... Choice of Glycol 20 4, Design Considerations 20 5, System Sizing 21 3, Glycol Powered Pumps 21 8 Glycol Dehydration Example, 22 2 Solid Bed Dehydration, 22 8 Process Description 22 9, Design ... 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 / Ken...
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... Tubing Tube OD In. 1 1 VA V/4 VA VA 114 114 VA VA VA 1!4 1!* V/i VA. VA 2 7 2 2 8.W.G. Gauge 18 20 1 8 10 11 12 13 14 16 18 20 10 12 14 16 11 12 13 14 Thickness In. .049 .035 .180 .165 .134 . 120 .109 .095 .083 .065 .049 .035 .134 .109 .083 .065 . 120 .109 .095 .083 Internal Area In, 2 .6390 .6793 . 622 1 .6648 .7574 .80 12 .8365 .8 825 . 922 9 .98 52 1 .0 42 1.094 1.1...
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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-pass fixed-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 Box 5. Stationary Head Nozzle 24 . Packing 6. Stationary Tubesheet 25 . Packing Gland 7. Tubes 26 . Lantern Ring 8. Shell 27 , Tierods and Spacers 9....
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 5 pps
... glycol MW 32. 04 46,07 60.10 62. 07 76.10 106.10 K 2, 335 2, 335 2, 335 2, 200 3,590 4,370 where AT = depression of hydrate formation temperature, °F MW = 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 psia at 76°F. 96 Design of GAS-HANDLING Sy...
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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) bubble caps (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...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 4 pdf
... Passes 1 0 6 12 21 32 38 52 70 89 1 12 138 164 193 22 4 25 8 29 6 336 378 428 4 92 570 658 7 42 838 10 42 2 0 6 12 16 32 38 52 70 88 1 12 138 164 184 22 4 25 6 29 6 3 32 370 426 4 92 566 648 729 823 1034 4 0 4 12 16 32 32 52 68 88 1 12 130 156 i84 21 6 25 6 28 2 3 32 370 414 484 556 648 722 810 1 026 "U"-T«be No, ... Passes 1 12 16 3...
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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 ,300 in. in. psig psig 1XS 0.179 5 ,27 0 2Std 0.154 2, 380 — 2XS 0 .21 8 3,440 — 2XXS 0.436 7,340 8,560 2J4Std 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 1 A 0.750 10, 720 12, 490 2 1 A 0.875 12, 530 14,600 3Std 0 .21 6 2, 260 — 3XS 0.300 3 ,20 0 — 3XXS 0.600 6, 820 7,940 4Std 0 .23...
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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 bed cross-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...
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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 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 ... 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 C...
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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 small amount of wet, byp...
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