ARNOLD, K (1999) Design of Gas-Handling Systems and Facilities (2nd ed ) Episode 1 Part 10 pdf
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 8-3Gas Consumption by Glycol Powered PumpContactorOperatingPressurepsig300400500600700800900 10 00 11 00 12 00 13 00 14 00 15 00PumpGasConsumptionsc ... because of a multitude of microscopic pores and capillary 216 Design of GAS-HANDLING Systems and Facilities Figure 8 -16 . Glycol concentration vs. glycol circulation when n = 1. 5...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 4 pdf
... Passes 1 8 14 26426485 11 0 14 7 18 4227280 316 3 71 434503576643738804946 10 87 12 40 13 97 15 92 19 6926 14 2640 61 76 10 6 13 8 17 5220265 313 370424489558634709787928 10 69 12 30 13 89 15 61 1945448 16 365672 10 0 12 8 16 8 212 252294358408468534604684772898 10 42 11 98 13 54 15 30 1 904Outside PackedFloating HeadNo. of Passes 1 7 10 22385673 10 0 13 0 17 0 212 258296355 416 475544 619 696768908 10 41 118 9 13 48 15 31 190624 10 18 36527298 12 6 16 22 01 2502943464084665296046797538 91 1 017 11 82 13 37 15 03 18 79444 16 28486088 11 6 14 8 18 8232276328392446 510 582660730860990 11 52 13 00 14 62 18 42"U"-TubeNo. ... Passes 1 5 12 21 3252 61 89 11 3 14 8 18 02 21 2 61 308359 418 477540608674788<JIO 10 37 11 81 ]4T724 10 18 32465882 11 2 13 8 17 4 210 2482963454 01 460526588654765885 10 18 11 60448 16 28405676 10 4 12 8 16 8200236286336388448508568640756866 10 00 11 42 11 07 ... OT 51 00HH2 1 i MOOi 1 1282 \ J W.OOFixedTube SheetNo. of Passes 1 12 21 37 61 97 11 3 15 6208256 314 379448522603688788897 10 09 11 18 12 98 15 00 17 142 10 18 325490 10 8 14 6 1% 244299363432504583667770873983 10 92 12 69 14 70lh 81 48 16 284884 10 4 13 6 18 4236294352 416 486568654756850958 10 66 12 50 14 40 16 501Q«...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 9 pdf
... gases. 19 2 Design of GAS-HANDLING Systems and Facilities ci Hin. _ft_ 18 1. 9.220 15 ,522 12 .824 10 .830 6.936 4.8An acceptable choice is a 30-in. OD vessel. The wall thicknesscan ... 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 1, 000 Btu/gal lean solutionq=l,000(50 8)( 60 ... DEA 19 8 Design of GAS-HANDLING Systems and Facilities Figure 8*2. Effective water content of CO2. (From Gas Processors SuppliersAssociation, engineering Data Book, 10 th Edition .) Process...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 1 pps
... Anti-Agglomerators, 10 7CHAPTER SLTX Units and Line Heaters 10 9LTX Units, 11 0Line Heaters, 11 2Heat Duty, 11 3Fire-Tube Size, 11 5Coil Sizing, 11 6Choose Temperatures 11 6, Choose ... atwww.bh.com/gujf 10 987654Library of Congress Cataloging-in-Publication Data Arnold, Ken, 19 42- Design of gas-handling systems and facilities / Ken Arnold, MauriceStewart. — 2nd ed. p. ... OperationsVOLUME 2 Design of Gas-Handling Systems and Facilities Copyright © 19 89, 19 99 by Elsevier Science (USA).All rights reserved. Printed in the United States of America.This book,...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 2 doc
