KR20040024777A - Water purified system for wastewater saving - Google Patents
Water purified system for wastewater saving Download PDFInfo
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- KR20040024777A KR20040024777A KR1020020056220A KR20020056220A KR20040024777A KR 20040024777 A KR20040024777 A KR 20040024777A KR 1020020056220 A KR1020020056220 A KR 1020020056220A KR 20020056220 A KR20020056220 A KR 20020056220A KR 20040024777 A KR20040024777 A KR 20040024777A
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- wastewater
- water
- filter
- membrane filter
- raw water
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 116
- 239000002351 wastewater Substances 0.000 title claims abstract description 55
- 239000012528 membrane Substances 0.000 claims abstract description 53
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 26
- 239000008213 purified water Substances 0.000 claims abstract description 25
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 23
- 239000013049 sediment Substances 0.000 claims abstract description 11
- 238000000746 purification Methods 0.000 claims description 25
- 230000001105 regulatory effect Effects 0.000 claims description 10
- 238000003780 insertion Methods 0.000 claims description 5
- 230000037431 insertion Effects 0.000 claims description 5
- 238000004891 communication Methods 0.000 claims description 2
- 238000001223 reverse osmosis Methods 0.000 description 5
- 239000000126 substance Substances 0.000 description 5
- 241000894006 Bacteria Species 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 230000003204 osmotic effect Effects 0.000 description 4
- 230000002028 premature Effects 0.000 description 4
- 239000008399 tap water Substances 0.000 description 3
- 235000020679 tap water Nutrition 0.000 description 3
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 2
- 229910052785 arsenic Inorganic materials 0.000 description 2
- RQNWIZPPADIBDY-UHFFFAOYSA-N arsenic atom Chemical compound [As] RQNWIZPPADIBDY-UHFFFAOYSA-N 0.000 description 2
- 231100000357 carcinogen Toxicity 0.000 description 2
- 239000003183 carcinogenic agent Substances 0.000 description 2
- 239000000460 chlorine Substances 0.000 description 2
- 229910052801 chlorine Inorganic materials 0.000 description 2
- 229910001385 heavy metal Inorganic materials 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000012857 radioactive material Substances 0.000 description 2
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- 241000532784 Thelia <leafhopper> Species 0.000 description 1
- 241000700605 Viruses Species 0.000 description 1
- 230000003542 behavioural effect Effects 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 239000011888 foil Substances 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 239000002917 insecticide Substances 0.000 description 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 238000011403 purification operation Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 238000004904 shortening Methods 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 239000000271 synthetic detergent Substances 0.000 description 1
Classifications
-
- 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
- B01D35/14—Safety devices specially adapted for filtration; Devices for indicating clogging
- B01D35/157—Flow control valves: Damping or calibrated passages
- B01D35/1573—Flow control valves
-
- 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
- B01D35/14—Safety devices specially adapted for filtration; Devices for indicating clogging
- B01D35/147—Bypass or safety valves
- B01D35/1475—Pressure relief valves or pressure control valves
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D39/00—Filtering material for liquid or gaseous fluids
- B01D39/14—Other self-supporting filtering material ; Other filtering material
- B01D39/20—Other self-supporting filtering material ; Other filtering material of inorganic material, e.g. asbestos paper, metallic filtering material of non-woven wires
- B01D39/2055—Carbonaceous material
- B01D39/2058—Carbonaceous material the material being particulate
- B01D39/2062—Bonded, e.g. activated carbon blocks
