KR20090032345A - Ro type purifier - Google Patents

Ro type purifier Download PDF

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KR20090032345A
KR20090032345A KR1020070097509A KR20070097509A KR20090032345A KR 20090032345 A KR20090032345 A KR 20090032345A KR 1020070097509 A KR1020070097509 A KR 1020070097509A KR 20070097509 A KR20070097509 A KR 20070097509A KR 20090032345 A KR20090032345 A KR 20090032345A
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South Korea
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filter
reverse osmosis
water
ion exchange
concentrated water
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KR1020070097509A
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Korean (ko)
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KR101443909B1 (en
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윤종현
김대환
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웅진코웨이주식회사
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D61/00Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/02Reverse osmosis; Hyperfiltration ; Nanofiltration
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D35/00Filtering devices having features not specifically covered by groups B01D24/00 - B01D33/00, or for applications not specifically covered by groups B01D24/00 - B01D33/00; Auxiliary devices for filtration; Filter housing constructions
    • B01D35/02Filters adapted for location in special places, e.g. pipe-lines, pumps, stop-cocks
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/44Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis

Abstract

A reverse osmosis water purification system is provided to extend lifetime of an ion exchange filter by processing the small amount of concentrate with the ion exchange filter and to recycle the concentrate as raw water to be purified by passing directly the concentrate through a reverse osmosis filter. A reverse osmosis water purification system includes a reverse osmotic pressure filter, an ion exchange filter, a flowing pipe, and a flow control unit(130). A flux control unit includes a valve body(132), a ball(137), and a control unit(140). The flux control unit is installed between the reverse osmotic pressure filter and the ion exchange filter. A flowing passage(133) is formed in the valve body. A cylindrical groove(134) is formed on one side of the flowing passage.

Description

역삼투 정수장치{RO TYPE PURIFIER}Reverse Osmosis Water Purification System {RO TYPE PURIFIER}

본 발명은 역삼투 정수장치에 관한 것으로서, 보다 상세하게는 역삼투압에 의해 정수가 이루어지는 멤브레인 필터에서 삼투압과 확산에 의한 역류가 방지되는 역삼투 정수장치에 관한 것이다.The present invention relates to a reverse osmosis water purification device, and more particularly, to a reverse osmosis water purification device in which reverse flow due to osmotic pressure and diffusion is prevented in a membrane filter in which water purification is performed by reverse osmosis.

일반적으로, 정수 장치는 원수 공급원으로부터 공급되는 원수를 필터링하여 사용자가 음용하기 위한 식수로 사용하거나 기타 용도에 사용하기 위한 것으로서, 정수기가 대표적인 예이다.In general, the water purifying device is to be used as drinking water for the user to drink by filtering the raw water supplied from the raw water supply source, or water purifier is a typical example.

한편, 정수 장치의 필터링 수단으로서 역삼투(Reverse Osmosis, RO) 멤브레인 모듈을 사용하는 경우, RO 멤브레인 모듈로 공급되는 원수 중 일부는 멤브레인에 의해 정수되어 정수수가 되고, 나머지는 용존 불순물이 포함된 농축수가 된다.On the other hand, when using a reverse osmosis (RO) membrane module as a filtering means of the water purification device, some of the raw water supplied to the RO membrane module is purified by the membrane to become purified water, the rest is concentrated with dissolved impurities It becomes a number.

이때, 정수수는 집수관으로 모아진 후 사용할 수 있게 배출되어 음용될 수 있으나, 농축수는 사용되지 못하고 배수관 등에 버려지게 되므로, 원수가 효율적으로 정수되지 못하는 문제점이 있었다.At this time, the purified water may be discharged to be used after being collected into the collecting pipe, but may be consumed, but since the concentrated water is not used and is discarded in the drainage pipe, there is a problem in that the raw water may not be purified effectively.

일반적인 정수기의 RO필터에서 발생한 원수의 낭비를 해결할 수 있는 기술이 등록실용신안20-0265610에 "폐수 없는 역삼투압 정수장치"로서 개시되어 있다.A technique that can solve the waste of raw water generated in the RO filter of a general water purifier is disclosed in the registered utility model 20-0265610 as a "reverse osmosis water purification device without wastewater".