... 26.78Sot.Vaporvg3306294724442036,4 17 03.2 12 06.7867,9633 .1 468.0350.4265.4203.27 15 7.34 12 3, 01 97.0777.2962.0650.2340.9633.6427.8226.80EnthalpySat.Liquid0.003.028.05 13 .06 18 ,0728.0638.0448,0257.9967.9777.9487.9297.90 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 0.07Evap.hfg 10 75,8 10 74 .1 10 71. 3 10 68,4 10 65.6 10 59.9 10 54.3 10 48.6 10 42.9 10 37.2 10 31, 6 10 25.8 10 20.0 10 14 .1 100 8.2 10 02.3996.3990.2984 .1 977,99 71. 6970,3Sat.Vaporkg 10 75.8 10 77 .1 107 9.3 10 81. 5 10 83.7 10 88.0 10 92,3 10 96.6 11 00.9 11 05.2 11 09.5 11 13.7 11 17.9 11 22,0 11 26 .1 113 0.2 11 34.2 11 38 .1 1 14 2.0 1 14 5.9 11 49.7 1 1. 50.4EntropySat.LiquidSf0.00000.00 61 0. 016 20.02620,03 61 0.05550.07450.09320 .11 150 .12 950 .14 71 0 .16 450 .18 160 ,19 840. 214 90.2 311 0.24720.26300.27850,2938Evap.%2 .18 772 .17 092 .14 352 ,11 672.09032.0393 1. 9902 1. 9428 1. 8972 1. 85 31 1. 810 6 1. 7694 1. 7296 1. 6 910 1. 6537 1. 617 4 1. 5822 1, 5480 1. 514 7 1, 48240.3090 ... 26.78Sot.Vaporvg3306294724442036,4 17 03.2 12 06.7867,9633 .1 468.0350.4265.4203.27 15 7.34 12 3, 01 97.0777.2962.0650.2340.9633.6427.8226.80EnthalpySat.Liquid0.003.028.05 13 .06 18 ,0728.0638.0448,0257.9967.9777.9487.9297.90 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 0.07Evap.hfg 10 75,8 10 74 .1 10 71. 3 10 68,4 10 65.6 10 59.9 10 54.3 10 48.6 10 42.9 10 37.2 10 31, 6 10 25.8 10 20.0 10 14 .1 100 8.2 10 02.3996.3990.2984 .1 977,99 71. 6970,3Sat.Vaporkg 10 75.8 10 77 .1 107 9.3 10 81. 5 10 83.7 10 88.0 10 92,3 10 96.6 11 00.9 11 05.2 11 09.5 11 13.7 11 17.9 11 22,0 11 26 .1 113 0.2 11 34.2 11 38 .1 1 ... .746 10 .0448.6287.4446.4495.6094.8964.2893.7703.3242.9392.6062. 317 2.06 51 SotVaporvs23 .15 19 .382 16 .323 13 .8 21 11. 763 10 .0 61 8.6457.4 61 6.4665.6264, 914 4.3073.7883.3422.9572.6252.3352.0836EnthalpySat.Liquidhf 18 8 .13 19 8.23208.34 216 .48228.64238.84249.06259. 31 269.59279.92290.28300.68 311 .13 3 21. 63332 .18 342,79353.45364 .17 Evap.Hfg965.2958.8952.2945.5938.79 31. 8924.7 917 .5 910 .1 902.6894.9887.0879.0870,7862.2853.5844.6835.4Sat.Vaporhs 11 53.4 11 57.0 11 60.5 11 64.0 1 16 7.3 1 17 0.6 11 73.8 11 76.8 1 17 9.7 11 82.5 11 85.2 11 87.7 11 90 .1 1 19 2,3 11 94.4 11 96.3 11 98 .1 1 19 9.6EntropySat.LiquidSf0.32390.33870.35 31 0.36750.3 817 0.39580.40960.42340.43690.45040.46370.47690.49000.50290. 515 80.52860.5 413 0.5539Evap.% 1. 42 01 1.39 01 1.3609 1. 3323 1. 3043 1. 2769 1. 25 01 1...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 3 pps
... VaporizationCompoundMethaneEthanePropanen-ButaneIsobutanen-PentaneIsopentaneHexaneHeptaneOctaneNonaneDecaneHeat of Vaporization, 1 4.696 psia atBoiling 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 29BMolecularWeight44. 010 28. 013 34.076 16 .04330.07044.09758 .12 458 .12 472 .15 172 .15 186 .17 8 14 7 19 .48Sum (Aj x B{ ) Sum ( Aj)CCriticalTemp. °R547.87227.3672.6343.37550.09666. 01 734.98765.65829 ,10 845.70 913 .70 11 12.0374.6Sum (A, x Cj)Sum ... Composition4.03 1. 440.0 019 85.555.74 1. 790. 41 0. 41 0.200 .13 0 .15 0 .15 10 0.00Sum (Aj) 19 .48_ '-^ - o 67— — \J,\J 1 29BMolecularWeight44. 010 28. 013 34.076 16 .04330.07044.09758 .12 458 .12 472 .15 172 .15 186 .17 8 14 7 19 .48Sum...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 5 pps
