Turboscrubber, Fluidized bed scrubbers, absorbers and strippersTurboscrubber, Fluidized bed scrubbers, absorbers and strippers

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Case Studies

 

Cleveland Potash, Rotary Dryer Exhaust Gas Cleaning & Heat Recovery.

VAW Stade, Aluminum Smelter Offgas Particulate Removal.

William Blythye, Dual SO2/Particulate Duty.

Wyeth Nutritionals, Boiler Flue Gas Cleaning &Heat Recovery.

Rhone Poulenc Biochimie, NOx Removal

Other Users.

 

 

CASE STUDY: Cleveland Potash, Rotary Dryer Exhaust

Commissioned in the summer of 1995 this TURBOSCRUBBER® unit simultaneously scrubs fine KCl salt crystals (outlet from cyclones) and soot particles (product of HSFO fired dryer), absorbs SO2 gas, and recovers over 4 MW of heat energy for reuse within the process. The scrubbing medium is, normally, process slurry, having an s.g. of at least 1.35 and containing 30% undissolved solids. The unique non-clogging feature of the TURBOSCRUBBER® ensures reliable and consistent operation without any increase in gas side pressure drop. Sea water is used during the rare periods when process slurry is unavailable. The system is integrated with the plant process control system to ensure optimum operation. A screen shot from the control system is shown below.

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System Details

Mass Transfer
Particle Transfer
Heat Transfer
Fluid Dynamics
Tower Design
Gas Absorbed
SO2
Particulates
KCI salt crystals and fine carbon (soot)
Inlet Gas Temp.
174ºC
Gas Flowrate
50,000 m³/hr
Column Dia.
2.3m
Liquid Medium
KCI/NaCI Slurry or seawater
Mean Particle Size
2.5 micron
% Approach Temp.
87%
Operating Mode
Once Throu'

Overall Height

8.5m
Inlet Concentration
300 ppm
% Removal
99%
Heat Transfer Rate
4.1 MW
Pressure Drop
1600 Pa
Construction Material
Mild Steel, Glass flake Coated
% Absorbed
99.8%

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CASE STUDY: VAW Stade, Aluminum Smelter Offgas Particulate Removal

In operation since the late 1980's these six large Turboscrubber® units efficiently handle a combined total gas flow of 1.5 million Am3/hr from several banks of primary aluminum smelter pots. A considerably cheaper option than bag filters on this scale the scrubbers simultaneously remove a fine particulate mixture comprising Al2O3 and combustion products as well as HF gas.

 

System Details

Mass Transfer
Particle Transfer
Heat Transfer
Fluid Dynamics
Tower Design
Gas Absorbed
HF
Particulates
AL203
Inlet Gas Temp.
80ºC
Gas Flowrate
260,000 Am³/hr
Colunm Dim.
7m x 4m
Liquid Medium
Water/Alkaline Solution
Mean Particle Size
1.7 micron
% Aproach Temp.
93%
Operating Mode
Recycle/ Bleed

Overall Height

30m
Inlet Concentration
50ppm
% Removal
85%
Heat Transfer Rate
3600 kW
Pressure Drop
800 Pa
Construction Material
Plastic lined steel
% Absorbed
99%

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CASE STUDY: William Blythe, Dual SO2/Particulate Duty

Installed in early 1996 this Turboscrubber® unit simultaneously scrubs fine Sodium Metabisulfite dust and SO2 gas, from dryers, to high efficiencies. The plant can be operated under either batch or pH control using a caustic soda solution whilst taking care to avoid equilibrium problems possible due to the liberation of SO2 during the dissolution of Na2S2O5. The unit was supplied with standby fans and pumps to avoid unnecessary production shut downs .

 

System Details

Mass Transfer
Particle Transfer
Heat Transfer
Fluid Dynamics
Tower Design
Gas Absorbed
SO2
Particulates

Na2 S2 O5

Inlet Gas Temp.
60ºC
Gas Flowrate
7000-17000 m³/hr
Column Dia.
1.15m
Liquid Medium
NaOH
Mean Particle Size
1 micron
% Approach Temp.
96%
Operating Mode
Recycle

Overall Height

7.2m
Inlet Concentration
2000ppm
% Removal
98%
Heat Transfer Rate
50 kW (reaction)
Pressure Drop
up to 3000 Pa
Construction Material
PP, GRP reinforced
% Absorbed
99.9%

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CASE STUDY: Wyeth Nutritionals, Boiler Flue Gases

Commissioned in the winter of 1997 this TURBOSCRUBBER® unit simultaneously scrubs fine soot particles (product of HSFO fuel boilers), absorbs SO2 gas, and recovers waste heat. The scrubbing medium is process effluent which typically has pH 8 to 12. This effluent was originally neutralized with acid (HCl) before discharging via a biological treatment plant. The operation of the TURBOSCRUBBER® is set such that the SO2 removal from the boiler flue gases is controlled to match that required to both naturalize the process effluent (without further chemical treatment) and maintain emission levels below legislative requirements.

The unique non-clogging feature of the TURBOSCRUBBER® ensures reliable and consistent operation without any increase in gas side pressure drop.

 

System Details

Mass Transfer
Particle Transfer
Heat Transfer
Fluid Dynamics
Tower Design
Gas Absorbed
SO2
Particulates

Fine Carbon (soot) from oil firing

Inlet Gas Temp.
135ºC
Gas Flowrate
41,000-82,000 m³/hr
Column Dia.
2.35m
Liquid Medium
Process Effluent
Mean Particle Size
2 micron
% Approach Temp.
98%
Operating Mode
Recycle with variable bleed & make-up

Overall Height

9.8m
Inlet Concentration
800ppm
% Removal
97%
Heat Transfer Rate

400 kW (typical)(4MW potential)

Pressure Drop
1000 Pa (typical)
Construction Material
Mild Steel Glass Flake coated
Outlet Concentration
Controlled at 150 ppm (typical)

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CASE STUDY: NOx Removal, Rhone Poulenc Biochimie

FTL/Osprey custom design, build & commission NOx scrubbing systems to be operated with either alkaline reagent (NaOH) or powerful oxidant (H2O2). TurboScrubber's high mass transfer performance allows for fabrication of compact towers thereby helping to minimise space requirements & capital costs.

Existing NOx scrubbers can easily be retrofitted at low cost to higher efficiency towers using the new Turbo-Pak fluidised bed packing range. The picture on the right shows a tower in Northern France retrofitted from fixed bed (Pall rings) operation & later upgraded further to ensure optimum efficiency in the same confined space

 

Other Turboscrubber® Users:

A.P.H./Wyeth, Ireland
Amoco. USA
Callidus/Shell, U.K
Cito, Germany
Cleavland Potash, U.K
Corning, U.K
Dakota Gas. USA
Delta. USA
E. R. M. USA
Engelhard, U.K
Geocore. USA
Groundwater Technology. USA
Hoechst, Germany
Kaneb Pipeline Co. USA
Kraft. USA
Mars, France
Montgomery Watson. USA
North British Distillery, U.K
Northern natural Gas. USA
Octel, U.K.
Raytheon. USA
Rhone Poulenc, France
Sasol, South Africa
Scott Ltd., U.K
Seacor. USA
Texaco (Star). USA
US Steel. USA
VAW, Germany
Waste Management. USA
William Blythe, U.K.

 

Updated by photo-design.co.uk