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

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

... propylene. 20 8* -37* 2, 5 — 0.05ml pass ( 1) No. 1 12 3 pass _. Test Methods ASTMD -2 16 3- 82 ASTMD- 12 6 7-84 ASTMD- 18 37- 81 ASTMD -2 16 3- 82 ASTM D -2 16 3- 82 ASTMD -2 15 8-80 ASTM D - 21 58-80 ASTMD- 18 38-84 ASTM ... Evaporated at 14 0°F Reid Vapor Pressure 34 30 26 22 18 14 10 25 ! Grade 34 -25 Grade 30 -25 Grade 26 -25 Grade 22 -25...
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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

... 399 1. 09 326 1. 39 355 1. 69 379 1. 99 400 1. 10 327 1. 40 356 1. 70 380 2. 00 400 1. 11 328 1. 41 357 1. 71 3 81 — 1. 12 329 1. 42 358 1. 72 3 82 — 1. 13 330 1. 43 359 1. 73 3 82 — 1. 14 ... Ratio of Specific Heat, C P /C V , or k kCkCkCkC 1. 01 317 a 1. 31 348 1. 61 373 1. 91 395 1. 02 318 1. 32 349 1. 62...
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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 ... 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...
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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 ... options. Figure 15 -1. Cutaway of ball valve. (Courtesy of Cameron Iron Works, Inc.] Figure 15 -2. Cutaway of plug valve. (Courtesy ofXomox Corp...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 13 docx

ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 13 docx

... sieves and, 16 0 -16 1 diameters, 11 7 -11 8 natural gas impurities, 4 length, 11 9- 12 0 permeable membranes and, 17 8 -17 9 sizing, 11 6- 12 0 physical solvent processes, 16 9 temperatures, 11 6 -11 7 pseudo ... process, 24 7 Bums, 393 Chokes, 2, 92- 93 ,11 4,440,4 61, 4 62 Busway, gasketed, 533 Choking, 10 0 -10 3 Butane, 5, 94, 24 1, 24 6,...
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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 10 0 10 5 20 10 0 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 19 0 380 9 14 3 28 6 Most Likely Centrifugal High ... the increased efficiency of compression. 28 2 Design of GAS-HANDLING Systems and Facilities...
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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

... (Reprinted with permission from API, Std. 618 , 3rd Ed. , Feb. 19 86 .) 29 6 Design of GAS-HANDLING Systems and Facilities Figure 11 -10 . The crosshead converts the rotating motion of ... double-act- Figure 11 -4. Single acting cylinders. (Courtesy of Dresser-Rand .) 304 Design of GAS-HANDLING Systems and Facilities Figure 11...
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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

... 7,500 16 ,300 18 ,800 17 ,700 17 ,700 17 ,400 16 ,300 17 ,500 16 ,300 17 ,500 11 ,20 0 — 12 , 300 10 ,20 0 18 ,300 20 ,000 21 700 23 ,300 15 ,000 16 ,700 18 ,10 0 1 6,900 18 ,300 18 ,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 ,000 16 ,700 20 ,000 16 ,700 Wall ... Vili Di...
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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

... in ( 2) (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 ,16 31b (c) Cone: _ ... head (a) Skirt: I-°^d + 2 j_j — " r jL 12 _ (0 .2 5) ( 12 0) | 12 = 4.50 ft W = (1 1) ( 12 0)...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 9 ppt

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

... 16 0- 520 11 4 7 31- 1040 6 41- 940 711 -960 6 61- 880 6 41- 870 6 21 -960 6 01- 810 6 01- 790 5 51- 740 16 0-740 16 0-750 16 0-740 16 0-700 16 0-690 16 0-690 16 0-690 16 0-680 16 0-680 5 21 -660 2 10 41- 12 0 0 9 41- 12 0 0 9 61- 12 0 0 8 81- 12 0 0 8 71- 1090 9 61- 116 0 811 -10 00 7 91- 970 7 41- 930 7 41- 900 7 51- 900 7 41- 900 7 01- 850 6 91- 840 6 91- 830 6 91- 830 6...
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