KR20180133715A - Hydroponic farm apprararus using oh radical generation water - Google Patents

Hydroponic farm apprararus using oh radical generation water Download PDF

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KR20180133715A
KR20180133715A KR1020170070925A KR20170070925A KR20180133715A KR 20180133715 A KR20180133715 A KR 20180133715A KR 1020170070925 A KR1020170070925 A KR 1020170070925A KR 20170070925 A KR20170070925 A KR 20170070925A KR 20180133715 A KR20180133715 A KR 20180133715A
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oxygen
water
mixed
radical
mixer
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최봉진
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최봉진
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    • A—HUMAN NECESSITIES
    • A01—AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
    • A01G—HORTICULTURE; CULTIVATION OF VEGETABLES, FLOWERS, RICE, FRUIT, VINES, HOPS OR SEAWEED; FORESTRY; WATERING
    • A01G31/00—Soilless cultivation, e.g. hydroponics
    • A01G31/02—Special apparatus therefor
    • A—HUMAN NECESSITIES
    • A01—AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
    • A01G—HORTICULTURE; CULTIVATION OF VEGETABLES, FLOWERS, RICE, FRUIT, VINES, HOPS OR SEAWEED; FORESTRY; WATERING
    • A01G7/00—Botany in general
    • A01G7/06—Treatment of growing trees or plants, e.g. for preventing decay of wood, for tingeing flowers or wood, for prolonging the life of plants
    • 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
    • C02F1/467—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction
    • C02F1/4676—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction by electroreduction
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P60/00—Technologies relating to agriculture, livestock or agroalimentary industries
    • Y02P60/20—Reduction of greenhouse gas [GHG] emissions in agriculture, e.g. CO2
    • Y02P60/21—Dinitrogen oxide [N2O], e.g. using aquaponics, hydroponics or efficiency measures
    • Y02P60/216—

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  • Forests & Forestry (AREA)
  • Ecology (AREA)
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  • Chemical & Material Sciences (AREA)
  • Biodiversity & Conservation Biology (AREA)
  • Engineering & Computer Science (AREA)
  • Hydrology & Water Resources (AREA)
  • Environmental & Geological Engineering (AREA)
  • General Chemical & Material Sciences (AREA)
  • Electrochemistry (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Wood Science & Technology (AREA)
  • Botany (AREA)
  • Organic Chemistry (AREA)
  • Treatment Of Water By Oxidation Or Reduction (AREA)
  • Hydroponics (AREA)

Abstract

The present invention relates to a hydroponic farming device using OH radical hydrogen water, the device comprising: a low-pressure air compressor configured to compress air; an oxygen separator configured to separate the air compressed by the air compressor into oxygen and nitrogen; an ozone generator configured to subject the oxygen separated by the oxygen separator to a corona discharge using high-voltage electricity to convert the oxygen to ozone; a Venturi pipe configured to mix the ozone generated by the ozone generator with water; a mixer configured to homogenize the mixed water mixed through the Venturi pipe and to discharge a surplus gas to the outside; a spray nozzle configured to turn gas inside the mixed water homogenized by the mixer into fine bubbles while generating iron ions; a reactor tank configured to allow the fine bubbles generated by the spray nozzle and the iron ions to react with each other effectively; and a device for using a product with the above function to generate OH radical hydrogen water and supplying the same to cultivate hydroponic plants.

Description

OH 라디칼 수소수를 이용한 수경농장기{HYDROPONIC FARM APPRARARUS USING OH RADICAL GENERATION WATER} HYDROPONIC FARM APPARARUS USING OH RADICAL GENERATION WATER USING OH RADICAL HYDROXY

본 발명은 OH 라디칼 수소수를 공급하는 수경농장기에 관한 것으로, 더욱 상세하게는 공기중의 산소를 효율적으로 분리하여 고압의 전원을 통과시켜 오존으로 변환시킨 후 오존이 물과 함께 반응하여 OH 라디칼을 형성하는 과정에서 Fe2+ 이온을 촉매로 활용하여 OH라디칼이 다량 발생하도록 하는 OH라디칼 수소수를 이용한 수경농장에 관한 것이다.The present invention relates to a hydroponic plant for supplying OH radical hydrogens, and more particularly, to a process for efficiently separating oxygen in the air and passing it through a high voltage power source to convert it into ozone, The present invention relates to hydroponic farms using OH radical hydrocarbons, in which Fe 2+ ions are used as catalysts to generate large amounts of OH radicals during formation.

