Special Applications & Considerations - Swirl Fluidizer

Swirl Fluidizer
Drying of filter cakes, pastes, and sludges

When producing powders of fine size from aqueous suspensions, it is a distinct advantage to first mechanically dewater so as to reduce the plant installation and operating costs of the final drying stage.

During dewatering, suspensions are converted to either filter cakes, pastes or thick viscous liquids, sometimes in the form of sludges.

Drying of such materials is ideal in the Nitro Swirl Fluidizer. This is a continuous one stage drying plant that can produce a fine particled powder without the need for back-mixing powder with feed material, a feature of more conventional technology, i.e. flash drying. The Swirl Fluidizer operates with very short product and air residence times and thus permits high production rates in small compact units.

There is an extensive range of materials suitable for Swirl Fluidizer drying, and further details are given below. Plants can be supplied in pilot or industrial size, both of which meet environmental and safety requirements. The Swirl Fluidizer process can be demonstrated at Niro's comprehensive test station facilities. Here feed and powder properties can be investigated and industrial plant specifications determined. The Swirl Fluidizer has already been proven over long periods of operation – a clear sign of Niro's unique drying experience and dedication to solving specific drying needs with customers.
 

Drying Process

Process advantages
The Swirl Fluidizer offers a number of important advantages when viscous liquids, sludges, pastes and filter cakes must be converted into powders:

  • Continuous operation
  • One stage drying
  • Compact layout – robust design
  • Effective heat and mass transfer – short drying times
  • Negligible heat loss – high thermal efficiency
  • Easy access and cleaning

Drying chamber
The heart of the drying process is a cylindrical drying chamber consisting of three important components: an air disperser, a rotating disintegrator, and a drying section.

The hot drying air enters the air disperser tangentially, and with the use of an advanced guide vane arrangement is introduced into the drying section as an intense, controlled swirling air flow. The rotating disintegrator is mounted at the base of the drying section. Under the influence of the disintegrator operation and swirling air flow, a feed comminution and drying process takes place, and the resulting dry fine particles pass out with the exhaust air for collection in a bag filter.

Disintegrator speed controls the degree of comminution, and hence particle size.

As the air residence time in the drying section is very short, typically 1-2 seconds, the Swirl Fluidizer is always a compact unit.

Feed system
Feed enters the feed tank under level control. The tank is fitted with a slowly rotating impeller which provides the base mounted dosing unit with a constant feed supply.

The rheological properties of the feed determine the design of the dosing unit. This can be a screw feeder or pump. The dosing rate to the dryer controls the outlet air temperature at a fixed level, which in turn ensures that the powder collected from the bag filter has a constant residual moisture content.

Hot air system
The drying air is heated either directly or indirectly, depending upon the feed material, the specified powder properties, and available fuel source. The heat sensitivity of the product determines the drying air temperature. The highest possible value is used in the interest of optimizing thermal efficiency

Powder discharge and exhaust air system
A bag filter is usually recommended for collecting the fine particles produced. The exhaust fan maintains a slight vacuum in the dryer, thus preventing powder leakage into the surroundings.

 

Typical Products Dried

Catalysts
Ceramics
Dyestuffs
Pigments
Inorganic chemicals
Organic chemicals
Zeolites
Kaolin

Dryer Selection

NIRO offers a range of dryer designs. The selection of the most suitable dryer depends upon feed solids, the rheology of the feed material, and desired powder properties, but any dust explosion and oxidation hazard can be handled, irrespective of dryer type. Testwork on the given feedstock is always recommended to confirm plant design.

Swirl Fluidizer
Solids properties: Insoluble, amorphous or crystalline fine particles
Feed characteristics: Viscous liquid, sludge, paste, filter cake, semi-dry powder Solids consisting of small particles insoluable in water or solvent
Powder characteristics: Fine particles of average size < 20 microns

Spray Dryer (Special literature available)
Solids properties:

  • Soluble or insoluble, often heat sensitive, thermoplastic and/or hygroscopic
    Feed characteristics:
  • Pumpable solution, suspension, emulsion, paste
  • Solids in water or solvent
    Powder characteristics:
  • Individual particles of average size in the range 20-300 microns, free- flowing, dustlees agglomerates or granulates of average 150-500

    Fluid Bed Dryer (Special literature available)
    Solids properties:

  • Soluble or insoluble, often heat sensitive, thermoplastic and/or hygroscopic
    Feed characteristics:
  • Friable filter or centrifuge cake, wet powder consisting of crystals, agglomerates, granules, pellets where average particle size is in the range of 50-5000 microns
  • Aqueous or solvent wet solids
    Powder characteristics:
  • Powder has approximately the same particle size as original feed

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