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D65/00—Accessories or auxiliary operations, in general, for separation processes or apparatus using semi-permeable membranes
- B01D65/02—Membrane cleaning or sterilisation ; Membrane regeneration
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D65/00—Accessories or auxiliary operations, in general, for separation processes or apparatus using semi-permeable membranes
- B01D65/08—Prevention of membrane fouling or of concentration polarisation
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F16—ENGINEERING ELEMENTS AND UNITS; GENERAL MEASURES FOR PRODUCING AND MAINTAINING EFFECTIVE FUNCTIONING OF MACHINES OR INSTALLATIONS; THERMAL INSULATION IN GENERAL
- F16K—VALVES; TAPS; COCKS; ACTUATING-FLOATS; DEVICES FOR VENTING OR AERATING
- F16K15/00—Check valves
- F16K15/02—Check valves with guided rigid valve members
- F16K15/04—Check valves with guided rigid valve members shaped as balls
- F16K15/044—Check valves with guided rigid valve members shaped as balls spring-loaded
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F16—ENGINEERING ELEMENTS AND UNITS; GENERAL MEASURES FOR PRODUCING AND MAINTAINING EFFECTIVE FUNCTIONING OF MACHINES OR INSTALLATIONS; THERMAL INSULATION IN GENERAL
- F16K—VALVES; TAPS; COCKS; ACTUATING-FLOATS; DEVICES FOR VENTING OR AERATING
- F16K27/00—Construction of housing; Use of materials therefor
- F16K27/02—Construction of housing; Use of materials therefor of lift valves
- F16K27/0209—Check valves or pivoted valves
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Materials Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Description
본 발명은 폐수절감형 정수시스템에 관한 것으로, 더욱 상세하게는 폐수조절밸브와 자동압력조절장치를 구비한 정수시스템에 있어서 폐수조절솔밸브를 이용해 정수시 폐수량을 1/10으로 줄이고 나머지를 부스터 펌프로 재순환시키고, 정수가완료되면 자동압력조절장치에 의해 멤브레인필터 표면의 막힘의 원인이 되는 물질을 분리하여 운전이 시작됨과 동시에 폐수조절솔밸브에 의해 표면의 막힘 물질을 제거함으로서 정수를 실시하는 폐수절감형 정수시스템에 관한 것이다.The present invention relates to a wastewater reduction type water purification system, and more particularly, in a water purification system equipped with a wastewater control valve and an automatic pressure control device, the wastewater volume during water purification is reduced to 1/10 using a wastewater control brush valve, and the rest is a booster pump. Waste water to purify the water by removing the material that is causing the blockage of the membrane filter by automatic pressure regulating device. It relates to a saving water purification system.
이러한 종래의 기술로서 등록실용신안등록번호 실013788호 "정수기"가 기재되어 있다. 도 1은 상기 등록실용신안의 일반적인 정수기의 구성을 도시한 개략도로서 수도꼭지(10)에 연결된 연결호스(11)를 통해 나온 원수는 굵은 찌거기나 부유물질을 걸러주는 세디멘트필터(12)를 통과하는 한편, 그 후 프리카본필터(13)로 유입을 제거하는 콘트롤장치(18)에 의해 작동하는 차단밸브(17)를 거치게 되고, 상기 차단밸브(17)를 통해 나온 물은 물 속의 염소성분을 제거하여 주는 프리카본필터(13)를 거치게 되며, 펌프(19)에 의해 강제적으로 압송된 물은 멤브레인필터(15)에서 기존의 0.0001㎛의 미세한 구멍을 통하여 일반세균 및 각종 불순물을 걸러내는 한편 냄새나 유해한 가스성분 등을 완전히 제거하여 주는 포스트카본필터(16)를 거쳐 정수탱크(20)에 저장된 물이 일정 상한 수위까지 차 오르게 되면 이를 감지하는 리미트스위치(21)가 차단밸브(17)로써 물의 유입을 막도록 콘트롤장치(18)에 신호를 인가하도록 구성되어 있다.As such a conventional technology, the registration utility model registration number No. 013788 "water purifier" is described. Figure 1 is a schematic diagram showing the configuration of a general water purifier of the utility model, the raw water coming out through the connection hose 11 connected to the faucet 10 is passed through the sediment filter 12 for filtering coarse residue or suspended matter On the other hand, thereafter through the shut-off valve 17 which is operated by the control device 18 to remove the inflow to the pre-carbon filter 13, the water coming out through the shut-off valve 17 to remove the chlorine component in the water After passing through the pre-carbon filter 13, the water forcibly pushed by the pump 19 filters the general bacteria and various impurities through the existing micro holes of 0.0001 ㎛ in the membrane filter 15, When the water stored in the purified water tank 20 rises to a certain upper limit level through a post carbon filter 16 which completely removes harmful gas components, the limit switch 21 for detecting this is used as a shutoff valve 17. It is configured to apply a signal to the control device 18 to prevent the inflow of water.
