KR200351518Y1 - Pressurized Wound Disassembler - Google Patents
Pressurized Wound Disassembler Download PDFInfo
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- KR200351518Y1 KR200351518Y1 KR20-2004-0006412U KR20040006412U KR200351518Y1 KR 200351518 Y1 KR200351518 Y1 KR 200351518Y1 KR 20040006412 U KR20040006412 U KR 20040006412U KR 200351518 Y1 KR200351518 Y1 KR 200351518Y1
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 55
- 239000002351 wastewater Substances 0.000 claims abstract description 41
- 238000007667 floating Methods 0.000 claims abstract description 16
- 238000000354 decomposition reaction Methods 0.000 claims abstract description 12
- 238000005188 flotation Methods 0.000 claims abstract description 5
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 19
- 229910052760 oxygen Inorganic materials 0.000 claims description 19
- 239000001301 oxygen Substances 0.000 claims description 19
- 239000000356 contaminant Substances 0.000 claims description 16
- 238000010790 dilution Methods 0.000 claims description 12
- 239000012895 dilution Substances 0.000 claims description 12
- 125000000129 anionic group Chemical group 0.000 claims description 10
- 230000005415 magnetization Effects 0.000 claims description 10
- 239000004480 active ingredient Substances 0.000 claims description 8
- 230000008859 change Effects 0.000 claims description 8
- 150000001450 anions Chemical class 0.000 claims description 7
- 238000006243 chemical reaction Methods 0.000 claims description 7
- 238000004065 wastewater treatment Methods 0.000 claims description 7
- 238000002347 injection Methods 0.000 claims description 6
- 239000007924 injection Substances 0.000 claims description 6
- 238000005086 pumping Methods 0.000 claims description 6
- 238000005273 aeration Methods 0.000 claims description 4
- 239000000428 dust Substances 0.000 claims description 4
- 238000000034 method Methods 0.000 claims description 4
- 230000008569 process Effects 0.000 claims description 4
- 239000013049 sediment Substances 0.000 claims description 4
- 239000007787 solid Substances 0.000 claims description 3
- 239000003344 environmental pollutant Substances 0.000 abstract description 19
- 231100000719 pollutant Toxicity 0.000 abstract description 19
- 238000000746 purification Methods 0.000 abstract description 11
- 239000000463 material Substances 0.000 description 11
- 239000004094 surface-active agent Substances 0.000 description 8
- 230000000694 effects Effects 0.000 description 5
- 230000015556 catabolic process Effects 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 238000010521 absorption reaction Methods 0.000 description 2
- 230000009471 action Effects 0.000 description 2
- 238000002144 chemical decomposition reaction Methods 0.000 description 2
- 238000010494 dissociation reaction Methods 0.000 description 2
- 230000005593 dissociations Effects 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 238000005342 ion exchange Methods 0.000 description 2
- 230000001590 oxidative effect Effects 0.000 description 2
- 230000010287 polarization Effects 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- 208000027418 Wounds and injury Diseases 0.000 description 1
- 239000011149 active material Substances 0.000 description 1
- 238000004887 air purification Methods 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 230000008878 coupling Effects 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 239000010840 domestic wastewater Substances 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 239000003673 groundwater Substances 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 208000014674 injury Diseases 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000003134 recirculating effect Effects 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 239000002352 surface water Substances 0.000 description 1
- 230000004083 survival effect Effects 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D1/00—Flotation
- B03D1/14—Flotation machines
- B03D1/1431—Dissolved air flotation machines
-
- 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
- C02F1/24—Treatment of water, waste water, or sewage by flotation
-
- 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
-
- 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
-
- 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
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/727—Treatment of water, waste water, or sewage by oxidation using pure oxygen or oxygen rich gas
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F7/00—Aeration of stretches of water
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
- C02F2101/301—Detergents, surfactants
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- Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Mechanical Engineering (AREA)
- Biotechnology (AREA)
- Physical Water Treatments (AREA)
- Water Treatment By Electricity Or Magnetism (AREA)
- Treatment Of Water By Oxidation Or Reduction (AREA)
Abstract
본 고안은 가압부상 분해기에 관한 것으로, 특히 본 고안은 오폐수의 오염성분인 계면활성 성분이나 부유성 성분들을 강제분해부상시키어 수 표면에 집합하여 제거하므로 타 오염성분의 분해제거를 용이하게 하여 오폐수를 정화처리하는 도록한 가압부상 분해기에 관한 것이다.The present invention relates to a pressurized floatation decomposer, and in particular, the present invention forcibly decomposes and removes the surface active or floating components, which are pollutants of the wastewater, on the surface of the water to facilitate the decomposition and removal of other pollutants. It relates to a pressure flotation cracker for purification.
