2 selection of design conditions
The Overseas Coastal Area Development Institute of Japan pptx
... 584 2. 1 2. 2 Principle of Design 584 Design of Mooring Facilities .585 2. 2.1 2. 2 .2 2 .2. 3 2. 2.4 2. 3 2. 4 2. 5 Length and Water Depth of Berths ... .538 Chapter 20 Aprons 540 20 .1 Principle of Design 540 20 .2 Type of Apron .540 20 .2. 1 20 .2. 2 20 .2. 3 20 .3 20 .4 20 .5 20 .6 20 .7 Width ... 13,000 16,000 20 ,000 23 ,000 Length overall (L) Molded breadth (B) 22 .3 m 25 .2 27.3 28 .2 28 .2 28 .2 1 42 m 167 185 1 92 1 92 200 Full load draft (d) 6.0 m 6.4 6.8 6.8 6.8 7 .2 Roll-on/roll-off vessels...
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Báo cáo hóa học: " Design of Uniformly Most Powerful Alphabets for HDF 2-Way Relaying Employing Non-Linear Frequency Modulations" ppt
... ≠ cA’, cB ≠ cB’ equal to 2, then (23 ) simplifies to + 2| α |2 − 2| α| scA − scA , scB − scB ≥ 2| α |2 (24 ) which further adjusts to ≥ |α| scA − scA , scB − scB (25 ) While (25 ) must hold for any |a| ... strategy in 2- WRC ⎤ 0 123 ⎢1 0⎥ ⎥ =⎢ 2 1⎦ 30 12 (3) (4) Hekrdla and Sykora EURASIP Journal on Wireless Communications and Networking 20 11, 20 11: 128 http://jwcn.eurasipjournals.com/content /20 11/1/ 128 ⎡ ... dependent on |a| as d2 (α) = 2| α |2 (10) Hekrdla and Sykora EURASIP Journal on Wireless Communications and Networking 20 11, 20 11: 128 http://jwcn.eurasipjournals.com/content /20 11/1/ 128 QPSK bitXOR:...
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Báo cáo hóa học: " Research Article Noniterative Design of 2-Channel FIR Orthogonal Filters" pptx
... z1−L H1 − z−1 = h2 + h2 L +2 h2 d + 2h1 hL Re zL−1 H1 (−z)H1 (z) − h2 L Re zC z B z = + 2h1 hL Re zL−1 C z2 (49) 2 − z 2 B z2 CONCLUSIONS We have presented a novel characterization of real paraunitary ... ) which is orthogonal, and unitary whenever h2 + h2 = 1/(1 + 02 + 02 + 02 ) = 1 L 3.1 DESIGN OF ORTHOGONAL FILTERS WITH DESIRABLE PROPERTIES Design of lowpass orthogonal filters Lowpass filters ... only if there exists a unique set of real numbers a1 , , aL /2 1 such that, for any k = 1, , L /2 − 1, k k h2k = − h2k+1 2 j a j , hL+1−2k = j =1 hL−2k +2 j a j (9) j =1 Or, in an equivalent...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 2 doc
... 1.1 92 1 .29 1 398 1.474 2. 433 2. 494 2. 573 2. 6 42 ,26 18 26 18 327 2 327 2 327 2 327 2 327 2 327 2 327 2 327 2 327 2 327 2 3 927 3 927 3 927 3 927 523 6 523 6 523 6 523 6 Ft2 Internal Surface Per Ft Length 23 61 24 35 ,23 30 ... 134 120 109 095 083 0 72 065 029 5 0333 0360 0373 0603 0731 0799 0860 1075 126 9 14 52 1548 1301 1486 655 1817 1 924 20 35 21 81 22 98 24 19 1 825 20 43 22 23 24 63 26 79 28 84 3019 3157 3339 36 32 3 526 420 8 ... 1130 .2 1134 .2 1138.1 1 42. 0 145.9 0 .23 11 0 .24 72 0 .26 30 0 .27 85 0 ,29 38 1.6174 1.5 822 1,5480 1.5147 1,4 824 1.8485 1. 829 3 1.8109 1.79 32 ! 77 62 160 170 180 190 20 0 21 0 21 2 14 123 14.696 0.01670 0.01672...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 1 docx
... Reid Vapor Pressure ! 34 30 26 22 18 14 10 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 18-40 Grade 14-40 ... 31.8 27 .7 0. 121 3 0.1686 0.1915 0 .20 54 0.1 820 0 .25 29 0 .28 72 0.3081 25 2 Design of GAS-HANDLING Systems and Facilities Table 9-4 Typical Fractionator-Absorber/Slripper Design Number of Trays Tower ... ASTMD- 1837-81 2. 5 — — 2, 5 ASTMD -2 163- 82 2.0 2. 0 — ASTM D -2 163- 82 — — — — ASTMD -2 158-80 ASTM D -21 58-80 ASTMD- 1838-84 ASTM D -27 84-80I GPA Propane Dryness Test (Cobalt Bromide) or D -27 13-81 —...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 2 pps
