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6. Steam enters a pressure reducing valve at a pressure of 2000 kPa, dry saturated. It is throttled adiabatically to 100 kPa. What is the temperature and internal energy of the steam at the lower pressure. (162 °C, 2600 kJ/kg)

6. Steam enters a pressure reducing valve at a pressure of 2000 kPa, dry saturated. It is throttled adiabatically to 100 kPa. What is the temperature and internal energy of the steam at the lower pressure. (162 °C, 2600 kJ/kg)

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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1. A boiler feedpump receives 10 °C water at a pressure of 500 kPa. The discharge pressure is 2 400 kPa. Given a pump capacity of 160 000 kg/h, and after correcting. for the temperature of the water, what is the power supplied to the water? (8 kW) 2. Water is supplied to a pump at a pressure of 200 kPa. The power transferred to the water is estimated to be 30 kW. The pump discharge pressure is 2 200 kPa and the specific volume is 0.00106 m3/kg. Estimate the amount of water pumped in cubic meters per min. (0.90 m3/min.) 3. Air enters a compressor with a velocity of 6.0 m/s and an enthalpy of 233 kJ/kg and leaves with a velocity of 12 m/s and an enthalpy of 477 kJ/kg. Assuming adiabatic compression and negligible change in potential energy, calculate the work required to compress 1.0 kg of air. (244 kJ/kg) 4. An air compressor is supplied with air at 101.3 kPa and a specific volume of 0.804 m3/kg. The air is discharged at 700 kPa and a specific volume of 0.162 m³/kg. The initial and final internal energies are 37.2 kJ/kg and 114 kJ/kg respectively. The cooling water removes 88.0 kJ/kg of air compressed. The change in kinetic and potential energy may be neglected. Calculate (a) the specific work required, (b) the power required given a mass flow rate of 45.6 kg/min. Also (c) if the heat being rejected is transferred to cooling water flowing through a coil, and the cooling water picks up 10ºC across that coil, and the pump forcing that cooling flow has a 100 kPa AP across it, calculate the power required to drive the cooling water pump (197 kJ/kg. 150 kW, 160 W) 5. Wet steam is throttled from 1000 kPa to 10 kPa and 130 °C. Find the dryness fraction at state 1. [98.3%] 6. Steam enters a pressure reducing valve at a pressure of 2000 kPa, dry saturated. It is throttled adiabatically to 100 kPa. What is the temperature and internal energy of the steam at the lower pressure. (162 °C, 2600 kJ/kg) 7. A pressure reducing valve receives 5 kg/s of steam at 2MPa with a specific volume of 0.1255 m³/kg and an internal energy of 2774 kJ/kg. If the pressure downstream of the throttle is 200 kPa and the velocity at that point is 4.25 m/s, determine to the nearest inch the required ID of the downstream piping in order to accommodate the volume flow rate. [54.0 inches] DVI & Dual HDMI inputs for high-definition support ho
