KR950005419B1 - Water clarifier and comtrol circuit - Google Patents
Water clarifier and comtrol circuit Download PDFInfo
- Publication number
- KR950005419B1 KR950005419B1 KR1019920018357A KR920018357A KR950005419B1 KR 950005419 B1 KR950005419 B1 KR 950005419B1 KR 1019920018357 A KR1019920018357 A KR 1019920018357A KR 920018357 A KR920018357 A KR 920018357A KR 950005419 B1 KR950005419 B1 KR 950005419B1
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- South Korea
- Prior art keywords
- water
- filter
- unit
- drinking water
- microcomputer
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 99
- 235000020188 drinking water Nutrition 0.000 claims abstract description 34
- 239000003651 drinking water Substances 0.000 claims abstract description 34
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 27
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims abstract description 23
- 230000001954 sterilising effect Effects 0.000 claims abstract description 13
- 229910052500 inorganic mineral Inorganic materials 0.000 claims abstract description 7
- 229910052742 iron Inorganic materials 0.000 claims abstract description 7
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 claims abstract description 7
- 239000011707 mineral Substances 0.000 claims abstract description 7
- 239000003599 detergent Substances 0.000 claims abstract description 6
- 238000001914 filtration Methods 0.000 claims abstract description 3
- 239000007787 solid Substances 0.000 claims abstract 2
- 239000008213 purified water Substances 0.000 claims description 19
- 238000000746 purification Methods 0.000 claims description 18
- 239000012528 membrane Substances 0.000 claims description 12
- 238000001223 reverse osmosis Methods 0.000 claims description 12
- 239000013618 particulate matter Substances 0.000 claims description 11
- 238000004659 sterilization and disinfection Methods 0.000 claims description 11
- 239000012510 hollow fiber Substances 0.000 claims description 10
- 238000001179 sorption measurement Methods 0.000 claims description 10
- 239000000126 substance Substances 0.000 claims description 8
- 241000894006 Bacteria Species 0.000 claims description 6
- 238000011001 backwashing Methods 0.000 claims description 5
- 238000000605 extraction Methods 0.000 claims description 5
- 239000008151 electrolyte solution Substances 0.000 claims description 4
- 239000004576 sand Substances 0.000 claims description 4
- 235000019645 odor Nutrition 0.000 claims description 3
- 238000010828 elution Methods 0.000 claims description 2
- 238000000034 method Methods 0.000 claims description 2
- 229910052754 neon Inorganic materials 0.000 claims description 2
- GKAOGPIIYCISHV-UHFFFAOYSA-N neon atom Chemical compound [Ne] GKAOGPIIYCISHV-UHFFFAOYSA-N 0.000 claims description 2
- 239000002245 particle Substances 0.000 abstract 2
- 229910052799 carbon Inorganic materials 0.000 abstract 1
- 239000011368 organic material Substances 0.000 abstract 1
- 238000007781 pre-processing Methods 0.000 abstract 1
- 238000010586 diagram Methods 0.000 description 6
- 230000002070 germicidal effect Effects 0.000 description 4
- 238000005406 washing Methods 0.000 description 3
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 2
- 239000000460 chlorine Substances 0.000 description 2
- 229910052801 chlorine Inorganic materials 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 239000010419 fine particle Substances 0.000 description 2
- 150000002500 ions Chemical class 0.000 description 2
- OKTJSMMVPCPJKN-OUBTZVSYSA-N Carbon-13 Chemical class [13C] OKTJSMMVPCPJKN-OUBTZVSYSA-N 0.000 description 1
- 230000001276 controlling effect Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000839 emulsion Substances 0.000 description 1
- 230000005284 excitation Effects 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 239000004745 nonwoven fabric Substances 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 239000008400 supply water Substances 0.000 description 1
- 239000008399 tap water Substances 0.000 description 1
- 235000020679 tap water Nutrition 0.000 description 1
- 238000003809 water extraction Methods 0.000 description 1
Classifications
-
- 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
- C02F1/30—Treatment of water, waste water, or sewage by irradiation
- C02F1/32—Treatment of water, waste water, or sewage by irradiation with ultraviolet light
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B67—OPENING, CLOSING OR CLEANING BOTTLES, JARS OR SIMILAR CONTAINERS; LIQUID HANDLING
- B67D—DISPENSING, DELIVERING OR TRANSFERRING LIQUIDS, NOT OTHERWISE PROVIDED FOR
- B67D1/00—Apparatus or devices for dispensing beverages on draught
- B67D1/07—Cleaning beverage-dispensing apparatus
-
- 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
- C02F1/441—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by reverse osmosis
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B67—OPENING, CLOSING OR CLEANING BOTTLES, JARS OR SIMILAR CONTAINERS; LIQUID HANDLING
- B67D—DISPENSING, DELIVERING OR TRANSFERRING LIQUIDS, NOT OTHERWISE PROVIDED FOR
- B67D1/00—Apparatus or devices for dispensing beverages on draught
- B67D1/07—Cleaning beverage-dispensing apparatus
- B67D2001/075—Sanitising or sterilising the apparatus
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/005—Processes using a programmable logic controller [PLC]
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/10—Solids, e.g. total solids [TS], total suspended solids [TSS] or volatile solids [VS]
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/14—Maintenance of water treatment installations
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/16—Regeneration of sorbents, filters
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Toxicology (AREA)
- Water Treatment By Sorption (AREA)
- Physical Water Treatments (AREA)
Abstract
Description
제1도 종래 음용수 정수장치의 구성도.1 is a block diagram of a conventional drinking water purification device.