여기서, 종래기술로서"폐수 없는 역삼투압 정수장치"는 RO필터에서 발생된 농축수를 폐수 재처리 필터에서 여과한 후 고탁도 필터를 거친 원수와 합수탱크에서 합류시킴으로써 농축수의 배수를 방지하게 되어 있다.Here, the conventional "reverse osmosis water purification device without waste water" is to prevent the drainage of the concentrated water by condensing the concentrated water generated in the RO filter in the wastewater reprocessing filter and then joining the raw water through the high turbidity filter in the mixing tank. have.

그러나, 종래기술은 고탁도 필터가 필요하지 않은 현재기술 상황에서 고탁도 필터를 세디먼트 필터 앞에 불필요하게 배치하고 있다. 즉, 세디먼트 필터가 고탁도 기능을 동시에 할 수 있고, 고탁도 기능은 해외 국가에서 필요한 기능이며, 국내에서는 필요가 없는 기능이다.However, the prior art unnecessarily arranges the high turbidity filter in front of the sediment filter in the state of the art in which the high turbidity filter is not necessary. That is, the sediment filter can simultaneously perform a high turbidity function, and the high turbidity function is a function required in an overseas country, and is a function not necessary in a domestic country.

그리고, 종래기술은 이온교환 필터를 재활용하기 위해서 소금(NaCl)을 이용한다. 그러나, 이온교환 필터를 재활용하는 기술은 노동비용과 환경비용을 생각하면 값이 저렴한 이온교환 필터를 일회용으로 하는 것이 더 경제적이다. 그리고, 종래기술은 합수탱크를 고탁도 필터 뒤, 세디먼트 필터 앞에 설치했다. 즉, 농축수는 RO필터에서 배수되기 전에 프리카본 필터를 통과하는데, 다시 앞의 필터로 되돌려 이미 통과한 프리카본 필터로 다시 유입시키는 것은 바람직하지 못하다.And, the prior art uses salt (NaCl) to recycle the ion exchange filter. However, the technology of recycling the ion exchange filter is more economical to use the inexpensive ion exchange filter for single use in consideration of labor cost and environmental cost. In the prior art, the condensation tank was installed after the high turbidity filter and before the sediment filter. In other words, the concentrated water passes through the precarbon filter before being drained from the RO filter, and it is not preferable to return the filter to the previous filter and return it to the precarbon filter that has already passed.

즉, 농축수는 RO필터를 통과하지 못해서 이온만 농축되어 있는 상태이므로 이온교환 필터를 통과한 후 관로가 RO필터 전, 프리카본 필터 후에 연결되는 것이 더 합리적이다. 여기서, 합수 탱크가 필요하다면 RO필터 전, 프리카본 필터 후에 연결하면 된다.In other words, since the concentrated water does not pass through the RO filter and only the ions are concentrated, it is more reasonable to connect the pipe after passing through the ion exchange filter before the RO filter and after the free carbon filter. Here, if a water tank is required, it may be connected before the RO filter and after the free carbon filter.

본 발명은 상기한 종래 기술의 문제점을 해결하기 위하여 안출된 것으로서, RO필터의 여과작용에 의해 만들어진 농축수가 폐수로서 방류됨을 방지하기 위해 농축수의 용존 불순물을 이온교환 필터에서 제거한 후 프리카본 필터를 거치지 않고 RO필터로 직접 통과시켜 정수될 원수로서 재활용할 수 있는 역삼투 정수장치를 제공함이 목적이다.The present invention has been made to solve the above-described problems of the prior art, the pre-carbon filter after removing the dissolved impurities in the concentrated water in the ion exchange filter to prevent the concentrated water produced by the filtration action of the RO filter as waste water It is an object of the present invention to provide a reverse osmosis water purification device that can be recycled as raw water to be purified by passing directly through a RO filter.

