3 design of mooring system
The Overseas Coastal Area Development Institute of Japan pptx
... 38 4 [3] Design of Piles 38 4 3. 3.2 Floating Breakwater 38 4 [1] General 38 4 [2] Selection of Design Conditions 38 5 [3] Design of Mooring System ... .33 3 [1] Outline 33 3 [2] Strength Parameters 33 4 [3] Calculation of Active Earth Pressure 33 4 [4] Case of Limited Area of Subsoil Improvement 33 5 ... .33 9 7.10.1 Principle of Design 33 9 [1] Scope of Application .33 9 [2] Basic Concept 33 9 7.10.2 Strength and Permeability of Sand Piles .33 9...
- 664
- 2,191
- 0
Báo cáo hóa học: " Design of Uniformly Most Powerful Alphabets for HDF 2-Way Relaying Employing Non-Linear Frequency Modulations" ppt
... The trellis of quaternary full-response CPM with modulation index κ = 1/2 Again, orthonormality of {si }3 implies i=0 bi-orthonormality of overall alphabet 10 p Figure 13 The sum of squared absolute ... by Grant Agency of the Czech Republic grant 102/09/1624; and by Grant Agency of the Czech Technical University in Prague, grant SGS 10/287/OHK3/3T/ 13 Endnotes a For the sake of notation simplicity, ... Theory 34 (2), 260–270 (1988) doi:10.1109/18.2 634 23 F Amoroso, Pulse and Spectrum Manipulation in the Minimum (Frequency) Shift Keying (MSK) Format Communications, IEEE Transactions on 24 (3) , 38 1 38 4...
- 18
- 346
- 0
Báo cáo hóa học: " Research Article Noniterative Design of 2-Channel FIR Orthogonal Filters" pptx
... (38 ): 3a2 + a4 , + a2 r (3) = h1 h4 = − a2 + a2 ( 43) r(1) − r (3) 10a2 + 3a4 − = + a2 (44) √ (37 ) We obtain that the maximum is achieved for a = ± For √ a = 3, we have √ √ √ √ h = √ − 3, − 3, + 3, ... using (27), the sum of the coefficients of h is a linear combination of the sum of each one of the two columns: s = h1 + ut (b + c) + hL + ut (c − b) (34 ) so we get the equation of a straight line ... the components of the filter by means of h1 , hL , and the L/2 − parameters This is one of the main results of this paper, which constitutes a new characterization and design method of all orthogonal...
- 7
- 188
- 0
ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 2 doc
... 0982 0982 0982 0982 130 9 130 9 130 9 130 9 1 636 1 636 1 636 1 636 1 636 1 636 1 636 1 636 1 636 19 63 39 63 19 63 19 63 9 63 39 63 19 63 39 63 19 63 19 63 2618 2618 2618 2618 2618 2618 2618 2618 Ft3 Internal Surface ... 2618 32 72 32 72 32 72 32 72 32 72 32 72 32 72 32 72 32 72 32 72 39 27 39 27 39 27 39 27 5 236 5 236 5 236 5 236 Ft2 Internal Surface Per Ft Length 236 1 2 435 , 233 0 2409 2571 2644 2702 2775 2, 838 2 932 30 16 30 89 32 25 ... 065 0295 033 3 036 0 037 3 06 03 0 731 0799 0860 1075 1269 1452 1548 130 1 1486 655 1817 1924 2 035 2181 2298 2419 1825 20 43 22 23 24 63 2679 2884 30 19 31 57 33 39 36 32 35 26 4208 4 536 48 03 51 53 54 63 5755...
