CN1989076A - water purification system - Google Patents
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- CN1989076A CN1989076A CNA2005800085032A CN200580008503A CN1989076A CN 1989076 A CN1989076 A CN 1989076A CN A2005800085032 A CNA2005800085032 A CN A2005800085032A CN 200580008503 A CN200580008503 A CN 200580008503A CN 1989076 A CN1989076 A CN 1989076A
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
- C02F1/003—Processes for the treatment of water whereby the filtration technique is of importance using household-type filters for producing potable water, e.g. pitchers, bottles, faucet mounted devices
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
- C02F9/20—Portable or detachable small-scale multistage treatment devices, e.g. point of use or laboratory water purification systems
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/283—Treatment of water, waste water, or sewage by sorption using coal, charred products, or inorganic mixtures containing them
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/50—Treatment of water, waste water, or sewage by addition or application of a germicide or by oligodynamic treatment
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/68—Treatment of water, waste water, or sewage by addition of specified substances, e.g. trace elements, for ameliorating potable water
- C02F1/685—Devices for dosing the additives
- C02F1/688—Devices in which the water progressively dissolves a solid compound
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/76—Treatment of water, waste water, or sewage by oxidation with halogens or compounds of halogens
- C02F1/766—Treatment of water, waste water, or sewage by oxidation with halogens or compounds of halogens by means of halogens other than chlorine or of halogenated compounds containing halogen other than chlorine
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/40—Liquid flow rate
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/18—Removal of treatment agents after treatment
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/18—Removal of treatment agents after treatment
- C02F2303/185—The treatment agent being halogen or a halogenated compound
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- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
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- Water Treatment By Sorption (AREA)
- Biological Treatment Of Waste Water (AREA)
Abstract
Description
技术领域technical field
本发明涉及一种重力自流给水净化系统,该系统用于提供经过净化的高品质饮用水。该水净化系统在确保去除有害污染物的同时长时间地持续供给大流量的饮用水。The invention relates to a gravity self-flow water purification system, which is used for providing purified high-quality drinking water. The water purification system continues to supply large flows of drinking water for a long time while ensuring the removal of harmful pollutants.
背景技术Background technique
世界上大量人口生活在卫生饮用水严重短缺的国家。人们不得不直接依靠如水井、池塘和河流等地下水源。这些水源经常受到污水、工业排放物和农业副产物例如杀虫剂残留物的污染。Large numbers of the world's population live in countries with severe shortages of sanitary drinking water. People have to rely directly on groundwater sources such as wells, ponds and rivers. These water sources are often contaminated by sewage, industrial discharge and agricultural by-products such as pesticide residues.
重力自流给水过滤器,例如球形窄颈过滤器(carafe filter)用于家庭使用已为人所知,其中水通过梯形过滤器较宽的顶部上的一系列小孔流入过滤器元件,并流动通过过滤器到达较窄的底部,期间流经由松散的吸附剂构成的多孔床。此类过滤器对获得有效流量存在固有的限制,因为水被要求流经由吸附颗粒构成的深床,且在通过少量的水后经常会发生阻塞的现象。另外此类过滤器不能有效地分离水中存在的有害病原体。Gravity-fed water filters such as spherical narrow-neck filters (carafe filters) are known for domestic use, in which water flows into the filter element through a series of small holes on the wider top of the trapezoidal-shaped filter and flows through the filter element. The filter reaches the narrow bottom, during which the flow passes through a porous bed of loose adsorbent. Such filters are inherently limited in achieving effective flow rates, as water is required to flow through a deep bed of adsorbent particles and often clogs after passing small amounts of water. Additionally such filters cannot effectively separate harmful pathogens present in the water.
在WO9529878(Recovery Engineering Inc.1995)号专利公报中披露了一种水净化装置,其包括一个由碘化树脂单元和活性炭单元组成的消毒单元。该消毒单元因为碘化树脂单元的高成本而存在其局限性。另外,残留在水中的碘对某些人的身体可能有害。A kind of water purification device is disclosed in WO9529878 (Recovery Engineering Inc.1995) No. patent publication, and it comprises a disinfection unit that is made up of iodinated resin unit and gac unit. This sanitizing unit has its limitations due to the high cost of the iodinated resin unit. In addition, iodine remaining in the water may be harmful to some people's health.