통상 역삼투압 정수기의 멤브레인필터(15)를 통과하는 정수량과 멤브레인필터(15)를 통과하지 못하여 폐수로 분류되는 폐수량은 약 1:3의 비율로 정수가 이루어지므로 이러한 일차 정수된 폐수가 아무런 소용없이 버려지는 실정이다.Usually, the amount of purified water that passes through the membrane filter 15 of the reverse osmosis water purifier and the wastewater that is not passed through the membrane filter 15 are classified into wastewater at a ratio of about 1: 3, so that the primary purified wastewater is of no use. Abandoned.
한편, UN의 워싱톤 소재 국제 인구행동연구소(PAI)의 발표에 따르면 한국의활용 가능한 물 자원량은 661억 톤으로서 이를 국민 1인당 활용 가능량으로 환산할 경우, 한국은 1950년 3,247톤에서 1995년에는 1,472톤으로 줄어들어 물 부족 국가로 분류되고 있는 현실이다.Meanwhile, according to the UN's Washington-based Institute of International Population and Behavioral Research (PAI), Korea's available water resource is 66.1 billion tons, which translates into 3,247 tons per capita in 1950 and 1,472 in 1995. It is reduced to tons and is classified as a water shortage country.
현재 사용되고 있는 역삼투압 정수기는 RO 멤브레인 필터의 막힘에 의한 정수수 수질 향상 및 정수량 감소를 막기 위해 일정량의 폐수를 배출하고 있다. 이 폐수의 양이 정수량의 3배 이상이 되므로 정수량 1리터를 얻기 위해 폐수량 3리터를 버리는 문제점이 있어 왔다.Reverse osmosis water purifiers are currently being used to discharge a certain amount of wastewater in order to prevent the improvement of purified water quality and decrease the amount of purified water by clogging the RO membrane filter. Since the amount of this wastewater is three times or more of the amount of purified water, there has been a problem of discarding the amount of wastewater 3 liters to obtain 1 liter of purified water.
통상적으로 역삼투압 방식의 정수기는 삼투압현상 즉 농도가 묽은 쪽의 액체가 삼투막을 통하여 농도가 진한 쪽으로 이동되는 자연현상으로부터 착안하여 상기 농도가 진한 쪽에 인위적인 압력을 가하여 고농도의 용액 속의 용매인 물이 삼투막을 통과하여 저농도쪽으로 이동토록 하는 인위적인 작용을 이용하여 정수를 이루는 것으로서, 제2도에는 역삼투압 방식의 정수기가 도시되어 있는데, 이는 수도전(1)으로부터 원수를 공급받아 5미크론 정도의 미세한 필터를 통해 먼지, 찌꺼기, 각종 부유 물질이 제거되는 세디먼트필터(12)와, 활성판의 흡착방식을 이용하여 발암물질(THM), 합성세제, 살충제등 인체에 유해한 화학물질과 염소 성분둥을 제거하는 프리카본필터(13), 0.0001미크론의 역삼투막으로 이루어져 납, 비소와 같은 중금속은 물론 나트륨, 박테리아 바이어스, 방사성 물질등을 걸러주며 일부는 드레인관(32)을 통해 수도전(1)측으로 회류시키는 멤브레인 필터(15), 불쾌한 맛과 냄새, 색소 등을 제거하는 포스트카본필터(16)로 이루어지며 상기세디먼트필터(12)와 프리카본필터(13)사이의 유로에는 솔레노이드밸브(14) 및 펌프(19)가 설치되어 소정의 압력을 가하며 원수를 공급할 수 있도록 되어 있고, 미설명부호 42는 미네랄투입수단이고, 44는 살균수단이다.In general, the reverse osmosis type water purifier focuses on the osmotic phenomenon, ie, a natural phenomenon in which a liquid having a thinner concentration moves to a higher concentration through an osmotic membrane. In order to achieve the purified water by using an artificial action to move through the membrane toward the lower concentration, a reverse osmosis water purifier is shown in FIG. 2, which receives raw water from the tap water (1) and filters the microfilter about 5 microns. The sediment filter 12 removes dust, debris and various suspended substances through the adsorption method of the active plate, and removes harmful substances such as carcinogens (THM), synthetic detergents, insecticides, and chlorine components. Free carbon filter (13), consisting of 0.0001 micron reverse osmosis membrane, heavy metals such as lead, arsenic, sodium, foil Filters the lia bias, radioactive material and the like, and part of the membrane filter 15 to flow back to the water field 1 through the drain pipe 32, and the post carbon filter 16 to remove unpleasant taste and smell, pigments, etc. The solenoid valve 14 and the pump 19 are installed in the flow path between the sediment filter 12 and the free carbon filter 13 to supply the raw water while applying a predetermined pressure. Mineral input means, 44 is a sterilization means.
