Process Engineering Equipment Handbook Episode 3 Part 5 ppsx
Process Engineering Equipment Handbook Episode 3 Part 5 ppsx
... Deposits 15. 1 0.80 15 .3 1.2 8.6 0. 83 0.08 14 .3 0.90 1.6 0.01 1 .5 0.01 0.9 0.00 0.00 1.4 0.01 0.6 0.06 0 .5 0.02 0 .3 0.02 0.09 0 .5 0. 03 13. 3 1.8 12.7 0.94 10 .3 0.06 0.84 12.9 0.66 36 .1 7.6 36 .6 7.2 20 .5 ... R-9 P -31 4 Pumps TABLE P-41 VCR8 Pumps Design Criteria Bowl Sizes Capacity Head (per Stage) Pressure Temperature Speed SI units 150 to 255 mm to 230 m 3 /h to...
Ngày tải lên: 21/07/2014, 16:21
Process Engineering Equipment Handbook Episode 3 Part 11 ppsx
... C -33 6 open loop, in magnetic bearings, B-10 overload/overspeed protection in, C -33 6, C -34 3 to C - 35 0, C -36 8 to C -37 4 power limitation in, C -33 3, C - 35 0 to C - 35 4 pressure control in, C -33 3, C -36 8 ... limitation in, C -33 3, C -37 7 to C -38 2 torque control, C -34 4 to C -34 5 turbocompressors, C -33 1 to C -33 6 valves for, CE-18 to CE -39 2 vaporizers, V- 25 to V -...
Ngày tải lên: 21/07/2014, 16:21
Process Engineering Equipment Handbook Episode 3 Part 6 ppsx
... L kD EI LLLLL LL kD EI LL LL v v 4 43 4 1 2 3 3 2 2 1 2 21 31 1 2 31 2 21 2 1 248 4 12 3 = - Ê Ë ˆ ¯ +-+ () + () {} -+ - () () {} K LL kD EI LL LL kD EI LL LL v v 3 32 1 2 22 2 31 1 2 31 2 21 2 4 12 3 = -+ - () -+ ... (O.D.) 6 5 / 8 ≤ 8 5 / 8 ≤ 12 3 / 4 ≤ 14≤ 16≤ 18≤ 20≤ In and out line sizes 2≤ 3 4≤ 6≤ 8≤ 10≤ 12≤ A Face-to-face 17≤ 20≤ 24≤ 26≤ 30 ≤ 34 ≤ 38 ≤ B A...
Ngày tải lên: 21/07/2014, 16:21
Process Engineering Equipment Handbook Episode 3 Part 10 pot
... (B16 .3, B16 .5, B16. 15 and B16 .34 ) and B31 (B31.1, B31 .3, B31.4, B31 .5, B31.8 and B31.9) Interpretations A39, A90, A112, B1, B2, B 15, B18, B20, B30, B36, B56, B 73, B94, CSD, MH14, N 45. 2, N509, N510, ... Karian (212) 59 1- 855 2 PTC 23. 1 Spray Cooling Systems Jack H. Karian (212) 59 1- 855 2 PTC 24 Ejectors William Hays (212) 59 1- 855 0 PTC 25 Pressure Relief Devices Umbert...
Ngày tải lên: 21/07/2014, 16:21
Process Engineering Equipment Handbook Episode 3 Part 9 doc
... -33 .3 Chorine -30 .1 -34 .5 Hydrogen chloride -121.0 - 85. 0 Hydrogen sulfide - 75 .3 -59 .6 Sulfur dioxide 14.0 -10.0 Methane - 258 .7 -161 .5 Ethane -127.8 -88.8 Propane - 43. 7 -42.1 N-Butane 31 .1 -0 .5 Ethylene ... table; 0 .5 5 give highest score to worst case scenario) Distance from Site Lane use (current or future) 0 30 0m 30 0 m–1km 1 5 km Residential 5 4 .5 3 Agricult...
Ngày tải lên: 21/07/2014, 16:21
Process Engineering Equipment Handbook Episode 3 Part 8 pptx
... 42 SD- 15- 1 .5 150 ,000 150 60 SD- 15 -3 150 ,000 30 0 54 SD- 15- 6 150 ,000 600 54 SD- 15- 10 150 ,000 1000 48 SD-20-1 .5 200,000 150 60 SD-20 -3 200,000 30 0 60 SD-20-6 200,000 600 54 SD-20-10 200,000 1000 54 * ... 20,000 600 36 SD-2-10 20,000 1000 36 SD -5- 1 .5 50,000 150 42 SD -5 -3 50 ,000 30 0 42 SD -5- 6 50 ,000 600 42 SD -5- 10 50 ,000 1000 36 SD-10-1 .5...
Ngày tải lên: 21/07/2014, 16:21
Process Engineering Equipment Handbook Episode 3 Part 7 pot
... is related, is 1.0 13 bar, and the actual air pressure normally varies within 1.0 13 ± 0. 05 bar. As the pressure affects the air density, and thus the mass flow through Turbines, Gas T -55 FIG. T-46 Power ... ASME Paper No. 85- GT-1 53 . Sedigh, F., and Saravanamuttoo, H. I. H., 1990, “A Proposed Method for Assessing the Susceptibility of Axial Compressors to Fouling,” ASME Paper No. 90...
Ngày tải lên: 21/07/2014, 16:21
Process Engineering Equipment Handbook Episode 3 Part 4 docx
... in power plants. See Figs. P -33 3 and P -33 4. General specifications Capacities to 15, 000 gpm (34 00 m 3 /h) Heads to suit Speeds to 7200 rpm Temperatures to 800°F (4 25 C) Pressure (hydrotest) to ... gas processing, H to 750 ft (229 m) general services. T to 650 °F (34 3°C) P to 59 5 psig (4100 kPa) Paper Stock/High Capacity Process Paper stock, solids and fibrous/stringy Q to 28,000 g...
Ngày tải lên: 21/07/2014, 16:21
Process Engineering Equipment Handbook Episode 3 Part 3 potx
... 1 25 37 .4 50 0 106 3, 100 4 15. 4 31 13. 1 130 38 .5 520 109 3, 200 4 25. 4 32 13. 5 1 35 39 .6 54 0 112 3, 300 4 35 .3 33 13. 8 140 40.6 56 0 1 15 3, 400 4 45. 2 34 14.1 1 45 41.8 58 0 118 3, 50 0 455 .0 35 14.4 150 42.8 ... 121 3, 600 464.7 36 14.7 155 43. 9 620 124 3, 700 474.4 37 15. 0 160 45. 0 640 127 3, 800 4 83. 9 38 15 .3 1 65 46.0 660 130 3, 900...
Ngày tải lên: 21/07/2014, 16:21
Process Engineering Equipment Handbook Episode 3 Part 2 ppt
... demand Saturated process steam bar 3 5 12 Mass flow t/h 24.6 206.7 76 .5 Sootblow steam bar 35 Mass flow t/h 11.7 Steam production Tomlinson boiler Bark boiler Mass flow t/h 31 9 .5 56 Pressure bar ... condensate pumps FIG. P-1 73 Vorecon type RWE 5 F3 driving a compressor in a Swedish refinery. Input speed n e = 2980 rpm; power requirement P a = 1 53 0 kW; output speed n a = 15, 03...
Ngày tải lên: 21/07/2014, 16:22