Rotary vacuum filter

The rotary vacuum filter is designed to clarify highly charged liquids, such as white must must and wine lees. It works by continuously scraping the filter layer attached to a rotating drum that is partially immersed in the tank containing the liquid to be filtered.
The liquid to be filtered is drawn through the adjuvant layer on the drum, forming a filter cake that is then scraped to remove the retained particles. Precise adjustment of rotation speed, vacuum level and knife feed are essential to optimise filtration and minimise losses.

Rotary vacuum filter

This equipment is designed for the clarification of highly charged liquids: white must lees, wine lees, early wines, press wines. The operating principle is the complete opposite of that of filtration using continuous alluvial filters: the initial filter layer is scraped continuously, so clogging is non-existent and the hourly flow rate is virtually constant throughout the filtration process.
Rotary vacuum filter diagram
Diagram of a rotary vacuum filter

Main components

Vacuum

This is produced by 1 or 2 "liquid ring" pumps which ensure a constant vacuum inside the drum. The vacuum created sucks the liquid through the layer of additive.

The drum

The drum is cylindrical and covered with a stainless steel reps mesh filter cloth. It rotates at an adjustable speed around its horizontal axis. It is partially immersed in a trough fitted with an agitator.
  • Sector drums: The drum is divided into sectors that do not communicate with each other. The filtrate is evacuated using the vacuum pump to an independent collector which separates the air from the liquid.
Diagram of a rotary sector vacuum filter
Diagram of a rotary sector vacuum filter
Rotary sector vacuum filter
Rotary sector vacuum filter
 
  • Full vacuum drum : The drum is not divided, it is completely evacuated. The filtrate is transferred directly to the storage tank by means of an extraction pump immersed in the lower part of the drum.
    In this case, there is a separation between evacuation of the drum and extraction of the filtered liquid (limited oxidation).
Diagram of a full vacuum rotary drum filter
Diagram of a rotary vacuum drum filter

The sizing tank

This is fitted with a stirrer to ensure that the water/additive mixture is homogeneous.
Its volume should be proportional to the surface area of the filter.

The scraper tank

This removes the clogged layer throughout the filtration process.
Scraper
Scraper

The control panel

It manages the following settings, among others:
  • Drum rotation speed
  • Knife advance
  • Vacuum level

Cake formation

After filling the sizing tank with water, the filtration aid (perlite or diatomaceous earth) is added.
To ensure perfect hydration and a homogeneous mixture :
  • the quantity of filter aid should not exceed 5% of the total volume of the tank,
  • It is important to agitate the water-adjuvant mixture for the time recommended by the manufacturer before transferring it to the filtration trough.
Vacuuming the rotating drum enables the filter aid to be fixed to the reps cloth; with each revolution, a layer of filter aid is deposited on the drum.

To obtain a stable filter layer, it is necessary to :
  • maintain an optimum liquid level in the trough,
  • maintain optimum drum rotation speed,
  • limit the drying out of the filterlayer at the end of the process.
The thickness of the precoat varies according to the application and depends on the quantity of filter product used.

Indicative maximum values
  • perlite: 20 kg/m²
  • diatomaceous earth: 30 kg/m²
Note: once the additive has been completely deposited on the drum, it is important to level the whole area using the scraper, in order to eliminate any imperfections in the filter cake.

Filtration control

The liquid to be filtered is fed into the filtration trough by the feed pump.

Under the action of the vacuum, the liquid to be filtered passes through the filter cake. The particles to be retained are stopped at the surface of the cake, forming a more or less fine film . After drying, this film is removed by the scraper blade. Its purpose is to continuously remove the undesirable products deposited, as well as a tiny part of the additive layer. This regeneration of the filter medium limits clogging.
 
Note : deep pollution of the filter cake leads to a reduction in flow rate. To remedy this, the feed rate of the scraper can be increased.

The following diagram shows that the surface of the drum during operation is divided into four different zones:
Different zones on the filtration drum
Different zones on the filtration drum
  1. filtration zone equal to the surface of the submerged part
  2. drying zone (approximately 2/3 of the total surface area)
  3. scraping zone
  4. regenerated sizing zone ready for immersion

Filtration parameters

Vacuum level

This can vary from -0.2 to -0.8 bar (approximately -200 to -800 mm Hg).
Rotary vacuum filters operate at a more or less constant differential pressure. In the specific case of musts, this is maintained at around -0.4 bar.

Drum immersion

This can vary between 20 and 50% of the total surface area. Increasing the level of immersion increases the actual filtration surface but reduces the surface area for drying residues.
 

Drum rotation speed

Drum rotation speed can vary from 0.2 to 5 rpm.
Increasing the speed of rotation increases the specific flow rate of the product to be filtered and, at the same time, increases residual moisture and wine losses, as the drying phase is reduced.

The graph below shows the optimum range of rotation speeds : this is the compromise between an acceptable specific flow rate and sufficient drying.
Vacuum filter rotation speed curve

Level of scraping

The aim is to remove the clogged layer with a minimum of filter media.
The knife feed rate can vary from 1 to around 30 mm per hour.

Optimising the scraping level means ensuring :
  • a correct cycle length
  • minimum consumption of filter media
     
Other variables come into play, such as
  • the % of particles in suspension (load)
  • the clogging capacity of the liquid to be filtered
  • the type of filter aids used
     
It is difficult to establish a general rule on the correlation of the above operational parameters.

Product to be filtered

Flow rate hL/h/m

Quantity of additive kg/hL

White musts, rosés, press wines

4 - 6

0,5 - 0,7

Cold settling sludge

3,5 - 4

0,8 - 1,0

Muted sludge

3 - 4

0,8 - 1,2

Raw red wines, primeur

6 - 8

0,3 - 0,4

Racked red wines

10 - 12

0,15 - 0,25

Fermented lees

1 - 2

1,5 - 1,7

Table: Average flow rates and consumption of filter products

Choosing the right equipment

Determining the most suitable filtering surface for a given production unit requires a whole series of technical, economic and practical parameters to be taken into account. To do this, a case-by-case study should be carried out with a professional.

Resolving malfunctions

The layer is cracked

  • Drying out too quickly
- Increase drum rotation speed
- Reduce the vacuum level if necessary
- If necessary, increase the liquid level in the trough
  • The admixture is unsuitable
- check adjuvant characteristics

The cake is irregular or inhomogeneous

  • The reps is scaled
- descale the entire drum
  • The percentage of soil is too high in relation to the volume of water
- rebalance the quantity of admixture to the volume of the tank

The layer is falling off

  • The quantity of admixture per m² is too high
- rebalance the quantity of adjuvant to the surface area of the filter

The flow rate is too low or drops

  • The knife feed rate is incorrectly adjusted
- increase the feed rate
  • The rotation speed is unsuitable
- Increase the rotation speed
  • The additive is too fine
- Adapt the additive to the product to be filtered

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