KR20030094144A - water main direct connection in water clean machine - Google Patents
water main direct connection in water clean machine Download PDFInfo
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- KR20030094144A KR20030094144A KR1020030074815A KR20030074815A KR20030094144A KR 20030094144 A KR20030094144 A KR 20030094144A KR 1020030074815 A KR1020030074815 A KR 1020030074815A KR 20030074815 A KR20030074815 A KR 20030074815A KR 20030094144 A KR20030094144 A KR 20030094144A
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- South Korea
- Prior art keywords
- filter
- water
- chamber
- activated carbon
- block
- Prior art date
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 147
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 143
- 239000012528 membrane Substances 0.000 claims abstract description 48
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 43
- 239000012510 hollow fiber Substances 0.000 claims abstract description 27
- 239000000919 ceramic Substances 0.000 claims abstract description 18
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 claims abstract description 16
- 229910052709 silver Inorganic materials 0.000 claims abstract description 16
- 239000004332 silver Substances 0.000 claims abstract description 16
- 230000008878 coupling Effects 0.000 claims description 19
- 238000010168 coupling process Methods 0.000 claims description 19
- 238000005859 coupling reaction Methods 0.000 claims description 19
- 239000004698 Polyethylene Substances 0.000 claims description 14
- 238000000034 method Methods 0.000 claims description 10
- 238000004062 sedimentation Methods 0.000 claims description 10
- 230000000845 anti-microbial effect Effects 0.000 claims description 8
- 238000001914 filtration Methods 0.000 claims description 7
- 238000011049 filling Methods 0.000 claims description 6
- 238000007500 overflow downdraw method Methods 0.000 claims description 6
- 239000004599 antimicrobial Substances 0.000 claims description 5
- 238000002955 isolation Methods 0.000 claims description 5
- 239000002245 particle Substances 0.000 claims description 5
- 239000004745 nonwoven fabric Substances 0.000 claims description 4
- -1 polyethylene Polymers 0.000 claims description 4
- 239000000945 filler Substances 0.000 claims description 3
- 229910001111 Fine metal Inorganic materials 0.000 claims description 2
- 238000002347 injection Methods 0.000 claims description 2
- 239000007924 injection Substances 0.000 claims description 2
- 238000009434 installation Methods 0.000 claims description 2
- 230000002093 peripheral effect Effects 0.000 claims description 2
- 229920000573 polyethylene Polymers 0.000 claims description 2
- 230000004308 accommodation Effects 0.000 claims 1
- 239000000126 substance Substances 0.000 claims 1
- 238000001556 precipitation Methods 0.000 abstract description 10
- 230000005465 channeling Effects 0.000 abstract description 6
- 230000000844 anti-bacterial effect Effects 0.000 abstract description 5
- 239000007787 solid Substances 0.000 abstract description 4
- 241000894006 Bacteria Species 0.000 description 5
- 239000008213 purified water Substances 0.000 description 4
- 239000012535 impurity Substances 0.000 description 3
- 229910052500 inorganic mineral Inorganic materials 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 239000011707 mineral Substances 0.000 description 3
- 239000000356 contaminant Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 229910001385 heavy metal Inorganic materials 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 230000001376 precipitating effect Effects 0.000 description 2
- 230000001902 propagating effect Effects 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 230000001580 bacterial effect Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 230000035622 drinking Effects 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 238000007373 indentation Methods 0.000 description 1
- 230000002401 inhibitory effect Effects 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 230000000149 penetrating effect Effects 0.000 description 1
- 239000011941 photocatalyst Substances 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D36/00—Filter circuits or combinations of filters with other separating devices
- B01D36/04—Combinations of filters with settling tanks
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D27/00—Cartridge filters of the throw-away type
- B01D27/08—Construction of the casing
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D35/00—Filtering 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
-
- 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
-
- 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
-
- 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
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/444—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by ultrafiltration or microfiltration
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/002—Construction details of the apparatus
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Water Treatment By Sorption (AREA)
Abstract
Description
본 발명은 씽크대에 설치된 수전구에 직접 연결하여 사용하거나 씽크대 아래에 설치하여 사용하는 수도 직결식 정수기에 관한 것이다.The present invention relates to a water direct type water purifier that is used by directly connecting to a power outlet installed in a sink, or installed and used under a sink.
주지된 바와 같이 수도 직결식 정수기는, 수도꼭지 또는 수전구에 연결되는 씽크대 내의 원수라인과 간단하게 연결하여 가정에서 간편하게 정수된 물을 취수 및 음용할 수 있도록하고, 냉장고 및 냉온수기 등의 주방용 생활가전제품에 연결하여 사용하는 것이다.As is well known, the water direct connection water purifier can be easily connected to the raw water line in the sink connected to the faucet or faucet so that the purified water can be easily ingested and consumed at home, and household appliances such as refrigerators and hot and cold water heaters To use it.
상기 수도 직결식 정수기는, 일반적으로 원수라인에서 공급된 물이 수압에 의해 직렬로 연결 배치된 다수의 필터를 순차적으로 통과하면서 정수되도록 구성되는 것으로, 이러한 다단계 휠터를 적용한 종래 수도 직결식 정수기의 구성을 설명하면 다음과 같다.The water direct connection water purifier is generally configured such that water supplied from a raw water line is purified while sequentially passing through a plurality of filters arranged in series by water pressure, and constitutes a conventional water direct connection water purifier to which such a multi-stage filter is applied. This is as follows.