Transcribed Image Text:1. A boiler feedpump receives 10 °C water at a pressure of 500 kPa. The discharge pressure is 2 400 kPa. Given a pump capacity of 160 000 kg/h, and after correcting. for the temperature of the water, what is the power supplied to the water? (8 kW) 2. Water is supplied to a pump at a pressure of 200 kPa. The power transferred to the water is estimated to be 30 kW. The pump discharge pressure is 2 200 kPa and the specific volume is 0.00106 m3/kg. Estimate the amount of water pumped in cubic meters per min. (0.90 m3/min.) 3. Air enters a compressor with a velocity of 6.0 m/s and an enthalpy of 233 kJ/kg and leaves with a velocity of 12 m/s and an enthalpy of 477 kJ/kg. Assuming adiabatic compression and negligible change in potential energy, calculate the work required to compress 1.0 kg of air. (244 kJ/kg) 4. An air compressor is supplied with air at 101.3 kPa and a specific volume of 0.804 m3/kg. The air is discharged at 700 kPa and a specific volume of 0.162 m³/kg. The initial and final internal energies are 37.2 kJ/kg and 114 kJ/kg respectively. The cooling water removes 88.0 kJ/kg of air compressed. The change in kinetic and potential energy may be neglected. Calculate (a) the specific work required, (b) the power required given a mass flow rate of 45.6 kg/min. Also (c) if the heat being rejected is transferred to cooling water flowing through a coil, and the cooling water picks up 10ºC across that coil, and the pump forcing that cooling flow has a 100 kPa AP across it, calculate the power required to drive the cooling water pump (197 kJ/kg. 150 kW, 160 W) 5. Wet steam is throttled from 1000 kPa to 10 kPa and 130 °C. Find the dryness fraction at state 1. [98.3%] 6. Steam enters a pressure reducing valve at a pressure of 2000 kPa, dry saturated. It is throttled adiabatically to 100 kPa. What is the temperature and internal energy of the steam at the lower pressure. (162 °C, 2600 kJ/kg) 7. A pressure reducing valve receives 5 kg/s of steam at 2MPa with a specific volume of 0.1255 m³/kg and an internal energy of 2774 kJ/kg. If the pressure downstream of the throttle is 200 kPa and the velocity at that point is 4.25 m/s, determine to the nearest inch the required ID of the downstream piping in order to accommodate the volume flow rate. [54.0 inches] DVI & Dual HDMI inputs for high-definition support ho
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Table 1 (continued...) Press k Pa р Properties of Saturated Steam - Pressure Table Temp °℃ t Specific Volume Sat. Liquid Vf Sat. Vapor Vg Note: 100k Pa = 1 Bar = 100,000N/m² Sat. Liquid Uf Internal Energy Evap. All Sat. Vapor Ug Enthalpy Sat. Liquid hf Evap. Sat. Vapor hg Entropy Sat. Liquid Sf Evap. Ufg hfg Sfg 2,000 2,799.5 3.8935 6.3409 1,890.7 2.4474 2,799.5 2.5035 3.7937 6.2972 1,865.2 2,250 212.42 1.1767 218.45 1.1872 223.99 1.1973 233.90 1.2165 3.7028 6.2575 3.5412 6.1869 2,500 3,000 3,500 99.63 88.75 79.98 66.68 57.07 49.78 39.44 242.60 1.2347 3.4000 6.1253 3.2737 6.0701 4,000 250.40 1.2522 3.2737 3.0532 5.9734 5,000 263.99 1.2859 