Liquid filtration system

Abstract
A liquid filtration system comprising a filtration tank with: a separating roof on which are mounted groups of hoses fixed to respective support plates; a fluid distributor plate comprising a central portion without perforations, and a peripheral portion with a plurality of perforations, said distributor plate being located between the hoses and a lower inlet duct for the water to be filtered comprising an upper opening for supplying liquid to the holes near the central portion of the distributor plate and a lower opening for supplying liquid to the holes of the peripheral portion which are furthest from the central portion. The filter comprises a filter material, an outlet duct for the filtered water at the upper area of the tank, a regeneration circuit of the filter medium; a filter self-cleaning circuit and a control panel.
Description
OBJECT OF THE INVENTION

The object of the present invention is a liquid filtration system, comprising a filtration tank with a lower inlet for the liquid to be filtered, an upper outlet for the filtered liquid, and inside a series of hoses, whose outer surface forms a support for a filter medium.


TECHNICAL FIELD

The system of this invention is applicable in the field of the purification of all types of liquids with a low or medium load of contaminants and, mainly, for large volumes of water, coming from swimming pools, lakes, ponds or the like.


STATE OF THE ART

Different types of filters are currently known, among which it worth mentioning:


a) Water filters with polyester container, with a filtration surface corresponding to its area or section.


These filters house a filter medium inside that can be silica sand or recycled glass. Water enters the upper part of the container and passes through the filter medium to access tubes with holes or slots allowing the passage of filtered water, which is collected by the lower part of the container. The flow rate of water through the interior of the filter to achieve good filtering quality varies depending on the use of the water, a suitable rate for most uses being 30 m3/hour per square metre of filtration area.


The polyester filter with the silica or glass filter medium has certain advantages such as low cost and diversity of models and sizes, and some disadvantages such as the use of a high amount of water in cleaning the filter, or the need to use numerous units for filtering large water volumes.


b) Steel filters with perlite regenerative filtering medium.


These filters are much more expensive than a polyester filter and have a vertical circular shape with sizes limited by their main characteristic of having a movable upper part and housing in their interior a movable roof from which hang hundreds of hoses, formed by a stainless steel base and coated with polyester mesh that serve as a support for the regenerative filtering medium, called perlite, and provide the filter with a large filtration surface, allowing it to work at low water flow rates with large volumes of water.


The water enters through the lower part of the filter and exits through the upper part after passing through the perlite filtering medium and through the hoses retaining in its interior any particles of dirt greater than 1 to 5 microns.


The useful filtering surface in this case is the area formed by the perlite that adheres to the hundreds of hoses. The movable roof inside has a pneumatic system, called Bump or Bumping, which goes up and down to regenerate the perlite that needs to be removed approximately every 4 hours and renewed approximately once a month. This movement causes the perlite to detach from the hoses.


Cleaning the filter requires manual intervention to leave the hoses perfectly clean. This cleaning is carried out by disassembling a front window of the filter and projecting pressurised water against the hoses, resulting in the waste of a significant amount of water.


A steel filter with hoses and perlite regenerative medium can have filtration surfaces of up to 150 m7 and work at low water flow rates, about 3 m3/hour for each square metre of filtering surface, which makes it possible to obtain a flow rate of about 450 m3/hour of filtered water with a single filter.


These steel filters with perlite regenerative filter medium have certain disadvantages: they must be made of steel because of their movable roof and this makes them very expensive; limited sizes due to their mechanical characteristics and the need to have manholes and removable elements; and the necessary manual cleaning is difficult and arduous and has to be carried out by trained personnel.


c) Polyester filters with regenerative perlite filter medium.


