Without verbal explanation the information on this document is incomplete
Fluidized-bed drying with superheated steam
Jochen Gaßmann, Mirko Löhn, Hartmut Hafemann
BMA Braunschweigische Maschinenbauanstalt AG Braunschweig, Germany
Steam drying
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…has been proven in a number of practical applications■
…takes place in a pressurized fluidized bed■
…uses superheated steam instead of hot air for fluidisation and drying■
…provides excess steam by evaporation of the product water■
…should be integreated into the energy system of a factory■
…is characterized by multiple use of primary energyOperating principle
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Main components(1) product feed system
(3) fuidized bed
(4) pruduct discharging system (6) rotary dust separator
(8) vapour discharge (9) heat exchanger (10) fan 1 3 4 6 8 9 10
Integration into an energy system (pulp drying)
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Main processes (1) steam generation (2) power generation 1 2 3 4(3) pressurized fluidized-bed steam drying (4) utilization of the excess steam
Advantages
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The vapour produced during drying has a high energy content.■
This energy potential can be used for downstream processes.■
Because of the closed system emissions can be avoided.■
No air pollution by dust and odours.■
No loss of product.■
Oxygen-free steam atmosphere prevents oxidative reactions.■
Volatile substances can be removed and recovered by condensation.■
Optimum conditions for sterilisation prozesses.New applications – Necessary investigations
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Assessment of the properties of the wet product before steam drying■
Investigation of flow characteristics■
Investigation of drying kinetics■
Assessment of product properties after the steam drying process In order to carry out such studies appropriate test equipment isTest unit fluidized-bed steam dryer
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Parameterbatch-wise operating device batch size: 0,5 to 2 kg
fluidized-bed: d = 200 mm
fluid velocity: up to 8 m/s
working pressure: up to 4,5 bar process temperature: up to 210 °C
Technological principle test unit
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Main components1
feeding lock system2
dryer3
fluidized bed with perforated plate4
steam injection5
discharge lock system6
cyclone for dust separation7
dust discharge8
fanDrying kinetics
Wheat stillage 120 130 140 150 160 170 180 190 200 0 60 120 180 240 300 Zeit [s] Zeit [s]Zeit [s] Zeit [s] T e m p e ra tu r [ ° C ] T e m p e ra tu r [ ° C ] T e m p e ra tu r [ ° C ] T e m p e ra tu r [ ° C ] Dampfeinlass Erweiterungsteil WS oben WS unten 120 130 140 150 160 170 180 190 200 210 T e m p e ra tu r [ ° C ] T e m p e ra tu r [ ° C ] T e m p e ra tu r [ ° C ] T e m p e ra tu r [ ° C ] Dampfeinlass Dampfeinlass Dampfeinlass Dampfeinlass Erweiterungsteil Erweiterungsteil Erweiterungsteil Erweiterungsteil WS o ben WS o ben WS o ben WS o ben WS unten WS unten WS unten WS unten eff. Dampftemp. eff. Dampftemp. eff. Dampftemp. eff. Dampftemp.■
Temperature profiles depend on the product characteristicsResults of steam drying tests
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Dried materials of different structures andcomposition after drying (reference particle d=5mm)
Wood chips
200°C, v=4 m/s, p=2 bar
Results of drying tests
Corn stillage 180°C 5 Min 1 bar 160°C 6 Min 1 bar 160°C 6 Min 2 bar 160°C 6 Min 3 bar 180°C 5 Min 2 bar 180°C 5 Min 3 bar 180°C 5 Min 4 bar 200°C 4 Min 3 bar 200°C 3 Min 4 bar 200°C 2 Min 4 bar Wheat stillageFlow characteristics
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The flow test unit represents the elements of a real dryerFlow characteristics
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to investigate the flow behavior during fluidization■
to investigate the efficiency of dust separationSummary
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The aim of the fluidized-bed steam drying technology is the multiple use of primary energy and the reduction of CO2 emissions.■
New applications require the possibility to conduct experiments.■
Investigations according real process conditions are necessary.■
The pressurized steam dryer is an highly efficient multiple utilisation system if integrated in combined plants or in energy networks180 190 200
The installation of the pilot plant was co-financed by Deutsche Bundesstiftung Umwelt (DBU) as part of a research project (Ref.No.: 26568-24/2)