도 1에 도시된 바와 같이 원수라인에서 유입된 원수를 1차 여과하도록 부직포 등으로 된 침전필터(11)가 구비되고, 상기 침전필터(11)를 통과한 물을 2차 여과하도록 입상활성탄필터(12)가 구비된 카본블록필터(10)와; 상기카본블록필터(10)를 통과한 물을 여과하도록 입상활성탄(21)과 세라믹(22)이 분리 충진된 카트리지필터(20)와; 상기 카트리지피터(20)를 통과한 물을 세균 및 미세불순물은 여과하고 미네랄은 통과시키도록 중공사막 멤브레인(31)을 구비하고, 그 하부에 세균번식을 억제하도록 은활성탄(32)을 충진시킨 중공사막필터(30)로 구성된다.As shown in FIG. 1, a sedimentation filter 11 made of a nonwoven fabric or the like is provided to primaryly filter the raw water introduced from the raw water line, and the granular activated carbon filter is configured to secondaryly filter the water passing through the precipitation filter 11. 12) is provided with a carbon block filter (10); A cartridge filter (20) in which granular activated carbon (21) and ceramics (22) are separated and filled to filter the water passing through the carbon block filter (10); Hollow fiber membrane 31 is provided with a hollow fiber membrane membrane 31 to filter bacteria and fine impurities and water to pass through the cartridge peter 20, and a silver activated carbon 32 is filled therein to suppress bacterial growth. It is composed of a desert filter (30).
또한 상기 침전필터(11)의 하부 중심에 원수라인과 급수관(1)이 연결되고, 침전필터(11)의 상부 중심과 입상활성탄필터(12)의 하부 중심, 그리고 입상활성탄필터(12)의 상부 중심과 카트리지필터(20)의 하부 중심, 그리고 카트리지필터(20)의 상부 중심과 중공사막필터(30)의 하부 중심이 각각 연결관(2)(2')(2")에 의해 순차적으로 연결된다.In addition, the raw water line and the water supply pipe 1 is connected to the lower center of the precipitation filter 11, the upper center of the precipitation filter 11, the lower center of the granular activated carbon filter 12, and the upper portion of the granular activated carbon filter 12 The center and the lower center of the cartridge filter 20, the upper center of the cartridge filter 20 and the lower center of the hollow fiber membrane filter 30 are sequentially connected by connecting tubes 2, 2 ', 2 ", respectively. do.
그런데 상기와 같이 구성된 종래의 수도 직결식 정수기는, 카본블록필터(10)가 부직포로 등으로 이루어진 침전필터(11)와 입상활성탄필터(12)로 각각 구성됨으로서, 구조가 복잡할 뿐만 아니라 여과효율이 저하되는 문제점이 있다.However, the conventional water direct type water purifier configured as described above is composed of a precipitation filter 11 and a granular activated carbon filter 12 each of which the carbon block filter 10 is made of a nonwoven fabric or the like. There is a problem of this deterioration.
또한 상기 카본블록필터(10)와 카트리지필터(20)로 급수되는 물이 하부에서 상부를 향해 일 방향으로 통수됨으로서, 충진물과의 접촉시간이 짧아 정수효과가 저하되는 문제점이 있으며, 수압에 의해 원수가 상향으로 통과할 때 물길이 한 쪽으로 생기는 채널링(channeling)현상이 발생하여 원수에 함유되어 있는 부유물질 및 불순물이 여과되지 않고 그대로 통과하게 되어 정수효과를 저하시키는 문제점이 있다.In addition, the water supplied to the carbon block filter 10 and the cartridge filter 20 is passed in one direction from the bottom to the top, there is a problem that the contact time with the filling is shortened so that the water purification effect is lowered, the raw water by the water pressure When the water passes upward, the channeling phenomenon occurs in one side of the water path, causing the suspended solids and impurities contained in the raw water to pass through without being filtered, thereby reducing the water purification effect.
또한 카트리지필터(20)를 통과한 물과 함께 활성탄이 중공사막필터(30)로 유입되면, 입상이 날카로운 활성탄의 직접적인 접촉에 의해 멤브레인(31)을 손상시키게 되는 문제점이 있으며, 멤브레인(31)을 통과하여 유로에 잔류한 물에 외부로부터 유입된 세균이 번식하는 것을 방지하기 위하여 광촉매, UV-램프 등과 같은 별도의 멸균장치가 요구되는 비경제적인 문제점이 있다.In addition, when activated carbon is introduced into the hollow fiber membrane filter 30 together with the water passing through the cartridge filter 20, the granules may be damaged by the direct contact of the activated carbon having a sharp granularity. There is an uneconomical problem that a separate sterilization device such as a photocatalyst, a UV-lamp, etc. is required in order to prevent the bacteria introduced from the outside into the water remaining in the flow path.
또한 각 필터의 챔버(40)에 내용물을 충진시킨 후 상부캡(41)을 복개하여 연결부 가장자리를 초음파로 가열하여 접합시키거나 회전에 의한 마찰접착을 시키게 되는데, 이러한 초음파 접착의 경우, 활성탄 분진 등의 영향에 의해 접합면에 편차가 발생하게 되고, 회전에 의한 마찰접착의 경우, 도 2에 도시된 바와 같이 상부캡(41)의 가장자리가 외향으로 돌출되는 현상(burr)이 생기며, 이를 제거하기 위한 후처리 작업의 공정이 별도로 필요하므로 작업능률이 떨어져 생산성이 저하되는 문제점이 있다.In addition, after filling the contents into the chamber 40 of each filter, the upper cap 41 is covered, and the edges of the connecting parts are heated by ultrasonic bonding or bonded by friction, and in the case of such ultrasonic bonding, activated carbon dust, etc. Deviation occurs in the joint surface by the influence of, and in the case of friction bonding by rotation, as shown in Figure 2, the edge of the upper cap 41 protrudes outward (burr) occurs, to remove it Since the post-treatment process is required for the separate process, there is a problem that the work efficiency is lowered and the productivity is lowered.