제2도 본 발명 음용수 정수장치의 구성도.2 is a block diagram of the drinking water purification device of the present invention.
제3도 본 발명 음용수 정수시의 제어회로도.3 is a control circuit diagram for drinking water purification of the present invention.
제4도 제2도에 있어서, 각부의 설명도.4 and 2, explanatory diagrams of respective parts.
제5도 제3도에 있어서, 각부의 입력에 대한 마이크로컴퓨터의 내부 구성도.5 is a diagram illustrating an internal configuration of a microcomputer for input of each part.
* 도면의 주요부분에 대한 부호의 설명* Explanation of symbols for main parts of the drawings
22 : 전처리필터부 24 : 활성탄흡착필터부22: pretreatment filter unit 24: activated carbon adsorption filter unit
27 : 역삼투압멤브레인필터부 30 : 미네랄용출용 필터부27: reverse osmosis membrane filter portion 30: mineral elution filter portion
31 : 자외선살균조 41 : 마이크로컴퓨터31: UV sterilization tank 41: microcomputer
42 : 부하구동부 44 : 플로우스위치부42: load driving unit 44: flow switch unit
45 : 표시부 46 : 필터수명설정부45: display section 46: filter life setting section
47 : 정수기능선택부 V1: 급수밸브47: water purification function selection unit V 1 : water supply valve
V2,V3: 역세척밸브 V4: 바이패스밸브V 2 , V 3 : Backwash valve V 4 : Bypass valve
RY1: 릴레이RY 1 : Relay
본 발명은 음용수에 포함되어 있는 입자성물질(철녹, 탈질, 잔류염소, 유기물, 중금속, 세균 등)을 제거하기 위한 정수장치에 관한 것으로, 특히 음용수 사용시만 자외선 살균 가능하도록 하고 필터의 수명 및 정수상태를 외부에 표시하여 소비자에게 상태를 알려주는 음용수 정수장치 및 그 제어회로에 관한 것이다.The present invention relates to a water purification device for removing particulate matter (iron rust, denitrification, residual chlorine, organic matter, heavy metals, bacteria, etc.) contained in drinking water, and in particular, UV sterilization is possible only when drinking water is used. The present invention relates to a drinking water purifier and a control circuit for indicating a status to an external user and informing a status to a consumer.
종래 음용수 정수장치 구성은 제1도에 도시된 바와같이, 감압변(1)을 통해 급수된 물의 양을 조절하여 점적조(3)로 공급하는 유량조절밸브(2)와, 상기 점적조(3)로부터 받은 물중의 입자성 물질 및 냄새를 유발하는 각종 성분을 제거하기 위한 여과사, 활성탄 및 소메라이트가 충전된 메인필터(7)와, 이 메인필터(7)를 통한 물중의 아주 미세한 입자성 물질 및 각종 세균을 제거하기 위한 중공사(8)가 몰딩 결속되어 있는 중공사필터(9)와, 이 중공사필터(9)를 통해 정수된 물을 보관하는 정수조(10)와, 이 정수조(10)에서 넘치는 물이 배수관(11)에 일정량이 되었을 때 조절하여 배수토록 하는 배수밸브(12)로 구성되고, 미설명 부호 13은 에어(air)밸브이다.Conventional drinking water purification device configuration, as shown in Figure 1, the flow control valve (2) for supplying to the dropping tank (3) by adjusting the amount of water supplied through the pressure reducing valve (1), the dropping tank (3) The main filter (7) filled with filtered sand, activated carbon, and someite for removing particulate matter and odor-causing components in the water received from the water), and very fine particulate matter in the water through the main filter (7). A hollow fiber filter 9 in which the hollow fiber 8 for removing substances and various bacteria is molded, a water purification tank 10 for storing purified water through the hollow fiber filter 9, and this purified water It consists of a drain valve 12 which adjusts and drains when the water overflowed in the tank 10 reaches a certain amount to the drain pipe 11, and reference numeral 13 is an air valve.
