KR100493636B1 - A direct water purifying method and apparatus using depth plant pressure floation in the sea, lakes and rivers - Google Patents

A direct water purifying method and apparatus using depth plant pressure floation in the sea, lakes and rivers Download PDF

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KR100493636B1
KR100493636B1 KR10-2002-0036730A KR20020036730A KR100493636B1 KR 100493636 B1 KR100493636 B1 KR 100493636B1 KR 20020036730 A KR20020036730 A KR 20020036730A KR 100493636 B1 KR100493636 B1 KR 100493636B1
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water
deep
injection
depth
pressurized
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KR20040001512A (en
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박경북
윤주열
명규남
김종수
조항문
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주식회사 에스디알앤디
(주)그린하이테코
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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/24Treatment of water, waste water, or sewage by flotation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20Mixing gases with liquids
    • B01F23/23Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F7/00Aeration of stretches of water
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/007Contaminated open waterways, rivers, lakes or ponds
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/08Seawater, e.g. for desalination

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  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
  • Physical Water Treatments (AREA)

Abstract

가. 청구범위에 기재된 발명이 속하는 기술분야.end. The technical field to which the invention described in the claims belongs.

본 발명은 대심도 가압부상공법을 이용한 수심이 깊은 바다, 호소, 하천 등의 직접 수질정화방법 및 장치에 관한 것으로, 특히, 가압수를 적은 에너지 비용으로 제조할 수 있도록 함과 동시에 처리시간을 단축시킬 수 있도록 한 것이 특징이다.The present invention relates to a direct water purification method and apparatus for deep seas, lakes, rivers, etc. using a large depth pressurization method, and in particular, it is possible to manufacture pressurized water at a low energy cost and at the same time reduce the treatment time. The feature is that it can be made.

나. 발명이 해결하려는 기술적 과제.I. The technical problem to be solved by the invention.

종래에 가압부상공법에 의한 수질정화방법은 수 기압의 고압 상태로 유지되는 고압탱크에서 물과 공기를 혼합시켜 공기를 과포화 상태로 용해시킨 가압수를 사용하였기 때문에 가압수 제조를 위한 고가의 장비와 에너지 비용이 많이 소요되는 문제점이 있었다.Conventionally, the water purification method using the pressure flotation method uses expensive water for mixing pressurized water by mixing water and air in a high pressure tank maintained at a high pressure of water pressure and dissolving the air in a supersaturated state. There was a problem of high energy costs.

특히 수심이 매우 깊은 곳에서는 미세기포가 상승하면서 크기가 작아져 부상속도가 느려지기 때문에 처리시간이 오래 소요될 뿐 아니라 공기의 용해도가 증가되어 이를 고려한 양의 가압수를 공급시켜야 하기 때문에 이에 따른 에너지 소모량은 더욱 증가되는 것이다.Particularly in the deep water depth, as the microbubble rises, the size decreases and the floating speed slows down, it takes not only long processing time but also the increase of the solubility of the air and the amount of pressurized water to be taken into account. Is further increased.

다. 발명의 해결방법의 요지All. Summary of Solution of the Invention

본 발명은 낮은 압력으로 물과 공기를 혼합시켜 제조한 가압수를 심층하향관을 통하여 수심 깊은 곳으로 주입시켜 수압에 의해 형성된 고압 효과로 많은 양의 가압수를 단시간에 주입시키고, 심층하향관의 내부 또는 외부에서 수심의 깊이에 따라 다단으로 분사수를 주입시켜 수심이 깊은 곳에서의 기포 용해방지 및 기포의 상승 속도를 증가시켜 현장 가압부상공법에 의한 직접 수질정화작업 시 소요되는 비용을 최소화할 수 있도록 함과 동시에 처리시간을 단축시켜 깊은 곳에서의 효율적인 수질정화가 가능토록 한 것이다.The present invention injects the pressurized water prepared by mixing water and air at a low pressure to the depth deep through the deep down pipe and injects a large amount of pressurized water in a short time by the high pressure effect formed by the water pressure, By spraying the spray water in multiple stages according to the depth of the water from the inside or the outside, it is possible to minimize the cost of direct water purification by on-site pressurization method by preventing bubble dissolution and increasing the rate of bubble rise in the deep water. In addition to this, the treatment time can be shortened and efficient water purification can be performed in deep water.

라. 발명의 중요한 용도.la. Important use of the invention.

