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Complete solution and units please. Use the sleam tables provided, and use 4 decimal places for solving. Final answers are shown in 2 decimal places. Draw the T-S diagram properly with respect to the saturation line. 2. A steam power plant uses the ideal Regenarative Rankine cycle with single open feedwater heater where the steam enters the high peremure turbine at 4 μPa and 500c. ot partially expands to 600 kPa then some steam is extracted at this point. The remaining steam expands and enters the condenser at 10 kPa. Sketch the schematic diagram and the TS diagram with labeled points, and solve for marr taken for feedwater heating, Qa, Qr, Wt, Wp. Whet, thermal efficienc and Steam rate. Neglect the condensate pump work!" Ansover: 20.01%, 2286.40 kJ. 1457 51 kJ 832.54 kJ 1 kg kg 3.74 k3 ку 828-89 k3 3.6.25% 1 4.34 ку kg ' I 41 kuh

Complete solution and units please. Use the sleam tables provided, and use 4 decimal places for solving. Final answers are shown in 2 decimal places. Draw the T-S diagram properly with respect to the saturation line. 2. A steam power plant uses the ideal Regenarative Rankine cycle with single open feedwater heater where the steam enters the high peremure turbine at 4 μPa and 500c. ot partially expands to 600 kPa then some steam is extracted at this point. The remaining steam expands and enters the condenser at 10 kPa. Sketch the schematic diagram and the TS diagram with labeled points, and solve for marr taken for feedwater heating, Qa, Qr, Wt, Wp. Whet, thermal efficienc and Steam rate. Neglect the condensate pump work!" Ansover: 20.01%, 2286.40 kJ. 1457 51 kJ 832.54 kJ 1 kg kg 3.74 k3 ку 828-89 k3 3.6.25% 1 4.34 ку kg ' I 41 kuh

Elements Of Electromagnetics
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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ܕ 13 Sat. 100 105 110 115 120 125 130 135 140 145 150 160 170 180 190 200 210 220 230 240 250 260 270 280 290 300 310 h 336.9 2565.1 2753.8 6.7832 277.0 2453.6 2608.7 6.4203 282.9 2464.7 2623.1 6.4585 288.7 2475.4 2637.1 6.4953 294.3 2486.0 2650.8 6.4507 6.5307 .4x11 299.8 2496.2 2664.1 6.5649 6.3224 6.5980 ..353 6.6300 6.5890 305.2 2506.3 2677.2 310.5 2516.1 2690.0 315.7 2525.8 2702.6 6.6610 320.8 2535.3 2715.0 6.6912 325.9 2544.7 2727.2 6.7205 6.6208 6.6515 6.6814 6.7105 307.5 2551.1 2735.6 316.7 2569.5 2759.5 6.7663 330.8 2553.9 2739.2 6.7490 340.6 2571.9 2762.7 6.8040 350.2 2589.6 2785.7 6.8564 359.6 2606.8 2808.2 6.9067 -368.9 2623.8 2830.4 6.9551 6.8195 325.8 2587.4 2782.8 334.7 2604.9 2805.7 343.4 2622.0 2828.1 6.8705 6.9194 7.0018 378.1 2640.5 2852.2 387.1 2657.1 2873.9 7.0470 396.1 2673.4 2895.3 7.0909 405.0 2689.7 2916.5 7.1335 413.8 2705.9 2937.6 7.1750 352.0 2638.9 2850.1 