An ideal regenerative cycle is executed with steam generation at 10 MPa and 600 deg C. Before condensation at 0.005 MPa, steam is extracted for feedwater heating first at 2.5 MPa and second at 0.6 MPa. On the basis of 1 kg of throttle steam, find:

a. m₁ and m₂ in kg/kg

b. e_c in percent

c. e_e in percent

Reminder:

1. For values taken from the steam tables: Use them as is, do not round off.

2. For values obtained by interpolation and final answers obtained by solving, use FOUR (4) decimal places.
Transcribed Image Text:Table 3. Vapor .60 (158.85) P(t Sat.) 56 (156.17) 58 (157.53) 10 v 10' v 10' v 6.7600 315.7 2567.4 2756.8 Sat. 336.9 2565.1 2753.8 325.9 2566.3 2755.3 6.7714 6.7832 256.0 2448.2 2601.8 261.7 2459.6 2616.7 267.3 2470.8 2631.1 272.7 2481.6 2645.2 277.9 2492.2 2658.9 6.3732 6.4127 6.4507 6.4872 6.5224 6.3965 6.4354 100 105 110 115 120 277.0 2453.6 2608.7 282.9 2464.7 2623.1 288.7 2475.4 2637.1 294.3 2486.0 2650.8 299.8 2496.2 2664.1 6.4203 6.4585 6.4953 6.5307 266.2 2450.9 2605.3 272.0 2462.2 2619.9 277.6 2473.I 2634.1 6.4728 283.1 2483.8 2648:0 288.5 2494.2 2661.5- 6.5087 6.5434 6.5649 283.1 2502.5 2672.3 288.1 2512.6 2685.5 293.1 2522.5 2698.3 297.9 2532.2 2711.0 302.7 2541.7 2723.4 6.5563 125 130 135 140 145 305.2 2506.3 2677.2 310.5 2516.J 2690.0 315.7 2525.8 2702.6 320.8 2535.3 2715.0 325.9 2544.7 2727.2 6.5980 6.6300 6.6610 6.6912 6.7205 293.8 2504.4 2674.8 298.9 2514.4 2687.8 304.0 2524.2 2700.5 309.0 2533.8 2713.0 313.9 2543.2 2725.3 6.5769 6.6093 6.6406 6.6711 6.7007. 6.5890 6.6 208 6.6515 6.6814 150 160 170 180 190 330.8 2553.9 2739.2 340.6 2571.9 2762.7 350.2 2589.6 2785.7 359.6 2606.8 2808.2 368.9 2623.8 2830.4 6.7490 6.8040 6.8564 6.9067 6.9551 318.7 2552.5 2737.4 328.3 2570.7 2761.1 337.6 2588.5 2784.3 346.7 2605.8 2806.9 355.7 2622.9 2829.2 6.7295 6.7849 6.8377 6.8883 6.9370 307.5 2551.1 2735.6 316.7 2569.5 2759.5 325.8 2587.4 2782.8 334.7 2604.9 2805.7 343.4 2622.0 2828.1 6.7105 6.7663 6.8195 6.8705 6.9194 200 210 220 230 240 378.1 2640.5 2852.2 387.1 2657.1 2873.9 396.1 2673.4 2895.3 405.0 2689.7 2916.5 413.8 27059 2937.6 7.0018 7.0470 7.0909 7.1335 7.1750 364.6 2639.7 2851.2 6.9839 373.4 2656.3 2872.9, 7.0293 382.1 2672.8 2894.4 390.7 2689.1 2915.7 399.2 2705.3 2936.8 7.0733 7.1160 7.1577 352.0 2638.9 2850.1 - 6.9665 360.5 2655.6 2871.9 7.0121 369.0 267.2.1 2893.5 377.3 2688.5 2914.8 385.6 2704.7 2936.1 7.0562 7.0991 7.1409