- 25
- 383
- 0
ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 1 docx
... 200-1100 24 -30 20-50 450-600 20 -30 20-50 175 -30 0 85-160 24 -30 2-60 20-50 16-60 550-650 35 0-500 200 -30 0 70-100 14 -30 10-70 17-70 18-70 26 -30 20-70 18-70 15-70 towers packing is used instead of trays ... Value of Gas >» Gas Component Ethane Propane Butane Pentane Net Heating Value Btu/SCF 1618 231 6 30 10 37 08 $3. 00/MMBtu SCF/Gallon Equivalent Value $/Gallon Equivalent Value $/Gallon 37 .5 36 .4 31 .8 ... at 95% evaporation deg F, max -37 * 36 * 36 * -37 * ASTMD- 1 837 -81 2.5 — — 2,5 ASTMD-2 1 63- 82 2.0 2.0 — ASTM D-2 1 63- 82 — — — — ASTMD-2 158-80 ASTM D-21 58-80 ASTMD- 1 838 -84 ASTM D-2784-80I GPA Propane...
- 25
- 459
- 0
ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 2 pps
... calculation of horsepower and number of stages depends upon the choice of type of compressor, and the type of compressor depends in part upon horsepower and number of stages A first approximation of the ... consideration of the advantages and disadvantages listed earlier In addition, local foundation conditions, type of drivers available, cost of fuel, availability of spare 272 Design of GAS-HANDLING Systems ... 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 19,602 88 190 38 0 Centrifugal Screw High Speed High Speed High Speed Screw 4.0 3. 0 3. 0 2 1 43 286 Vane Screw...
- 25
- 351
- 0
ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 3 potx
... The effects of the seat area, the lift area, and the flow paths are automati- 30 2 Design of GAS-HANDLING Systems and Facilities Figyre 11-16 Cut-away view of poppet valve {Courtesy of 0resser-Roncf ... 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 ... capacity of the cylinder is a function of piston displacement and volumetric efficiency This is in turn a function of cylinder clearance, compression ratio, and gas properties 30 8 Design of GAS-HANDLING...
- 25
- 332
- 0
ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 4 pdf
... 11 ,30 0 12,500 13, 800 12,700 13, 800 13, 800 15,000 15,000 15,000 13, 900 7,500 16 ,30 0 18,800 17,700 17,700 17,400 16 ,30 0 17,500 16 ,30 0 17,500 11,200 — 12 ,30 0 10,200 18 ,30 0 20,000 21 700 23, 300 15,000 ... 16,700 18,100 6,900 18 ,30 0 18 ,30 0 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 16,700 20,000 16,700 Mechanical Design of Pressure Vessels ... Class ~20°FtolOO°F 100°Fto200°F 150 30 0 400 600 900 1500 2500 285 740 990 1480 2220 37 05 6170 250 675 900 135 0 2025 33 75 5625 Mechanical Design of Pressure Vessels 33 1 process conditions in their...
- 25
- 417
- 0
ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 5 pps
... SA-240 -31 6L SA-106-B SA-106-B SA -33 3-6 SA-105 SA-181-1 SA-1 93- B7 SA-194-2H SA-105 SA-181-1 SA-1 93- B7M SA-194-2M SA -35 0-LF1 SA -31 2 TP -30 4 SA-182 F -30 4 SA-1 93- B8 SA-194-8A SA -31 2 TP -31 6L SA-182 F -31 6L ... Weight of shell = (11)(120)(0.8125)(20.7) = 22,200 Ib 35 3 35 4 Design of GAS-HANDLING Systems and Facilities (c) Summary: Shell Head Head Skirt Cone Misc 22,200 4,1 63 4,1 63 2,970 L656 35 ,152 ... The weight of one 2:1 ellipsoidal head is approximately: The weight of a cone is: a = one half the cone apex angle 33 9 34 0 Design of GAS-HANDLING Systems and Facilities The weight of nozzles...
