With complete and clear units/conversion factors. Box your final answer and round to the nearest 2 decimal places. Thank you 1. A Rankine cycle is useturbine at 2·25 Mpa and 300 c then exits at 0.0 25 MPa. The puump receivesFor a steam powor plant . Liqud First enters thesaturated liquid tromthe condener bepore sending it to the boiler at the ariginalpressure .a. Draw the T-s diagramb. Find the dry ness at turbine exitC. Wpd. Qae. Qrf. Wrh. EFFiciency ( l-)i: Steam rate( kg/ kwn)Anewer choices° lo0%, 3.12 ku/kg,4.63 kg/kwh3016.3 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 Wh83.73°, 2.21 ku/ kg, 2742.1 k/kg, 1964.48 kJ/ kq. 119.89 ku/kg2P:36°%, 4.03kg/ kWhlo0 '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 v1090.73 2601.7 2801.3 6.3056 88.75 2602.0 2801.7 6.2972 Set.86.71 25715 2762.2 6.224888.38 2584.I 2778.5 6.258790.01 2596.3 2794.3 6.291291.38 2608.1 2809.5 6.322320020586.06 25813 2774.9 6.2423 21087.66 2593.7 2790.9 6.2753 21589.23 2605.7 2806.4 6.3068 22093.12 2619.5 2824.4 6.352394.63 2630.7 2838.9 6.3812 92.23 2628.6 2836.1 6.366496.10 2641.6 2853.0 6.4092 93.69 2639.6 2850.4 6.394797.54 2652.2 2866.8 6.4362 95.11 2650.4 2864.4 6.422098.96 2662.7 2880.4 6.4626 96.51 2660.9 2878.1 6.448690.75 2617.3 -2821.5 6,3372225230235240245100.35 2672.9 2893.7 6.4881 97.88 2671.3 2891.5 6.4744 250103.08 2693.0 2919.7 6.5374 100.57 2691.4 2917.7 6.5240 260105.74 2712.4 2945.0 6.5844 103.19 2711.0 2943.2 6.5713 270108.34 2731.4 2969.7 6.6294 105.74 2730.1 2968.0 6.6167 280110.89 2750.0 2993.9 6.6728 108.25 2748.8 2992.3 6.6603290113.40 2768.2 3017.7 6.7147 110.71 2767.1 3016.3 6.7023 300115.87 2786.3 3041.2 6.7553 113.14 2785.2 3039.8 6.7431 310118.31 2804.1 3064.4 6.7947 115.54 2803.1 3063.1 6.7827 320120.72 2821.7 3087.3 6.8331 117.90 2820.9 3086.1 6.8212 330123.11 2839.3 3110.1 6.8706 120.25 2838.4 3109.0 6.8588340125.48 2856.7 3132.7 6.9071 122.57 2855.9 3131.7 6.8955 390127.83 2874.0 3155.2 6.9429 124.87 2873.3 3154.2 6.9314 360130.16 2891.3 3177.6 6.9780132.47 2908.5 3199.9 7.0124134.77 2925.6 3222.1 7.0462127.15 2890.5 3176.6 6.9665 370129.42 2907.8 3199.0 7.0010 380131.68 2925.0 3221.3 7.0349390Specific VolumeSat.Vapor10vgInternal EnergySat.LiquidEnthalpySat.LiquidEntropySat.Press.MPаTempLiquidSat.VaporSat.VaporSat.LiquidSat.VaporEvap.Evap.Evap.10°vSg271.90 2191:2 2463.1275.58 2188.7 2464.2279.14 2186.2 2465.3282.60 2183.8 2466.4285.95 2181.5 2467.4271.93 2346.3 2618.2275.61 2344.1 2619.7279.17 2342.0 2621.2282.62 2340.0 2622.6285.98 2338.0 2624.08931 6.9383 7.83149040 6.9139 7.81799145 6.8904 7.8049.9246 6.8678 7.79249344 6.8459 7.78031.01996204.5980.5772.5579.5398.64.97.025.026.027.028.0291.020465.8566.70 1.020967.53 1.021468.33 1.0218289.23 2336.1 2625.3295.48 2332.4 2627.89439 6.8247 7.76869622 6.7843 7.74655229.4922.650.4408.4190.289.20 2179.2 2468.4295.45 2174.9 2470.3301.37 2170.8 2472.1 301.40 2328.8 2630.2 9793 6.7463 7.7257307.01 2166.8 2473.8 307.05 2325.5 2632.5312.39 2163.1 2475.5 312.43 2322.3 2634.769.10 1.0223.030.032.034.036.03870.601.023272.011.02419956 6.7104 7.70611.0111 6.6764 7.687673.361.024974.641.02571.0259 6.6441 7.67001.0400 6.6133 7.65341.0536 6.5839 7.6375317.53 2159.5 2477.0 317.58 2319.2 2636.83993.3815. 322.47 2156.0 2478.5 322.51 2316.2 2638.73652. 327.22 2152.7 2479.9 327.26 2313.4 2640.63503.3367.75.87 1.026577.05.040042044.0460481.027278.18 1.027979.27 1.02861.0293331.78 2149.5 2481.3 331.83 2310.6 2642.5 1.0666 6.5558 7.6223336.23 2308.0 2644.280.32336.19 2146.4 2482.61.0790 6.5288 7.6078

Answered: complete and clear units/conversion…

Engineering

Mechanical Engineering

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

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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Question

100%

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

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

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