본 발명은 상술한 바와 같은 종래의 제반 문제점을 해결하기 위한 것으로, 그 목적은, 침전필터와 활성탄필터를 하나의 카본블록필터로 단일화하여 복합적인 기능을 수행할 수 있도록 하며, 각 필터로 통수되는 물과 충진물과의 접촉시간을 증대시켜 채널링(channeling)현상을 방지함으로서 부유물질을 효과적으로 여과할 수 있고, 활성탄이 중공사막필터로 유입되는 것을 차단하여 날카로운 입상의 활성탄에 의해 멤브레인이 손상되는 것을 방지하며, 멤브레인을 통과한 후 잔류한 물에 세균이 번식하는 것을 방지할 수 있고, 각 필터의 챔버와 상부캡을 견고하고 미려하게 결합할 수 있는 수도직결식 정수기를 제공함에 있다.The present invention is to solve the conventional problems as described above, the object of the sedimentation filter and the activated carbon filter to a single carbon block filter to perform a complex function, and passed through each filter By increasing the contact time between the water and the fillers to prevent channeling phenomenon, it is possible to effectively filter the suspended solids and to prevent the activated carbon from entering the hollow fiber membrane filter to prevent damaging the membrane by the sharp granular activated carbon. In addition, it is possible to prevent bacteria from propagating in the remaining water after passing through the membrane, and to provide a water-directed water purifier capable of firmly and beautifully coupling the chamber and the upper cap of each filter.
이러한 목적을 달성하기 위한 본 발명 수도직결식 정수기는, 급수관으로 공급된 물이 외곽의 PE블록(침전블록)을 통과하면서 침전된 후 내측으로 유입되어 카본블록의 하부 중앙으로 통수되도록 카본블록필터를 구성하고, 상기 카본블록필터를 통해 여과되어 하부 중앙으로 배출된 물이 하부 중앙에서 상부 중앙으로 유입된 후 입상활성탄과 세라믹을 순차적으로 통과하여 하부 외곽으로 통수되도록 카트리지필터를 구성하며, 상기 카트리지필터의 하부 외곽으로 배출된 물이 하부외곽을 통하여 은활성탄을 상향으로 통과하고, 은활성탄을 통과한 물이 상부 외곽에서 다시 여과된 후 멤브레인을 하향으로 통과하며, 멤브레인을 통과한 물은 항균실에 잔류한 후 하부 중앙으로 통수되어 토출관으로 배출하도록 중공사막필터를 구성하는 것을 특징으로 하는 것이다.The water direct connection water purifier of the present invention for achieving this purpose, the carbon block filter so that the water supplied to the water supply pipe is precipitated while passing through the outer PE block (sedimentation block) is introduced into the inner side to pass through the lower center of the carbon block. The cartridge filter is configured so that the water filtered through the carbon block filter and discharged to the lower center flows from the lower center to the upper center, and then passes through the granular activated carbon and ceramics sequentially and passes through the lower outer area. The water discharged to the lower outer portion of the passes through the lower activated carbon through the silver activated carbon upwards, the water passing through the silver activated carbon is filtered again in the upper outer portion and passes downward through the membrane, and the water passing through the membrane passes through the antimicrobial chamber. It is characterized in that the hollow fiber membrane filter is configured to pass through to the lower center after the remaining It is.
또한 본 발명 수도직결식 정수기는, 각 필터의 챔버와 상부캡을 회전융착방식으로 형합한 것을 특징으로 하는 것이다.In addition, the water direct connection water purifier of the present invention is characterized in that the chamber and the upper cap of each filter are molded in a rotary fusion method.
도 1은 종래에 원수를 여과하는 필터의 구성을 나타낸 개략 단면도1 is a schematic cross-sectional view showing a configuration of a filter for filtering raw water in the related art.
도 2는 종래의 초음파방식으로 융착시킨 필터케이스의 단면도2 is a cross-sectional view of a filter case fused by a conventional ultrasonic method
도 3은 본 발명이 적용된 수도 직결식 정수기의 사시도3 is a perspective view of a water direct type water purifier to which the present invention is applied.
도 4는 본 발명이 적용된 수도 직결식 정수기의 단면도4 is a cross-sectional view of the water direct type water purifier to which the present invention is applied.
도 5는 본 발명이 적용된 카본블록필터를 나타낸 단면도5 is a cross-sectional view showing a carbon block filter to which the present invention is applied.
도 6은 본 발명이 적용된 카트리지필터를 나타낸 단면도Figure 6 is a cross-sectional view showing a cartridge filter to which the present invention is applied
도 7은 본 발명이 적용된 카트리지필터의 지지부재를 나타낸 사시도Figure 7 is a perspective view showing a support member of the cartridge filter to which the present invention is applied
도 8은 본 발명이 적용된 카트리지필터의 여과판을 나타낸 사시도Figure 8 is a perspective view showing a filter plate of the cartridge filter to which the present invention is applied
도 9는 본 발명이 적용된 중공사막필터를 나타낸 단면도9 is a cross-sectional view showing a hollow fiber membrane filter to which the present invention is applied
도 10은 본 발명이 적용된 중공사막필터의 지지부재를 나타낸 사시도10 is a perspective view showing a supporting member of the hollow fiber membrane filter to which the present invention is applied
도 11은 본 발명이 적용된 수도 직결식 정수기의 작동상태도11 is an operating state of the water direct type water purifier to which the present invention is applied.
