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

... throttle valves, 27 8, 28 2designing, 23 2 -24 0 pressure, compressors, 27 6, 27 8drying cycle time, 23 3 scrubbers, 25 6, 28 0, 28 5gas velocities, 23 3 shutdown bypass valve, 28 5introduction, ... 175-176SO 2 . See Sulfur dioxide. Stripping gasSolid bed process glycol process, 20 3 -20 4bed height and diameter, 23 4 glycol reboilers, 21 1costs, 22 9 Suctiondescription, 22 9 -23 2 ... discharge, 27 3 -27 6 Turboexpanders, 24 8 -24 9 design, 445difference, average, 12 U.S. Coast Guard, 529 difference, log mean (LMTD), 11 -14 U.S. Code of Federal Regulations, 5 52 drop,...

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 rotatingparts and on which the cylinders and crossheads are mounted. (Courtesy of Dresser-Rand Company .) 310 Design of GAS-HANDLING Systems and Facilities Compressor ... 28 8 Design of GAS-HANDLING Systems and Facilities facturers for a maximum continuous horsepower, speed (rpm), and rodload. The rated horsepower is determined by the...

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

... = 20 ,000 5 = 23 ,300in. in. psig psig1XS 0.179 5 ,27 02Std 0.154 2, 380 —2XS 0 .21 8 3,440 —2XXS 0.436 7,340 8,5602J4Std 0 .20 3 2, 600 — 2! 4XS 0 .27 6 3,610 —2I4XXS 0.5 52 7,770 ... 2O-0''8 -2- XH8-y'XXH8 -2& quot;XH8 -2& quot;XXHTO-r'XHio-r'xxM6-3"XH6-3"XXH 2- 2"XH 12- r'XXHWXH8.3-XXH 14- r'XH 14- T'XXH1O-3"XH1O-3"XXH1« -2& quot;XHie -2- xxn10-3"XM10-3"XXH344073403440734034407340 320 06 820 34407340 320 06 820 34407340 320 068*034407340 320 06 820 29 -S 26 .5 42. 638.364.4580594S3.B93.485.9948BS934.0 20 .54S.O31.47B.758066.950.4S4547676 114 114 70.970.9166166J13 .2 11X2 23 7 23 7173.1173.1311311198.1198.1 2. 9 2. 96.06.010.S10.510.310.317.917.917.517.8 28 .7 28 .7 28 .0 28 .051.851.851 .2 SI. 2 1.4001.610 2, 210 2. 510 2. 87S3.32S3,0303.6164.0604, 725 4.3905,3355,6506.60O6 .23 S7*7810,11011.36010,580 12. 240NOMINAL DIMENSIONAL ... —2I4XXS 0.5 52 7,770 9,050 2 1A 0.750 10, 720 12, 490 2 1A 0.875 12, 530 14, 6003Std 0 .21 6 2, 260 —3XS 0.300 3 ,20 0 —3XXS 0.600 6, 820 7,9404Std 0 .23 7 1, 920 —4XS 0.337 2, 770 —4XXS 0.674...

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

... 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 14- 4055iGrade ... Typically, high-speed compressors run at a speed of 900 toJ 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 ... ratio in therange of 5 to 20 .* Reviewed for the 1999 edition by John H. Galey of Paragon Engineering Services, Inc, 25 3 25 2 Design of GAS-HANDLING Systems and Facilities Table...

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 881903809 143 28 6MostLikelyCentrifugalHigh SpeedHigh ... theincreased efficiency of compression. 28 2 Design of GAS-HANDLING Systems and Facilities Figure 10-15. Graphic illustration of a "stonewall/' or a choked flow condition.«If ... service. 26 2 Design of GAS-HANDLING Systems and Facilities Figure 10-5. Integral engine compressor. (Courtesy of Cooper Industries EnergyServices Group .) sidered low-speed units....

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

... 7,50016,30018,80017,70017,70017,40016,30017,50016,30017,50011 ,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 ... 1.1Class1503004006009001500 25 00 ~20 °FtolOO° 28 5740990 148 0 22 2037056170MAWP, psigF 100°Fto200°F 25 06759001350 20 2533755 625 Mechanical Design of Pressure Vessels 335Figure 12- 2. Internal ... 1 .25 X, 1.75X The wave length may be calculated from: 314 Design of GAS-HANDLING Systems and Facilities the least expensive and are used in small air compressors. Forced-feed systems ...

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 ... Examined Examined31.00 0.85 0.700.90 0.80 0.65— 0.60— — 0.55on page)3 52 Design of GAS-HANDLING Systems and Facilities (b)Head:( 12 5) ( 12 0) |- == , _ ,— = y 505 in( 2) ... head(a) Skirt:I-°^d + 2 j_j — " r jL 12 _ (0 .2 5) ( 12 0) | 12 = 4.50 ftW = (1 1) ( 12 0) (0. 5) (4. 5) = 2, 970 Ib(b )^ ELn!aiy: Shdl 12 <870Head 4,163Head 4,163Skirt...

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

... back-pressure of 500 psig the pressure rating of ANSI Class 150 (maximum pres-sure of 28 5 psig at 100°F) is inadequate.3 82 Design of GAS-HANDLING Systems and Facilities 2, ... plus ?2 364 Design of GAS-HANDLING Systems and Facilities Figure 13-5. Operation of balanced-bellows safety-relief valve. (Reprinted withpermission from API 520 .) Balanced bellows ... 13-3Standard Orifice Areas and DesignationsOrificeDEFGHJ K LMNPQRTAreain. 2 0.1100.1960.3070.5030.7851 .28 71.838 2. 8533.604.346.3811.0516.0 26 .0380 Design of GAS-HANDLING ...

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

... Figure 14 -2. Hazard free for production facility. (Source: API RP14 .) Figure 14* 4, Continued.410 Design of GAS-HANDLING Systems and Facilities (text continued from page 40 6) nal ... of injury that may be associated with building failure.Figure 14- 1. Hazard tree for injury suffered white walking in a hallway.4 02 Design of GAS-HANDLING Systems and Facilities Table ... the design of the logicnecessary to carry out the functions that are to be performed when a sig-(text continued on page 41 0) 388 Design of GAS-HANDLING Systems and Facilities nating...

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

... (Courtesy of Jenkins Bros .) 430 Design of GAS-HANDLING Systems and Facilities Table 15 -2 (Continued)Example Specifications of Pipe, Valves, and FittingsCouplings1 -in. and smaller ... HighTemperature 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 ... Ib ANSI CS RF Etc.flanged, standard trim,hand wheel or lever operated418 Design of GAS-HANDLING Systems and Facilities (text continued from page 41 0) HAZARDS ANALYSISA hazards...

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