ARNOLD, K (1999) Design of Gas-Handling Systems and Facilities (2nd ed ) Episode 2 Part 12 pps
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 0 536 T2A 26 0 500 T2B 23 0 446 T2C 21 5 419 T2D 20 0 3 92 ... T3 180 356 T3A 165 329 T3B 160 320 T3C 135 27 5 T4 120 24 8 T4A 100 21 2 T5 J*5 J85 T6 Table 17-1 (Continued) Comparison of Batteries by Cell Type Proje...
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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 = 0.505 + 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 ... head (a) Skirt: I-°^d + 2 j_j — " r jL 12 _ (0 .2 5) ( 12 0) | 12 = 4.50 ft W = (1 1) ( 12 0)...
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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 1 Part 1 pps
... 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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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 ... Burner Btu/hr 100,000 25 0,000 500,000 750,000 1,000,000 1,500,000 2, 000,000 2, 500,000 3,000,000 3,500,000 4,000,000 5,000,000 Table 2- 12 Sizes and Minimum Diameter Minimu...
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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 2 Part 1 docx
... Typically, high-speed compressors run at a speed of 900 to J 20 0 rpm and slow-speed units at speeds of 20 0 to 600 rpm. 24 0 Design of GAS-HANDLING Systems and Facilities The regeneration ... 140°F Reid Vapor 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 Grad...
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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 Speed High ... the increased efficiency of compression. 28 2 Design of GAS-HANDLING Systems and Facilities Figure...
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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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