Steam undergoes an Isentropic process where it is initially at 1.05 MPa and 304C. The isentropic process causes its pressure to drop to 30 kPa. Find the tsat2, dryness, and enthalpy change. (69.10C, 90.4%, -657.34 kJ/kg)

Introduction to Chemical Engineering Thermodynamics
8th Edition
ISBN:9781259696527
Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Publisher:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Chapter1: Introduction
Section: Chapter Questions
Problem 1.1P
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Use the given values at the table. Do not round off it. 

 

 

Steam undergoes an Isentropic process where it is initially at 1.05 MPa
and 304C. The isentropic process causes its pressure to drop to 30 kPa. Find
the tsat2, dryness, and enthalpy change. (69.1oC, 90.4%, -657.34 kJ/kg)
1.05 (182.04)
(t Sat.)
1.0 (179.91)
10 v
10 v
6.5696
Sat.
6.5865
185.60 2585.1 2780.0
194.44 2583.6 2778.1
179.07 2532.0 2711.1
182.29 2542.9 2725.1 6.4669
185.43 2553.4 2738.9
188.50 2563.8 2752.3
150
155
160
165
170
6.4342
6.4984
6.3289
172.60 2539.2 2720.4
175.66 2550.0 2734.5
178.64 2560.6
6.4356
6.4678
2748.2
6.4989
175
180
185
190
195
6.5289
6.5580
191.53 2573,9 2765.4
194.50 2583.8 2778.3 6.5870
197.42 2593.6 2791.0 6.6148
200.30 2603.2 2803.5 6.6419
203.15 2612.6 2815.8 6.6682
181.56 2570.9 2761.6
184.44 2581.0 · 2774.7
187.26 2590.9 2787.5 6.5863
190.04 2600.7 2800.2 6.6137
192.79 2610.2 2812.7 6.6405
6.5584
206.0 2621.9 2827.9 6.6940
211.5 2640.2 2851.7 6.7437
216.9 2658.0 2874.9 6.7914
222.2 2675.6 2897.8 6.8374
227.5 2692.9 2920.4 6.8817
195.49 2619.7 2824.9 5.6666
200.81 2638.1 2849.0 6.7169
206.02 2656.2 2872.5 6.7651
211.14 2673.9 2895.6 6.8114
216.18 2691.3 2918.3
200
210
220
230
240
6.8561
232.7 2709.9 2942.6 6.9247
237.8 2726.8 2964.6 6.9664
242.9 2743.6 2986.5 7.0069
248.0 2760.2 3008.2 7.0465
253.0 2776.7 3029.7 7.0851
221.2 2708.5 2940.7
226.1 2725.5 2962.9
231.0 2742.3 2984.8
235.8 2759.1 3006.6
240.6 2775.7 3028.3
6.8994
6.9414
6.9822
7.0219
7.0607
250
260
270
280
290
245.3 2792.2 3049.8
250.1 2808.7 3071.3 7.1358
254.8 2825.2 3092.7
259.5 2841.6 3114.1
264.1 2858.0 3135.4
300
310
320
330
340
7.0986
257.9 2793.2 3051.2 7.1229
262.9 2809.7 3072.6 7.1599
267.8 2826.1 3093.9 7.1962
272.7 2842.5 3115.2 7.2318
277.6 2858.8 3136.4 7.2667
7.1722
7.2079
7.2429
Specific Volume
St.
Sat.
Vapor
Liquid
10S
10'v
Internal Energy
Sat,
Liquid
Enthalpy
Sat,
Liquid
hy
Entropy
Prems.
MP
Sat.
Vapor
Sat.
Liquid
Sat.
Vapor
Temp
Evap.
Sat.
Vapor
Evap.
Evap.
t.
u,
h,
Su
.025
.026
.027
.028
.029
64.97 1.0199
65.85 1.0204
66.70 1.0209
1.0214
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 2181.5 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
67.53