이와 같이 구성된 종래의 정수장치에 있어서, 수도로부터 급소된 물은 감압변(1) 및 유량조절밸브(2)를 통해 물의 양이 조절되어 점적조(3)에 공급되는데, 이 점적조(3)에 공급된 물은 수압으로 인해 메인필터(7)에 공급되면 여과사(4)에 의해 물중의 철녹 등 큰 입자성 물질이 제거되고, 활성탄(5) 및 소메라이트(6)를 통해 냄새를 유발하는 각종 성분 및 유기물, 세제 등이 제거되어 다시 중공사필터(9)에 공급된다.In the conventional water purification device configured as described above, the water supplied from the tap water is supplied to the drop tank 3 by adjusting the amount of water through the pressure reducing valve 1 and the flow regulating valve 2, which is the drop tank 3. When the water supplied to the main filter 7 is supplied due to water pressure, large particulate matter such as iron rust in the water is removed by the filter sand 4, and the odor is caused through the activated carbon 5 and the sommite 6. Various components, organic substances, detergents, and the like are removed and supplied to the hollow fiber filter 9 again.
그러면 중공사필터(9)내에 중공사(8)에 의해 미세한 입자성물질 및 각종 세균을 제거한다. 이와 같이 메인필터(7) 및 중공사필터(9)를 통해 정수된 물이 정수조(10)에 공급되면 사용자는 취출콕을 통해서 정수된 물을 취출할 수 있다.Then, fine particles and various bacteria are removed by the hollow fiber 8 in the hollow fiber filter 9. As such, when the purified water is supplied to the purified water tank 10 through the main filter 7 and the hollow fiber filter 9, the user may extract the purified water through the blower cock.
그리고 정수된 물이 정수조(10)에 공급되다가 넘치게 되면 그 물은 배수관(11)에 저장되다 일정량이 초과되면 배수밸브(12)에 의해 외부로 배수된다.When the purified water is supplied to the purified water tank 10 and overflowed, the water is stored in the drain pipe 11, and when a predetermined amount is exceeded, the water is drained out by the drain valve 12.
그러나, 상기와 같이 동작하는 종래 정수장치에 있어서, 정수시 유속상태에 따라 필터의 수명이 달라지므로 필터의 교환시기를 일치시킬 수 없으며, 물의 정수상태를 알 수 없어서 소비자가 안심하고 물을 마실 수 없는 등의 문제점이 있었다.However, in the conventional water purifier that operates as described above, the life of the filter varies depending on the flow rate of the purified water, so that the replacement time of the filter cannot be matched, and the consumer can drink water with confidence because the purified water of the water cannot be known. There was no such problem.
따라서 종래의 문제점을 해결하기 위하여 본 발명은 지역별 수질상태에 따라 필터수명시간을 다르게 설정할 수 있게하여 필터의 사용시간을 적산한 후 잔여필터 수명을 외부에 표시하고, 정수상태를 전해질용액센서(TDS)로 정수상태를 파악한 후 그 정수상태를 외부에 표시하며, 음용수 취출시에 연동가능한 스위치로서 응용수를 자외선 살균하도록 하여 사용자에게 안정성 및 신뢰감을 제공하는 음용수 정수장치를 창안한 것으로, 이하 첨부한 도면을 참조하여 상세히 설명하면 다음과 같다.Therefore, in order to solve the conventional problems, the present invention enables the filter life time to be set differently according to the water quality conditions of each region, after which the remaining filter life is displayed externally after integrating the use time of the filter, and the purified state is the electrolyte solution sensor (TDS). After identifying the purified water condition, the purified water status is displayed on the outside, and it is a switch that can be interlocked when discharging drinking water to create a drinking water purifier that provides stability and reliability to users by UV sterilization of applied water. When described in detail with reference to the drawings as follows.