因此,在确保去除所有的有害污染物包括颗粒物和可溶物如有害气味、杀虫剂残留物和其它有机物以及有害微生物如孢囊、细菌和病毒的同时,仍然需要开发一种成本低廉且能持续和更加有效地以所期望的速度生产健康饮用水的改进型水净化系统。同时在人们使用净化水前除去所有用于杀死病原微生物的杀菌剂也是十分重要的。更加重要的是,系统必须在几厘米的重力压头作用下,长时间地持续提供所希望的大流量纯净水。此外还希望无需对水净化系统进行频繁的清洗、更换零件或维护。现有技术未能提供上述所需的特征。Therefore, there remains a need to develop a low-cost and capable Improved water purification systems that consistently and more efficiently produce healthy drinking water at the desired rate. It is also very important to remove all fungicides used to kill pathogenic microorganisms before people use the purified water. More importantly, the system must continue to provide the desired large flow of pure water for a long time under the action of a few centimeters of gravity head. It is also desirable to eliminate the need for frequent cleaning, replacement parts or maintenance of the water purification system. The prior art fails to provide the desired features described above.
发明内容Contents of the invention
因此,本发明的目的在于提供一种能够在长时间内以约100~200ml/min的高流量持续供给清洁饮用水的重力自流给水净化系统,其中在进水压头发生变化的情况下,流量不会发生显著改变。Therefore, the purpose of the present invention is to provide a gravity feed water purification system capable of continuously supplying clean drinking water at a high flow rate of about 100-200ml/min for a long time, wherein the flow rate No significant changes will occur.
本发明的目的还在于提供一种能够供给不含颗粒物等污染物、溶解性杂质如有害气味、杀虫剂残留物和其它有机物以及有害病原体如孢囊、细菌和病毒的饮用水的重力自流给水净化系统。It is also an object of the present invention to provide a gravity-fed water supply capable of supplying drinking water free from pollutants such as particulate matter, dissolved impurities such as harmful odors, pesticide residues and other organic matter, and harmful pathogens such as cysts, bacteria and viruses purification system.
本发明的目的还在于提供一种不需要任何外部能量比如电能来运行所述单元的重力自流给水净化系统。It is also an object of the present invention to provide a gravity fed water purification system that does not require any external energy such as electricity to operate the unit.
本发明的目的还在于提供一种不需要使用昂贵的更换零件,由此维护费用低廉的重力自流给水净化系统。It is also an object of the present invention to provide a gravity fed water purification system which does not require the use of expensive replacement parts and thus is low maintenance.
因此,本发明提供一种重力自流给水净化系统,所述重力自流给水净化系统包括适于分离进水中的颗粒物和可溶物的过滤单元,该单元与一个化学品分配单元流体连通,从而使得在水接触由化学品分配单元分配的杀菌剂前通过流量控制装置调节过滤单元的出水流量,然后该水在贮水室中停留一段预定的时间后,通过用于从出水中分离出分配的杀菌剂的清除装置排出水净化系统。Accordingly, the present invention provides a gravity fed water purification system comprising a filtration unit adapted to separate particulates and solubles from feed water, the unit being in fluid communication with a chemical dispensing unit such that Before the water contacts the bactericide dispensed by the chemical dispensing unit, the effluent flow of the filter unit is adjusted by the flow control device, and then the water stays in the water storage chamber for a predetermined period of time, and then passes through the sterilizing agent used to separate the dispensed from the effluent water. The removal device of the agent exits the water purification system.
具体实施方式Detailed ways
因此,本发明提供一种重力自流给水净化系统,包括:Therefore, the present invention provides a gravity gravity feed water purification system, comprising:
-适于分离进水中的颗粒物和可溶物的过滤单元,该单元流体连通- a filter unit suitable for separating particulate matter and soluble matter in the incoming water, the unit being in fluid communication
-化学品分配单元,从而使得在水接触由化学品分配单元分配的杀菌剂前,过滤单元的出水流量通过- chemical distribution unit, so that the effluent flow from the filter unit passes through the
-流量控制装置进行控制,然后该水在-The flow control device is controlled, then the water in the
-贮水室中停留一段预定的时间后,通过- After staying in the water storage chamber for a predetermined period of time, pass
-用于从出水中分离出分配的杀菌剂的清除装置排出水净化系统。- Cleaning means for separating the dispensed biocide from the effluent water out of the water purification system.
所述流量控制装置优选包括适于排放所需体积水的预定尺寸的流量控制箱,该箱包括至少一个用于使水从所述过滤单元的出口流入所述箱的入口装置和至少一个操作连接至所述流量控制箱且适于控制所述水箱的流出水量的虹吸排放装置。Said flow control means preferably comprises a flow control tank of predetermined size adapted to discharge a desired volume of water, the tank comprising at least one inlet means for passing water from an outlet of said filtration unit into said tank and at least one operative connection A siphon discharge to said flow control tank adapted to control the flow of water out of said tank.