- 25
- 452
- 0
ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 6 docx
... 1.28 1.29 1 .30 C k a 31 7 31 8 31 9 32 0 32 1 32 2 32 3 32 5 32 6 32 7 32 8 32 9 33 0 33 1 33 2 33 3 33 4 33 5 33 6 33 7 33 8 33 9 34 0 34 1 34 2 34 3 34 4 34 5 34 6 34 7 1 .31 1 .32 1 .33 1 .34 1 .35 1 .36 1 .37 1 .38 1 .39 14 1.41 ... 1.51 1.52 1. 53 1.54 1.55 1.56 1.57 1.58 1.59 16 C 34 8 34 9 35 0 35 1 35 2 35 3 35 3 35 4 35 5 35 6 35 7 35 8 35 9 36 0 36 0 36 1 36 2 36 3 36 4 36 5 36 5 36 6 36 7 36 8 36 9 36 9 37 0 37 1 37 2 37 3 k 1.61 1.62 1. 63 J.64 1.65 ... 1. 73 1.74 1.75 17 17 1.78 1.79 1.80 1.81 1.82 1. 83 1.84 1.85 18 1.87 1.88 1.89 19 C 37 3 37 4 37 5 37 6 37 6 37 7 37 8 37 9 37 9 38 0 38 1 38 2 38 2 38 3 38 4 38 4 38 5 38 6 38 6 38 7 38 8 38 9 38 9 39 0 39 1 39 1 39 2 39 3...
- 25
- 289
- 0
ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 7 docx
... elimi- 38 8 Design of GAS-HANDLING Systems and Facilities nating one of the conditions Since no condition can be eliminated with absolute certainty, an attempt is made to minimize the occurrence of ... 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 39 4 Design of GAS-HANDLING Systems and Facilities ... would be required, given the degree of reliability of shutdown systems and the consequences 400 Design of GAS-HANDLING Systems and Facilities of failure However, it is more costly in engineering...
- 25
- 299
- 0
ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 8 docx
... rating of their elastomer seats Figure 15-1 Cutaway of ball valve (Courtesy of Cameron Iron Works, Inc.] Figure 15-2 Cutaway of plug valve (Courtesy ofXomox Corp.) 432 Design of GAS-HANDLING Systems ... pressure into or out 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 ... replace Because of the erosive action of the fluid when the valve is throttling, they should not be used for on/off service, A tight seal may not be possible, 434 Design of GAS-HANDLING Systems and...
- 25
- 252
- 0
ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 9 ppt
... 2 21A 21A VA VA 2 21A 3 VA VA 21A 21A 3 VA VA 21A 21A 3 VA VA 2 1A 2{A 3 VA VA 2}A 21A 3M VA VA 2 1A 2{A 31 A VA VA 21A 21A 3yi VA VA 1}A 3 3^ VA VA VA VA 2 2}A 21A 3 314 3{ A /4 Table 15-7C Typical ... Minimum Temp, without Special Testing A -33 3 Grade ! A -33 4 Grade A -31 2TP304L A^12_TP316L - SOT - 50°F -425°F If^I For sour service, National Association of Corrosion Engineers (NACE) MR-01-75 requires ... 440 Design of GAS-HANDLING Systems and Facilities Table 15-4 Sample Valve Designation System Each valve designation has four (4), and possibly five (5), parts (1) This part of each valve designation...
- 25
- 245
- 0
ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 10 pptx
... 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 Systems ... 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 ... for more in-depth discussion of design details ^Reviewed for the 1999 edition by Santiago Pacheco of Paragon Engineering Services, Inc 467 468 Design of GAS-HANDLING Systems and Facilities RECIPROCATING...
- 25
- 422
- 0
ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 11 ppsx
... accumulation of significant quantities of vapor-air mixtures in concentrations above 25% of their lower flammable (explosive) limit (LFL) 510 Design of GAS-HANDLING Systems and Facilities Figure 17- 13 ... accordance with Article 500, NEC Code—1984 (Courtesy of R Stahl, Inc.] 501 502 Design of GAS-HANDLING Systems and Facilities Electrical Systems 5 03 recommends that mixtures containing less than 25% ... portion of the fuel to burn without the presence of a flame This significantly reduces combustion temperature 492 Design of GAS-HANDLING Systems and Facilities Based on the results of the catalytic...