39.44 275.64 1.3187 32.44 2.8625 5.8892 2.6922 5.8133 285.88 1.3513 295.06 1.3842 303.40 1.4178 1,316.64 1,316.64 906.44 1,693.8 2,600.3 908.79 936.49 933.83 1,668.2 2,602.01 1,865.2 2,801.7 1,841.0 2,803.1 2.5547 959.11 1,644.0 2,603.1 962.11 1,008.42 1,795.7 2,804.2 2.6457 1,004.78 1,599.3 2,604.1 1,045.43 1,558.3 2,603.7 1,049.75 1,753.7 2,803.4 2.7253 2.7964 1,082.31 1,520.0 2,602.3 1,087.31 1,714.1 2,801.4 1,147.81 1,449.3 2,597.1 1,154.23 1,640.1 2,794.3 2.9202 1,213.35 1,571.0 2,784.3 3.0267 6,000 1,205.44 1,384.3 2,589.7 1,267.00 1,505.1 2,772.1 3.1211 7,000 27.37 1,257.55 1,323.0 2,580.5 1,441.3 2,758.0 3.2068 2.5364 5.7432 1,441.3 8,000 1,305.57 1,264.2 2,569.8 23.52 1,350.51 1,207.3 2,557.8 1,378.9 2,742.1 3.2858 2.3915 5.6772 9,000 20.48 3.3596 2.2544 5.6141 1,393.04 1,151.4 2,544.4 1,317.1 2,724.7 10,000 311.06 1.4524 18.026 3.4295 2.1233 5.5527 1,433.7 1,096.0 2,529.8 11,000 318.15 1.4886 15.987 3.4962 1.9962 5.4924 1,473.0 1,040.7 2,513.7 12,000 324.75 1.5267 14.263 13,000 330.93 1.5671 12.780 1,511.1 2,496.1 1,531.5 985.0 14,000 336.75 1.6107 11.485 1,548.6 928.2 2,476.8 15,000 342.24 1.6581 10.337 1,585.6 869.8 2,455.5 16,000 347.44 1.7107 9.306 1,622.7 809.0 2,431.7 17,000 352.37 1.7702 744.8 1,255.5 2,705.6 1,363.26 1,407.56 1,450.1 1,491.3 1,531.5 1,571.1 1,193.6 2,684.9 1,130.7 2,662.2 3.5606 1.8718 5.4323 1,066.5 2,637.6 1.7485 5.3717 1,610.5 1,000.0 2,610.5 1,650.1 2,580.6 8.364 1,660.2 2,405.0 1,690.3 1,698.9 675.4 2,374.3 1,732.0 18,000 357.06 1.8397 7.489 19,000 361.54 930.6 856.9 777.1 688.0 583.4 3.6232 3.6848 1.6249 5.3098 3.7461 1.4994 5.2455 3.8079 1.3698 5.1777 2,547.2 3.8715 1.2329 5.1044 2,509.1 3.8715 3.9388 1.0839 5.0228 2,464.5 0.9130 4.9269 4.039 2,409.7 4.1075 2,334.6 0.6938 4.8013 2,165.6 4.3110 2,099.3 4.4298 1.9243 6.657 598.1 2,338.1 1,776.5 5.834 2,293.0 20,000 365.81 21,000 369.89 2.036 2.207 1,826.3 4.952 1,739.9 1,785.6 507.5 1,842.1 388.5 125.2 1,961.9 0 1,888.4 446.2 22,000 373.80 2.742 3.568 2,230.6 2,087.1 2,022.2 2,029.6 143.4 22,090 374.14 3.155 3.155 2,029.6 0.2216 4.5327 4.4298 2,099.3 0 0 O John Wiley and Sons, Inc., Keenan, Keyes, Hill, and Moore. This material has been copied under license from CANCOPY. Resale or further copying of this material is strictly prohibited. Sat. Vapor Sg
Transcribed Image Text:Table 1 (continued...) Press k Pa р Properties of Saturated Steam - Pressure Table Temp °℃ t Specific Volume Sat. Liquid Vf Sat. Vapor Vg Note: 100k Pa = 1 Bar = 100,000N/m² Sat. Liquid Uf Internal Energy Evap. All Sat. Vapor Ug Enthalpy Sat. Liquid hf Evap. Sat. Vapor hg Entropy Sat. Liquid Sf Evap. Ufg hfg Sfg 2,000 2,799.5 3.8935 6.3409 1,890.7 2.4474 2,799.5 2.5035 3.7937 6.2972 1,865.2 2,250 212.42 1.1767 218.45 1.1872 223.99 1.1973 233.90 1.2165 3.7028 6.2575 3.5412 6.1869 2,500 3,000 3,500 99.63 88.75 79.98 66.68 57.07 49.78 39.44 242.60 1.2347 3.4000 6.1253 3.2737 6.0701 4,000 250.40 1.2522 3.2737 3.0532 5.9734 5,000 263.99 1.2859 39.44 275.64 1.3187 32.44 2.8625 5.8892 2.6922 5.8133 285.88 