• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    The invention relates to a device for filtering water with a filter arrangement with a chemical-free self-cleaning function for filter cleaning and with an ozonization device. To create favorable filter conditions, a supply line (1) for contaminated water is connected to a pump (7), to the supply line (1) the ozone supply (6) an ozone source, in particular an ozone generator (5), for the purpose of supplying ozone contaminated Water is connected, wherein the pump (7) ozonated water a filter module (8), especially a cross-flow ultrafiltration module, zuleitet and purified water on the one hand in an outlet (9) and on the other hand in a container (10) for pure drinking water, wherein the Container (10) via lines and a return cleaning pump (11) for flushing the filter membranes in the filter module (8) is connected to the filter module and wherein the flushing of in the filter module (8) retained impurities via a waste water outlet (15) associated pressure control device (14) , in particular a valve, takes place
    公开号:AT516359A1
    申请号:T50698/2014
    申请日:2014-10-01
    公开日:2016-04-15
    发明作者:
    申请人:Deltacore Gmbh；
    IPC主号:
    专利说明:

    The invention relates to an apparatus and a method for the gravitational filtration of water with a filter arrangement with chemical-free Selbstreini¬gungsfunktion for filter cleaning and with an ozonizer.
    Ultrafiltration is a low pressure process that removes pathogens and solid slurries from the water. When drinking water by ultrafiltration a high quality of the starting water is achieved. There are many types of ultrafiltration membranes made of different materials. A common problem of all of these membranes is that they act as a molecular sieve and are thus clogged very quickly. For effective efficacy, they require a system for chemical membrane cleaning.
    The following ultrafiltration membranes are known: cellulose acetate membranes (CA), polysulfone membranes (PS), polyvinylidene fluoride membranes (PVFD), polyester sulfonimembranes (PES), polypropylene membranes (PP), polyvinylchloride membranes (PVC), polyacrylonitrile membranes (PAN) and polyamide membranes (PA). All of these membranes have pores through which hygroscopic water is allowed. The permeability is measured in the MWCO unit (molecular weight cutoff) or permeability limit of the molecular mass. All of these membranes have a common problem, namely the congestion of membranes, which consequently results in reduced flow. The membranes become clogged by the inorganic and organic particles present in the water, which are retained on the surface and in the membrane pores, and thus the permeability of the membranes is reduced. Blockage reduces the flow through the membrane to complete impermeability. To reduce the reduced flow, the membrane must be chemically cleaned. Ultrafiltration chemical purification of polymer membranes is the appropriate process for minimal loss of flow through irreversible plugging of the flow. The choice of the cleaning method of polymer membranes depends on the membrane material, its chemical and physical resistance as well as its tendency to clog. The driving force of the process is the pressure difference that causes the density of the volume flow of permeate through the membrane. In ultrafiltration processes, the fabrics are separated by the sieving phenomenon due to particle size. Ultrafiltration is a pulp separation process using membranes having a pore size of 0.1 to 0.01 micron and removing the high molecular weight materials between 1000 and 20,000 g / mol, colloidal materials, and organic and inorganic polymer molecules. Slurry solids, structural molecules, and high molecular weight solvates are retained on the membrane, whereas low molecular weight water and solvates flow through the membrane. Since only the molecules having a high molecular weight are removed, the difference in osmotic pressure on the surface of the ultrafiltration membrane is negligible, therefore, the use of low pressure is sufficient to achieve a high degree of flow through the membrane.
    The driving force in pressure-induced membrane process is the pressure with which a solution penetrates through the membrane. According to the flow direction on FIG. 1, the pressure-related membrane processes include dead-end filtration on the left-hand side and cross-flow filtration on the right-hand side of FIG. In dead-end filtration, the feed solution flows perpendicular to the membrane surface. All solids 2 which exceed the size of the membrane pores are retained on the surface of the membrane 3 and form a solid cake. The liquid passing through the membrane is called permeate 4. The mass of the filter cake increases until the maximum filter capacity is reached. The membrane must be cleaned or replaced. In cross-flow filtration, the feed solution flows tangentially to the membrane surface. An advantage of cross-flow filtration over conventional (dead-end) filtration is a reduction in the concentration of polarization and unwanted clogging due to retention of the bulk of the solution on the interface with the membrane. Water contaminated with contaminants is discarded from the filter 5.