Transcribed Image Text:Table 2. Saturation: Pressures Enthalpy Entropy Internal Energy Sat, Specific Volume Se. Vagor 10, Sat. Vapor Sat Liquid h, Sat. Vapor Sat, Liquid Sat. Evap. Temp Sat. Liquid Evap. Vapor Pres. MP Te Evap. Pre MP u, h, 10 657,3 548.59. 1991.9 2540.5 548.89 2172.4 2721.3 646.3 551.18 1990.0 2541.2 551.48 2170.7. 2722.I 635.7 553.72 1988.1 2541.8 625.4 556.23 1986.2 2542.4 615.4 558.71 1984.3 2543.0 1.6408 5.3801 7.0209 1.6472 5.3677 7.0149 554.02 2168.9 2723.0 1.6535 5.3555 7.0090 556.54 2167.2 2723.8 1.6597 5.3435 7.003) 559.02 2165.5 2724.5 1.6658 5.3317 6.997 16 130.60 1.0703 131.21 1.0709 131.81 1.0715 132.39 1.0720 132.97 1.0726 .15 .76 .77 .78 .79 275 280 200 205 561.47 2163.8 2725.3 1.6718 5.3201 6.9910 380 305 310 315 320 133.55 1.0732 605.8 561.15 1982.4 2543.6 134.11 1.0737 596.5 563.56. 1980.6 2544.1 563.88 2162.2, 2726.1 1.6777 5.3087 6 9 134.67 1.0743 135.22 1.0749 135.76 1.0754 587.5 565.94 1978.8 2544.7 566.27 2160.6 2726.8 1.6835 5.2974 6.9810 578.7 568.29 1977.0 2545.3 570.2 .80 .81 .82 .83 .84 568.62 2158.9 2727.6 1.6893 5.2863 6.9756 $70.95 2157.3 2728.3 1.6950 5.2754 6.9704 570.61 1975.2 2545.8 573.25 2155.8 2729.0 1.7006 5.2646 6.965) 325 330 335 340 136.30 1.0759 136.83 1.0765 137.35 1.0770 137.87 1.0775 138.38 562.0 554.0 546.3 538.7 $31.4 572.90 1973.5 2546.4 $75.16 1971.7 2546.9 575.52 2154.2 2729.7 1.7061 5.2540 6.9601 577.40 1970.0 2547.4 579.61 1968.3 2547.9 581.79 1966.6 2548.4 577.76- 2152.6 2730.4 1.7116 5.2435 6.9551 579.97 2151.I 2731.1 1.7169 5.2332 6.9502 582.16 2149.6 2731.8 · 1.7222 5.2230 6.9453 .85 86 .87 -88 .89 1.0781 524.3 517.3 510.6 504.0 497.6 583.95 1965.0 2548.9 586.09 1963.3 2549.4 S88.20 1961.7 2549.9 $90.29 1960.1 2550.4 592.36 1958.5 2550.9 584.33 2148.1 2732.4 1.7275 5.2130 6.940s 586.47 2146.6 2733.1 1.7327 5.2031 6.9358 588.59 2145.1. 2733.7 1.7378 5.1933 6.9311 590.68 2143.7 2734.4 1.7428 5.1836 6.9265 592.75 2142.2 2735.0 .90 .91 .92 .93 .94 138.88 1.0786 139.38 1.0791 139.87 1.0796 140.36 1.0801 140.84 370 1.0806 1.7478 5.1741 6.9219 .95 .96 .97 .98 .99 141.32 1.081I 141.79 375 380 385 390 395 1.0816 142.26 1.0821 142.72 1.0826 1.0831. 491.4 485.3 479.4 473.6 468.0 594.81 2140.8 2735.6 1.7528 5.1647 6.9175 596.83 2139.4 2736.2 1.7577 5.1554 6.9130 598.84 2138.0 2736.8 1.7625 5.1462 6.9087 600.41 1952.3 2552.7 600.83 2136.6 2737.4 1.7673 5.1371 6.9044 1.7720 5.1281 6.9001 594.40 1956.9 2551.3 596.42 1955.4 2551.8 598.43 1953.8 2552.2 143.18 602.37 1950.8 2553.1 602.80 2135.2 2738.0 604.74 2133.8 2738.6 608.59 2131.1 2739.7 1.7858 5.1018 6.8877 612.36 2128.4 2740.8 1.7948 5.0848 6.8796 616.06 2125.8 2741.9 619.68 2123.2 2742.9 1.06 1.0 1.0 1.0 1.0 1.0836 604.31 1949.3 2553.6 608.14 1946.3 2554.4 611.90 1943.4 2555.3 615.59 1940.5 2556.1 619.21 1937.6 2556.9 1.7766 5.1193 6.8959 41 .42 43 44 143.63 144.53 1.0845 145.40 462.5 451.9 441.7 432.1 422,8 1.0855 1.0864 1.0873 1.8036 5.0681 6.8717 1.8122 5.0518 6.8641 146.26 147.10 1.8207 5.0359 6.8565 626.26 1932.1 2558.4 626.76 2118.2 2744.9 1.8290 5.0202 6.8492 629.70 1929,4 2559.1 630.21 2115.7 2745.9 1.8371 5.0049 6.8420 633.60 2113.2 2746.8 1.8451 4.9898 6.8349 1.8530 4.97S1 6.8280 1.1 1. 