Description
본 고안은 가압부상 분해기에 관한 것으로, 특히 본 고안은 오폐수의 오염성분인 계면활성 성분이나 부유성 성분들을 강제분해부상시키어 수 표면에 집합하여 제거하므로 타 오염성분의 분해제거를 용이하게 하여 오폐수를 정화처리하는 도록한 가압부상 분해기에 관한 것이다.The present invention relates to a pressurized floatation decomposer, and in particular, the present invention forcibly decomposes and removes the surface active or floating components, which are pollutants of the wastewater, on the surface of the water to facilitate the decomposition and removal of other pollutants. It relates to a pressure flotation cracker for purification.
일반적으로 생활하수폐수나 산업폐수 등은 오염성분의 종류가 다양하고 또한 복잡하므로 그 성질이 분해 및 정화처리하는 데 매우 어려운 실정임은 이미 잘 알려진 사실이다.In general, it is well known that domestic wastewater and industrial wastewater have various kinds of contaminants and are complex, so that their properties are very difficult to decompose and purify.
그리고 오폐수는 사람의 생존 생활활동이나 산업활동으로 수중에 원하지 않는 오염성분 등이 포함됨으로써 발생하여 시간이 경과하면서 다시 화학적, 생물학적 변화가 상호간 일어나면서 더욱 복잡한 오염상태로 발전하고 있는 실정이다.In addition, wastewater is generated by the inclusion of unwanted pollutants in the water as human living activities or industrial activities. As time goes by, chemical and biological changes occur each other, and they are developing into a more complicated pollution state.
특히 현대인들이 제일 많이 다량으로 사용하고 있는 계면활성 성분들은 거의 대다수가 오폐수에 포함되어 배출되므로 정화처리가 매우 어렵게되는 것이다.In particular, since most of the surface active ingredients used in large quantities by modern people are contained in wastewater, the purification process becomes very difficult.
계면활성성분이나 고분자물질은 그 성질상 수중분해가 매우 곤란하여 제거가 극히 곤란한 것은 물론 다른 오염성분의 분해정화처리에도 결정적으로 방해하여 처리효율을 저하시키고 있다.Due to its nature, surfactants and polymers are very difficult to disintegrate in water, and are extremely difficult to remove, and deterministically interfere with decomposition and purification of other contaminants.
일반적으로 계면활성성분과 고분자성분은 그 분해가 곤란하거나 불가능하다고까지 판단될 정도로 어렵고 이는 분해처리가 곤란함으로 인해 크기가 매우 작은 오염성분이 계면활성성분에 포위, 희석 등의 상태로 포함되어 있는 경우에는 이의 처리도 매우 어렵게 되어 전체적으로 볼 때 오폐수 정화처리의 처리효율이 저하되므로 처리시간, 면적, 부피, 비용이 필요이상으로 대폭 증가하면서도 정화처리는 잘 되지 않는 것이다.In general, surfactants and polymers are difficult enough to be deemed difficult or impossible to decompose, which is difficult to decompose. In addition, its treatment is also very difficult, and as a whole, the treatment efficiency of wastewater purification treatment is lowered, so that the treatment time, area, volume, and cost increase significantly more than necessary, but the purification treatment is not good.
오폐수의 정화처리가 미흡한 상태에서 처리수를 방류할 시에는 지표수와 지하수의 오염을 일으킨다는 것은 곧 인간과 자연생물의 생존을 파괴한다는 사실은 이미 공지된 사실이고, 이에 오폐수의 정확한 정화처리는 필수불가결한 전제조건인 것이다.It is already known that the contamination of surface water and groundwater destroys the survival of humans and natural organisms when the treated water is discharged while the wastewater is not sufficiently treated. Therefore, accurate purification of wastewater is essential. It is an indispensable precondition.