제2도는 본 발명 음용수 정수장치의 구성도로서 이에 도시한 바와 같이, 급수밸브(V1)를 통해 급수된 물중의 철녹 등 큰 입자성 물질을 제거하기 위한 여과사 사리층 및 부직포열 성형층(21)으로 충전된 전처리필터부(22)와, 물중의 냄새를 유발하는 각종 성분 및 유기물, 세제 등을 흡착제거하기 위한 활성탄(23)이 충전된 활성탄흡착필터부(24)와, 아주 미세한 입자성 물질 및 각종 세균을 제거하기 위한 중공사(26)가 몰딩 결속되어 있는 역삼투압멤브레인필터부(27)와, 상기 역삼투압멤브레인필터부(27)를 통과시켜 정수된 물을 압력저장탱크(28)에 저장하도록 가압하는 수중가압펌프(25)와, 상기 역삼투압멤브레인필터부(27)의 배수관에 부착되어 정수상태를 파악할 수 있도록 한 전해질용액센서(TDS)(29)와, 상기 압력저장탱크(28)로부터 정수된 물에 미네랄 성분이 함유되도록 미네랄 성분을 용출하는 미네랄용출용 필터부(30)와, 이 필터부(30)를 통한 물에 대해 자외선 살균을 하는 자외선살균조(31)와, 취출콕(33)에 의한 음용수 취출시 온.오프하여 음용수를 배수토록한 플로우(FLOW) 스위치(32)와, 역세척시 활성탄흡착필터부(24) 및 전처리필터부(22)를 통해 세척되어 이물질이 포함된 물을 배출하도록 한 역세척밸브(V2),(V3)로 구성하였다.2 is a block diagram of the drinking water purifying apparatus of the present invention, as shown therein, a filter yarn layer and a nonwoven fabric forming layer for removing large particulate matter such as iron rust in the water supplied through the water supply valve V 1 ( 21, the activated carbon adsorption filter unit 24 filled with the pretreatment filter unit 22 filled with activated carbon 23 for adsorption and removal of various components, organic substances, detergents, etc., which cause odors in water, and very fine particles. Pressure storage tank (28) for passing purified water through the reverse osmosis membrane filter unit (27), to which the hollow fiber (26) is molded to remove the substance and various bacteria, and the reverse osmosis membrane filter unit (27). And an electrolyte solution sensor (TDS) (29) attached to a drain pipe of the reverse osmosis membrane filter unit (27) to pressurize the water to be stored in the tank and the pressure storage tank. Mineral water in water purified from 28 Extraction of the drinking water by the mineral dissolution filter unit 30 for eluting the mineral component, the ultraviolet sterilization tank 31 for ultraviolet sterilization of water through the filter unit 30, and the extraction cock 33. When the water is turned on and off, the drinking water is flushed out through the flow switch 32 and the activated carbon adsorption filter unit 24 and the pretreatment filter unit 22 during backwashing to discharge water containing foreign substances. It consists of backwash valves (V 2 ) and (V 3 ).
여기서 미설명 부호 V4는 바이패스밸브이고, 34는 압력스위치이다.Here, reference numeral V 4 is a bypass valve, 34 is a pressure switch.
그리고 본 발명 음용수 정수시의 제어회로는 제3도에 도시한 바와 같이, 전체 시스템을 제어하는 마이크로컴퓨터(4)와, 이 마이크로컴퓨터(41)의 제어출력에 따라 부하를 구동하는 부하구동부(42)와, 전해질용액센서에 의해 정수상태를 감지하는 TDS센서부(43)와, 물의 흐름상태를 체크하는 플로우스위치부(44)와, 상기 마이크로컴퓨터(41)의 제어신호에 따라 램프(L1-L10)를 구동시켜 역세척, 정수상태 및 필터잔여수명 등을 표시하는 표시부(45)와, 가변저항(VR1)을 이용하여 수질상태에 따라 필터수명의 초기값을 설정하는 필터수명설정부(46)와, 상기 마이크로컴퓨터(41)의 제어신호에 따라 정수를 하도록 하는 정수기능선택부(47)로 구성되고, 마아크로컴퓨터는 제5도에 도시된 바와 같이 외부로부터 신호를 입력받는 신호입력부(41-1)와, 이 신호입력부(41-1)의 신호입력에 따라 연산처리를 행하는 씨피유(41-2)와 각종 데이타를 내장하는 이이피롬(41-3)으로 구성하였다.As shown in FIG. 3, the control circuit for drinking water purification of the present invention includes a microcomputer 4 for controlling the entire system and a load driver 42 for driving a load in accordance with the control output of the microcomputer 41. ), The TDS sensor unit 43 for detecting the purified state by the electrolyte solution sensor, the flow switch unit 44 for checking the flow of water, and the lamp L 1 according to the control signal of the microcomputer 41. -L 10 ) is driven to display the backwash, the purified water condition and the filter remaining life, and the display unit 45, and the filter life setting to set the initial value of the filter life according to the water quality using the variable resistor (VR 1 ) And a water purifying function selection unit 47 for performing water purification according to the control signal of the microcomputer 41. The microcomputer receives a signal from the outside as shown in FIG. A signal input section 41-1, and this signal input section 41-1. It was constructed in the ssipiyu (41-2) and this pirom (41-3) to embed data for performing various operation processing in accordance with the input signal.