그러나 이와 같은 방식은 상기 정수 단계 중 가장 미세한 구멍을 갖는 멤브레인필터(15)의 청소기능이 구비되어 있지 않아 멤브레인필터(15)에 필터링된 물질(박테리아, 바이러스, 방사성물질, 납, 비소 등)이 누적되어 정수효율이 떨어질 뿐만 아니라 특히 위생상태를 저하시킬 우려를 갖고 있었다. 또한 경도성 물질을 다량 함유하고 있는 물을 정수하는데 있어 멤브레인필터(15)의 작동능력에 한계가 있고 경도성 물질이 멤브레인필터(15)의 막에 스케일을 발생시켜 조기 막힘을 유발한다. 그리고 이러한 경도가 높은 물은 정수기의 수명과 부품의 수명을 단축시키는 문제점이 있어 왔다.However, this method is not equipped with a cleaning function of the membrane filter 15 having the finest hole in the water purification step, so that the filtered material (bacteria, viruses, radioactive materials, lead, arsenic, etc.) in the membrane filter 15 Accumulated to reduce the efficiency of water purification, in particular, there was a fear of lowering the hygiene. In addition, there is a limit to the operation ability of the membrane filter 15 in purifying water containing a large amount of the hardness material, and the hardness material generates scale on the membrane of the membrane filter 15 to cause premature clogging. And such high hardness water has a problem of shortening the life of the water purifier and the life of the parts.
본 발명은 상기와 같은 문제점을 해결하기 위해 안출된 것으로,The present invention has been made to solve the above problems,
본 발명의 제1목적은 멤브레인필터에서 버려지는 생활용수를 재사용하는 폐수절감형 정수시스템을 제공하는 것이고,It is a first object of the present invention to provide a wastewater reduction type purification system for reusing living water discarded in a membrane filter.
본 발명의 제2목적은 멤브레인필터의 조기막힘을 방지하고 안정적인 수질의 정수수를 공급할 수 있는 시스템을 제공하는데 있다.It is a second object of the present invention to provide a system capable of preventing premature clogging of a membrane filter and supplying purified water of stable water quality.
도 1, 2는 종전 정수시스템을 개략적으로 도시한 도면이고,1 and 2 is a view schematically showing a conventional water purification system,
도 3a는 본 발명에 따른 폐수절감형 정수시스템의 동작을 설명하기 위한 시스템 블록도이고,Figure 3a is a system block diagram for explaining the operation of the wastewater reduction type purification system according to the present invention,
도 3b는 본 발명에 따른 폐수절감형 정수시스템의 동작을 설명하기 위한 정수흐름도이고,Figure 3b is a flow chart for explaining the operation of the wastewater reduction type purification system according to the present invention,
도 4는 본 발명에 따른 자동압력조절장치의 단면도이다.4 is a cross-sectional view of the automatic pressure control device according to the present invention.
