KR200369031Y1 - Hot and cool ionization and purification system - Google Patents
Hot and cool ionization and purification system Download PDFInfo
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- KR200369031Y1 KR200369031Y1 KR20-2004-0015001U KR20040015001U KR200369031Y1 KR 200369031 Y1 KR200369031 Y1 KR 200369031Y1 KR 20040015001 U KR20040015001 U KR 20040015001U KR 200369031 Y1 KR200369031 Y1 KR 200369031Y1
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- 238000000746 purification Methods 0.000 title 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 192
- 230000002378 acidificating effect Effects 0.000 claims abstract description 37
- 239000008213 purified water Substances 0.000 claims abstract description 16
- 239000002131 composite material Substances 0.000 claims abstract description 14
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 7
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 7
- 239000000919 ceramic Substances 0.000 claims description 4
- 238000000034 method Methods 0.000 claims 5
- 230000000694 effects Effects 0.000 abstract description 5
- 238000002203 pretreatment Methods 0.000 abstract description 2
- 150000002500 ions Chemical class 0.000 description 17
- 238000010411 cooking Methods 0.000 description 7
- 241000048246 Gallicrex cinerea Species 0.000 description 6
- 238000012805 post-processing Methods 0.000 description 4
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 3
- 229910010293 ceramic material Inorganic materials 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000005868 electrolysis reaction Methods 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- 235000019738 Limestone Nutrition 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- 230000035622 drinking Effects 0.000 description 1
- 239000010433 feldspar Substances 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 239000006028 limestone Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 229910044991 metal oxide Inorganic materials 0.000 description 1
- 150000004706 metal oxides Chemical class 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- -1 shells Chemical class 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 239000004575 stone Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000008400 supply water Substances 0.000 description 1
- 239000000454 talc Substances 0.000 description 1
- 229910052623 talc Inorganic materials 0.000 description 1
- 239000008399 tap water Substances 0.000 description 1
- 235000020679 tap water Nutrition 0.000 description 1
Classifications
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- 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
- B01D35/06—Filters making use of electricity or magnetism
-
- 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
- C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
- C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
- C02F1/46104—Devices therefor; Their operating or servicing
- C02F1/4618—Devices therefor; Their operating or servicing for producing "ionised" acidic or basic water
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F5/00—Softening water; Preventing scale; Adding scale preventatives or scale removers to water, e.g. adding sequestering agents
-
- 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
- C02F2201/005—Valves
-
- 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
- C02F2209/06—Controlling or monitoring parameters in water treatment pH
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Water Supply & Treatment (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Water Treatment By Sorption (AREA)
Abstract
본 고안은 이온 냉온정수기에 관한 것으로, 그 구성은 유입된 원수를 전기분해하여 알칼리수와 산성수를 공급시키는 이온 정수기에 있어서, 원수을 전처리 필터, 제 1솔레노이드 밸브, 카본 필터에 차례로 통과시켜 정수하는 전처리 필터부와, 상기 전처리 필터부에서 정수된 정제수를 전기분해하여 알칼리수와 산성수로 이온화시키는 전해조와, 상기 전해조의 알칼리수와 산성수의 흐름를 제어하는 제 2솔레노이드 밸브와, 상기 제 2솔레노이드 밸브를 통과한 알칼리수와 산성수의 스케일을 제거하는 후처리 복합 필터부 및 상기 후처리 복합 필터부에서 정수된 알칼리수와 산성수를 냉수 저장하는 냉수통과 온수 저장하는 온수통이 구성된 저장부가 포함되어 구성된 것으로서, 스케일이 제거되어 맑고 깨끗한 정제수를 음용할 수 있고 냉ㆍ온수통의 열효율을 높일 수 있으며 이온수의 효과를 높이는 등의 효과가 있다.The present invention relates to an ion cold and hot water purifier, the configuration of which is an ion water purifier for supplying alkaline water and acidic water by electrolyzing the raw water introduced, the pre-treatment to pass the raw water through the pretreatment filter, the first solenoid valve, the carbon filter in order to purify A filter unit, an electrolytic cell for electrolyzing purified water purified by the pretreatment filter unit and ionizing it with alkaline water and acidic water, a second solenoid valve for controlling the flow of alkaline water and acidic water in the electrolytic cell, and the second solenoid valve A post-treatment composite filter unit for removing a scale of alkaline water and acidic water and a storage unit including a cold water tank for storing cold water and alkaline water for storing purified alkaline water and acidic water in the post-treatment composite filter unit, the scale including Removed, you can drink clear and clean purified water and heat the cold / hot water It can increase the efficiency and increase the effect of the ionized water.
