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 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,...
- 25
- 362
- 0
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...
- 25
- 383
- 0
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...
- 25
- 348
- 0
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...
- 25
- 379
- 0
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...
- 25
- 351
- 0
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 ...
- 25
- 473
- 0
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...
- 25
- 391
- 0
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...
- 25
- 403
- 0
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...
- 25
- 438
- 0
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...
- 25
- 446
- 0
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...
- 25
- 459
- 0
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 ...
- 25
- 289
- 0
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...
- 25
- 299
- 0
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...
- 25
- 252
- 0
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...
- 25
- 372
- 0
Từ khóa: the design of water transport and distribution systemsthermodynamics dynamic equilibrium and implications for the design of control systemsa flow chart summary of the itraq™ experiment design of 4 plex and 8 plex systems 63design of control systemsperformance evaluation of computer systems and networksdesign of control systems for dc drives pdfdesign of control systems pptdesign of control systems using matlabdesign of control systems for a quadrotordesign of control systems pdfdesign of control systems in state spacedesign of control systems for dc drives3a program and project management for the acquisition of capital assets and doe m 413 3 1 project management for the acquisition of capital assets and doe std 1189 2008 integration of safety into the design processuse of telemedicine systems and devices for patient monitoringgrounding of electrical systems and equipmentNghiên cứu sự biến đổi một số cytokin ở bệnh nhân xơ cứng bì hệ thốngBáo cáo quy trình mua hàng CT CP Công Nghệ NPVMột số giải pháp nâng cao chất lượng streaming thích ứng video trên nền giao thức HTTPBiện pháp quản lý hoạt động dạy hát xoan trong trường trung học cơ sở huyện lâm thao, phú thọGiáo án Sinh học 11 bài 13: Thực hành phát hiện diệp lục và carôtenôitGiáo án Sinh học 11 bài 13: Thực hành phát hiện diệp lục và carôtenôitGiáo án Sinh học 11 bài 13: Thực hành phát hiện diệp lục và carôtenôitNGHIÊN CỨU CÔNG NGHỆ KẾT NỐI VÔ TUYẾN CỰ LY XA, CÔNG SUẤT THẤP LPWAN SLIDENghiên cứu, xây dựng phần mềm smartscan và ứng dụng trong bảo vệ mạng máy tính chuyên dùngNghiên cứu về mô hình thống kê học sâu và ứng dụng trong nhận dạng chữ viết tay hạn chếNghiên cứu tổng hợp các oxit hỗn hợp kích thƣớc nanomet ce 0 75 zr0 25o2 , ce 0 5 zr0 5o2 và khảo sát hoạt tính quang xúc tác của chúngĐịnh tội danh từ thực tiễn huyện Cần Giuộc, tỉnh Long An (Luận văn thạc sĩ)Kiểm sát việc giải quyết tố giác, tin báo về tội phạm và kiến nghị khởi tố theo pháp luật tố tụng hình sự Việt Nam từ thực tiễn tỉnh Bình Định (Luận văn thạc sĩ)BT Tieng anh 6 UNIT 2Tăng trưởng tín dụng hộ sản xuất nông nghiệp tại Ngân hàng Nông nghiệp và Phát triển nông thôn Việt Nam chi nhánh tỉnh Bắc Giang (Luận văn thạc sĩ)Giáo án Sinh học 11 bài 14: Thực hành phát hiện hô hấp ở thực vậtGiáo án Sinh học 11 bài 14: Thực hành phát hiện hô hấp ở thực vậtChiến lược marketing tại ngân hàng Agribank chi nhánh Sài Gòn từ 2013-2015MÔN TRUYỀN THÔNG MARKETING TÍCH HỢPQUẢN LÝ VÀ TÁI CHẾ NHỰA Ở HOA KỲ