<도면의 주요 부분에 대한 부호의 설명><Explanation of symbols for the main parts of the drawings>
100: 카본블록필터 130: 카본블록100: carbon block filter 130: carbon block
140: PE블록(침전블록) 200: 카트리지필터140: PE block (precipitation block) 200: cartridge filter
240: 세라믹 260: 입상활성탄240: ceramic 260: granular activated carbon
300: 중공사막필터 340: 항균실300: hollow fiber membrane filter 340: antibacterial chamber
350: 맴브레인 360: 은활성탄350: membrane 360: silver activated carbon
이하 첨부된 도면에 의거하여 본 발명 일 실시예의 구성을 상세히 설명한다. 도 3은 본 발명이 적용된 수도 직결식 정수기의 사시도이고, 도 4는 본 발명이 적용된 수도 직결식 정수기의 단면도이다.Hereinafter, the configuration of an embodiment of the present invention will be described in detail with reference to the accompanying drawings. 3 is a perspective view of a water direct type water purifier to which the present invention is applied, and FIG. 4 is a cross-sectional view of a water direct type water purifier to which the present invention is applied.
본 발명 정수기는, 급수관(1)으로 공급된 물이 외곽의 PE블록(침전블록)(140)을 통과하면서 침전된 후 내측으로 유입되어 카본블록(130)의 하부 중앙으로 통수되도록 카본블록필터(100)를 구성하고, 상기 카본블록필터(100)를 통해 여과되어 하부 중앙으로 배출된 물이 하부 중앙에서 상부 중앙으로 유입된 후 입상활성탄(260)과 세라믹(240)을 순차적으로 통과하여 하부 외곽으로 통수되도록 카트리지필터(200)를 구성하며, 상기 카트리지필터(200)의 하부 외곽으로 배출된 물이 하부외곽을 통하여 은활성탄(360)을 상향으로 통과하고, 은활성탄(360)을 통과한 물이 상부 외곽에서 다시 여과된 후 멤브레인(340)을 하향으로 통과하며, 멤브레인(340)을 통과한 물은 항균실(330)에 잔류한 후 하부 중앙으로 통수되어 토출관(410)으로 배출하도록 중공사막필터(300)를 구성한다.The water purifier of the present invention, the water supplied to the water supply pipe (1) is precipitated while passing through the PE block (sedimentation block) 140 of the outside and then introduced into the carbon block filter so as to pass through the lower center of the carbon block 130 ( 100), and the water filtered through the carbon block filter 100 and discharged to the lower center flows from the lower center to the upper center, and then passes through the granular activated carbon 260 and the ceramic 240 in sequence to the lower outer portion. The cartridge filter 200 is configured to pass through the water, and the water discharged to the lower outer portion of the cartridge filter 200 passes upward through the lower activated carbon to the silver activated carbon 360 and passes through the silver activated carbon 360. After the filter is filtered again at the upper outer side, the membrane 340 passes downward, and the water passing through the membrane 340 remains in the antimicrobial chamber 330 and passes through the lower center to be discharged into the discharge tube 410. Configure the desert filter 300 .
그리고 이러한 각 필터(100)(200)(300)는 직립된 상태로 순차적으로 배치되고, 그 외곽에는 상부가 개폐되는 함체상의 케이스(400)로 감싸도록 구성되며, 상부 일측으로 방향 전환이 가능하도록 플랙시블한 토출관(410)이 구비되어 중공사막필터(300)의 출구에 연결되고, 케이스(400)의 전방 중앙에는 각 필터의 교환시기를 디스플레이하는 인디케이터(420)가 장착되는 것으로, 이를 좀더 구체적으로 설명하면 다음과 같다.And each of these filters 100, 200, 300 are sequentially arranged in an upright state, the outer portion is configured to wrap in a case 400 on the enclosure that is opened and closed, so that the direction can be switched to one side of the upper The flexible discharge pipe 410 is provided to be connected to the outlet of the hollow fiber membrane filter 300, the front center of the case 400 is equipped with an indicator 420 for displaying the replacement time of each filter, more Specifically, it is as follows.
상기 카본블록필터(100)는, 도 5에 도시된 바와 같이, 상부가 개방된 원통형 용기의 내부와 연통되도록 내주면에 나사산이 형성되어 상부로 돌출된 지지편(111)이 하부에 관통되고, 이 지지편(111)의 둘레에 일정각도 이격되게 안내공(112)이 관통되며, 상기 원통형 용기의 상면에 소정깊이의 결합홈(113)이 형성된 챔버(110)가 구비되고, 상기 지지편(111)의 나사산에 내부가 관통된 체결편(121)이 체결되며, 이 체결편(121)의 상부로 중앙에 통로를 형성하도록 보스(122)가 상향으로 돌출되고, 외주면에 안내리브(123)가 상기 챔버(110)의 하부 내주면에 밀착되어 원수가 이동될 수 있는 유입로(124)를 형성한 하부고정부재(120)가 구비된다.As shown in FIG. 5, the carbon block filter 100 has a thread formed on an inner circumferential surface thereof so as to communicate with an interior of an open cylindrical container, and a support piece 111 protruding upward is passed through the lower portion thereof. The guide hole 112 penetrates a predetermined angle around the support piece 111, and a chamber 110 having a coupling groove 113 having a predetermined depth is formed on an upper surface of the cylindrical container, and the support piece 111 is provided. The fastening piece 121 through which the inside penetrates to the thread of the screw), and the boss 122 protrudes upward to form a passage in the center of the fastening piece 121, and the guide rib 123 is formed on the outer circumferential surface thereof. The lower fixing member 120 is formed in close contact with the lower inner circumferential surface of the chamber 110 to form an inflow path 124 through which raw water can move.