6.9655 360.5 2655.6 2871.9 7.0121 369.0 2672.1 2893.5 7.0562 377.3 2688.5 2914.8 7.0991 385.6 2704.7 2936.1 7.1409 7.1816 7.2214 422.6 2721.9 2958.6 7.2155 431.3 2738.0 2979.5 7.2551 440.0 2753.9 3000.3 7.2939 448.7 2769.9 3021.2 7.3318 457.3 2785.8 3041.9 7.3690 393.8 2720.9 2957.2 402.0 2737.0 2978.2 410.2 2753.0 2999.1 418.3 2769.0 3020.0 426.3 2785.0 3040.8 7,2603 7.2984 7.3357 465.9 2801.8 3062.7 7.4056 474.4 2817.7 3083.4 7.4415 7.3724 434.4 2801.0 3061.6 442.4 2817.0 3082.5 7.4084 . 4.0 (250.40) 4.1 (251.87) p (t Sat.) 13 13 6.0701 48.53 2601.9 2800.9 6.0597 49.78 2602.3 2801.4 Sat. 240 6.0297 47.04 2580.7 2773.6 6.0074 245 48.60 2585.9 2780.3 48.13 2596.3 2793,6 6.0459 250 49.17 2611.1 2812.7 6.0672 6.1026 6.1362 6.1683 6.1990 49.69 2601.1 27999 50.74 2615.5 2818.5 51.74 2629.4 2836.3 52.71 2642.7 2853.5 53.65 2655.5 2870.1 260 6.0822 255 50.17 2625.2 2830.9 6.1165 51.14 2638.8 2848.5 6.1493 52.07 2651.9 2865.4 6.1805 265 270 275 54.57 2667.9 2886.2 6.2285 52.98 2664.5 2881.7 6.2105 53.86 2676.7 2897.6 6.2568 6.2393 55.46 2680.0 2901.8 280 6.2842 6.2671 56.33 2691.7 2917.0 285 54.72 2688.7 2913.0 55.56 2700.3 2928.1 6.2940 290 57.18 2703.2 2931.9 6.3108 58.02 2714.4 2946.4 6.3365 56.39 2711.6 2942.8 6.3200 295 300 310 6.3453 57.20 2722.7 2957.2 58.77 2744.3 2985.3 6.3939 6.4401 60.30 2765.2 3012.5 61.79 2785.6 3038.9 6.4843 330 63.25 2805.4 3064.8 58.84 2725.3 2960.7 6.3615 60.44 2746.7 2988.5 6.4095 61.99 2767.4 30.15.4 6.4553 63.51 2787.6 3041.6 6.4991 6.5413 64.99 2807.3. 3067.3 320 6.5268 340 350 360 66.45 2826.7 3092.5 6.5821 67.88 2845.7 3117.2 6.6215 69.29 2864.6 3141.7 6.6598 70.68 2883.2 3165.9 6.6971 6.7335 72.05 2901.6 3189.8 64.68 2824.9, 3090.1 16.5678 66.08 2844.1 3115.0 6.6075 67.47 2863.0 3139.6 6.6460 68.83 2881.7 3163.9 6.6834 380 390 70.18 2900.2 3188.0 6.7200 370 ܐA ܐܐ1 ntܐ .60 (158.85) U 315.7 2567.4 2756.8 256.0 2448.2 2601.8 261.7 2459.6 2616.7 267.3 2470.8 2631.1 14 ܤ1 ܬ ?4816245ܐ 7ܐܐܐ h58ܐ ܐܐ49ܐ 79ܐܐ 283.1 2502.5 2672.3 288.1 2512.6 2685 5 6983ܐ ܝܐܐšܐ ܐܨܐ ܐܐ ܐܐ ܐܐܐܪܐ ܙ7ܙܐ 34ܐܐܐ ܐܐ4ܝܐ ܐ.ܐ30 ܐ ܂ 6.7600 6.3732 ܐܐܐ4ܙ ܘܐ ܩ ܀
Transcribed Image Text:ܕ 13 Sat. 100 105 110 115 120 125 130 135 140 145 150 160 170 180 190 200 210 220 230 240 250 260 270 280 290 300 310 h 336.9 2565.1 2753.8 6.7832 277.0 2453.6 2608.7 6.4203 282.9 2464.7 2623.1 6.4585 288.7 2475.4 2637.1 6.4953 294.3 2486.0 2650.8 6.4507 6.5307 .4x11 299.8 2496.2 2664.1 6.5649 6.3224 6.5980 ..353 6.6300 6.5890 305.2 2506.3 2677.2 310.5 2516.1 2690.0 315.7 2525.8 2702.6 6.6610 320.8 2535.3 2715.0 6.6912 325.9 2544.7 2727.2 6.7205 6.6208 6.6515 6.6814 6.7105 307.5 2551.1 2735.6 316.7 2569.5 2759.5 6.7663 330.8 2553.9 2739.2 6.7490 340.6 2571.9 2762.7 6.8040 350.2 2589.6 2785.7 6.8564 359.6 2606.8 2808.2 6.9067 -368.9 2623.8 2830.4 6.9551 6.8195 