    The division of membrane clogging into irreversible and reversible clogging is based on the interaction strength between the particles on the material surface. The reversible membrane clogging can be removed by means of a strong shear force during backwashing. Formation of a solid matrix of the clogged solvate layer during the continuous filtration process converts reversible membrane clogging into irreversible clogging. An irreversibly clogged membrane can be cleaned with chemical reagents. The membranes can be cleaned dynamically, where the membrane is inserted under pressure in an ultrafiltration housing. The other type is static: the membrane is removed from the housing and immersed in a detergent solution. Normally, sodium chloride (NaOCl), sodium hydroxide (NaOH) and citronic acid are used for membrane cleaning. Membrane plugging is the main reason why the ultrafiltration systems are introduced relatively slowly as technological solutions. The cleaning process with chemical cleaning agents prevented us from using these otherwise very effective solutions. Several types of membrane clogging, as shown in Figure 2, are known: adsorption clogging, colloid clogging, biological clogging, inorganic clogging.
    There are some known solutions of portable ultrafiltration devices using ozone. The oldest known solution for the ultrafiltration of contaminated water to pure drinking water using ozone is known from US20050139530 A1. In this document, ultrafiltration from a water source is passed through a feed channel by means of a submersible pump. In the water source there are filter arrangements with different filtration functions and the filter arrangements are exchanged if the water flow through the filters is reduced or the filters are clogged. The device has many loopbacks, which not only provides better cleaning, but also
    Self-cleaning of the filter arrangements allows, as well as a pantry, is stored in the purified water. The device ends with a Chlo¬ridanalysator and previously ozone and oxygen are injected into the water. It is about a mobile system on a trailer, which is suitable for larger Siedlun¬gen or densely populated areas.
    Another solution for microfiltration and ultrafiltration of contaminated water to drinking water is known from US Pat. No. 8,419,947. The solution also includes the reverse osmosis process and provides a pre-purification of water by water, then the water is treated with ozone as in the present apparatus. Thus, the solution does not include a self-cleaning function of the ultrafiltration membranes and in a useful form ozone is added after prefiltration, which is not identical to the present solution, prefiltration is used in the solution of the invention but no chemical prefiltration and backwashing allows self-purification of ultrafiltration membranes. A solution for the filtration of contaminated water is known from US Pat. No. 5,244,585 A, the cleaning being carried out by ceramic filters with a return pump in such a way that high-pressure injection of air is used. The cleaning is used in swimming pools and can be both mechanical and bacteriological and antiviral. This means that such water, with some modifications, is actually drinkable.
    CA 2389284 A1 discloses a solution for the filtration of contaminated waste streams, wherein contaminated water flows directly into the ultrafiltration membrane, the particles of which are then collected on the microfilter because of the low-pressure flow. The low pressure flow allows the particles to form an irregular matrix in which the particles are trapped. The permeate thus obtained allows some of the purified water to flow back into the ultrafiltration membranes, where it can be repeatedly cleaned to form permeate and concentrate. Purification by the combination and ozone thus allows a self-cleaning function of the ultrafiltration membrane, which is purified by filtered water. While the device is also in transportable form, it does not filter contaminated water into pure drinking water by using ozone before the ultrafiltration assembly, but first filters contaminated water through the ultrafiltration membrane and then allows the self-cleaning function of the ultrafiltration membrane using ozone.
    The object of the invention is to provide an apparatus and a method in which the filter module service life can be significantly improved by simple means.
