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

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

... contains the rotating parts and on which the cylinders and crossheads are mounted. (Courtesy of Dresser-Rand Company .) 31 0 Design of GAS-HANDLING Systems and Facilities Compressor ... Design of GAS-HANDLING Systems and Facilities tlon and discharge valves so that the valves can be removed and rein- stalled. These clearances are c...
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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

... °R 547.87 22 7 .3 6 72. 6 34 3 .37 550.09 666.01 734 .98 765.65 829 ,10 845.70 9 13. 70 11 12. 0 37 4.6 Sum (A, x Cj) Sum (Aj) D Critical psia 1071.0 4 93. 0 1 036 .0 667.8 707.0 616 .3 529 . 1 550.7 490.4 488.6 436 .9 30 4 680.5 Sum ... Vaporization Compound Methane Ethane Propane n-Butane Isobutane n-Pentane Isopentane Hexane Heptane Octane Nonane Decane Heat of Vaporizat...
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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- XH 8-y'XXH 8 -2& quot;XH 8 -2& quot;XXH TO-r'XH io-r'xxM 6 -3& quot;XH 6 -3& quot;XXH 2- 2"XH 12- r'XXH WXH 8 .3- XXH 14-r'XH 14-T'XXH 1O -3& quot;XH 1O -3& quot;XXH 1« -2& quot;XH ie -2- xxn 10 -3& quot;XM 10 -3& quot;XXH 34 40 734 0 34 40 734 0 34 40 734 0 32 0 0 6 820 34 40 734 0 32 0 0 6 820 34 40 734 0 32 0 0 68*0...
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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

... Evaporated at 140°F Reid Vapor Pressure 34 30 26 22 18 14 10 25 ! Grade 34 -25 Grade 30 -25 Grade 26 -25 Grade 22 -25 Grade 18 -25 Grade 14 -25 40 i Grade 34 -40 Grade 30 -40 Grade 26 -40 Grade 22 -40 Grade ... >» Gas Component Ethane Propane Butane Pentane Net Heating Value Btu/SCF 1618 23 16 30 10 37 08 SCF/Gallon 37 .5 36 .4 31 .8 27 .7 52. 00/MMBtu...
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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

... Gas Vapor Recovery Flow Rate MMscfd 100 10 5 20 100 2 2 4 0.1 1.0 2. 0 R 2. 0 2. 0 2. 7 2, 7 2. 7 2. 0 2. 0 2. 0 4.0 3. 0 3. 0 n 1 ! 3 3 .3 1 2 2 1 2 2 Approx. bhp 4,400 440 980 3, 920 19,6 02 88 190 38 0 9 1 43 28 6 Most Likely Centrifugal High Speed High ... the increased efficiency of compression. 28 2 Design of GAS-HANDLING Systems and Facili...
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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

... 6,900 18 ,30 0 18 ,30 0 20 ,000 20 ,000 20 ,000 20 ,000 23 ,30 0 21 ,700 25 ,000 25 ,000 25 ,000 25 .000 21 .700 23 ,30 0 21 ,700 23 ,30 0 20 ,000 16,700 20 ,000 16,700 Wall thickness 2: 1 ellipsoidal heads Wall thickness—hemispherical ... 1.1 Class 150 30 0 400 600 900 1500 25 00 ~20 °FtolOO° 28 5 740 990 1480 22 20 37 05 6170 MAWP, psig F 100°Fto200°F 25 0 67...
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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) = 4,1 631 b (c) Cone: _ Pd ~ 2 ... Examined Examined 3 1.00 0.85 0.70 0.90 0.80 0.65 — 0.60 — — 0.55 on page) 3 52 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 6 docx

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

... Ratio of Specific Heat, C P /C V , or k kCkCkCkC 1.01 31 7 a 1 .31 34 8 1.61 37 3 1.91 39 5 1. 02 31 8 1. 32 34 9 1. 62 37 4 1. 92 39 5 1. 03 31 9 1 .33 35 0 1. 63 37 5 1. 93 39 6 1.04 32 0 ... 1 .34 35 1 J.64 37 6 1.94 39 7 1.05 32 1 1 .35 3 52 1.65 37 6 1.95 39 7 1.06 32 2 1 .36 35 3 1.66 37 7 1.96 39 8 1.07 3...
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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

... prior to a shut-in, and provide informa- 39 8 Design of GAS-HANDLING Systems and Facilities evaluated for the third failure mode of this check valve. Check valves are easy. A ... the design of the logic necessary to carry out the functions that are to be performed when a sig- (text continued on page 41 0) 38 8 Design of GAS-HANDLING Sy...
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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 Fittings Couplings 1 -in. and smaller ... High Temperature Safety Low None (table continued on next page) 422 Design of GAS-HANDLING Systems and Facilities form their work safely and to be...
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