Patent application PCT/ES2018/070356, claiming priority of the Spanish patent ES2690100 B2, of the same applicant of the present invention, describes a filter for the purification of large water volumes, and comprising: a polyester tank with a lower part and an upper part separated by a fixed separating roof; a collector for the inlet and distribution of water arranged in the lower part of the tank, with the water outlets facing downwards, and connected to a water inlet; a lower drain with a valve to remove dirt during cleaning of the filter; a cleaning device comprising a cleaning collector arranged above the collector for the inlet and distribution of water, consisting of a ring of tubes with small jets facing the upper area of the filter, said cleaning collector being connected to pump means for pumping pressurised fluid inwards during the cleaning steps thereof; a plurality of hoses secured to and suspended from the fixed separating roof, said hoses forming a support for the perlite filtering medium; a manhole for the assembly and maintenance of interior components; an upper opening for the outlet and purge of air provided, on the one hand, with air-detecting sensors connected to a control panel and, on the other hand, with a valve for opening and closing for air evacuation, automatically controlled by the control panel based on the signals provided by the probes; and an upper outlet for filtered water.


This filter provides different advantages such as low cost; possibility of having a variety of models and sizes, ability to filter large water volumes with a single unit; automatic cleaning using little water and without the need for specialised personnel.


The applicant themselves have identified some aspects that could be improved in this filter. Specifically, an aspect to be improved in this type of filter is the uncontrolled and sudden entry of water to be filtered from the inlet collector to the hoses, which can cause the perlite filter material to be released from the outer surface of the hoses, overriding or excessively reducing the filtration capacity of the system. This uncontrolled and sudden entry of water can also cause the lower ends of the hoses to hit each other and deteriorate, requiring replacement.


This replacement is an added problem because to make the change of any of the hundreds of hoses included in the tank it is necessary to disassemble the separating roof and remove the plate that covers all the hoses that are attached to it.


DESCRIPTION OF THE INVENTION

The liquid filtration system object of this invention, being of the type described in the aforementioned patent application PCT/ES 2018/070356 of the same applicant, incorporates technical characteristics that solve the aforementioned drawbacks.


Specifically, the invention presents technical characteristics that make it possible to successfully solve the aforementioned drawbacks, with regard to the uncontrolled entry of water to be filtered into the area of the tank in which the hoses and the perlite filtering filler are located, and the difficulty of replacing any of the hundreds of hoses included in the tank.


The system of the invention is of the type comprising: a filtration tank provided with a lower wall, a side wall and an upper wall; —a separating roof dividing the interior of the tank into a lower compartment and an upper compartment; —a pressure inlet duct for the liquid to be filtered towards an area close to the lower wall of said tank, —a plurality of hoses protruding from the separating roof towards the lower compartment, said hoses comprising: an outer surface forming a support for a filter medium, and an inner surface defining a duct, closed at the lower end and opened at the upper end, for circulating the filtered fluid towards the upper compartment, —an outlet duct for filtered water at the upper area of the tank, and—a regeneration circuit for the filter medium.


In order to avoid an uncontrolled and turbulent entry of water into the hoses and the filter medium comprised therebetween, the invention contemplates the incorporation into the tank of a fluid distributor plate, arranged between the inlet tube for the liquid to be filtered and the lower end of the hoses, said distributor plate comprising a central portion without perforations and a peripheral portion with a plurality of perforations for the passage and distribution of the liquid to be filtered towards the hoses.


To achieve virtually uniform distribution of the incoming liquid throughout the horizontal section of the tank, the inlet duct for the liquid to be filtered is arranged horizontally within the tank and comprises: an upper opening for supplying liquid to the holes proximate the central portion of the distributor plate, facing the central portion of the distributor plate, and a lower opening for supplying liquid to the holes of the peripheral portion of the distributor plate, facing a concave lower surface of the filtration tank.


The hoses comprise technical characteristics consisting of the incorporation of reinforcements at their upper and lower ends, further presenting the particularity that all the hoses are divided into independent groups, the hoses of each group being fixed to a support plate removably mounted on the separating roof of the filter tank. This feature allows disassembling any of the groups of hoses from the separating roof and replacing it with another group of hoses, without the need to disassemble the whole of the separating roof, nor the rest of the groups of hoses mounted on it.





DESCRIPTION OF THE FIGURES

In order to complement the description that is being carried out and with the purpose of facilitating the understanding of the features of the invention, the present description is accompanied by a set of drawings wherein, by way of a non-limiting example, the following has been represented:



FIG. 1 shows a schematic elevation view of an exemplary embodiment of the liquid filtering system according to the invention, in which the tank has been sectioned along a vertical plane.



