ARNOLD, K (1999) Design of Gas-Handling Systems and Facilities (2nd ed ) Episode 1 Part 3 pps

... 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...

Ngày tải lên: 06/08/2014, 02:20

... glycol MW 32 .04 46,07 60 .10 62.07 76 .10 10 6 .10 K 2 ,33 5 2 ,33 5 2 ,33 5 2,200 3, 590 4 ,37 0 where AT = depression of hydrate formation temperature, °F MW = molecular weight of inhibitor (Table 4- 2) K ... (Figure 3 -1 0): Calculate number of tubes: 86 Design of GAS-HANDLING Systems and Facilities [text continued from page 8 3) Generall...

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... 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 Facilities Table 7 -1 Physiological Effects of H 2 S ... Air Percent Parts per Grains by Million per Volume by Volume lOOscf* 0.00 0 13 0 . 13 0.008 0,0 01 10 0. 63 0,005 50 3 .15 0. 01 10 0 6 .30 0.0...

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... Stress Values 3 31 , Determining Wall Thickness 3 31 , Corrosion Allowance 33 3 viii 6 Design of GAS-HANDLING Systems and Facilities Chapter 9 discusses the refrigeration and cryogenic ... 11 3 Fire-Tube Size, 11 5 Coil Sizing, 11 6 Choose Temperatures 11 6, Choose Coil Diameter 11 7, Choose Wall Thickness 11 8, Coil Lengths 11 9 Standar...

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... .746 10 .044 8.628 7.444 6.449 5.609 4.896 4.289 3. 770 3. 324 2. 939 2.606 2. 31 7 2.06 51 Sot Vapor v s 23 .15 19 .38 2 16 .32 3 13 .8 21 11. 7 63 10 .0 61 8.645 7.4 61 6.466 5.626 4, 914 4 .30 7 3. 788 3. 342 2.957 2.625 2 .33 5 2.0 836 Enthalpy Sat. Liquid hf 18 8 . 13 19 8. 23 208 .34 216 .48 228.64 238 .84 249.06 259. 31 269.59 279.92 290.28 30 0.68 31 1 ....

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... Passes 1 7 8 19 29 42 52 69 92 12 1 14 7 17 4 19 6 237 280 31 3 35 7 416 4 61 511 596 687 790 896 10 08 12 41 2 4 6 14 26 38 48 68 84 11 0 13 8 16 5 19 6 226 269 31 3 34 6 4 01 4 53 4 93 579 6 73 4 4 4 12 20 34 44 60 78 10 4 12 8 15 6 18 4 224 256 294 33 2 38 6 432 478 570 662 782 ... Passes 1 9 12 22 38 56 69 97 12 9 16 4 202 234 272 3...

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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& quot;XH 6 -3& quot;XXH »2-2"XH 12 -r'XXH WXH 8 .3- XXH 14 -r'XH 14 -T'XXH 1O -3& quot;XH 1O -3& quot;XXH 1 -2"XH ie-2-xxn 10 -3& quot;XM 10 -3& quot;XXH 34 40 734 0 34 40 734 0 34 40 734 0 32 00 6820 34 40 734 0 32 00 6820 34 40 734 0 32 00 68*0 34 40 73...

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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 Facilit...

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... 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 6.9 36 4.8 An acceptable choice is a 30 -in. OD vessel. The wall thickness can ... weight of 26 that is in equilibrium with a 3% brine at a pressure of 3, 000 psia and a temperature of 15 0°R From Figure 8 -1 at a t...

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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 30 0 400 500 600 700 800 900 10 00 11 00 12 00 13 00 14 00 15 00 Pump Gas Consumption sc ... bed and water displaces the previously adsorbed gases until 214 Design of GAS-HANDLING Systems and Facilities Figure 8 -...

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