所述过滤单元优选包括碳块过滤介质。该碳块过滤介质由粉末活性炭(PAC)和粘合剂通过充分混合、加压和热处理步骤加工成块体。该粉末活性炭优选为由烟煤、椰子壳或木炭或石油沥青制得的精选碳。优选所用粉末活性炭尺寸均匀系数小于2,更优选小于1.5,四氯化碳的量超过50%,更优选超过60%。The filter unit preferably comprises a carbon block filter medium. The carbon block filter media is processed into a block from powdered activated carbon (PAC) and a binder through the steps of thorough mixing, pressurization and heat treatment. The powdered activated carbon is preferably selected carbon made from bituminous coal, coconut shell or charcoal or petroleum pitch. Preferably, the size uniformity coefficient of the powdered activated carbon used is less than 2, more preferably less than 1.5, and the amount of carbon tetrachloride exceeds 50%, more preferably exceeds 60%.
适合的碳块过滤介质已在GB2390987号专利文献中公开,更优选也在我们的共同待审的申请320/MUM/2004中公开。该共同待审的申请记载了用于重力自流给水过滤器中的碳块过滤介质,所述碳块过滤介质由颗粒尺寸大小使得95%(重量)的颗粒能通过50目筛且不超过12%的颗粒能通过200目筛的粉末活性炭(PAC)和熔体流动速率(MFR)小于5的粘合剂材料制成。更优选碳块过滤介质包含55~80%(重量)的粉末活性炭的颗粒尺寸在100~200目之间且体积小于碳块的50%。Suitable carbon block filter media are disclosed in patent document GB2390987 and more preferably also in our co-pending application 320/MUM/2004. This co-pending application describes carbon block filter media for use in gravity feed water filters, the carbon block filter media having a particle size such that 95% by weight of the particles pass through a 50 mesh screen and no more than 12% The granules can be made of powdered activated carbon (PAC) passing through a 200 mesh screen and a binder material with a melt flow rate (MFR) of less than 5. More preferably, the carbon block filter media comprises 55-80% by weight of powdered activated carbon having a particle size between 100-200 mesh and having a volume less than 50% of the carbon block.
通过使用上述过滤单元,有可能在75mm重力水压头的条件下,在长时间内持续地保持100~300ml/min的流量,并且能够满足从化学污染物中去除颗粒污染物的需要。By using the above filter unit, it is possible to continuously maintain a flow rate of 100-300ml/min for a long time under the condition of 75mm gravity water head, and can meet the requirement of removing particle pollutants from chemical pollutants.
所述过滤单元可与其它已公知的过滤装置比如沉淀过滤装置一起使用,优选地,一种可冲洗或可更换的沉淀过滤器用于去除细小的灰尘和其它微小颗粒。该沉淀过滤器可以是无纺织物,优选为微孔尺寸适于截留3微米或以上颗粒的多微孔织物。最优选的是,水在通过碳块过滤介质前首先通过沉淀过滤器。The filter unit may be used with other known filter devices such as a sediment filter, preferably a flushable or replaceable sediment filter for removal of fine dust and other microscopic particles. The sediment filter may be a non-woven fabric, preferably a microporous fabric with a pore size suitable for retaining particles of 3 microns or above. Most preferably, the water first passes through the sediment filter before passing through the carbon block filter media.
根据本发明所述的重力自流给水净化系统包括用于调节过滤单元出水流量的流量控制装置。流量调节优选利用不需要外部能量比如电能输入的装置得以实现。该流量控制装置可包括例如旋塞阀、阀门、文丘里管和导流板等节流装置。更优选地,可使用记载在我们的共同待审的申请927/MUM/2002中的流量控制装置,所述流量控制装置包括适于控制水流量的直的水道和至少一个弯曲部的组合。特别优选的用于满足本发明目的流量控制装置记载在WO2004/074182号专利文献中。后一个流量控制装置包括用于排放所需体积水的预定尺寸的流量控制箱,该箱包括至少一个用于使水从所述过滤单元的出口流入所述箱的入口装置和至少一个操作连接至所述流量控制箱且适于控制所述水箱的流出水量的虹吸排放装置。The gravity gravity feedwater purification system according to the present invention includes a flow control device for adjusting the water flow rate of the filter unit. Flow regulation is preferably achieved using means that do not require an input of external energy, such as electrical energy. The flow control means may include throttling devices such as stopcocks, valves, venturis, and baffles. More preferably, a flow control device as described in our co-pending application 927/MUM/2002 comprising a combination of a straight channel and at least one bend adapted to control the flow of water may be used. A particularly preferred flow control device for meeting the object of the present invention is described in WO2004/074182 patent document. The latter flow control means comprises a flow control tank of predetermined size for discharging a desired volume of water, the tank comprising at least one inlet means for allowing water to flow into said tank from an outlet of said filtration unit and at least one operatively connected to The flow control box is a siphon discharge device suitable for controlling the amount of water flowing out of the water tank.
