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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

ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 1 pps

... Anti-Agglomerators, 10 7CHAPTER SLTX Units and Line Heaters 10 9LTX Units, 11 0Line Heaters, 11 2Heat Duty, 11 3Fire-Tube Size, 11 5Coil Sizing, 11 6Choose Temperatures 11 6, Choose ... modern and common practices. We have either personallybeen involved in the design and troubleshooting of facilities throughoutxiii 10 Design of GAS-HANDLING Systems and Facilities where ... Diameter 11 7,Choose Wall Thickness 11 8, Coil Lengths 11 9Standard Size Line Heaters, 12 0Line Heater Design Example Problem, 12 2CHAPTER 6Condensate Stabilization 13 0Partial Pressures,...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 1 docx

ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 1 docx

... propylene. 20 8*-37* 2, 5—0.05mlpass (1) No. 1 12 3 pass_.TestMethodsASTMD -2 16 3- 82 ASTMD- 12 6 7-84ASTMD- 18 37- 81 ASTMD -2 16 3- 82 ASTM D -2 16 3- 82 ASTMD -2 15 8-80ASTM D - 21 58-80ASTMD- 18 38-84ASTM ... at 14 0°FReid Vapor Pressure3430 26 22 18 14 10 25 !Grade 34 -25 Grade 30 -25 Grade 26 -25 Grade 22 -25 Grade 18 -25 Grade 14 -25 40iGrade 34-40Grade 30-40Grade 26 -40Grade 22 -40Grade 18 -40Grade ... >»GasComponentEthanePropaneButanePentaneNetHeatingValueBtu/SCF 16 18 23 16 3 010 3708SCF/Gallon37.536.4 31. 8 27 .7 52. 00/MMBtuEquivalentValue$/Gallon0. 12 1 30 .16 860 .19 150 .20 54$3.00/MMBtuEquivalentValue$/Gallon0 .1 820 0 .25 290 .28 72 0.30 81 Gas...
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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 2 Part 2 pps

... GasVaporRecoveryFlowRateMMscfd100105 20 100 2 240.11.0 2. 0R 2. 0 2. 0 2. 7 2, 7 2. 7 2. 0 2. 0 2. 04.03.03.0n1!33.31 2 21 2 2Approx.bhp4,4004409803, 920 19,6 02 881903809143 28 6MostLikelyCentrifugalHigh ... This horsepowerloss and additional equipment cost may be more than offset by theincreased efficiency of compression. 28 2 Design of GAS-HANDLING Systems and Facilities Figure 10-15. ... lower 26 6 Design of GAS-HANDLING Systems and Facilities Disadvantagesã Must have clean air or gas.ôTakes 5 to 20 % more horsepower than reciprocating.* Uses ten times the oil of...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 3 potx

ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 3 potx

... contains the rotatingparts 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 Company.)a place to vent and ... from:where Qg = gas throughput, MMscfd 3 02 Design of GAS-HANDLING Systems and Facilities Figyre 11-16. Cut-away view of poppet valve. {Courtesy of 0resser-Roncf Company,)cally...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 4 pdf

ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 4 pdf

... 7,50016,30018,80017,70017,70017 ,40 016,30017,50016,30017,50011 ,20 0— 12, 30010 ,20 018,300 20 ,000 21 700 23 ,30015,00016,70018,1001 6,90018,30018,300 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 ,00016,700 20 ,00016,700Wall ... onTable 12- 2Summary ANSI Pressure Ratings Material Group 1.1Class150300 40 06009001500 25 00 ~20 °FtolOO° 28 5 740 990 148 0 22 2037056170MAWP, psigF 100°Fto200°F 25 06759001350 20 2533755 625 ... cl .2 Grade 22 , cl .2 Grade 21 , cl .2 Grade 5, cl .2 SA -20 3 Grade AGrade BGrade DGrade ESA - 24 0 Grade 3 04 Grade 304LGrade 3 16Grade316LASME Section ViliDiv. 1 Div, 2 -20 °F...
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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

... 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 ,50 0 x 0. 85 - 0.6 x 1 25 )Required thickness = 0 .58 5 + 0 . 25 0 ... specification sheet. 354 Design of GAS-HANDLING Systems and Facilities (c) Summary: Shell 22 ,20 0Head 4,163Head 4,163Skirt 2, 970Cone __L 656 35, 1 52 Misc. _5JQQ40,1 52 Ib CHAPTER13Pressure...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 6 docx

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 3971.05 321 1.35 3 52 1 .65 3 76 1.95 3971. 06 322 1. 36 353 1 .66 377 1. 96 3981.07 323 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 1.83 389 — ã1 .24 341 1.54 368 1.84 ... 1 .25 3 42 1.55 369 1.85 391 — —1 . 26 343 1. 56 369 1. 86 391 —1 .27 344 1.57 370 1.87 3 92 — —1 .28 345 1.58 371 1.88 393 — —1 .29 3 46 1.59 3 72 1.89 393 — —1.30 347 1 .60 ...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 7 docx

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 largeshutdown system design. On smaller systems, ... propagate outside thefire tube and out into the open. The flame would then become a source of 400 Design of GAS-HANDLING Systems and Facilities of failure. However, it is more ... the design of the logicnecessary to carry out the functions that are to be performed when a sig-(text continued on page 410) 388 Design of GAS-HANDLING Systems and Facilities nating...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 8 docx

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 LowNone(table continued on next page) 422 Design of GAS-HANDLING Systems and Facilities form their work safely and to be aware of environmental considerations.Training should ... Jenkins Bros.) 430 Design of GAS-HANDLING Systems and Facilities Table 15 -2 (Continued)Example Specifications of Pipe, Valves, and FittingsCouplings1 -in. and smaller 6000...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 9 ppt

ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 9 ppt

... in.H11VAVAVA 2 23/411VAVA 2 2 2 111VAVA 2 2 2 VA1VAVAVA 2 2 2 ]A 2 1VAVA 2 2 2 2}ATAIVAVA 2 2 2 1A 2 1A31VAVA 2 2 2 1A 2 1A41VAVA 2 2}A 2 1A 2 1A61VA 2 2 2 1A 2 1A38VAVA 2 2 2 1A3310VAVA 2 21A 2 1A33 12 VAVA 2 21A 2 1A3314VAVA 2 21A 2 {A3316VAVA 2 2}A 2 1A33M18VAVA 2 21A 2 {A331AFiat 20 ... 160- 520 114731-1040641 -94 0711 -96 0661-880641-870 621 -96 0601-810601- 790 551-740160-740160-750160-740160-700160- 690 160- 690 160- 690 160-680160-680 521 -660 2 1041- 120 0 94 1- 120 0 96 1- 120 0881- 120 0871-1 090 96 1-1160811-1000 791 -97 0741 -93 0741 -90 0751 -90 0741 -90 0701-850 691 -840 691 -830 691 -830681- 820 681-810661- 790 2H_—__1 091 - 120 01161- 120 01001- 120 0 97 1-1 125 93 1-1 090 90 1-1 090 90 1-1060 90 1-1030851-1000841 -98 0831 -97 0831 -97 0 821 -96 0811 -95 0 791 -90 06(in.)3—___—_1 126 - 120 01 091 - 120 01 091 - 120 01061- 120 01031-11701001-1130 98 1-1 120 97 1-1100 97 1-1100 96 1-1 090 95 1-1080 90 1-10107 ... in.H11VAVAVA 2 23/411VAVA 2 2 2 111VAVA 2 2 2 VA1VAVAVA 2 2 2 ]A 2 1VAVA 2 2 2 2}ATAIVAVA 2 2 2 1A 2 1A31VAVA 2 2 2 1A 2 1A41VAVA 2 2}A 2 1A 2 1A61VA 2 2 2 1A 2 1A38VAVA 2 2 2 1A3310VAVA 2 21A 2 1A33 12 VAVA 2 21A 2 1A3314VAVA 2 21A 2 {A3316VAVA 2 2}A 2 1A33M18VAVA 2 21A 2 {A331AFiat 20 24 30 Surf,VA VA VA VAVA VA VA VA 22 22 21A...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 10 pptx

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 generatesteam,Effect of Ambient ConditionsAvailable ... Figures 16-1 and 16 -2 illustrate a cross section and anidealized P-V diagram for a four-cycle spark-ignited engine, respectively. 476 Design of GAS-HANDLING Systems and Facilities CarhuretionFuel ... illustrates how waste heat can be recovered and usedto heat process fluids. 4 62 Design of GAS-HANDLING Systems and Facilities Often on high-pressure wells two chokes are...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 11 ppsx

ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 11 ppsx

... reduction and theother one for oxidation. The oxidation process with CO takes place as;2CO + O 2 <-» 2CO 2 The oxidation of UHC is:2O 2 + CH4 <-» CO 2 + 2H 2 O And finally, ... reduction of NOX 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 temperature exceeds 500°~6QO°F (26 0°-316°C). ... edition by Dinesh P. Patel of Paragon Engineering Services, Inc.493 4 92 Design of GAS-HANDLING Systems and Facilities Based on the results of the catalytic combustor, there...
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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

... T2A 26 0 500 T2B 23 0 446 T2C 21 5 419 T2D 20 0 3 92 T3180 356 T3A165 329 T3B160 320 T3C135 27 5 T4 120 24 8 T4A100 21 2 T5J*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-proof alarm devices. (Courtesy of ... 17 -24 .Sealing FittingsConduit and cable sealing fittings as shown in Figures 17 -25 and 17- 26 are provided for the following purposes: 5 32 Design of GAS-HANDLING Systems and ...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 13 docx

ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 13 docx

... positive-displacement, 25 5bearings, 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 9capacity control devices, 3 02 low-speed, 25 9 -26 4casinghead gas, 25 4 process ... Generators facilities, 3 classified areas, 461fields, 130 , 25 3 continuous duty, 496fields, compressor use, 25 4, 26 2 engine-driven, 493559 5 42 Design of GAS-HANDLING Systems and Facilities Electric ... considerations, 27 6 -28 0centrifugal, 3, 26 7 -27 0, 28 6 rod, 29 4, 310-311centr i fugal proces s considerations, rotary ,3 ,25 5 28 1 -28 5 screw, 25 5, 26 6 -26 7centrifugal, stonewalling, 28 0 -28 1...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 14 pot

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 1costs, 22 9 Suctiondescription, 22 9 -23 2 pressure throttle valves, 27 8, 28 2designing, 23 2 -24 0 pressure, compressors, 27 6, 27 8drying ... drop, 23 4 -23 5 Sulfinol process, 171-1 72 pressures, 23 2 -23 3 Sulfolane, 171temperatures, 23 2 Sulfreen process, 174two-tower unit, 22 9 -23 2 Sulfur, 1 72- 174, 176Sour gas, 151, 1 62 Sulfur ... stabilizers, 141 -145 pipe, 376,447 contactors, kinds, 198 -20 0Surge distillation towers, 134 ! 37, 25 1control and stonewalling, 28 0 -28 1 Treating, tail-gas, 174control valves, 28 1 -28 2 Triethylene...
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