    The invention solves this problem by a supply line for contaminated water to which a pump is connected, to the supply line the ozone supply of an ozone source, in particular an ozone generator, for supplying ozone to the contaminated water is connected, the pump ozonated waterfilter module, in particular a cross-flow ultrafiltration module and, purified water flows on the one hand into an outlet and on the other hand into a container for pure drinking water, wherein the container is connected to the filter module via lines and a return cleaning pump for flushing the filter membranes in the filter module and the rinsing out of contaminants contained in the filter module a waste water outlet associated pressure control device, in particular a valve takes place
    According to the invention, therefore, frequent replacement of the filter arrangements is not necessary since the device has a self-cleaning function which is based on a pre-injection of ozone and on backwashing by flushing out the contaminants.
    The subject of the invention is a device for ultrafiltration of water with automatic dynamic membrane cleaning without the use of chemicals with ozonization, as well as the method and the mechanical device, is filled in the contaminated water, which is then filtered by means of ozone injection andUltrafiltration to pure drinking water; a part of the contaminated Was¬sers remains in the device and the filter system is then cleaned by Rückreinin¬ tion such that the wastewater flows away tangent to the membrane and the membrane is self-cleaning superficially and thus the membranes can be cleaned without chemicals.
    The technical problem solved by the invention is such a construction of the ultrafiltration device which will enable the self-cleaning function with known water ultrafiltration by means of ozone feed before ultrafiltration arrangements and with backwashing and thus ensure the multiple application of ultrafiltration membranes without the use of chemicals Ultrafiltration module tangential itself.
    The feed line is preferably arranged downstream of a pre-filter which retains solid particles, and the ozone generator preferably comprises an air inlet opening with associated air filter and forwards ozone which has been produced in the ozone generator via the ozone feed line into the feed line. The backwash pump for counterflushing the filter membranes in the filter module can be made via another filter module, an ultrafilter. The filter modules are membrane filter modules.
    The inventive method for the filtration of water with a Filteranordnung with chemical-free self-cleaning function for filter cleaning and Ozonisierung the water is characterized in that, the contaminated, if necessary. Pre-purified, water is first added to ozone, after which the water-ozone mixture through a filter module, in particular a cross-flow ultrafiltration module, is promoted, wherein a part of the water is filtered through the membrane and another part of the water via a pressure regulator, in particular In particular, a valve is passed unfiltered back out of the filter module and the water filtered through the membrane is divided into two parts, one part of the water is ready for use and the other part is stored in a container for back-cleaning the filter module, the purified water is fed back to the Rückreiin¬gung of the filter module through the filter module, the backgeför¬derte water flows parallel to the filter surface of the filter module with cleaning of the filter surface via a pressure regulator. The recirculated water, together with contaminated, possibly pre-cleaned, water, parallel to
    Outflow filter surface from the filter module under cleaning of the filter surface via a pressure regulator
    The invention is illustrated by means of an embodiment and drawings. They show:
    1 shows on the left a scheme of a - dead-end filtration and right a cross-flow
    filtration,
    2 shows patterns of different pore clogging forms,
    3 schematic of a cross-flow filtration,
    Fig. 4 Scheme of an oxidation process and
    Fig. 5 is a system diagram of a device according to the invention.
    In the cross-flow filtration illustrated in Figure 3, input water flows tangentially to the membrane surface. By supplying ozone into the water before entering the membrane, a whole series of reactions is achieved which allow a better effect of the ultrafilter and prevent the development of microorganisms, so there is no biological blockage. The inorganic contaminants are oxidized by ozone and thereby the accumulations of contaminants, which penetrate more severely through the membrane pores, are increased. Due to the tangential flow and the open exit on the membrane, the contaminants are flushed out through the drain.