본 발명에 따른 역삼투 정수장치의 구성은 일측에서 유입된 원수를 역삼투압에 의해 정수하여 용존 불순물이 제거된 정수수와 용존 불순물의 농도가 높아진 농축수로 각각 배출하는 역삼투압 필터와, 상기 역삼투압 필터에서 배출된 농축수에서 용존 불순물의 농도를 낮추는 이온교환 필터 및 상기 이온교환 필터에서 용존 불순물의 농도가 낮아진 농축수를 상기 역삼투압 필터로 직접 유입시키는 유동관을 포함한다.The reverse osmosis water purifying apparatus according to the present invention comprises a reverse osmosis filter for discharging raw water introduced from one side by purified reverse osmosis and purifying the purified water having dissolved impurities removed and the concentrated water having a higher concentration of dissolved impurities, and the reverse osmosis pressure. An ion exchange filter for lowering the concentration of dissolved impurities in the concentrated water discharged from the filter, and a flow tube for directly introducing the concentrated water having a low concentration of dissolved impurities in the ion exchange filter into the reverse osmosis filter.

여기서, 상기 역삼투압 필터와 상기 이온교환 필터 사이에는 상기 역삼투압 필터에서 상기 이온교환 필터로 유동하는 농축수의 유량을 상기 역삼투압 필터에서 배출되는 정수수의 유량에 따라 조절하는 유량조절수단이 구비될 수 있다.Here, between the reverse osmosis filter and the ion exchange filter is provided with a flow rate adjusting means for adjusting the flow rate of the concentrated water flowing from the reverse osmosis filter to the ion exchange filter in accordance with the flow rate of the purified water discharged from the reverse osmosis filter Can be.

그리고, 상기 유량조절수단은 일측에서 농축수가 유입되어 타측으로 배출되게 형성되며, 농축수가 유동하는 유동통로가 내부에 형성되고, 상기 유동통로의 일 측 벽에 원통홈이 형성된 밸브몸체와, 상기 밸브몸체의 유동통로에 배치되어 농축수에 대한 유동저항을 제공하거나 솔레노이드의 작동에 의해 상기 원통홈으로 내입되어 상기 유동통로의 유동량을 증가시키는 볼과, 상기 솔레노이드를 주기적으로 작동시켜 상기 유동통로를 통과하는 농축수의 유동량을 주기적으로 증가시키는 제어부를 포함한다.In addition, the flow rate control means is formed so that the concentrated water flows from one side and discharged to the other side, a flow passage through which the concentrated water flows is formed therein, a valve body having a cylindrical groove formed on one side wall of the flow passage, and the valve A ball disposed in the flow passage of the body to provide flow resistance to the concentrated water or to be introduced into the cylindrical groove by the operation of the solenoid to increase the flow volume of the flow passage, and to periodically operate the solenoid to pass through the flow passage. And a controller for periodically increasing the flow rate of the concentrated water.

이때, 상기 역삼투압 필터의 일측에는 상기 이온교환 필터에서 용존 불순물이 낮아진 농축수와 합류되기 위한 원수가 여과되는 세디먼트 필터와 프리카본 필터가 배치된다.At this time, one side of the reverse osmosis filter is a sediment filter and a precarbon filter for filtering the raw water to join the concentrated water is lowered in the dissolved impurities in the ion exchange filter.

또한, 상기 세디먼트 필터와 상기 프리카본 필터는 상기 역삼투압 필터로 유입되는 원수가 차례로 지나게 하나의 케이스에 내에 배치되어 복합필터를 구성한다.In addition, the sediment filter and the precarbon filter are disposed in one case so as to pass raw water flowing into the reverse osmosis filter to form a composite filter.

상기와 같이 구성되는 본 발명에 의한 역삼투 정수장치는 RO필터의 여과작용에 의해 만들어진 농축수가 폐수로서 방류됨을 방지하기 위해 농축수의 용존 불순물을 이온교환필터에서 제거한 후 프리카본필터를 거치지 않고 RO필터로 직접 통과시켜 정수될 원수로서 재활용할 수 있는 효과를 얻을 수 있다.The reverse osmosis water purifying apparatus according to the present invention configured as described above removes the dissolved impurities in the concentrated water from the ion exchange filter to prevent the concentrated water produced by the filtration of the RO filter as wastewater, and then passes the RO filter without passing through the precarbon filter. It can be directly recycled as raw water to be purified by direct passage.

