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BHS Filtration
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Vacuum belt filter

General Description

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The BHS-vacuum belt filter can be used for separating sedimenting and abrasive solids from suspensions with little wear. The various filtrates are separated exactly and without intermixing. If required, the filter cake can undergo further treatment in the form of multiple reverseflow washing, suction drying or pressing. vacuum belt filter

Technical Description

BHS-vacuum belt filters are continuously operating, pneumatically driven horizontal vacuum filters. A circulating belt, moving in cycles, is the filter medium. The suspension is fed continuously or in batches onto the belt, the filtrate is sucked away from below. The filter cake forms on top of the belt and under-goes further treatment in the form of washing, extraction, suction drying or pressing. With very little vacuum loss, the belt is stationary during filtration process. When the belt moves forward, the vacuum trays are vented so as to ease strain on the belt.

Vacuum trays

The vacuum trays are divided into zones corresponding the length of belt feed. Supporting grids with large open sections are provided in the vacuum trays to support the belt.

Filtrate drain

Each individual zone in the vacuum trays is separately connected to the filtrate manifold. The filtrate manifold is divided up in line with the zones for filtrate separation. Rapidly opening and closing shut-off valves cut out the vacuum when the belt advances and vent the filtrate chamber.

Belt conveyance

The continuous, circulating filter cloth belt is moved in cycles by pneumatic cylinder and conveyer roller. While the belt is stationary, vacuum is applied to the trays, holding the belt in place. The length of cloth moved forward corresponds exactly to one zone length and is taken from the belt storage device. The return movement is completely free from strain.

Suspension delivery

The suspension is delivered from a stationary distributing facility. An oscillating delivery unit can be provided for heavily sedimenting sus-pensions.

Cake washing

Washing media are delivered by spray systems or distributing channels. The delivery units can be positioned with precision on the vacuum trays.

Cake discharge

Part of the cake is removed during forward feed, the remainder when the extraction roller travels back. A mechanical scraper removes any cake re-sidue still adhering to the cloth.

Cake pressing

A pressing plate is pneumatically or hydraulically pressed onto the cake for one cycle unit. Compressed air or hot air is additionally blown through the cake.

Drying

Following the normal filtration, washing and dewatering stages, it is possible to apply a variety of drying systems to dry the product.

Confildry

The Confildry version consists of heatable upper rams and heatable vacu-um trays. Hot gas can also be drawn through the cake. This produces a high level of heat transfer, resulting in efficient drying.

Criteria / demands

The BHS vacuum belt filter can be used to good effect where the following criteria need to be met:

  • Several consecutive process steps
  • Enclosed gastight production
  • Fully automatic operation
  • Temperature up to 95°C
  • Dewatering by mechanical expression up to 6 bar
  • Filter cake drying

Encased filters

To meet customer specifications, various types of encased filters are available:

  • simply hood type
  • with closed hood over the entire filter
  • closed box type
  • gas- and pressure tight box type
  • pharmaceutical type

Normally, an encased box type will be used here, with particular attention focused on surface quality (Ra up to 0.8µ), processing directives (GMP) and the use of permissible materials (FDA).

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Applications

  Pharmaceuticals
 
  • Drug filtration
  • Penicillins
  • Fermentation solutions
  • Semi-synthetic antibiotics

 
Foodstuffs
 
  • Flavouring extraction
  • Citric acid
  • Ascorbic acid
  • Pectins
  • Cakoa butter

 
Environmental technology
 
  • Gypsum from flue gas desulphuration
    plants
  • flue ash from waste incineration
    plants

 
Dyestuffs
 
  • Initial and intermediate products
  • AZO dyestuffs
  • Pigments
  • Phthalocyanines

 
Chemicals
 
  • Detergent additives
  • Organic and inorganic additives
  • Precipitation residue
  • Active carbon
  • Heavy metal salts

 
Zeolites
 
  • Alumina
  • Ion exchanger
  • FCC

 

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Technical Data

  type Belt width
in m
Effective filter area
in m
Dimension (WxHxL)
in m
Air consumption (m3/h)
at 6 bar
   LBF 0,1 0,1 0,2 x 0,6 x 1,5 1,5 - 2   
   BF 2,5   0,25 0,8 - 1,6 1,3 x 1,7 x 5,0 - 8,3   10 - 15
   BF 5 0,5   1,5 - 5,25 1,8 x 1,9 x 5,4 - 12,9 15 - 20
   BF 10 1,0   3,0 - 12,0 2,3 x 1,9 x 5,4 - 14,4 25 - 40
   BF 15 1,5   6,0 - 24,0 2,8 x 1,9 x 6,5 - 18,5 35 - 50
   BF 20 2,0   8,0 - 32,0 3,3 x 1,9 x 6,5 - 18,5 50 - 70
   BF 25 2,5 18,0 - 45,0   3,8 x 1,9 x 11,0 - 22,0 100 - 120
   BF 30 3,0 30,0 - 60,0   4,3 x 1,9 x 10,0 - 20,0 150 - 250
   BF 35 3,5 40,0 - 75,0   4,8 x 1,9 x 15,0 - 22,0 180 - 300

Materials

  • Filter cloths: PP, PE, PVDF, Luxilar, PA
  • Components contacting the product: special steels, PP, PVDF
  • Seals in all common sealing materials

Technical data may change due to technical progress. Subject to modification without notice.

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