    Ozone is one of the most powerful oxidants in nature. It decomposes after the equation 03 ~ > 02 + 0, and the resulting atomic oxygen has an extraordinary ability to oxidize. The use is extremely safe, because even in the case of overdose, no dangerous compounds for humans are formed. The ozone, which is an allotropic modification of oxygen, is extremely unstable and reactive and disintegrates rapidly, therefore it must be generated directly in place prior to application. It is fabricated such that oxygen is passed through electrodes creating an electric field with high voltage and medium high frequency. Ozone is mostly used to clean drinking water. It is used for the oxidation of metals and organic substances as well as for sterilization. Compared to other disinfectants (CI, ...), the disinfection with ozone proceeds much faster and independent of the ammonia content and pH of the water. Among other things, ozone removes unpleasant odors from the water (by removing organic contamination) and reduces the concentration of dissolved heavy metals such as Fe and Mg. Unlike other disinfectants, there are no human hazardous substances in the water, although ozone is overdosed.
    In FIG. 4, the oxygen molecule O 2 is passed through the electrodes in the ozone generator, producing an electric field with high voltage and medium high frequency. The ozone 03 is generated. 03 oxidizes metals and organic matter and destroys microorganisms. In the reaction, 03 is converted back to oxygen 02 without production of coproducts.
    In Fig. 5, the ultrafiltration of contaminated water to pure drinking water by the entry of contaminated water through the feed line 1 after the purification of solid particles after prefiltration in the pre-filter 2 is shown. At the air inlet port 4, air is supplied through the air filter 3. The ozone 5 generated in the ozone generator 5 is fed via the ozone feed line 6 to the previously coarsely purified water. With the pump 7, ozonated water is fed to the ultrafiltration module 8, which transports purified drinking water to the outlet 9; The remaining purified water 16 flows into the tank 10 with pure drinking water, which serves to flush the ultrafiltration membranes through the purge pump 11 and the ultrafilter 12 for backwashing in the direction of the backwash 13 to the pressure regulator 14. Waste water that cleans the ultrafiltration membranes flows through the waste water outlet 15 separately.
    The process for the ultrafiltration of water with automatic dynamic membrane cleaning without the use of chemicals with ozonization proceeds as follows. Contaminated water is pumped in with the pump and in the first phase ozone is added. Water and the ozone mixture then flow tangentially through the ultrafiltration module. Part of the water seeps through the membrane, while part of the water flows out of the membrane through the pressure regulator. The water infiltrated by the membrane is divided into two parts. One part of the water is ready for use, but the other part is stored in the container and used to clean the membrane. The water, which flows tangentially out of the membrane, simultaneously cleans the membrane and prevents the development of microorganisms and a biofilm on the membrane. Because of this process, no chemical agents are needed in membrane cleaning.
    Ultrafiltration of water with the exchange of drinking and waste water and with the self-cleaning function of filter assemblies without the use of chemicals with ozonation is carried out by a mechanical device that pumps in water contaminated with the pump and adds ozone in the first phase. Water and the ozone mixture then flow tangentially through the ultrafiltration module. Part of the water seeps through the membrane, while part of the water flows out of the membrane through the pressure regulator. The water seeped through the membrane is divided into two parts. Some of the water is ready for use, but the other part is stored in the tank and used to clean the membrane. The water that flows tangentially out of the membrane simultaneously cleans the membrane and prevents the development of microorganisms and biofilm on the membrane. Because of this process, no chemical agents are needed in membrane cleaning.
    权利要求:
    Claims (7)
    [1]
    1. Apparatus for filtering water with a filter assembly with chemika¬lienfreier self-cleaning function for filter cleaning and with a Ozonisierungs¬einrichtung, characterized by a supply line (1) for contaminated water andie a pump (7) is connected to the supply line (1 ) the ozone supply line (6) of an ozone source, in particular an ozone generator (5), is connected for supplying ozone to the contaminated water, the pump (7) supplying and purifying ozonated water to a filter module (8), in particular a crossflow ultrafiltration module Water on the one hand in an outlet (9) and on the other hand in a container (10) for pure drinking water, wherein the Behäl¬ter (10) via lines and a back cleaning pump (11) for counterflushing the filter membranes in the filter module (8) is connected to the filter module and wherein rinsing out of impurities retained in the filter module (8) via a drain Assert outlet (15) associated pressure control device (14), in particular a valve, takes place.