在以上共同待审的申请记载的方案中,通过选择控制箱的尺寸和选择虹吸排放装置的具体形式,如预先选择虹吸管的直径和形状,优选一种适合于控制流量的倒置管状U/V形构件,可使水流量在很大的范围内得到调节。流量控制装置该优选特征的应用确保了不论过滤单元的出水量如何都能够对水流量进行良好地调节。In the scheme described in the above co-pending application, by selecting the size of the control box and selecting the specific form of the siphon discharge device, such as pre-selecting the diameter and shape of the siphon tube, an inverted tubular U/V shape suitable for flow control is preferred Components that allow water flow to be adjusted over a wide range. The application of this preferred feature of the flow control device ensures a good regulation of the water flow regardless of the water output of the filter unit.
流量控制装置的出水接触由化学品分配单元分配的杀菌剂。该化学品分配单元优选为一种不需要外部能量比如电能就可以分配杀菌剂的单元。在水流经化学品分配单元时,化学品分配单元被构造用以将所需浓度的杀菌剂释放到水中。化学品分配单元中的杀菌剂可以液态的形式存在并且以控制好的量加入到水中。杀菌剂优选以固态的形式存在并且当水和固体表面接触时,杀菌剂以控制好的速度溶解到水中。更优选地,所述固体为一个或多个药片的形式。当超过一个药片时,化学品分配单元优选包括一个管状体,药片在其中堆叠在一起。药片以一种控制好的方式将杀菌剂释放到水中,可使用任何一种能达到此目的的手段。本发明的化学品分配单元优选可包括在我们的共同待审的申请926/MUM/2002中公开的化学消毒系统。优选在释放的过程中,药片缓慢溶解,当前一粒药片溶解完全后一粒新的药片才开始和水接触。The effluent from the flow control device contacts the biocide dispensed by the chemical dispensing unit. The chemical dispensing unit is preferably a unit that dispenses the sterilant without the need for external energy, such as electrical energy. The chemical dispensing unit is configured to release a desired concentration of biocide into the water as water flows through the chemical dispensing unit. The biocide in the chemical dispensing unit may be in liquid form and added to the water in controlled quantities. The biocide is preferably present in solid form and when the water comes into contact with the solid surface, the biocide dissolves into the water at a controlled rate. More preferably, the solid is in the form of one or more tablets. When there is more than one tablet, the chemical dispensing unit preferably comprises a tubular body in which the tablets are stacked. Tablets release the biocide into the water in a controlled manner, using any means available for this purpose. The chemical dispensing unit of the present invention may preferably comprise the chemical disinfection system disclosed in our co-pending application 926/MUM/2002. Preferably, the tablet dissolves slowly during release, and a new tablet does not come into contact with the water until the previous tablet has completely dissolved.
以上共同待审的申请中记载的化学消毒系统包含消毒单元,该单元装有化学消毒剂并在其底部设有开口,用于将水引入该单元进行消毒的装置具有一个类似喷嘴的顶部,该顶部选择性设置在该单元下部附近并且面对该单元底部的开口,该类似喷嘴的顶部具有一个选择性有角度的圆锥形外表面,从而有利于在水流与通过所述开口暴露的消毒剂相接触后调节接触和输送所述活性消毒剂。The chemical sanitizing system described in the above co-pending application comprises a sanitizing unit containing a chemical sanitizing agent and having an opening at the bottom, the means for introducing water into the unit for sanitizing has a nozzle-like top, the The top is optionally disposed near the lower portion of the unit and facing the opening in the bottom of the unit, the nozzle-like top having an optionally angled conical outer surface to facilitate contact between the flow of water and the disinfectant exposed through the opening. Post-contact conditioning exposure and delivery of the active disinfectant.
所述化学品分配单元优选具有圆柱形剖面,所述圆柱形剖面在打孔圆盘或无纺织物上将杀菌剂药片堆叠在一起。在杀菌剂贮存处的下部中央位置有进水口,水从进口流入与药片的表面接触后通过贮存处周边的窗口(开口)排出。The chemical dispensing unit preferably has a cylindrical section that stacks the antiseptic tablets together on a perforated disc or non-woven fabric. There is a water inlet at the lower central position of the fungicide storage place, water flows in from the inlet and contacts with the surface of the tablet, and then is discharged through the windows (openings) around the storage place.
