 °C by using underground water at 15 °C as the heat source. Select reasonable pressures for the evaporator and the condenser and explain your choice.
Question 4 a. A factory requires electrical power for its machinery along with 80 MW of heat for process heating. The combined demand is achieved by using a superheated Rankine steam cycle in which the turbine is used to supply the electrical power required and the condenser cooling water provides the process heating to the factory. Steam is generated in a boiler at a pressure of 70 bar and it leaves the superheater at a temperature of 400°C. The steam expands through the turbine to a condenser pressure of 3 bar. The turbine isentropic efficiency is 0.85. The steam is condensed to saturated liquid in the condenser and a feed pump increases the condensate pressure to 70 bar for return to the boiler. The feed pump work may be neglected in the calculation. i. Sketch the cycle in a T-s diagram. ii. Calculate the steam mass flow rate required to satisfy the process heating demand. iii. Calculate the power available from the turbine. iv. Determine the thermal efficiency of the cycle.
Read the questions carefully before answering. Box or indicate your final answers when solving and draw your diagrams cleanly or use correction tape/fluid. Use the steam tables provided and DO NOT ROUND the values from the steam table. Use 4 decimal places when solving and use 2 decimal places for final answers only. Draw the TS diagram with proper placement and label of points when required. An Actual Rankine Engine receives steam at 10 MPa and 350C. The steam expands adiabatically to a pressure of 100 kPa with quality of 85%, and then condenses at the same pressure. Find the Indicated thermal efficiency, Brake Steam Rate, Combined Heat Rate, and electrical power produced if 2.12 kg/s of steam flowsin the cycle. The turbogenerator has a mechanical efficiency is 85% and the generator efficiency is 95%.
Answer letters A, H, I. Use the steam tables provided and DO NOT ROUND the values from the steam table. Write down the values taken from the steam table
Please solve the question on the sheet and get a clear picture and submit the picture. thankyou
Completely solve and box the final answers. Write legibly
Y3a please help me with the solution and answer thank you
Complete solution and units please. Use the steam tables provided, and use 4 decimal places for solving. Final answers are shown in 2 decimal places. Draw the T-S diagram properly with respect to the saturation line. 2. A steam power plant uses the ideal Regenarative Rankine cycle with single open feedwater heater where the steam enters the high pressure turbine at 4 UPa and sooc. At partially expands to 600 kPa then some steam is extracted at this point. The remaining steam expands and enters the condenser at 10 kPa. Sketch the schematic diagram and the TS diagram with labeled points, and solve for marr taken for feedwater heating, Qa, Qr, Wt, Wp. What, thermal exter efficiency and Steam rate. Neglect the condensate pump work." Answer: 20.01% 2286.40 kJ. 1457.51 kJ 1 832.54 kJ 1 kg 3.74 kJ kg kg 36.25%, 4.34 £] 828.89 kJ " kg ку. kuh Specific Volume Internal Sal. Enthalpy Press. MPa Se Entropy Sat, V Sat. Sat. Sat. Evap. Liquid Evap. Vapor Vapor р 10¹ Liquid Uy 103 apor U₂ h, hre h₂…
Q3/ In a steam power plant the high pressure turbine is fed with steam at 60 bar, 450°C and enters low pressure turbine at 3 bar with a portion of steam bled out for feed heating at this intermediate pressure. Steam finally leaves low pressure turbine at 0.05 bar for inlet to condenser. Closed feed heater raises the condensate temperature to 115°C and produces saturated liquid. Bled steam leaving closed feed heater is passed through trap to mix with condensate leaving condenser. Consider power output to be 30 MW. Determine: (a) The fraction of steam bled for feed heating. (b) The capacity of boiler in kg/hr. (c) The overall thermal efficiency of plant. (d) Give layout and T-s diagram of the cycle.