    [2]
    2. Device according to claim 1, characterized in that the supply line (1) is arranged downstream of a solid particle retaining pre-filter (2).
    [3]
    3. Apparatus according to claim 1 or 2, characterized in that the ozone generator (5) an air inlet opening (4) with associated air filter (3) um¬fasst and on the ozone feed line (6) in the ozone generator (5) generated ozone in the feed line (1) passes.
    [4]
    4. Device according to one of claims 1 to 3, characterized in that the return cleaning pump (11) for backwashing the filter membranes in the filter module (8) via a further filter module (12), an ultrafilter, to the filter module (8) the filter module (8) is connected.
    [5]
    5. Device according to one of claims 1 to 4, characterized in that the filter modules (8, 12) are membrane filter modules.
    [6]
    6. A process for the filtration of water with a filter assembly with chemika¬lienfreier self-cleaning function for filter cleaning and ozonation of the water, characterized in that the contaminated, possibly pre-cleaned, water is first added ozone, after which the water-ozone mixture through a filter module, in particular a cross-flow - Ultrafiltration module is conveyed, wherein a part of the water is filtered through the membrane and another part of the water, however, via a pressure control device, in particular a valve, unfiltered again out of the filter module is passed and wherein the filtered through the membrane water is divided into two parts part of the water is ready for use and the other part is stored in a container for cleaning the Filtermo¬duls, wherein the purified water for back cleaning of the filter module is fed back through the filter module, the returned water parallel to the filter surface of the Filter module under cleaning of the filter surface via a pressure regulator flows out.
    [7]
    7. The method according to claim 6, characterized in that the rückgeför¬derte water flows together with contaminated, possibly pre-cleaned, water, parallel to the filter surface of the filter module under cleaning of the filter surface a pressure control device.
    类似技术:
    公开号 | 公开日 | 专利标题
    Zularisam et al.2007|The effects of natural organic matter | fractions on fouling characteristics and flux recovery of ultrafiltration membranes
    DE69829952T2|2006-03-02|PORTABLE REVERSE OSMOSIZE UNIT FOR DRINKING WATER TREATMENT
    DE60125461T2|2007-05-16|Porous hollow fiber membranes and process for their preparation
    DE102008006501A1|2008-09-25|Combined ultrasonic air backwash process to clean immersed membranes involves applying ultrasound to liquid during backwash and blowing gas over outer membrane surface
    You et al.2007|Effect and mechanism of ultrafiltration membrane fouling removal by ozonation
    KR101193902B1|2012-10-29|Water-purifying system and method using membrane filtration for manufacturing purified water
    DE102006060592B3|2008-04-30|Desalination of seawater and other salt containing water e.g. brackish water by reverse osmosis, comprises mixing ozone to the solution to be desalinated and leading the mixture over a ceramic ultrafiltration membrane and an adsorber
    DD296621A5|1991-12-12|MEMBRANE SEPARATOR AND APPLICATION METHOD
    DE10001737C1|2001-10-18|Water purification apparatus comprises housing which operates like cyclone and has tangential inlet, axial membrane and outlet in form of central dip pipe
    JP2007252966A|2007-10-04|Membrane module and water treatment system
    AT516359B1|2021-06-15|Device for the filtration of water with a filter arrangement
    EP0833687B1|1999-12-08|Method for treating water according to the principle of reversed osmosis
