Patent Application
20200094171
The present invention relates to an apparatus and method for filtering any liquid through a filter material in order to remove pollution from the liquid in a single upright filtration tank.
Today's methods for filtering liquids are as follows:
All methods are intended to remove pollution in a liquid
The cartridge filter has a woven filter cartridge with a specific opening for letting the liquid pass through. All particles bigger than the defined mesh size will be stopped in the filter cartridge. The filter cartridge must be replaced when the filter cartridge is saturated with particles
The drum filters have the filter material fixed to the inside of a drum shaped container. Liquid is introduced into the drum and the drum is rotating. The particles bigger than the mesh in the filter is stopped on the inside of the filter and is scraped of once during every rotation. The pollution in the filter drum is discharged.
Membrane filters works by pressurizing a liquid through layers of membranes and the clean liquid passes through the membrane. The pollution will be led out an opening for consecrated pollution.
Mineral filters have often a cartridge or manual filled filter material containing minerals such as clay. The liquid is forced through the minerals in the filter and leave the pollution in the minerals. The minerals have to be replaced when saturated with pollution
All known filtration methods are targeting to extract pollution from a liquid.
U.S. Pat. No. 3,786,923 A disclose that a filter-adsorption media, such as activated carbon, is supplied to one end of a screw conveyor having a variable pitch along its length with the greater pitch being at the supply end. Sewage, such as from a marine toilet, is passed through a macerator and chemically treated before being introduced into the central portion of the screw conveyor to be mixed with the filter-adsorption media and compacted as the screw conveyor is rotated. The compacting produces a mixture of filter-adsorption media and sludge at the discharge end while the liquid is passed through the conveyor in counter-flow relationship, to the incoming filter-adsorption media and through the filter-adsorption media, and then to a discharge.
GB 2052469 A disclose a cleaning filter that has a cylindrical tank through which an axial pipe extends, the pipe having a screw blade attached thereon and being rotatable in the tank. A drum rotatably carried on the axial pipe is disposed within the tank and around the screw blade, the drum having a cylindrical body and an end cover mounted on the cylindrical body such that the cylindrical body is rotatable relative to the end cover. The end cover has a cleansing agent inlet and a cleansing agent outlet with the cleansing agent being removed from the drum by rotating the pipe means and the screw blade, the latter engaging the cleansing agent in the drum to thereby move the cleansing agent axially to the cleansing agent outlet. A filter is disposed on the outer periphery of the cylindrical body of the drum so that when the liquid to be cleaned flows into the tank from an inlet and is discharged through an outlet on the axial pipe, the liquid passes through the filter and the cleansing agent in the drum to thereby remove impurities from the liquid.
US 2003010699 A disclose a filtration apparatus comprising a container that houses a filtration tank to which contaminated water is supplied, a cleansing tank, and a screw conveyor disposed within said cleansing tank. Filtration media is housed within the cleansing tank and the container. The cleansing tank has lateral surface openings, lower openings, and an upper opening. When the screw conveyor rotates, filtration media as well as water (contaminated water) is conveyed upward from the lower openings to the upper opening while being agitated. At the same time, filtration media circulates between the cleansing tank and the container and is cleansed. When cleansing is complete, a backwash water supply pump backwashes water, and expels contaminants separated and removed from the filtration media out of the container by an expulsion pump. Lateral surface doors close lateral surface openings by drive means only during cleansing (agitation). This structure increases the filtration area.
EP 1683561 A1 disclose a filtration device equipped with: a filtration tank; a layer of particulate activated carbon within the filtration tank; a cleansing tank, which is vertically placed within the filtration tank and which has an opening at the lower end thereof; and the screw conveyor for cleansing the filtration media, which is provided within the cleansing tank. The screw conveyor has a shaft, which is suspended within the filtration tank from above. The upper portion of the shaft is driven, and the lower portion of the shaft is supported by an axial support section, which is fixed to the lower portion of the cleansing tank. The axial support section is equipped with a frictional wear compensating mechanism at a portion thereof at which the shaft and the axial support section contact each other.