미설명 부호 ⓐ와 ⓑ는 AC상용전원을 나타낸다.Unexplained symbols ⓐ and ⓑ represent AC commercial power.
이와 같이 구성된 본 발명의 작용 및 효과를 상세히 설명하면 다음과 같다.Referring to the operation and effect of the present invention configured as described above in detail.
먼저 음용수 저장기능에 대해 살펴보면, 마이크로퓨터(41)에서 출력포트(P1),(P5)를 통해 부하구동부(42)로 로우신호를 인가하면 이는 인버터부(41)를 통해 반전된 하이신호가 트리이악(T1),(T5)이 게이트로 인가되어 온되므로 급수밸브(V1)와 트랜스(TRANS1)에 의해 수증가압펌프(25)가 온된다.First, referring to the drinking water storage function, when a low signal is applied from the microcomputer 41 to the load driver 42 through the output ports P 1 and P 5 , the high signal inverted through the inverter unit 41 is applied. Since the triacs T 1 and T 5 are applied to the gate, the water pressure booster pump 25 is turned on by the water supply valve V 1 and the transformer 1 .
그러면 급수밸브(V1)를 통해 유입된 물은 전처리필터부(22)의 여과사(11)층을 통과하면서 철녹등 큰 입자성 물질이 제거되고, 활성탄흡착필터부(24)의 내부로 유입, 상향하면서 물속에 함유된 염소, 유기물, 세제 등의 성분이 활성탄(13)중에서 물리흡착이 이루어져 정수된 물이 역삼투압멤브레인펄터부(27)로 유입된다. 이 유입된 물속에 아주 미세한 입자성 물질 및 각종 세균 등이 중공사(26)층을 통과하면서 제거되어 정수 제균된 물이 압력저장탱크(28)에 저장된다. 상기 압력저장탱크(28)의 압력스위치(34)에 의해 일정전압을 감지하였을 때 마이크로컴퓨터(41)에 출력포트(P1),(P5)를 통해 하이신호를 출력시켜 급수밸브(V1)와 수증가압펌프(25)의 구동을 중지시킨다.Then, the water introduced through the water supply valve V 1 passes through the filter sand 11 layer of the pretreatment filter unit 22 to remove large particulate matter such as iron rust and flows into the activated carbon adsorption filter unit 24. In addition, chlorine, organic substances, detergents, and the like contained in the water are physically adsorbed in the activated carbon 13, and purified water is introduced into the reverse osmosis membrane filter unit 27. Very fine particulate matter, various bacteria, and the like are removed in the flowed water through the hollow fiber 26 layer, and the purified water sterilized water is stored in the pressure storage tank 28. When a certain voltage is detected by the pressure switch 34 of the pressure storage tank 28, a high signal is output to the microcomputer 41 through the output ports P 1 and P 5 to supply a water supply valve V 1. ) And the water pressure booster pump 25 are stopped.
상기에서 압력저장탱크(28)로 정수 제균된 물이 유입될 때 TDS센서(29)에 의해 감지된 전압(V+)과 스위치어레이(56)에 의해 설정된 값(V+)이 연산증폭기(OP1)로 입려된다.When the purified water is introduced into the pressure storage tank 28, the voltage V + sensed by the TDS sensor 29 and the value V + set by the switch array 56 are calculated by the operational amplifier OP. 1 )
이 연산증폭기(OP1)에서 비교연산된 값을 마이크로컴퓨터(41)로 출력하면 제5도에 도시한 마이크로컴퓨터(41)내 씨피유(41-2)에서 이이피램(41-3)에 저장된 값과 비교하여 물의 정수상태를 체크한다.When the value calculated by the operation amplifier OP 1 is output to the microcomputer 41, the value stored in the EPI ram 41-3 in the CPI 41-2 in the microcomputer 41 shown in FIG. Check the water purification status in comparison with.