    JPH10225682A|1998-08-25|Method of removing boron in reverse osmosis seawater desalination
    AT505282B1|2008-12-15|METHOD AND DEVICE FOR REDUCING BIOFOULING ON MEMBRANES OF PRESSURE-DRIVEN MEMBRANE SEPARATION METHOD
    EP2794073B1|2019-02-06|Method for cleaning a filter and recovery apparatus
    DE3106772A1|1982-09-09|Membrane separation process and membrane separation installation
    DE102009017125A1|2010-10-21|Processing surface water, industrial water, brackish water and/or grey water to drinking water, comprises initially sucking the water by prefiltration, and subsequently subjecting the sucked water to microfiltration and/or ultrafiltration
    Pertile et al.2018|Evaluation of membrane microfiltration fouling in landfill leachate treatment
    US20140326666A1|2014-11-06|Apparatus and methods for removing contaminants from wastewater
    AT410314B|2003-03-25|METHOD AND DEVICE FOR THE TREATMENT OF ORGANICALLY LOADED WASTE WATER
    EP1265819B1|2003-09-03|Method and device for effluent treatment
    DE102011082285A1|2013-03-07|Process for the separation of radioactive nuclides by means of ceramic filter membranes
    JP4304803B2|2009-07-29|Water treatment apparatus cleaning method and water treatment apparatus
    DE19730441A1|1999-01-21|Process to clean membrane water filter unit back-flushes permeate side
    EP2055680A1|2009-05-06|Plant to clean water
    同族专利:
    公开号 | 公开日
    WO2016049675A1|2016-04-07|
    EP3201139A1|2017-08-09|
    AT516359B1|2021-06-15|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    JPH01277060A|1988-04-28|1989-11-07|Mitsubishi Electric Corp|Method for compressing multi-gradation picture data|
    WO2000027510A1|1998-11-10|2000-05-18|Asahi Kasei Kogyo Kabushiki Kaisha|Method for filtration with membrane|
    US20100292844A1|2009-05-14|2010-11-18|Omni Water Solutions Llc|Self-contained portable multi-mode water treatment system and methods|DE102017011936A1|2017-12-21|2019-06-27|ONI-Wärmetrafo GmbH|Apparatus for the treatment of contaminated water|US5244585A|1991-01-11|1993-09-14|Akitoshi Sugimoto|Method of cleaning porous ceramic filters|
    JP3896687B2|1998-03-30|2007-03-22|栗田工業株式会社|Manganese-containing water treatment equipment|
    US6322703B1|1999-04-20|2001-11-27|Asahi Kasei Kabushiki Kaisha|Method for purifying aqueous suspension|
    WO2001044115A2|1999-10-27|2001-06-21|Rwe Nukem Corporation|Waste water treatment system|
    JP2003285059A|2002-03-27|2003-10-07|Jfe Engineering Kk|Control method of ozone supply in water treatment using ozone oxidation and membrane filtration|
    US7632410B2|2003-08-21|2009-12-15|Christopher Heiss|Universal water purification system|
    FR2891540B1|2005-09-30|2007-12-28|Otv Sa|METHOD FOR TREATING WATER COMPRISING A RAPID DECANTATION STEP FOLLOWED BY A FILTRATION STEP DIRECTLY ON MEMBRANES OF MICRO OR ULTRA-FILTRATION, AND CORRESPONDING DEVICE|
    US20130313191A1|2009-05-14|2013-11-28|Omni Water Solutions, Inc.|Water treatment systems and methods|
    CN103298542A|2010-10-15|2013-09-11|艾克塞勒雷克斯公司|Large volume disposable ultrafiltration systems and methods|AT519319B1|2016-11-14|2020-09-15|Va Tech Wabag Gmbh|Treatment of wastewater into drinking water using ozone|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    ATA50698/2014A|AT516359B1|2014-10-01|2014-10-01|Device for the filtration of water with a filter arrangement|ATA50698/2014A| AT516359B1|2014-10-01|2014-10-01|Device for the filtration of water with a filter arrangement|
    EP15787432.2A| EP3201139A1|2014-10-01|2015-09-30|Device and method for filtering water|
    PCT/AT2015/050245| WO2016049675A1|2014-10-01|2015-09-30|Device and method for filtering water|
    [返回顶部]