杀菌剂优选为能够输送活性氯到水中以确保杀死微生物的化学制剂。任何可能被使用的释放氯的杀菌剂包括氯化磷酸三钠、次氯酸钙、次氯酸锂、各种本领域中已公知的能够释放活性氯的N-氯化的化合物比如钠或钾的二氯异氰尿酸盐、三氯氰尿酸、一氯胺、二氯胺、[(单三氯)-四(二氯一钾)]五异氰尿酸盐、1,3-二氯-5,5-二甲基(dimethylidanotone),氯胺T,p-甲苯-硫代二氯酰胺,三氯三聚氰胺,N-氯胺,N-氯琥珀酰亚胺,N,N’一二氯偶氮二脲,N-氯乙酰脲,N,N-二氯偶氮二脲,N-氯乙酰脲,N,N-二氯联二脲,氯化二氰二酰安。The biocide is preferably a chemical agent capable of delivering active chlorine into the water to ensure the killing of microorganisms. Any chlorine-releasing fungicides that may be used include chlorinated trisodium phosphate, calcium hypochlorite, lithium hypochlorite, various N-chlorinated compounds known in the art to release active chlorine such as sodium or potassium Dichloroisocyanurate, trichlorocyanuric acid, monochloramine, dichloramine, [(monotrichloro)-tetrakis(dichloromonopotassium)]pentaisocyanurate, 1,3-dichloro -5,5-Dimethyl (dimethylidanotone), chloramine T, p-toluene-thiodichloroamide, trichloromelamine, N-chloramine, N-chlorosuccinimide, N, N'-dichloro Azodiurea, N-chloroacetylurea, N,N-dichloroazodiurea, N-chloroacetylurea, N,N-dichlorobiurea, dicyandiamide chloride.
在本发明的一个优选方面中,水净化系统还包括指示装置,所述指示装置在使用一段时间后当所有的可用杀菌剂药片被用完时可以提供指示。所述指示装置优选在杀菌剂药片完全用完或接近完全用完时提供可视指示。本领域中已公知的任何一种指示装置都可能在本发明中使用。特别优选一种指示装置,所述指示装置包括一粒放置在杀菌剂药片堆顶部的带有颜色的药片和一个设置在化学品分配单元底部的透明窗口,通过该窗口可以肉眼观察最下部的大部分药片。带有颜色的药片可以是惰性的,其在有水和杀菌剂的环境中是很稳定的。当杀菌剂是释放氯的化学制剂时,惰性药片由对氯的氧化特性具有很强惰性的材料制成。另一种可选方式是,惰性药片上可涂覆有对氯具有很强惰性的材料尤其是聚合材料。In a preferred aspect of the invention, the water purification system further comprises an indicator device which, after a period of use, provides an indication when all available biocide tablets have been used up. The indicator device preferably provides a visual indication when the antiseptic tablet is completely or nearly completely used up. Any indicating device known in the art may be used in the present invention. Particularly preferred is an indicating device comprising a colored tablet placed on top of the stack of biocide tablets and a transparent window located at the bottom of the chemical dispensing unit through which the lowermost large Portion of pills. Colored tablets can be inert, which is very stable in the presence of water and bactericides. When the fungicide is a chlorine releasing chemical, the inert tablet is made of a material that is very inert to the oxidizing properties of chlorine. Alternatively, the inert tablet can be coated with a material which is very inert to chlorine, especially a polymeric material.
在本发明的另一个优选方面中,水净化系统还包括水断流装置,所述水断流装置确保当杀菌剂被用完时,没有水流过流量控制装置。所述水断流装置优选包括所述惰性药片。该药片可由磁性材料优选铁或镍制成,其上适当地涂覆有对杀菌剂具有惰性的涂层,并且一块反向磁体可被放置在化学品分配单元的底部,从而使得当所有的杀菌剂被用完时,两块磁体就会相互靠近紧紧贴在一起,由此起到确保切断排出控制装置的水流的阀门装置的作用。In another preferred aspect of the present invention, the water purification system further includes a water shut-off device that ensures that no water flows through the flow control device when the sterilant is used up. Said water shut-off means preferably comprises said inert tablet. The tablet can be made of a magnetic material, preferably iron or nickel, suitably coated with a coating inert to the biocide, and a counter-magnet can be placed at the bottom of the chemical dispensing unit so that when all the biocides When the agent is used up, the two magnets will come close to each other and stick tightly together, thereby acting as a valve mechanism to ensure that the flow of water out of the control device is cut off.
