ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 7 ppsx

... Anti-Agglomerators, 10 7 CHAPTER S LTX Units and Line Heaters 10 9 LTX Units, 11 0 Line Heaters, 11 2 Heat Duty, 11 3 Fire-Tube Size, 11 5 Coil Sizing, 11 6 Choose Temperatures 11 6, Choose ... modern and common practices. We have either personally been involved in the design and troubleshooting of facilities throughout xiii 10 Design of...

Ngày tải lên: 06/08/2014, 02:20

... / -X4 % % /i /'4 ;/4 ã% /'i 3/; | s I i 1 1 1 1 B.W.G. Gauge 22 24 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 8 10 11 12 13 14 15 16 Thickness In. . 028 . 022 . 018 . 016 .049 .035 , 028 . 022 .065 .049 .035 . 028 .10 9 .095 .083 .0 72 .065 .058 .049 .0 42 .035 ,13 4 . 12 0 .10 9...

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... Vaporization Compound Methane Ethane Propane n-Butane Isobutane n-Pentane Isopentane Hexane Heptane Octane Nonane Decane Heat of Vaporization, 1 4.696 psia at Boiling Point, Btu/lb 219 .22 210 . 41 1 83. 05 16 5.65 15 7. 53 15 3. 59 14 7 . 13 14 3. 95 13 6. 01 129. 53 12 3. 76 11 8.68 ... 1 29 B Molecular Weight 44. 010 28. 0 13 34 .076 16 .0 43 30.070 44.097...

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... Passes 1 12 21 37 61 97 11 3 15 6 208 256 3 14 379 44 8 522 603 688 788 897 10 09 11 18 12 98 15 00 17 14 2 10 18 32 54 90 10 8 14 6 1% 244 299 363 43 2 5 04 583 667 770 873 983 10 92 12 69 14 70 lh 81 4 8 16 28 48 84 10 4 13 6 18 4 236 2 94 352 41 6 48 6 568 6 54 756 850 958 10 66 12 50 14 40 16 50 1Qô ... Passes 1 12 16 32 52...

Ngày tải lên: 06/08/2014, 02:20

... linearly, y n , Mole Fraction in Gas 0. 014 4 0.0403 0.000 019 0. 855 5 0. 057 4 0. 017 9 0.00 41 0.00 41 0.0063 1. 0000 Y/K =1. 0at74 0 ] At 70 Kn Infinity Infinity 0.3 0. 95 0.72 0. 25 0 . 15 0.72 Infinity F °F y n /i< n 0.00 0.00 0.00 0.90 0.08 0.07 0.03 0.00 0.00 J.08 At ... 2 -14 ) 10 0 Design of GAS-HANDLINCr Systems and facilities by Figure 4-6. The grap...

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... 2O-0'' 8-2-XH 8-y'XXH 8-2"XH 8-2"XXH TO-r'XH io-r'xxM 6- 3"XH 6- 3"XXH ằ2-2"XH 12 -r'XXH WXH 8.3-XXH 14 -r'XH 14 -T'XXH 1O-3"XH 1O-3"XXH 1 -2"XH ie-2-xxn 10 -3"XM 10 -3"XXH 3440 7340 3440 7340 3440 7340 3200 68 20 3440 7340 3200 68 20 3440 7340 3200 68 *0 3440 7340 3200 68 20 29-S 26. 5 42 ....

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... on 1% hydrogen sulfide = 629 .77 gr /10 0 scfat 14 .696 psia and 59°F, or 10 1,325 kPa and 75 °C. 15 6 Design of GAS-HANDLING Systems and Facilities (text continued from page 15 3) GAS ... threat- *Reviewed for the 19 99 edition by K. S. Chiou of Paragon Engineering Services, Inc. 15 1 15 2 Design of GAS-HANDLING Systems and Fa...

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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 17 6 Design of GAS-HANDLING Systems and Facilities Figure ... developed and patented by NL Treating Chemicals and is now a product of Exxon Energy Chem- 16 2 Design of GAS-HANDLING Systems and Facili...

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... rate Figure 8 -9. Equilibrium water dew points at different temperatures for gases. 19 2 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 ... a pressure of 3,000 psia and a temperature of 15 0°R From Figure 8 -1 at a temperature of 15 0°F and pressure of 3,000 psia there is...

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... 222 Design of GAS-HANDLING Systems and Facilities Table 8-3 Gas Consumption by Glycol Powered Pump Contactor Operating Pressure psig 300 400 500 600 700 800 900 10 00 11 00 12 00 13 00 14 00 15 00 Pump Gas Consumption sc ... (Volume 1, Chapter 4). This is: 218 Design of GAS-HANDLING Systems and Facilities Table 8 -1 Example Contactor Sizes fo...

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... propylene. 20 8* -37* 2, 5 — 0.05ml pass (1) No. 1 12 3 pass _. Test Methods ASTMD -2 16 3- 82 ASTMD- 12 6 7-84 ASTMD- 18 37- 81 ASTMD -2 16 3- 82 ASTM D -2 16 3- 82 ASTMD -2 15 8-80 ASTM D - 21 58-80 ASTMD- 18 38-84 ASTM ... at 14 0°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...

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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 ... This horsepower loss and additional equipment cost may be more than offset by the increased efficiency of compression...

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... contains the rotating parts and on which the cylinders and crossheads are mounted. (Courtesy of Dresser-Rand Company.) 31 0 Design of GAS-HANDLING Systems and Facilities Compressor ... (bottom). 29 4 Design of GAS-HANDLING Systems and Facilities Figure 11-8. Valve-in-piston double-acting compressor cylinder, (Courtesy of Dresser-Rand...

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... to 406 Design of GAS-HANDLING Systems and Facilities tion about the initial cause of a shut-in. They are a vital party of any large shutdown system design. On smaller systems, ... propagate outside the fire tube and out into the open. The flame would then become a source of 400 Design of GAS-HANDLING Systems and Facilities of fai...

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... reduction and the other one for oxidation. The oxidation process with CO takes place as; 2CO + O 2 <-» 2CO 2 The oxidation of UHC is: 2O 2 + CH 4 <-» CO 2 + 2H 2 O And finally, ... reduction of NO X with CO results in N 2 and CO 2 : NO 2 + CO <-» NO + CO 2 2NO + 2CO <-» N 2 + 2CO 2 Catalytic reactions occur when the t...

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