A Steam power plant uses a Rankine cycle to produce electrical power. The boiler pressure is 2 MPa and the temperature at the turbine inlet is 300C. The pump inlet pressure is 0.025 MPa and the entropy is 0.8931 kJ/kg-k. The turbine gives 1MW of work to the generator. Find the dryness of the steam at turbine exit, Wp, Qa, Qr, Wt, Wnet, efficiency, SR, and mass flow rate of steam. (84.65%, 2.0143 kJ/kg, 2749.56 kJ/kg, 1986.15 kJ/kg, 765.42 kJ/kg, 763.41 kJ/kg, 27.76%, 4.7157 kg/kWh, 1.3064 kg/s) -Draw the T-S diagram with properly labelled points and solve the problems. Show your COMPLETE solution - Use the Steam Table provided if necessary.

Refrigeration and Air Conditioning Technology (MindTap Course List)
8th Edition
ISBN:9781305578296
Author:John Tomczyk, Eugene Silberstein, Bill Whitman, Bill Johnson
Publisher:John Tomczyk, Eugene Silberstein, Bill Whitman, Bill Johnson
Chapter36: Refrigeration Applied To Air-conditioning
Section: Chapter Questions
Problem 9RQ: What are higher-efficiency refrigerant blends that can be used as long-term replacements for R-22 in...
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A Steam power plant uses a Rankine cycle to produce electrical power. The boiler pressure is 2 MPa and the temperature at the turbine inlet is 300C. The pump inlet pressure is 0.025 MPa and the entropy is 0.8931 kJ/kg-k. The turbine gives 1MW of work to the generator. Find the dryness of the steam at turbine exit, Wp, Qa, Qr, Wt, Wnet, efficiency, SR, and mass flow rate of steam. (84.65%, 2.0143 kJ/kg, 2749.56 kJ/kg, 1986.15 kJ/kg, 765.42 kJ/kg, 763.41 kJ/kg, 27.76%, 4.7157 kg/kWh, 1.3064 kg/s)

-Draw the T-S diagram with properly labelled points and solve the problems. Show your COMPLETE solution

- Use the Steam Table provided if necessary.

hot gases
1.
steam generator
4
turbine
condenser
pump
3
2.
Transcribed Image Text:hot gases 1. steam generator 4 turbine condenser pump 3 2.
Table 3. Vapor
P(t Sat.)
2.00 (212.42)
10 v
Specific Volume
Sat.
Internal Energy
Sat.
Liquid
Enthalpy
Sat,
Liquid
Entropy
Prom.
MP
Teme
Sat.
Sat.
Vapor
Nat.
Vapor
Sat
Liquid
Sat.
Vapor
Sat.
99.63 2600.3 2799,5
6.3409
Liquid
Vaper
Evap.
Evap
Evap.
10'v,
10v,
h,
200
205
210
215
220
95.27 2570.6 2761.1
97.06 2582.8 2777.0
025
026
027
.028
029
64.97 1.0199
65.85 1.0204
66.70 - 1.0209
67.53 1.0214
68.33 1.0218
6204.
5980.
5772.
5579.
5398.
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.S 2467.4
271.93 2346.3 2618.2
275.61 2344.I 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 78179
9145 6.8904 7.8049
9246 6.8678 7.1924
9344 6.8459 7.7803
6.2608
6.2941
6.3259
6.3566
6.3861
98.80 2594.7 2792.3
TOU.50 2606.2 2807.2
102.15 2617.4 2821.7
225
230
235
240
245
6.4147
69.10 1.0223
70.60 1.0232
72.01 1.0241
73.36 1.0249
74.64
5229.
4922.
650.
4408.
4190.