일반적으로 OH라디칼수 제조방식은 오존을 물속에 투입시켜 물과의 반응으로 제조하는 과정이다. 이러한 OH라디칼수 제조방법은 산소를 고압의 전류에 의한 코로나방전에 의해서 오존을 만들고 가스상태의 오존을 물에 흡수시켜 물과 오존이 반응하여 OH라디칼을 발생하는 방식이다.Generally, the process for preparing OH radical water is a process in which ozone is introduced into water and reacted with water. This method of producing OH radical water is a method in which ozone is generated by corona discharge caused by high-voltage current, and ozone in a gaseous state is absorbed in water, and OH radical is generated by reaction of water and ozone.

그런데, 이러한 방법은 오존과 물과의 단순반응이므로 반응성이 낮아 OH생성효율이 낮을 뿐만 아니라 고농도의 OH함유수를 제조하는데 많은 어려움이 있었다.      However, since this method is a simple reaction between ozone and water, the reactivity is so low that the OH production efficiency is low, and there is a great difficulty in producing OH-containing water at a high concentration.

그래서, 예를들면 한국 등록특허공보 제 1020160046689호에는, OH라디칼수 생성 및 농도제어장치에 대한 기술에 대한 것으로 액체(물)에 이온화장치를 통과하게 되면 OH 라디칼이 형성된다고 개시되어 있다.      Thus, for example, Korean Patent Publication No. 1020160046689 discloses a technology for an OH radical water production and concentration control device, which discloses that an OH radical is formed when a liquid (water) is passed through an ionization device.

그러나, 상기와 같은 장치에 있어서는 ND자석의 자력을 이용하여 OH라디칼수를 발생하는 장치로서 OH라디칼수 생산효율이 그다지 높지 않고, 대량의 OH라디칼수를 생산하는데 문제점이 있었다.      However, in the above-described apparatus, the OH radical water production efficiency is not so high as to generate OH radical water using the magnetic force of the ND magnet, and there is a problem in producing a large amount of OH radical water.

본 발명은 전술한 바와 같은 종래의 제반 문제점을 해결 보완하기 위한 것으로,       SUMMARY OF THE INVENTION The present invention has been made to solve the above-mentioned problems occurring in the prior art,

본 발명의 목적은 효율적으로 OH라디칼을 생성후 물속에 흡수시켜 다량의 라디칼수를 생산할 수 있고, 물류비 및 인건비를 절감 할 수 있는 OH라디칼 수소수를 이용한 수경농장을 제공하는데 있다.       It is an object of the present invention to provide a hydroponic farm using OH radical hydrogens which can efficiently produce OH radicals and absorb them into water to produce a large amount of radical water, and reduce logistics costs and labor costs.

본 발명의 다른 목적은 다양한 적용분야를 가지고 있는 OH라디칼 수소수를 이용한 수경농장을 소비자들에게 손쉽게 제공하는데 있고 특히 사회적으로 문제시되고 있는 유해성물질을 사용한 농작물로 인한 건강상의 문제를 기존 수경재배보다 20%이상 향상된 성장속도와 친환경적으로 아파트형 가정이나 일반식당에서 직접 수경재배 하여 국민건강을 증진하는데 있다. Another object of the present invention is to provide a hydroponic farm using OH radical hydro- phonic water having various application fields easily to consumers. In particular, the health problems caused by crops using harmful substances which are socially problematic are compared with conventional hydroponic cultivation % Growth rate and eco - friendly way to improve the public health by hydroponically cultivating directly in apartment type family or general restaurant.