바다, 호소, 하천등에서의 깊은 곳에서의 수질정화.Water purification at depth from the sea, appeal, river.

Description

대심도 가압부상공법을 이용한 수심이 깊은 바다, 호소, 하천에서의 직접수질정화방법 및 장치{A direct water purifying method and apparatus using depth plant pressure floation in the sea, lakes and rivers}Direct water purifying method and apparatus using depth plant pressure floation in the sea, lakes and rivers}

본 발명은 대심도 가압부상공법을 이용한 수심이 깊은 바다, 호소, 하천 등의 직접 수질정화방법 및 장치에 관한 것으로, 통상의 가압부상공법보다 낮은 압력으로물과 공기를 혼합시킨 가압수를 심층하향관을 통해 깊은 곳으로 보내어 수압에 의해 형성된 압력으로 많은 양의 가압수를 적은 에너지 비용으로 제조할 수 있어 기존의 가압부상공법보다 수질정화비용을 줄일 수 있도록 한 것이다.The present invention relates to a direct water purification method and apparatus for deep seas, lakes, rivers, etc. using a large-depth pressurized floatation method, and deeply pressurized water mixed with water and air at a lower pressure than a conventional pressurized floatation method. It is possible to manufacture a large amount of pressurized water at a low energy cost through the pressure formed by the water pressure through the pipe to reduce the water purification cost than the conventional pressurization buoyancy method.

종래의 현장 가압부상공법에 의한 수질정화방법은 물론 함께 공기를 수 기압의 고압탱크에서 혼합시켜 공기를 과포화 상태로 용해시킨 가압수를 오염된 물 속에 분사시킬 때 생성되는 미세기포가 오염물질에 부착되면서 오염물질과 함께 수면위로 부상되도록 하여 제거하는 방법으로, 가압수 제조공정에 있어서 고압펌프, 고압탱크, 고압공기압축기 등 고가의 장비와 고압을 유지하기 위한 에너지 비용이 많이 소요되는 문제점이 있었다.As well as the conventional water purification method by the on-site pressurization flotation method, the fine bubbles generated when mixing the air in a high pressure tank of water pressure and spraying the pressurized water dissolved in the supersaturated state into the contaminated water adhere to the contaminants. As a method of removing by floating on the water along with the contaminants, there was a problem that the high cost of high-pressure pumps, high-pressure tanks, high-pressure air compressors and energy costs to maintain high pressure in the pressurized water manufacturing process.

또한 미세기포가 적정 크기를 유지하여야 오염물질에 효율적으로 부착되고 적절한 부상속도를 유지할 수 있는 것이나, 수중에서 가압수 분사시 발생되는 미세기포는 수면으로부터 깊은 곳에서 분사될수록 기포의 크기가 작아지게 되어 부상속도가 매우 느려 작업효율이 극도로 저하되기 때문에 수심이 깊은 곳에서의 현장 가압부상공법을 이용한 수질정화효과가 실제적으로 매우 어려울 수밖에 없는 것이었다.In addition, microbubbles should be maintained at the proper size to effectively attach to contaminants and maintain proper floating speed.However, microbubbles generated during the injection of pressurized water in water become smaller as they are injected deeper from the surface of the water. As the floating speed is very slow, the work efficiency is extremely low, and the water purification effect using the field press flotation method in the depth of water is actually very difficult.

즉, 수심 Dm인 지점에서의 압력은(1+D/10)기압이 되므로 표층에서보다 공기의 용해도가(1+D/10)배로 증가하는 반면 기포크기는 1/(1+D/10)으로 줄어들기 때문이다.That is, the pressure at the depth Dm becomes (1 + D / 10) air pressure, so that the solubility of air increases by (1 + D / 10) times than at the surface layer, while the bubble size is 1 / (1 + D / 10). Because it decreases.

예를 들어 수심이 50m인 지점에서 분사할 경우, 그 지점에서의 용존공기(용존산소와 용존질소)의 농도가 포화상태라 하더라도 표층에서 분사된 기포의 1/6밖에 되지 않아 부상속도가 매우 느리게 되는 것이다. For example, when spraying at a depth of 50m, even if the concentration of dissolved air (dissolved oxygen and dissolved nitrogen) at that point is saturated, only 1/6 of the bubbles injected from the surface layer is very slow. Will be.