<도면의 주요부호에 대한 설명><Description of Major Symbols in Drawing>
1: 수도전 10: 수도꼭지1: faucet 10: faucet
11: 연결호스 12: 세디먼트필터11: connection hose 12: sediment filter
13: 프리카본필터 14: 솔레노이드밸브13: precarbon filter 14: solenoid valve
15: 멤브레인필터 16: 포스트카본필터15: membrane filter 16: post carbon filter
17: 차단밸브 18: 콘트롤장치17: shut-off valve 18: control device
19: 펌프 20: 정수탱크19: pump 20: water purification tank
21: 리미트스위치 32: 드레인관21: limit switch 32: drain pipe
100: 원수 110: 세디메트 필터100: enemies 110: sedimet filters
120: 부스터 펌프 121: 원수공급단1120: booster pump 121: raw water supply stage 1
122: 폐수공급단 123: 토출관122: wastewater supply stage 123: discharge pipe
130: 프리카본필터 140, 170: 자동압력조절장치130: free carbon filter 140, 170: automatic pressure regulating device
141: 하우징 141a: 시트141: housing 141a: sheet
141b: 단턱 142: 원수유입구141b: step 142: raw water inlet
143: 대기압유입구 144: 원수유출구143: atmospheric pressure inlet 144: raw water outlet
145: 스프링 밸브 145a: 볼145: spring valve 145a: ball
145b: 삽지구 145c: 스프링145b: Insertion Strip 145c: Spring
150: 멤브레인필터 151: 원수공급단2150: membrane filter 151: raw water supply stage 2
152: 폐수토출관 153: 분지관152: wastewater discharge pipe 153: branch pipe
160: 포스트카본필터 180: 정수탱크160: post carbon filter 180: water purification tank
190: 폐수조절솔밸브 191: 드레인관190: wastewater control brush valve 191: drain pipe
본 발명은 세디멘트필터, 프리카본필터, 멤브레인필터, 포스트카본필터, 정수탱크로 이루어진 정수시스템에 폐수조절솔밸브와 자동압력조절장치가 장착되어 이루어진다.The present invention consists of a sewage filter, a free carbon filter, a membrane filter, a post carbon filter, and a water purification system consisting of a wastewater control brush valve and an automatic pressure regulating device.
본 발명을 첨부된 도면에 의하여 상세히 설명하면 다음과 같다.The present invention will be described in detail with reference to the accompanying drawings.
도 3a는 본 발명에 따른 폐수절감형 정수시스템의 동작을 설명하기 위한 시스템 블록도이고, 도 3b는 본 발명에 따른 폐수절감형 정수시스템의 동작을 설명하기 위한 정수흐름도로서, 본 발명에 따른 폐수절감형 정수시스템은 수도전(미도시)으로부터 원수를 공급받아 세디멘트필터(110), 프리카본필터(130), 멤브레인필터(150), 포스트카본필터(160)를 순차적으로 거쳐 정수된 물을 정수탱크(180)에 저장하는 정수시스템에 있어, 상기 멤브레인필터(150) 하단의 폐수토출관(152)에서 유출되는 폐수는 분지관(153)에서 폐수공급단(122)과 폐수조절솔밸브(190)와 연결되고, 상기 멤브레인필터(150) 유입단과 상기 프리카본필터(130) 유출단에는 자동압력조절장치(140)가 설치되어 이루어진다.Figure 3a is a system block diagram for explaining the operation of the wastewater reduction water purification system according to the present invention, Figure 3b is a water flow diagram for explaining the operation of the wastewater reduction water purification system according to the present invention, wastewater according to the present invention The reduced water purification system receives raw water from a tap water (not shown) and sequentially passes water through the sediment filter 110, the free carbon filter 130, the membrane filter 150, and the post carbon filter 160. In the water purification system to be stored in the water purification tank 180, the wastewater flowing out of the wastewater discharge pipe 152 at the bottom of the membrane filter 150 is the wastewater supply stage 122 and the wastewater control brush valve in the branch pipe 153 ( 190 is connected to the membrane filter 150 inlet end and the pre-carbon filter 130 outlet end is made of an automatic pressure control device 140 is installed.
수도전(미도시)의 원수(100)가 세디멘트필터(110) 일측 공급단에 공급되도록 연결되어 있으며, 상기 세디멘트필터(110) 타측은 통과한 원수를 부스터펌프(120)일측에 있는 원수공급단1(121)에 공급되도록 연결되어 있으며, 또한 상기 부스터펌프(120) 일측은 재순환되는 폐수를 공급받을 수 있도록 상기 원수공급단1(121) 측면에 폐수공급단(122)이 연결되고 타측은 토출관(123)을 통하여 프리카본필터(130) 일측단에 공급되도록 연결된다. 상기 폐수공급단(122) 하단은 분지관(153)에 연결되어 있다.The raw water 100 of the tap water (not shown) is connected to be supplied to one end of the sediment filter 110, and the other side of the sediment filter 110 feeds the raw water that has passed through the booster pump 120. It is connected to be supplied to the supply stage 1 (121), and also one side of the booster pump 120 is connected to the waste water supply stage 122 to the raw water supply stage 1 (121) side to receive the recycled waste water and the other The side is connected to be supplied to one end of the precarbon filter 130 through the discharge pipe 123. The lower end of the wastewater supply stage 122 is connected to the branch pipe (153).