1. 1. 623.25 2120.7 2743.9 A5 46 47 1.0882 148.74 1.0891 149.54 1.0900 150.32 147.93 414.0 405.5 397.4 389.6 382.1 622.77 1934.9 2557.6 1.0909 151.10 1.0917 633.08 1926.8 2559.8 636.40 1924.1 2560.6 49 636.94 2110.8 2747.8 50 51 52 53 54 639.68 1921.6 2561.2 640.23 2108.5 2748.7 1.8607 4.9606 6.8213 642.90 1919.O 2561.9 643.46 2106.1 2749.6 1:8682 4.9464 6.8146 646.65 2103.8 2750.5 649.78 2101.5 2751.3 652.87 2099.3 2752.1 151.86 1.0926 374.9 368.0 361.3 354.9 348.7 152.60 1.0934 153.34 1.0942 154.06 1.0951 154.78 646.08 1916.5 2562.6 649.20 1914.0 2563.2 652.28 1911.6 2563.9 1.8757 4.9324 6.8081 1.8830 4.9187 6.8017 1.8902 4.9052 6.79SS 1.0959 55 .56 57 58 99 155.48 1.0967 156.17 1.0975 156.86 1.0983 157.53 342.7 336.9 331.3 325.9 320.7 655.32 1909.2 2564.5 658.32 1906.8 2565.1 658.93 2094.8 2753.8 661.27 1904.4 2565.7 661.90 2092.7 2754.5 664.18 1902.I 2566.3 667.06 1999.8 2566.8 655.93 2097.0 2753.0 1.8973 4.8920 6.7893 1.9043 4.8789 6.7832 1.9112 4.8661 6.7773 1.9180 4.8535 6.7714 1.9246 4.8411 6.7657 1.0991 664.83 2090.5 2755.3 667.71 2088.4 2756.1 158.20 1.0999 .60 .61 .62 .63 54 158.85 1.1006 315.7 310.8 306.0 301.5 297.0 669.90 1897.5 2567.4 672.70 1895.3 2568.0 675.47 1893.0 2568.5 678.20 1890.8 2569.0 680.90 1888.7 2569.6 670.56 2086.3 2756.8 673.37 2084.2 2757.5 1.9377 4.8168 6.7545 676.15 2082.1 2758.3 678.89 2080.1 2759.0 681.60 2078.0 2759.6 159.50 1,1014 1.9312 4.8288 6.7600 160.14 1.1021 160.77 1.1029 161.39 1.1036 1.9441 4.8049 6.7490 1.9504 4.7932 6.7436 1.9566 4.7817 6.7383 .65 .66 .67 68 162.01 1.1044 162.61 1.1051 163.21 292.7 288.5 284.4 280.5 276.6 683.56 1886.5 2570.1 686.20 1884.4 2570.6 688.80 1882.3 2571.1 691.38 1880.2 2571.6 693.93 1878.1 2572.0 684.28 2076.0 2760.3 686.93 2074.0 2761.0 689.55 2072.1 2761.6 692.13 2070.1 2762.3 694.69 2068.2 2762.9 1.9627 4.7703 6.7331 1.9688 4.7591 6.7279 1.9748 4.7481 6.7228 1.9807 4.7372 6.7178 1.9865 4.7264 6.7129 1.1058 163.81 1.1066 164.39 1.1073 70 71 72 73 74 164.97 165.55 166.11 166.67 167.23 1.1108 1.1080 1.1087 1.1094 1.1101 272.9 269.2 265.7 262.2 258.9 696.44 1876.1 2572.5 698.93 1874.0 2573.0 701.40 1872.0 2573.4 703.84 1870.0 2573.9 706.25 1868.1 2574.3 697.22 2066.3 2763.5 699.72 2064.4 2764.1 702.20 2062.5 2764.7 704.64 2060.7 2765.3 707.07 2058.8 2765.9 1.9922 4.7158 6.7080 1.9979 4.7053 6.7032 2.0035 4.6950 6.6985 2.0091 4.6848 6.6938 2.0146 4.6747 -6.6892