그런 다음 마이크로컴퓨터(41)는 표시부(45)인 인버터부(52),(53)로 하이 또는 로우신호를 출려시키는데 물의 정수상태가 양호할 때는 L9를 온시키고, 불량일 때는 L10을 온시킨다. 여기서 스위치어레이(56)는 설정 값을 정할 때 미세조정이 가능하다.The microcomputer 41 then emits a high or low signal to the inverters 52, 53, which are the display portion 45. When the water purification condition is good, L 9 is turned on, and when it is bad, L 10 is turned on. Let's do it. Here, the switch array 56 can be fine-tuned when setting the set value.
TDS센서(29)는 제4도의 (c)에 도시한 바와 같이 물에 포함된 이온성분을 전도도에 의하여 검출하는 것으로, 유로관(29-1)을 통해 흐르는 물을 TDS센서전극(29-2)으로 감지하는데 이온성분이 많으면 전도도가 상승하고 센서저항이 줄어들어 제3도에서 감지전압(V+)이 설정전압(V-)보다 크므로(V+>V-)연산증폭기(OP1)를 통해 하이전압이 마이크로컴퓨터(41)로 출력된다. 또한 이온성분이 적으면 전도도가 하강하고 센서저항이 커져서 서정전압(V-)이 감지전압(V+) 보다 커서 연산증폭기(OP1)를 통한 로우전압이 상기 마이크로컴퓨터(41)로 출력된다.The TDS sensor 29 detects ions contained in the water by conductivity as shown in FIG. 4C, and the TDS sensor electrode 29-2 detects the water flowing through the flow path tube 29-1. ) as to sense large, the ion components conductivity rises and the sensor resistance is a third degree detected voltage (V + from) the set voltage (V reduced-greater than) (V +> V -) of the operational amplifier (OP 1) Through this, a high voltage is output to the microcomputer 41. In addition, when the ionic component is small, the conductivity decreases and the sensor resistance becomes large, so that the lyric voltage V − is greater than the sensing voltage V + so that the low voltage through the operational amplifier OP 1 is output to the microcomputer 41.
이상에서 물의 정수상태가 양호하다는 가정하에 사용자가 입력저장탱크(28)에 저장된 음용수를 취출콕(33)을 통해 취출하여 압력저장탱크(28)의 유량이 일정량이하로 저하되면 재차 급수밸브(V1)와 수중가압펌프(25)를 구동시켜 압력저장탱크(28)에 항상 일정량 이상의 유량을 보유하도록 한다.Under the assumption that the purified water of the water is good, the user withdraws the drinking water stored in the input storage tank 28 through the extraction cock 33, and when the flow rate of the pressure storage tank 28 falls below a certain amount, the water supply valve V again. 1 ) and the underwater pressure pump 25 is driven to always maintain a certain amount or more of the flow rate in the pressure storage tank (28).
상기에서 취출콕(33)에 의한 음용수 취출시 플로우스위치(Flow Switch)(32)는 제4도(a)에 도시한 바와 같이 입력부(32-1) 수압에 의해 볼(ball)베어링(32-3)이 위로 올라가므로 발광다이오드(L11)에서 발광된 빛을 포트랜지스터(TR1)에서 수광하므로 포토트랜지스터(TR1)가 도통된다. 따라서 플로우스위치부(44)에서 마이크로컴퓨터(41)의 입력포트(P11)로 로우신호가 입력되므로(제3도) 상기 마이크로컴퓨터(41)는 음용수 취출상태를 인식하고 출력포트(P6)를 통해 하이신호를 출려시켜 릴레이(RY1)의 여자코일을 여자시켜 초크코일(LC)에 전압을 인가한다.The flow switch 32 when the drinking water is taken out by the extraction cock 33 is a ball bearing 32- by the pressure of the input part 32-1 as shown in FIG. Since 3) rises upward, light emitted from the light emitting diode L 11 receives light from the phototransistor TR 1 , so that the phototransistor TR 1 is turned on. Therefore, since the low signal is input from the flow switch unit 44 to the input port P 11 of the microcomputer 41 (FIG. 3), the microcomputer 41 recognizes the drinking water extraction state and outputs the output port P 6 . By applying a high signal through the excitation coil of the relay (RY 1 ) to apply a voltage to the choke coil (LC).