오폐수 속에 절대 다량 포함된 계면활성 오염성분의 분해제거가 어느 정도냐에 따라 전체 오폐수 정화처리 효과를 좌우하게 되어 이의 해결이 시급하게 선결되어야만 오폐수의 정확한 정화처리가 되는 것이다.Depending on the degree of decomposition and removal of the surface-active contaminant contained in a large amount of wastewater, the overall wastewater purification treatment effect is influenced.
이와 같은 종래의 단점을 해결하기 본 고안은 초단파 파장이 진행시 만나는 성분에 초단파가 흡수되거나 통과되는 작용현상, 초단파의 공명현상과 공명 흡수작용 현상을 이용하여 물과 계면활성 성분의 분해 또는 타 오염성분과의 분해를 이루고 음이온산소 공기에 의해 분해된 계면활성 성분 및 기타 상기 과정중 같이 분해된 부유성 오염성분을 같이 부상시키어 수 표면에 포집시키면서 제거하도록 한 가압부상 분해기를 제공하는 것을 그 목적으로 한다.In order to solve the above disadvantages, the present invention uses a phenomenon in which microwaves are absorbed or passed through a component that meets the progress of microwave wavelengths, decomposition and other pollution of water and surfactant components using resonance and resonance absorption of microwaves. It is an object of the present invention to provide a pressurized flotation cracker which decomposes with the components and floats the surface-active component decomposed by anionic oxygen air and other floating contaminants decomposed during the above process and is collected on the water surface and removed. do.
상기와 같은 목적을 달성하기 위한 본 고안은 음이온산소 공기의 부상력으로 오폐수를 조성된 교번자장대(N : N 자장대, N : S 자장대)를 통과시키면서 N : N 극 자화와 N : S 극 자화가 이루어져 물과 큰물분자의 구조를 개선하고 활성화시키므로 오염성분과의 해리엔탈피가 높아지는 전처리를 수행함으로써 초단파에 의한 분해가 더욱 효과적이고 확실하게 이루어지도록 한다.The present invention for achieving the above object is the N: N pole magnetization and N: S while passing through the alternating magnetic field (N: N magnetic field, N: S magnetic field) to create the waste water by the floating force of the anionic oxygen air The polarization is performed to improve and activate the structure of water and large water molecules so that dissociation by microwaves can be more effectively and surely performed by performing pretreatment to increase dissociation enthalpy with contaminants.
그리고 교번자석과 영구자석의 사이에 일어나는 교번자석 극성교차에 따른 교번 자장대는 오폐수의 분해와 분해된 오염성분간의 결합을 이루면서 양 자석간의 인력과 반발력에 의해 초단파 진동판이 진동을 일으키도록 하며 초단파를 오폐수에 방출하여 대단한 속도와 힘으로 분해를 일으킨다.The alternating magnetic field according to the alternating magnet polarity crossing between the alternating magnet and the permanent magnet forms the coupling between the decomposed wastewater and the decomposed pollutants, causing the microwave diaphragm to vibrate by the attraction and repulsive force between the two magnets and the wastewater. Emissions occur at great speed and force to cause decomposition.
상기의 분해되는 오염성분과 계면활성제는 음이온산소 공기의 직접 반응과 자화 및 자화공명, 초단파파장 및 파장공명에 의하여 상호 상승작용을 일으키며 물질변화를 일으키어 재이온화나 수중 재융해가 일어나지 않도록 하여 오폐수를 정화처리하도록 한다.The pollutants and surfactants decomposed above generate synergism by direct reaction of anionic oxygen air and magnetization and magnetization resonance, ultra-short wavelength and wavelength resonance, and cause material change to prevent re-ionization or re-melting in the waste water. Purify.