FIG. 2 shows a perspective view of the plate for the distribution of the fluid to be filtered, represented in FIG. 1 inside the tank.



FIG. 3 shows a perspective view of one of the Independent groups of hoses attached to the corresponding support plate and disassembled from the tank separating roof.





PREFERRED EMBODIMENT OF THE INVENTION

In the exemplary embodiment shown in FIG. 1, the liquid filtration system comprises a filtration tank 100 made of resin provided with a lower wall 101, a side wall 102 and an upper wall 103.


A separating roof 104 is mounted in said tank 100 that divides the interior of said tank into a lower compartment 105 and an upper compartment 106.


The tank 100 has a lower draining opening 107 with a drain valve 108 and an upper outlet 109 with a venting valve 110.


It further comprises water detection sensors 111 located in the upper compartment and two pressure sensors 112 connected to a control panel 113. Such pressure sensors 112 detect the differential pressure existing between the lower compartment 105 and the upper compartment 106 of the tank.


The tank 100 has, at its lower end, an inlet duct 200 for the liquid to be filtered towards n area close to the lower wall 101 of said tank and, at its upper end, an outlet duct 300 for the filtered water.


A first valve 204, a pump 203 for pumping liquid into the tank 100, and a second opening and closing valve 205 are mounted on the inlet duct 200 outside the tank 100.


The outlet 300 also has an opening and closing valve 301.


Inside said tank 100, a plurality of hoses 401 protruding downwards from said separating roof 104 towards the lower compartment 105 is arranged.


The outer surface of the aforementioned hoses 401 forms a support of an unrepresented perlite filter medium.


The tank 100 comprises a fluid distributor plate 500 arranged horizontally between the inlet duct 200 and the lower end of the hoses 401.


As can be seen in FIG. 2, said distributor plate 500 comprises a central portion 501, without perforations, and a peripheral portion 502 with a plurality of perforations for passage and distribution of the liquid to be filtered supplied by the inlet duct 200 towards the filter medium fixed externally to the hoses 401.


In FIG. 1, the inlet duct 200 has an upper opening 201 for supplying liquid to the holes in the distributor plate 500 proximate the central portion 501 of the distributor plate 500 and a lower opening 202 for supplying liquid to the holes of the peripheral portion 502 of the distributor plate which are furthest away from the central portion 501. This lower opening 202 faces the lower surface 101, which is concave and guides the liquid projected by said lower opening 202 into the holes of the peripheral portion 502, which are furthest away from the central portion 501 of the distributor plate 500.


In FIG. 1, the path described by the liquid projected by the upper 201 and lower 202 openings of the inlet duct 200 towards the holes of the distributor plate 500 has been represented with a dashed line.


The central portion 501 of the distributor plate 500 has no holes and preferably has a circular shape and a diameter greater than the diameter of the inlet duct 200, thereby ensuring that the water flow projected through the upper opening 201 inevitably hits the aforementioned central portion 501 of the plate that distributes it towards the nearest holes of the peripheral portion 502, preventing it from suddenly or turbulently entering the lower compartment 105 of the tank, in which the hoses and the perlite filter medium are housed.


The hoses 401 included in the tank, which are generally hundreds of hoses to define a large filtration surface, are distributed into independent groups 400, such as that depicted by way of example in FIG. 3.


Each group 400 forms a single, inseparable monoblock assembly comprising several hoses 401 attached at their upper end to a support plate 402 removably mounted on the separating roof 104 of the tank 100; such that each group 400 can be individually disassembled and replaced without the need to disassemble the separating roof 104, or to remove the remaining groups 400 of hoses 401 mounted on said separating roof 104.


The support plate 402 has through holes for mounting fixing screws to the separator roof 104 of the tank 100.


The hoses 401 are closed at their lower end and have protective coatings 405, 406 respectively at the upper and lower ends.


