ARNOLD, K (1999) Design of Gas-Handling Systems and Facilities (2nd ed ) Episode 2 Part 5 pps
ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 5 pps
... (17 ,50 0) (0.8 5) - (0. 2) ( 12 5) Required thickness = 0 .50 5 + 0 . 25 0 = 0. 755 in. Use—-in. head (0.8 12 5) W = (0.3 4)( 0.8 12 5) ( 12 0) 2 + (1. 9)( 0.8 12 5) ( 12 0) = 4,1631b (c) Cone: _ Pd ~ 2 ... 0.6P) t ( 12 5) ( 12 0) t = • = 0 .58 5 in. (2 cos 3 0) (17 ,50 0 x 0. 85 - 0.6 x 12 5) Required thickness...
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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, 3 35 2, 3 35 2, 3 35 2, 200 3 ,59 0 4,370 where AT = depression of hydrate formation temperature, °F MW = molecular weight of inhibitor (Table 4- 2) K ... duty T, = 6 35 R T 2 = 56 0°R T av =59 7 .5 R P c = 680 psia (Table 2- 1 0) P R = P/P C =1.47 T r = 3 75 R (Table 2- 1 0) T R = T av /T...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 11 ppsx
... CH 4 <-» CO 2 + 2H 2 O And finally, the reduction of NO X with CO results in N 2 and CO 2 : NO 2 + CO <-» NO + CO 2 2NO + 2CO <-» N 2 + 2CO 2 Catalytic reactions ... there *Reviewed for the 1999 edition by Dinesh P. Patel of Paragon Engineering Services, Inc. 493 4 92 Design of GAS-HANDLING Systems and Facilities Based o...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 12 pps
... 17 -2 Temperature Ratings of Explosion-Proof Enclosures Maximum Temperature Identification °C °F Number 450 8 42 Tl 300 5 72 T2 28 0 53 6 T2A 26 0 50 0 T2B 23 0 446 T2C 21 5 419 T2D 20 0 3 92 ... 3 92 T3 180 356 T3A 1 65 329 T3B 160 320 T3C 1 35 27 5 T4 120 24 8 T4A 100 21 2 T5 J *5 J 85 T6 Table 17-1 (Continued) Comparison of Batteries...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 1 pps
... at www.bh.com/gujf 10 987 654 Library of Congress Cataloging-in-Publication Data Arnold, Ken, 19 42- Design of gas-handling systems and facilities / Ken Arnold, Maurice Stewart. — 2nd ed. p. cm. ... Pumps 21 8 Glycol Dehydration Example, 22 2 Solid Bed Dehydration, 22 8 Process Description 22 9, Design Considerations 23 2 Dry Desiccant Design E...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 3 pps
... Burner Btu/hr 100,000 25 0,000 50 0,000 750 ,000 1,000,000 1 ,50 0,000 2, 000,000 2, 50 0,000 3,000,000 3 ,50 0,000 4,000,000 5, 000,000 Table 2- 12 Sizes and Minimum Diameter Minimum Diameter-in. 2. 5 3.9 5. 5 6.7 7.8 9 .5 11.0 12, 3 13 .5 14.6 15. 6 17.4 * 42 Design ... 1 29 B Molecular Weight 44.010 28 .013 34.076 16.043 30.070 44.097 58 . 124 58 . 124...
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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) ... rescued promptly and given artificial resuscitation. *Based on 1% hydrogen sulfide = 629 .77 gr/100 scfat 14.696 psia and 59 °F, or 101, 3 25 kPa and 75...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 1 docx
... Pressure 34 30 26 22 18 14 10 25 ! Grade 34 - 25 Grade 30 - 25 Grade 26 - 25 Grade 22 - 25 Grade 18 - 25 Grade 14 - 25 40 i Grade 34-40 Grade 30-40 Grade 26 -40 Grade 22 -40 Grade 18-40 Grade 14-40 55 i Grade 34 -55 Grade ... Beads Fluorite Alumina Gel (H- 15 1) Silica Gel Molecular Sieves (4A) Bulk Density (Jb/fc 3) 51 49 50 52 45 45 Specific Heat (...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 2 pps
... Gas Vapor Recovery Flow Rate MMscfd 100 10 5 20 100 2 2 4 0.1 1.0 2. 0 R 2. 0 2. 0 2. 7 2, 7 2. 7 2. 0 2. 0 2. 0 4.0 3.0 3.0 n 1 ! 3 3 .3 1 2 2 1 2 2 Approx. bhp 4,400 440 980 3, 920 19,6 02 88 190 380 9 143 28 6 Most Likely Centrifugal High ... service. 26 2 Design of GAS-HANDLING Systems and Facilities Figure 10 -5. Integral engine compressor. (Cou...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 3 potx
... Design of GAS-HANDLING Systems and Facilities tlon and discharge valves so that the valves can be removed and rein- stalled. These clearances are called fixed clearances and ... contains the rotating parts and on which the cylinders and crossheads are mounted. (Courtesy of Dresser-Rand Company .) 310 Design of GAS-HANDLING Systems...
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