그리고, 농축수 저감밸브로서 유량조절수단이 정수기에 설치됨으로써 농축수가 절반 가까이 줄어든다. 따라서 제안하는 자사 정수기 시스템은 기존 특허 정수기보다 적은 양의 농축수를 이온교환 필터로 처리하기 때문에 이온교환 필터의 수 명이 더 길다.As the concentrated water reducing valve is installed in the water purifier, the concentrated water is reduced by almost half. Therefore, the proposed company's water purifier system has a longer life of ion exchange filter because it treats less concentrated water with ion exchange filter than the existing patented water purifier.

이하, 본 발명에 따른 역삼투 정수장치의 바람직한 실시예를 첨부된 도면을 참조하여 설명한다. 이 과정에서 도면에 도시된 선들의 두께나 구성요소의 크기 등은 설명의 명료성과 편의상 과장되게 도시되어 있을 수 있다. 또한, 후술되는 용어들은 본 발명에서의 기능을 고려하여 정의된 용어들로서 이는 사용자, 운용자의 의도 또는 관례에 따라 달라질 수 있다. 그러므로, 이러한 용어들에 대한 정의는 본 명세서 전반에 걸친 내용을 토대로 내려져야 할 것이다.Hereinafter, with reference to the accompanying drawings a preferred embodiment of the reverse osmosis water purification apparatus according to the present invention. In this process, the thickness of the lines or the size of the components shown in the drawings may be exaggerated for clarity and convenience of description. In addition, terms to be described below are terms defined in consideration of functions in the present invention, which may vary according to the intention or convention of a user or an operator. Therefore, definitions of these terms should be made based on the contents throughout the specification.

이하, 첨부된 도면들을 참조하여 본 발명에 따른 역삼투 정수장치의 바람직한 실시예를 첨부된 도면을 참조하여 설명한다. 또한, 하기 실시예는 본 발명의 권리범위를 한정하는 것이 아니라 단지 예시로 제시하는 것이며, 본 기술 사상을 통해 구현되는 다양한 실시예가 있을 수 있다.Hereinafter, with reference to the accompanying drawings will be described a preferred embodiment of the reverse osmosis water purification apparatus according to the present invention with reference to the accompanying drawings. In addition, the following examples are not intended to limit the scope of the present invention but merely presented by way of example, and there may be various embodiments implemented through the present invention.

실시예Example

도 1은 본 발명의 일 실시예에 따른 역삼투 정수장치의 계통도이고, 도 2는 도 1의 유량조절수단의 상세 단면도이며, 도 3은 도 2에 도시된 유량조절수단이 작동도이다.1 is a system diagram of a reverse osmosis water purification apparatus according to an embodiment of the present invention, Figure 2 is a detailed cross-sectional view of the flow control means of Figure 1, Figure 3 is an operation diagram of the flow control means shown in FIG.

도 1 내지 도 3에 도시된 바와 같이, 본 발명의 일 실시예에 따른 역삼투압 정수기는 일측에서 유입된 원수를 역삼투압에 의해 정수하여 용존 불순물이 제거된 정수수와 용존 불순물의 농도가 높아진 농축수로 각각 배출하는 역삼투압 필터(100) 및 역삼투압 필터(100)에서 배출된 농축수에서 용존 불순물의 농도를 낮추는 이온교환 필터(120)를 포함한다.As shown in Figures 1 to 3, the reverse osmosis water purifier according to an embodiment of the present invention purified by the reverse osmosis of the raw water introduced from one side of the purified water and the concentration of the dissolved impurities and the concentration of the dissolved impurities is removed The reverse osmosis filter 100 and the ion exchange filter 120 for lowering the concentration of dissolved impurities in the concentrated water discharged from the reverse osmosis filter 100, respectively.

여기서, 이온교환 필터(120)와 하류에는 용존 불순물의 농도가 낮아진 농축수를 역삼투압 필터(100)로 직접 유입시키는 유동관(122)이 포함될 수 있으며, 유동관(122)은 역삼투압 필터(100)로 원수를 공급하는 원수관(110)이 역삼투압 필터(100)에 연결되기 바로 직전에 연결됨으로써 이온교환 필터(120)를 통과한 농축수는 다른 필터를 거치지 않고 역삼투압 필터(100)로 바로 유입될 수 있다.Here, the ion exchange filter 120 and downstream may include a flow tube 122 for directly introducing the concentrated water of which the concentration of dissolved impurities is lowered into the reverse osmosis filter 100, the flow tube 122 is a reverse osmosis filter 100 The raw water pipe 110 for supplying the raw water is directly connected to the reverse osmosis filter 100 so that the concentrated water passing through the ion exchange filter 120 passes directly to the reverse osmosis filter 100 without passing through another filter. Can be introduced.