325.8 2587.4 2782.8 334.7 2604.9 2805.7 343.4 2622.0 2828.1 6.8705 6.9194 7.0018 378.1 2640.5 2852.2 387.1 2657.1 2873.9 7.0470 396.1 2673.4 2895.3 7.0909 405.0 2689.7 2916.5 7.1335 413.8 2705.9 2937.6 7.1750 352.0 2638.9 2850.1 6.9655 360.5 2655.6 2871.9 7.0121 369.0 2672.1 2893.5 7.0562 377.3 2688.5 2914.8 7.0991 385.6 2704.7 2936.1 7.1409 7.1816 7.2214 422.6 2721.9 2958.6 7.2155 431.3 2738.0 2979.5 7.2551 440.0 2753.9 3000.3 7.2939 448.7 2769.9 3021.2 7.3318 457.3 2785.8 3041.9 7.3690 393.8 2720.9 2957.2 402.0 2737.0 2978.2 410.2 2753.0 2999.1 418.3 2769.0 3020.0 426.3 2785.0 3040.8 7,2603 7.2984 7.3357 465.9 2801.8 3062.7 7.4056 474.4 2817.7 3083.4 7.4415 7.3724 434.4 2801.0 3061.6 442.4 2817.0 3082.5 7.4084 . 4.0 (250.40) 4.1 (251.87) p (t Sat.) 13 13 6.0701 48.53 2601.9 2800.9 6.0597 49.78 2602.3 2801.4 Sat. 240 6.0297 47.04 2580.7 2773.6 6.0074 245 48.60 2585.9 2780.3 48.13 2596.3 2793,6 6.0459 250 49.17 2611.1 2812.7 6.0672 6.1026 6.1362 6.1683 6.1990 49.69 2601.1 27999 50.74 2615.5 2818.5 51.74 2629.4 2836.3 52.71 2642.7 2853.5 53.65 2655.5 2870.1 260 6.0822 255 50.17 2625.2 2830.9 6.1165 51.14 2638.8 2848.5 6.1493 52.07 2651.9 2865.4 6.1805 265 270 275 54.57 2667.9 2886.2 6.2285 52.98 2664.5 2881.7 6.2105 53.86 2676.7 2897.6 6.2568 6.2393 55.46 2680.0 2901.8 280 6.2842 6.2671 56.33 2691.7 2917.0 285 54.72 2688.7 2913.0 55.56 2700.3 2928.1 6.2940 290 57.18 2703.2 2931.9 6.3108 58.02 2714.4 2946.4 6.3365 56.39 2711.6 2942.8 6.3200 295 300 310 6.3453 57.20 2722.7 2957.2 58.77 2744.3 2985.3 6.3939 6.4401 60.30 2765.2 3012.5 61.79 2785.6 3038.9 6.4843 330 63.25 2805.4 3064.8 58.84 2725.3 2960.7 6.3615 60.44 2746.7 2988.5 6.4095 61.99 2767.4 30.15.4 6.4553 63.51 2787.6 3041.6 6.4991 6.5413 64.99 2807.3. 3067.3 320 6.5268 340 350 360 66.45 2826.7 3092.5 6.5821 67.88 2845.7 3117.2 6.6215 69.29 2864.6 3141.7 6.6598 70.68 2883.2 3165.9 6.6971 6.7335 72.05 2901.6 3189.8 64.68 2824.9, 3090.1 16.5678 66.08 2844.1 3115.0 6.6075 67.47 2863.0 3139.6 6.6460 68.83 2881.7 3163.9 6.6834 380 390 70.18 2900.2 3188.0 6.7200 370 ܐA ܐܐ1 ntܐ .60 (158.85) U 315.7 2567.4 2756.8 256.0 2448.2 2601.8 261.7 2459.6 2616.7 267.3 2470.8 2631.1 14 ܤ1 ܬ ?4816245ܐ 7ܐܐܐ h58ܐ ܐܐ49ܐ 79ܐܐ 283.1 2502.5 2672.3 288.1 2512.6 2685 5 6983ܐ ܝܐܐšܐ ܐܨܐ ܐܐ ܐܐ ܐܐܐܪܐ ܙ7ܙܐ 34ܐܐܐ ܐܐ4ܝܐ ܐ.ܐ30 ܐ ܂ 6.7600 6.3732 ܐܐܐ4ܙ ܘܐ ܩ ܀
Complete solution and units please. Use the sleam tables provided, and use 4 decimal places for solving. Final answers are shown in 2 decimal places. Draw the T-S diagram properly with respect to the saturation line. 2. A steam power plant uses the ideal Regenarative Rankine cycle with single open feedwater heater where the steam enters the high pressure turbine at 4 UPa and sooc. At upa partially expands to 600 kPa then some steam is extracted at