또한, 상기 보스(121)의 상면으로 중앙에 통로(131)가 형성되도록 입상활성탄을 압착 성형한 카본블록(130)을 구비하고, 그 외주면에는 다공성 폴리에틸렌(부직포 등)의 재질로 상기 카본블록(130)면을 소정 두께로 감싸 형성한 PE블록(침전블록)(140)을 안착시키며, 상기 카본블록(130)과 PE블록(침전블록)(140)의 상면에 장착되어 상기 챔버(110)의 상부 내주면을 밀폐시키고 중앙에 통로를 형성할 수 있는 보스(151)가 하향으로 돌출된 상부고정부재(150)가 구비되고, 상기 챔버(110)의 결합홈(113)에 대응하도록 결합돌기(161)가 하향으로 돌출된 고정캡(160)을 회전시키면서 강제로 압입하는 회전융착방식으로 접합시킨다.In addition, the upper surface of the boss 121 is provided with a carbon block 130 is formed by pressing the granular activated carbon to form a passage 131 in the center, the outer peripheral surface of the carbon block (such as non-woven fabric) of the polyethylene ( 130 is seated on the PE block (precipitating block) 140 formed by wrapping the surface with a predetermined thickness, and is mounted on the upper surface of the carbon block 130 and PE block (precipitating block) 140 of the chamber 110 The upper fixing member 150 is provided with a boss 151 which seals the upper inner circumferential surface and forms a passage in the center, and protrudes downward, and the coupling protrusion 161 to correspond to the coupling groove 113 of the chamber 110. ) Is joined in a rotary fusion method forcibly press-fitting while rotating the fixing cap 160 protruding downward.
상기 카트리지필터(200)는, 도 6에 도시된 바와 같이, 상부가 개방된 원통형 용기의 내부와 연통되도록 상부로 돌출된 지지편(211)이 하부에 관통되고, 이 지지편(211)의 둘레에 일정각도 이격되게 안내공(212)이 관통되며, 상기 원통형 용기의 내주면 상.하부에 걸림턱(213)(213')이 형성되고, 상면에 소정깊이의 결합홈(214)이 형성된 챔버(210)가 구비되며, 상기 챔버(210)의 상.하부 걸림턱(213)(213')에 안착되어 상기 카본블록필터(100)를 통과한 물의 이물질과 충진물을 여과시키는 상.하부 여과판(220)(220')이 구비된다.As shown in FIG. 6, the cartridge filter 200 has a support piece 211 protruding upward so as to communicate with an inside of an open cylindrical container. The guide hole 212 penetrates at a predetermined angle to the chamber, and the locking jaws 213 and 213 'are formed on the upper and lower inner circumferential surfaces of the cylindrical container, and a chamber in which the coupling groove 214 of a predetermined depth is formed on the upper surface. 210 is provided, the upper and lower filter plate 220 which is seated on the upper and lower locking jaw (213, 213 ') of the chamber 210 to filter the foreign matter and the filling of water passing through the carbon block filter 100. 220 'is provided.
또한, 상기 상.하부 여과판(220)(220')의 사이에 장착되어 일측 단부가 상기 챔버(210)의 지지편(211)에 결합되도록 내부가 관통된 보스(231)가 형성되고, 이 보스(231)의 하단부 외주면에 하기의 세라믹(240)이 골고루 충진되도록 안내하는날개(232)가 방사상으로 형성된 지지부재(230)가 도 7에 도시된 바와 같이 구비되며, 상기 하부여과판(220')의 상부에 세라믹(240)이 상기 지지부재(230)의 날개(232)에 의해 챔버(210)의 내부에 골고루 충진된다.In addition, a boss 231 is formed between the upper and lower filter plates 220 and 220 ′ so that one end thereof is coupled to the support piece 211 of the chamber 210. A support member 230 having a radially formed wing 232 for guiding the ceramic 240 to be evenly filled on the outer circumferential surface of the lower end of 231 is provided as shown in FIG. 7, and the lower filtration plate 220 ′. On top of the ceramic 240 is evenly filled in the interior of the chamber 210 by the wing 232 of the support member 230.
또한, 상기 세라믹(240)의 상면으로 하기의 입상활성탄(260)의 입자는 통과시키지 않고 물만 통과시키는 격리부재(250)가 구비되며, 상기 격리부재(250)와 상부여과판(220)의 사이에는 입상활성탄(260)이 충진되고, 상기 챔버(210)의 결합홈(214)에 대응하도록 결합돌기(271)가 하향으로 돌출된 고정캡(270)을 회전시키면서 강제로 압입하는 회전융착방식으로 접합시킨다.In addition, the upper surface of the ceramic 240 is provided with an isolation member 250 for passing only the water without passing the particles of the granular activated carbon 260 below, between the isolation member 250 and the upper filter plate 220 The granular activated carbon 260 is filled and joined in a rotary fusion method forcibly indenting while rotating the fixing cap 270 protruding downward from the coupling protrusion 271 to correspond to the coupling groove 214 of the chamber 210. Let's do it.
상기 상.하부여과판(220)(220')은, 도 8에 도시된 바와 같이, 중앙에 설치공이 관통되어 리브가 형성된 상.하부몸체(221)(222)의 사이에 미세한 금속망(223)을 인서트 사출에 의해 고정시킨다.As illustrated in FIG. 8, the upper and lower filtration plates 220 and 220 ′ include a fine metal mesh 223 between upper and lower bodies 221 and 222 having ribs formed by penetrating an installation hole in a center thereof. Secure by insert injection.