즉, 원수와 이온교환 필터(120)에서 용존 불순물이 제거된 농축수는 역삼투압 필터(100)로 유입되어 역삼투압 필터(100)의 RO 멤브레인에서 역삼투압 작용에 의해 정수수와 농축수로 분리되고, 농축수는 역삼투압 필터(100)에서 재차 이온교환 필터(120)로 유입되며, 정수수는 역삼투압 필터(100)에 연결된 포스트 카본필터(125)로 유입되어 여과된 후 음용 가능하게 메인탱크(127)에 저장될 수 있다.That is, the concentrated water from which dissolved impurities are removed from the raw water and the ion exchange filter 120 is introduced into the reverse osmosis filter 100 and separated into purified water and concentrated water by reverse osmosis at the RO membrane of the reverse osmosis filter 100. The concentrated water is introduced into the ion exchange filter 120 again from the reverse osmosis filter 100, and the purified water is introduced into the post carbon filter 125 connected to the reverse osmosis filter 100, filtered, and then used for drinking. 127).

여기서, 역삼투압 필터(100)와 이온교환 필터(120) 사이에는 역삼투압 필터(100)에서 이온교환 필터(120)로 유동하는 농축수의 유량을 역삼투압 필터(100)에서 배출되는 정수수의 유량에 따라 조절하는 유량조절수단(130)이 구비될 수 있다.Here, the flow rate of the purified water discharged from the reverse osmosis filter 100 to the flow rate of the concentrated water flowing from the reverse osmosis filter 100 to the ion exchange filter 120 between the reverse osmosis filter 100 and the ion exchange filter 120. It may be provided with a flow control means 130 to adjust according to.

이때, 유량조절수단(130)은 역삼투압 필터(100)에서 유출되는 농축수의 유량을 감소시켜 이온교환 필터(120)로 유입되는 농축수의 유량을 줄이기 위한 것으로서, 역삼투압 필터(100)에서 농축수의 농도가 증가하여 역삼투압 필터(100)에서 포 스트 카본필터(125) 측으로 유동되는 정수수의 유량이 현저하게 감소하는 상태를 방지한다.At this time, the flow rate control means 130 is to reduce the flow rate of the concentrated water flowing into the ion exchange filter 120 by reducing the flow rate of the concentrated water flowing out of the reverse osmosis filter 100, in the reverse osmosis filter 100 The concentration of the concentrated water is increased to prevent a state in which the flow rate of purified water flowing from the reverse osmosis filter 100 to the post carbon filter 125 side is significantly reduced.

상세하게는, 유량조절수단(130)은 일측에서 농축수가 유입되어 타측으로 배출되게 형성되며, 농축수가 유동하는 유동통로(133)가 내부에 형성되고, 유동통로(133)의 일측 벽에 원통홈(134)이 형성된 밸브몸체(132)와, 밸브몸체(132)의 유동통로(133)에 배치되어 농축수에 대한 유동저항을 제공하거나 솔레노이드(135)의 작동에 의해 원통홈(134)으로 내입되어 유동통로(133)의 유동량을 증가시키는 볼(137)과, 솔레노이드(135)를 주기적으로 작동시켜 유동통로(133)를 통과하는 농축수의 유동량을 주기적으로 증가시키는 제어부(140)를 포함한다.In detail, the flow regulating means 130 is formed so that the concentrated water flows from one side to be discharged to the other side, a flow passage 133 through which the concentrated water flows is formed therein, and a cylindrical groove on one wall of the flow passage 133. 134 is formed in the valve body 132 and the flow passage 133 of the valve body 132 to provide a flow resistance to the concentrated water or to enter the cylindrical groove 134 by the operation of the solenoid 135 And a ball 137 that increases the flow amount of the flow passage 133, and a controller 140 that periodically operates the solenoid 135 to periodically increase the flow amount of the concentrated water passing through the flow passage 133. .

