KR20000020733A - Water treatment method using magnetic force - Google Patents
Water treatment method using magnetic force Download PDFInfo
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- KR20000020733A KR20000020733A KR1019980039470A KR19980039470A KR20000020733A KR 20000020733 A KR20000020733 A KR 20000020733A KR 1019980039470 A KR1019980039470 A KR 1019980039470A KR 19980039470 A KR19980039470 A KR 19980039470A KR 20000020733 A KR20000020733 A KR 20000020733A
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- 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
- C02F1/4608—Treatment of water, waste water, or sewage by electrochemical methods using electrical discharges
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- 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
- C02F1/305—Treatment of water, waste water, or sewage by irradiation with electrons
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- 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
- C02F1/34—Treatment of water, waste water, or sewage with mechanical oscillations
- C02F1/36—Treatment of water, waste water, or sewage with mechanical oscillations ultrasonic vibrations
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- 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
- C02F1/48—Treatment of water, waste water, or sewage with magnetic or electric fields
- C02F1/481—Treatment of water, waste water, or sewage with magnetic or electric fields using permanent magnets
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- 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
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/5236—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents
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Abstract
Description
본 발명은 비열 플라즈마 및 자기화를 이용한 수처리 방법에 관한 것이다.The present invention relates to a water treatment method using non-thermal plasma and magnetization.
비열 플라즈마 공정은 상압 기체 흐름내의 저농도 VOCs, NOx, HAPs의 방지에 적용할 수 있는 최신 기술로서 전기 방전 또는 전자빔을 이용하여 플라즈마를 형성시킬 수 있다.Non-thermal plasma processing is a state-of-the-art technology that can be applied to the prevention of low concentrations of VOCs, NOx and HAPs in atmospheric gas streams, which can form plasma using an electrical discharge or electron beam.
1970연대부터 발전소 배기가스내의 NOx 제거에 전자빔을 이용하는 방법이 연구되어 왔고 최근 들어 전기 방전 방법이 배기가스 정화 분야에 이용되고 있다. 특히, 비열 플라즈마를 디젤엔진 배기가스내의 NOx 처리에 응용하는 방안에 많은 관심이 집중되고 있는데 산소가 풍부한 경우 NOx의 화학적 환원법은 자동차 등의 이동오염원에 새로운 돌파구를 제시할 것으로 여겨지나 현재는 고정 연소오염원에만 적용되고 있다.Since the 1970s, a method of using an electron beam to remove NOx in exhaust gas of a power plant has been studied. In recent years, an electric discharge method has been used in the field of exhaust gas purification. In particular, much attention has been focused on the application of non-thermal plasma to NOx treatment in diesel engine exhaust gas.In the case of oxygen-rich, NOx chemical reduction method is expected to present new breakthroughs in mobile pollutants such as automobiles. Applied only to pollutants.
이러한 비열 플라즈마 공정은 전기 에너지의 대부분이 기체의 가열보다는 강력한 전자를 생산하는데 이용되며 변환점에서 플라즈마가 발생되는 원리를 이용한 것으로 전자 충격 해리나 배경 기체 분자의 이온화를 통해 강력한 전자가 오염물질 분자를 산화, 환원, 또는 파괴할 수 있는 자유기와 이온 및 또 다른 분자를 생성하게 된다. 대부분 저농도 대기 오염 물질을 제어할 경우 에너지 선택성으로 인하여 비열 플라즈마 방법이 가장 많이 적용되어 왔다.This non-thermal plasma process uses the principle that most of the electrical energy is used to produce strong electrons rather than heating the gas, and the plasma is generated at the transition point. The strong electrons oxidize contaminant molecules through electron impact dissociation or ionization of background gas molecules. It creates free radicals, ions, and other molecules that can be reduced, reduced, or destroyed. In most low concentration air pollutants, the non-thermal plasma method has been most frequently applied due to energy selectivity.
또한, 물의 자기화 공정은 물 분자의 구조를 변경시켜서 물 분자가 육각수 구조를 가지도록 하는데 사용되어 왔다.In addition, the water magnetization process has been used to change the structure of water molecules so that the water molecules have a hexagonal structure.
본 발명은 상기한 비열 플라즈마 공정 및 자기화 공정을 수처리 방법에 도입하고자 한다.The present invention seeks to introduce the above-described nonthermal plasma process and magnetization process into a water treatment method.
본 발명은 비열 플라즈마 공정 및 자기화 공정을 수처리 방법에 도입하는데 적합한 수처리 방법을 제공하고자 한다.The present invention seeks to provide a water treatment method suitable for introducing a non-thermal plasma process and a magnetization process into a water treatment method.