상기 프리카본필터(130)의 타측단은 자동압력조절장치(140)와 연결되어 멤브레인필터(150)의 일측단과 연통되고, 상기 멤브레인필터(150) 타단은 분지관(153)에 연결된 폐수토출관(152)과 원수공급단2(151)에 연결되어 있다.The other end of the precarbon filter 130 is connected to the automatic pressure regulating device 140 to communicate with one end of the membrane filter 150, the other end of the membrane filter 150 is connected to the branch pipe 153 wastewater discharge pipe 152 and the raw water supply stage 2 (151).
상기 멤브레인필터(150)를 통과한 원수는 원수공급단2(151)를 통하여 포스트카본필터(160)를 거친 원수는 자동압력조절장치(170)를 거쳐 정수탱크(180)에 연결되어 있다.Raw water passed through the membrane filter 150 is passed through the post carbon filter 160 through the raw water supply stage 2 (151) is connected to the purified water tank 180 through the automatic pressure control device (170).
상기 분지관(153)에서 폐수는 폐수공급단(122)과 드레인관(191)으로 분배되고, 드레인관(191)에는 폐수조절솔밸브(190)가 설치된다.In the branch pipe 153, the wastewater is distributed to the wastewater supply stage 122 and the drain pipe 191, and the wastewater control brush valve 190 is installed in the drain pipe 191.
도 4는 자동압력조절장치의 단면도로서, 상기 자동압력조절장치(140)(170)는 원수유입구(142)와 시트(141a) 및 단턱(141b)이 형성된 대기압유입구(143), 원수유출구(144)가 일체로 형성된 하우징(141), 상기 대기압유입구(143)와원수유출구(144)에 스프링 밸브(145)가 삽입된다.4 is a cross-sectional view of the automatic pressure control device, the automatic pressure control device 140, 170 is a raw water inlet 142, the atmospheric pressure inlet 143, the seat 141a and step 141b is formed, the raw water outlet 144 The spring valve 145 is inserted into the housing 141, the atmospheric pressure inlet 143 and the raw water outlet 144 are formed integrally.
상기 스프링 밸브(145)는 삽지구(145b)가 장착된 볼(145a)과 일단은 상기 삽지구(145b) 외주연에 장착되고 타단은 단턱(141b)에 고정되는 스프링(145c)을 포함한다.The spring valve 145 includes a ball 145a on which the insertion hole 145b is mounted, and one end of which is mounted on an outer circumference of the insertion hole 145b and the other end of which is fixed to the step 141b.
첨부된 도면에 의거하여 본 발명의 작용, 효과를 설명하면 다음과 같다.Referring to the operation and effects of the present invention based on the accompanying drawings as follows.
원수(100)가 세디멘트필터(110)를 통과하면서 원수 속에 포함된 큰 입자의 부유물질 및 녹 찌거기를 제거하고, 상기 세디멘트필터(110)를 통과한 원수는 부스터펌프(120)를 통해 가압된 후 자동압력조절장치(140)를 통과하면서 멤브레인필터(150)에 공급된다. 상기 자동압력조절장치(140)는 원수유입구(142)를 통과한 수압에 의해 시트(141a)에서 볼이(145a) 떨어지고, 원수유출구(144)를 통해 배출되는 원수를 프리카본필터(130)를 통과시키고, 상기 프리카본필터(130)를 통과한 원수를 압력 손실없이 멤브레인필터(150)에 공급한다. 정수작용이 끝나면 개방되었던 스프링 밸브(145)가 스프링(145c)의 탄성력에 의해 볼(145a)이 시트(141a)를 막게 되고, 대기압유입구(143)를 통과하여 외부공기가 유입되어 원수유출구(144)로 원수가 흐르지 못하므로 상기 멤브레인필터(150) 내부에는 수압이 걸리지 않아 멤브레인필터(150) 내부에 잔존해 있던 고농축 생활용수를 배출시켜 멤브레인필터(150)의 조기 막힘을 방지한다.As the raw water 100 passes through the sediment filter 110, the floating particles and rust residues of the large particles contained in the raw water are removed, and the raw water passing through the sediment filter 110 is pressurized through the booster pump 120. After passing through the automatic pressure control device 140 is supplied to the membrane filter 150. The automatic pressure control device 140 is a ball 145a from the seat 141a by the water pressure passed through the raw water inlet 142, the raw water discharged through the raw water outlet 144 to the pre-carbon filter 130 The raw water passed through the precarbon filter 130 is supplied to the membrane filter 150 without pressure loss. When the water purification operation is completed, the spring valve 145, which was opened, blocks the seat 141a by the elastic force of the spring 145c, and the outside air flows through the atmospheric pressure inlet 143 to feed the raw water outlet 144. Since the raw water does not flow into the membrane filter 150, the water pressure is not applied to the membrane filter 150, thereby discharging the highly concentrated living water remaining in the membrane filter 150 to prevent premature clogging of the membrane filter 150.