68.33
1.0218
.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
2336.1 2625.3
.030
.032
.034
.036
.038
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
289.2.
295.48 2332.4 2627.8
301.40 2328.8 2630.2
307.05 2325.5 2632.5
312.43 2322.3 2634.7
1.0257
Transcribed Image Text:Steam undergoes an Isentropic process where it is initially at 1.05 MPa and 304C. The isentropic process causes its pressure to drop to 30 kPa. Find the tsat2, dryness, and enthalpy change. (69.1oC, 90.4%, -657.34 kJ/kg) 1.05 (182.04) (t Sat.) 1.0 (179.91) 10 v 10 v 6.5696 Sat. 6.5865 185.60 2585.1 2780.0 194.44 2583.6 2778.1 179.07 2532.0 2711.1 182.29 2542.9 2725.1 6.4669 185.43 2553.4 2738.9 188.50 2563.8 2752.3 150 155 160 165 170 6.4342 6.4984 6.3289 172.60 2539.2 2720.4 175.66 2550.0 2734.5 178.64 2560.6 6.4356 6.4678 2748.2 6.4989 175 180 185 190 195 6.5289 6.5580 191.53 2573,9 2765.4 194.50 2583.8 2778.3 6.5870 197.42 2593.6 2791.0 6.6148 200.30 2603.2 2803.5 6.6419 203.15 2612.6 2815.8 6.6682 181.56 2570.9 2761.6 184.44 2581.0 · 2774.7 187.26 2590.9 2787.5 6.5863 190.04 2600.7 2800.2 6.6137 192.79 2610.2 2812.7 6.6405 6.5584 206.0 2621.9 2827.9 6.6940 211.5 2640.2 2851.7 6.7437 216.9 2658.0 2874.9 6.7914 222.2 2675.6 2897.8 6.8374 227.5 2692.9 2920.4 6.8817 195.49 2619.7 2824.9 5.6666 200.81 2638.1 2849.0 6.7169 206.02 2656.2 2872.5 6.7651 211.14 2673.9 2895.6 6.8114 216.18 2691.3 2918.3 200 210 220 230 240 6.8561 232.7 2709.9 2942.6 6.9247 237.8 2726.8 2964.6 6.9664 242.9 2743.6 2986.5 7.0069 248.0 2760.2 3008.2 7.0465 253.0 2776.7 3029.7 7.0851 221.2 2708.5 2940.7 226.1 2725.5 2962.9 231.0 2742.3 2984.8 235.8 2759.1 3006.6 240.6 2775.7 3028.3 6.8994 6.9414 6.9822 7.0219 7.0607 250 260 270 280 290 245.3 2792.2 3049.8 250.1 2808.7 3071.3 7.1358 254.8 2825.2 3092.7 259.5 2841.6 3114.1 264.1 2858.0 3135.4 300 310 320 330 340 7.0986 257.9 2793.2 3051.2 7.1229 262.9 2809.7 3072.6 7.1599 267.8 2826.1 3093.9 7.1962 272.7 2842.5 3115.2 7.2318 277.6 2858.8 3136.4 7.2667 7.1722 7.2079 7.2429 Specific Volume St. Sat. Vapor Liquid 10S 10'v Internal Energy Sat, Liquid Enthalpy Sat, Liquid hy Entropy Prems. MP Sat. Vapor Sat. Liquid Sat. Vapor Temp Evap. Sat. Vapor Evap. Evap. t. u, h, Su .025 .026 .027 .028 .029 64.97 1.0199 65.85 1.0204 66.70 1.0209 1.0214 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 2181.5 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 67.53 68.33 1.0218 .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 2336.1 2625.3 .030 .032 .034 .036 .038 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 2475.5 289.2. 295.48 2332.4 2627.8 301.40 2328.8 2630.2 307.05 2325.5 2632.5 312.43 2322.3 2634.7 1.0257
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