Description
본 고안은 이온 냉온정수기에 관한 것으로, 더욱 상세하게는 원수로 유입된 수도물을 정수시킨 후에 전기 분해하여 알칼리수와 산성수로 이온화시켜 냉수, 온수 그리고 상온수로 구분하여 사용자의 급수 요구가 있을때 바로 공급할 수 있는 이온 냉온정수기에 관한 것이다.The present invention relates to an ion cold and hot water purifier, and more particularly, after the tap water introduced into the raw water is purified and electrolyzed and ionized into alkaline water and acidic water, and divided into cold water, hot water, and room temperature water, and can be supplied immediately when the user's water supply needs. The present invention relates to an ion cold / hot water purifier.
일반적으로 사회가 산업화, 공업화로 발전함에따라 산업 발전의 부산물에 발생되는 각종의 산업 쓰레기에의해 대지가 황폐화되고 수질과 대기가 오염되어 깨끗한 환경, 오염되지않은 자연 환경에서 살고자하는 욕구가 증가하고 , 특히 인간의 몸을 70%이상을 차지하는 깨끗한 물을 많이 찾게 되었다.In general, as society develops into industrialization and industrialization, various industrial wastes generated by by-products of industrial development are devastated, pollution of water quality and air is increased, and the desire to live in clean and uncontaminated natural environment increases. In particular, they found a lot of clean water, which occupies more than 70% of the human body.
그래서, 각 가정마다 정수기를 비치하여 정수물을 애용하게 되었는데, 최근에는 생활 수준이 높아지고 건강에 대한 관심이 증가함에따라 깨끗하면서도 몸에 좋은 물을 찾게되어 몸에 좋은 물을 공급할 수 있는 이온 정수기가 증가하는 추세이다.So, each household has a water purifier to use the purified water. Recently, as the standard of living and the health concern increase, the water purifier finds clean and healthy water and supplies water to the body. The trend is increasing.
그런데, 종래의 이온 냉온 정수기는 전기 분해로 분해된 알칼리수에서 스케일이 발생하여 냉수 탱크 및 온수 탱크가 오염이 되고, 냉수 탱크 재질이 금속 재질이라서 분해된 이온 성분이 금속과 결합하여 안정화 상태로 돌아가 이온 성분이 빠르게 소멸되어 이온수로서의 효과를 보지 못하였다.However, in the conventional ion cold / hot water purifier, scale occurs in alkaline water decomposed by electrolysis to contaminate the cold water tank and the hot water tank, and since the cold water tank is made of metal, the decomposed ionic component is combined with the metal to return to a stable state. The component disappeared rapidly and did not see the effect as ionized water.
또한, 이온수 처리 단계가 필터부 → 냉ㆍ온 탱크 → 전해조 순으로 배열되어 필터부를 통해 정수된 물은 냉ㆍ온수로 저장되었다가 사용자의 요구가 있을때마다 저장된 냉ㆍ온수를 이온화시켜 공급하게되는데 전해조가 냉수와 온수를 번갈아 수용하게되어 냉수의 이온수가 차지 않고, 온수의 이온수가 뜨겁지 않아 냉온수의 역활을 제대로 못하며, 또한 냉ㆍ온수 탱크에서 전해조에 물을 공급하기 위해서는 별도의 펌프가 더 요구되어 제조 원가를 상승시키는 문제점이 있었다.In addition, the ionized water treatment step is arranged in the order of the filter unit → cold / hot tank → electrolytic bath, the water purified through the filter unit is stored as cold and hot water, and ionized stored cold and hot water whenever the user requests. The cold water and hot water are alternately accommodated, the cold water is not occupied, the hot water is not hot, and the hot and cold water does not function properly.In addition, a separate pump is required to supply water from the cold and hot water tanks to the electrolytic cell. There was a problem of raising the cost.
