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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 6 potx

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 1 Part 2 doc

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

... /-X4%%/i/'4;/4ã%/'i3/;|sIi 1 1 1 1B.W.G.Gauge 22 24 26 27 18 20 22 24 16 18 20 22 12 13 14 15 16 17 18 19 20 10 11 12 13 14 15 16 17 18 20 8 10 11 12 13 14 15 16 ThicknessIn.. 028 . 022 . 018 . 016 .049.035, 028 . 022 .065.049.035. 028 .10 9.095.083.0 72 .065.058.049.0 42 .035 ,13 4 . 12 0 .10 9.095.083.0 72 .065.058.049.035 .16 5 .13 4 . 12 0 .10 9.095.083.0 72 .065internalArea!n. 2 . 029 5.0333.0360.0373.0603.07 31 .0799.0860 .10 75 . 12 69 .14 52 .15 48 .13 01 .14 86. ... 26 .78Sot.Vaporvg3306 29 47 24 44 20 36,4 17 03 .2 12 06.7867,9633 .1 468.0350.4 26 5.4 20 3 .27 15 7.34 12 3, 01 97.0777 .29 62. 0650 .23 40.9633.64 27 . 82 26.80EnthalpySat.Liquid0.003. 02 8.05 13 .06 18 ,07 28 .0638.0448, 02 57.9967.9777.9487. 92 97.90 10 7.89 11 7.89 12 7.89 13 7.90 14 7. 92 15 7.95 16 7.99 17 8.05 18 0.07Evap.hfg 10 75,8 10 74 .1 10 71. 3 10 68,4 10 65.6 10 59.9 10 54.3 10 48.6 10 42. 9 10 37 .2 10 31, 6 10 25 .8 10 20 .0 10 14 .1 1008 .2 10 02. 3996.3990 .2 984 .1 977,99 71. 6970,3Sat.Vaporkg 10 75.8 10 77 .1 1079.3 10 81. 5 10 83.7 10 88.0 10 92, 3 10 96.6 11 00.9 11 05 .2 11 09.5 11 13.7 11 17.9 11 22 ,0 11 26 .1 113 0 .2 11 34 .2 11 38 .1 1 14 2. 0 1 14 5.9 11 49.7 1 1. 50.4EntropySat.LiquidSf0.00000.00 61 0. 016 2 0. 026 20,03 61 0.05550.07450.09 32 0 .11 150 . 12 950 .14 71 0 .16 450 .18 160 ,19 840. 21 4 90 .2 311 0 .24 72 0 .26 300 .27 850 ,29 38Evap.% 2 .18 77 2 .17 09 2 .14 35 2 ,11 67 2. 0903 2. 0393 1. 99 02 1. 9 428 1. 89 72 1. 85 31 1. 810 6 1. 7694 1. 729 6 1. 6 910 1. 6537 1. 617 4 1. 5 822 1, 5480 1. 514 7 1, 4 824 0.3090 ... 1. 50.4EntropySat.LiquidSf0.00000.00 61 0. 016 2 0. 026 20,03 61 0.05550.07450.09 32 0 .11 150 . 12 950 .14 71 0 .16 450 .18 160 ,19 840. 21 4 90 .2 311 0 .24 72 0 .26 300 .27 850 ,29 38Evap.% 2 .18 77 2 .17 09 2 .14 35 2 ,11 67 2. 0903 2. 0393 1. 99 02 1. 9 428 1. 89 72 1. 85 31 1. 810 6 1. 7694 1. 729 6 1. 6 910 1. 6537 1. 617 4 1. 5 822 1, 5480 1. 514 7 1, 4 824 0.3090...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 3 pps

ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 3 pps

... VaporizationCompoundMethaneEthanePropanen-ButaneIsobutanen-PentaneIsopentaneHexaneHeptaneOctaneNonaneDecaneHeat of Vaporization, 1 4.696 psia atBoiling Point, Btu/lb 219 .22 210 . 41 1 83. 05 16 5.65 15 7. 53 15 3. 59 14 7 . 13 14 3. 95 13 6. 01 129. 53 12 3. 76 11 8.68 ... 1 29BMolecularWeight44. 010 28. 0 13 34 .076 16 .0 43 30.07044.09758 .12 458 .12 472 .15 172 .15 186 .17 8 14 7 19 .48Sum (Aj x B{)Sum ( Aj)CCriticalTemp. °R547.87227 .3 672.6 34 3 .37 550.09666. 01 734 .98765.65829 ,10 845.70 9 13 .70 11 12.0 37 4.6Sum ... Composition4. 03 1. 440.0 019 85.555.74 1. 790. 41 0. 41 0.200 . 13 0 .15 0 .15 10 0.00Sum (Aj) 19 .48_ '-^ - o 67— — \J,\J 1 29BMolecularWeight44. 010 28. 0 13 34 .076 16 .0 43 30.07044.09758 .12 458 .12 472 .15 172 .15 186 .17 8 14 7 19 .48Sum...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 4 pdf

ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 4 pdf

... Passes 1 12 21 37 61 97 11 3 15 6208256 3 14 379 44 8522603688788897 10 09 11 18 12 98 15 00 17 14 2 10 18 32 54 90 10 8 14 6 1% 244 299363 43 25 04 583667770873983 10 92 12 69 14 70lh 81 4 8 16 28 48 84 10 4 13 6 18 4 2362 94 352 41 6 48 65686 54 756850958 10 66 12 50 14 40 16 501Qô ... Passes 1 12 16 3252 81 97 14 0 18 82 41 296356 41 4 48 2570658 742 846 952 10 62 12 32 14 24 16 36 18 45 26 16 285278 94 13 2 17 82 24 280 344 40 6 47 6562 640 7328 31 9 31 1 045 12 22 14 15 16 34 18 322080 | 206f 4 4 12 24 527688 12 4 17 2 216 276332392 46 8 548 640 732820928 10 26 12 18 13 86 16 02 18 182(W4i ... SheetNo. of Passes 1 78 19 29 42 526992 12 1 14 7 17 4 19 6237280 313 357 41 6 4 61 511 596687790896 10 08 12 41 2 4 6 14 2638 48 68 84 11 0 13 8 16 5 19 6226269 313 346 4 01 45 3 49 3579673 4 4 4 12 20 34 44 6078 10 4 12 8 15 6 18 4 2 24 2562 94 332386 43 2 47 8570662782...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 5 pps

ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 5 pps

... linearly,yn, MoleFractionin Gas0. 014 40.04030.000 019 0. 855 50. 057 40. 017 90.00 41 0.00 41 0.0063 1. 0000Y/K =1. 0at740]At 70KnInfinityInfinity0.30. 95 0.720. 25 0 . 15 0.72InfinityF°Fyn/i<n0.000.000.000.900.080.070.030.000.00J.08At ... 2 -14 ) 10 0 Design of GAS-HANDLINCr Systems and facilities by Figure 4-6. The graph shows the water content in pounds of water perMMscf of saturated gas at any pressure and ... amount of water vapor saturated in the gas is given 4-7, Typical Gas Association, ICHh 11 0 Design of GAS-HANDLING Systems and Facilities LTX UNITSThese units are designed...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 6 potx

ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 6 potx

... 2O-0''8-2-XH8-y'XXH8-2"XH8-2"XXHTO-r'XHio-r'xxM 6- 3"XH 6- 3"XXHằ2-2"XH 12 -r'XXHWXH8.3-XXH 14 -r'XH 14 -T'XXH1O-3"XH1O-3"XXH 1 -2"XHie-2-xxn 10 -3"XM 10 -3"XXH3440734034407340344073403200 68 20344073403200 68 20344073403200 68 *0344073403200 68 2029-S 26. 542 .6 38.3 64 .4580594S3.B93.485.9948BS934.020.54S.O 31. 47B.7580 66 .950.4S454 76 76 11 4 11 470.970.9 16 6 16 6 J13.2 11 X2237237 17 3 .1 173 .1 311 311 19 8 .1 198 .1 2.92.9 6. 0 6. 0 10 .S 10 .5 10 .3 10 .3 17 .9 17 .9 17 .5 17 .828.728.728.028.0 51. 8 51. 8 51. 2SI. 2 1. 400 1. 61 0 2, 210 2. 510 2.87S3.32S3,0303. 61 6 4. 060 4,7254.3905,3355 ,65 0 6. 60O 6. 23S7*78 10 ,11 0 11 . 360 10 ,580 12 .240NOMINAL ... 2O-0''8-2-XH8-y'XXH8-2"XH8-2"XXHTO-r'XHio-r'xxM 6- 3"XH 6- 3"XXHằ2-2"XH 12 -r'XXHWXH8.3-XXH 14 -r'XH 14 -T'XXH1O-3"XH1O-3"XXH 1 -2"XHie-2-xxn 10 -3"XM 10 -3"XXH3440734034407340344073403200 68 20344073403200 68 20344073403200 68 *0344073403200 68 2029-S 26. 542 .6 38.3 64 .4580594S3.B93.485.9948BS934.020.54S.O 31. 47B.7580 66 .950.4S454 76 76 11 4 11 470.970.9 16 6 16 6 J13.2 11 X2237237 17 3 .1 173 .1 311 311 19 8 .1 198 .1 2.92.9 6. 0 6. 0 10 .S 10 .5 10 .3 10 .3 17 .9 17 .9 17 .5 17 .828.728.728.028.0 51. 8 51. 8 51. 2SI. ... B 31. 3 and B 31. 8, or American Petroleum Institute (API) Specification 12 K. Volume 1 has the tables for ANSI B 31. 3 and ANSI B 31. 8. Table 5 -1 12 8 Design ofGAS-HANDUNG Systems and ...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 7 ppsx

ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 7 ppsx

... on 1% hydrogen sulfide = 629 .77 gr /10 0 scfat 14 .696 psia and 59°F, or 10 1,325 kPa and 75 °C. 15 6 Design of GAS-HANDLING Systems and Facilities (text continued from page 15 3)GAS ... threat-*Reviewed for the 19 99 edition by K. S. Chiou of Paragon Engineering Services, Inc. 15 1 15 2 Design of GAS-HANDLING Systems and Facilities Table 7 -1 Physiological Effects of H2S Concentrations ... 44.080 .10 + 10 00+ 62.98Milligramsper m3*0 .18 14 . 41 72 . 07 14 4 .14 288.06 72 0.49 10 08.55 14 40.98+PhysiologicalEffectsObvious and unpleasant odorgenerally perceptible at 0 .13 ppm and quite...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 8 doc

ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 8 doc

... rate of deposition of 15 grains of H2S/min/ft2 of bedcross-sectional area is also recommended to allow for the dissipation of 17 6 Design of GAS-HANDLING Systems and Facilities Figure ... developed and patentedby NL Treating Chemicals and is now a product of Exxon Energy Chem- 16 2 Design of GAS-HANDLING Systems and Facilities The absorption occurs as a result of the ... areas of carbon steel that have been 16 8 Design of GAS-HANDLING Systems and Facilities Figure 7-5. Hot carbonate system for gas sweetening.stream. The high temperature of the...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 9 pdf

ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 9 pdf

... rateFigure 8 -9. Equilibrium water dew points at different temperatures for gases. 19 2 Design of GAS-HANDLING Systems and Facilities ci Hin. _ft_ 18 1. 9. 220 15 ,522 12 .824 10 .830 ... a pressure of 3,000 psia and atemperature of 15 0°R From Figure 8 -1 at a temperature of 15 0°F and pressure of 3,000 psia there is 10 4 Ib of water per MMscf of wet gas. ... the inlet temperature and pressure con-ditions, but adsorbs water at the reboiler conditions of atmospheric pres- 19 0 Design of GAS-HANDLING Systems and Facilities When MEA is...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 10 pdf

ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 10 pdf

... 222 Design of GAS-HANDLING Systems and Facilities Table 8-3Gas Consumption by Glycol Powered PumpContactorOperatingPressurepsig300400500600700800900 10 00 11 00 12 00 13 00 14 00 15 00PumpGasConsumptionsc ... (Volume 1, Chapter 4). This is: 218 Design of GAS-HANDLING Systems and Facilities Table 8 -1 Example Contactor Sizes for Dehydrating 50 MMscfdat 1, 000 psig and 10 0°FTowerTower ... because of a multitude of microscopic pores and capillary 216 Design of GAS-HANDLING Systems and Facilities Figure 8 -16 . Glycol concentration vs. glycol circulation when n = 1. 5...
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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 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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