역삼투압 필터(100)에서 배출되는 농축수의 유량이 감소할 때 역삼투압 필터(100)의 정수효율은 감소하게 되어 정수수의 배출이 현전하게 감소될 수 있으므로, 제어부(140)는 역삼투압 필터(100)에서 농도가 증가된 농축수를 솔레노이드(135)를 작동시켜 주기적으로 이온교환 필터(120) 측에 대한 농축수의 유동량을 증가시키게 된다.When the flow rate of the concentrated water discharged from the reverse osmosis filter 100 is reduced, the water purification efficiency of the reverse osmosis filter 100 is reduced, so that the discharge of purified water can be reduced significantly, the control unit 140 is a reverse osmosis filter ( In operation 100, the solenoid 135 is operated to increase the concentration of the concentrated water to increase the flow rate of the concentrated water to the ion exchange filter 120 side.

여기서, 볼(137)은 밸브몸체(132)의 유동통로(133)를 차단하고 있다가 솔레노이드(135)에 의해 밸브몸체(132)의 원통홈(134) 측으로 이동되어 유동통로(133)를 통과하는 농축수의 유량을 증가시키게 되며, 제어부(140)는 솔레노이드(135)를 주기적으로 작동시키도록 프로그램화된 마이크로컨트롤러를 구비할 수 있다.Here, the ball 137 blocks the flow passage 133 of the valve body 132 and is moved to the cylindrical groove 134 side of the valve body 132 by the solenoid 135 to pass through the flow passage 133. In order to increase the flow rate of the concentrated water, the control unit 140 may include a microcontroller programmed to periodically operate the solenoid 135.

그리고, 역삼투압 필터(100)의 일측에는 이온교환 필터(120)에서 용존 불순물이 낮아진 농축수와 합류되기 위한 원수가 여과되는 세디먼트 필터(142)와 프리 카본 필터(143)가 배치되어야 한다.And, on one side of the reverse osmosis filter 100, a sediment filter 142 and a pre-carbon filter 143 through which raw water is filtered to join with concentrated water having a low dissolved impurity in the ion exchange filter 120 should be disposed.

또한, 세디먼트 필터(142)와 프리카본 필터(143)는 역삼투압 필터(100)로 유입되는 원수가 차례로 지나게 하나의 케이스 내에 배치되어 복합필터(145)를 구성함으로써 소형화된 정수장치를 제공할 수 있다.In addition, the sediment filter 142 and the pre-carbon filter 143 are arranged in one case so that the raw water flowing into the reverse osmosis filter 100 in order to form a complex filter 145 to provide a compact water purification device. Can be.

도 1은 본 발명의 일 실시예에 따른 역삼투 정수장치의 계통도이다.1 is a system diagram of a reverse osmosis water purification device according to an embodiment of the present invention.

도 2는 도 1의 유량조절수단의 상세 단면도이다.2 is a detailed cross-sectional view of the flow control means of FIG.

도 3은 도 2에 도시된 유량조절수단의 작동도이다.3 is an operation of the flow control means shown in FIG.

<도면의 주요 부분에 관한 부호의 설명><Explanation of symbols on main parts of the drawings>

100: 역삼투압 필터 110: 원수관100: reverse osmosis filter 110: raw water pipe

120: 이온교환 필터 122: 유동관120: ion exchange filter 122: flow tube

125: 포스트 카본필터 127: 메인탱크125: post carbon filter 127: main tank

130: 유량조절수단 132: 밸브몸체130: flow rate control means 132: valve body

133: 유동통로 134: 원통홈133: flow passage 134: cylindrical groove

135: 솔레노이드 137: 볼135: solenoid 137: ball

140: 제어부 142: 세디먼트 필터140: control unit 142: sediment filter

143: 프리카본 필터 145: 복합필터143: pre-carbon filter 145: composite filter

Claims (5)