상기와 같은 목적을 달성하기 위한 본 발명에 따르면 공기압축식 산소분리장치에 있어서 콤프레샤에 의해서 압축된 공기를 제오라이트와 알루미나가 충진된 관을 통과시키면 초기 저압부분에서 산소가 분리되고 고압부분에서 질소가 분리되므로 질소는 대기중으로 방출시키고 저압부분의 산소만을 선택하여 고압방전관을 통과시키면서 4,000볼트의 고압으로 방전을 시키면 산소(O2)는 분해 합성과정을 통하여 O1, O2, O3의 혼합가스가 발생되고, 이혼합가스는 순환펌핑되고 있는 라인의 벤츄리관의 흡입작용에 의해서 물과 혼합되어 순환수와 혼합가스 혼합탱크로 들어가게 된다. 혼합탱크의 마지막 배출부분은 배출구가 6-7미리의 적은 구멍으로 축소되는 노즐이 붙어 있으며 이 노즐을 통과하여 나오게 되는 혼합수는 압력이 현저히 상승되어 방해판과 충돌을 일으키게 되고, 혼합수에 섞여 있는 혼합가스는 미세하게 쪼개지면서 마이크로 버블이 발생하게 된다. 노즐의 중심부에 있는 철심에 플러스(+)전원을 공급하고 노즐의 외벽에는 마이너스(-)의 직류전원이 공급되면 플러스(+)전극에서 철 2가이온(Fe++)이 발생하여 미세화된 혼합가스와 섞여서 저장탱크로 이송되고 철 2가이온은 오존이 Oh라디칼로 변하는 과정에서 촉매 역할을 하므로 많은 양의 OH라디칼수가 생성되게 된다. 혼합탱크의 상부에는 부유물을 제거 할 수 있는 스키머가 장착되있으며 하부측에는 침전물의 배출장치가 부착되어 있다. According to the present invention, when air compressed by a compressor is passed through a tube filled with zeolite and alumina, oxygen is separated from the initial low pressure portion and nitrogen is separated from the high pressure portion O2, O2, and O3 are generated by decomposing and synthesizing oxygen (O2) when discharged at a high pressure of 4,000 volts while passing nitrogen through the high-pressure discharge tube by selectively discharging nitrogen into the atmosphere, The divide gas is mixed with the water by the inhalation action of the venturi tube of the circulating pumping line and enters the circulating water and mixed gas mixing tank. The final discharge part of the mixing tank is equipped with a nozzle whose outlet is reduced to a small hole of 6-7 mm, and the mixed water coming out through this nozzle is remarkably increased in pressure, causing a collision with the disturbing plate, The microbubbles are generated by finely dividing the mixed gas. (+) Power is supplied to the iron core at the center of the nozzle, and when a negative DC power is supplied to the outer wall of the nozzle, ferrous ions (Fe ++) are generated at the positive electrode, Mixed and transported to the storage tank, and the iron bivalent ion acts as a catalyst in the process of changing ozone to Oh radical, so that a large amount of OH radicals are generated. The upper part of the mixing tank is equipped with a skimmer capable of removing suspended matter, and the lower part is provided with a sediment discharging device.

상기와 같은 본 발명의 실시 예에 따른 OH라디칼 수소수를 이용한 수경농장은 수돗물을 원수로 사용하여 누구나 많은 비용을 들이지 않고 사회적으로 문제시되고 있는 유해성물질을 사용한 농작물로 인한 건강상의 문제를 본 발명은 기존 수경재배보다 20%이상 향상된 성장속도와 친환경적으로 아파트형 가정이나 일반식당에서 직접 수경재배 하여 국민건강을 증진시킬 수 있는 효과를 제공한다In the hydroponic farm using the OH radical hydrogens according to the present invention as described above, the health problem caused by crops using harmful substances, which are not socially troublesome and costly to anyone, It provides the effect of improving the national health by cultivating hydroponics directly in the apartment type family or general restaurant in the growth rate and the environment friendly which is 20% higher than the existing hydroponic cultivation

