Embed Size (px)
DESCRIPTION
ChemSOFver 0.0Online Chemical Engineering SoftwaresPACKED TOWER SIZINGDate By1.00Column Tag No. Column Name Project NumberT-101 Amine Absorber P9785615-Mar-10 ChemsofProcess Data 1 Liquid Flowrate 2 Gas Flowrate 3 Liquid Density 4 Gas Density 5 Liquid Viscosity 6 Packing Type 7 Packing Factor Calculation Type 1100 1136 62.3 0.0737 1 lb / h lb / h lb / ft3 lb / ft3 cP 1100 lb / h 1136 lb / h 62.3 lb / ft3 0.1 lb / ft3 1 cP0.40 0.20 0.10 0.04 1.50 1.00 0.50 0.25 0.10 0.01 0.006 0.
Citation preview
ver 0.0
Column Tag No. T-101 Date 15-Mar-10Column Name Amine Absorber By ChemsofProject Number P97856
Process Data
1 Liquid Flowrate 1100 lb / h #VALUE!
2 Gas Flowrate 1136 lb / h #VALUE!
3 Liquid Density 62.3 lb / ft3 #VALUE!
4 Gas Density 0.0737 lb / ft3 #VALUE!
5 Liquid Viscosity 1 cP #VALUE!
6 Packing Type Intalox Saddle Ceramic , 1.5"
7 Packing Factor 52
Calculation Type Enter % Flooding
50 % 50 %
ResultsX Coordinate #VALUE!Y Flood #VALUE!Y Coordinate #VALUE!
Pressure Drop #VALUE! inch H2O/ ft
Column Diameter #VALUE! ft
% Flooding 50.00 %
Reference where, L = Liquid mass rate, lb / h- Distillation Design, Henry Z. Kister G = Gas mass rate, lb / h
- Applied Process Design, Volume 2, Ernest E Ludwig
- Packed Tower Design and Applications, R.F. Strigle = Liquid Density, lb / ft3
- Gas Purification, 5th Edition G*ν = Liquid Kinematic viscosity, cSt
ρG = Gas Density, lb / ft3
ρL
= Gas mass velocity, lb / ft2 - s
ChemSOFOnline Chemical Engineering Softwares PACKED TOWER SIZING
www.chemsof.com
0.00 0.01 0.10 1.00 10.000.00
0.01
0.10
1.00
0.20
0.40
0.04
0.0060.05
Strigle modified Eckert's Generalized Pressure Drop Correlation (GPDC)
Flooding
X
Y0.10
0.25
0.50
1.001.50
∆P - inch H2O/ ft
X= LG ( ρGρL )
0 .5
Y= G¿ 2Fυ0 .1
32.2 ρG (ρL−ρG )
www.chemsof.com