도1은 본 발명에 의한 비열 플라즈마 및 자기화를 이용한 수처리 방법의 공정도이다.1 is a process chart of a water treatment method using non-thermal plasma and magnetization according to the present invention.
* 도면의 주요한 부분에 대한 부호의 설명 *Explanation of symbols on the main parts of the drawings
10 : 자장교반기 20 : 초음파발생기10: magnetic stirrer 20: ultrasonic generator
30 : 비열 플라즈마 장치 40 : 자화장치30: non-thermal plasma apparatus 40: magnetization apparatus
50 : 전자빔 램프50: electron beam lamp
11 : 1차분해조 12 : 2차분해조11: primary digestion tank 12: secondary digestion tank
13 : 응집조 14 : 침전조13: flocculation tank 14: sedimentation tank
상기한 바와 같은 목적을 달성하기 위하여, 본 발명에 의한 비열 플라즈마 및 자기화를 이용한 수처리 방법은, 영구자석을 교반시켜서 원수 흐름을 원활하게 하는 자기교반기, 고형 물질을 분해시키고 오염 물질을 탈리시키는 초음파발생기 및 공기를 비열 플라즈마화하여 주입하는 비열 플라즈마 장치에 의하여 유입수 내의 오염 물질을 분해하고 질소를 제거하는 1차분해조 단계; 상기한 자기교반기, 초음파발생기, 비열 플라즈마 장치 이외에, 물분자의 구조를 변경하기 위한 자화장치, 전자빔을 조사하기 위한 전자빔램프를 수반하여, 상기 1차분해조 단계를 거친 처리수에 대하여 물 분자의 구조를 변경하고, 오염 물질을 분해하고 질소를 재차 제거하는 2차분해조 단계; 상기 2차분해조 단계를 거친 처리수 중 고형 물질을 응집시키는 응집조 단계; 및 상기 응집조 단계에서 응집된 고형 물질을 침전시켜 제거하는 침전조 단계를 포함하는 것을 특징으로 한다.In order to achieve the object as described above, the water treatment method using the non-thermal plasma and magnetization according to the present invention, the magnetic stirrer to smooth the flow of raw water by stirring the permanent magnet, ultrasonic wave to decompose the solid material and decontaminate the pollutant A primary decomposition tank step of decomposing contaminants in the influent and removing nitrogen by a non-thermal plasma apparatus for injecting the generator and air into non-thermal plasma; In addition to the magnetic stirrer, the ultrasonic generator, and the non-thermal plasma apparatus, the structure of the water molecules with respect to the treated water having undergone the first decomposition tank step is accompanied by a magnetization apparatus for changing the structure of the water molecules and an electron beam lamp for irradiating the electron beam. A second decomposition tank step of decomposing and decomposing contaminants and removing nitrogen again; An agglomeration tank step of agglomerating the solid material in the treated water that has passed through the secondary decomposition tank step; And a precipitation tank step of precipitating and removing the solid matter aggregated in the flocculation tank step.
이하에서, 첨부된 도면을 참조하면서 본 발명의 바람직한 일실시예에 의한 수처리 방법을 상세하게 설명한다.Hereinafter, with reference to the accompanying drawings will be described in detail the water treatment method according to an embodiment of the present invention.
도1은 본 발명에 의한 비열 플라즈마 및 자기화를 이용한 수처리 방법의 공정도이다.1 is a process chart of a water treatment method using non-thermal plasma and magnetization according to the present invention.
도1에 도시된 바와 같이, 본 발명에 의한 수처리 방법은, 1차분해조(11), 2차분해조(12), 응집조(13) 및 침전조(14)로 구성된다.As shown in Fig. 1, the water treatment method according to the present invention comprises a primary decomposition tank 11, a secondary decomposition tank 12, a coagulation tank 13, and a precipitation tank 14.
1차분해조(11)에는 자장교반기(10), 초음파발생기(20) 및 비열 플라즈마 장치(30)가 수반된다.The primary decomposition tank 11 is accompanied by a magnetic stirrer 10, an ultrasonic generator 20, and a non-thermal plasma apparatus 30.
자장교반기(10)는 영구자석를 교반시켜서 1차분해조(11) 내의 원수 흐름을 원활하게 함에 의하여, 비열 플라즈마 장치(30)를 통과한 공기가 골고루 주입되도록 한다. 초음파발생기(20)는 고형 물질을 분해시키고 오염 물질을 탈리시킨다.The magnetic stirrer 10 stirs the permanent magnets to smooth the flow of raw water in the primary digestion tank 11 so that the air passing through the non-thermal plasma apparatus 30 is evenly injected. The ultrasonic generator 20 decomposes the solid material and desorbs the pollutant.
