Solar energy engineering processes and systems 2nd ed 2014

The 8051 microcontroller and embedded systems using assembly and c 2nd ed

The 8051 microcontroller and embedded systems using assembly and c 2nd ed

... University, TAIWAN MICROCONTROLLERS AND EMBEDDED PROCESSORS Microcontrollers for Embedded Systems An embedded product uses a microprocessor (or microcontroller) to one task and one task only There is only ... The 8051 Microcontroller and Embedded Systems Using Assembly and C Second Edition Muhammad Ali Mazidi Janice Gillispie Mazidi Rolin D McKinlay CONTENTS I...

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

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....

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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 4 pdf

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

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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 5 pps

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

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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 6 potx

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

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

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

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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 8 doc

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

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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 9 pdf

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

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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 10 pdf

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

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

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

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

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...

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

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

... 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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