ARNOLD, K (1999) Design of Gas-Handling Systems and Facilities (2nd ed ) Episode 2 Part 2 pps
ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 1 pps
... Choice of Glycol 20 4, Design Considerations 20 5, System Sizing 21 3,Glycol Powered Pumps 21 8Glycol Dehydration Example, 22 2Solid Bed Dehydration, 22 8Process Description 22 9, Design ... atwww.bh.com/gujf10 987654Library of Congress Cataloging-in-Publication Data Arnold, Ken, 19 42- Design of gas-handling systems and facilities / Ken Arnold, MauriceStewart. — 2nd ed. p. cm. — (Surface ... OperationsVOLUME 2 Design of Gas-Handling Systems and Facilities Copyright © 1989, 1999 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
... TubingTubeODIn.11VAV/4VAVA114114VAVAVA1!41!*V/iVA.VA 2 7 2 28.W.G.Gauge18 20 181011 12 13141618 20 10 12 141611 12 1314ThicknessIn..049.035.180.165.134. 120 .109.095.083.065.049.035.134.109.083.065. 120 .109.095.083InternalAreaIn, 2 .6390.6793. 622 1.6648.7574.80 12 .8365.8 825 . 922 9.98 52 1 .0 42 1.0941.1 92 1 .29 11 .3981.474 2. 433 2. 494 2. 573 2. 6 42 Ft 2 ExternalSurfacePer FtLength ,26 18 .26 18. 327 2. 327 2. 327 2. 327 2. 327 2. 327 2. 327 2. 327 2. 327 2. 327 2.3 927 .3 927 .3 927 .3 927 . 523 6. 523 6. 523 6. 523 6Ft 2 InternalSurfacePer ... FtLength ,26 18 .26 18. 327 2. 327 2. 327 2. 327 2. 327 2. 327 2. 327 2. 327 2. 327 2. 327 2.3 927 .3 927 .3 927 .3 927 . 523 6. 523 6. 523 6. 523 6Ft 2 InternalSurfacePer FtLength .23 61 .24 35 ,23 30 .24 09 .25 71 .26 44 .27 02 .27 75 .2, 838 .29 32 .3016.3089. 322 5.3356.34 92 .3587.4608.4665.4739.480!where ... /-X4%%/i/'4;/4•%/'i3/;|sIi1111B.W.G.Gauge 22 24 26 27 18 20 22 24 1618 20 22 12 13141516171819 20 1011 12 131415161718 20 81011 12 13141516ThicknessIn.. 028 . 022 .018.016.049.035, 028 . 022 .065.049.035. 028 .109.095.083.0 72 .065.058.049.0 42 .035,134. 120 .109.095.083.0 72 .065.058.049.035.165.134. 120 .109.095.083.0 72 .065internalArea!n. 2 . 029 5.0333.0360.0373.0603.0731.0799.0860.1075. 126 9.14 52 .1548.1301.1486....
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 3 pps
... example of a two-passfixed-tube exchanger is shown in Figure 3 -2. 56 Design of GAS-HANDLING Systems and Facilities Figure 3-9. Heat exchanger components (continued). (From ... 23 . Packing Box5. Stationary Head Nozzle 24 . Packing6. Stationary Tubesheet 25 . Packing Gland7. Tubes 26 . Lantern Ring8. Shell 27 , Tierods and Spacers9. Shell Cover 28 . ... nozzle.Many of the rear end types allow the head to "float" as the tube bundleexpands and contracts.60 Design of GAS-HANDLING Systems and Facilities TEMA Glasses and ...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 5 pps
... glycolMW 32. 0446,0760.10 62. 0776.10106.10 K 2, 335 2, 335 2, 335 2, 2003,5904,370where AT = depression of hydrate formation temperature, °FMW = molecular weight of inhibitor (Table 4- 2) K ... gas of our example field (Table 2- 1 0), Figure 4-5 predicts a hydrate formation temperature at 4,000 psiaat 76°F.96 Design of GAS-HANDLING Systems and Facilities Figure 4 -2, ... Data Book, 10th 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, shell ID = 29 in.Use...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 7 ppsx
... I, and computing:1 42 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) ... ele-ments of structured packing are placed. Beds of structured packing typi-cally have lower pressure drops than beds of random packing of compa-rable mass transfer efficiency. Structured ... is introducedquickly the heat of reaction may ignite the bed.140 Design of GAS-HANDLING Systems and Facilities Table 6-1Vapor Pressure and Relative Volatility of Various...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 4 pdf