In one exemplary embodiment, the upper end protective coating 405 comprises a retractable polyolefin tube that protects it from possible friction with the separating roof 104; while the lower end protective coating 406 comprises a flange for keeping the braided fibre covering each hose 401 tensioned, a retractable polyolefin tube, and a resin coating of a polymeric compound with high resistance to high temperatures and chemical agents. With this protective coating 406, the lower end of the hose 401 is closed without using a plastic plug or other element capable of being accidentally disassembled and released from the hose 401.


This protective coating 406 also prevents the lower end of the hoses 401 from easily deteriorating due to, for example, hitting the other hoses.


To perform regeneration of the filter medium housed inside the tank, this system comprises a regeneration circuit of the filter medium, depicted in FIG. 1.


Said regeneration circuit comprises an air supply pipe 700 connected to a blower pump 701 and provided with an opening and closing valve 702, said air supply pipe 700 having a plurality of air outlets 703 located below the distributor plate 500.


The filter self-cleaning circuit comprises a water supply pipe 600 connected to a cleaning pressure pump 601 and provided with a valve 602, said water supply pipe 600 having a plurality of water outlets 603, located above the distributor plate 500 and below the hoses, and facing the upper area. Said water outlets 603 are constituted by fan sprinklers positioned in such a way that they access all the passageways located between the hoses 401.


During filtration, the filter medium regeneration circuit remains inoperative, with pumps 601, 701 inactive and valves 602,702 in the closed position.


In the embodiment shown in FIG. 1, the valves 204, 205 are arranged in series in the inlet duct 200, and the valve 301 is also arranged in series in the outlet duct 300, said valves delimiting in the inlet duct 200 and in the outlet duct 300 sections connected by branches 801, 802, provided with separate valves 803, 804 for backwashing and recirculation of filtered water towards the inlet duct respectively inside the tank.


This system allows different operations and work cycles to be carried out.


Precoat: During this operation the perlite filter medium adheres to the outer surface of the hoses 401. In this phase, the pump 203 is activated at low speed by means of a frequency variator, taking into account that, in each installation, the rate will vary and must be adjusted during the start-up of the filtration system, at a speed lower than the usual working speed.


Once the pump 203 is activated, the valve 205 and the aeration valve 110 are opened, when the sensors 111 detect that all air has exited the tank 100, the aeration valve 110 is closed and the recirculation valve 804 is opened. After a certain time, with the perlite filter material girding the hoses, the system is passed to the filtration phase.


Filtering: Once the previous precoat operation has been performed, in which the perlite has been placed around the hoses, the recirculation valve 804 is closed, the valve 301 is opened and the speed of the pump 203 is increased until the desired flow rate is reached, maintaining the filtration until the perlite filter medium is saturated, that is, it has retained in its external part so many dirt particles that the differential pressure between the upper compartment 106 and the lower compartment 105 is increased; this differential pressure increase being detected by the pressure sensors 112 located in the upper compartment 106 and in the lower compartment 105 of the tank.


Regeneration of the filter medium (perlite): In this regeneration phase the suction and pumping valves 205 and 301 are closed and the aeration valve 110 is opened; then the blower pump 701 is started and the valve 702 is opened by injecting pressurised air through the air outlets 703 of the air supply duct 700 located under the distributor plate 500. The air supplied passes through the perforations of the distributor plate 500, ascending perfectly distributed throughout the tank section. After a while, the valve 702 is closed and the blower pump 701 is disconnected. In this regeneration phase, all the perlite filter medium and dirt are removed, and a new precoat operation must then be performed to reposition the perlite around the hoses 401.


Filter self-cleaning and changing the filter medium: After a certain time of use, and several regenerations of the perlite filter medium, it is necessary to make its change and the self-cleaning of the filter. The process of self-cleaning and change of perlite is fully automated except for the filling of perlite, which will usually be a manual process, being able to be carried out automatically by means of some hopper feed system or similar, and can be carried out only starting from the idle state, in which all the valves are closed and all the pumps switched off.


