KR101003705B1 - Apparatus for disposing waste water - Google Patents

Apparatus for disposing waste water Download PDF

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KR101003705B1
KR101003705B1 KR20100041132A KR20100041132A KR101003705B1 KR 101003705 B1 KR101003705 B1 KR 101003705B1 KR 20100041132 A KR20100041132 A KR 20100041132A KR 20100041132 A KR20100041132 A KR 20100041132A KR 101003705 B1 KR101003705 B1 KR 101003705B1
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South Korea
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tank
waste water
water tank
water distribution
aerobic microbial
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KR20100041132A
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Korean (ko)
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정관선
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주식회사 우빈기술개발
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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
    • C02F3/00—Biological treatment of water, waste water, or sewage
    • C02F3/30—Aerobic and anaerobic processes
    • C02F3/302—Nitrification and denitrification treatment
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00—Biological treatment of water, waste water, or sewage
    • C02F3/02—Aerobic processes
    • C02F3/10—Packings; Fillings; Grids
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00—Biological treatment of water, waste water, or sewage
    • C02F3/02—Aerobic processes
    • C02F3/12—Activated sludge processes
    • C02F3/24—Activated sludge processes using free-fall aeration or spraying
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00—Biological treatment of water, waste water, or sewage
    • C02F3/30—Aerobic and anaerobic processes
    • C02F3/308—Biological phosphorus removal
    • 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
    • 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
    • Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00—Technologies for wastewater treatment
    • Y02W10/10—Biological treatment of water, waste water, or sewage

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  • Life Sciences & Earth Sciences (AREA)
  • Biodiversity & Conservation Biology (AREA)
  • Microbiology (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Molecular Biology (AREA)
  • Biological Treatment Of Waste Water (AREA)
  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)

Abstract

PURPOSE: A multistage structured wastewater treatment apparatus using the potential energy is provided to effectively purify waste water by successively and repetitively forming an aerobic microbial carrier an anaerobic microbial carrier effective for different pollutants. CONSTITUTION: A multistage structured wastewater treatment apparatus using the potential energy comprises an outer water tank(1400), a bottom water tank(1300), a middle water tank(1200), a top water tank(1100), and a wastewater supply pipe(100). The outer water tank includes a drainpipe(1410). The bottom water tank is formed on the inner center of the outer water tank with the smaller diameter than the outer water tank. The wastewater supply pipe is formed on the upper side of the top water tank.

Description

위치에너지를 이용한 다단식 폐수처리장치{Apparatus for disposing waste water}Multi-stage wastewater treatment system using potential energy {Apparatus for disposing waste water}

본 발명은 위치에너지를 이용한 다단식 폐수처리장치에 관한 것으로서 좀더 상세하게 설명하면 호기성 미생물담체와 혐기성 미생물 담체를 구비하는 수조를 다단(多段)으로 적층하고, 가장 상부의 수조로 부터 폐수를 흘려보내면서 반복적으로 호기성 미생물담체와 혐기성 미생물 담체에 의해 순차적으로 정화되도록 하기 위한 위치에너지를 이용한 다단식 폐수처리장치에 관한 것이다.
The present invention relates to a multi-stage wastewater treatment apparatus using potential energy, which will be described in more detail. The tank comprising aerobic microbial carriers and anaerobic microbial carriers is stacked in multiple stages, and the wastewater flows from the uppermost tank. It relates to a multi-stage wastewater treatment apparatus using potential energy to be sequentially purified by aerobic microbial carrier and anaerobic microbial carrier.

산업이 고도로 발달함에 따라 환경오염의 심각성은 날로 대두되고 있다. 특히, 가정이나 공장, 혹은 축사 등에서 방출되는 오폐수, 공장 폐수, 축산 폐수 등(이하, 이들을 통틀어 '유기성폐수'라 함)은 지하수 및 하천으로 흘러 결국에는 바다를 오염시키게 된다. 이처럼 유기성폐수를 처리하여 정화하지 않고 그대로 방류하면 각종 유기물, 미생물 및 질소(N), 인(P) 등으로 인해 하천 등의 부영화 현상을 초래하며 이로 인해 수중 생태계가 파될 뿐만 아니라 토양의 오염을 유발하여 생활환경이나 생태계의 먹이사슬까지 파괴함으로써 인간의 생존권을 위협할 수밖에 없다.As the industry is highly developed, the seriousness of environmental pollution is increasing day by day. In particular, wastewater, factory wastewater, and livestock wastewater (hereinafter, collectively referred to as 'organic wastewater') emitted from homes, factories, or livestock farms flow to groundwater and rivers, and eventually pollute the sea. As such, when organic wastewater is treated and discharged without purification, various organic matters, microorganisms, nitrogen (N), phosphorus (P), etc., cause the sublimation phenomenon of rivers, etc. By destroying the living environment and even the food chain of the ecosystem, we have no choice but to threaten human right to life.