... Passes106 12 21 32 38 52 70891 12 138164193 22 4 25 8 29 6336378 428 4 92 5706587 42 83810 42 206 12 16 32 38 52 70881 12 138164184 22 4 25 6 29 63 32 370 426 4 92 566648 729 823 1034404 12 16 32 32 52 68881 12 130156i84 21 6 25 6 28 23 32 370414484556648 722 8101 026 "U"-T«beNo, ... Passes1 12 16 32 52 8197140188 24 1 29 63564144 82 5706587 42 8469 52 10 62 123 21 424 16361845 2 616 28 52 78941 32 178 22 4 28 03444064765 62 6407 32 8319311045 122 21415163418 32 2080 | 20 6f44 12 24 52 7688 124 1 72 216 27 63 32 3 92 4685486407 32 820 928 1 026 121 8138616 02 1818 2( W4i ... Passes146 12 243745618097 124 1451 72 210 24 1 27 23103563964 42 5186 02 6 82 7708 62 1084 2 46 12 22 34 42 607695 124 145168 20 2 23 4 26 83063533874385186 02 681760860444 12 16 32 42 52 7688 120 144164 20 2 23 0 26 83 02 3383844345 02 5886767568561070...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 6 potx
... = 20 ,000 5 = 23 ,300in. in. psig psig1XS 0.179 5 ,27 02Std 0.154 2, 380 —2XS 0 .21 8 3,440 —2XXS 0.436 7,340 8,5602J4Std 0 .20 3 2, 600 — 2! 4XS 0 .27 6 3,610 —2I4XXS 0.5 52 7,770 ... —2I4XXS 0.5 52 7,770 9,050 2 1A 0.750 10, 720 12, 490 2 1A 0.875 12, 530 14,6003Std 0 .21 6 2, 260 —3XS 0.300 3 ,20 0 —3XXS 0.600 6, 820 7,9404Std 0 .23 7 1, 920 —4XS 0.337 2, 770 —4XXS 0.674 ... of the fire tube is normally calculated based on a heat fluxrate of 10,000 Btu/hr-ft 2 . The fire-tube length can be determined from: 124 Design of GAS-HANDLING Systems and ...
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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 H 2 S/min/ft 2 of bedcross-sectional area is also recommended to allow for the dissipation of 176 Design of GAS-HANDLING Systems and Facilities Figure ... is required and use the appropriate guide:Removal of H 2 S with no CO 2 present (Figure 7-1 1) Removal of H 2 S and CO 2 (Figure 7-1 2) Removal of CO 2 with no H 2 S present ... restrict the amount of H 2 S that can bevented or flared in the regeneration cycle.1 82 Design of GAS-HANDLING Systems and Facilities Figure 7-13. CO2 removal, no h^S.The...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 9 pdf
... gases.1 92 Design of GAS-HANDLING Systems and Facilities ci Hin. _ft_18 1.9 .2 20 15,5 22 12. 8 24 10.830 6.936 4.8An acceptable choice is a 30-in. OD vessel. The wall thicknesscan ... at the reboiler conditions of atmospheric pres-190 Design of GAS-HANDLING Systems and Facilities When MEA is used in the presence of COS and CS 2 , they react to formheat-stable ... DEA198 Design of GAS-HANDLING Systems and Facilities Figure 8 *2. Effective water content of CO 2 . (From Gas Processors SuppliersAssociation, engineering Data Book, 10th Edition .) Process...
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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 21 4 Design of GAS-HANDLING Systems and Facilities Figure 8-14. Structured (matrix) packing, (from Koch Industries .) Contactor ... Too much 23 2 Design of GAS-HANDLING Systems and Facilities mit some of the wet gas to bypass the desiccant bed. Only a smallamount of wet, bypassed gas is needed to cause ... atmosphere. 21 2 Design of GAS-HANDLING Systems and Facilities Figure 8- 12. Effect of stripping gas on glyco! concentration.dehydrators are designed for approximately three gallons of ...
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