이러한 오폐수 속의 계면활성제를 중점적으로 처리하므로 타 오염성분의 계면활성 성분으로 말미암은 수처리 효율 저하현상을 방지하고, 정교하며 정확한 수처리를 이루는 이러한 효과를 더욱 증진키 위해 처리수조의 오폐수를 공기물펌프에 의해 외부로 배수하면서 고전압의 전기에서 방전하는 음전자를 공기휠터를 통해 분진과 오염성분이 제거된 공기에 방전하여 음이온산소 공기를 생산하도록 한 후, 공기물펌프에서 오폐수와 희석하여 수조의 가압부상 분해기로 압송하여 폭기와 분사가 동시에 이루어지게 하므로 효과가 더욱 증진하는 작용을 회류에 의해 지속적으로 일으키게 한다.Since the surfactants in the wastewater are treated intensively, the wastewater in the treatment tank is prevented by the air water pump in order to prevent the degradation of water treatment efficiency caused by the surface active ingredients of other pollutants and to further enhance the effect of achieving precise and accurate water treatment. The negative electrons discharged from the high voltage electricity while draining to the outside are discharged to the air from which dust and contaminants have been removed through the air filter to produce anion oxygen air, and then diluted with waste water in an air water pump to pressurize the cracker in the tank. As the aeration and spraying are carried out at the same time, the effect is further enhanced by the continuous flow.
도1은 본 고안의 측단면도.1 is a side cross-sectional view of the present invention.
* 도면의 주요부분에 대한 부호의 설명 *Explanation of symbols on the main parts of the drawings
1 : 공기정화부 2 : 승압콘트롤부1: air purification unit 2: boost control unit
3 : 공기물펌프 4 : 공기물 희석드럼3: air water pump 4: air water dilution drum
5 : 상부 초단파 진동판 6 : 하부 초단파 진동판5: Upper Microwave Diaphragm 6: Lower Microwave Diaphragm
7 : 부유물질 배출관 8 : 침전물 배출관7: floating material discharge pipe 8: sediment discharge pipe
이하 본 고안을 첨부도면에 의거 상세히 기술하여 보면 다음과 같다.Hereinafter, the present invention will be described in detail with reference to the accompanying drawings.
정수처리하기 위해 오폐수 처리수조에 인입하여 충진시킨 오폐수는 공기물펌프(3)와 오수회류관(3b)를 통해 공기물 희석 펌핑실(3c)에 흡입되도록 하고,The wastewater introduced into and filled with the wastewater treatment tank for water treatment is sucked into the airwater dilution pumping chamber 3c through the airwater pump 3 and the wastewater return pipe 3b.
상기 공기물펌프(3)의 흡입력에 의해 공기공급관(3a)를 통하여 공기물펌프(3)로 이동하는 공기는 공기정화기(1)에 흡입되어 공기휠터(1a)에서 분진과 오염성분이 여과된 후, 승압 콘트롤부(2)에서 고전압으로 승압되어 음전자방전부(1b)에 의해 방전되는 음전자와 만나 반응하여 음이온산소 공기로 되어 공기물 희석 펌핑실(3c)에서 인입된 오폐수와 희석되도록 하고,Air moving to the air water pump 3 through the air supply pipe 3a by the suction force of the air water pump 3 is sucked into the air purifier 1 to filter dust and contaminants from the air filter 1a. Thereafter, the voltage is boosted to a high voltage in the boost control unit 2 and reacts with negative electrons discharged by the negative electron discharge unit 1b to react with the anion oxygen to dilute the waste water introduced in the air water dilution pumping chamber 3c. and,
상기의 공기와 희석된 오폐수는 공기물 희석 투입관(3d)으로 토출되면서 음이온산소군이 내부에 융해되고 착이온되어 용존산소량이 증가하여 이온상태나 융해상태의 오염성분을 산화시키면서 물질변화되도록 하고,The waste water diluted with the air is discharged into the air dilution inlet tube (3d), and the anion oxygen group is melted and ionized inside to increase the dissolved oxygen amount so that the material changes while oxidizing the pollutants in the ionic or molten state. ,
