Process Engineering Equipment Handbook 2009 Part 5 potx
Process Engineering Equipment Handbook 2009 Part 5 potx
... 29 41 57 80 G 2 1.1 1.4 1.6 2.0 2.3 2 .5 3.2 4 .5 6.3 G 3 25 33 40 50 69 85 120 1 65 230 G 4 36 48 53 66 100 120 155 2 05 270 mr 2 18 27 45 85 150 280 50 0 880 1 ,57 0 Q 4 passes 3 25 3 25 430 54 0 59 3 680 ... 400 450 50 0 600 700 800 900 H 1 4,800 5, 600 5, 400 5, 700 7,200 7, 750 8,700 9,900 11,000 H 2 6,700 8,200 7,400 7,900 10,100 10, 850 12,100 13,700 15, 200 H 3 5...
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Process Engineering Equipment Handbook 2009 Part 13 potx
... waterworks 1 .5 1.7 2.0 Dredge 2.0 2.4 2 .5 Rotary: axial flow—all types 1 .5 1 .5 1.8 Rotary: gear 1 .5 1 .5 1.8 Rotary: liquid piston 1.7 1.7 2.0 Rotary: lobe 1.7 1.7 2.0 Rotary: sliding vane 1 .5 1 .5 1.8 Reciprocating: ... features (see Fig. P -57 ) H S - 60/7 - H size of coupling/synchronizer See also Figs. P -56 and P -57 . Power generation Synchronous clutch coupling (see Figs....
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Process Engineering Equipment Handbook 2009 Part 14 potx
... 0.002 35 0.4–0.9 800 35 45 104 87 45 4 2.1 0.003 40 0.6–1.3 700 40 52 109 94 52 5 2 .5 0.003 45 0.8–1.7 620 45 58 116 102 60 7 2.8 0.004 50 1.1–2.2 56 0 50 65 122 109 65 8 3.4 0.006 60 1.8–3.6 450 ... 0. 150 150 23.0–46.0 1 85 150 180 238 2 35 1 75 13 22 0.180 160 36.0–71.0 1 75 160 200 246 260 1 95 15 27 0.260 170 39.0–78.0 1 65 170 210 256 256 191 15 28 0.290 180...
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Process Engineering Equipment Handbook 2009 Part 20 ppt
... (EMS) in, E -52 forest preservation and, E -52 key ratios in, E -51 life cycle assessment (LCA) in, E -55 to E -56 packaging, resource efficient, E -52 to E -54 profitability, long term, E -52 to E -55 research ... P-1 environmental economics, E-47 to E -56 biological diversity and, E -50 cost-benefit analysis for, E -51 to E -56 ecolabeling in, E -54 to E -55 emission reduction and, E...
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Process Engineering Equipment Handbook 2009 Part 1 ppsx
... Class 2 Class 3 63–1 25 50–160 2 3 4 250 50 0 200–630 1 .5 2 4 1000–4000 800 50 00 1 1 .5 4 6300 2 2 .5 4 A-Weighted (50 –6300 Hz) 1 1 .5 4 NOTES: 1. Class 1 = Precision Grade, Class 2 = Engineering Grade, ... chart. Chemistry Carbon . 85% –1.20% Manganese S70–S110 . 35% –1.20% S170 .50 %–1.20% S-230 and larger .60%–1.20% Silicon .40%–1 .50 % Sulfur . 05% max Phosphorus . 05% max Hard...
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Process Engineering Equipment Handbook 2009 Part 2 pdf
... end process may require removal down to 0.1 mm; 1 to 5 mm is common). 2. Electrostatic precipitation (can remove up to 90% plus of the particles in the air). 3. Air washing (can remove between 50 ... Air Inlet Filtration for Gas Turbines A- 65 FIG. A -53 Water penetration through the inlet silencer. (Source: Altair Filters International Limited.) FIG. A -54 Corrosion in plenum. (Source:...
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Process Engineering Equipment Handbook 2009 Part 3 doc
... 3 .5 D 4 .5 DD Loss on ignition, max, % 3.0 3.0 3.0 2 .5 3.0 Insoluble residue, max, % 0. 75 0. 75 0. 75 0. 75 0. 75 Tricalcium silicate (C 3 S) C max, % — — — 35 F — Dicalcium silicate (C 2 S) C min, % — — ... types of 15 30% — — May be either SO x , CO, THC kilns) positive or may increase adverse LNB High (all types of 15 30% 110–160 340 57 0 May vary with May vary with Indirect-fi...
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Process Engineering Equipment Handbook 2009 Part 4 pdf
... -93°C Discharge 2nd 6.8 bar - 45 to + 35 C Maintenance report on these compressor applications. By the end of January 1996 the first three compressors had all passed 15, 000 running hours. One compressor was ... loaded parts, to optimize the aerodynamic characteristics, to influence the movement of the dynamic parts, to introduce improved materials and manufacturing techniques. Compressors C-1...
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Process Engineering Equipment Handbook 2009 Part 6 pps
... obtain value in Ø rad/s 1 0.017 45 6.283 0.1047 rad/s 2 degree/s 57 .30 1 360 6.00 degree/s 2 rev/s 0. 159 2 0.00278 1 0.0167 rev/s 2 rev/min 9 .54 9 0.1667 60 1 rev/min/s Ø C- 252 Condensers FIG. C-283 CB ... very small amplitude near 650 0 rpm. 15 FIG. C-303 The “steps” noted may mean the phase shift indications between 1° and 359 ° can cause extreme travel of the plotter pen. 15 Figu...
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Process Engineering Equipment Handbook 2009 Part 7 pdf
... of turbocompressors. See Figs. C- 355 through C- 357 . Safety: to prevent the compressor from operating in an unstable range or at other hazardous conditions Process: to adapt the compressor ... other hazardous conditions Process: to adapt the compressor performance to the demands of the process FIG. C- 355 Antisurge control system and combined discharge pressure/power limit control...
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