본 고안은 상기한 바와 같은 종래의 문제점을 해소하고자 한 데 있는 것으로, 정제수를 알칼리수와 산성수로 이온화시키는 전해조에 후처리 필터부를 설치하여 이온수 생성 후 발생하는 스케일 문제를 제거하였고, 후처리 필터부에 냉수통과 온수통을 각각 설치함으로서 저장되는 이온수가 냉수, 온수가 분리되어 냉ㆍ온 이온수가 혼합되면서 열효율이 떨어지든 것을 차단하며, 이온수를 공급하기 위해 존재하던 펌프가 제거되어 제조 단가를 줄이고, 또한 냉수통을 세라믹 재질로 저장하여 이온수의 효능이 저하되는 것을 방지한 이온 냉온정수기을 제공하는데 있다.The present invention is to solve the conventional problems as described above, by installing a post-treatment filter unit in the electrolytic cell to ionize purified water with alkaline water and acidic water to eliminate the scale problem that occurs after the generation of ionized water, the post-treatment filter unit By installing a cold water tank and a hot water tank on each side, the stored cold water and hot water are separated and the cold and hot ion water are mixed to prevent the thermal efficiency from dropping, and the existing pump is removed to reduce the manufacturing cost. In addition, the cold water reservoir is stored in a ceramic material to provide an ion cold and hot water purifier that prevents the efficacy of the ionized water is lowered.
도 1는 본 고안에 따른 이온 냉온정수기의 흐름을 나타낸 구성도1 is a block diagram showing the flow of the ion cold and hot water purifier according to the present invention
<도면의 주요부분에 대한 부호의 설명><Description of the symbols for the main parts of the drawings>
10. 전처리 필터부 20. 전해조10. Pretreatment filter part 20. Electrolyzer
30. 제 2솔레노이드 밸브 40. 후처리 복합 필터부30. Second solenoid valve 40. Post treatment composite filter
50. 저장부 60. 퇴수 조절 밸브50. Reservoir 60. Drain control valve
70. 압력 센서 80. 제어부70. Pressure sensor 80. Control unit
90. 선택부90. Selection
상기와 같은 목적을 달성하기 위한 본 고안에 따른 이온 냉온정수기는 유입된 원수를 전기분해하여 알칼리수와 산성수를 공급시키는 이온 정수기에 있어서, 원수을 전처리 필터, 제 1솔레노이드 밸브, 카본 필터에 차례로 통과시켜 정수하는 전처리 필터부와, 상기 전처리 필터부에서 정수된 정제수를 전기분해하여 알칼리수와 산성수로 이온화시키는 전해조와, 상기 전해조의 알칼리수와 산성수의 흐름를 제어하는 제 2솔레노이드 밸브와, 상기 제 2솔레노이드 밸브를 통과한 알칼리수와 산성수의 스케일을 제거하는 후처리 복합 필터부 및 상기 후처리 복합 필터부에서 정수된 알칼리수와 산성수를 냉수 저장하는 냉수통과 온수 저장하는 온수통이 구성된 저장부가 포함되어 구성된 것을 특징으로 한다.The ion cold / hot water purifier according to the present invention for achieving the above object is an ion water purifier for supplying alkaline water and acidic water by electrolyzing the raw water introduced, and the raw water is passed through the pretreatment filter, the first solenoid valve, the carbon filter in order. A pretreatment filter unit for purifying water, an electrolytic cell for electrolyzing purified water purified by the pretreatment filter unit and ionizing it with alkaline water and acidic water, a second solenoid valve for controlling the flow of alkaline water and acidic water in the electrolytic cell, and the second solenoid A post-processing composite filter unit for removing the scale of alkaline and acidic water passing through the valve, and a storage unit including a cold water reservoir for storing cold water and alkaline water purified from the post-treatment composite filter unit and a hot water tank for storing hot water It is characterized by.
또한, 상기 전해조에 연결되는 퇴수 조절 밸브가 포함되어 구성된 것을 특징으로 한다.In addition, it characterized in that configured to include a discharge control valve connected to the electrolytic cell.
또한, 상기 전해조와 상기 제 2솔레노이드 밸브사이에 연결되는 압력 센서가 포함되어 구성된 것을 특징으로 한다.In addition, the pressure sensor is connected between the electrolytic cell and the second solenoid valve is characterized in that it is configured to include.
