Process Engineering Equipment Handbook 2009 Part 2 pdf

Process Engineering Equipment Handbook 2009 Part 2 pdf

Process Engineering Equipment Handbook 2009 Part 2 pdf

... Delaval.) 1. Filtration (the 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 ... Filsorption II process) is used for separation of submicron particles, heavy metals, and toxic hydrocarbons by a combination of filtering, “sorption,” and chemical reaction. The Wetpac ® proces...

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Process Engineering Equipment Handbook 2009 Part 4 pdf

Process Engineering Equipment Handbook 2009 Part 4 pdf

... common engineering Compressors C- 121 FIG. C-106 The labyrinth piston. (Source: Sulzer-Burckhardt.) C- 122 Compressors FIG. C-107 The compressor valve. (Source: Sulzer-Burckhardt.) Compressors C- 129 FIG. C-117A ... between cylinder and crankcase is essential and where process gas is permitted in the open distance piece (e.g., for O 2 , N 2 , CO 2 , process air, etc., generally...

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Process Engineering Equipment Handbook 2009 Part 7 pdf

Process Engineering Equipment Handbook 2009 Part 7 pdf

... We see that operating the compressor at a specific speed range— 12, 000 rpm—will excite the 20 0-Hz first harmonic (20 0 Hz = 20 0 ¥ 60 = 120 0 rpm). This range should be avoided. Condition Monitoring; ... 19 72. 17. Thomson, Mechanical Vibrations, 2d ed., Prentice Hall, Englewood Cliffs, NJ, 1961. 18. Buscarello, R., vibration course notes, 1980. 19. Handbook on vibration, McGraw-Hill, Ne...

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Process Engineering Equipment Handbook 2009 Part 10 pdf

Process Engineering Equipment Handbook 2009 Part 10 pdf

... (1), (2) Kerosene (K-1) 43.0 (18,500) (2) Jet A 43 .2 (18,600) (2) Naphtha 44 .2 (19,000) (2) , ( 12) , (13), (14) Condensate fuel 45 .2 (19,400) (2) , ( 12) , (13), (14) Methanol 19.9 (8,555) (2) , ( 12) Ethanol ... Comments* Natural gas 35.5 (900) (1), (2) , (4) LNG 35.5 (900) (2) , (3), (6) LPG (typical blend) 104.8 (2, 700) (2) , (3), (5) Propane 91 .2 (2, 300) (2) , (5) Butane 11...

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Process Engineering Equipment Handbook 2009 Part 16 pdf

Process Engineering Equipment Handbook 2009 Part 16 pdf

... mm to 475 m 3 /h to 60 m 70 bar to 20 5°C to 29 60 rpm 12 in U.S. units 12 to 18 in to 21 00 gpm to 20 0 ft 1000 psi to 400°F to 1800 rpm other sizes FIG. P- 322 Pump external view (type CD 8). (Source: ... example, the ODP of R- 12 is 1.0, while one of its interim replacements, R-409A, a blend of three HCFCs (R -22 , R- 124 , and R- 142b), has an ODP of 0.05. Some of the HCFCs, such a...

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Process Engineering Equipment Handbook 2009 Part 20 ppt

Process Engineering Equipment Handbook 2009 Part 20 ppt

... C -21 9 to C -22 8 applications for, C -22 0 to C -22 2, C -22 5 to C -22 8 compact (CVK) design, C -22 7 to C -22 8 HVK series, C -22 0 internal view of, C -22 9, C -23 3, C -23 5, C -23 7 multistage design in, C -21 9 operating ... C-193, C -20 7, C -22 3 inlet guide vanes in, C -20 7 to C -20 8, C -21 4 to C -21 6 intercooler in, C-193 to C-196, C -20 7 to C -20 8, C -21 5 to C -21 6, C...

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Process Engineering Equipment Handbook 2009 Part 1 ppsx

Process Engineering Equipment Handbook 2009 Part 1 ppsx

... Predicted 63 125 25 0 500 1000 20 00 4000 8000 3-mm steel Predicted 16 22 28 34 40 43 35 44 Measured 16 21 27 33 38 39 33 — 6-mm steel Predicted 22 28 34 40 43 35 44 53 Measured 22 27 35 39 44 37 42 — 6-mm ... dB 63 125 25 0 500 1000 20 00 4000 8000 Panel A151 821 2 428 323 738 Panel B 15 21 24 25 29 33 37 38 TABLE A-7 Predicted Parameters for Three Panels (the panels were ma...

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Process Engineering Equipment Handbook 2009 Part 3 doc

Process Engineering Equipment Handbook 2009 Part 3 doc

... formulas: ss(C 4 AF + C 2 F) = (2. 100 ¥ % Al 2 O 3 ) + (1.7 02 ¥ % Fe 2 O 3 ) Tricalcium silicate = (4.071 ¥ % CaO) - (7.600 ¥ % SiO 2 ) - (4.479 ¥ % Al 2 O 3 ) - (2. 859 ¥ % Fe 2 O 3 ) - (2. 8 52 ¥ % SO 3 ). No ... SiO 2 ) - (6.718 ¥ % Al 2 O 3 ) - (1.430 ¥ % Fe 2 O 3 ) - (2. 8 52 ¥ % SO 3 ) Dicalcium silicate = (2. 867 ¥ % SiO 2 ) - (0.7544 ¥ % C 3 S) Tricalcium alum...

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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 85 120 165 23 0 G 4 36 48 53 66 100 120 155 20 5 27 0 mr 2 18 27 45 85 150 28 0 500 880 1,570 Q 4 passes 325 325 430 540 593 ... x = 0. 021 x = 0. 021 mass using Fig. C -21 1 M f = 28 .58 kg/kmol M f = 28 .58 kg/kmol Wet gas constant R f = 29 0.94 J/kgK R f = 29 0.94 J/kgK 2 Calculation of the wet...

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Process Engineering Equipment Handbook 2009 Part 6 pps

Process Engineering Equipment Handbook 2009 Part 6 pps

... 1 0.0311 0.0 025 9 0.001 02 0.1 02 g ft/s 32. 16 1 0.0833 0.0 328 3 .28 ft/s 2 in/s 386 12. 0 1 0.3937 39.37 in/s 2 cm/s 980 30.48 2. 540 1 100 cm/s 2 m/s 9.80 0.3048 0. 025 4 0.010 1 m/s 2 Ø TABLE C-19 ... rev/min or Æ rad/s 2 degree/s 2 rev/s 2 rev/min/s By To obtain value in Ø rad/s 1 0.01745 6 .28 3 0.1047 rad/s 2 degree/s 57.30 1 360 6.00 degree/s 2 rev/s 0.15 92...

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