뿐만 아니라 오염된 수역의 심층부에서는 용존산소가 거의 없어 혐기성으로 유지되기 때문에 강바수 분사 시 형성된 미세기포의 대부분이 물속으로 용해됨으로써 기포의 크기는 더욱 작아질 뿐 만 아니라, 온도도 낮아 기체 용해도도 증가되기 때문에 적정 A/S(Air PER Solid Patio)를 유지하면 훨씬 많은 양의 공기와 가압수를 공급하여야 하기 때문에 에너지 비용이 많이 들고 작업효율도 저하되는 문제점이 있는 것이다.In addition, in the deep part of the contaminated water, there is little dissolved oxygen and remains anaerobic, so that most of the micro bubbles formed during the spraying of the river water are dissolved in water, which not only reduces the size of the bubble but also increases the gas solubility due to the low temperature. Therefore, if you maintain an appropriate A / S (Air PER Solid Patio), because much air and pressurized water must be supplied, there is a problem in that energy costs are high and work efficiency is also lowered.

따라서 본 발명은 상기한 종래의 문제점을 해결하기 위하여 안출한 것으로서, 본 발명의 목적은 현장 가압부상공업에 의한 직접 수질정화작업 시 소요되는 비용을 최소화할수 있도록 함과 동시에 처리시간을 단축시켜 깊은 곳에서의 효율적인 수질정화가 가능토록 하고자 함이다.Therefore, the present invention has been made in order to solve the above-mentioned conventional problems, the object of the present invention is to minimize the cost required for the direct water purification work by on-site pressurized flotation industry and at the same time to shorten the processing time deep It is intended to enable efficient water purification in Korea.

이를 위한 수질정화방법으로서, 낮은 압력으로 물과 공기를 혼합시켜 제조한 가압수를 심층하향관을 통하여 수심 깊은 곳으로 주입시켜 수압에 의해 형성된 고압 효과로 많은 양의 가압수를 단시간에 주입시킬 수 있도록 하였으며, 심층하향관의 내부 또는 외부에서 수심의 깊이에 따라 다단으로 분사수를 주입시켜 수심이 깊은 곳에서의 기포 용해방지 및 기포의 상승속도를 증가시킬 수 있도록 한 것이다.As a water purification method for this purpose, the pressurized water prepared by mixing water and air at low pressure can be injected into the depth through the deep down pipe, and a large amount of pressurized water can be injected in a short time by the high pressure effect formed by the water pressure. The injection water is injected into the multi-stage according to the depth of the water from the inside or the outside of the deep down pipe to prevent bubble dissolution and increase the rate of bubble rise in the deep water.

본 발명의 수심이 깊은 바다, 호소 , 하천등의 처리수역을 가압부상공법을 이용하여 수질을 효과적으로 정화시키는 방법이다.It is a method for effectively purifying water quality by using a pressurized flotation method in a deep sea, an appeal, a river, etc. of the present invention.

이하 다음의 실시예에 의하여 본 발명은 보다 상세히 설명하기로 한다. Hereinafter, the present invention will be described in more detail with reference to the following examples.

우선, 도 1은 본 발명의 일 실시예를 도시한 것으로, 처리대상수역의 지표면으로부터 수중으로 심층하향관(10)을 설치하고, 심층하향관(10)의 내부에 수심에 따라 관경을 변화시킨 증식 확장형 가압수 주입관(20)을 설치하여 통상의 가압부상공법에서 보다 낮은 압력으로 물, 공기, 약품을 혼삽시켜 제조한 가압수(1)를 주입시키고, 가압수 주입관(20)의 외주면으로 수심의 깊이에 따라 분사사 주입노즐(31)이 다단으로 설치된 분사수 주입관(30)을 설치하여 분사수(2)가 주입토록 하여 상기 심층하향관(10)내부에서 가압부상공법을 이용한 수질정화가 이루어지도록 한것이다.First, FIG. 1 illustrates an embodiment of the present invention, in which a deep down pipe 10 is installed underwater from the ground surface of a water to be treated, and the diameter of the deep down pipe 10 is changed according to the depth of water. Proliferation expansion type pressurized water inlet tube 20 is installed to inject pressurized water 1 prepared by mixing water, air, and chemicals at a lower pressure than in a normal pressurization method, and an outer peripheral surface of the pressurized water inlet tube 20 According to the depth of the water injection nozzle injection nozzle 31 is installed in a multi-stage injection water injection pipe 30 is installed so that the injection water (2) is injected to the inside of the deep down pipe (10) using a pressurized buoyancy method Water purification is to be done.