도 1은 본 발명의 처리계통도.
도 2는 본 발명의 실시예 따른 OH라디칼수 발생장치에 사용된 산소분리기를 보인 개략도
도 2a는 발명의 실시예 따른 OH라디칼 발생장치에 사용된 산소분리기를 보인 상세도
도 3는 본 발명의 실시예 따른 OH라디칼수 발생장치에 사용된 오존발생장치를 보인 사시도.
도 4는 본 발명의 실시예 따른 OH라디칼수 발생장치에 사용된 혼합가스 흡입기를 보인 사시도.
도 5는 본 발명의 실시예 따른 OH라디칼수 발생장치에 사용된 버블발생자치를 보인 개략도
도 6은 본 발명의 실시예 따른 OH라디칼수 발생장치에 사용된 철이온 발생장치를 보인 개략단면도.
도 7은 본 발명의 실시예 따른 OH라디칼수 발생장치에 사용된 OH라디칼 수소수를 이용한 수경농장을 보인 개략단면도.1 is a processing system diagram of the present invention.
2 is a schematic view showing an oxygen separator used in an OH radical water generating apparatus according to an embodiment of the present invention.
2A is a detailed view showing an oxygen separator used in an OH radical generating apparatus according to an embodiment of the present invention.
3 is a perspective view showing an ozone generator used in an OH radical water generator according to an embodiment of the present invention.
4 is a perspective view showing a mixed gas inhaler used in an OH radical water generating apparatus according to an embodiment of the present invention.
5 is a schematic view showing a bubble generator used in an OH radical water generator according to an embodiment of the present invention.
6 is a schematic cross-sectional view showing an iron ion generating device used in an OH radical water generating apparatus according to an embodiment of the present invention.
7 is a schematic cross-sectional view showing a hydroponic farm using OH radical hydrogens used in an OH radical water generator according to an embodiment of the present invention.

이하, 본 발명에 따른 펜톤반응에 의한 OH라디칼 수소수를 이용한 수경농장에 대한 바람직한 실시예에 대해 첨부된 도면들을 참조로 하여 상세히 설명한다.       BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, preferred embodiments of a hydroponic farm using OH radical hydrogens by Fenton reaction according to the present invention will be described in detail with reference to the accompanying drawings.

우선, 도면들 중, 동일한 구성요소 또는 부품들은 가능한 동일한 참조부호로 나타내고 있음을 유의해야 한다. 또한, 본 발명을 설명함에 있어, 관련된 공지기능 혹은 구성에 대한 구체적인 설명은 본 발명의 요지를 모호하지 않게 하기 위하여 생략하기로 한다.      First, in the drawings, it is to be noted that like components or parts are denoted by the same reference symbols as possible. In the following description of the present invention, a detailed description of known functions and configurations incorporated herein will be omitted so as to avoid obscuring the subject matter of the present invention.

도1에 도시된 바와 같이, 본 발명의 실시에에 따른 펜톤반응(Fenton reaction)에 의해서 OH라디칼 발생장치는, 대기중으로부터 공기를 유입시켜 산소를 분리하는 산소발생장치(10), 분리된 산소를 오존으로 변환 시키는 오존발생장치(20), 발생된 오존과 잔존하는 산소, 발생기산소등이 혼합된 혼합가스를 물에 흡수시키는 벤츄리관(30), 혼합가스와 물을 혼합시키고 잉여의 가스를 배출시키는 혼합기(40), 물과 혼합된 혼합가스를 미세화 시킴과 동시에 철2가(Fe++)이온을 발생시키는 노즐(50), 최종적으로 철2가이온을 촉매로 하여 미세화된 혼합가스와 물이 펜톤반응이 이루어지도록 하는 반응탱크(60), OH라디칼 수소수를 생산하는 장치가 있는 수경농장(70) 기능들로 구성된다.       As shown in FIG. 1, the OH radical generating apparatus by the Fenton reaction according to the embodiment of the present invention includes an oxygen generating apparatus 10 for separating oxygen by introducing air from the atmosphere, A venturi tube 30 for absorbing a mixed gas formed by mixing generated ozone and remaining oxygen, generator oxygen, etc. into water, and a venturi tube 30 for mixing a mixed gas and water, A mixer 40 for discharging the water, a nozzle 50 for micronizing the mixed gas mixed with water and generating iron (II) ions (Fe ++), and finally a mixed gas and water A reaction tank 60 for allowing the Fenton reaction to take place, and a hydroponic farm 70 having an apparatus for producing OH radical hydrogens.

상기 산소발생장치(10)는 콤프레샤(10a)로 부터 유입된 압축공기를 제오라이트와 알루미나로 충진된 관(10b)을 통과하게 되면 도 3에에서 보는 바와 같이 초기 저압부분(10d)에서 산소가 분리되고 고압부분(10c)에서 질소가 분리되는데 질소는 대기중으로 배출하고 21%의 산소만을 사용하여 다음공정으로 보내주게 된다.        3, when the compressed air introduced from the compressor 10a passes through the pipe 10b filled with zeolite and alumina, the oxygen generator 10 separates oxygen from the initial low-pressure portion 10d Nitrogen is separated from the high-pressure portion 10c. Nitrogen is discharged to the atmosphere and is sent to the next process using only 21% of oxygen.