在流过杀菌剂分配单元后,含有杀菌剂的水被储存在系统的贮水室中一段预定的时间。不希望受到理论的限制,据信将含有杀菌剂的水储存长达这段时间是为了确保所有的病原微生物如细菌和病毒能够被杀死。优选水在贮水室中的储存时间为30~300分钟,更优选为60~180分钟。可使用任何使水在水净化系统中储存这样一段时间的方式。比较适合的方式已在WO2004/000732号中被公开。另一种可选的确保水在贮水室中储存这样一段时间的优选方式是通过一些向下的水管将水从化学品分配单元的底部引入到贮水室,在贮水室中通过隔板将近似层流的水分为两层或更多的水平部分。贮水室的进口和每个水平部分的出口的距离为了保证每个进口点和出口点之间的距离最远而取最大值。水流过的长距离和在贮水室中水流动的层流状态确保了所需的储存时间。After flowing through the biocide dispensing unit, the biocide-containing water is stored in the system's reservoir for a predetermined period of time. Without wishing to be bound by theory, it is believed that storing the water containing the biocide for this period of time is to ensure that all pathogenic microorganisms such as bacteria and viruses are killed. Preferably, the storage time of water in the water storage chamber is 30-300 minutes, more preferably 60-180 minutes. Any means of storing the water in the water purification system for such a period of time may be used. A more suitable method is disclosed in WO2004/000732. Another alternative preferred way to ensure that the water is stored in the storage chamber for such a period of time is to introduce water from the bottom of the chemical dispensing unit to the storage chamber through some downpipes, where it passes through a partition Divide nearly laminar water into two or more horizontal sections. The distance between the inlet of the water storage chamber and the outlet of each horizontal section takes the maximum value in order to ensure that the distance between each inlet point and outlet point is the farthest. The long distance the water travels and the laminar flow of the water in the storage chamber ensure the required storage time.
排出贮水室的水在排出水净化系统前还要经过一个清除装置。该清除装置从水中分离出分配的杀菌剂。该清除装置优选为抑菌型活性炭。The water exiting the water storage chamber also passes through a cleaning device before exiting the water purification system. The removal device separates the dispensed biocide from the water. The removal device is preferably antibacterial activated carbon.
尽管水可以上向流或是下向流的方式流经清除装置,但本发明优选上向流。各种具体实施形式可以参照WO2004/014803号专利文献中记载的水流方式。Although water may flow through the removal device in an upflow or downflow fashion, upflow is preferred in the present invention. For various specific implementation forms, reference may be made to the water flow method described in WO2004/014803 patent document.
根据发明的进一步优选特征,提供的重力自流给水净化装置包括:According to a further preferred feature of the invention, the gravity gravity feed water purification device provided comprises:
具有粗过滤器的供水室,待净化的水通过所述粗过滤器被供给进入供水室;a water supply chamber with a coarse filter through which water to be purified is fed into the water supply chamber;
碳块过滤介质和具有相对应形状的无纺织物沉淀过滤器,所述沉淀过滤器可更换/可冲洗,适于从进水中分离颗粒物和溶解物,carbon block filter media and a correspondingly shaped non-woven sediment filter, replaceable/flushable, suitable for separating particulate matter and dissolved matter from the feed water,
其流体连通一个包括指示装置的化学品分配单元,从而使得在水接触由化学品分配单元分配的杀菌剂前,过滤单元的出水流量通过It is in fluid communication with a chemical dispensing unit that includes an indicator device such that the effluent flow from the filter unit passes through the
流量控制装置进行控制,所述流量控制装置包括流量控制箱和虹吸装置,然后水会被储存在The flow control device is controlled by the flow control device, which includes a flow control box and a siphon device, and then the water will be stored in the
贮水室中达一段预定的时间,最后通过in the water storage chamber for a predetermined period of time, and finally through the
一个上向流清除装置排出水净化系统,所述清除装置适于从出水中分离出分配的杀菌剂。An upflow removal device exits the water purification system, the removal device being adapted to separate the dispensed biocide from the effluent water.
下面将通过根据附图1的水净化系统的特定的非限制性实例对本发明加以说明。The invention will be illustrated below by means of a specific non-limiting example of a water purification system according to FIG. 1 .
实例example