Question

An ideal regenerative cycle is executed with steam generation at 10 MPa and 600 deg C. Before condensation at 0.005 MPa, steam is extracted for feedwater heating first at 2.5 MPa and second at 0.6 MPa. On the basis of 1 kg of throttle steam, find:

a. m₁ and m₂ in kg/kg

b. e_c in percent

c. e_e in percent

Reminder:

1. For values taken from the steam tables: Use them as is, do not round off.

2. For values obtained by interpolation and final answers obtained by solving, use FOUR (4) decimal places.

Table 3. Vapor
.60 (158.85)
P(t Sat.)
56 (156.17)
58 (157.53)
10 v
10' v
10' v
6.7600
315.7 2567.4 2756.8
Sat.
336.9 2565.1 2753.8
325.9 2566.3 2755.3 6.7714
6.7832
256.0 2448.2 2601.8
261.7 2459.6 2616.7
267.3 2470.8 2631.1
272.7 2481.6 2645.2
277.9 2492.2 2658.9
6.3732
6.4127
6.4507
6.4872
6.5224
6.3965
6.4354
100
105
110
115
120
277.0 2453.6 2608.7
282.9 2464.7 2623.1
288.7 2475.4 2637.1
294.3 2486.0 2650.8
299.8 2496.2 2664.1
6.4203
6.4585
6.4953
6.5307
266.2 2450.9 2605.3
272.0 2462.2 2619.9
277.6 2473.I 2634.1 6.4728
283.1 2483.8 2648:0
288.5 2494.2 2661.5-
6.5087
6.5434
6.5649
283.1 2502.5 2672.3
288.1 2512.6 2685.5
293.1 2522.5 2698.3
297.9 2532.2 2711.0
302.7 2541.7 2723.4
6.5563
125
130
135
140
145
305.2 2506.3 2677.2
310.5 2516.J 2690.0
315.7 2525.8 2702.6
320.8 2535.3 2715.0
325.9 2544.7 2727.2
6.5980
6.6300
6.6610
6.6912
6.7205
293.8 2504.4 2674.8
298.9 2514.4 2687.8
304.0 2524.2 2700.5
309.0 2533.8 2713.0
313.9 2543.2 2725.3
6.5769
6.6093
6.6406
6.6711
6.7007.
6.5890
6.6 208
6.6515
6.6814
150
160
170
180
190
330.8 2553.9 2739.2
340.6 2571.9 2762.7
350.2 2589.6 2785.7
359.6 2606.8 2808.2
368.9 2623.8 2830.4
6.7490
6.8040
6.8564
6.9067
6.9551
318.7 2552.5 2737.4
328.3 2570.7 2761.1
337.6 2588.5 2784.3
346.7 2605.8 2806.9
355.7 2622.9 2829.2
6.7295
6.7849
6.8377
6.8883
6.9370
307.5 2551.1 2735.6
316.7 2569.5 2759.5
325.8 2587.4 2782.8
334.7 2604.9 2805.7
343.4 2622.0 2828.1
6.7105
6.7663
6.8195
6.8705
6.9194
200
210
220
230
240
378.1 2640.5 2852.2
387.1 2657.1 2873.9
396.1 2673.4 2895.3
405.0 2689.7 2916.5
413.8 27059 2937.6
7.0018
7.0470
7.0909
7.1335
7.1750
364.6 2639.7 2851.2 6.9839
373.4 2656.3 2872.9, 7.0293
382.1 2672.8 2894.4
390.7 2689.1 2915.7
399.2 2705.3 2936.8
7.0733
7.1160
7.1577
352.0 2638.9 2850.1 - 6.9665
360.5 2655.6 2871.9 7.0121
369.0 267.2.1 2893.5
377.3 2688.5 2914.8
385.6 2704.7 2936.1
7.0562
7.0991
7.1409