비열 플라즈마화된 공기는 유입수내의 OH 라디칼을 증대시키며 전자에 의한 질소의 처리도 동시에 할 수 있다.Non-thermal plasmad air increases OH radicals in the influent and can simultaneously process nitrogen by electrons.
비열 플라즈마 장치(30)내에서 전자가 공기와 충돌하면 공기중의 산소분자와 질소분자는 다음과 같은 반응이 일어난다.When electrons collide with air in the nonthermal plasma apparatus 30, oxygen molecules and nitrogen molecules in the air occur as follows.
e-+ O2→ e-+ O(3P) + O(1D) e - + O 2 → e - + O (3 P) + O (1 D)
e-+ N2→ e-+ N + N e - + N 2 → e - + N + N
상기한 반응을 일으킨 각 원소들은 물 속에서 다음과 같은 복합적인 반응하여 OH 라디칼을 생성하여 오염 물질을 제거하거나, 암모니아성 질소 및 질산성 질소를 제거한다.Each of the elements causing the above reaction generates a complex reaction in water to generate OH radicals to remove contaminants or to remove ammonia nitrogen and nitrate nitrogen.
먼저, OH 라디칼을 생성하여 오염 물질을 제거하는 공정을 살펴본다.First, the process of generating OH radicals to remove contaminants is described.
O(1D) + H2O → OH + OHO ( 1 D) + H 2 O → OH + OH
M(오염 물질) + OH → Moxid(산화된 오염 물질)M (pollutant) + OH → Moxid (oxidized pollutant)
암모니아성 질소를 제거하는 공정을 살펴본다.Examine the process for removing ammonia nitrogen.
2NH3+ 6OH → N2↑ + 6H202NH 3 + 6OH → N 2 ↑ + 6H 2 0
질산성 질소를 제거하는 공정을 살펴본다.Look at the process for removing nitrate nitrogen.
NO3 -+ 2H2O + 3e-→ NO + 4OH-또는, NO3 -+ 4H++ 3e-→ NO + 2H2O NO 3 - + 2H 2 O + 3e - → NO + 4OH - or, NO 3 - + 4H + + 3e - → NO + 2H 2 O
N + NO → N2↑ + ON + NO → N 2 ↑ + O
1차분해조(11)는 또한, 유입수를 저장하는 저류조의 역할을 동시에 수행한다.The primary cracking tank 11 also simultaneously serves as a storage tank for storing the influent.
2차분해조(12)에는 자장교반기(10), 초음파발생기(20), 비열 플라즈마 장치(30), 자화장치(40) 및 전자빔램프(50)가 수반된다.The secondary decomposition tank 12 includes a magnetic stirrer 10, an ultrasonic generator 20, a non-thermal plasma apparatus 30, a magnetization apparatus 40, and an electron beam lamp 50.
1차분해조(11)를 통과한 처리수는 2차분해조(12)에서 재차 비열 플라즈마화된 공기에 의하여 오염 물질 및 질소가 제거된다. 또한, 2차분해조(12)에서는 자화장치(40)에 의하여 물 분자의 구조 변경이 일어나며, 전자빔 램프(50)에 의하여 전자빔이 조사되어 전자에 의한 질산성 질소 제거 효율을 높인다. 2차분해조(12)에서도 1차분해조(11)에서와 마찬가지로, 자장교반기(10)는 영구자석를 교반시켜서 2차분해조(12) 내의 원수 흐름을 원활하게 함에 의하여, 비열 플라즈마 장치(30)를 통과한 공기가 골고루 주입되도록 하고, 초음파발생기(20)는 고형 물질을 분해시키고 오염 물질을 탈리시킨다. 물 분자의 구조 변경을 위한 자화장치(40)의 자기장의 세기는 약 6,000가우스 이상이 바람직하다.The treated water that has passed through the primary cracking tank 11 is removed from the secondary cracking tank 12 by the non-thermal plasmad air again to remove contaminants and nitrogen. In addition, in the secondary decomposition tank 12, the structure of water molecules is changed by the magnetization device 40, and the electron beam is irradiated by the electron beam lamp 50 to increase the nitrate nitrogen removal efficiency by electrons. Similarly to the primary decomposition tank 11, the magnetic stirrer 10 also passes through the non-thermal plasma apparatus 30 by smoothing the flow of raw water in the secondary decomposition tank 12 by stirring the permanent magnet in the secondary decomposition tank 12. The air is evenly injected, and the ultrasonic generator 20 decomposes the solid matter and desorbs the pollutant. The magnetic field strength of the magnetizer 40 for changing the structure of water molecules is preferably about 6,000 gauss or more.
