Cable supported bridges, concept and design, 2nd ed (Một cuốn sách nổi tiếng thời đại đầu thế kỷ 21 về thiết kế và thi công cầu dây văng.)
Cable supported bridges, concept and design, 2nd ed (Một cuốn sách nổi tiếng thời đại đầu thế kỷ 21 về thiết kế và thi công cầu dây văng.)
Ngày tải lên: 25/05/2016, 21:26
ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 1 pps
... 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 Coil Diameter 11 7, Choose ... Operations Design of Gas-Handing Systems and Facilities Ken Arnold Maurice Stewart SECOND EDITION Surface Production Operations VOLUME Design of Gas...
Ngày tải lên: 06/08/2014, 02:20
ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 2 doc
... 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...
Ngày tải lên: 06/08/2014, 02:20
ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 3 pps
... 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 40 Design of GAS-HANDLING Systems and Facilities Natural Gas Sensible Heat Duty ... 672.6 34 3 .37 16 .0 43 667.8 707.0 30 .070 550.09 44.097 616 .3 666. 01 734 .98 529 58 .12 4 58 .12 4 550.7 765.65 490.4 72 .15 1 829 ,10 488....
Ngày tải lên: 06/08/2014, 02:20
ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 4 pdf
... 649 648 782 780 768 9 04 8 94 8 74 10 34 10 27 10 12 11 78 11 55 11 50 13 22 13 07 12 84 16 54 16 40 16 32 "IP-Tube No of Passes 0 2 12 19 25 10 18 24 36 49 64 34 48 62 83 10 0 12 0 78 98 11 6 14 2 16 6 14 5 13 8 16 6 ... 8 91 860 35.00 10 03 10 31 976 37.00 11 52 11 34 10 90 39.00 12 73 12 59 12 22 14 85 14 61 4. 0 20 14 34 45.00 17 21...
Ngày tải lên: 06/08/2014, 02:20
ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 5 pps
... 60 .10 62.07 76 .10 10 6 .10 2,3 35 2,3 35 2,3 35 2,200 3 ,59 0 4,370 10 6 Design of GAS-HANDLING Systems and Facilities Water content (8,000 psig and 224°F)= 230 Ib/MMscf Water content (4,000 psig and 65 F) ... 0.3 0.000 019 0. 855 5 Methane 0. 95 Ethane 0. 057 4 0.72 0. 017 9 Propane 0. 25 Isobutane 0.00 41 0 . 15 0.72 0.00 41 n-Butane Infinity Pentane "1" 0.0063 1...
Ngày tải lên: 06/08/2014, 02:20
ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 6 potx
... T6" 1O-3"XXH 68 *0 31. 4 17 3 .1 28.0 7*78 3,000.000 60 "x20'0f 1 -2"XH 3440 7B.7 311 51. 8 10 ,11 0 2,000.000 eO^iWO" ie-2-xxn 7340 580 311 51. 8 11 . 360 7.000.000 60 "x20'0" 10 -3"XM 3200 66 .9 19 8 .1 51. 2 ... S3.B 70.9 10 .3 3. 61 6 1. 000.000 42" » 1, 000.000 42" « 1, 000.000 42"* 1, 000,000 42" x 4'«" 1. 500.000 48" * 7 '6" 1, 500.000 4'4" »2-2"XH 3440 93.4 16 6...
Ngày tải lên: 06/08/2014, 02:20
ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 7 ppsx
... 0.00 013 Parts per Million by Volume Grains per lOOscf* 0 .13 0.008 0 .18 Milligrams per m3* 0,0 01 10 0.63 14 . 41 0,005 50 3 .15 72 . 07 0. 01 100 6.30 14 4 .14 0.02 200 12 .59 288.06 0.05 500 31. 49 72 0.49 ... 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 -...
Ngày tải lên: 06/08/2014, 02:20
ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 8 doc
... process is best suited for wet gas streams of 0.5 -15 MMscfd containing less than 10 0 ppm H2S 1 78 Design of GAS-HANDLING Systems and Facilities The advantages of amine-aldehyde condensates are water ... in the rich 16 8 Design of GAS-HANDLING Systems and Facilities Figure 7-5 Hot carbonate system for gas sweetening stream The high temperature of the syst...
Ngày tải lên: 06/08/2014, 02:20
ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 9 pdf
... from 16 .8 in to 37.6 in is acceptable Choose a cycle time for one month: Assume Fe = Ib/Bu and rearrange: 19 1 19 2 Design of GAS-HANDLING Systems and Facilities ci in 18 20 22 24 30 36 H _ft_ 1. 9. 2 ... and 390 °F to minimize degradation of the glycol This effectively limits the lean glycol concentration to between 98 .5% and 98 .9% 210 Design of GAS-HAND...
Ngày tải lên: 06/08/2014, 02:20
ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 10 pdf
... 212 Design of GAS-HANDLING Systems and Facilities Figure 8 -12 Effect of stripping gas on glyco! concentration dehydrators are designed for approximately three gallons of glycol per pound of ... (Volume 1, Chapter 4) This is: Gas Dehydration 215 Figure 8 -15 Various types of packing (Courtesy: McGraw-Hill Book Company.} 216 Design of GAS-HANDLING Systems and Fa...
Ngày tải lên: 06/08/2014, 02:20
ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 1 docx
... 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 -...
Ngày tải lên: 06/08/2014, 02:20
ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 2 pps
... 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...
Ngày tải lên: 06/08/2014, 02:20