따라서 자외선 살균램프(LP2) 양단에 고전압이 유기되어 자외선살균램프(LP2)가 점등하게 된다. 즉 음용수 취출시 음용수를 살균하는 것이다. 이와 동시에 네온램프(LP3)에 전압이 인가되므로 자외선살균램프(LP2)와 동시에 구동하게 되어 자외선살균램프(LP2)가 구동중임을 알려 음용수를 음용할 수 있음을 표시한다.Therefore, a high voltage across the UV germicidal lamp (LP 2) is an organic light is an ultraviolet germicidal lamp (LP 2). That is, sterilization of drinking water when drinking water is taken out. In the same time, because the voltage applied to the neon lamp (LP 3) is driven at the same time as the UV germicidal lamp (LP 2) indicates that the UV germicidal lamp (LP 2) can be potable drinking water offer a drive is in progress.
이상에서와 같이 음용수를 정수하여 저장탱크에 저장하고 그 저장된 음용수를 마실 경우 살균하여 배수토록 하는데 이와 같이 동작이 반복되어 소정시간이 경과하면 마이크로컴퓨터(41)는 출력포트(P2),(P3)로 로우신호를 출려시켜 역세척밸브(V2),(V3)를 구동시킨다.As described above, the drinking water is purified and stored in the storage tank, and the stored drinking water is sterilized and drained when the drink is stored. As described above, when the predetermined time elapses, the microcomputer 41 outputs the output port (P 2 ), (P 3 ) Drives the low signal to drive the backwash valves (V 2 ) and (V 3 ).
따라서 역세척밸브(V3)가 온되어 급수가 이루어져 유입된 물은 활성탄 흡착필터부(24)와 전처리필터부(22)내에 충전된 활성탄(23) 및 여과시(21)층에 잔존해 있는 유기물, 세제나 철녹, 탁질, 진흑 등의 입자성 물질이 떨어지면서 물속에 섞여 역세척밸브(V2)를 지나서 외부로 토출된다. 이 역세척은 제2도에서 실선으로된 화살표 방향과 같고, 또한 표시부(45)에서 L1에 불이 들어오면 역세척 중임을 표시하는 것이다.Therefore, the backwash valve V 3 is turned on to supply water, and the water introduced therein remains in the activated carbon 23 filled in the activated carbon adsorption filter unit 24 and the pretreatment filter unit 22 and in the filtration layer 21. Organic substances, detergents, iron rust, turbidity, dark black and other particulate matter are dropped into the water and discharged through the backwash valve (V 2 ) to the outside. The back washing is the same as the direction of the arrow with a solid line in FIG. 2, which will also show the cleaning when being lit, the reverse L 1 in the display section 45. The
통상 역세척시는 정수 제균시보다 유속이 빠르기 때문에 입자성 물질이 거의 다 떨어진다.In general, the backwashing process has a higher flow rate than the clean water sterilization, so almost all of the particulate matter falls.
그리고 초기전원공급시는 필터층의 오염가능성 있는 물을 배수하기 위하여 역삼투압멤브레인필터부(27)를 세척한 후 역세척밸브(V2),(V3)를 구동시킨다. 상기에서 역삼투압멤브레인필터부(27)의 세척은 역세척밸브(V2)와 바이패스밸브(V4)를 구동시켜 전처리필터부(22)와 역삼투압멤브레인필터부(27)에 유입된 오염가능성이 있는 물을 배수시킨다.When the initial power supply, the reverse osmosis membrane filter unit 27 is washed to drain the contaminated water of the filter layer, and then the back washing valves V 2 and V 3 are driven. In the above, the reverse osmosis membrane filter unit 27 is cleaned by driving the reverse washing valve V 2 and the bypass valve V 4 to contaminate the pretreatment filter unit 22 and the reverse osmosis membrane filter unit 27. Drain any likely water.
