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

ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 14 pot

... throttle valves, 27 8, 28 2 designing, 23 2 -24 0 pressure, compressors, 27 6, 27 8 drying cycle time, 23 3 scrubbers, 25 6, 28 0, 28 5 gas velocities, 23 3 shutdown bypass valve, 28 5 introduction, ... 175-176 SO 2 . See Sulfur dioxide. Stripping gas Solid bed process glycol process, 20 3 -20 4 bed height and diameter, 23 4 glycol reboilers, 21 1 co...

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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 rotating parts and on which the cylinders and crossheads are mounted. (Courtesy of Dresser-Rand Company .) 310 Design of GAS-HANDLING Systems...

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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

... = 20 ,000 5 = 23 ,300 in. in. psig psig 1XS 0.179 5 ,27 0 2Std 0.154 2, 380 — 2XS 0 .21 8 3,440 — 2XXS 0.436 7,340 8,560 2J4Std 0 .20 3 2, 600 — 2! 4XS 0 .27 6 3,610 — 2I4XXS 0.5 52 7,770 ... 2O-0'' 8 -2- XH 8-y'XXH 8 -2& quot;XH 8 -2& quot;XXH TO-r'XH io-r'xxM 6-3"XH 6-3"XXH 2- 2"XH 12- r'XXH WXH 8.3-XXH 14- r'XH...

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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

... 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 18-40 Grade 14- 40 55 i Grade ... Typically, high-speed compressors run at a speed of 900 to J 20 0 rpm and slow-speed units at speeds of 20 0 to 600 rpm. 24 0 Design of G...

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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 88 190 380 9 143 28 6 Most Likely Centrifugal High Speed High ... the increased efficiency of compression. 28 2 Design of GAS-HANDLING Systems and Facilities Figure...

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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 18,100 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 ... 1.1 Class 150 300 400 600 900 1500 25 00 ~20 °Ft...

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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 ... 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 Facil...

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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, ... plus ?2 364 Design of GAS-HANDLING Systems and Facilities Figure 13-5. Operation of balanced-bellows safety-relief valve. (Reprinted with permission from...

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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 GA...

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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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