Saturation: PressuresSpecifie VolumeSaInternal EnergySalLiguleEntropySet.LigurdEnthalpyPrTegpLigld10,Sat.VaperSal.LiquidSatVeperSat.VaporErapEr10DO06113.0007COC3.co0901 1.0002 206 1361.89 1.0001 181 2553.77 1.0001 159 6755.45- 1.0001 142 78900 2.75.3 237537.90 23700 2377.915.81 2364.7 2380622.88 23600 2382.9· O1 25013 2501.47.91 24969 2504 815.81 2492.5 2508.322.89 2488 5 2511.40000 9.1562 9.15620288 9.0775 9,10640575 8.9999 9.0573ON29 8.9312 9,0:42.0010001100120013.00146.98 1.0002 129 2088.37 1.0002 118 0429.66 LO003 108 69610.8611.9829.30 2355.7 2385.035.17 23518 2386.940.58 2348.1 2388.745.60 2344.7 2390350.31 23416 2391.929.30 24849 2514.235.17 2481.6 2516.840.58 2478.6 2519.145.60 2475.7 25213503I 2473.1 2523.41059.R8697 8.97561268 8.8140 8.94081460 8.7631 8.90911637 8.7162 8.87991802 8.6727 8.85291.0004 100 7551.0005 93 92254.71 2338.6 2393.358.87 2335.8 2394.762.80 2333.2 2396.066.53 2330.7 2397270.09 2328.3 2398.454.71 2470.6 2525.358.87 2468.3 2527.162.80 2466.0 2528.866.54 2463.9 2530.570.10 2461.9 2532.0.1957 8.6322 8.82792102 8.5943 8.80442238 85586 8.78252368 8.5250 8.76182491 8.4931 $.74221.0007 879801.0008 82 763,0015.0016.00170018001913.0314.0214.95 1.0009 78 14615.84 1.0010 14 03016.69 -1.0012 70 337.0050005500600065007032.88 1.0053 28 1921.0058 25 7691.006437.6) 1.0069 2201410074137.81 2282.7 24205144.94 2277.9 24228151.53 2273.4 2425.0157.66 2269.J 2426.9163.39 2265 4 2428.8137.82 2423.7 2561.5144.95 2419.6 2564.5IS1.53 2415.9 2567.4157.67 2412.4 2570.0163.40 2409.I 2572.54764 7.9187 8.39514997 7.8616 8.36135210 7.8094 8.33045408 7,7613 8.30205592 1,7167 8 275834.5836.1623 73939.0020 5305764 76750 8.25153926 7.6361 8.22876079 75994 8.20736224 7.5648 8.1872.6362 7.5321 8.168240.29 1.0079- 19 23841.51 1.0054 18 103168,78 2261.7 2430.5173.87 2258J 24322. 173.88 2403.1 2577.0178.69 22550 2433.7 178.70 2400 3 2579.0183.27 2251.9 2435.2: 183.29 2397.7 2581.0187,64 2248.9 2436.6168.79 2406.0 2574.8007500800oss. 42.67 1.0089 47 099.0090009543.76 1.0094 16 20344,81 1.0098 15 399187.65 2395.2 2582.91694.01618.41549.5148641428,4417.36 2088.7 2506.1423.13 2084.6 2507.7428.68 20805 2509.2434,03 2076.7 2510.7439.20 2072.9 2512.141746 2258.0 2675.5423.24 2254,4 2677.6428.79 2250.9 2679.7434.15 2247.5 2681.7439 32 2244.2 2683.5 13608 5.9373 7.298113026 60568 7.359413181 6.0249 7.343013329 5.9944 7.327313471 59653 1J12499.63 1.0432J00105 101.00 1.0443.110115 103.58.120 104.80 1.0473102.31 1.04531.0463Table 3. Vapor5.0 (263.99)P(t Sat.)U 261AS)49 262.73)10, .39.44 2597.1 2794.3 5.9734Sat.41.18 2598.4 2796.05.991640.29 2597. 2795.2 5.98242552602652701919 2376.8 276J10.00 21017 2700 0 190zIT5 26096 28104 6.01842.75 2624.7 2829,9 6.05443.939438.67 2583 7 277719.63 2600.4 2798.6 5.981340.54 2616.2 2818.93.941119.77 2388 2120.722605.12804.641.62 2620.5 2824.5 6.03675 06073.99996.018927528028529029543.62 2639.1 28485 6.088544,46 2652.9 28663 6.120945.28 2666.2 2883.6 6.151946.07 2679.1 2900.2 6.181646.83 2691.6 2916.4 6210242.45 2635.2 2843.4 6.071443.J3 2649.3 2861.6 6.104444,14 2662.8 2879.1 6.135944.92 2675.9 2896.0 6.166145.69 2688.6 2912.4 6.195141.41 2631. 