동시에 이온교환에 의한 화학적 분해집합으로 물과 오염성분의 분해와 오염성분간의 집합이 이루어지는 등의 정화작용을 일으키며 공기물 희석드럼(4)에 인입되어 일부는 기포와 함께 물공기 분사공(4b)으로 분사되면서 고압에서 저압으로의 급속한 전환으로 인한 분자간 결합엔달피의 파괴로 분해되도록 하고,At the same time, the chemical decomposition set by ion exchange causes the purification of water and pollutants and the collection of pollutants.They are introduced into the air dilution drum 4, and some of them are bubbled with air bubbles 4b. To break down due to the breakdown of intermolecular bonds due to rapid transition from high pressure to low pressure,
상기 기포중 일부는 물과 분리되어 공기집합실(4c)에 모여 음이온산소 공기폭기부(4a)에 의해 수중으로 폭기되어 오폐수처리 수조의 오폐수를 정화하고 분해된 계면활성성분과 부유성 오염성분을 부상시키어 수표면에 집합시키도록 하고,Some of the bubbles are separated from the water, gathered in the air collection chamber 4c and aerated in the water by the anion oxygen air aeration section 4a to purify the waste water of the wastewater treatment tank, and decompose the decomposed surfactant and floating contaminants. To float to the surface of the water,
물공기 분사공(4b)에서 분사되는 물과 음이온산소 공기의 기포는 분사력과 공기부상력에 의해 수조전체의 물과 함께 대류와 와류를 일으키면서 하부 초단파진동판(6)의 오폐수 통과공(6a)을 통해 자화 초단파 분해실로 인입되어 상부 초단파 진동판(5)에 장착된 영구자석(5a)과 하부 초단파 진동판(6)의 중앙에 부착된 교번자석(6b)과의 사이에 교번자석(6b)의 극성이 바뀜으로 인해 조성된 교번자장대와 진동형태의 인력과 반발력을 전달받는 상부 초단파 진동판(5)과 하부 초단파 진동판(6)들이 진동하여 초단파 파장을 내외로 방출하도록 하고,Bubbles of water and anionic oxygen air injected from the water-air injection hole 4b cause convection and vortex with the water of the entire tank by the injection force and the air floating force, and the wastewater passage hole 6a of the lower microwave vibration plate 6. The polarization of the alternating magnet 6b between the permanent magnet 5a and the alternating magnet 6b attached to the center of the lower microwave diaphragm 6 is introduced into the magnetization microwave decomposition chamber through Due to this change, the alternating magnetic field and the upper microwave diaphragm 5 and the lower microwave diaphragm 6, which receive the attraction force and repulsive force of the vibration type, vibrate to emit microwave wavelengths in and out,
상기의 초단파 파장은 외부의 오폐수를 자화공명과 초단파공명 작용으로 분해분리시키고 음이온산소공기에 의해 물질변화를 일으켜 계면활성성분과 부유성 오염성분은 수면부상하여 집합되고 비중이 높은 침전성 오염성분은 물질변화로 인한 오염복원화 현상이 없이 오폐수 처리수조 하단부로 침전집합되어 침전물 배출관(8)을 통해 배출되도록 하고,The microwave wavelength is separated from the external waste water by the magnetic resonance and the microwave resonance action, and the material changes by the anionic oxygen air, so that the surface active ingredient and the floating pollutant are collected by surface injury, and the high specific gravity sedimentary pollutant There is no pollution restoration caused by the change of material settles to the bottom of the waste water treatment tank to be discharged through the sediment discharge pipe (8),
자화 초단파 분해실로 인입되는 전처리된 오폐수는 교번자장대에 의한 자화 및 강력한 초단파에 의해 완전분해 되어 물질변화되며 반응수 통과공(5c)을 통해 기기 상부로 토출되면서 계면활성성분과 부유물질은 부상하여 부유물질 배출관(7)을 통해 외부로 배출시키고,The pretreated wastewater flowing into the magnetization microwave decomposition chamber is completely decomposed by magnetization by the alternating magnetic field and strong microwaves, and is changed into material. The surface active material and floating material are floated as it is discharged to the upper part through the reaction water passage hole (5c). Discharge to the outside through the suspended solids discharge pipe (7),
위와 같은 반응처리가 공기물펌프(3)의 구동에 의해 회류시키면서 지속적으로 반복처리되도록 하여 오폐수를 정화처리시키도록 한 것이다.The reaction treatment as described above is to continuously process while recirculating by driving the air water pump (3) to purify the waste water.