图1是根据本发明的水净化系统的一个实施例。该系统具有一个供水室(FC),待净化的水通过粗过滤器(FC)被加到供水室中,所述粗过滤器(FC)粗过滤器适用于捕获大的颗粒。供水容器具有最大20cm的较小高度,其为水通过碳块过滤介质(CBF)进行过滤提供一个低重力压头。一个由无纺织物制成且具有与碳块过滤介质(CBF)相对应形状的沉淀过滤器(SF)被放置其上。该沉淀过滤器去除尺寸在3~6微米的颗粒。碳块过滤器分离出尺寸小于3微米的颗粒、溶解的有机物和杀虫剂。碳块过滤器还过滤具有抗氯性的孢囊。在重力作用下,从碳块过滤器中流出的水进入到流量控制装置(FCM)中,所述流量控制装置包括控制箱和虹吸排放装置,其能够在水与杀菌剂接触前有效地控制水的流量。流量控制装置能够保证将流量控制在一个很窄的范围之内而不用考虑供水室(FC)中的水压头的情况。杀菌剂从化学品分配单元(CDU)中被分配到排出流量控制装置(FCM)的出水中。化学品分配单元具有一堆杀虫剂药片(BT)和一个包括带有颜色的惰性药片的指示装置(IM)。一个透明窗口(TM)被设置在化学品分配单元(CDU)的底部,通过该窗口,当所有的药片被用完时,指示装置(IM)就能被观察到。含有杀菌剂的水接着进入到贮水室(RC),在此将停留一段预先决定的时间以杀死所有病毒和细菌。隔板(B)被设置在贮水室(RC)中以保证水经过选择好的路线流动,以此来确保所希望的停留时间。接下来水以上向流的方式流经清除装置(SM)以分离水中的杀虫剂。然后水在收集室(CC)中收集。最后去除了所有污染物的净化水通过水龙头(T)被分配。Fig. 1 is an embodiment of a water purification system according to the present invention. The system has a water supply chamber (FC) into which the water to be purified is fed through a coarse filter (FC) adapted to capture large particles. The water supply container has a minimum height of 20cm which provides a low gravity head for water to be filtered through carbon block filter media (CBF). A sediment filter (SF) made of non-woven fabric and having a shape corresponding to the carbon block filter medium (CBF) was placed on it. The sediment filter removes particles between 3 and 6 microns in size. The carbon block filter separates out particles less than 3 microns in size, dissolved organics and pesticides. The carbon block filter also filters chlorine resistant cysts. Water exiting the carbon block filter is fed by gravity into a flow control device (FCM) consisting of a control box and a siphon discharge that effectively controls the water before it comes in contact with the biocide traffic. The flow control device can ensure that the flow is controlled within a narrow range regardless of the water pressure head in the water supply chamber (FC). The biocide is distributed from the chemical distribution unit (CDU) into the effluent from the flow control device (FCM). The chemical dispensing unit has a stack of insecticide tablets (BT) and an indicator device (IM) consisting of colored inert tablets. A transparent window (TM) is provided at the bottom of the chemical dispensing unit (CDU), through which the indicator (IM) can be observed when all tablets have been used. The water containing the biocide then enters the Reservoir (RC) where it will stay for a predetermined period of time to kill all viruses and bacteria. Baffles (B) are placed in the reservoir chamber (RC) to ensure that the water flow is routed to ensure the desired residence time. The water then passes through the removal unit (SM) in an upward flow to separate the pesticide from the water. The water is then collected in the collection chamber (CC). Finally purified water with all contaminants removed is dispensed through a tap (T).
因此通过本发明有可能提供一种简单且具有成本效率的重力自流给水净化系统,该系统可在长时间内以所希望的高流量持续地供给去除了所有污染物的干净饮用水,所述污染物包括颗粒物,微生物和包括了杀虫剂残留物的溶解物。It is therefore possible by the present invention to provide a simple and cost-effective gravity-fed water purification system that can continuously supply clean drinking water at a desired high flow rate over a long period of time, free of all contaminants that Matter includes particulate matter, micro-organisms and dissolved matter including pesticide residues.
Claims (21)
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| BR (1) | BRPI0508282B1 (en) |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102548904A (en) * | 2009-09-17 | 2012-07-04 | 荷兰联合利华有限公司 | Water purifying device |
| CN116547243A (en) * | 2020-10-15 | 2023-08-04 | 创新水护理有限责任公司 | Chlorine treatment skimming basket |
Families Citing this family (24)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US8167141B2 (en) | 2004-06-30 | 2012-05-01 | Brita Lp | Gravity flow filter |
| ZA200803892B (en) * | 2005-11-22 | 2009-08-26 | Unilever Plc | Filter cartridge for water purification |
| DE602006004620D1 (en) * | 2005-11-22 | 2009-02-12 | Unilever Nv | FILTER CARTRIDGE FOR WATER CLEANING |
| EP1870381B1 (en) * | 2006-06-12 | 2009-06-24 | Unilever N.V. | A biocide cartridge |
| CN101472659B (en) * | 2006-06-23 | 2012-01-11 | 荷兰联合利华有限公司 | Filter and process to prepare the same |
| USD615150S1 (en) | 2007-09-20 | 2010-05-04 | Omnipure Filter Co., Inc. | Filter block for liquid filtration |
| USD617869S1 (en) | 2009-03-25 | 2010-06-15 | Omnipure Filter Co., Inc. | Filter block for liquid filtration |
| UA100688C2 (en) * | 2007-04-18 | 2013-01-25 | Юнилевер Н.В. | Disinfectant unit and method for disinfection of water |