In this phase, the aeration valve 110 is opened, the blower pump 701 is activated, and the valve 702 is opened causing the micronized perlite to detach completely from the hoses 401. While the blower pump 701 is operating, the emptying valve 108 is opened so that the tank 100 is emptied while the fluid and the perlite remain under the effects of the pressurised air stream. When the tank is empty, the valve 702 is closed and the blower pump 701 is deactivated.


Subsequently, the self-cleaning sequence continues, opening the valve 602 and activating the cleaning pump 601 the pressurised water exits through the outlets 603 of the tube 600, cleaning all the hoses 401 and the tank. Once performed the cleaning, the cleaning pump 601 is deactivated and the valve 602 is closed.

    • Backwashing: This operation is carried out after cleaning with pressurised air to separate the micronized perlite from the hoses and having rinsed the hoses and tank with water.


Backwashing or washing backwards, allows a final rinse of the hoses 401 by injecting water in backward flow. To do this, the pump 203 is activated at low speed and the backwash valve 803 is opened keeping the emptying valve 108 and the aeration valve 110 open going into the idle state.


Once the nature of the invention as well as an example of preferred embodiment have been sufficiently described, it is stated for all pertinent purposes that the materials, form, size and arrangement of the elements described are susceptible to changes, provided these do not involve an alteration of the essential features of the invention which are claimed below.

