... 388 — 1 .22 339 1. 52 366 1. 82 389 — — 1 .23 340 1.53 367 1.83 389 — —• 1 .24 341 1.54 368 1.84 390 — 1 .25 3 42 1.55 369 1.85 391 — — 1 . 26 343 1. 56 369 1. 86 391 — 1 .27 344 ... 13-3 Standard Orifice Areas and Designations Orifice D E F G H J K L M N P Q R T Area in. 2 0.110 0.1 96 0.307 0.503 0.785 1 .28 7 1.838 2. 853 3 .60 4.34 6....
Ngày tải lên: 06/08/2014, 02:20
... 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 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 60 0 rpm. 24 0...
Ngày tải lên: 06/08/2014, 02:20
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 ... 14.5. {figure continued on pugf) 3 96 Design of GAS-HANDLING Systems and Facilities detectors and manual shutdown stations to provide adequate warning...
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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 ... ofXomox Corp .) 4 26 Design of GAS-HANDLING Systems and Facilities 5. Welding certification and inspection requirements. 6, Design details (if...
Ngày tải lên: 06/08/2014, 02:20
ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 13 docx
... positive-displacement, 25 5 bearings, 29 6 -29 8 reciprocating, 3, 25 5 - 26 4 ,28 6- 3 26 booster, 25 4, 27 6, 28 6 high-speed, 25 8 -25 9 capacity control devices, 3 02 low-speed, 25 9 - 26 4 casinghead gas, 25 4 process ... considerations, 27 6 -28 0 centrifugal, 3, 26 7 -27 0, 28 6 rod, 29 4, 310-311 centr i fugal proces s considerations,...
Ngày tải lên: 06/08/2014, 02:20
ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 6 potx
... 9,050 2 1 A 0.750 10, 720 12, 490 2 1 A 0.875 12, 530 14 ,60 0 3Std 0 .21 6 2, 260 — 3XS 0.300 3 ,20 0 — 3XXS 0 .60 0 6, 820 7,940 4Std 0 .23 7 1, 920 — 4XS 0.337 2, 770 — 4XXS 0 .67 4 5, 860 6, 830 6Std ... 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...
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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 ... service. 26 2 Design of GAS-HANDLING Systems and Facilities Figure 10-5. Integral engine compr...
Ngày tải lên: 06/08/2014, 02:20
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 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 60 0 900 1500...
Ngày tải lên: 06/08/2014, 02:20
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, 163 1b (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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