this point. The remaining steam expands and entert the condenser at 10 kPa. Sketch the schematic diagram and the TS diagram with labeled points, and solve for man taken for feedwater heating, Qa, Qr, Wt, Wp. Whet, thermal efficiency and steam rate. Neglect the condensate pump work. Answer: 20.01%/1 22 86.40 kJ, 1457 51 kJ 832.54 kJ 1 kg 3.74 k3 ку 828.89 k3 kg 1 3 (0.25% ку ку. 4.34 £1 Specific Volume Internal Energy Тепер Sel. MPa Sal. L V Evap. Sat, Liquid Sat. Р t Liquid Uy 10¹ 10³ Evap. Vapor h₂ h, h 1006113 0007 004 Vapor .01 1.0002 206 136 -1.89 1.0001 181 255 .00 2375.3 7.90 2370.0 2375.3. 2377.9 0005 3.77 1.0001 159 675 5.45 1.0001 142 789 .01 2501.3 2501.4 7.91 2496.9 2504.8 15.81 2492.5 2508.3 22.89 2488.5 2511.4 0009 15.81 2364.7 2380.6 22.88 2360.0 2382.9 20010 0011 .0012 .0013 0014 6.98 1.0002 129 208 8.37 1.0002 118 042 9.66 1.0003 108 696 10.86 1.0004 100 755 11.98 1.0005 93 922 29.30 2355.7 2385.0 35.17 2351.8 2386.9 40.58 2348.1 2388.7 45.60 2344.7 2390.3 50.31 2341.6 2391.9 29.30 2484.9 2514.2 35.17 2481.6 2516.8 40.58 2478.6 2519.1 45.60 2475.7 2521.3 50.31 2473.1 2523.4 20 0015 13.03 0016 14.02 0017 14.95 1.0007 87 980 1.0008 82 763 1.0009 78 146 1.0010 74 030 16.69 -1.0012 70 337 54.71 2338.6 2393.3 58.87 2335.8 2394.7 62.80 2333.2 2396.0 66.53 2330.7 2397:2 70.09 2328.3 2398.4 54.71 2470.6 2525.3 58.87 2468.3 2527.1 62.80 2466.0 2528.8 66.54 2463.9 2530.5 70.10 2461.9 2532.0 0018 15.84 0019 .0050 32.88 1.0053 28 192 .0055 34.58 1.0058 25 769 .0060 36.16 1.0064 23 739 .0065 37.63 1.0069 22 014 .0070 39.00 1.0074 20 530 137.82 2423.7 2561.5 144.95 2419.6 2564.5 151.53 2415.9 2567.4 157.67 2412.4 2570.01 163.40 2409.1 2572.5 .0075 40.29 1.0079 19 238 .0080 41.51 1.0084 18 103 .0085 42.67 1.0089 17 099 .0090 43.76 1.0094 16 203 .0095 44.81 1.0098 15 399 168.79 2406.0 2574.8 173.88 2403.1 2577.0 178.70 2400.3 2579.0 183.29 2397.7 2581.0 187.65 2395.2 2582.9 .010 45.81 1.0102 14 674 .011 47.69 1.0111 13 415 .012 49.42 1.0119 12 361 .013 51.04 1.0126 i! 465 .014 52.55 1.0134 10 693 191.83 2392.8 2584.7 199.67 2388:3 2588.0 206.92 2384.1 2591.1 213.67 2380.2 2593.9 219.99 2376.6 2596.6 55 155.48 1.0967 342.7 .56 156.17 1.0975 336.9 156.86 1.0983 331.3 325.9 320.7 57 655.93 2097.0 2753.0 658.93 2094.8 2753.8 661.90 2092.7 2754.5 664.83 2090.5 2755.3 667.71 2088.4 2756.1 58 157.53 1.0991 59 158.20 1.0999 .60 158.85 1.1006 .61 159.50 1.1014 .62 160.14 1.1021 160.77 1.1029 670.56 2086.3 2756.8 673.37 2084.2 2757.5 676.15 2082.1 2758.3 678.89 2080.1 2759.0 681.60 2078.0 2759.6 161 30 11036 ~222 11mmm I 137.81 2282.7 2420.5 144.94 2277.9 2422.8 151.53 2273.4 2425.0 157.66 2269.3 2426.9 163.39 2265.4 2428.8 168.78 2261.7 2430.5 173.87 2258.3 2432.2 178.69 2255.0 2433.7 183,27 2251.9 2435.2 187.64 2248.9 2436.6 191.82 2246.1 