또한, 상기 정수를 흐름을 제어하는 제 1솔레노이드 밸브, 상기 알칼리수와 산성수의 이온 농도를 조절하는 전해조, 상기 알칼리수와 산성수의 흐름을 제어하는 제 2솔레노이드 밸브와 압력 센서에 각각 연결되어 흐름과 농도를 제어하는 제어부가 포함되어 구성된 것을 특징으로 한다.In addition, the first solenoid valve for controlling the flow of the purified water, an electrolytic cell for adjusting the ion concentration of the alkaline and acidic water, the second solenoid valve and the pressure sensor for controlling the flow of the alkaline and acidic water, respectively, A control unit for controlling the concentration is included.
또한, 상기 제어부에 연결되어 알칼리수, 산성수의 농도를 조절, 입력하는 선택부가 포함되어 구성된 것을 특징으로 한다.In addition, it is connected to the control unit is characterized in that it comprises a selection unit for adjusting, inputting the concentration of alkaline water, acidic water.
또한, 상기 냉수통이 세라믹으로 구성된 것을 특징으로 한다.In addition, the cold water container is characterized in that composed of a ceramic.
이하, 본 고안의 바람직한 실시예에 따른 이온 냉온정수기을 첨부된 도면에 의거하여 상세히 설명한다.Hereinafter, an ion cold / hot water purifier according to a preferred embodiment of the present invention will be described in detail with reference to the accompanying drawings.
도면 중 미설명 부호 1는 조리콕이고, 2은 냉수콕이며, 3는 온수콕이다.In the figure, reference numeral 1 is a cooking cock, 2 is a cold water cock, and 3 is a hot water cock.
도 1는 본 고안에 따른 이온 냉온정수기의 흐름을 나타낸 구성도를 나타낸 것이다.Figure 1 shows a block diagram showing the flow of the ion cold and hot water purifier according to the present invention.
상기 도 1에 도시된 바와 같이, 이온 냉온정수기는 전처리 필터부(10), 전해조(20), 제 2솔레노이드 밸브(30), 후처리 복합 필터부(40), 저장부(50), 퇴수 조절 밸브(60), 압력 센서(70), 제어부(80), 선택부(90)를 포함하고 있다.As shown in FIG. 1, the ion cold / hot water purifier has a pretreatment filter unit 10, an electrolytic cell 20, a second solenoid valve 30, a post-treatment composite filter unit 40, a storage unit 50, and discharge control. The valve 60, the pressure sensor 70, the control part 80, and the selection part 90 are included.
상기 전처리 필터부(10)는 유입한 원수를 정수하는데 다수 개의 필터로 구성되고 본 고안에서는 전처리 필터(11), 카본 필터(13)로 구성되며 전처리 필터(11)는 1차적으로 유입된 원수에서 모래, 녹찌꺼기 등의 입자가 큰 이 물질을 제거하고, 카본 필터(13)는 전처리 필터를 통과한 정제수에서 유해 화학 성분을 흡착하게 된다.The pretreatment filter unit 10 consists of a plurality of filters to purify the incoming raw water, and in the present invention, the pretreatment filter 11 and the carbon filter 13 are constructed. The large particles such as sand and debris are removed, and the carbon filter 13 adsorbs harmful chemical components in purified water passing through the pretreatment filter.
상기 전해조(20)는 전처리 필터부(10)에서 정수한 정제수를 제어부(80)에서 전달하는 신호에따라 전기 분해하여 알칼리수 혹은 산성수로 이온화시킨다.The electrolyzer 20 electrolyzes purified water purified by the pretreatment filter unit 10 according to a signal transmitted from the control unit 80 and ionizes the alkaline water or the alkaline water.
상기 제 2솔레노이드 밸브(30)는 전해조(20)에서 전기 분해된 알칼리수와 산성수가 다음 단계인 후처리 복합 필터부(40)로 흘러가는 것을 제어하게 된다.The second solenoid valve 30 controls the flow of the alkaline water and the acidic water electrolyzed in the electrolytic cell 20 to the post-processing composite filter unit 40, which is the next step.
상기 후처리 복합 필터부(40)는 상기 전해조(20)에서 전기 분해로 발생된 알칼리수와 산성수를 정수하게 되는데, 전해조(20)에서 발생한 스케일을 제거하고, 상기 전처리 필터부(10)에서 완전하게 정수하지 못한 정균 및 살균하며, 정제수의 맛과 냄새 등을 다시 거르게 된다.The post-treatment composite filter unit 40 purifies alkaline water and acidic water generated by electrolysis in the electrolytic cell 20, and removes scale generated in the electrolytic cell 20, and completely completes the pre-treatment filter unit 10. The bacteria and sterilization can not be purified, and the taste and smell of purified water are filtered again.