JPS55100898 A disclose separation of water and solids by suction-filtering material in a treating tank with a tubular filter, discharging the remained treating material to the outside of the tank with a screw conveyor and sucking the residual water leaching out from the discharge route into the tubular filter. When the treating material such as sludge is pressure-fed into a treating tank through lead-in port, the fine granular solids and water leaches into a tubular filter through its water feed port of the filter and the treating material leaches in that state into the filter from the open bottom surface of the filter. Next, when the revolving speed of the revolving shaft increases, the solids in the filter are flown toward the inside wall surface by centrifugal force and drop into the tank and remain there. The water content in the filter is sucked through suction hole into suction barrel and is discharged through a discharge pipe and discharge housing. On the other hand, the revolution of a screw causes the treating material in the bottom of the tank to be conveyed upward in a conveying barrel, where it is compressed and the squeezed out water content passes through the water feed port through the through-hole and is fed into the filter.
The method and filtration apparatus according to the invention differs from the known methods by being a continuous filtration method contrary to the known methods which are batch methods, and where the filter insert have to be replaced. The in-line filtration invention may result in a filtration process:
It is thus an object of the present invention to provide an apparatus and method for a basically continuous filtration process, in where there is no need for cleaning of the filtration tank. The invention will also give the flexibility to change to a new/different filter material type in short time, thus making it possible to change filtration characteristic for a different liquid or pollution.
It is at least an object to provide an improved apparatus and method for continuously filtering of liquid.
According a first aspect of the invention, a method for filtering a liquid through a filter material is provided, comprising the steps: feeding of fresh filter material via a fresh filter material inlet in a lower part of the filtration tank, feeding of polluted liquid via a liquid inlet in an upper part of the filtration tank, mixing of the filter material and the polluted liquid in the single upright filtration tank to filter the polluted liquid by conveying filter material from the lower part of the filtration tank to the upper part of the filtration tank, discharge of used filter material through an upper used filter material outlet in the upper part of the filtration tank, and discharge of clean liquid from the filtration tank through a lower clean liquid outlet in the lower part of the filtration tank.
Filter material can be continuously conveyed from the lower part of the filtration tank to the upper part of the filtration tank by a screw conveyer, and polluted liquid is pumped in through the liquid inlet in the upper part of the filtration tank at a temperature that together with the filter material ends up at desired filtering temperature in the filtration tank.
Alternatively, filter material can be semi-continuously conveyed from the lower part of the filtration tank to the upper part of the filtration tank, in that filter material for a complete filter batch is fed into the filtration tank, and conveyed up in the tank by a screw conveyer, and polluted liquid is pumped in through the liquid inlet in the upper part of the filtration tank at a temperature that together with the filter material ends up at desired filtration temperature in the filtration tank.
The time to convey the filter material from the lower part of the filtration tank to the upper part of the filtration tank can be set to a time which optimizes the use of the filter material before it is saturated, such as approximately 60 to 500 minutes.
Liquids can be circulated from the lower part of the filtration tank to the upper part of the filtration tank in a sparging loop comprising a circulation pump.
Further, polluted liquid can be heated or heat is maintained in the sparging loop by a heat exchanger.
Used filter material can be discharged through the upper used filter material outlet when the filter material is saturated.
Fresh filter material feed via the filter material inlet to the filtration tank can be at least one of clay, activated charcoal, moss, sand, sintered glass, or ceramic filter material.
According to a second aspect of the invention, a filtration apparatus for filtration of liquids is provided, comprising a single upright filtration tank for holding liquid and filter material, said filtration tank having a lower part with a lower fresh filter material inlet and a lower clean liquid outlet, an upper part with an upper used filter material outlet and an upper liquid inlet for polluted liquid, wherein said filtration tank further comprises an internal conveyer for feeding of filter material from the lower part of the filtration tank to the upper part of the filtration tank.
Said conveyer can be a screw conveyer. Further, the filtration tank can be an upright circular-cylindrical cylinder, and the conveyer a vertical screw conveyer located inside the filtration tank.
The lower part of the filtration tank may comprise a screw conveyer for feeding of fresh filter material from the filter material inlet to the interior of the filtration tank. A filter material hopper can be located above the screw conveyer in the filter material inlet.