상기 지지부재(230)의 날개(232)는, 상기 세라믹(240)을 안내하는 안내편(222a)이 상.하부에 형성되고, 이 안내편(222a)의 사이에 세라믹(240)이 이동될 수 있도록 이동공간(222b)이 적층되게 형성된다.The wing 232 of the support member 230, the guide piece 222a for guiding the ceramic 240 is formed on the upper and lower sides, the ceramic 240 is to be moved between the guide piece 222a. The moving space 222b is formed to be stacked so that it can be stacked.
상기 중공사막필터(300)는, 도 9에 도시된 바와 같이, 상부가 개방된 원통형 용기의 내부와 연통되도록 상부로 돌출된 지지편(311)이 하부에 관통되고, 이 지지편(311)의 둘레에 일정각도 이격되게 안내공(312)이 관통되며, 상기 원통형 용기의 내주면 상.하부에 걸림턱(313)(313')이 형성되고, 상면에 소정깊이의 결합홈(314)이 형성된 챔버(310)가 구비되며, 상기 챔버(310)의 상.하부 걸림턱(313)(313')에 안착되어 상기 카트리지필터(200)를 통과한 물의 이물질과 충진물을 여과시키는하.상부 여과판(320)(320')이 구비된다.As shown in FIG. 9, the hollow fiber membrane filter 300 has a support piece 311 protruding upwardly so as to communicate with an inside of a cylindrical container having an upper portion penetrated through the lower portion of the hollow fiber membrane filter 300. The guide hole 312 penetrates at a predetermined angle around the chamber, and upper and lower locking jaws 313 and 313 'are formed on the inner and outer circumferential surfaces of the cylindrical container, and a chamber in which a coupling groove 314 of a predetermined depth is formed on the upper surface. It is provided with a 310, the upper and lower locking projections (313, 313 ') of the chamber 310, the lower and upper filter plate 320 for filtering foreign matter and the filling of water passing through the cartridge filter 200. 320 'is provided.
또한, 상기 하부 여과판(320')의 상부에 안착되어 상기 챔버(310)의 지지편(311)에 결합되도록 내부가 관통된 보스(331)가 형성되며, 이 보스(331)의 상부에 수용공간(332)이 형성되며, 상기 보스(331)의 외주면에 하기의 은활성탄(360)이 골고루 충진되도록 날개(333)가 방사상으로 형성된 지지부재(330)가 도 10에 도시된 바와 같이 구비된다.In addition, a boss 331 is formed in the upper portion of the lower filter plate 320 'and penetrated therein so as to be coupled to the support piece 311 of the chamber 310. 332 is formed, and the support member 330 is radially provided with a wing 333 so that the silver activated carbon 360 below is evenly filled on the outer circumferential surface of the boss 331, as shown in FIG. 10.
또한, 상기 지지부재(330)의 수용공간(332)에 항균제(341)를 함유한 항균실(340)이 구비되며, 이 항균실(340)의 상부인 수용공간(332)에 맴브레인(350)이 내장된 맴브레인하우징(351)을 안착시키고, 상기 하.상부 여과판(320)(320')의 사이에 은활성탄(360)을 지지부재(330)의 날개(333)를 회전시키면서 챔버(310)의 내부에 골고루 충진시키며, 상기 챔버(310)의 결합홈(314)에 대응하도록 결합돌기(371)가 하향으로 돌출되고, 내부에 에어밴트(372)가 장착된 고정캡(370)을 회전시키면서 강제로 압입하는 회전융착방식으로 접합시킨다.In addition, an antimicrobial chamber 340 containing an antimicrobial agent 341 is provided in the receiving space 332 of the support member 330, and the membrane 350 is disposed in the receiving space 332 which is an upper portion of the antimicrobial chamber 340. The built-in membrane housing 351 is seated, and the chamber 310 is rotated while the wing 333 of the support member 330 rotates the activated carbon 360 between the lower and upper filter plates 320 and 320 '. Filling the inside evenly, the coupling protrusion 371 protrudes downward to correspond to the coupling groove 314 of the chamber 310, while rotating the fixing cap 370 is equipped with an air vent 372 therein It is joined by the rotation welding method which is forced indentation.
한편 상기와 같이 구성된 카본블록필터(100)와 카트리지필터(200) 및 중공사막필터(300)를 각각의 연결관(2)으로 연결하고, 상기 카본블록필터(100)에는 급수관(1)을 연결하며, 상기 중공사막필터(300)에는 토출관(410)을 연결하여 케이스(400)의 내부에 위치시킨 후, 상기 중공사막필터(300)의 일측에 여과되어 배출되는 정수의 량을 측정하는 인디케이터(420)를 장착한다.Meanwhile, the carbon block filter 100, the cartridge filter 200, and the hollow fiber membrane filter 300 configured as described above are connected to each of the connection pipes 2, and the water supply pipe 1 is connected to the carbon block filter 100. The hollow fiber membrane filter 300 is connected to the discharge pipe 410 and positioned inside the case 400, and then measures an amount of purified water discharged by being filtered on one side of the hollow fiber membrane filter 300. 420 is mounted.
상기와 같이 구성된 본 발명의 작동과정을 설명하면 다음과 같다.Referring to the operation of the present invention configured as described above are as follows.