1.3513 295.06 1.3842 303.40 1.4178 1,316.64 1,316.64 906.44 1,693.8 2,600.3 908.79 936.49 933.83 1,668.2 2,602.01 1,865.2 2,801.7 1,841.0 2,803.1 2.5547 959.11 1,644.0 2,603.1 962.11 1,008.42 1,795.7 2,804.2 2.6457 1,004.78 1,599.3 2,604.1 1,045.43 1,558.3 2,603.7 1,049.75 1,753.7 2,803.4 2.7253 2.7964 1,082.31 1,520.0 2,602.3 1,087.31 1,714.1 2,801.4 1,147.81 1,449.3 2,597.1 1,154.23 1,640.1 2,794.3 2.9202 1,213.35 1,571.0 2,784.3 3.0267 6,000 1,205.44 1,384.3 2,589.7 1,267.00 1,505.1 2,772.1 3.1211 7,000 27.37 1,257.55 1,323.0 2,580.5 1,441.3 2,758.0 3.2068 2.5364 5.7432 1,441.3 8,000 1,305.57 1,264.2 2,569.8 23.52 1,350.51 1,207.3 2,557.8 1,378.9 2,742.1 3.2858 2.3915 5.6772 9,000 20.48 3.3596 2.2544 5.6141 1,393.04 1,151.4 2,544.4 1,317.1 2,724.7 10,000 311.06 1.4524 18.026 3.4295 2.1233 5.5527 1,433.7 1,096.0 2,529.8 11,000 318.15 1.4886 15.987 3.4962 1.9962 5.4924 1,473.0 1,040.7 2,513.7 12,000 324.75 1.5267 14.263 13,000 330.93 1.5671 12.780 1,511.1 2,496.1 1,531.5 985.0 14,000 336.75 1.6107 11.485 1,548.6 928.2 2,476.8 15,000 342.24 1.6581 10.337 1,585.6 869.8 2,455.5 16,000 347.44 1.7107 9.306 1,622.7 809.0 2,431.7 17,000 352.37 1.7702 744.8 1,255.5 2,705.6 1,363.26 1,407.56 1,450.1 1,491.3 1,531.5 1,571.1 1,193.6 2,684.9 1,130.7 2,662.2 3.5606 1.8718 5.4323 1,066.5 2,637.6 1.7485 5.3717 1,610.5 1,000.0 2,610.5 1,650.1 2,580.6 8.364 1,660.2 2,405.0 1,690.3 1,698.9 675.4 2,374.3 1,732.0 18,000 357.06 1.8397 7.489 19,000 361.54 930.6 856.9 777.1 688.0 583.4 3.6232 3.6848 1.6249 5.3098 3.7461 1.4994 5.2455 3.8079 1.3698 5.1777 2,547.2 3.8715 1.2329 5.1044 2,509.1 3.8715 3.9388 1.0839 5.0228 2,464.5 0.9130 4.9269 4.039 2,409.7 4.1075 2,334.6 0.6938 4.8013 2,165.6 4.3110 2,099.3 4.4298 1.9243 6.657 598.1 2,338.1 1,776.5 5.834 2,293.0 20,000 365.81 21,000 369.89 2.036 2.207 1,826.3 4.952 1,739.9 1,785.6 507.5 1,842.1 388.5 125.2 1,961.9 0 1,888.4 446.2 22,000 373.80 2.742 3.568 2,230.6 2,087.1 2,022.2 2,029.6 143.4 22,090 374.14 3.155 3.155 2,029.6 0.2216 4.5327 4.4298 2,099.3 0 0 O John Wiley and Sons, Inc., Keenan, Keyes, Hill, and Moore. This material has been copied under license from CANCOPY. Resale or further copying of this material is strictly prohibited. Sat. Vapor Sg
Table 3 Abs Press. kPa (Sat. Temp) 100 150 200 V v 17,196 19,512 21,825 h 2,687.5 2,783.0 2,879.5 S 8.4479 8.6882 8.9038 10 (45.81) 30 (69.10) 50 (81.33) 100 (99.63) 200 (120.23) 500 (151.86) v V V 5,715 6,493 h 2,685.0 S 7.9357 h s V h 300 (133.55) S V h S 5,000 (263.99) V h S V 1,000 h (179.91) S V 2,000 h (212.43) S V 3,000 h (233.90) S V 4,000 h (250.40) S v 1,695.8 1,936.4 2,172 2,406 h 2,676.2 2,776.4 2,875.3 2,974.3 7.3614 7.6134 7.8343 8.0333 s Table of Properties for Superheated Steam V h S 7,267 2,781.5 2,878.6 8.3952 8.1785 V 6,000 h (275.64) S 3,889 4,356 3,418 2,682.5 2,780.1 2,877.7 7.6947 7.9401 8.1580 Temperature Degrees Celsius 250 24,136 2,977.3 9.1002 8,040 2,976.7 8.5923 4,820 2,976.0 8.3556 *** 796.4 633.9 716.3 2761.0 2,865.6 2,967.6 7.0778 7.3115 7.5166 Note: 100k