The upper part of the filtration tank can also comprise a screw conveyer for feeding of used filter material from the interior of the tank to the used filter material outlet.
The filtration tank may further comprise a circulation pump for creation of a sparging loop, where the liquid is circulated from the lower part of the filtration tank to the upper part of the filtration tank. A heat exchanger to heat or maintain heat in the liquid during the filtration process can be included in the sparging loop.
Embodiments of the present invention will now be described, by way of example only, with reference to the following diagrams wherein:
The upright filtration tank 12 further comprises an internally and vertically placed conveyer, preferable a screw conveyer 24, for transport of filter material, and liquid, vertically in the filtration tank 12.
Each screw conveyer 24,26,28 are preferable driven by an adjoining drive motor (not shown), and connected to a control system. The filter material inlet 16 can also be connected to the same control system. The same applies to the clean liquid outlet 20 and used filter material outlet 18. All parts of the apparatus 10 may be connected to said control system, thus providing an automatic filtration process.
The method according to the invention may include two filtration processes.
A first idea of the present invention is to have a continuous filtration process instead of batch process. This is done by feeding the fresh filter material into the lower part 14a of the cylindrical upright filtration tank 12, where the transport screw 24 is located inside. The time to move the filter material, by the screw 24, from the bottom 14a of the filtration tank 12 to the top outlet 18 for used filter material in the upper part 14b of the filtration tank 12, is preferable equal to the time for saturating the filter material (normally 60-500 minutes). In the upper part 14b of the single upright filtration tank 12 the polluted liquid will be pumped in through the liquid inlet 22 at a temperature that together with the filter material ends up at the ideal filtration temperature in the filtration tank 12. The outside of the filtration tank 12 can be heat traced if required. When the filter material, injected in the bottom 14a of the filtration tank 12, meets the polluted liquid it will filter the pollution in the liquid. In the bottom the filter material will have the maximum ability to absorb pollutions and in the top, near the exit, it will have the minimum ability to absorb pollutions. The liquid will have its maximum pollution in the top of the tank 12 and its minimum pollution in the bottom of the tank 12, near the exit. The volumetric flow and the filter material vs. the volumetric flow of the polluted liquid will give the efficiency of the filtration. If required the apparatus 10 can be equipped with the sparging loop 36 where the polluted liquid can be circulated from the bottom of the filtration tank 12 to the top of the filtration tank. If required this loop can pass the heat exchanger 34 to heat or maintain heat during the filtration process. The cleaned liquid will be taken out in the bottom of the filtration tank 12 through the clean liquid outlet 20 and the used filter material will be discharged in the top of the filtration tank 12 through the used filter material outlet 18.
A second idea of the present invention is to have a semi-continuous filtration process instead of a batch process. This is done by feeding the fresh filter material into the lower part 14a of the single upright filtration tank 12, where the transport screw 24 is located inside. The filter material for a complete filtration batch will then be screwed up to a level in the filtration tank 12. In the top of the filtration tank 12 the polluted liquid will be pumped in through the liquid inlet 22 at a temperature that together with the filter material ends up at the ideal filtration temperature in the filtration tank 12. The outside of the filtration tank 12 can be heat traced if required. If required the apparatus 10 can be equipped with the sparging loop 36 where the liquid can be circulated from the bottom 14a of the filtration tank 12 to the top 14b of the filtration tank 12. If required this loop 36 can pass the heat exchanger 34 to heat or maintain heat during the filtration process. When the filtration batch is completed the clean liquid is drained out in the bottom 14a of the apparatus 10, through the clean liquid outlet 20, and the used filter material is discharged at the top 14b through the used filter material outlet 18.
Fresh filter material feed via the filter material inlet 16 to the filtration tank 12 can for instance be picked from a group of: clay, activated charcoal, moss, sand, sintered glass, or ceramic filter material. The filter material can be at least one of said materials, or a combination of materials. Other filter material may also be used.
| Number | Date | Country | Kind |
|---|---|---|---|
| 20170832 | May 2017 | NO | national |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/NO2018/050132 | 5/22/2018 | WO | 00 |