2차분해조(12)에서는 2차분해조(12)의 다음 단계인 응집조(13)에서의 고형 물질의 응집을 용이하게 하기 위하여 응집촉진제로서 소석회와 맥반석을 주입할 수도 있다. 이때 주입되는 소석회와 맥반석의 비율은 폐수의 농도에 따라서 조절된다.In the secondary cracking tank 12, slaked lime and ganban stone may be injected as flocculating accelerators in order to facilitate flocculation of the solid matter in the flocculating tank 13, which is the next step of the secondary cracking tank 12. At this time, the ratio of slaked lime and elvan rock is adjusted according to the concentration of wastewater.
2차분해조(12)에서 오염 물질이 분리된 처리수는 응집조(13)에서 고형 물질의 응집이 일어난다. 이때 응집을 용이하게 하기 위하여 고분자 물질을 첨가할 수도 있다.In the treated water in which the pollutant is separated in the secondary decomposition tank 12, the flocculation tank 13 causes the aggregation of the solid material. In this case, a polymer material may be added to facilitate aggregation.
응집조(13)를 거친 처리수에 포함된 응집된 고형 물질은 침전조(14)에서 침전되어 처리수와 분리된다.Aggregated solid matter contained in the treated water passed through the coagulation tank 13 is precipitated in the settling tank 14 to be separated from the treated water.
한편, 오염 물질의 종류에 따라서 1차분해조(11) 및 2차분해조(12)에서 분해된 오염 물질이 침전되지 않는 성질을 가질 수도 있다. 이러한 경우에는 상기한 응집조(13) 및 침전조(14)를 대신하여, 가압부상조 또는 부상조를 사용하여 오염 물질을 처리수 상부로 부상시켜서 제거할 수도 있다.On the other hand, depending on the type of contaminants may have a property that the contaminants decomposed in the primary decomposition tank 11 and the secondary decomposition tank 12 does not precipitate. In this case, instead of the flocculation tank 13 and the settling tank 14 described above, the contaminant may be floated and removed by using a pressurized flotation tank or flotation tank.
침전조(14)를 거친 처리수는 선택적으로, 치환조를 이용한 부가적인 여과공정을 더 거칠 수도 있다.The treated water passing through the settling tank 14 may optionally be further subjected to an additional filtration step using a substitution bath.
이상에서 설명한 바와 같이, 본 발명은 비열 플라즈마 및 자기화를 이용한 수처리 방법을 제공한다. 본 발명에 의하면 비열 플라즈마를 이용하여 오염 물질, 암모니아성 질소 및 질산성 질소를 제거할 수 있고, 자기화장치를 이용하여 물분자의 구조를 변경할 수 있다.As described above, the present invention provides a water treatment method using non-thermal plasma and magnetization. According to the present invention, contaminants, ammonia nitrogen and nitrate nitrogen can be removed using a non-thermal plasma, and the structure of water molecules can be changed using a magnetizer.
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Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20000012731A (en) * | 1999-12-22 | 2000-03-06 | 지종기 | High density plasma method and device coupled with ultrasonic wave for waste water treatment using magnet and tungsten catalyst |
KR100418362B1 (en) * | 2001-10-09 | 2004-02-11 | 박성돈 | Ionized gas aided system and method for treating high concentration organic wastewater |
KR100708367B1 (en) * | 2006-06-21 | 2007-04-18 | 한국원자력연구소 | Method for enhancing biological treatment efficiency of nitrogen using radiation |
KR101011701B1 (en) * | 2008-09-01 | 2011-01-28 | 김동휘 | Waste Cooking Oil Recyling Device |
-
1998
- 1998-09-23 KR KR1019980039470A patent/KR20000020733A/en not_active Application Discontinuation
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20000012731A (en) * | 1999-12-22 | 2000-03-06 | 지종기 | High density plasma method and device coupled with ultrasonic wave for waste water treatment using magnet and tungsten catalyst |
KR100418362B1 (en) * | 2001-10-09 | 2004-02-11 | 박성돈 | Ionized gas aided system and method for treating high concentration organic wastewater |
KR100708367B1 (en) * | 2006-06-21 | 2007-04-18 | 한국원자력연구소 | Method for enhancing biological treatment efficiency of nitrogen using radiation |
KR101011701B1 (en) * | 2008-09-01 | 2011-01-28 | 김동휘 | Waste Cooking Oil Recyling Device |
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