필터교환시기가 되어 필터를 바꾼 다음 초기 세척을 해야 하는데 이에 대해 살펴보면, 마이크로컴퓨터(41)가 출력포트(P10)를 통해 로우신호를 정수기능선택부(48)로 입력하면 정수기능이 중단된다. 이후 일정시간 동안 역세척밸브(V2),(V3)를 구동시켜 전처리 필터부(22)의 유제성분을 세척한 후 역세척밸브(V3)만을 오프시키고 바이패스밸브(V4)를 구동시켜 활성탄흡착필터부(24) 및 역삼투압멤브레인필터부(27)를 세척하고, 이 세척은 제2도에서 점선으로 표시된 화살표방향과 같다.When it is time to replace the filter, it is necessary to change the filter and perform initial cleaning. Looking at this, when the microcomputer 41 inputs the low signal to the water purification function selection unit 48 through the output port P 10 , the water purification function is stopped. . After driving the backwash valve (V 2 ), (V 3 ) for a certain time to wash the emulsion component of the pretreatment filter unit 22, only the backwash valve (V 3 ) is turned off and the bypass valve (V 4 ) In operation, the activated carbon adsorption filter unit 24 and the reverse osmosis membrane filter unit 27 are washed, and this washing is the same as the direction indicated by the dotted line in FIG.
급수밸브(V2),(V3)의 구동시간은 제5도에 도시한 마이크로컴퓨터(41)내 씨피유(41-2)에서 적산한 다음 필터수명설정부(46)의 가변저항(VR1)에 의하여 설정된 필터수명초기값 시간과 비교하여 각 설정시간의 잔여시간 비율만큼 표시부(45)의 램프를 구동시켜 필터수명의 잔여시간 비율은 외부에 알린다.The driving time of the water supply valves V 2 and V 3 is integrated in the CPI 41-2 in the microcomputer 41 shown in FIG. 5, and then the variable resistance VR 1 of the filter life setting unit 46 is obtained. By driving the lamp of the display unit 45 by the remaining time ratio of each set time compared to the filter life initial value time set by), the remaining time ratio of the filter life is informed to the outside.
필터수명설정부(46)에서 가변저항(VR1)값에 따라 마이크로컴퓨터(41)에 인가되는 전압이 달라지므로 그 전압크기에 따라 몇 단계 나누어 필터수명의 초기설정값을 설정하는데, 초기설정은 수질 상태에 따라 달리한다.Since the voltage applied to the microcomputer 41 in the filter life setting unit 46 varies according to the value of the variable resistor VR 1 , the initial setting value of the filter life is set by dividing the voltage by several steps. It depends on the water quality.
이상에서 상세히 설명한 바와 같이 본 발명은 지역별 수질상태에 따라 필터의 수명을 다르게 설정함과 아울러 사용시간을 적산하여 필터수명의 잔여시간을 외부에 표시하고, 정수상태를 TDS센서로 파악하여 외부에 표시하며, 음용수 사용시에만 자외선 살균을 가능하도록하고, 필터세척이 자동적으로 이루어질 수 있도록 하여 소비자에게 정수기에 대한 신뢰감과 만족감을 줄 수 있도록 한 효과가 있다.As described in detail above, the present invention sets the life of the filter differently according to the water quality conditions of each region, displays the remaining time of the filter life by integrating the use time, and displays the purified state by the TDS sensor. In addition, ultraviolet sterilization is possible only when drinking water is used, and filter washing is automatically performed, thereby providing consumers with confidence and satisfaction with the water purifier.
Claims (5)
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KR1019920018357A KR950005419B1 (en) | 1992-10-07 | 1992-10-07 | Water clarifier and comtrol circuit |
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KR1019920018357A KR950005419B1 (en) | 1992-10-07 | 1992-10-07 | Water clarifier and comtrol circuit |
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KR940009071A KR940009071A (en) | 1994-05-16 |
KR950005419B1 true KR950005419B1 (en) | 1995-05-24 |
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KR100883035B1 (en) * | 2007-09-10 | 2009-02-09 | 한국건설기술연구원 | Monitoring device of taste and odor matters(2-mib) in drinking water treatment and method thereof |
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KR100329401B1 (en) * | 1999-04-14 | 2002-03-20 | 김형일 | display device of pure & ultra purification system and display method of the same |
KR20020076881A (en) * | 2001-03-31 | 2002-10-11 | 제이에이비에이코리아(주) | Movement condition displaying method for Reverse-Osmosis and Ultra-Pure manufacturing system and movement condition displaying device thereof |
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KR100883035B1 (en) * | 2007-09-10 | 2009-02-09 | 한국건설기술연구원 | Monitoring device of taste and odor matters(2-mib) in drinking water treatment and method thereof |
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