먼저, 도 11에 도시된 바와 같이, 급수관(1)을 통해 유입되는 원수는, 수압에 의해 챔버(110)의 안내공(112)을 통과하여 하부고정부재(120)의 유입로(124)를 경유하여 챔버(110)의 내주면을 따라 상부로 유입하면서 원수에 함유되어 있는 입자가 큰 이물질을 PE블록(침전블록)(140)에서 침전시키면서 여과시키고, 여과된 물은 PE블록(침전블록)(140)을 통과하게 된다.First, as shown in FIG. 11, the raw water flowing through the water supply pipe 1 passes through the guide hole 112 of the chamber 110 by hydraulic pressure, thereby opening the inflow path 124 of the lower fixing member 120. While passing through the inner circumferential surface of the chamber 110 through the upper part, the foreign particles having large particles contained in the raw water are filtered while precipitated in the PE block (sedimentation block) 140, and the filtered water is PE block (sedimentation block) ( 140).
또한, 상기 PE블록(침전블록)(140)을 통과한 물은, 다시 카본블록(130)을 통과하면서 유기성 오염물질과 중금속을 제거한다.In addition, the water passing through the PE block (precipitation block) 140, while passing through the carbon block 130 again to remove organic contaminants and heavy metals.
이때, 상기 카본블록필터(100)로 유입되는 원수가 챔버(110)의 내주면을 따라 상부로 유입되면서 PE블록(침전블록)(140)의 외주면을 통해 골고루 유입되기 때문에 채널링(channeling) 현상을 미연에 방지할 수 있는 것이다.At this time, since the raw water flowing into the carbon block filter 100 flows upward along the inner circumferential surface of the chamber 110 and evenly flows through the outer circumferential surface of the PE block (sedimentation block) 140, the channeling phenomenon is not shown. To prevent it.
한편, 상기 카본블록(130)을 통과한 물은, 카본블록(130)의 통로(131)를 따라 하부로 이동하여 하부고정부재(120)의 체결편(121) 내측으로 배출되는 것이다.On the other hand, the water passing through the carbon block 130 is moved downward along the passage 131 of the carbon block 130 is discharged into the fastening piece 121 of the lower fixing member 120.
그리고, 상기와 같은 과정을 통해 카본블록필터(100)에 여과되어 배출된 물은 연결관(2)을 통해 카트리지필터(200)의 내부로 유입된다.Then, the water filtered and discharged to the carbon block filter 100 through the above process is introduced into the cartridge filter 200 through the connection pipe (2).
이때, 상기 카트리지필터(200)의 내부로 유입된 물은, 지지부재(230)의 보스(231) 내부를 경유하여 하부중앙에서 상부중앙으로 유입되며, 상부중앙으로 유입된 물이 상기 보스(231)의 단부를 중심으로 하여 외측으로 분산된다.In this case, the water introduced into the cartridge filter 200 flows from the lower center to the upper center via the boss 231 of the support member 230, and the water introduced into the upper center is the boss 231. It is distributed to the outside about the end of the).
이렇게 물이 분산되면, 상부여과판(220)의 금속망(223)에서 카본블록필터(100)를 통과하여 유입되는 물속에 함유된 이물질을 여과시켜 하부로 배출한다.When water is dispersed in this way, the foreign matter contained in the water flowing through the carbon block filter 100 in the metal mesh 223 of the upper filter plate 220 is filtered and discharged to the lower portion.
또한, 상기 상부여과판(220)의 하부로 배출된 물은 입상활성탄(260)을 통과하면서 다시 유기성 오염물질을 제거함과 동시에 격리부재(250)에서 입상활성탄(260)과 물을 분리하여 입상활성탄(260)은 통과시키지 않고 여과된 물만 통과시킨다.In addition, the water discharged to the lower portion of the upper filtration plate 220 passes through the granular activated carbon 260 to remove organic contaminants again and at the same time separates the granular activated carbon 260 and the water from the sequestering member 250 to obtain granular activated carbon ( 260 does not pass, but only filtered water.
한편, 상기 격리부재(250)를 통과한 물은, 중금속을 흡착시키고, 칼슘 등의 미네랄과 철이온을 공급하며 원적외선을 방사하는 세락믹(240)을 경유면서 챔버(210)의 하부로 이동하며, 하부여과판(220')의 금속망(223)에서 세라믹(240)의 분말이나 가루와 물을 분리하여 미네날과 철이온이 공급된 물만 통과시켜 챔버(210)의 안내공(212)을 통과하여 카트리지필터(200)의 외곽으로 배출되는 것이다.Meanwhile, the water passing through the isolation member 250 adsorbs heavy metals, supplies minerals such as calcium and iron ions, and moves to the lower portion of the chamber 210 via the ceramic 240 which emits far infrared rays. By separating the powder or powder and water of the ceramic 240 from the metal mesh 223 of the lower filtration plate 220 'and passing only the water supplied with the mineral and the iron ions, it passes through the guide hole 212 of the chamber 210. It is discharged to the outside of the cartridge filter 200.
이때, 카본블록필터(100)를 통과하여 지지부재(230)의 내부로 유입되어 지지부재(230)의 단부에서 외측으로 분산되어 하부로 이동되는 물이 카트리지필터(200)의 내부에 충진된 충진물과의 접촉시간을 증대시켜 정수의 효율을 증대시키게 되는 것이다.At this time, the water that passes through the carbon block filter 100 into the support member 230 and is dispersed outward from the end of the support member 230 and moved to the bottom is filled in the cartridge filter 200. Increasing the contact time with the will increase the efficiency of the purified water.
또한, 상기 카트리지필터(200)에서 여과되어 배출된 물은 연결관(2)을 통해 중공사막필터(300)의 내부로 유입된다.In addition, the water filtered and discharged from the cartridge filter 200 is introduced into the hollow fiber membrane filter 300 through the connection pipe (2).