289.20 2179.2 2468.4
295.45 2174.9 2470.3
301.37 2170.8 2472.1
307.01 2166 8 2473.8
312.39 2163.1 2475.5
289.23 2336.1 2625.3
295.48 2332.4 2627.8
301.40 2328 8 2630.2
307.05 2325.5 2632.5
312.43 2322.3 2634.7
9439 6.8247 7.7686
9622 6.7843 7.7465
9793 6.7463 7.7257
9956 6.7104 7.7061
1.0111 6.6764 7.6876
103.77 2628.3 2835.8
105.36 2638.9 2849.6 6.4423
106.91 2649.4 2863,2 6.4691
108.45 2659.6 2876.5 6.4952
109.95 2669.7 2889.6 6.5205
030
032
134
836
038
1.0257
75.87
77.05
78. 18
79.27
80.32
1.0265
1.0272
1.0279
1.0286
1.0293
3993.
3815
3652.
3503.
3367.
317.53 2159.,5 2477.0
322.47 2156.0 2478.5
327.22 2152.7 2479.9
331.78 2149,5 2481 3
336.19 2146.4 2482.6
317.58 2319.2 2636.8
322.51 2316.2 2638.7
327.26 2313.4 2640.6
331,83 2310.6 2642.5
336,23 2308.0 2644.2
1.0259 6.6441 7.6700
1.0400 6.6133 7,6534
1.0536 6.5839 7.6375
1.0666 6.5558 7.6223
1.0790 6.5288 7.6078
250
260
270
280
290
1I1.44 2679.6 2902.5 6.5453
114.36 2699.0 2927.7 6.5931
117.21 2717.9 2952.3 6.6388
120.01 2736.4 2976.4 6.6828
122.76 2754.6 3000.2
.040
042
044
046
48
6.7253
81.33
83.72
85.94
88.01
89.95
3240.
2964.
2732
2535,
2365.
340.44 2143.4 2483.9
350.48 2136,4 2486.8
359.79 2129.,8 2489.6
368.48 2123.6 2492.1
376.63 2117.8 2494 5
340.49 23054 2645.9
350.54 2299,3 2649.8
359.86 2293.6 2653.5
368.54 2288.3 2656.9
376.70 2283.3 2660.0
1.0910 6.5029 7.5939
1.1193 6.4422 7.5615
1.1453 6.3867 5320
1.1694 6.3354 7.5048
1.1919 6.2878 7.4797
050
1.0300
1.0316
1.0331
1.0346
1.0360
300
310
320
330
340
125.47 2772.6 3023.5 6.7664
128.14 2790.3 3046.6
130.79 2807.9 3069.5
133.40 2825.3 3092.1
136.00 2842.6 3114.6 6.9201
6.8063
6.8452
6.8831
060
65
070
675
080
085
090
1.0373
1.0386
95.14, 1.0398
1.0410
384.31 2112.4 2496.7
391.58 2107.2 2498.8
398.48 2102.3 2500.7
405.06 2097.6 2502.6
384,39 2278.6 2663.0
391.66 2274.! 2665.8
398.57 2269.8 2668.4
405.15 2265.7 2670.9
12130 6.2434 74564
1.2329 6.2017 74346
1.2517 6.1625 7.4141
1.2695 6.1254 7.3949
91.78
2217.
2087
1972.
1869.