이때 상기 가압수 주입관(20)을 수심에 따라 증식 확장형으로 형성시키는 이유는 관경이 변화되는 지점에서의 압력변화에 따른 가압수의 교란작용이 증대되어 물 속에 용존된 공기가 기포로 쉽게 생성되기 때문에 수심이 깊은 경우에도 적은 에너지 비용으로 많은 양의 기포를 생성시킬 수 있기 때문이다.At this time, the reason for forming the pressurized water inlet tube 20 into the expansion type according to the depth is that the disturbance action of the pressurized water according to the pressure change at the point where the diameter of the pipe is changed, so that the air dissolved in the water is easily generated as bubbles. This is because even in deep water, a large amount of bubbles can be generated at a low energy cost.

또한, 교란작용에 의한 기포에 전하, 친수성과 소수성, 응집반응 등의 기능성기를 부여하기 쉽다.Moreover, it is easy to give functional groups, such as an electric charge, hydrophilicity, hydrophobicity, and aggregation reaction, to the bubble by a disturbing action.

또한 상기 가압수 주입부(11)의 외주면으로 분사수 주입노즐(31)을 수심별로 다단계 설치한 이유는 분사수 주입노즐(31)을 통하여 분사되는 분사수의 상승기류에 의하여 수중에서 가압수가 노출되는 순간 생성되는 미세기포의 부상속도를 증가시켜 처리시간을 단축시킬 수 있기 때문이다.In addition, the reason why the spray water injection nozzles 31 are installed in multiple stages on the outer circumferential surface of the pressurized water injection unit 11 is that the pressurized water is exposed in the water by the rising airflow of the sprayed water sprayed through the spray water injection nozzles 31. This is because the processing time can be shortened by increasing the floating speed of the generated microbubbles.

또한, 기포의 상승속도가 늦으면 수면위로 올라올 때 압력변화에 따라 미세기포가 대기포로 전환되어 응집물과의 부착현상이 깨져 처리효율의 저하를 불러오는데, 분사수로 메시기포가 대기포로 전환되기 때문에 전에 수면위로 부상시켜 처리효율의 저하를 방지할 수 있기 때문이다.In addition, when the rising speed of the bubble is slow, the fine bubbles are converted into the air bubble as the pressure changes when it rises on the water surface, and the adhesion phenomenon with the aggregates is broken, resulting in a decrease in the treatment efficiency. This is because it can prevent the fall of treatment efficiency by floating above the water surface.

이때 수 표면으로 부상된 부상물은 별도로 마련된 흡입장치(40)로 흡입시켜 탈수장치(50)에 의하여 탈수시켜 제거하는 것으로, 가압부상공법에서의 통상적인 부상물의 처리방법이고, 가압수(1)에는 압축기(60)로부터 공급되는 압축공기와 약품탱크(60)로부터 공급되는 약품이 포함되어 약품에 의한 응집반응과 압축공기에 의한 산소의 주입이 가능토록 함은 물론이다.At this time, the wounded to the surface of the water is sucked by a separate suction device 40 provided to dehydrate by the dehydration device 50 is removed, it is a conventional method of treatment of the wound in the buoyancy method, pressurized water (1) The compressed air supplied from the compressor (60) and the medicine supplied from the chemical tank (60) is included to enable the coagulation reaction by the chemical and the injection of oxygen by the compressed air, of course.

또한 가압수(1)와 분사수(2)에 사용되는 물은 처리수역의 물을 사용하는 것이다.In addition, the water used for the pressurized water 1 and the injection water 2 uses the water of a treated water area.

도 2는 본 발명의 또 다른 실시예를 도시한 것으로, 상기 분사수 주입관(30)을 심층하향관(10)의 외측에 설치하여 심층하향관(10)의 외부에서 가압부상공법에 의한 수질정화가 이루어지도록 하는 방법으로, 이때 가압수 주입관(20)을 통하여 심층부까지 주입된 가압수(1)는 심층하향관(10)의 외측으로 상승되어 외측에 다단으로 설치된 분사수 주입관(30)을 통하여 발생되는 분사수(2)와 접촉하게 되는 것이다.Figure 2 shows another embodiment of the present invention, the injection water injection pipe 30 is installed on the outside of the deep down pipe 10, the water quality by the pressure buoyancy method from the outside of the deep down pipe 10 In this way, the purification is made, the pressurized water 1 injected to the deep portion through the pressurized water injection pipe 20 is raised to the outside of the deep down pipe 10 is installed in multiple stages injection water injection pipe 30 Contact with the injection water (2) generated through the).