상기 오존발생장치(20)는 산소발생장치(10)로 부터 유입된 산소를 4,000볼트의 전기를 직류전기로 변환하여 양극판(20a)과 음극판(20b)의 관으로 통과하게 되면 산소(O2)는 발생기산소(O)로 분해되고 발생기 산소는 산소(O2)와 결합하여 오존(O3)이 발생하게 된다.       When the ozone generator 20 converts 4,000 volts of oxygen introduced from the oxygen generator 10 into DC electricity and passes through the cathode plate 20a and the cathode plate 20b, The generator oxygen is decomposed into oxygen (O) and the generator oxygen is combined with oxygen (O2) to generate ozone (O3).

반응식 : O2 + hv(λ<310nm) → O + O2Reaction: O2 + hv (λ <310 nm) → O + O2

O + O2 + hv(λ<310nm) → O + O2 + O3          O + O 2 + hv (λ <310 nm) → O + O 2 + O 3

상기 벤츄리관(30)은 오존발생장치(20)로부터 유입된 혼합가스, 발생기산소(O), 산소(O2), 오존(O3)을 순환펌프(40a)로부터 2kg/cm2의 압력으로 유입(30a)되면 벤츄리원리에 의해서 진공이 형성(30b)되므로 물과 혼합가스가 혼합(30c)되어 배출되게 된다.       The venturi tube 30 introduces the mixed gas introduced from the ozone generator 20, the generator oxygen 0, the oxygen 02 and the ozone 03 from the circulation pump 40a at a pressure of 2 kg / The vacuum is formed by the venturi principle 30b so that water and the mixed gas are mixed 30c and discharged.

상기 혼합기(40)는 벤츄리관(30)으로부터 유입된 혼합수를 물과의 접촉시간을 최대화 하여 균일한 혼합이 이루어지도록 하기 위하여 순환펌프(40a)의 토출압력을 2kg/cm2으로 관리(40b)하여 혼합가스와 물의 혼합이 최대가 되도록 한다. 이때 물과의 혼합되지 않는 잉여의 가스는 버블발생의 장애가 되므로 외부로 배출(40c)한다.       The mixer 40 controls the discharge pressure of the circulation pump 40a to be 2 kg / cm 2 in order to uniformly mix the mixed water introduced from the venturi pipe 30 by maximizing the contact time with water, So that the mixture of the mixed gas and water is maximized. At this time, surplus gas not mixed with water is discharged (40c) to the outside because it becomes a hindrance of bubble generation.

상기 노즐(50)은 미세기포 발생과 철이온(Fe++)을 동시에 발생하기 위한 목적이며 혼합기(40)으로부터 유입된 혼합수를 축소된 원형의 다수의 구멍으로 통과하게 하여 전면에 위치한 충돌막(50b)과 충돌하게 하면 혼합가스의 기포는 미세하게 됨과 동시에 충돌막 뒤에 위치한 철편과 노즐의 본체에는 직류전기가 흐르므로 철편에서 철이온(Fe++)이 방출되어 최종적으로 미세화된 혼합가스와 철이온이 반응조로 유입되어 반응조에서는 펜톤 반응에 의해서 OH라디칼 수가 생성되게 된다.       The nozzle 50 is for generating fine bubbles and iron ions at the same time and allows the mixed water introduced from the mixer 40 to pass through a plurality of reduced circular holes to form a collision film 50b The bubbles of the mixed gas become fine and at the same time, the direct current flows to the body of the iron piece and the nozzle located behind the collision film, so that iron ions (Fe ++) are released from the iron pieces and finally, And OH radicals are generated by the Fenton reaction in the reaction tank.

펜톤 반응식 :Fenton's reaction:

Figure pat00001
Figure pat00001

Figure pat00002
Figure pat00002

10: 산소발생기 10a: 콤프레샤
10b: 충진관 10c: 질소배출관
10d: 산소배출관 20: 코로나 방전관
20a: 양극관 20b: 음극관
20c; 오존 30: 벤츄리관
30a: 벤츄리 유입구 33b: 혼합가스 유입구
30c: 혼합가스 배출구 40: 혼합기
40a: 순환펌프 40b: 압력계
40c: 잉여가스배출구 50: 분사노즐
50a: 혼합수축소분사구 50b: 충돌막
50c: 철편 60: 반응조탱크
70:수경농장기10: Oxygen generator 10a: Compressor
10b: a filling pipe 10c: a nitrogen discharge pipe
10d: oxygen discharge pipe 20: corona discharge tube
20a: anode tube 20b: cathode tube
20c; Ozone 30: Venturi tube
30a: Venturi inlet 33b: Mixed gas inlet
30c: Mixed gas outlet 40: Mixer
40a: circulation pump 40b: pressure gauge
40c: surplus gas outlet 50: injection nozzle
50a: Mixed water reduction nozzle 50b: Collision film
50c: iron piece 60: reactor tank
70: Can cervical organ

Claims (7)

펜톤반응에 의해서 OH라디칼 수소수 수경농장기에 있어서,
저압의 콤프레샤(10a)에 의해서 공기가 압축되어 충진관(10b)으로 유입된 후 산소는 저압단계에서 분리(10d)되고 질소는 고압단계에서 분리(10c)되는 산소발생기(10);
상기 산소발생기(10)를 통해서 분리된 산소를 양극관(20a)과 음극관(20b) 사이를 통과 시키면서 고압의 전기로 코로나 방전을 시켜 오존을 발생시키는 코로나방전관(20);
상기 코로나방전관(20)에서 발생된 오존을 순환펌프(40a)의 상부토출부에 설치되어 있는 벤츄리유입구(30a)로 유입시켜 순환수에 흡수되도록 하는 벤츄리관(30);
상기 벤츄리관(30)을 통하여 혼합된 혼합수가 균등하게 혼합되도록 압력계(40b)의 압력을 일정하게 유지하면서 유체의 흐름을 난류흐름으로 유도하고 잉여의 가스가 발생하면 혼합기(40) 상부에 설치되어 있는 잉여가스배출구(40c)를 통하여 배출하게 하는 혼합기(40);
상기 혼합기(40)을 통하여 균등하게 혼합된 혼합수중의 기포들을 더욱 더 미세한 기포로 만들기 위하여 혼합수 축소분사구(50a)의 축소된 구멍을 통과시켜 압력을 증가시킨 후 충돌막(50b)과 충돌하도록 함과 동시에 철편(50c)에 직류전원을 흐르게 하여 철편(50c)이 철이온을 방출하게 하는 분사노즐(50);
상기 분사노즐(50)을 통하여 통과된 혼합수가 철이온(Fe++)을 촉매로 하여 펜톤반응이 이루어지도록 하는 반응조 탱크(60);를
상기 기능을 가진 제품을 통하여 OH라디칼 수소수 수경농장기(70);를 포함하여 구성되는 것을 특징으로 하는 OH라디칼 수소수 수경농장기.In the OH radical hydrofinishing plantation plant by the Fenton reaction,
An oxygen generator 10 for compressing air by a low-pressure compressor 10a to be introduced into a filling pipe 10b, separating oxygen 10d at a low pressure stage and nitrogen 10c at a high pressure stage;
A corona discharge tube 20 for generating ozone by discharging oxygen separated through the oxygen generator 10 between an anode tube 20a and a cathode tube 20b by a high-voltage electric corona discharge;
A venturi pipe 30 for allowing the ozone generated in the corona discharge tube 20 to flow into the venturi inlet 30a provided in the upper discharge portion of the circulation pump 40a to be absorbed into the circulating water;
The flow of the fluid is guided to the turbulent flow while the pressure of the pressure gauge 40b is kept constant so that the mixed water mixed through the venturi pipe 30 is uniformly mixed. A mixer 40 for discharging the gas through the surplus gas outlet 40c;
The bubbles in the mixed water evenly mixed through the mixer 40 are passed through the reduced hole of the mixed water reducing jet opening 50a to increase the pressure and collide with the collision film 50b An injection nozzle 50 for allowing direct current to flow through the iron piece 50c to cause the iron piece 50c to emit iron ions;
And a reaction tank 60 for allowing the Fenton reaction to be performed using the mixed water passed through the injection nozzle 50 with Fe ++ as a catalyst
And an OH radical hydrogensconcentrating organ (70) through the product having the above function. 청구항 1에 있어서, 상기 충진관(10b)은, 공기중의 산소와 질소를 저압상태에서 효율적으로 분리하기 위하여 제오라이트와 알루미나를 혼합하여 충진하는 것을 특징으로 하는 OH라디칼 수소수 수경농장기.[Claim 6] The method according to claim 1, wherein the filling tube (10b) is filled with zeolite and alumina in order to efficiently separate oxygen and nitrogen in the air at a low pressure. 청구항 1에 있어서, 상기 코로나 방전관(20)은, 산소를 오존으로 변환시키기 위하여 직류전원을 사용하여 양극과 음극의 전압을 4,000볼트로 하여 방전하는 것을 특징으로 하는 OH라디칼 수소수 수경농장기.The corona discharge tube (20) according to claim 1, wherein the corona discharge tube (20) is discharged by using a DC power source to convert oxygen into ozone, the voltage between the anode and the cathode being 4,000 volts. 청구항 1에 있어서, 상기 혼합기(40)는, 순환수와 혼합가스가 균등하게 혼합이 되도록 하기 위하여 혼합기 내부에서 난류흐름으로 유도하고 잉여의 가스는 외부로 배출하게 하는 것을 특징으로 하는 OH라디칼 수소수 수경농장기.The mixer (40) according to claim 1, wherein the mixer (40) induces a turbulent flow in the mixer and a surplus gas to the outside in order to uniformly mix the circulating water and the mixed gas. Can a cervical organ. 청구항 1에 있어서, 상기 분사노즐(50)은, 혼합수 중에 포함되어 있는 혼합가스 기포크기를 미세화 하기 위하여 분사구(50a)를 유체가 흐르는 관경보다 적은 구경으로 구성하거나 다수의 적은 구경으로 구성하고 분사구경의 3배수 거리 이내에 충돌막을 설치하는 것을 특징으로 하는 OH라디칼 수소수 수경농장기.The injection nozzle (50) according to claim 1 or 2, wherein the injection nozzle (50) is configured such that the injection port (50a) is formed to have a diameter smaller than the diameter of the flow of the fluid or a plurality of small diameters Wherein the impingement film is installed within a distance of three times the diameter of the aperture. 청구항 1에 있어서, 상기 분사노즐(50)은, 2가의 철이온(Fe++)이 발생되게 하기 위해서 노즐 본체를 양극으로 하고 내부의 철편을 음극으로 하거나, 노즐본체를 음극으로 하고 내부의 철편을 양극으로 하거나, 음극과 양극이 주기적으로 바뀌도록 하는 것을 특징으로 하는 OH라디칼 수소수 수경농장기.[2] The apparatus according to claim 1, wherein the injection nozzle (50) comprises a nozzle body as an anode, an inner iron piece as a cathode, a nozzle body as a cathode, and an inner iron piece as an anode Or alternatively, the cathode and the anode are periodically changed. 청구항 1에 있어서, 상기 기능으로 이루어지진 OH라디칼 수소수를 공급하는 것을 특징으로 하는 OH라디칼 수소수 수경농장기.




