AS 4254 1995 amdt 2 1999 ductwork for air handling systems i

... 26 27 18 20 22 24 16 18 20 22 12 13 14 15 16 17 18 19 20 10 11 12 13 14 15 16 17 18 20 10 11 12 13 14 15 16 028 022 018 016 049 035 , 028 022 065 09 035 028 10 9 095 083 0 72 065 058 09 0 42 035 ,13 4 ... 0 .11 15 0 . 12 95 2. 0393 1. 99 02 1. 9 428 1. 89 72 1. 85 31 20 4 98 20 4 ,67 2. 0360 20 8 07 9 826 60 70 80 90 10 0 11 09.5 11 13.7...

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... 36.4 31. 8 27 .7 0. 12 1 3 0 .16 86 0 .19 15 0 .20 54 0 .1 820 0 .25 29 0 .28 72 0.30 81 25 2 Design of GAS-HANDLING Systems and Facilities Table 9-4 Typical Fractionator-Absorber/Slripper Design Number of Trays ... Number 20 0 -11 00 24 -30 20 -50 450-600 20 -30 20 -50 17 5-300 85 -16 0 24 -30 2- 60 20 -50 16 -60 550-650 350-500 20 0-300 70 -10 0 14 -30 10 -...

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... Selection Alternate 100 2. 0 4,400 Centrifugal Integral (onshore only) 10 20 2. 0 2. 7 2, 7 ! 3 440 980 3, 920 High Speed High Speed Centrifugal 100 2 2.7 2. 0 2. 0 2. 0 2 19,6 02 88 190 380 Centrifugal ... consideration of the advantages and disadvantages listed earlier In addition, local foundation conditions, type of drivers available, cost of fuel, availability of s...

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... acting cylinders (Courtesy of Dresser-Rand.) 29 0 Design of GAS-HANDLING Systems and Facilities Figure 11-5 Typical double-acting compressor cylinder (Courtesy of Dresser-Rand Company.} ing cylinders ... regularly (Courtesy of Dresser-Rand Company.} Figure 11- 12 Journal bearings allow axial and circumferential oil flow abng the bearing 29 8 Design of GAS-HANDLING...

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... 11 ,20 0 — 12, 300 10 ,20 0 18,300 20 ,000 21 700 23 ,300 15,000 16,700 18,100 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 ... clearance of 17. 92% , a rod load limit of 25 ,000 Ib, and rod diameter of 1.75 in Assume k = 1 .26 , Zs = 0.88, and Zd = 0.85  322 Design...

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... = 0 .50 7 + 0 . 25 0 = 0. 757 in 3 52 Design of GAS-HANDLING Systems and Facilities (b)Head: |- == ( 1 25 ) ( 120 ) , _ ,— = y 50 5 in (2) (17 ,50 0) (0. 85) - (0 .2) ( 1 25 ) Required thickness = 0 .50 5 + 0 . 25 0 ... (0 .23 ) (0 . 25 ) ( 120 )2 sin 30 lb (b) Shell: Height of cone = tan 30 = 8.7 ft Length of shell = 12 + 8.7 = 20 .7 ft Weight of shell = (11)( 120 )(0...

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... 1 .24 1 .25 1 . 26 1 .27 1 .28 1 .29 1.30 C k a 317 318 319 320 321 322 323 325 3 26 327 328 329 330 331 3 32 333 334 335 3 36 337 338 339 340 341 3 42 343 344 345 3 46 347 1.31 1. 32 1.33 1.34 1.35 1. 36 1.37 ... 1.41 1. 42 14 14 1.45 14 14 14 14 1.50 1.51 1. 52 1.53 1.54 1.55 1. 56 1.57 1.58 1.59 16 C 348 349 350 351 3 52 353 353 354 355 3 56 357 358 359 360 360 361 3 62 363 36...

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... cases only one level of protection would be required, given the degree of reliability of shutdown systems and the consequences 400 Design of GAS-HANDLING Systems and Facilities of failure However, ... sense the presence of a fuel in a confined space, and fire 396 Design of GAS-HANDLING Systems and Facilities detectors and manual shutdown stations to p...

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... of a system These valves are the most common general-purpose on/off valves in production facilities (text continued from page 430) 4 28 Design of GAS-HANDLING Systems and Facilities Table 15 -2 ... Design of GAS-HANDLING Systems and Facilities Table 15 -2 (Continued) Example Specifications of Pipe, Valves, and Fittings Couplings -in and smaller J4-in Plugs...

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... 2} A I VA VA 2 21A 21 A 1 VA VA 2 21A 21 A VA VA 2} A 21 A 21 A VA 2 21A 21 A VA VA 2 21A 3 VA VA 21 A 21 A 3 VA VA 21 A 21 A 3 VA VA 2 1A 2{ A 3 VA VA 2} A 21 A 3M VA VA 2 1A 2{ A 31A VA VA 21 A 21 A 3yi VA ... 1 091 - 120 0 1061- 120 0 1031-1170 1001-1130 98 1-1 120 97 1-1100 97 1-1100 96 1-1 090 95 1-1080 90 1-1010 _ „ _ _ _ _ _ _ _ 1171- 120 0 1131- 120...

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... Figure 16 -10 This schematic illustrates how waste heat can be recovered and used to heat process fluids 4 82 Design of GAS-HANDLING Systems and Facilities Figure 16*11 The combined cycle of waste ... They may trap small leaks of sour gas and keep them from being dispersed in the atmosphere Figure 15 -26 Flange protector types 464 Design of GAS-HANDLING Systems...

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... reduction and the other one for oxidation The oxidation process with CO takes place as; 2CO + O2

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... 100 J*5 8 42 5 72 536 500 446 419 3 92 356 329 320 27 5 24 8 21 2 J85 Identification Number Tl T2 T2A T2B T2C T2D T3 T3A T3B T3C T4 T4A T5 T6 Electrical Systems 523 Purged Enclosures Purged enclosures ... salt air and other contaminants Table 17 -2 Temperature Ratings of Explosion-Proof Enclosures Maximum Temperature °C °F 450 300 28 0 26 0 23 0 21 5 20 0 180 165 160 135 120...

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... foundation design, 319 frames, 28 7 -28 9 gas lift, 25 4, 26 2, 27 6, 27 8 general, 25 3 -28 5 heads, 461 Helical-Lobe, 26 6 -26 7 industry specifications, 320 - 321 integral units, 25 8, 25 9, 28 8 kinetic, 25 5 lubrication ... piston wear bands, 29 6 pistons and piston rods, 29 6 positive-displacement, 25 5 reciprocating, 3, 25 5 -26 4 ,28 6- 326 high-speed, 25 8 -25 9 lo...

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... height and diameter, 23 4 costs, 22 9 description, 22 9 -23 2 designing, 23 2 -24 0 drying cycle time, 23 3 gas velocities, 23 3 introduction, 157 iron sponge, 157-159 pressure drop, 23 4 -23 5 pressures, 23 2 -23 3 ... relief valves and, 360 transformers, 541 wiring, 5 32 Oil 130, 25 4, 26 2 pollution, 389-3 92, 395 production facilities, 65, 522 spills, 389-393, 395 treater,...

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