이 방법에 있어서, 분사수 주입노즐(31)은 수표면으로 올라갈수록 가압수(10)에 의하여 생성된 미세기포가 상승하면서 수표면으로 올라갈수록 처리수역의 넓은 영역으로 확산되는 것을 감안하여 수표면으로 올라갈수록 반경이 넓게 형성시키는 것이 바람직하다.In this method, the injection water injection nozzle 31 takes into consideration that the fine bubbles generated by the pressurized water 10 rises as they rise to the water surface, and diffuses to a large area of the treated water as they rise to the water surface. It is preferable to form a wider radius as it goes up.

도 3은 본 발명의 제 3실시예를 도시한 것으로, 상기 가압수 주입관(20)을 심층하향관(10)의 내부에 다수개 형성시켜 모듈형으로 형성시킬 수 있는 것으로, 이러한 방식은 넓은 처리수역을 한꺼번에 처리할 경우에 용이하게 적용할 수 있는 방법이다.Figure 3 shows a third embodiment of the present invention, a plurality of the pressurized water inlet pipe 20 can be formed in the interior of the deep down pipe 10 can be formed in a modular form, this manner is wide It is a method that can be easily applied when treating treated water at once.

따라서 상기와 같이 구성된 본 발명은 낮은 압력으로 물과 공기를 혼합시켜 제조한 가압수(1)를 심층하향관(10)을 통하여 수심깊은 곳까지 주입시킴으로서 수압에 의해 형성된 고압 효과로 많은 양의 가압수를 단시간에 주입시킬 수 있는 것이고, 심층하향관(10)의 내부 또는 외부에 수심의 깊이에 따라 분사수 주입노즐(31)이 다단으로 형성된 분사수 주입관(20)이 설치되어 이 분사수(2)에 의한 수심이 깊은 곳에서의 기포 용해방지 및 기포의 상승 속도를 증가시킬 수 있는것이다.Therefore, the present invention configured as described above is a large amount of pressurization by the high pressure effect formed by the water pressure by injecting the pressurized water (1) prepared by mixing water and air at a low pressure to the depth deep through the deep down pipe (10) The water can be injected in a short time, and the injection water injection pipe 20 in which the injection water injection nozzle 31 is formed in multiple stages is installed inside or outside the deep down pipe 10 according to the depth of the water. It is possible to prevent bubble dissolution and increase the rate of bubble rise in the deep water by (2).

본 발명에 의하면, 종래의 현장 가압부상공법에 의한 수질정화작업 시 가압시 주입을 위하여 소요되는 에너지 비용을 대폭 절감할 수 있음과 동시에 발생되는 미세기포의 상승속도를 증가시켜 처리시간을 단축시켜 깊은 곳에서의 효율적인 수질정화가 가능하게 되는 것이다.According to the present invention, it is possible to drastically reduce the energy cost required for injection during pressurization during the water purification work by the conventional on-site pressurization method and at the same time increase the rate of rise of the microbubbles generated to shorten the treatment time and increase the depth. Efficient water purification will be possible here.

도 1은 본 발명의 일 실시예에 따른 처리공정도.1 is a process chart according to an embodiment of the present invention.

도 2는 본 발명의 또 다른 실시예를 나타낸 처리공정도.Figure 2 is a process chart showing another embodiment of the present invention.

도 3은 본 발명의 제3실시예를 나타낸 처리공정도.3 is a process flowchart showing a third embodiment of the present invention.

<도면의주요부분에대한부호의설명>Explanation of symbols on the main parts of the drawing

1 : 가압수 2 : 분사수1: pressurized water 2: sprayed water

10 : 심층하양관 20 : 가압수 주입관10: deep deep pipe 20: pressurized water injection pipe

30 : 분사수 주입관 40 : 흡입장치30: injection water injection pipe 40: suction device

50 : 탈수장치 60 : 약품탱크50: dehydration device 60: chemical tank

Claims (3)

