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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

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

... CH4 <-» CO 2 + 2H 2 O And finally, the 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 ... there*Reviewed for the 1999 edition by Dinesh P. Patel of Paragon Engineering Services, Inc.4934 92 Design of GAS-HANDLING Systems and Facilities Based on the results of the ... powercapacitors.490 Design of GAS-HANDLING Systems and Facilities water and CO 2 . A recent catalytic converter design called three-wayconverters also controls NOX using a reduction process....
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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

... I, and computing:1 42 Design of GAS-HANDLING Systems and Facilities is controlled by ( 1) perforations in the tray deck (sieve trays), ( 2) bubblecaps (bubble cap trays), or ( 3) ... ele-ments of structured packing are placed. Beds of structured packing typi-cally have lower pressure drops than beds of random packing of compa-rable mass transfer efficiency. Structured ... is introducedquickly the heat of reaction may ignite the bed.140 Design of GAS-HANDLING Systems and Facilities Table 6-1Vapor Pressure and Relative Volatility of Various...
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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

... 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 ... 140°FReid Vapor Pressure3430 26 22 181410 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 ... 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...
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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 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....
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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

... 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...
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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

... 7,50016,30018,80017,70017,70017,40016,30017,50016,30017,500 11 ,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 57409901480 22 2037056170MAWP, psigF 100°Fto200°F 25 06759001350 20 2533755 625 Mechanical Design of Pressure Vessels 335Figure 12- 2. Internal ... cl.lGrade21,cl.lGrade 5, cl.lGrade 2, cl .2 Grade 1 .2, cl .2 Grade 11, 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 304Grade 304LGrade...
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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

... (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 ... 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 ... 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) ...
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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

... 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, ... 13-3Standard Orifice Areas and DesignationsOrificeDEFGHJ K LMNPQRTAreain. 2 0 .110 0.1960.3070.5030.7851 .28 71.838 2. 8533.604.346.38 11. 0516.0 26 .0380 Design of GAS-HANDLING ... 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...
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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

... 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 ... prior to a shut-in, and provide informa-398 Design of GAS-HANDLING Systems and Facilities evaluated for the third failure mode of this check valve. Check valves areeasy. A ... 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...
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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

... (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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