Process Engineering Equipment Handbook 2009 Part 3 doc

Process Engineering Equipment Handbook 2009 Part 3 doc

Process Engineering Equipment Handbook 2009 Part 3 doc

... 3. 0 3. 0 3. 5 2 .3 2 .3 When (C 3 A) C is more than 8% 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, ... % Al 2 O 3 ) - (1. 430 ¥ % Fe 2 O 3 ) - (2.852 ¥ % SO 3 ) Dicalcium silicate = (2.867 ¥ % SiO 2 ) - (0.7544 ¥ % C 3 S) Tricalcium aluminate = (2.650 ¥ % Al 2 O 3...

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Process Engineering Equipment Handbook 2009 Part 15 doc

Process Engineering Equipment Handbook 2009 Part 15 doc

... Remarks A48, Classes 20, 25, 30 , 35 , 40, and 50 . . . . . . Gray iron—six grades A 339 , A395, and A396 . . . . . . Nodular cast iron—five grades B1 43, 1B and 2A; B144, 3A; B145, 4A . . . . . . Tin ... . 1, 030 Carbon steel A217—C5 . . . 501 5% chromium steel A296—CA15 CA15 410 13% chromium steel A296—CB30 CB30 . . . 20% chromium steel A296—CC50 CC50 446 28% chromium steel A296—CF-8 CF-8...

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Process Engineering Equipment Handbook 2009 Part 17 doc

Process Engineering Equipment Handbook 2009 Part 17 doc

... (ft) Mass GSV GSV Mass Mass GSV 20–18 66–60 0 .31 0 .30 0 .30 0.28 0.28 3. 09 4–2 13 6.5 0.14 0.10 0.10 0.28 0.28 0.61 20–26 66–6.5 0.11 0.04 0.04 0. 03 0. 03 0.47 Batch transfer uncertainties in (%) NOTE: ... G.S.V. G.S.V. Mass Mass G.S.V. 20 66 0.12 0.06 0.06 0.04 0.04 0. 43 10 33 0.12 0.07 0.07 0.08 0.08 0.41 2 6.5 0. 13 0.08 0.08 0.40 0.40 0 .34 Inventory uncertainties in (%) termi...

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Process Engineering Equipment Handbook 2009 Part 20 ppt

Process Engineering Equipment Handbook 2009 Part 20 ppt

... control in, C -33 3 load limit control in, C -33 4 monitoring logic in, C -33 6 power limitation in, C -33 3 pressure control in, C -33 3 pressure limitation in, C -33 3 process control in, C -33 3 to C -33 4 safety ... 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 -...

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Process Engineering Equipment Handbook 2009 Part 1 ppsx

Process Engineering Equipment Handbook 2009 Part 1 ppsx

... Predicted 63 125 250 500 1000 2000 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 ... 53 Measured 22 27 35 39 44 37 42 — 6-mm aluminum Predicted 13 19 25 31 34 26 35 44 Measured 13 19 25 30 36 30 32 — PREDICTED MEASURED 50 40 30 20 10 0 63 125 250...

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Process Engineering Equipment Handbook 2009 Part 2 pdf

Process Engineering Equipment Handbook 2009 Part 2 pdf

... American Iron and Steel Institute AISI 30 4 and AISI 32 1, do not have sufficient corrosion protection, particularly if the material is work hardened. AISI 31 6 is the most popular choice since it ... that is particularly adaptable to very light loads in either horizontal or vertical shafts. Because of the small Bearings B -3 FIG. B-2 Ring-oil lubrication. (Source: Demag Delaval.) FIG. B -...

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Process Engineering Equipment Handbook 2009 Part 4 pdf

Process Engineering Equipment Handbook 2009 Part 4 pdf

... cylinders. The process data for this compressor are: Gas CH 4 (98%) + N 2 (2%) Suction 1st 1. 036 bar -106 to -160°C Discharge 1st 2.9 bar -36 to -97°C Suction 2nd 2.9 bar -33 to - 93 C Discharge ... Compressor runs at 30 0 rpm with a power input of 233 0 kW. (Source: Sulzer-Burckhardt.) FIG. C-78 Compressor installation in Germany. 2600 m 3 /h of hydrogen at 1 bar abs are compressed to...

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Process Engineering Equipment Handbook 2009 Part 5 potx

Process Engineering Equipment Handbook 2009 Part 5 potx

... 13, 700 15,200 H 3 5 ,30 0 6,500 6 ,30 0 6,700 9,000 9,650 10,800 12,100 13, 400 G 1 8.2 11.1 14 17 .3 24 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 85 120 165 230 G 4 36 ... 6,700 7, 230 8,450 9 ,30 0 10,400 B 3, 800 4,000 4,200 4,400 4,900 5,270 5,750 6,200 6,500 C 3, 400 4,100 3, 700 4,000 5,700* 6,600* 7 ,30 0* 8,100* 9,000* D 1,840 2,250 2,040...

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Process Engineering Equipment Handbook 2009 Part 6 pps

Process Engineering Equipment Handbook 2009 Part 6 pps

... obtain value in Ø g-s, 1 0. 031 1 0.00259 0.00102 0.102 g ft/s 32 .16 1 0.0 833 0. 032 8 3. 28 ft/s 2 in/s 38 6 12.0 1 0 .39 37 39 .37 in/s 2 cm/s 980 30 .48 2.540 1 100 cm/s 2 m/s 9.80 0 .30 48 0.0254 0.010 1 m/s 2 Ø TABLE C-19 ... terms of Ø Amplitude 1 1.571 1.414 0.500 Average 0. 637 1 0.900 0 .31 8 value Root-mean- 0.707 1.111 1 0 .35 4 square (rms) value Peak-to-peak 2.000 3. 14...

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Process Engineering Equipment Handbook 2009 Part 7 pdf

Process Engineering Equipment Handbook 2009 Part 7 pdf

... Controls C -33 5 FIG. C -35 9 Antisurge control system and combined discharge pressure/power limit control system. (Source: Sulzer-Burckhardt.) Control Systems; Controls C -33 7 FIG. C -36 0 Automatic process ... System(s) C -32 3 FIG. C -34 9A Rigid supports and a flexible rotor. 13 FIG. C -34 9B Flexible supports and rigid rotors. 13 TABLE C-29 Characteristics of Forced and Self-Excite...

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