이와 같이 구성한 본 고안의 가압부상 분해기는 정수처리하기 위해 오폐수 처리수조에 인입하여 충진시킨 오폐수는 공기물펌프(3)와 오수회류관(3b)를 통해 공기물 희석펌핑실(3c)로 흡입된다.The pressurized floatation decomposer of the present invention configured as described above is introduced into and filled with a wastewater treatment tank for water purification, and the wastewater is sucked into the airwater dilution pumping chamber 3c through the airwater pump 3 and the wastewater return pipe 3b. .
상기 공기물펌프(3)의 흡입력에 의해 공기공급관(3a)를 통하여 공기 물펌프(3)로 이동하는 공기는 외부로부터 공기정화기(1)에 흡입되어 공기휠터(1a)에서 분진과 오염성분이 여과되고 승압 콘트롤부(2)에서 승압된 고전압이 공급되는 음전자 방전부(1b)에서 방전되는 음전자와 만나 반응하여 음이온산소 공기로 된 후 공기물 희석 펌핑실(3c)로 이동하여 오수회류관(3b)을 통해 인입된 오폐수와 희석된다.Air moving to the air water pump (3) through the air supply pipe (3a) by the suction force of the air water pump (3) is sucked into the air purifier (1) from the outside, the dust and contaminants in the air filter (1a) It reacts with the negative electrons discharged from the negative electron discharge unit 1b supplied with the high voltage, which is filtered and boosted by the boosting control unit 2, becomes anion oxygen air, and then moves to the air water dilution pumping chamber 3c to carry out sewage flow. It is diluted with the wastewater introduced through the tube 3b.
상기의 음이온산소 공기와 희석된 오폐수는 공기물 희석 투입관(3d)으로 토출되면서 음이온산소 군이 내부에 융해되고 착이온되어 용존산소량이 증가하여 이온상태나 융해상태의 오염성분을 산화시키면서 물질이 변화되도록 한다.The anion oxygen air and the diluted waste water are discharged into the air dilution inlet tube 3d, and the anion oxygen group melts and is ionized to increase the dissolved oxygen, thereby oxidizing the pollutants in the ionic or molten state. To change.
그리고 이온교환에 의한 화학적 분해집합으로 물과 오염성분의 분해와 오염성분간의 집합이 이루어지는 등의 정화작용을 일으키며 공기물 희석드럼(4)에 인입되어 일부는 기포와 함께 물공기 분사공(4b)으로 분사되면서 고압에서 저압으로의 급속한 전환으로 인한 분자간 결합엔달피의 파괴로 물에 포함된 오염성분이 분해되도록 한다.The chemical decomposition set by ion exchange causes the purification of water and pollutants and the collection of pollutants.They are introduced into the air dilution drum 4, and some of them are bubbled with air bubbles 4b. As it is sprayed on, it breaks down the contaminant contained in water due to the breakdown of intermolecular bonds due to the rapid conversion from high pressure to low pressure.
상기 기포중 일부는 물과 분리되어 공기집합실(4c)에 모여 음이온산소 공기폭기부(4a)에 의해 수중으로 폭기되어 오폐수처리 수조의 오폐수를 정화하고 분해된 계면활성 성분과 부유성 오염성분을 부상시키어 수표면에 집합시킨다 .Some of the bubbles are separated from the water and gathered in the air collection chamber 4c and aerated in the water by the anion oxygen air aeration section 4a to purify the waste water of the wastewater treatment tank and remove the decomposed surfactant and floating contaminants. Float and collect on the surface of the water.
물공기 분사공(4b)에서 분사되는 물과 음이온산소 공기의 기포는 분사력과 공기부상력에 의해 수조 전체의 물과 함께 대류와 와류를 일으키면서 하부 초단파 진동판(6)의 오폐수 통과공(6a)을 통해 자화 초단파 분해실로 인입된다.Bubbles of water and anionic oxygen air injected from the water-air injection hole 4b cause convection and vortex with the water of the entire tank by the injection force and the air floating force, and the wastewater passage hole 6a of the lower microwave diaphragm 6. Is introduced into the magnetization microwave decomposition chamber.