[3] The cryogenic organ of OH radical hydrogens as claimed in claim 1, wherein the OH radical hydrofluoric acid having the above function is supplied.




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CN112082902A (en) * 2020-07-25 2020-12-15 东北电力大学 Device for improving density of OH free radicals discharged in water and measuring method thereof
KR20210140887A (en) * 2020-05-14 2021-11-23 주식회사 그룬 Apparatus for supply nutrient to support crop growth
KR20210141845A (en) * 2020-05-14 2021-11-23 주식회사 그룬 Method for supply nutrient to support crop growth
CN116655098A (en) * 2023-08-01 2023-08-29 中建安装集团有限公司 Method for degrading phenol by catalytic oxidation of microbubble ozone

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20210140887A (en) * 2020-05-14 2021-11-23 주식회사 그룬 Apparatus for supply nutrient to support crop growth
KR20210141845A (en) * 2020-05-14 2021-11-23 주식회사 그룬 Method for supply nutrient to support crop growth
CN112082902A (en) * 2020-07-25 2020-12-15 东北电力大学 Device for improving density of OH free radicals discharged in water and measuring method thereof
CN112082902B (en) * 2020-07-25 2024-02-13 东北电力大学 Device for improving density of OH free radicals discharged in water and measuring method thereof
CN116655098A (en) * 2023-08-01 2023-08-29 中建安装集团有限公司 Method for degrading phenol by catalytic oxidation of microbubble ozone
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