... (Table 2 -1 0) PR = P/PC =1. 47Tr = 375°R (Table 2 -1 0) TR = Tav/Tc = 1. 59qg = 41. 7(AT)CgQgCg = 2.64 [29 x S x C -f ACpjC - 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, the following design criteria should be provided ... Association, Engineering Data Book, 10 th Edition .) 90 Design of GAS-HANDLING Systems and Facilities From Table 3-4 for 1- in. OD, IM-in, square pitch, fixed tubesheet, four passes,...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 6 potx
... 2O-0''8-2-XH8-y'XXH8-2"XH8-2"XXHTO-r'XHio-r'xxM6-3"XH6-3"XXH»2-2"XH 12 -r'XXHWXH8.3-XXH 14 -r'XH 14 -T'XXH1O-3"XH1O-3"XXH 1 -2"XHie-2-xxn 10 -3"XM 10 -3"XXH34407340344073403440734032006820344073403200682034407340320068*0344073403200682029-S26.542.638.364.4580594S3.B93.485.9948BS934.020.54S.O 31. 47B.758066.950.4S4547676 11 4 11 470.970.9 16 6 16 6J13.2 11 X2237237 17 3 .1 173 .1 311 311 19 8 .1 198 .1 2.92.96.06.0 10 .S 10 .5 10 .3 10 .3 17 .9 17 .9 17 .5 17 .828.728.728.028.0 51. 8 51. 8 51. 2SI. ... 2O-0''8-2-XH8-y'XXH8-2"XH8-2"XXHTO-r'XHio-r'xxM6-3"XH6-3"XXH»2-2"XH 12 -r'XXHWXH8.3-XXH 14 -r'XH 14 -T'XXH1O-3"XH1O-3"XXH 1 -2"XHie-2-xxn 10 -3"XM 10 -3"XXH34407340344073403440734032006820344073403200682034407340320068*0344073403200682029-S26.542.638.364.4580594S3.B93.485.9948BS934.020.54S.O 31. 47B.758066.950.4S4547676 11 4 11 470.970.9 16 6 16 6J13.2 11 X2237237 17 3 .1 173 .1 311 311 19 8 .1 198 .1 2.92.96.06.0 10 .S 10 .5 10 .3 10 .3 17 .9 17 .9 17 .5 17 .828.728.728.028.0 51. 8 51. 8 51. 2SI. 2 1. 400 1. 610 2, 210 2. 510 2.87S3.32S3,0303. 616 4.0604,7254.3905,3355,6506.60O6.23S7*78 10 ,11 0 11 .360 10 ,580 12 .240NOMINAL DIMENSIONAL DATASPECIFICATIONS•Subject ... ANSI B 31. 8. Table 5 -1 128 Design ofGAS-HANDUNG Systems and Facilities Estimated U from Figure 2 -11 LTX Units and Line Heaters 11 9illustrates the ratings from API Spec 12 K, ...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 7 ppsx
... rescuedpromptly and given artificialresuscitation.*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 Table 7 -1 Physiological Effects of H2S ... I, and computing: 14 2 Design of GAS-HANDLING Systems and Facilities is controlled by ( 1) perforations in the tray deck (sieve trays), ( 2) bubblecaps (bubble cap trays), or ( 3) ...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 8 doc
... rate of deposition of 15 grains of H2S/min/ft2 of bedcross-sectional area is also recommended to allow for the dissipation of 17 6 Design of GAS-HANDLING Systems and Facilities Figure ... developed and patentedby NL Treating Chemicals and is now a product of Exxon Energy Chem- 16 2 Design of GAS-HANDLING Systems and Facilities The absorption occurs as a result of ... shows asimplified process diagram of the process. 1 78 Design of GAS-HANDLING Systems and Facilities The advantages of amine-aldehyde condensates are water (or oil) solu-ble...
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