| USD612906S1 (en) | 2007-09-20 | 2010-03-30 | Omnipure Filter Company, Inc. | Filter block for liquid filtration |
| USD614259S1 (en) | 2007-09-20 | 2010-04-20 | Omnipure Filter Company, Inc. | Filter block for liquid filtration |
| USD615149S1 (en) | 2007-09-20 | 2010-05-04 | Omnipure Filter Company, Inc. | Filter block for liquid filtration |
| MX2011003140A (en) * | 2008-09-23 | 2011-05-25 | Unilever Nv | Water purification device. |
| EP2184263A1 (en) | 2008-11-06 | 2010-05-12 | Unilever N.V. | Water purification device |
| NZ603933A (en) | 2009-01-13 | 2014-03-28 | Access Business Group Int Llc | Gravity feed water treatment system |
| USD645538S1 (en) | 2009-03-25 | 2011-09-20 | Omnipure Filter Company, Inc. | Filter block for liquid filtration |
| USD618761S1 (en) | 2009-03-25 | 2010-06-29 | Omnipure Filter Company, Inc. | Filter block for liquid filtration |
| WO2011151157A1 (en) * | 2010-05-31 | 2011-12-08 | Unilever Nv | A fortificant dispensing device |
| EA021746B1 (en) | 2010-05-31 | 2015-08-31 | Юнилевер Н.В. | WATER TREATMENT DEVICE |
| PL2603460T3 (en) | 2010-08-09 | 2014-11-28 | Unilever Nv | Low cost water purification device |
| MX2013002056A (en) * | 2010-08-24 | 2013-04-03 | Unilever Nv | WATER PURIFICATION DEVICE INCLUDING A FILTER FEEDED BY GRAVITY. |
| WO2014003841A1 (en) * | 2012-06-29 | 2014-01-03 | 3M Innovative Properties Company | Gravity feed fluid purification system |
| WO2014016082A1 (en) | 2012-07-23 | 2014-01-30 | Unilever N.V. | Biocidal filter medium |
| CN104870376B (en) * | 2012-12-20 | 2016-11-23 | 荷兰联合利华有限公司 | Tablet composition for automatic closing mechanism |
| CN109231314A (en) * | 2018-11-19 | 2019-01-18 | 江苏绿途环保科技有限公司 | A kind of high-effect drinking-water filter |
Family Cites Families (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| TW469832U (en) * | 1997-03-14 | 2001-12-21 | Astra Ab | Inhalation device |
| RU2125974C1 (en) * | 1997-08-21 | 1999-02-10 | Закрытое акционерное общество "АКВАФОР" | Method of liquid purification by filtering and filter for liquid purification |
| DE19844167A1 (en) * | 1998-09-25 | 2000-04-06 | Ticona Gmbh | Activated carbon filter |
| US6281802B1 (en) * | 1998-12-01 | 2001-08-28 | Aerobic & Pump Controls, Inc. | Automatic chlorinator alarm system |
| JP3535992B2 (en) * | 1999-07-08 | 2004-06-07 | 株式会社アルソア本社 | Retention cartridge used for water purifier |
| US6309551B1 (en) * | 1999-09-14 | 2001-10-30 | Hoot Aerobic Systems, Inc. | Solution treatment agent supply apparatus |
| CN2508230Y (en) * | 2001-10-18 | 2002-08-28 | 刘崇崑 | Liquid supply device that can maintain a constant flow rate |
| RU2188165C1 (en) * | 2001-11-29 | 2002-08-27 | Гутенев Владимир Владимирович | Method of multi-stage through purification of water |
| CN1331762C (en) * | 2002-06-19 | 2007-08-15 | 荷兰联合利华有限公司 | Water purification system |
| RU2364912C2 (en) * | 2003-02-18 | 2009-08-20 | Юнилевер Н.В. | Water-purifying system for control of biocides discharge in water |
-
2005
- 2005-03-01 ZA ZA200606790A patent/ZA200606790B/en unknown
- 2005-03-01 CN CNB2005800085032A patent/CN100556821C/en not_active Expired - Fee Related
- 2005-03-01 WO PCT/EP2005/002254 patent/WO2005095284A1/en not_active Ceased
- 2005-03-01 BR BRPI0508282-0A patent/BRPI0508282B1/en not_active IP Right Cessation
- 2005-03-01 PL PL380684A patent/PL380684A1/en unknown
- 2005-03-01 RU RU2006136907/15A patent/RU2379235C2/en not_active IP Right Cessation
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102548904A (en) * | 2009-09-17 | 2012-07-04 | 荷兰联合利华有限公司 | Water purifying device |
| CN102548904B (en) * | 2009-09-17 | 2014-03-19 | 荷兰联合利华有限公司 | water purification device |
| CN116547243A (en) * | 2020-10-15 | 2023-08-04 | 创新水护理有限责任公司 | Chlorine treatment skimming basket |
Also Published As
| Publication number | Publication date |
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| RU2379235C2 (en) | 2010-01-20 |
| CN100556821C (en) | 2009-11-04 |
| BRPI0508282A (en) | 2007-08-07 |
| ZA200606790B (en) | 2007-11-28 |
| WO2005095284A1 (en) | 2005-10-13 |
| PL380684A1 (en) | 2007-03-05 |
| BRPI0508282B1 (en) | 2015-08-18 |
| RU2006136907A (en) | 2008-04-27 |
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