tower t-1001 design in acrylic acid process
DESCRIPTION
Tower T-1001 Design in Acrylic Acid Process. Heuristic: Operate near 70% of Flooding Velocity. Taken From Mass Transfer Operations, 3 rd Ed., Treybal , R.E. . Structured Packing. Taken From Mass Transfer Operations, 3 rd Ed., Treybal , R.E. . Compressor C-1001 A/B - PowerPoint PPT PresentationTRANSCRIPT
Tower T-1001 Design in Acrylic Acid Process
Heuristic: Operate near 70% ofFlooding Velocity
Taken From Mass Transfer Operations, 3rd Ed., Treybal, R.E.
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1
22
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gJmFactorPackingCmkg Density,
smkg Viscosity,Liquid
smkg Flux, GasG' ;
smkg Flux, LiquidL'
Structured Packing
31.1;
105.6;1000;84.1
1895,4.2,40,8
27.62,5.3,310,6
21
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433
GL
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mm
GL
smkg
mkg
mkg
hrtonnembarPCTstreamFor
hrtonnembarPCTstreamFor
Taken From Mass Transfer Operations, 3rd Ed., Treybal, R.E.
m 3.6 Diameter Textbook
m C for mDmA
m 65 C for mDmA
mareaAAGs
kgm
Floodingsm
kgGsm
kgGmC For
Floodingsm
kgGsm
kgGmC For
CG
C
CG
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166.3;1.10
6.4;8.16
,;'29.17
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8.95'
1665
025.0'
2
2
2
221
221
2
1.02
Compressor C-1001 A/BInlet: Air @ 1362.9 kmol/hr, 1.0 Bar, 25 oCOutlet : 5 barHeuristics:Use fans for increases of 30 cm waterUse blowers for increases of 2.75 bargUse compressors for greater than 2.75 barg
kWTextbookkWkWPowerShaft
78% 76 efficiency ,compressor lcentrifuga Uses
mRateFlowVolumetric
kWPowerTotal
kWJskWK
KmoleJ
smolesPower
kWJskWK
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stagesbetween C to cool15 stageeach in Ratio
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286.015.298314.86.378
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286.04.114.1
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286.0
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Heat Exchanger E-1006
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m 73.3A tonne/hr, 54.5m TextbookmATtonne/hr m
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approach. C 10 using outlet C 37 inlet C 30 at wateris fluid Cooling
side. shell:vapor condensing C,T
C 10 is approach etemperatur Minimum
fluids pressurehigh and scaling,fouling, corrosive, for is sideTubefluids condensing and viscous for is sideShell
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