상기 저장부(50)는 냉수통(51)과 온수통(52)으로 구성되는데, 상기 후처리 복합 필터부(40)를 통과한 정제된 알칼리수와 산성수는 냉수통(51)과 온수통(52)에 각각 저장되어 냉수통(51)과 온수통(52)에 각각 연결된 냉수콕(2)과 온수콕(3)으로 배출된다.The storage unit 50 is composed of a cold water tank 51 and a hot water tank 52, the purified alkaline water and acidic water passed through the post-processing composite filter unit 40 is a cold water tank 51 and hot water tank ( Each of which is stored in 52 and discharged to the cold water cock 2 and the hot water cock 3 respectively connected to the cold water tank 51 and the hot water tank 52.
상기 퇴수 조절 밸브(60)는 상기 전해조(20)에 연결되는데 퇴수관과 연결되어 있어 전해조(20)에서 생성한 알칼리수와 산성수를 완전히 배출하여 새로운 알칼리수와 산성수를 채울 수 있다.The discharge control valve 60 is connected to the electrolytic cell 20, and is connected to the discharge pipe so as to completely discharge the alkaline and acidic water generated in the electrolytic cell 20 to fill new alkaline and acidic water.
상기 압력 센서(70)는 상기 전해조(20)와 상기 제 2솔레노이드 밸브(30)사이에 연결되는데, 조리콕(1)과 연결되어 상기 전해조(20)에서 생성된 알칼리수와 산성수를 조리용 혹은 다른 목적으로 사용하기 위해 조리콕(1)을 개방하면 알칼리수와 산성수의 흐르는 것을 제어하게 된다.The pressure sensor 70 is connected between the electrolytic cell 20 and the second solenoid valve 30, is connected to the cooking cock 1 for cooking or acidic water generated in the electrolytic cell 20 Opening the cooking cock 1 for other purposes will control the flow of alkaline and acidic water.
상기 제어부(80)은 제 1솔레노이드 밸브(12), 전해조(20), 제 2솔레노이드 밸브(30), 압력 센서(70)와 연결되는데, 제 1솔레노이드 밸브(12)와 연결되어 전처리 필터(11)를 통과하여 정제된 정제수가 카본 필터(13)로 흐르는 것을 제어하고, 전해조(20)에 연결되어 알칼리수, 산성수의 생성과 알칼리수와 산성수의 PH를 조절하며, 제 2솔레노이드 밸브(30)와 연결되어 전해조(20)에서 생성된 알칼리수와 산성수가 후처리 복합 필터부(40)로 흐르는 것을 제어하고, 그리고 압력 센서(70)와 연결되어 전해조(20)에서 생성된 알칼리수, 산성수가 조리 혹은 여러 목적으로 사용하기위해 흘러나가는 이온수를 제어하게 된다.The controller 80 is connected to the first solenoid valve 12, the electrolytic cell 20, the second solenoid valve 30, and the pressure sensor 70, and is connected to the first solenoid valve 12 to pretreatment filter 11. Control the purified purified water flowing through the carbon filter 13, and is connected to the electrolytic cell 20 to adjust the generation of alkaline water, acidic water and the pH of the alkaline water and acidic water, the second solenoid valve 30 Connected to and controls the alkaline water and acidic water generated in the electrolytic cell 20 to the post-treatment composite filter 40, and the alkaline water, acidic water generated in the electrolytic cell 20 is connected to the pressure sensor 70 to cook or It controls the flow of ionized water for various purposes.
상기 선택부(90)은 상기 제어부(80)와 연결되고 정수기의 전면에 형성되는데, PH를 조절할 수 있는 다양한 버튼이 있어 상기 버튼을 조작하여 전해조(20)의 PH를 조절할 수 있다.The selection unit 90 is connected to the control unit 80 and is formed on the front of the water purifier, and there are various buttons for adjusting the PH so that the PH of the electrolyzer 20 can be adjusted by operating the buttons.
