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Characterization of Packing Materials for CO2 Absorption...Koch-Glitsch, Flexipak 2Y HC 49 Julius...

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1 Post Combustion Capture Conference 2011, Abu Dhabi UAE May 17th-19th Characterization of Packing Materials for CO 2 Absorption Norwegian University of Science and Technology (NTNU) Department of Chemical Engineering Trondheim, Norway Ali Zakeri a , Aslak Einbu b , Hallvard F. Svendsen a a NTNU, N-7465 Trondheim, Norway. b SINTEF, N-7465 Trondheim, Norway.
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Page 1: Characterization of Packing Materials for CO2 Absorption...Koch-Glitsch, Flexipak 2Y HC 49 Julius Montz, Montz-Pak B1-250M. 4 Post Combustion CaptureConference 2011, AbuDhabi UAE May

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Post Combustion Capture Conference 2011, Abu Dhabi UAE May 17th-19th

Characterization of Packing Materials for CO2 Absorption

Norwegian University of Science and Technology (NTNU)Department of Chemical Engineering

Trondheim, Norway

Ali Zakeria, Aslak Einbub, Hallvard F. Svendsena

aNTNU, N-7465 Trondheim, Norway.bSINTEF, N-7465 Trondheim, Norway.

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Outline

• Introduction.• Pressure drop.• Liquid holdup.• Effective mass transfer

area.• Conclusions.

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Introduction

The aim of the present work is to test three modern structured packing by measuring pressure drop, liquid hold-up and effective mass transfer area as function of gas and liquid load.

Focus on intermediate and low liquid flow rates Packings studied:

Sulzer, Mellapak 2X, Koch-Glitsch, Flexipak 2Y HC 49Julius Montz, Montz-Pak B1-250M.

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Geometric data for the different packings studied

Packing model Angle of inclination

Packing element height [mm]

Specific surface area[m2/m3]

Void fraction[m3/m3]

Sulzer Mellapak 2X 60 222 205 0.99

Koch-Glitsch Flexipac 2Y HC 45 137 225 0.97

Montz-Pak B1-250M 45 207 244 0.98

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The VOCC absorber test rig

AB

SO

RB

ER

BLOWERC

YC

LO

NE

GA

S C

OO

LE

R

Column ID 0.5 m, packing height 5 m

Superficial gas velocities up to 5 m/s

Liquid flow rate up to 200 l/min

2000 liter holding tanks for batch runs

External CO2 supply (delivers up to 300 kg CO2/h)

Sensors for column pressure- and temperature profile

Gas analyser for CO2 content in-/out of column

Setup for continous measurement of liquid hold-up in packing

Setup for online measurement of CO2 loading of amine

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Pressure drop

Pressure drops were measured based on pressure measurement at 6 positions along the packing height. Position 1 is below the packing, and positions 2- 6 are 0.5 m, 1.5 m, 2.5m, 3.5m, 4.5 m into the packing respectively.

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• (Pa0.5)

Sulzer Mellapak 2x, Air/Water system

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Pressure drop in mbar/m as a function of F-factor for two liquid loads for viscosities ranging between 1 and 12cP using sucrose as viscosifier.

Sulzer Mellapak 2x

ab

5 m3/m2h 25 m3/m2h

Page 9: Characterization of Packing Materials for CO2 Absorption...Koch-Glitsch, Flexipak 2Y HC 49 Julius Montz, Montz-Pak B1-250M. 4 Post Combustion CaptureConference 2011, AbuDhabi UAE May

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Pressure drop in mbar/m as a function of F-factor for two liquid loads for viscosities ranging between 1 and 12cP using sucrose as viscosifier.

ab

5 m3/m2h 25 m3/m2h

Koch-Glitsch Flexipak 2Y HC

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Pressure drop in mbar/m as a function of F-factor for two liquid loads for viscosities ranging between 1 and 12cP using sucrose as viscosifier.

ab

5 m3/m2h 25 m3/m2h

Montz-Pak B1-250M

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Pressure-drop as function of F-factor for the different packings at 5 and 25m3/m2h liquid load.

Air/water Air/sugar soln(5cP) Air/sugar soln(12cP)

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Pressure-drop as function of F-factor for the different packings at 5 and 25m3/m2h liquid loads. Experiments with 30 wt% MEA/air system.

30 wt% MEA/air system

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Calculated pressure drops using the SULCOL, KgTower and Montz Pak compared with experimental data

Mellapak 2X Flexipac 2Y HC

Montz B1 250M

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Sulzer Mellapak 2xAir/Water system

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Liquid hold up as function of F-factor for the different packings at low liquid load .

Mellapak 2X5.7m3/m2h

Flexipac 2Y HC5.0m3/m2h

Montz B1-250M5.0m3/m2h

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Liquid hold up as function of F-factor for the different packings at high liquid load(25 m3/m2h).

Mellapak 2X Flexipac 2Y HC Montz B1-250M

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Liquid hold up as function of F-factor for the different packings

d

Air/water Air/sugar soln(5cP)

Air/30%MEA

Air/sugar soln(12cP)

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Liquid holdup measured and Liquid hold up from literature vs. F-factor

Flexipac 2Y HC Montz B1 250M

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Fractional effective area (ae/ap) as a function of liquid load (m3/m2h) for three different ranges of superficial gas

Absorption of CO2 in 0.3 M NaOH.

Mellapak 2X Flexipac 2Y HC Montz B1 250M

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• = 0.3

Fractional effective area (ae/ap) as a function of liquid load (m3/m2h) for three different ranges of superficial gas

Absorption of CO2 in 30 wt% MEA.

• = 0.2

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Conclusions Pressure drop, liquid hold up and effective mass transfer area were successfully determined in

a pilot plant absorber (0.5 m ID, 5.4 m packing height) as function of liquid viscosity and gas and liquid flow rate.

The variations of the hydraulic parameters are in reasonable agreement with correlations found in literature for F-factors below 3.

A slight influence of viscosity on pressure drop and flooding velocity was found.

Increased viscosity has a significant influence on hold-up especially at high liquid loads.

Both for NaOH and MEA solutions the active area increases with liquid load up to about 25 m3/m2h.

Gas flow rate has a very small effect on active area.

The values of measured effective mass transfer area are close to values found in literature for the NaOH system.

Initial evaluation of effective mass transfer area for the loaded MEA systems show a particularly strong influence of liquid load in the low range. Needs further investigation.

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THANK YOU


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