2838.3 6.054442.24 2645.6 2856.8 6.088043,04 2659.4 2874.6 6.120143.82 2672.7 28918 6.150744.58 2685.5 2908.46.180130031032033034047.58 2703.7 2932.1 6.237749.03 2727.0 2962.4 6.290250.43 2749.4 2991.5 6.339651.78 2771.0 3019.5 6.386553.09 2792.0 3046.8 6.431346.43 2700.8 2928.3 6.223047.86 2724.5 2959.0 6.276049.24 2747.1 2988.4 6.326050.57 2768.9 3016.751.87 2790.0 3044.145.32 2698.0 2924.5 6.208446.74 2721.9 2955.6 6.262148.10 2744,7 2985.3 6.312549.42 2766.7 3013.8 6.360350.70 2788.0 3041.5 6.4058637336.418553.13 2810,5 3070.954.36 2830.7 3097.0 6.503455.57 2850.4 3122.7 6.543656.76 2869.8 3148.0 6.582557.93 2889.0 3172.951.94 2808.7 3068.4 6.449353.16 2828.9 3094.7 6.491254.35 2848.8 3120.5 6.531755.52 2868.3 3145.9 6.570856.68 2887.6 3171.0 6.60896.461735036037038039054.37 2812.4 3073.3 6.474355.62 2832.4 3099.3 6.515756.84 2852.O 3124.8 6.555758.05 28713 3150.0 6.594459.24 2890.4 3174.8 6.63216.620460.41 2909.3 3199.3 6.668861.57 2928.0 3223.6 6.704662.72 2946.6 3247.7 6.739663,85 2965.1 3271.6 6.773964.98 2983.5 3295440341059.09 2908.0 3197.5 6.657260.23 2926.8 3221.9 6.693261.35 2945.4 3246.0 6.728362.47 2963.9 3270.0 6.762763.57 2982.4 3293.9 6.796457.81 2906.6 3195,758.93 2925.5 3220.2 6.682060.04 2944.2 3244.4 6.717261.14 2962.8 3268.562.23 29813 3292.46.64594354436.75176.78556.807510.0 (311.06)10.2 (312.52)P(t Sat.)10',10',18.026 2544.4 2724.7 5.614117.588 2541.6 2721.0. 5.6017 Sat.30517.864 2338.3 2717.1 3.601118.593 2565.1 27510 5.658919.253 2588.8 2781.3 5.710317.197 25269 27023 S 5697 310T7.950 2555.T 2738.2 5.6309 3155.684818.626 2580.0 2770.032019.861 2610.4 2809.120.429 2630.4 2834.7 5.799620.964 2649.1 2858.7 5.839221.472 2666.6 2881.4 5.876321.957 2683.3 2902.9 5.911219.244 2602.5 2798,819.819 2623.2.2825.4 5.7174 33020.358 2642.5 2850.1 5.8183 33520.869 2660.6 2873.4 5.8564 34021.355 2677.5 2895.5 5.39225.75685.7332 32534521.82 2693.9 2916.5 5.926122.70 2724.4 2955.9 5.988922.42 2699.2 2923.4 5.944323.31 2729.1 2962.1 6.006024.14 2756.9 2998.3 6.062624.93 2783.2 3032.5 6.115425.68 2808.3 3065.1 6.165035036023.53 2752.7 2992.7 6.046524.31 2779.4 3027.4 6.100025.06 2804.8 3060.4 6.150337038039026.41 2832.4 3096.5 5.212027.11 2855.7 3126.8 6.256727.80 2878.4 3156.3 6.299528.46 2900,4 3185.1 6.340729.11 2922.1 3213.2 6.380525.78 2829.1 3092.1 6.197726.48 2852.7 3122.8 6.242927.16 2875.5 3152.5 6.28614004104204306.3677. 44028.46 2919.6 3209.9 1. A steam power plant Dperates uing The idealRankine Cycle where 'steam initially enteo the turkingott 5.0 uPa and 400 c thencondenses at 7kPa and enteradhi exits as saturatedliquid- Draw the IS diagram find the thermalefticienay, and steam rate.after expanding t

Answered: Image /qna-images/answer/b7060292-0fa9-48b6-b5ae-6ca210510db0.jpg

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

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

A stear power plant operates bstween a boller pressure of 52 bar and a condenser pressure of 0.045 bar. Calculate for these Imis he cycle afficiency for a Rankine cyce with dry saturated steam at entry to the turbine.