2437.9 199.66 2240.8 2440.4 206.91 2235.8 2442.7 213.66 2231.2 2444.9 219.98 2226.9 2446.9 655.32 1909.2 2564.5 658.32 1906.8 2565.1 661.27 1904.4 2565.7 664.18 1902.1 2566.3 667.06 1899.8 2566.8 315.7 669.90 1897.5 2567.4 310.8 672.70 1895.3 2568.0 306.0 675.47 1893.0 2568.5 301.5 678.20 1890.8 2569.0 680 90 1888.7 2569.6 2970 I Enthalpy kuh Sat. Sat. Entropy Liquid Evap. 8, 8% Vapor 9, 0000 9.1562 9.1562 0288 9.0775 9.1064 .0575 8.9999 9.0573 0829 8.9312 9.0142 .1059 8.8697 8.9756 .1268 8.8140 8.9408 1460 8.7631 8.9091 1637 8.7162 8.8799 .1802 8.6727 8.8529 .1957 8.6322 8.8279 .2102 8.5943 8.8044 .2238 8.5586 8.7825 .2368 8.5250 8.7618 .2491 8.4931 8.7422 4764 7.9187 8.3951 4997 7.8616 8.3613 5210 7.8094 8.3304 .5408 7.7613 8.3020 .5592 7.7167 8.2758 .5764 7.6750 8.2515 .5926 7.6361 8.2287 .6079 7.5994 8.2073 .6224 7.5648 8.1872 .6362 7.5321 8.1682 .6493 7.5009 8.1502 6738 7.4430 8.1168 .6963 7.3900 8.0863 7172 7.3412 8.0584 7366 7.2959 8.0325 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 1.9312 4.8288 6.7600 1.9377 4.8168 6.7545 1.9441 4.8049 6.7490 1.9504 4.7932 6.7436 1.9566 4.7817 6.7383
Transcribed Image Text:Complete solution and units please. Use the sleam tables provided, and use 4 decimal places for solving. Final answers are shown in 2 decimal places. Draw the T-S diagram properly with respect to the saturation line. 2. A steam power plant uses the ideal Regenarative Rankine cycle with single open feedwater heater where the steam enters the high pressure turbine at 4 UPa and sooc. At upa partially expands to 600 kPa then some steam is extracted at this point. The remaining steam expands and entert the condenser at 10 kPa. Sketch the schematic diagram and the TS diagram with labeled points, and solve for man taken for feedwater heating, Qa, Qr, Wt, Wp. Whet, thermal efficiency and steam rate. Neglect the condensate pump work. Answer: 20.01%/1 22 86.40 kJ, 1457 51 kJ 832.54 kJ 1 kg 3.74 k3 ку 828.89 k3 kg 1 3 (0.25% ку ку. 4.34 £1 Specific Volume Internal Energy Тепер Sel. MPa Sal. L V Evap. Sat, Liquid Sat. Р t Liquid Uy 10¹ 10³ Evap. Vapor h₂ h, h 1006113 0007 004 Vapor .01 1.0002 206 136 -1.89 1.0001 181 255 .00 2375.3 7.90 2370.0 2375.3. 2377.9 0005 3.77 1.0001 159 675 5.45 1.0001 142 789 .01 2501.3 2501.4 7.91 2496.9 2504.8 15.81 2492.5 2508.3 22.89 2488.5 2511.4 0009 15.81 2364.7 2380.6 22.88 2360.0 2382.9 20010 0011 .0012 .0013 0014 6.98 1.0002 129 208 8.37 1.0002 118 042 9.66 1.0003 108 696 10.86 1.0004 100 755 11.98 1.0005 93 922 29.30 2355.7 2385.0 35.17 2351.8 2386.9 40.58 2348.1 2388.7 45.60 2344.7 2390.3 50.31 2341.6 2391.9 29.30 2484.9 2514.2 35.17 2481.6 2516.8 40.58 2478.6 2519.1 45.60 2475.7 2521.3 50.31 2473.1 2523.4 20 0015 13.03 0016 14.02 0017 14.95 1.0007 87 980 1.0008 82 763 1.0009 