Table 2. Saturation: Pressures
Enthalpy
Entropy
Internal Energy
Sat,
Specific Volume
Se.
Vagor
10,
Sat.
Vapor
Sat
Liquid
h,
Sat.
Vapor
Sat,
Liquid
Sat.
Evap.
Temp
Sat.
Liquid
Evap.
Vapor
Pres.
MP
Te
Evap.
Pre
MP
u,
h,
10
657,3 548.59. 1991.9 2540.5 548.89 2172.4 2721.3
646.3 551.18 1990.0 2541.2 551.48 2170.7. 2722.I
635.7 553.72 1988.1 2541.8
625.4 556.23 1986.2 2542.4
615.4 558.71 1984.3 2543.0
1.6408 5.3801 7.0209
1.6472 5.3677 7.0149
554.02 2168.9 2723.0 1.6535 5.3555 7.0090
556.54 2167.2 2723.8 1.6597 5.3435 7.003)
559.02 2165.5 2724.5 1.6658 5.3317 6.997
16
130.60 1.0703
131.21 1.0709
131.81 1.0715
132.39 1.0720
132.97 1.0726
.15
.76
.77
.78
.79
275
280
200
205
561.47 2163.8 2725.3 1.6718 5.3201 6.9910
380
305
310
315
320
133.55 1.0732 605.8 561.15 1982.4 2543.6
134.11 1.0737 596.5 563.56. 1980.6 2544.1 563.88 2162.2, 2726.1 1.6777 5.3087 6 9
134.67 1.0743
135.22 1.0749
135.76 1.0754
587.5 565.94 1978.8 2544.7 566.27 2160.6 2726.8 1.6835 5.2974 6.9810
578.7 568.29 1977.0 2545.3
570.2
.80
.81
.82
.83
.84
568.62 2158.9 2727.6 1.6893 5.2863 6.9756
$70.95 2157.3 2728.3 1.6950 5.2754 6.9704
570.61 1975.2 2545.8
573.25 2155.8 2729.0 1.7006 5.2646 6.965)
325
330
335
340
136.30 1.0759
136.83 1.0765
137.35 1.0770
137.87 1.0775
138.38
562.0
554.0
546.3
538.7
$31.4
572.90 1973.5 2546.4
$75.16 1971.7 2546.9 575.52 2154.2 2729.7 1.7061 5.2540 6.9601
577.40 1970.0 2547.4
579.61 1968.3 2547.9
581.79 1966.6 2548.4
577.76- 2152.6 2730.4 1.7116 5.2435 6.9551
579.97 2151.I 2731.1 1.7169 5.2332 6.9502
582.16 2149.6 2731.8 · 1.7222 5.2230 6.9453
.85
86
.87
-88
.89
1.0781
524.3
517.3
510.6
504.0
497.6
583.95 1965.0 2548.9
586.09 1963.3 2549.4
S88.20 1961.7 2549.9
$90.29 1960.1 2550.4
592.36 1958.5 2550.9
584.33 2148.1 2732.4 1.7275 5.2130 6.940s
586.47 2146.6 2733.1 1.7327 5.2031 6.9358
588.59 2145.1. 2733.7 1.7378 5.1933 6.9311
590.68 2143.7 2734.4 1.7428 5.1836 6.9265
592.75 2142.2 2735.0
.90
.91
.92
.93
.94
138.88
1.0786
139.38
1.0791
139.87
1.0796
140.36 1.0801
140.84
370
1.0806
1.7478 5.1741 6.9219
.95
.96
.97
.98
.99
141.32 1.081I
141.79
375
380
385
390
395
1.0816
142.26 1.0821
142.72 1.0826
1.0831.
491.4
485.3
479.4
473.6
468.0
594.81 2140.8 2735.6 1.7528 5.1647 6.9175
596.83 2139.4 2736.2 1.7577 5.1554 6.9130
598.84 2138.0 2736.8 1.7625 5.1462 6.9087
600.41 1952.3 2552.7 600.83 2136.6 2737.4 1.7673 5.1371 6.9044
1.7720 5.1281 6.9001
594.40 1956.9 2551.3
596.42 1955.4 2551.8
598.43 1953.8 2552.2
143.18
602.37 1950.8 2553.1
602.80 2135.2 2738.0
604.74 2133.8 2738.6
608.59 2131.1 2739.7 1.7858 5.1018 6.8877
612.36 2128.4 2740.8 1.7948 5.0848 6.8796
616.06 2125.8 2741.9
619.68 2123.2 2742.9
1.06
1.0
1.0
1.0
1.0
1.0836
604.31 1949.3 2553.6
608.14 1946.3 2554.4
611.90 1943.4 2555.3
615.59 1940.5 2556.1
619.21 1937.6 2556.9
1.7766 5.1193 6.8959
41
.42
43
44
143.63
144.53 1.0845