그리고, 상기 저장부(50) 중에서 냉수통(51)은 재질이 세라믹으로 제작되는데, 상기 세라믹은 장석, 석회석, 도석, 규석, 활석과 같은 원료와 조개껍질, 탄산칼슘 등과 같은 금속산화물이 많이 함유된 물질을 적정 비율로 배합하여 제조된 것으로, 1300℃의 고열로 가공되어 내포된 유해 성분이 모두 제거되고, 인체에 유익한 원적외선이 다량 배출되는 것으로 알려져 있다. 때문에 냉수통(51)은 저장된 이온수를 살균 소독할뿐 아니라 이온수이 효능의 증진 및 보존 효과가 뛰어나다.In addition, the cold water container 51 of the storage unit 50 is made of a ceramic material, the ceramic contains a lot of raw materials such as feldspar, limestone, pottery stone, silica, talc and metal oxides such as shells, calcium carbonate, etc. It is known that it is prepared by mixing the prepared material in an appropriate ratio, and all the harmful components contained in the high temperature of 1300 ° C. are removed, and a large amount of far infrared rays beneficial to the human body are known to be emitted. Due to the cold water tank 51 sterilizes and sterilizes the stored ion water, the ion water is excellent in the improvement and preservation effect.
상기와 같은 구성을 가진 본 발명의 실시예에 따른 이온 냉온정수기는 다음과 같이 사용된다.The ion cold / hot water purifier according to the embodiment of the present invention having the configuration as described above is used as follows.
먼저, 정수기의 전면에 설치된 선택부(90)에서 선택자가 목적과 용도에 맞게 알칼리수, 산성수를 선택하면 상기 선택부(90)의 입력 내용이 제어부(80)에 입력되고 유입된 원수가 비교적 큰 입자를 정제하는 전처리 필터(11)를 통과하여 제 1솔레노이드 밸브(12)에서 정제수의 흐름이 멈추게 된다. 이때 제어부(80)에서 제 1솔레노이드 밸브(12)에 개방하라는 신호를 송신하여 제 1솔레노이드 밸브(12)는 밸브를 개방하여 다음 단계인 카본 필터에서 유해 성분을 흡착하게 된다.First, when the selector selects alkaline water or acidic water according to the purpose and purpose in the selector 90 installed at the front of the water purifier, the input contents of the selector 90 are input to the controller 80 and the raw water introduced is relatively large. The flow of purified water is stopped at the first solenoid valve 12 through the pretreatment filter 11 for purifying the particles. At this time, the control unit 80 transmits a signal to open the first solenoid valve 12 so that the first solenoid valve 12 opens the valve to adsorb harmful components in the carbon filter, which is the next step.
이어서, 전처리 필터부(10)를 통과한 정제수는 전해조(20)에 유입되는데, 전해조(20)는 선택부(90)의 신호에 따라 제어 신호를 송신하는 제어부(80)의 송신 신호에 의해 알칼리수, 산성수의 PH에 맞춰 이온수를 생성하게 된다. 이때 전해조(20)에 퇴수 조절 밸브(60)가 연결되어 있는데 전해조(20) 내용물인 알칼리수와 산성수를 완전히 배수시킬때 퇴수 조절 밸브(60)을 개방하여 완전 배수하게 된다.Subsequently, the purified water passing through the pretreatment filter unit 10 flows into the electrolytic cell 20, and the electrolytic cell 20 is alkaline water by the transmission signal of the control unit 80 which transmits a control signal according to the signal of the selection unit 90. In addition, the ionized water is generated according to the pH of the acidic water. At this time, the drainage control valve 60 is connected to the electrolytic cell 20. When the alkaline and acidic water, which is the contents of the electrolytic cell 20, are completely drained, the drainage control valve 60 is opened to completely drain the water.
이어서, 상기와 같이 전해조(20)에서 생성된 알칼리수와 산성수는 제 2솔레노이드 밸브(30)에서 흐름을 멈추게 된다. 이때 이온수는 후처리 복합 필터부(40)와 압력 센서(70)로 흘러가는데 압력 센서(70)로 흐르는 이온수는 만약, 조리콕(1)을 개방하면 제어부(80)에서 신호를 송신하여 제 2솔레노이드 밸브(30)는 차단되고 압력 센서(70)가 개방되어 조리콕(1)으로 알칼리수 또는 산성수가 배출된다.Subsequently, the alkaline water and the acidic water generated in the electrolytic cell 20 stop the flow in the second solenoid valve 30 as described above. At this time, the ionized water flows into the post-processing composite filter unit 40 and the pressure sensor 70. The ionized water flowing into the pressure sensor 70 transmits a signal from the controller 80 when the cooking cock 1 is opened. The solenoid valve 30 is shut off and the pressure sensor 70 is opened to discharge alkaline water or acidic water to the cooking cock 1.