이때, 상기 중공사막필터(200)의 내부로 유입된 물은, 챔버(310)의 안내공(312)으로 유입되어 하부여과판(320)의 금속망에서 카트리지필터(200)에서 여과된 물을 다시 여과시켜 상향으로 유입시키면, 은활성탄(360)에서 잔류염소나유기물질을 제거하고, 항균기능을 발휘하며 이미, 이취 등을 해결할 수 있다.At this time, the water introduced into the hollow fiber membrane filter 200 is introduced into the guide hole 312 of the chamber 310 and the water filtered by the cartridge filter 200 in the metal mesh of the lower filter plate 320 again. When the filter is introduced upwards, it removes residual chlorine or organic matter from the silver activated carbon 360, exerts antibacterial function, and can solve the odor.
상기 은활성탄(360)을 경유하는 물은, 상부여과판(320')에서 날카로운 입자의 은활성탄(360)과 물을 분리하여 여과된 물만 통과시키게 되며, 상기 상부여과판(320')을 통과한 물은 0.1㎛ 이하의 중공사막이 세균 및 미세불순물을 여과시키고, 몸에 유익한 미네랄은 통과시키는 맴브레인(340)을 하향으로 통과하여 항균실(330)에 잔류하며, 상기 항균실(330)에 잔류한 물은 항균제(331)에 의해 미생물의 증식을 억제하고 물때의 형성을 방지하면서 위생적으로 사용할 수 있으며, 상기 항균실(330)을 경유한 물은 지지부재(330)의 보스(331)를 통과하여 중공사막필터(300)의 외곽으로 배출되는 것이다.The water passing through the silver activated carbon 360 separates the silver activated carbon 360 and the water of the sharp particles from the upper filter plate 320 'and passes only the filtered water, and the water passed through the upper filter plate 320'. The hollow fiber membrane of 0.1 μm or less passes through the membrane 340 through which bacteria and fine impurities are filtered, and minerals that are beneficial to the body pass downward to remain in the antibacterial chamber 330, and remain in the antibacterial chamber 330. Water can be used hygienically while inhibiting the growth of microorganisms by the antimicrobial agent 331, and prevents the formation of scale, water passing through the antimicrobial chamber 330 passes through the boss 331 of the support member 330 It is discharged to the outside of the hollow fiber membrane filter (300).
상기의 과정을 통해 정수된 물은, 토출관(410)을 통해 배출되며, 컵과 같은 용기에 저장하여 음용할 수 있고, 상기 정수의 사용량을 측정하여 필터의 교환시키를 인디케이터(420)에 표시하고, 표시된 내용으로 필터를 교환하여 사용하면 되는 것이다.The water purified through the above process is discharged through the discharge pipe 410, and stored in a container such as a cup for drinking, and the indicator of the use of the purified water to measure the replacement of the filter on the indicator 420 And replace the filter with the displayed content.
이상에서와 같이 본 발명은, 침전필터와 활성탄필터를 하나의 카본블록필터로 단일화하여 복합적인 기능을 수행할 수 있도록 하고, 각 필터로 통수되는 물과 충진물과의 접촉시간을 증대시켜 채널링(channeling)현상을 방지함으로서 부유물질을 효과적으로 여과할 수 있도록 하며, 활성탄이 중공사막필터로 유입되는 것을 차단하여 날카로운 입상의 활성탄에 의해 멤브레인이 손상되는 것을 방지할 수 있고,멤브레인을 통과한 후 잔류한 물에 세균이 번식하는 것을 방지할 수 있으며, 각 필터의 챔버와 상부캡을 견고하고 미려하게 접합시킬 수 있는 이점을 가지는 것이다.As described above, the present invention, the precipitation filter and the activated carbon filter can be combined into a single carbon block filter to perform a complex function, and the channeling (channeling) by increasing the contact time of the water and the fillers passed through each filter By preventing phenomena, it is possible to effectively filter suspended solids, prevent activated carbon from entering the hollow fiber membrane filter, and prevent the membrane from being damaged by sharp granular activated carbon.The water remaining after passing through the membrane The bacteria can be prevented from propagating and have the advantage of firmly and beautifully bonding the chamber and the upper cap of each filter.
Claims (6)
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Cited By (3)
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KR100765827B1 (en) * | 2006-08-01 | 2007-10-10 | 이피엔피(주) | Apparatus of sediment filter |
KR100851616B1 (en) * | 2008-04-07 | 2008-08-12 | 김웅기 | Water purifier informing change time of filter |
KR102343749B1 (en) | 2021-04-28 | 2021-12-28 | 주식회사 에콘 | Water treatment system including multiple filter units |
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KR20160120613A (en) | 2015-04-08 | 2016-10-18 | 주식회사 모아나눔 | water purifier directiy connected to faucet |
KR101700932B1 (en) | 2015-05-08 | 2017-02-01 | 주식회사 금산 | water purifier directiy connected to faucet |
KR102452491B1 (en) | 2021-06-17 | 2022-10-11 | 주식회사 제일아쿠아 | Water faucet for kithen |
KR102364228B1 (en) | 2021-07-16 | 2022-02-17 | 주식회사 에스와이코리아 | Water faucet direct connection type water purification apparatus |
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Publication number | Priority date | Publication date | Assignee | Title |
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KR100765827B1 (en) * | 2006-08-01 | 2007-10-10 | 이피엔피(주) | Apparatus of sediment filter |
KR100851616B1 (en) * | 2008-04-07 | 2008-08-12 | 김웅기 | Water purifier informing change time of filter |
KR102343749B1 (en) | 2021-04-28 | 2021-12-28 | 주식회사 에콘 | Water treatment system including multiple filter units |
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