145.40
462.5
451.9
441.7
432.1
422,8
1.0855
1.0864
1.0873
1.8036 5.0681 6.8717
1.8122 5.0518 6.8641
146.26
147.10
1.8207 5.0359 6.8565
626.26 1932.1 2558.4 626.76 2118.2 2744.9 1.8290 5.0202 6.8492
629.70 1929,4 2559.1 630.21 2115.7 2745.9 1.8371 5.0049 6.8420
633.60 2113.2 2746.8 1.8451 4.9898 6.8349
1.8530 4.97S1 6.8280
1.1
1.
1.
1.
623.25 2120.7 2743.9
A5
46
47
1.0882
148.74 1.0891
149.54 1.0900
150.32
147.93
414.0
405.5
397.4
389.6
382.1
622.77 1934.9 2557.6
1.0909
151.10 1.0917
633.08 1926.8 2559.8
636.40 1924.1 2560.6
49
636.94 2110.8 2747.8
50
51
52
53
54
639.68 1921.6 2561.2 640.23 2108.5 2748.7 1.8607 4.9606 6.8213
642.90 1919.O 2561.9 643.46 2106.1 2749.6 1:8682 4.9464 6.8146
646.65 2103.8 2750.5
649.78 2101.5 2751.3
652.87 2099.3 2752.1
151.86
1.0926
374.9
368.0
361.3
354.9
348.7
152.60
1.0934
153.34 1.0942
154.06 1.0951
154.78
646.08 1916.5 2562.6
649.20 1914.0 2563.2
652.28 1911.6 2563.9
1.8757 4.9324 6.8081
1.8830 4.9187 6.8017
1.8902 4.9052 6.79SS
1.0959
55
.56
57
58
99
155.48 1.0967
156.17 1.0975
156.86 1.0983
157.53
342.7
336.9
331.3
325.9
320.7
655.32 1909.2 2564.5
658.32 1906.8 2565.1 658.93 2094.8 2753.8
661.27 1904.4 2565.7 661.90 2092.7 2754.5
664.18 1902.I 2566.3
667.06 1999.8 2566.8
655.93 2097.0 2753.0
1.8973 4.8920 6.7893
1.9043 4.8789 6.7832
1.9112 4.8661 6.7773
1.9180 4.8535 6.7714
1.9246 4.8411 6.7657
1.0991
664.83 2090.5 2755.3
667.71 2088.4 2756.1
158.20
1.0999
.60
.61
.62
.63
54
158.85
1.1006
315.7
310.8
306.0
301.5
297.0
669.90 1897.5 2567.4
672.70 1895.3 2568.0
675.47 1893.0 2568.5
678.20 1890.8 2569.0
680.90 1888.7 2569.6
670.56 2086.3 2756.8
673.37 2084.2 2757.5 1.9377 4.8168 6.7545
676.15 2082.1 2758.3
678.89 2080.1 2759.0
681.60 2078.0 2759.6
159.50
1,1014
1.9312 4.8288 6.7600
160.14
1.1021
160.77 1.1029
161.39 1.1036
1.9441 4.8049 6.7490
1.9504 4.7932 6.7436
1.9566 4.7817 6.7383
.65
.66
.67
68
162.01 1.1044
162.61 1.1051
163.21
292.7
288.5
284.4
280.5
276.6
683.56 1886.5 2570.1
686.20 1884.4 2570.6
688.80 1882.3 2571.1
691.38 1880.2 2571.6
693.93 1878.1 2572.0
684.28 2076.0 2760.3
686.93 2074.0 2761.0
689.55 2072.1 2761.6
692.13 2070.1 2762.3
694.69 2068.2 2762.9
1.9627 4.7703 6.7331
1.9688 4.7591 6.7279
1.9748 4.7481 6.7228
1.9807 4.7372 6.7178
1.9865 4.7264 6.7129
1.1058
163.81
1.1066
164.39
1.1073
70
71
72
73
74
164.97
165.55
166.11
166.67
167.23 1.1108
1.1080
1.1087
1.1094
1.1101
272.9
269.2
265.7
262.2
258.9
696.44 1876.1 2572.5
698.93 1874.0 2573.0
701.40 1872.0 2573.4
703.84 1870.0 2573.9
706.25 1868.1 2574.3
697.22 2066.3 2763.5
699.72 2064.4 2764.1
702.20 2062.5 2764.7
704.64 2060.7 2765.3
707.07 2058.8 2765.9
1.9922 4.7158 6.7080
1.9979 4.7053 6.7032
2.0035 4.6950 6.6985
2.0091 4.6848 6.6938
2.0146 4.6747 -6.6892

Accepted Answer

Answered: Image /qna-images/answer/b7fb7583-0e5c-4434-862f-68f6eb0b4b4a.jpg