Do part d and e
THERMODYNAMICS The combustion peak pressure is 900 psia of a gasoline engine. The volumetric compression ratio of 10 and befont compression has air at 520 R, 22 psia in the cylinder Assume cold air properties. What is the cycle's maximum temperature? Determine the temperature at the start of the exhaust (heat rejection) as well as the over cycle efficiency. Show Complete Solution on a Paper.
Conside a Steam power plant that operates tolbine Simple ideal Ranicine cycle. Steam enters of a3,031 kg/s at WIth a mess flan rate g 33,031 kg/s a pressurT Of 7MPG ard at a temperatur q 500°c .The steam the conde nser escaping fem turbine 1s cooled in 'Coeling water Hom
a steam engine operation between 150C and 550C. ehat is theorithical maximum thermal effciency?
4. An evaporator has R-410A at -20°C and quality 80% flowing in. The exit flow is saturated vapor at -20°C. a. Consider the heating to be a reversible process and find the specific heat transfer from the entropy balance. (Answer: 48.7 kJ/kg) b. If the heat source was at -10°C and the inlet and outlet streams still have the same properties as in a), calculate the specific entropy generation? (Answer: 7.33 J/(kg K))
thermodynamics
40 CHAPTER 2 FORCE VECTORS *2 *2-40. Solve Prob. 2-1 by summing the rectangular or x, y components of the forces to obtain the resultant force. 2- 2-41. Solve Prob. 2-22 by summing the rectangular or x, y components of the forces to obtain the resultant force. an po 2-42. Determine the magnitude and orientation, measured counterclockwise from the positive y axis, of the resultant force acting on the bracket, if FB = 600 N and 0 = 20°, y FB 30° FA = 700 N B Prob. 2-42
Please help with the correct answer Thermodynamics problem
3. Adia batic Steam turbine has inlet of 6 kg/s at 5 mpa, 600 c° The a Ctual, Steam exit from turbine is at lo0 k pa. with quality of lo0% find G The pouser output (Wout) in Mw @ The isentropicefficiency? Steam bkgls 5M pa 600 C Adiabatic Turbine X=100 ソ0 100 kpa
2. A camot eng hie reguiras 85k1/s from Hhe the hot soune, The engme produces 15 kw of pawer and the tem pevafure of Ahe sink is 26ʻc , What Is #he tempevature of the hot sourze?
10 0.9967. Ans. H.W 2 A smaller power plant produces steam at 3 MPa, 600 C, in the boiler. It keeps the condenser at 45 C by the transfer of 10MW out as heat transfer. The first turbine section expands to 500 kPa, and then flow is reheated followed by the expansion in the low-pressure turbine. Find the reheat temperature so that the turbine output is saturated vapor. For this reheat, find the total turbine power output and the boiler heat transfer. Answer. (Reheat temperature= 529°C , total turbine power output= 6487 kW, the boiler heat transfer= 16 475 kW)