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 ,40 0 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 40 0 600 900 1500 25 00 ~20...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 4 pdf
... Passes 1 12 16 32 52 81 97 140 188 24 1 29 6 356 41 4 4 82 570 658 7 42 846 9 52 10 62 123 2 1 42 4 1636 1 845 2 6 16 28 52 78 94 1 32 178 22 4 28 0 344 40 6 47 6 5 62 640 7 32 831 931 1 045 122 2 141 5 16 34 18 32 2080 | 20 6f 4 4 12 24 52 76 88 1 24 1 72 216 27 6 3 32 3 92 46 8 548 640 7 32 820 928 1 026 121 8 1386 16 02...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 9 pdf
... gases. 1 92 Design of GAS-HANDLING Systems and Facilities ci H in. _ft_ 18 1.9 .2 20 15,5 22 12. 8 24 10.8 30 6.9 36 4. 8 An acceptable choice is a 30-in. OD vessel. The wall thickness can ... point of triethyl- ene glycol ( 546 °F) and water (21 2°F), the still column can be relatively short (10 to 12 ft of packing). The glycol liquid...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 10 pdf
... bed and water displaces the previously adsorbed gases until 21 4 Design of GAS-HANDLING Systems and Facilities Figure 8- 14. Structured (matrix) packing, (from Koch Industries .) Contactor ... 25 to 50% of the heat required to vaporize the water in the glycol) and losses to atmosphere. 21 2 Design of GAS-HANDLING Systems and Facilitie...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 1 docx
... Evaporated at 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 ... (H- 15 1) Silica Gel Molecular Sieves (4A) Bulk Density (Jb/fc 3) 51 49 50 52 45 45 Specific Heat (Btu/ib/*F) 0 . 24 0 .25 0 . 24 0 ....
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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 44 0 980 3, 920 19,6 02 88 190 380 9 143 28 6 Most Likely Centrifugal High Speed High ... is reached at the exit of a compressor wheel. When this point is reached, flow through the compre...
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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 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 ... 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) (0....
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 6 docx
... 380 2. 00 40 0 1.11 328 1 .41 357 1.71 381 — 1. 12 329 1. 42 358 1. 72 3 82 — 1.13 330 1 .43 359 1.73 3 82 — 1. 14 331 1 .44 360 1. 74 383 1.15 3 32 1 .45 360 1.75 3 84 1.16 333 1 .46 ... 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 34...
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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 RP 14 .) Figure 14* 4, Continued. 41 0 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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