ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 1 pps
ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 1 pps
... Anti-Agglomerators, 10 7 CHAPTER S LTX Units and Line Heaters 10 9 LTX Units, 11 0 Line Heaters, 11 2 Heat Duty, 11 3 Fire-Tube Size, 11 5 Coil Sizing, 11 6 Choose Temperatures 11 6, Choose ... modern and common practices. We have either personally been involved in the design and troubleshooting of facilities throughout xiii 10 Design of...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 1 docx
... propylene. 20 8* -37* 2, 5 — 0.05ml pass (1) No. 1 12 3 pass _. Test Methods ASTMD -2 16 3- 82 ASTMD- 12 6 7-84 ASTMD- 18 37- 81 ASTMD -2 16 3- 82 ASTM D -2 16 3- 82 ASTMD -2 15 8-80 ASTM D - 21 58-80 ASTMD- 18 38-84 ASTM ... at 14 0°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...
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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 ... This horsepower loss and additional equipment cost may be more than offset by the increased efficiency of compression...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 3 potx
... contains the rotating parts and on which the cylinders and crossheads are mounted. (Courtesy of Dresser-Rand Company.) 31 0 Design of GAS-HANDLING Systems and Facilities Compressor ... (bottom). 29 4 Design of GAS-HANDLING Systems and Facilities Figure 11-8. Valve-in-piston double-acting compressor cylinder, (Courtesy of Dresser-Rand...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 4 pdf
... 7,500 16,300 18,800 17,700 17,700 17 ,40 0 16,300 17,500 16,300 17,500 11 ,20 0 — 12, 300 10 ,20 0 18,300 20 ,000 21 700 23 ,300 15,000 16,700 18,100 1 6,900 18,300 18,300 20 ,000 20 ,000 20 ,000 20 ,000 23 ,300 21 ,700 25 ,000 25 ,000 25 ,000 25 .000 21 .700 23 ,300 21 ,700 23 ,300 20 ,000 16,700 20 ,000 16,700 Wall ... on Table 12- 2 Summary ANSI Pressure Ratings...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 5 pps
... Facilities (b)Head: ( 1 25 ) ( 120 ) |- == , _ ,— = y 50 5 in (2) (17 ,50 0) (0. 85) - (0 .2) ( 1 25 ) Required thickness = 0 .50 5 + 0 . 25 0 = 0. 755 in. Use—-in. head (0.8 1 25 ) W = (0.34)(0.8 1 25 )( 120 ) 2 + ... (1.9)(0.8 1 25 )( 120 ) = 4,1631b (c) Cone: _ Pd ~ 2 cos a (SE - 0.6P) t ( 1 25 ) ( 120 ) t = ã = 0 .58 5 in. (2 cos 30) (17...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 6 docx
... 1.33 350 1 .63 375 1.93 3 96 1.04 320 1.34 351 J .64 3 76 1.94 397 1.05 321 1.35 3 52 1 .65 3 76 1.95 397 1. 06 322 1. 36 353 1 .66 377 1. 96 398 1.07 323 1.37 353 1 .67 378 1.97 ... 3 36 1.49 364 1.79 3 86 — 1 .20 337 1.50 365 1.80 387 — 1 .21 338 1.51 365 1.81 388 — 1 .22 339 1. 52 366 1. 82 389 — — 1 .23 340 1.53 367...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 7 docx
... to 406 Design of GAS-HANDLING Systems and Facilities tion about the initial cause of a shut-in. They are a vital party of any large shutdown system design. On smaller systems, ... propagate outside the fire tube and out into the open. The flame would then become a source of 400 Design of GAS-HANDLING Systems and Facilities of fai...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 8 docx
... each service and pressure rating. *Reviewed for the 1999 edition by Jorge Zafra of Paragon Engineering Services, Inc. 425 424 Design of GAS-HANDLING Systems and Facilities These ... Safety Low None (table continued on next page) 422 Design of GAS-HANDLING Systems and Facilities form their work safely and to be aware of environmental c...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 9 ppt
... in. H 1 1 VA VA VA 2 2 3 /4 1 1 VA VA 2 2 2 1 1 1 VA VA 2 2 2 VA 1 VA VA VA 2 2 2 ] A 2 1 VA VA 2 2 2 2 } A TA I VA VA 2 2 2 1 A 2 1 A 3 1 VA VA 2 2 2 1 A 2 1 A 4 1 VA VA 2 2 } A 2 1 A 2 1 A 6 1 VA 2 2 2 1 A 2 1 A 3 8 VA VA 2 2 2 1 A 3 3 10 VA VA 2 2 1 A 2 1 A 3 3 12 VA VA 2 2 1 A 2 1 A 3 3 14 VA VA 2 2 1 A 2 { A 3 3 16 VA VA 2 2...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 10 pptx
... 4 82 Design of GAS-HANDLING Systems and Facilities Figure 16*11. The combined cycle of waste heat recovery can be used to generate steam, Effect of Ambient Conditions Available ... Figures 16-1 and 16 -2 illustrate a cross section and an idealized P-V diagram for a four-cycle spark-ignited engine, respectively. 476 Design of GAS-HANDLING Sy...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 11 ppsx
... reduction and the other one for oxidation. The oxidation process with CO takes place as; 2CO + O 2 <-» 2CO 2 The oxidation of UHC is: 2O 2 + CH 4 <-» CO 2 + 2H 2 O And finally, ... 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 occur when the t...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 12 pps
... 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 ... devices and are not acceptable (text continued on page 529 ) 528 Design of GAS-HANDLING Systems and Facilities Figure 17-17. Standard explosion-pro...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 13 docx
... positive-displacement, 25 5 bearings, 29 6 -29 8 reciprocating, 3, 25 5 -26 4 ,28 6- 326 booster, 25 4, 27 6, 28 6 high-speed, 25 8 -25 9 capacity control devices, 3 02 low-speed, 25 9 -26 4 casinghead gas, 25 4 process ... Generators facilities, 3 classified areas, 461 fields, 130 , 25 3 continuous duty, 496 fields, compressor use, 25 4, 26 2 engine-...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 14 pot
... height and diameter, 23 4 glycol reboilers, 21 1 costs, 22 9 Suction description, 22 9 -23 2 pressure throttle valves, 27 8, 28 2 designing, 23 2 -24 0 pressure, compressors, 27 6, 27 8 drying ... drop, 23 4 -23 5 Sulfinol process, 171-1 72 pressures, 23 2 -23 3 Sulfolane, 171 temperatures, 23 2 Sulfreen process, 174 two-tower unit, 22 9 -23 2 Sulfur,...
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