상기 멤브레인필터(150)는 기존의 0.0001㎛의 미세한 구멍을 통하여 일반세균 및 각종 불순물을 걸러내는 한편 원수에 포함된 각종 중금속이나 발암물질, 박테리아 등의 세균을 제거하여 정수된 물들을 포스트카본필터(160)에 공급하도록 연결되어 있다.The membrane filter 150 filters the general bacteria and various impurities through the existing micropore of 0.0001 μm, and removes various heavy metals, carcinogens, bacteria, etc. contained in the raw water and removes purified water from the post carbon filter ( 160 to supply.
상기 포스트카본필터(160)는 정수된 물의 냄새를 제거하고 미생물의 번식을 차단하여 자동압력조절장치(170)를 통과한다. 상기 자동압력조절장치(170)는 정수된 물을 상기 정수탱크(180)에 공급하고, 상기 정수탱크(180)로부터 정수물의 역류를 차단하며 정수시스템의 운전 정지시 외부공기 유입으로 포스트카본필터(160)에 잔존해 있던 정수된 물을 상기 멤브레인필터(150)로 역류시킨다. 이 경우 삼투압현상으로 인해 멤브레인필터(150) 표면으로 정수된 물을 방출하여 멤브레인필터(150) 표면에 쌓인 멤브레인필터(150) 막힘현상을 일으키는 물질들을 멤브레인필터(150) 표면과 분리시킨다. 상기 멤브레인필터(150)를 통과하지 못한 폐수들은 폐수토출관(152)을 통해 분지관(153)에서 일부는 폐수공급관(122)을 통과하여 부스터펌프(120)에 공급되어 프리카본필터(130) 및 멤브레인필터(150)를 거쳐 필터링되고, 일부는 드레인관(191)과 연통되어 있는 폐수조절솔밸브(190)를 통해 배출된다.The post carbon filter 160 removes the smell of purified water and blocks the growth of microorganisms and passes through the automatic pressure regulating device 170. The automatic pressure regulating device 170 supplies purified water to the purified water tank 180, blocks the reverse flow of purified water from the purified water tank 180, and post-carbon filters into the inflow of external air when the purified water system is stopped. The purified water remaining in 160 is returned to the membrane filter 150. In this case, the purified water is discharged to the surface of the membrane filter 150 due to the osmotic pressure to separate substances causing the clogging of the membrane filter 150 accumulated on the surface of the membrane filter 150 from the surface of the membrane filter 150. Wastewater that has not passed through the membrane filter 150 is partially supplied from the basin pipe 153 through the wastewater supply pipe 122 through the wastewater discharge pipe 152 and supplied to the booster pump 120 to supply the free carbon filter 130. And is filtered through the membrane filter 150, a part is discharged through the waste water control brush valve 190 in communication with the drain pipe 191.