그리고, 조리콕(1)이 차단되고 이온수가 다음 단계로 흘러가면 제 2솔레노이드 밸브(30)는 개방되어 이온수가 후처리 복합 필터부(40)를 통과하여 다시 한번 더 정제되어 냉수통, 온수통으로 유입된다.Then, when the cooking cock 1 is blocked and the ionized water flows to the next stage, the second solenoid valve 30 is opened so that the ionized water passes through the post-treatment composite filter 40 and is purified once more to a cold water tank or a hot water tank. Inflow.
상기와 같은 흐름에 의해 정제된 이온수는 냉수통(51), 온수통(52)에 각각 저장되어 냉수콕(2), 혹은 온수콕(3)을 개방하여 음용하게 된다.The ionized water purified by the above flow is stored in the cold water tank 51 and the hot water tank 52, respectively, to open the cold water cock 2 or the hot water cock 3 for drinking.
그리고, 상기의 냉수통(51)은 상기에서 언급한 재질인 세라믹으로 제작되어 이온수가 저장 되는데, 보온 효과가 우수하고, 이온수의 효능을 증진시키며, 장기간 보존이 가능하게 된다.In addition, the cold water container 51 is made of the ceramic material of the above-mentioned material is stored in the ionized water, it is excellent in the thermal insulation effect, improve the efficacy of the ionized water, it is possible to long-term storage.
이상에서와 같이 본 고안에 따른 이온 냉온정수기에 의하면, 스케일이 제거되어 맑고 깨끗한 정제수를 음용할 수 있고 냉ㆍ온수통의 열효율을 높일 수 있으며 펌프가 설치되는 것을 제거함으로써 제조 단가를 낮출 수 있는 효과가 있다.As described above, according to the ion cold / hot water purifier according to the present invention, the scale can be removed to drink clean and clean purified water, increase the thermal efficiency of the cold / hot water tank, and reduce the manufacturing cost by eliminating the installation of the pump. There is.
또한 냉수통을 세라믹통으로 저장하여 이온수 효능을 증진시킬 수 있는 등의 효과가 있다.In addition, there is an effect such as to store the cold water in a ceramic barrel to improve the ion water efficiency.
본 발명은 첨부된 도면에 도시된 실시예를 참고로 설명하였으나, 이는 예시적인 것이며, 당해 분야에서 통상의 지식을 가진 자라면 이로부터 다양한 변형 및 균등한 실시예가 가능하다는 점을 이해할 수 있을 것이다. 따라서 본 발명의 진정한 보호 범위는 첨부된 청구 범위에 의해서만 정해져야 할 것이다.Although the present invention has been described with reference to the embodiments illustrated in the accompanying drawings, it is intended to be understood by those skilled in the art that various modifications and equivalent embodiments are possible. Therefore, the true scope of protection of the present invention should be defined only by the appended claims.
스케일이 제거되어 맑고 깨끗한 정제수를 음용할 수 있고 냉ㆍ온수통의 열효율을 높일 수 있으며 펌프가 설치되는 것을 제거함으로써 제조 단가를 낮출 수 있는 효과가 있다.The scale can be removed to drink clean and clean purified water, to improve the thermal efficiency of the cold and hot water tank, and to reduce the manufacturing cost by eliminating the installation of the pump.
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KR100648718B1 (en) * | 2004-06-03 | 2006-11-23 | 삼성에스디아이 주식회사 | Liquid crystal display |
KR100858971B1 (en) | 2007-10-24 | 2008-09-17 | 유인수 | Central water purification system with sterilizer, sterilization method and cleaning method |
KR100947300B1 (en) | 2009-03-13 | 2010-03-11 | (주)진보엔지니어링 | Apparatus for automatically supplying a certain amount of antiseptic solution without electric power supply |
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KR100648718B1 (en) * | 2004-06-03 | 2006-11-23 | 삼성에스디아이 주식회사 | Liquid crystal display |
KR100858971B1 (en) | 2007-10-24 | 2008-09-17 | 유인수 | Central water purification system with sterilizer, sterilization method and cleaning method |
KR100947300B1 (en) | 2009-03-13 | 2010-03-11 | (주)진보엔지니어링 | Apparatus for automatically supplying a certain amount of antiseptic solution without electric power supply |
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