Pa = 1 Bar = 100,000N/m² 232.7 206.0 2,827.9 2,942.6 6.6940 6.9247 600 700 500 400 300 26,445 31,063 35,679 40,295 44,911 3,928.7 3,076.5 3,279.6 3,489.1 3,705.4 10.4028 9.6077 9.8978 10.1608 9.2813 959.6 1,080.3 1,198.8 1,316.2 2,768.8 2,870.5 2,971.0 3,071.8 7.2795 7.5066 7.7086 7.8926 7.8926 8,811 3,076.0 8.7736 5,284 3,075.5 8.5373 2,639 3,074.3 8.2158 424.9 474.4 522.6 2,855.4 2,960.7 3,064.2 7.0592 7.2709 7.2709 7.4599 10,351 3,279.2 9.1003 111.44 125.47 2,902.5 3,023.5 6.5453 6.7664 6,209 3,278.9 8.8642 70.58 81.14 2,855.8 2,993.5 6.2872 6.5390 3,103 3,278.2 8.5435 875.3 1,031.5 1,186.7 3,069.3 3,275.0 7.7022 8.0330 3,486.0 8.3251 257.9 306.6 3,263.9 3,051.2 7.1229 7.4651 617.3 3,271.9 7.7938 1,1891 3,488.9 9.3906 99.36 3,230.9 6.9212 58.84 73.41 2,960.7 3,213.6 6.3615 6.7690 7,134 7,134 8,057 8,057 3,488.7 3,705.1 9.1546 9.4178 3,565 4,028 3,488.1 3,704.7 8.8342 9.0976 1,549.3 1,781.4 2,013 2,244 3,276.6 3,487.1 3,704.0 8.2218 8.5133 8.7770 3,927.6 9.0194 36.16 6.0674 2,884.2 3,177.2 710.9 3,483.9 8.0873 13,430 3,705.3 9.6537 354.1 3,478.5 7.7622 151.20 175.68 199.60 3,247.6 3,467.6 3,690.1 3,247.6 7.1271 7.4317 7.7024 86.43 3,445.3 7.0901 45.32 57.81 68.57 2,924.5 3,195.7 3,433.8 6.2084 6.6459 6.9759 1,341.4 3,703.2 8.5892 804.1 3,701.7 8.3522 401.1 3,697.9 8.0290 116.19 132.43 3,456.5 3,682.3 7.2338 7.5085 98.95 3,674.4 3,674.4 7.3688 78.69 3,666.5 7.2589 65.25 47.39 56.65 3,422.2 6.5408 6.8803 7.1677 3,658.4 14,969 3,928.6 19,585 16,508 18,047 4,158.9 4,396.4 4,640.5 9.8957 10.1210 10.3325 10.5322 8,981 9,904 10,828 11,751 3,928.5 4,158.9 4,396.3 4,640.5 9.6599 9.8852 10.0967 10.2964 9.6599 4,490 3,928.2 9.3398 1,495.7 3,927.1 8.8319 896.9 3,925.9 8.5952 447.8 3,923.1 8.2731 223.2 3,917.4 7.9487 800 900 1,000 49,526 54,141 58,757 4159.0 4,396.4 4,640.6 10.6281 10.8396 11.0393 110.95 3,905.9 7.6198 88.49 3,900.1 7.5122 4,952 5,414 5,875 4,158.6 4,396.1 4,640.3 9.5652 9.7767 9.9764 2,475 4,158.2 9.2449 1,649.9 1,804.1 1,958.1 4,157.8 4,395.4 4,639.7 9.0576 9.2692 9.2692 9.4690 989.6 1,082.2 1,174.7 4,156.9 4,394.7 4,639.1 8.8211 9.0329 9.2328 2,706 2,937 4,395.8 4,395.8 4,640.0 9.4566 9.6563 246.7 4,150.3 8.1765 494.3 4,154.7 8.4966 8.7118 148.38 3,911.7 7.7571 7.9862 8.1999 8.4009 164.14 197.80 195.41 4,145.9 4,385.9 4,631.6 122.87 4,141.5 7.8502 540.7 587.1 4,392.9 4,637.6 8.7118 8.9119 98.11 4,137.1 7.7440 270.0 293.3 4,389.4 4,634.6 8.3895 8.5901 134.69 146.45 4,382.3 4,628.7 8.0647 8.2662 107.62 117.07 4,378.8 4,625.7 7.9593 8.1612 73.52 89.58 97.49 81.60 4,132.7 4,375.3 4,622.7 3,894.2 7.4234 7.6566 7.8727 8.0751