폐수절감형 정수시스템에서 정수가 멈추면 폐수조절솔밸브(190)가 열리게 되고, 자동압력조절장치(140)에 의해 상기 멤브레인필터(150)에 남아 있던 농축폐수가 배출된다. 또한 자동압력조절장치(170)에 의해 포스트카본필터(160)에 남아있던 정수된 물이 멤브레인필터(150)로 공급된다. 이 경우 삼투압현상으로 인해 정수된 물이 상기 멤브레인필터(150) 표면으로 흘러 상기 멤브레인필터(150) 표면의 이물질들을 분리시킨 후, 정수 시작 전 10초 동안 순간 후레싱으로 이물질들을 배출하여 멤브레인필터(150)를 세척한다.When the purified water stops in the wastewater reduction type purification system, the wastewater control brush valve 190 is opened, and the concentrated wastewater remaining in the membrane filter 150 is discharged by the automatic pressure regulating device 140. In addition, purified water remaining in the post carbon filter 160 is supplied to the membrane filter 150 by the automatic pressure regulating device 170. In this case, water purified by osmotic pressure flows to the surface of the membrane filter 150 to separate foreign substances on the surface of the membrane filter 150, and then discharges foreign substances by flash flashing for 10 seconds before the start of water purification. )).
본 발명은 상기와 같은 구성을 취함으로서The present invention takes the configuration as described above
멤브레인 필터에서 버려지는 생활용수를 폐수조절솔밸브를 이용해 재사용하여, 종래의 정수시스템에서 평균 정수량의 3배 이상의 폐수가 버려지던 것을 재순환시스템을 사용함으로써, 수도수 사용량을 3배 이상 감소시킬 수 있으며 안정된 정수수의 수질을 유지 할 수 있다.The water used in the membrane filter can be reused by using the wastewater control brush valve, and by using the recirculation system, the wastewater of three times or more of the average purified water was discarded in the conventional water purification system. Maintain stable water quality.
또한 자동압력조절장치를 사용함으로서 멤브레인 필터의 조기막힘을 방지하고 원수TDS의 지속적인 상승을 억제시킬 수 있다.The use of an automatic pressure regulator also prevents premature clogging of the membrane filter and suppresses the continuous rise of raw water TDS.
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Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2006126791A1 (en) * | 2005-05-26 | 2006-11-30 | Chang-Woo Park | Water purifying system equipped with supply means for mixed water |
KR101331842B1 (en) * | 2011-11-08 | 2013-11-22 | 정휘동 | Sterilizing method for water tank of water purifier and sterilizing water purifier applied thereof |
CN110182984A (en) * | 2019-07-02 | 2019-08-30 | 中建水务(深圳)有限公司 | Water purification system |
CN110182983A (en) * | 2019-07-02 | 2019-08-30 | 中建水务(深圳)有限公司 | Water purification system |
CN110182868A (en) * | 2019-07-02 | 2019-08-30 | 中建水务(深圳)有限公司 | Water purification system |
CN110182867A (en) * | 2019-07-02 | 2019-08-30 | 中建水务(深圳)有限公司 | Water purification system |
CN110182985A (en) * | 2019-07-02 | 2019-08-30 | 中建水务(深圳)有限公司 | Water purification system |
KR102326306B1 (en) * | 2020-12-24 | 2021-11-17 | 주식회사 진성하이테크 | Waste water treatment system for edging machine |
-
2002
- 2002-09-16 KR KR1020020056220A patent/KR20040024777A/en not_active Application Discontinuation
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2006126791A1 (en) * | 2005-05-26 | 2006-11-30 | Chang-Woo Park | Water purifying system equipped with supply means for mixed water |
KR101331842B1 (en) * | 2011-11-08 | 2013-11-22 | 정휘동 | Sterilizing method for water tank of water purifier and sterilizing water purifier applied thereof |
CN110182984A (en) * | 2019-07-02 | 2019-08-30 | 中建水务(深圳)有限公司 | Water purification system |
CN110182983A (en) * | 2019-07-02 | 2019-08-30 | 中建水务(深圳)有限公司 | Water purification system |
CN110182868A (en) * | 2019-07-02 | 2019-08-30 | 中建水务(深圳)有限公司 | Water purification system |
CN110182867A (en) * | 2019-07-02 | 2019-08-30 | 中建水务(深圳)有限公司 | Water purification system |
CN110182985A (en) * | 2019-07-02 | 2019-08-30 | 中建水务(深圳)有限公司 | Water purification system |
KR102326306B1 (en) * | 2020-12-24 | 2021-11-17 | 주식회사 진성하이테크 | Waste water treatment system for edging machine |
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