초단파 분해실의 상부 초단파 진동판(5)에 장착된 영구자석(5a)과 하부 초단파 진동판(6)의 중앙에 부착된 교번자석(6b)과의 사이에는 교번자석(6b)의 극성이 빈번하게 바뀜으로 인해 조성된 교번자장대와 진동형태의 인력과 반발력이 발생하여 이를 전달받는 상부 초단파 진동판(5)과 하부 초단파 진동판(6)들이 진동하여 초단파 파장을 내외로 방출하게 된다The polarity of the alternating magnet 6b frequently changes between the permanent magnet 5a mounted on the upper microwave diaphragm 5 of the microwave disassembly chamber and the alternating magnet 6b attached to the center of the lower microwave diaphragm 6. Due to the alternating magnetic field generated by the alternating magnetic field and the vibration-like attraction and repulsive force is generated, the upper microwave diaphragm 5 and the lower microwave diaphragm 6 receiving the vibration vibrate to emit microwave wavelengths in and out.
상기의 초단파 파장은 외부의 오폐수에 포함된 오염성분을 자화공명과 초단파공명 작용으로 분해분리시키면서 음이온산소공기에 의해 물질변화를 일으켜 계면활성성분과 부유성 오염성분은 수면으로 부상하여 집합되고, 비중이 높은 침전성 오염성분은 물질변화로 인한 오염복원화 현상이 없이 오폐수 처리수조 하단부로 침전집합되어 침전물 배출관(8)을 통해 배출되도록 한다.The microwave wavelength causes the change of the pollutant contained in the external waste water by the magnetic resonance and microwave resonance action, causing material change by the anionic oxygen air, and the surface active ingredient and the floating pollutant are collected by rising to the surface, and the specific gravity This high sedimentary pollutant is collected and discharged through the sediment discharge pipe 8 at the bottom of the wastewater treatment tank without contaminant restoration due to material change.
자화 초단파 분해실로 인입되는 전처리된 오폐수는 교번자장대에 의한 자화및 강력한 초단파에 의해 완전히 분해되어 물질변화되며 반응수 통과공(5c)을 통해 내부의 상부로 토출되면서 계면활성성분과 부유물질은 부상하여 부유물질 배출관(7)을 통해 외부로 배출시킨다.The pretreated wastewater introduced into the magnetization microwave decomposition chamber is completely decomposed by magnetization by the alternating magnetic field and strong microwaves and is changed into substances. The surface active ingredient and floating material are injured by being discharged to the upper part through the reaction water passage hole (5c). To discharge to the outside through the floating material discharge pipe (7).
위와 같은 반응처리가 공기물펌프(3)의 구동에 의해 회류되면서 지속적으로 복본처리되어 오폐수를 정화처리시키는 것이다.As the reaction treatment as described above is circulated by the driving of the air water pump (3) is continuously duplicated to purify the waste water.
또한 수중계면활성성분의 제거는 이후 여타의 물리적처리, 화학적처리, 생물화학적처리 시에도 계면활성성분의 난해한 방해를 받지 않게 되므로 정확하고 용이한 고효과의 수처리가 이루어지게 됨을 알 수 있다.In addition, the removal of the water-based surface active ingredient is not affected by the difficult disturbance of the surface active ingredient even during other physical treatment, chemical treatment, and biochemical treatment, it can be seen that the high-efficiency water treatment is made easy and accurate.
따라서 본 고안의 가압부상 분해기는 초단파 파장이 진행시 만나는 오염성분에 초단파가 흡수되거나 통과되는 작용현상, 초단파의 공명현상 및 공명 흡수작용 현상을 이용하여 물과 계면활성 성분의 분해 또는 타 오염성분과의 분해를 이루고 음이온산소 공기에 의해 분해된 계면활성 성분 및 기타 상기 과정중 같이 분해된 부유성 오염성분을 같이 부상시키어 수 표면에 포집시키면서 제거하도록 한 것이다.Therefore, the pressure flotation decomposition device of the present invention utilizes a phenomenon in which microwaves are absorbed or passed through the contaminants encountered when the microwave wavelength progresses, resonant phenomena and resonance absorption phenomena of the water and the surfactant, In order to decompose and surface-active components decomposed by anionic oxygen air and other floating contaminants decomposed during the above-mentioned process, they are floated together and collected while being collected on the surface of water.
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