Transcribed Image Text:Table 3 Abs Press. kPa (Sat. Temp) 100 150 200 V v 17,196 19,512 21,825 h 2,687.5 2,783.0 2,879.5 S 8.4479 8.6882 8.9038 10 (45.81) 30 (69.10) 50 (81.33) 100 (99.63) 200 (120.23) 500 (151.86) v V V 5,715 6,493 h 2,685.0 S 7.9357 h s V h 300 (133.55) S V h S 5,000 (263.99) V h S V 1,000 h (179.91) S V 2,000 h (212.43) S V 3,000 h (233.90) S V 4,000 h (250.40) S v 1,695.8 1,936.4 2,172 2,406 h 2,676.2 2,776.4 2,875.3 2,974.3 7.3614 7.6134 7.8343 8.0333 s Table of Properties for Superheated Steam V h S 7,267 2,781.5 2,878.6 8.3952 8.1785 V 6,000 h (275.64) S 3,889 4,356 3,418 2,682.5 2,780.1 2,877.7 7.6947 7.9401 8.1580 Temperature Degrees Celsius 250 24,136 2,977.3 9.1002 8,040 2,976.7 8.5923 4,820 2,976.0 8.3556 *** 796.4 633.9 716.3 2761.0 2,865.6 2,967.6 7.0778 7.3115 7.5166 Note: 100k Pa = 1 Bar = 100,000N/m² 232.7 206.0 2,827.9 2,942.6 6.6940 6.9247 600 700 500 400 300 26,445 31,063 35,679 40,295 44,911 3,928.7 3,076.5 3,279.6 3,489.1 3,705.4 10.4028 9.6077 9.8978 10.1608 9.2813 959.6 1,080.3 1,198.8 1,316.2 2,768.8 2,870.5 2,971.0 3,071.8 7.2795 7.5066 7.7086 7.8926 7.8926 8,811 3,076.0 8.7736 5,284 3,075.5 8.5373 2,639 3,074.3 8.2158 424.9 474.4 522.6 2,855.4 2,960.7 3,064.2 7.0592 7.2709 7.2709 7.4599 10,351 3,279.2 9.1003 111.44 125.47 2,902.5 3,023.5 6.5453 6.7664 6,209 3,278.9 8.8642 70.58 81.14 2,855.8 2,993.5 6.2872 6.5390 3,103 3,278.2 8.5435 875.3 1,031.5 1,186.7 3,069.3 3,275.0 7.7022 8.0330 3,486.0 8.3251 257.9 306.6 3,263.9 3,051.2 7.1229 7.4651 617.3 3,271.9 7.7938 1,1891 3,488.9 9.3906 99.36 3,230.9 6.9212 58.84 73.41 2,960.7 3,213.6 6.3615 6.7690 7,134 7,134 8,057 8,057 3,488.7 3,705.1 9.1546 9.4178 3,565 4,028 3,488.1 3,704.7 8.8342 9.0976 1,549.3 1,781.4 2,013 2,244 3,276.6 3,487.1 3,704.0 8.2218 8.5133 8.7770 3,927.6 9.0194 36.16 6.0674 2,884.2 3,177.2 710.9 3,483.9 8.0873 13,430 3,705.3 9.6537 354.1 3,478.5 7.7622 151.20 175.68 199.60 3,247.6 3,467.6 3,690.1 3,247.6 7.1271 7.4317 7.7024 86.43 3,445.3 7.0901 45.32 57.81 68.57 2,924.5 3,195.7 3,433.8 6.2084 6.6459 6.9759 1,341.4 3,703.2 8.5892 804.1 3,701.7 8.3522 401.1 3,697.9 8.0290 116.19 132.43 3,456.5 3,682.3 7.2338 7.5085 98.95 3,674.4 3,674.4 7.3688 78.69 3,666.5 7.2589 65.25 47.39 56.65 3,422.2 6.5408 6.8803 7.1677 3,658.4 14,969 3,928.6 19,585 16,508 18,047 4,158.9 4,396.4 4,640.5 9.8957 10.1210 10.3325 10.5322 8,981 9,904 10,828 11,751 3,928.5 4,158.9 4,396.3 4,640.5 9.6599 9.8852 10.0967 10.2964 9.6599 4,490 3,928.2 9.3398 1,495.7 3,927.1 8.8319 896.9 3,925.9 8.5952 447.8 3,923.1 8.2731 223.2 3,917.4 7.9487 800 900 1,000 49,526 54,141 58,757 4159.0 4,396.4 4,640.6 10.6281 10.8396 11.0393 110.95 3,905.9 7.6198 88.49 3,900.1 7.5122 4,952 5,414 5,875 4,158.6 4,396.1 4,640.3 9.5652 9.7767 9.9764 2,475 4,158.2 9.2449 1,649.9 1,804.1 1,958.1 4,157.8 4,395.4 4,639.7 9.0576 9.2692 9.2692 9.4690 989.6 1,082.2 1,174.7 4,156.9 4,394.7 4,639.1 8.8211 9.0329 9.2328 2,706 2,937 4,395.8 4,395.8 4,640.0 9.4566 9.6563 246.7 4,150.3 8.1765 494.3 4,154.7 8.4966 8.7118 148.38 3,911.7 7.7571 7.9862 8.1999 8.4009 164.14 197.80 195.41 4,145.9 4,385.9 4,631.6 122.87 4,141.5 7.8502 540.7 587.1 4,392.9 4,637.6 8.7118 8.9119 98.11 4,137.1 7.7440 270.0 293.3 4,389.4 4,634.6 8.3895 8.5901 134.69 146.45 4,382.3 4,628.7 8.0647 8.2662 107.62 117.07 4,378.8 4,625.7 7.9593 8.1612 73.52 89.58 97.49 81.60 4,132.7 4,375.3 4,622.7 3,894.2 7.4234 7.6566 7.8727 8.0751
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