... 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 Screw High Speed High Speed High Speed Screw 4.0 3.0 3.0 2 143 28 6 Vane Screw High ... disadvantages listed earlier In addition, local foundation conditions, type of drivers available, cost of fuel, availability of spare 27 2 Design of GAS-HANDLING Systems and Facilities Figure 10-11 Curve ... Type Selections Service Flow Rate MMscfd Booster Gas Lift Flash Gas Vapor Recovery R n Approx bhp Most Likely Selection Alternate 100 2. 0 4,400 Centrifugal Integral (onshore only) 10 20 2. 0 2. 7 2, 7...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 3 potx
... constructed of a number of pairs of rings, as shown in Figure 11-14 The gas pressure is higher on one side of each ring This compresses the rings against the sealing area Each pair of rings consists of ... The effects of the seat area, the lift area, and the flow paths are automati- 3 02 Design of GAS-HANDLING Systems and Facilities Figyre 11-16 Cut-away view of poppet valve {Courtesy of 0resser-Roncf ... Single 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...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 4 pdf
... 11 ,20 0 — 12, 300 10 ,20 0 18,300 20 ,000 21 700 23 ,300 15,000 16,700 18,100 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 ... Table 12- 2 Summary ANSI Pressure Ratings Material Group 1.1 MAWP, psig Class ~20 °FtolOO°F 100°Fto200°F 150 300 400 600 900 1500 25 00 28 5 740 990 1480 22 20 3705 6170 25 0 675 900 1350 20 25 3375 5 625 ... cl.l Grade 2, cl .2 Grade 1 .2, cl .2 Grade 11, cl .2 Grade 22 , cl .2 Grade 21 , cl .2 Grade 5, cl .2 Grade A Grade B Grade D Grade E Grade 304 Grade 304L Grade 16 Grade316L Wall thickness 2: 1 ellipsoidal...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 5 pps
... ( 120 )2 sin 30 lb (b) Shell: Height of cone = tan 30 = 8.7 ft Length of shell = 12 + 8.7 = 20 .7 ft Weight of shell = (11)( 120 )(0.8 125 ) (20 .7) = 22 ,20 0 Ib 353 354 Design of GAS-HANDLING Systems and Facilities ... Use—-in head (0.8 125 ) W = (0.34)(0.8 125 )( 120 )2 + (1.9)(0.8 125 )( 120 ) = 4,1631b (c) Cone: _ Pd ~ cos a (SE - 0.6P) t t= ( 125 ) ( 120 ) • = 0.585 in (2 cos 30) (17,500 x 0.85 - 0.6 x 125 ) Required thickness ... Misc 12, 870 4,163 5,796 7 ,26 0 30,089 5.000 35,089 Ib Mechanical Design of Pressure Vessels Case II—Ellipsoidal head (a) Skirt: I-°^d +r2jL j_j — " 12 _ (0 .25 ) ( 120 ) | 12 = 4.50 ft W = (11) ( 120 )...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 6 docx
... 1 .22 1 .23 1 .24 1 .25 1 .26 1 .27 1 .28 1 .29 1.30 C k a 317 318 319 320 321 322 323 325 326 327 328 329 330 331 3 32 333 334 335 336 337 338 339 340 341 3 42 343 344 345 346 347 1.31 1. 32 1.33 1.34 1.35 ... 13 -2 Gas Constant, C, as Function of Ratio of Specific Heat, CP/CV, or k k 1.01 1. 02 1.03 1.04 1.05 1.06 1.07 1.08 1.09 1.10 1.11 1. 12 1.13 1.14 1.15 1.16 1.17 1.18 1.19 1 .20 1 .21 1 .22 1 .23 1 .24 ... and Designations Orifice D E F G H J K L M N P Q R T Area in .2 0.110 0.196 0.307 0.503 0.785 1 .28 7 1.838 2. 853 3.60 4.34 6.38 11.05 16.0 26 .0 Pressure Relief 375 cal Inlet piping should be designed...