- 25
- 286
- 0
ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 12 pps
... 230 215 200 180 165 160 135 120 100 J*5 842 572 536 500 446 419 39 2 35 6 32 9 32 0 275 248 212 J85 Identification Number Tl T2 T2A T2B T2C T2D T3 T3A T3B T3C T4 T4A T5 T6 Electrical Systems 5 23 ... toward the installation of cable systems rather than conduit systems Offshore, the vast majority of new systems are 534 Design of GAS-HANDLING Systems and Facilities Figure 17- 23 Liquidtight and flexible ... where ignitible concentrations of gases and vapors not occur for appreciable lengths of time Electrical Systems 533 However, the non-armored cables must satisfy IEEE 38 3 or IEEE 45 flarnmability...
- 25
- 224
- 0
ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 13 docx
... capacity, defined, 30 7 clearance, 30 5 -30 7 cooling systems, compressors, 31 2 -31 3 lubrication systems, compressors, 31 3 -31 7 s izi ng, compressors, 30 7 -31 .0 throughput capacity, 30 9 Cylinders compressors ... American Society of Mechanical Bearings, compressor, 296-298 Engineers (ASME), 52, 32 7, 32 8, Bernoulli's Law, 255 33 1 33 3 35 6, 39 6 Blanket gas systems, inert, 165 Amine Block valves, 37 5 -37 6, 462, 465 ... reflux, 136 lubricating systems, compressor, 31 2 -31 7 Cord, flexible electrical, 533 Corrosion allowance, pressure vessels, 33 3 amine systems, 190 condensed water, 195 conduits, 534 electrical systems,...
- 25
- 372
- 0
ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 14 pot
... pressure, 32 8 -33 1 drains, 464 ellipsoidal heads, 33 2 head types, 33 1 -33 3 inspection procedures, 33 3 -33 4 low-pressure, 33 0 maximum stress values, 33 1 mechanical design, 32 7 -35 4 non-code, 32 8 564 ... heads, 33 0 specifications, 34 0 -35 0 venting, 38 9 -39 2 wall thickness, 32 7, 33 1 -33 3 weight, 33 5 -34 0 wellhead shut-in, 118,462 working, 32 8 -32 9 Prime movers, 467-492 Process components FMEA, 39 6 -39 8 ... 36 0 -36 2, 37 2 critical flow, 36 7 -36 8 cylinder discharge, 279 determination, 35 6 -35 7 discharges, 37 4 -37 6 gas flow rate, 37 0 -37 1 inlet piping, 37 4 -37 5 installation, 37 4 -37 6 liquid flow rates, 37 2 -37 4...
- 9
- 297
- 0
Tìm thêm: khảo sát chương trình đào tạo của các đơn vị đào tạo tại nhật bản khảo sát chương trình đào tạo gắn với các giáo trình cụ thể tiến hành xây dựng chương trình đào tạo dành cho đối tượng không chuyên ngữ tại việt nam điều tra với đối tượng sinh viên học tiếng nhật không chuyên ngữ1 khảo sát thực tế giảng dạy tiếng nhật không chuyên ngữ tại việt nam khảo sát các chương trình đào tạo theo những bộ giáo trình tiêu biểu nội dung cụ thể cho từng kĩ năng ở từng cấp độ xác định mức độ đáp ứng về văn hoá và chuyên môn trong ct phát huy những thành tựu công nghệ mới nhất được áp dụng vào công tác dạy và học ngoại ngữ mở máy động cơ lồng sóc mở máy động cơ rôto dây quấn các đặc tính của động cơ điện không đồng bộ hệ số công suất cosp fi p2 đặc tuyến mômen quay m fi p2 đặc tuyến tốc độ rôto n fi p2 động cơ điện không đồng bộ một pha sự cần thiết phải đầu tư xây dựng nhà máy thông tin liên lạc và các dịch vụ từ bảng 3 1 ta thấy ngoài hai thành phần chủ yếu và chiếm tỷ lệ cao nhất là tinh bột và cacbonhydrat trong hạt gạo tẻ còn chứa đường cellulose hemicellulose chỉ tiêu chất lượng 9 tr 25