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

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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 )

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