일측에서 유입된 원수를 역삼투압에 의해 정수하여 용존 불순물이 제거된 정수수와 용존 불순물의 농도가 높아진 농축수로 각각 배출하는 역삼투압 필터;A reverse osmosis filter which purifies raw water introduced from one side by reverse osmosis to discharge purified water from which dissolved impurities are removed and concentrated water having a higher concentration of dissolved impurities; 상기 역삼투압 필터에서 배출된 농축수에서 용존 불순물의 농도를 낮추는 이온교환 필터; 및An ion exchange filter for lowering the concentration of dissolved impurities in the concentrated water discharged from the reverse osmosis filter; And 상기 이온교환 필터에서 용존 불순물의 농도가 낮아진 농축수를 상기 역삼투압 필터로 직접 유입시키는 유동관을 포함하는 역삼투 정수장치.Reverse osmosis water purification apparatus comprising a flow pipe for directly introducing the concentrated water of the concentration of dissolved impurities in the ion exchange filter to the reverse osmosis filter. 제 1 항에 있어서,The method of claim 1, 상기 역삼투압 필터와 상기 이온교환 필터 사이에는 상기 역삼투압 필터에서 상기 이온교환 필터로 유동하는 농축수의 유량을 상기 역삼투압 필터에서 배출되는 정수수의 유량에 따라 조절하는 유량조절수단이 구비되는 것을 특징으로 하는 역삼투 정수장치.Between the reverse osmosis filter and the ion exchange filter is provided with a flow rate adjusting means for adjusting the flow rate of the concentrated water flowing from the reverse osmosis filter to the ion exchange filter in accordance with the flow rate of purified water discharged from the reverse osmosis filter Reverse osmosis water purification device. 제 2 항에 있어서,The method of claim 2, 상기 유량조절수단은 일측에서 농축수가 유입되어 타측으로 배출되게 형성되며, 농축수가 유동하는 유동통로가 내부에 형성되고, 상기 유동통로의 일측 벽에 원통홈이 형성된 밸브몸체;The flow rate control means is formed to be discharged to the other side by the inflow of concentrated water from one side, the flow passage through which the concentrated water is formed therein, the valve body formed with a cylindrical groove on one side wall of the flow passage; 상기 밸브몸체의 유동통로에 배치되어 농축수에 대한 유동저항을 제공하거나 솔레노이드의 작동에 의해 상기 원통홈으로 내입되어 상기 유동통로의 유동량을 증가시키는 볼; 및A ball disposed in the flow passage of the valve body to provide a flow resistance to the concentrated water or to be introduced into the cylindrical groove by the operation of the solenoid to increase the flow volume of the flow passage; And 상기 솔레노이드를 주기적으로 작동시켜 상기 유동통로를 통과하는 농축수의 유동량을 주기적으로 증가시키는 제어부를 포함하는 것을 특징으로 하는 역삼투 정수장치.And a control unit periodically operating the solenoid to periodically increase the flow amount of the concentrated water passing through the flow passage. 제 1 항에 있어서,The method of claim 1, 상기 역삼투압 필터의 일측에는 상기 이온교환 필터에서 용존 불순물이 낮아진 농축수와 합류되기 위한 원수가 여과되는 세디먼트 필터와 프리카본 필터가 배치되는 것을 특징으로 하는 역삼투 정수장치.One side of the reverse osmosis filter is a reverse osmosis water purification device, characterized in that the sediment filter and pre-carbon filter for filtering the raw water to join the concentrated water is lowered in the dissolved impurities in the ion exchange filter. 제 4 항에 있어서,The method of claim 4, wherein 상기 세디먼트 필터와 상기 프리카본 필터는 상기 역삼투압 필터로 유입되는 원수가 차례로 지나게 하나의 케이스 내에 배치되어 복합필터를 구성하는 것을 특징으로 하는 역삼투 정수장치.The sediment filter and the pre-carbon filter is reverse osmosis water purification apparatus, characterized in that the raw water flowing into the reverse osmosis filter is disposed in one case to form a composite filter.
KR1020070097509A 2007-09-27 2007-09-27 Ro type purifier KR101443909B1 (en)

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KR20110058972A (en) * 2009-11-27 2011-06-02 웅진코웨이주식회사 A system for regenerating ion exchange resin and regeneration method of the same

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KR20020076197A (en) * 2001-03-27 2002-10-09 아쿠아텍아시아(주) Reverse Osmosis Water Purification Apparatus for Coercive Circulation of Waste Water
JP2005510338A (en) * 2001-04-18 2005-04-21 バディ ドン グレイ, System for recirculating tangential filtration concentrate

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20110058972A (en) * 2009-11-27 2011-06-02 웅진코웨이주식회사 A system for regenerating ion exchange resin and regeneration method of the same

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