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...

Ngày tải lên: 06/08/2014, 02:20

... propylene. 20 8* -37* 2, 5 — 0.05ml pass ( 1) No. 1 123 pass _. Test Methods ASTMD -2 163- 82 ASTMD- 126 7 -84 ASTMD- 183 7 -81 ASTMD -2 163- 82 ASTM D -2 163- 82 ASTMD -2 1 58- 80 ASTM D -21 58- 80 ASTMD- 183 8 -84 ASTM ... 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...

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... 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 0.196 0.307 0.503 0. 785 1 . 28 7 1 .83 8 2. 85 3 3.60 4.34 6. 38 11.05 16.0 26 .0 380 Design of GAS-HANDLING ... 1.76 384 — 1.17 334 1.47 3 62 1.77 385 — 1. 18 335 1. 48 363 1. 78 386 — — 1.19 336 1.49 364 1.79 386 — 1 .20 337 1.50 365 1 .80 387 —...

Ngày tải lên: 06/08/2014, 02:20

... 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) 388 Design of GAS-HANDLING Systems and Facilities nating ... prior to a shut-in, and provide informa- 3 98 Design of GAS-HANDLING Systems and Facilities evaluated for the third failure mode of this check val...

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... frames, 28 6 positive-displacement, 25 5 bearings, 29 6 -29 8 reciprocating, 3, 25 5 -26 4 , 28 6- 326 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 ... 26 6 -26 7 glycol reflux, 20 2 industry specifications, 320 - 321 Conditions, future operating, 447 integral units, 25 8, 25 9,...

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... rate of deposition of 15 grains of H 2 S/min/ft 2 of bed cross-sectional area is also recommended to allow for the dissipation of 176 Design of GAS-HANDLING Systems and Facilities Figure ... is required and use the appropriate guide: Removal of H 2 S with no CO 2 present (Figure 7-1 1) Removal of H 2 S and CO 2 (Figure 7-1...

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... 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...

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... 28 8 Design of GAS-HANDLING Systems and Facilities facturers for a maximum continuous horsepower, speed (rpm), and rod load. The rated horsepower is determined by the ... 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...

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... 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 0...

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... (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 ... 0.6P) t ( 12 5) ( 12 0) t = • = 0. 585 in. (2 cos 3 0) (17,500 x 0 .85 - 0.6 x 12 5) Required thickne...

Ngày tải lên: 06/08/2014, 02:20