93.50
350
360
370
380
390
138.57 2859.8 3137.0 6.9563
141.13 2877.0 3159.3 6.9917
143.66 2894.1 3181.4 7.0265
146.19 2911.2 3203.6 7.0606
148.70 2928.2 3225.6 7.0941
96.71
Transcribed Image Text:Table 3. Vapor P(t Sat.) 2.00 (212.42) 10 v Specific Volume Sat. Internal Energy Sat. Liquid Enthalpy Sat, Liquid Entropy Prom. MP Teme Sat. Sat. Vapor Nat. Vapor Sat Liquid Sat. Vapor Sat. 99.63 2600.3 2799,5 6.3409 Liquid Vaper Evap. Evap Evap. 10'v, 10v, h, 200 205 210 215 220 95.27 2570.6 2761.1 97.06 2582.8 2777.0 025 026 027 .028 029 64.97 1.0199 65.85 1.0204 66.70 - 1.0209 67.53 1.0214 68.33 1.0218 6204. 5980. 5772. 5579. 5398. 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.S 2467.4 271.93 2346.3 2618.2 275.61 2344.I 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 78179 9145 6.8904 7.8049 9246 6.8678 7.1924 9344 6.8459 7.7803 6.2608 6.2941 6.3259 6.3566 6.3861 98.80 2594.7 2792.3 TOU.50 2606.2 2807.2 102.15 2617.4 2821.7 225 230 235 240 245 6.4147 69.10 1.0223 70.60 1.0232 72.01 1.0241 73.36 1.0249 74.64 5229. 4922. 650. 4408. 4190. 289.20 2179.2 2468.4 295.45 2174.9 2470.3 301.37 2170.8 2472.1 307.01 2166 8 2473.8 312.39 2163.1 2475.5 289.23 2336.1 2625.3 295.48 2332.4 2627.8 301.40 2328 8 2630.2 307.05 2325.5 2632.5 312.43 2322.3 2634.7 9439 6.8247 7.7686 9622 6.7843 7.7465 9793 6.7463 7.7257 9956 6.7104 7.7061 1.0111 6.6764 7.6876 103.77 2628.3 2835.8 105.36 2638.9 2849.6 6.4423 106.91 2649.4 2863,2 6.4691 108.45 2659.6 2876.5 6.4952 109.95 2669.7 2889.6 6.5205 030 032 134 836 038 1.0257 75.87 77.05 78. 18 79.27 80.32 1.0265 1.0272 1.0279 1.0286 1.0293 3993. 3815 3652. 3503. 3367. 317.53 2159.,5 2477.0 322.47 2156.0 2478.5 327.22 2152.7 2479.9 331.78 2149,5 2481 3 336.19 2146.4 2482.6 317.58 2319.2 2636.8 322.51 2316.2 2638.7 327.26 2313.4 2640.6 331,83 2310.6 2642.5 336,23 2308.0 2644.2 1.0259 6.6441 7.6700 1.0400 6.6133 7,6534 1.0536 6.5839 7.6375 1.0666 6.5558 7.6223 1.0790 6.5288 7.6078 250 260 270 280 290 1I1.44 2679.6 2902.5 6.5453 114.36 2699.0 2927.7 6.5931 117.21 2717.9 2952.3 6.6388 120.01 2736.4 2976.4 6.6828 122.76 2754.6 3000.2 .040 042 044 046 48 6.7253 81.33 83.72 85.94 88.01 89.95 3240. 2964. 2732 2535, 2365. 340.44 2143.4 2483.9 350.48 2136,4 2486.8 359.79 2129.,8 2489.6 368.48 2123.6 2492.1 376.63 2117.8 2494 5 340.49 23054 2645.9 350.54 2299,3 2649.8 359.86 2293.6 2653.5 368.54 2288.3 2656.9 376.70 2283.3 2660.0 1.0910 6.5029 7.5939 1.1193 6.4422 7.5615 1.1453 6.3867 5320 1.1694 6.3354 7.5048 1.1919 6.2878 7.4797 050 1.0300 1.0316 1.0331 1.0346 1.0360 300 310 320 330 340 125.47 2772.6 3023.5 6.7664 128.14 2790.3 3046.6 130.79 2807.9 3069.5 133.40 2825.3 3092.1 136.00 2842.6 3114.6 6.9201 6.8063 6.8452 6.8831 060 65 070 675 080 085 090 1.0373 1.0386 95.14, 1.0398 1.0410 384.31 2112.4 2496.7 391.58 2107.2 2498.8 398.48 2102.3 2500.7 405.06 2097.6 2502.6 384,39 2278.6 2663.0 391.66 2274.! 2665.8 398.57 2269.8 2668.4 405.15 2265.7 2670.9 12130 6.2434 74564 1.2329 6.2017 74346 1.2517 6.1625 7.4141 1.2695 6.1254 7.3949 91.78 2217. 2087 1972. 1869. 93.50 350 360 370 380 390 138.57 2859.8 3137.0 6.9563 141.13 2877.0 3159.3 6.9917 143.66 2894.1 3181.4 7.0265 146.19 2911.2 3203.6 7.0606 148.70 2928.2 3225.6 7.0941 96.71
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