처리대상수역의 지표면으로부터 수중으로 심층하향관(10)을 설치하고, 심층하향관(10)의 내부에 증식 확장형 가압수 주입관(20)을 설치하여 통상의 가압부상공법에서 보다 낮은 압력으로 가압수(1)을 주입시키고, 가압수 주입관(20)의 외주면으로 수심에 따라 분사수 주입노즐(31)이 다단으로 설치돤 분사수 주입관(30)을 설치하여 분사수(2)가 주입토록 함으로서, 심층하향관(10) 내부에서 가압수(1)로부터 생성된 미세기포와 분사수(2)가 상승되면서 가압부상공법을 이용한 수질정화가 이루어지도록 함을 특징으로 하는 대심도 가압부상공법을 이용한 수심이 깊은 해양, 호소, 하천에서의 직접수질정화방법.The deep down pipe 10 is installed in the water from the ground surface of the water to be treated, and the proliferation expansion type pressurized water inlet pipe 20 is installed inside the deep down pipe 10 to pressurize at a lower pressure than in the normal pressure flotation method. Water (1) is injected into the outer peripheral surface of the pressurized water injection pipe (20) and the injection water injection nozzle (31) is installed in multiple stages according to the depth of the water, the injection water injection pipe (30) is installed and the injection water (2) is injected As a result, the deep bubble pressurization method is characterized in that the fine water generated from the pressurized water (1) and the injection water (2) in the deep down pipe (10) is raised to achieve water purification using the pressurization buoyancy method. Direct water purification method in deep ocean, lake and river. 처리대상수역의 지표면으로부터 수중으로 심층하향관(10)을 설치하고, 심층하향관(10)의 내부에 증식 확장형 가압수 주입관(20)을 설치하여 통상의 가압부상공법에서 보다 낮은 압력으로 가압수(1)를 주입시키고, 심층하향관(10)의 외측에 수심에 따라 분사수 주입노즐(31)이 다단으로 설치된 분사수 주입관(30)을 설치하여 분사수(2)가 주입토록 함으로서, 심층하향관(10)의 외부로 가압수(1)가 배출되어 생성된 미세기포와 분사수(2)가 상승되면서 가압부상공법에 의한 수질정화가 이루어지도록 함을 특징으로 하는 대심도 가압부상공법을 이용한 수심이 깊은 해양, 호소, 하천에서의 직접수질정화방법.The deep down pipe 10 is installed in the water from the ground surface of the water to be treated, and the proliferation expansion type pressurized water inlet pipe 20 is installed inside the deep down pipe 10 to pressurize at a lower pressure than in the normal pressure flotation method. By injecting water (1), the injection water injection pipe (30) provided with the injection water injection nozzle (31) in multiple stages in accordance with the water depth on the outer side of the deep down pipe (10) to inject the injection water (2) , Pressurized water buoyancy method characterized in that the water quality is purified by the pressure buoyancy method as the pressurized water (1) is discharged to the outside of the deep down pipe (10) is raised and the injection water (2) is raised Direct water purification method in deep ocean, lake and river using 제1항에 있어서, 상기 가압수 주입관(20)을 다수개 설치하여 모듈형으로 형성시킴을 특징으로 하는 대심도 가압부상공법을 이용한 수심이 깊은 해양, 호소, 하천에서의 직접수질정화방법.The method of claim 1, wherein a plurality of the pressurized water injection pipes (20) are installed and formed in a modular form.
KR10-2002-0036730A 2002-06-28 2002-06-28 A direct water purifying method and apparatus using depth plant pressure floation in the sea, lakes and rivers KR100493636B1 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0970504A (en) * 1995-09-04 1997-03-18 Hiroyuki Nagasaki Method for recovering sludge scum and device therefor
KR19980069218A (en) * 1997-02-27 1998-10-26 최동민 Pressurized Flotation Cracker
KR20010062914A (en) * 1999-12-21 2001-07-09 이종경 A removal system of deposit in rivers used an inhaler
JP2001279707A (en) * 2000-03-31 2001-10-10 Shimonoseki Ichi Sludge removing system
KR200242302Y1 (en) * 2001-04-19 2001-10-11 김한규 Sludge cart using water jet

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0970504A (en) * 1995-09-04 1997-03-18 Hiroyuki Nagasaki Method for recovering sludge scum and device therefor
KR19980069218A (en) * 1997-02-27 1998-10-26 최동민 Pressurized Flotation Cracker
KR20010062914A (en) * 1999-12-21 2001-07-09 이종경 A removal system of deposit in rivers used an inhaler
JP2001279707A (en) * 2000-03-31 2001-10-10 Shimonoseki Ichi Sludge removing system
KR200242302Y1 (en) * 2001-04-19 2001-10-11 김한규 Sludge cart using water jet

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