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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 RP14.) * Indicates sources that can be anticipated by sensing changes in process conditions Figure 14 -2 Continued 3 92 Design of GAS-HANDLING ... radiation The probability of injury from any of these conditions is increased by an inability to escape All the conditions tend to be more likely to lead to 394 Design of GAS-HANDLING Systems and ... of stating this is that many of the sources and conditions identified on the hazard tree require design considerations that not appear on mechanical flow diagrams The need for proper design of...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 8 docx
... periodic training of existing employees is necessary to educate personnel to be able to per- 422 Design of GAS-HANDLING Systems and Facilities form their work safely and to be aware of environmental ... edition by Jorge Zafra of Paragon Engineering Services, Inc 425 426 Design of GAS-HANDLING Systems and Facilities Welding certification and inspection requirements 6, Design details (if not already ... of a system These valves are the most common general-purpose on/off valves in production facilities (text continued from page 430) 428 Design of GAS-HANDLING Systems and Facilities Table 15-2...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 9 ppt
... 2} A I VA VA 2 21A 21 A 1 VA VA 2 21A 21 A VA VA 2} A 21 A 21 A VA 2 21A 21 A VA VA 2 21A 3 VA VA 21 A 21 A 3 VA VA 21 A 21 A 3 VA VA 2 1A 2{ A 3 VA VA 2} A 21 A 3M VA VA 2 1A 2{ A 31A VA VA 21 A 21 A 3yi VA ... 19 20 Fiat Surf, Nominal Pipe Size, in Aninttniim fYlIf IIIIIwlII Temperature ro H 40 30 20 10 -10 -20 1 VA VA VA 2 VA TA 10 12 14 16 18 20 24 30 1 1 1 VA VA 2 VA VA 2 VA VA VA 2 2]A VA VA 2 2}A ... 1091- 120 0 1061- 120 0 1031-1170 1001-1130 981-1 120 971-1100 971-1100 961-1090 951-1080 901-1010 _ „ _ _ _ _ _ _ _ 1171- 120 0 1131- 120 0 1 121 - 120 0 1101- 120 0 1101- 120 0 1091- 120 0 1081- 120 0 1011-1 120 ...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 10 pptx
... fuel flow to the range of 0,06 to 0.07 Ib of fuel per Ib of air Fuel Injection This is another method of supplying an engine with the correct quantity of fuel Three types of fuel injection are ... employed The principle of operation is to direct a stream of hot gases against the blading of a turbine rotor As shown in Figures 16-6 and 16-7, the gas turbine consists of 478 Design of GAS-HANDLING ... heat process fluids 4 82 Design of GAS-HANDLING Systems and Facilities Figure 16*11 The combined cycle of waste heat recovery can be used to generate steam, Effect of Ambient Conditions Available...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 12 pps
... Temperature °C °F 450 300 28 0 26 0 23 0 21 5 20 0 180 165 160 135 120 100 J*5 8 42 5 72 536 500 446 419 3 92 356 329 320 27 5 24 8 21 2 J85 Identification Number Tl T2 T2A T2B T2C T2D T3 T3A T3B T3C T4 T4A ... (center-to-center) distance between A] and A2, ft Aj = free area of lower opening, ft2 A2 = free area of upper opening, ft2 For example, assume a building with inside dimensions of ft wide, 10 ft long, and ft ... required is: A= (8X10X8) 1 ,20 0 [2. 97(10/54Q)]1 /2 = 2. 27 ft for both the inlet and the outlet GAS DETECTION SYSTEMS Combustible gas detection systems are frequently used in areas of poor ventilation...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 13 docx
... foundation design, 319 frames, 28 7 -28 9 gas lift, 25 4, 26 2, 27 6, 27 8 general, 25 3 -28 5 heads, 461 Helical-Lobe, 26 6 -26 7 industry specifications, 320 - 321 integral units, 25 8, 25 9, 28 8 kinetic, 25 5 lubrication ... wear bands, 29 6 pistons and piston rods, 29 6 positive-displacement, 25 5 reciprocating, 3, 25 5 -26 4 ,28 6- 326 high-speed, 25 8 -25 9 low-speed, 25 9 -26 4 process considerations, 27 6 -28 0 rod, 29 4, 310-311 ... overall, 25 3 specifying, 27 0 -27 2 stages, determining, 27 2 -27 6 use, oil and gas fields, 25 4 Compressors acoustical pulsations, 317-319 balanced opposed frames, 28 6 bearings, 29 6 -29 8 booster, 25 4, 27 6,...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 14 pot
... 22 9 -23 2 designing, 23 2 -24 0 drying cycle time, 23 3 gas velocities, 23 3 introduction, 157 iron sponge, 157-159 pressure drop, 23 4 -23 5 pressures, 23 2 -23 3 temperatures, 23 2 two-tower unit, 22 9 -23 2 Sour ... gels, 23 6 Silicones, 522 , 546 Slugging, 445 Smoking, hazard, 3 92 SNPA-DEA systems, design, 185 SO2 See Sulfur dioxide Solid bed process bed height and diameter, 23 4 costs, 22 9 description, 22 9 -23 2 ... 111, 130, 135, 24 7, 24 9, 25 0, 503, 523 Methanol, 103,180 Minerals Management Service (MMS), 513, 529 5 62 Moisture, 521 , 523 Mole sieves, 24 7, 24 8 Molecular sieve process, 160-161 ,23 6 Monoethanolamine...
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