Claims
  • 1. A liquid filtration system, comprising: a filtration tank provided with a lower wall, a side wall and an upper wall;a separating roof dividing the inside of the tank into a lower compartment and an upper compartment;a pressure inlet duct for the liquid to be filtered towards an area close to the lower wall of said tank;a plurality of hoses protruding from the separating roof towards the lower compartment;
  • 2. A liquid filtration system, including the features of claim 1, wherein the central portion of the distributor plate is circular, and has a diameter larger than the diameter of the inlet duct for the liquid to be filtered.
  • 3. A liquid filtration system, including the features of claim 1, wherein the hoses comprise a spring externally coated with a braided fibre made of a high toughness, high chemical resistance polymeric compound and capable of withstanding high temperatures, said hoses externally comprising, at the upper and lower ends, protective coatings comprising a polyolefin retractable tube and, further, at the lower end, a resin coating of a polymeric compound with high resistance to high temperatures and chemical agents.
  • 4. A liquid filtration system, including the features of claim 1, wherein the hoses are divided into independent groups; and the hoses of each group are attached at their upper end to a filter plate removably mounted on the separating roof of the filter tank.
  • 5. A liquid filtration system, including the features of claim 1, wherein said air supply tube has a plurality of air outlets located below the distributor plate.
  • 6. A liquid filtration system, including the features of claim 1, wherein said water supply pipe has a plurality of water outlets located above the distributor plate and below the hoses.
  • 7. A liquid filtration system, including the features of claim 1, wherein the inlet duct and the outlet duct have opening and closing valves arranged in series delimiting two sections of inlet and outlet duct connected by branches of recirculation for the filtered water towards the inlet and circulating duct against the flow through the interior of the tank.
US Referenced Citations (104)
Number Name Date Kind
385333 Way Jun 1888 A
2301430 Malanowski Nov 1942 A
2475561 Cooperider et al. Jul 1949 A
2651414 Lawson Sep 1953 A
2819800 Goodloe Jan 1958 A
2872044 Kasten Feb 1959 A
3055290 Arvanitakis Sep 1962 A
3100190 Hobson, Jr. Aug 1963 A
3310175 McLagan Mar 1967 A
3319793 Miller, Jr. May 1967 A
3394815 Harms Jul 1968 A
3447690 Kracklauer Jun 1969 A
3556304 Collard Jan 1971 A
3642141 Hobson, Jr. Feb 1972 A
4089781 Asp May 1978 A
4094784 Hirano Jun 1978 A
4157900 Margraf Jun 1979 A
4246114 Krebs Jan 1981 A
4292180 Zylka Sep 1981 A
4340477 Hobson, Jr. Jul 1982 A
4439327 Muller Mar 1984 A
4526688 Schmidt, Jr. Jul 1985 A
4578197 Muller Mar 1986 A
4592847 Schumacher Jun 1986 A
4609462 Flynn Sep 1986 A
4622137 Kessler Nov 1986 A
4657673 Kessler Apr 1987 A
4836936 Schewitz Jun 1989 A
4872981 Hobson, Jr. Oct 1989 A
4919801 Hobson, Jr. Apr 1990 A
4944887 Frederick Jul 1990 A
5017241 Ryan May 1991 A
5084176 Davis Jan 1992 A
5114596 Laterra May 1992 A
5203998 Benian Apr 1993 A
5227076 Bogen Jul 1993 A
5230131 Hobson, Jr. Jul 1993 A
5401406 Johnson Mar 1995 A
5407570 Hobson, Jr. Apr 1995 A
5437788 Geibel Aug 1995 A
5441633 Schewitz Aug 1995 A
5494591 Stamm Feb 1996 A
5591329 Davidson Jan 1997 A
5609835 Pitcher Mar 1997 A
5871641 Davidson Feb 1999 A
6036862 Stover Mar 2000 A
6051138 Hobson, Jr. Apr 2000 A
6217781 Hobson, Jr. Apr 2001 B1
6309552 Hobson, Jr. Oct 2001 B1
6332977 Janecek Dec 2001 B1
6365054 Kruger Apr 2002 B1
6437211 Kaye Aug 2002 B2
6439273 Kruger Aug 2002 B1
6472580 Kaye Oct 2002 B2
6660164 Stover Dec 2003 B1
6814878 Tully Nov 2004 B2
6886698 Tully May 2005 B2
6890129 Fabbri May 2005 B2
6959504 Fabbri Nov 2005 B2
8066953 Muth Nov 2011 B2
8470182 Muth Jun 2013 B2
8992775 Swindell Mar 2015 B2
9108872 Salmisuo Aug 2015 B2
10406458 Nehlen, III Sep 2019 B1
10427076 Swindell Oct 2019 B2
10814255 Nehlen, III Oct 2020 B1
10814256 Nehlen, III Oct 2020 B1
10850216 Nehlen, III Dec 2020 B1
10981091 Nehlen, III Apr 2021 B1
11065566 Nehlen, III Jul 2021 B2
11072541 Nazzer Jul 2021 B2
11148071 Kelsey Oct 2021 B2
11167226 Nehlen, III Nov 2021 B2
11331616 Henderson May 2022 B2
20010009969 Kaye Jul 2001 A1
20010053869 Kaye Dec 2001 A1
20020006769 Tsuihiji Jan 2002 A1
20030000101 Fabbri Jan 2003 A1
20030000103 Fabbri Jan 2003 A1
20030196951 Tully Oct 2003 A1
20040026312 Tully Feb 2004 A1
20050218058 Tully Oct 2005 A1
20060231510 Benachenhou Oct 2006 A1
20080099408 Swindell May 2008 A1
20080237152 Benachenhou Oct 2008 A1
20150174515 Swindell Jun 2015 A1
20150196182 Hekman Jul 2015 A1
20160271531 Nazzer Sep 2016 A1
20170043278 Kelsey Feb 2017 A1
20180161706 Masetto Jun 2018 A1
20180222769 Nazzer Aug 2018 A1
20190263678 Nazzer Aug 2019 A1
20190291028 Nehlen, III Sep 2019 A1
20200384387 Nehlen, III Dec 2020 A1
20210039023 Nehlen, III Feb 2021 A1
20210052996 Nehlen, III Feb 2021 A1
20210086111 Nehlen, III Mar 2021 A1
20210170308 Nazzer Jun 2021 A1
20210229006 Nehlen, III Jul 2021 A1
20210268409 Ruzicka Sep 2021 A1
20210331098 Nehlen, III Oct 2021 A1
20210346824 Curley Nov 2021 A1
20220062802 Nehlen, III Mar 2022 A1
20220143534 Vallejo May 2022 A1
Foreign Referenced Citations (1)
Number Date Country
WO-2018211161 Nov 2018 WO
Related Publications (1)
Number Date Country
20220143534 A1 May 2022 US