ARNOLD, K (1999) Design of Gas-Handling Systems and Facilities (2nd ed ) Episode 1 Part 10 pdf

... bed and water displaces the previously adsorbed gases until 214 Design of GAS-HANDLING Systems and Facilities Figure 8 -14 . Structured (matrix) packing, (from Koch Industries .) Contactor ... 222 Design of GAS-HANDLING Systems and Facilities Table 8-3 Gas Consumption by Glycol Powered Pump Contactor Operating Pressure psig 300 400 500 600 700 80...

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... Passes 1 8 14 26 42 64 85 11 0 14 7 18 4 227 280 316 3 71 434 503 576 643 738 804 946 10 87 12 40 13 97 15 92 19 69 2 6 14 26 40 61 76 10 6 13 8 17 5 220 265 313 370 424 489 558 634 709 787 928 10 69 12 30 13 89 15 61 1945 4 4 8 16 36 56 72 10 0 12 8 16 8 212 252 294 358 408 468 534 604 684 772 898 10 42 11 98 13 54 15 30 1 904 Outside Packed Fl...

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... gases. 19 2 Design of GAS-HANDLING Systems and Facilities ci H in. _ft_ 18 1. 9.2 20 15 ,5 22 12 .8 24 10 .8 30 6.9 36 4.8 An acceptable choice is a 30-in. OD vessel. The wall thickness can ... Book, 10 th Edition .) 19 4 Design of GAS-HANDLING Systems and Facilities Use 72-in. ID tower w/24 trays, 4. Determine reboiler duty: Using...

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... Anti-Agglomerators, 10 7 CHAPTER S LTX Units and Line Heaters 10 9 LTX Units, 11 0 Line Heaters, 11 2 Heat Duty, 11 3 Fire-Tube Size, 11 5 Coil Sizing, 11 6 Choose Temperatures 11 6, Choose ... at www.bh.com/gujf 10 987654 Library of Congress Cataloging-in-Publication Data Arnold, Ken, 19 42- Design of gas-handling systems and facilities /...

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... 26.78 Sot. Vapor v g 3306 2947 2444 2036,4 17 03.2 12 06.7 867,9 633 .1 468.0 350.4 265.4 203.27 15 7.34 12 3, 01 97.07 77.29 62.06 50.23 40.96 33.64 27.82 26.80 Enthalpy Sat. Liquid 0.00 3.02 8.05 13 .06 18 ,07 28.06 38.04 48,02 57.99 67.97 77.94 87.92 97.90 10 7.89 11 7.89 12 7.89 13 7.90 14 7.92 15 7.95 16 7.99 17 8.05 18 0.07 Evap. hfg 10 75,8 10 74 .1 10 71. 3...

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... Vaporization Compound Methane Ethane Propane n-Butane Isobutane n-Pentane Isopentane Hexane Heptane Octane Nonane Decane Heat of Vaporization, 1 4.696 psia at Boiling Point, Btu/lb 219 .22 210 . 41 183.05 16 5.65 15 7.53 15 3.59 14 7 .13 14 3.95 13 6. 01 129.53 12 3.76 11 8.68 ... 1 29 B Molecular Weight 44. 010 28. 013 34.076 16 .043 30.070 44.097 58 .12 4 58 .12...

Ngày tải lên: 06/08/2014, 02:20

... (Table 2 -1 0) P R = P/P C =1. 47 T r = 375°R (Table 2 -1 0) T R = T av /T c = 1. 59 q g = 41. 7(AT)C g Q g C g = 2.64 [29 x S x C -f AC p j C - 0.528 Btu/lb°F (Figure 2 -1 4) 10 0 Design ... (Figure 3 -1 0): Calculate number of tubes: 86 Design of GAS-HANDLING Systems and Facilities [text continued from page 8 3) Generally,...

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... 2O-0'' 8-2-XH 8-y'XXH 8-2"XH 8-2"XXH TO-r'XH io-r'xxM 6-3"XH 6-3"XXH »2-2"XH 12 -r'XXH WXH 8.3-XXH 14 -r'XH 14 -T'XXH 1O-3"XH 1O-3"XXH 1 -2"XH ie-2-xxn 10 -3"XM 10 -3"XXH 3440 7340 3440 7340 3440 7340 3200 6820 3440 7340 3200 6820 3440 7340 3200 68*0 3440 7340 3200 6820 29-S 26.5 42.6 38.3 64.4 5...

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... rescued promptly and given artificial resuscitation. *Based on 1% hydrogen sulfide = 629.77 gr /10 0 scfat 14 .696 psia and 59°F, or 10 1,325 kPa and 75°C. 15 6 Design of GAS-HANDLING ... threat- *Reviewed for the 19 99 edition by K. S. Chiou of Paragon Engineering Services, Inc. 15 1 15 2 Design of GAS-HANDLING Systems and Facilities...

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... rate of deposition of 15 grains of H 2 S/min/ft 2 of bed cross-sectional area is also recommended to allow for the dissipation of 17 6 Design of GAS-HANDLING Systems and Facilities Figure ... developed and patented by NL Treating Chemicals and is now a product of Exxon Energy Chem- 16 2 Design of GAS-HANDLING Systems and Facilit...

Ngày tải lên: 06/08/2014, 02:20