78 146 1.0010 74 030 16.69 -1.0012 70 337 54.71 2338.6 2393.3 58.87 2335.8 2394.7 62.80 2333.2 2396.0 66.53 2330.7 2397:2 70.09 2328.3 2398.4 54.71 2470.6 2525.3 58.87 2468.3 2527.1 62.80 2466.0 2528.8 66.54 2463.9 2530.5 70.10 2461.9 2532.0 0018 15.84 0019 .0050 32.88 1.0053 28 192 .0055 34.58 1.0058 25 769 .0060 36.16 1.0064 23 739 .0065 37.63 1.0069 22 014 .0070 39.00 1.0074 20 530 137.82 2423.7 2561.5 144.95 2419.6 2564.5 151.53 2415.9 2567.4 157.67 2412.4 2570.01 163.40 2409.1 2572.5 .0075 40.29 1.0079 19 238 .0080 41.51 1.0084 18 103 .0085 42.67 1.0089 17 099 .0090 43.76 1.0094 16 203 .0095 44.81 1.0098 15 399 168.79 2406.0 2574.8 173.88 2403.1 2577.0 178.70 2400.3 2579.0 183.29 2397.7 2581.0 187.65 2395.2 2582.9 .010 45.81 1.0102 14 674 .011 47.69 1.0111 13 415 .012 49.42 1.0119 12 361 .013 51.04 1.0126 i! 465 .014 52.55 1.0134 10 693 191.83 2392.8 2584.7 199.67 2388:3 2588.0 206.92 2384.1 2591.1 213.67 2380.2 2593.9 219.99 2376.6 2596.6 55 155.48 1.0967 342.7 .56 156.17 1.0975 336.9 156.86 1.0983 331.3 325.9 320.7 57 655.93 2097.0 2753.0 658.93 2094.8 2753.8 661.90 2092.7 2754.5 664.83 2090.5 2755.3 667.71 2088.4 2756.1 58 157.53 1.0991 59 158.20 1.0999 .60 158.85 1.1006 .61 159.50 1.1014 .62 160.14 1.1021 160.77 1.1029 670.56 2086.3 2756.8 673.37 2084.2 2757.5 676.15 2082.1 2758.3 678.89 2080.1 2759.0 681.60 2078.0 2759.6 161 30 11036 ~222 11mmm I 137.81 2282.7 2420.5 144.94 2277.9 2422.8 151.53 2273.4 2425.0 157.66 2269.3 2426.9 163.39 2265.4 2428.8 168.78 2261.7 2430.5 173.87 2258.3 2432.2 178.69 2255.0 2433.7 183,27 2251.9 2435.2 187.64 2248.9 2436.6 191.82 2246.1 2437.9 199.66 2240.8 2440.4 206.91 2235.8 2442.7 213.66 2231.2 2444.9 219.98 2226.9 2446.9 655.32 1909.2 2564.5 658.32 1906.8 2565.1 661.27 1904.4 2565.7 664.18 1902.1 2566.3 667.06 1899.8 2566.8 315.7 669.90 1897.5 2567.4 310.8 672.70 1895.3 2568.0 306.0 675.47 1893.0 2568.5 301.5 678.20 1890.8 2569.0 680 90 1888.7 2569.6 2970 I Enthalpy kuh Sat. Sat. Entropy Liquid Evap. 8, 8% Vapor 9, 0000 9.1562 9.1562 0288 9.0775 9.1064 .0575 8.9999 9.0573 0829 8.9312 9.0142 .1059 8.8697 8.9756 .1268 8.8140 8.9408 1460 8.7631 8.9091 1637 8.7162 8.8799 .1802 8.6727 8.8529 .1957 8.6322 8.8279 .2102 8.5943 8.8044 .2238 8.5586 8.7825 .2368 8.5250 8.7618 .2491 8.4931 8.7422 4764 7.9187 8.3951 4997 7.8616 8.3613 5210 7.8094 8.3304 .5408 7.7613 8.3020 .5592 7.7167 8.2758 .5764 7.6750 8.2515 .5926 7.6361 8.2287 .6079 7.5994 8.2073 .6224 7.5648 8.1872 .6362 7.5321 8.1682 .6493 7.5009 8.1502 6738 7.4430 8.1168 .6963 7.3900 8.0863 7172 7.3412 8.0584 7366 7.2959 8.0325 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 1.9312 4.8288 6.7600 1.9377 4.8168 6.7545 1.9441 4.8049 6.7490 1.9504 4.7932 6.7436 1.9566 4.7817 6.7383
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