물론, 이와 같은 피해를 줄이기 위해서는 근본적으로 유기성폐수의 배출을 줄이는 것이 가장 바람직하겠지만 산업이 발달함에 따라 각종 유기성폐수의 배출은 불가피한 실정이다. 이에, 이러한 유기성폐수를 적절하게 처리할 수 있는 방법의 개발이 필요한 바, 근자에 들어서는 각계 각층에서는 유기성폐수를 처리할 수 있도록 한 유기성폐수 처리방법에 대해 수많은 연구개발과 투자가 이루어지고 있는 실정이다. Of course, in order to reduce such damages, it is most desirable to basically reduce the emission of organic wastewater, but as the industry develops, the discharge of various organic wastewater is inevitable. Therefore, it is necessary to develop a method for properly treating such organic wastewater, and in recent years, many research and development and investments have been made on organic wastewater treatment methods for treating organic wastewater in various layers. .

유기성폐수를 처리하는 종래의 방법에는 크게, 물리적 처리방법 및 화학적 처리방법 또는 생물학적처리 방법을 병합하여 유기성폐수를 처리하는 방법이 있다. 그러나, 이러한 전형적인 처리방법은 다분히 임의적이고 처리대상 유기성 폐수의 성상, 목표 제거율, 처리시설의 특징 등의 변화에 빠르게 대처하지 못하는 단점이 있다.Conventional methods for treating organic wastewater include a method of treating organic wastewater by combining physical treatment, chemical treatment or biological treatment. However, such a typical treatment method is much arbitrary and has a disadvantage in that it does not cope quickly with changes in the characteristics of the organic wastewater to be treated, the target removal rate, and the characteristics of the treatment facility.

또한, 종래에 공지된 유기성폐수 처리방법 중, 주로 사용된 활성오니법에 의 하면, 비교적 많은 양의 슬러지가 발생되고 고액분리를 위한 처리 약품의 과다사용으로 유지비가 많이 소요될 뿐만 아니라 그 처리능력 또한 저조한 단점이 있다.In addition, in the conventionally known organic wastewater treatment method, the activated sludge method is mainly used, a relatively large amount of sludge is generated, and the maintenance cost is not only high due to the excessive use of the treatment chemical for solid-liquid separation, There is a disadvantage.

특히, 질소화합물과 인화합물의 처리에는 난분해성으로 인하여 처리능력이 현저히 떨어지며, 이를 하천이나 호수 및 바다에 방류하게 되면 적조현상의 발생에 의한 용존산소의 결핍으로 인하여 수생태계의 파괴를 유발시키는 원인을 야기한다.In particular, the treatment of nitrogen compounds and phosphorus compounds is considerably degraded due to poor degradability, and when discharged into rivers, lakes, and seas, the cause of destruction of aquatic ecosystems due to the lack of dissolved oxygen caused by the red tide phenomenon. Cause.

그리고, 종래에는 폐수처리 장치의 설치비용 및 설치면적의 과다로 인하여 효율적인 국토 이용에 문제가 있으며, 특히 폐수처리를 위한 수조를 수평적으로 배치함으로써 반복적으로 펑핌해야 하는 등 많은 에너지의 낭비를 유발하는 단점을 갖는 것이다.
In addition, in the related art, there is a problem in the efficient use of land due to the excessive installation cost and the installation area of the wastewater treatment device. It has a disadvantage.

본 발명은 상기와 같은 문제점을 해결하기 위하여 개발된 것으로서, 유기성폐수를 호기성 미생물담체와 혐기성 미생물 담체에 의해 순차적으로, 특히 반복적으로 정화되도록 하되 최소의 면적으로 최대의 정화효과를 얻을 수 있도록 하는 위치에너지를 이용한 다단식 폐수처리장치를 제공하기 위한 것이다.
The present invention has been developed in order to solve the above problems, the organic waste water to be purified sequentially, in particular repeatedly by the aerobic microbial carrier and anaerobic microbial carrier, but the position to obtain the maximum purification effect with a minimum area It is to provide a multi-stage wastewater treatment apparatus using energy.

상기와 같은 목적을 달성하기 위하여 본 발명은 호기성 현수식 미생물담체와 혐기성 유동상 미생물 담체를 구비하는 수조를 다단(多段)으로 적층하여 배치하되, 가장 상부의 수조로 부터 폐수를 흘려 보냄으로써 폐수가 최상단의 수조에서 최하단의 수조를 거치면서 호기성 미생물담체와 혐기성 미생물 담체에 의해 반복적으로 정화되도록 구성됨을 특징으로 한다.
In order to achieve the above object, the present invention is arranged by stacking a multi-stage water tank having an aerobic suspension-type microbial carrier and anaerobic fluidized bed microbial carrier, wastewater by flowing the waste water from the uppermost tank It is characterized in that it is configured to be repeatedly purified by the aerobic microbial carrier and anaerobic microbial carrier while passing through the tank at the bottom of the tank at the top.

상술한 바와 같이 본 발명은 각각 다른 오염원에 효과적인 호기성 미생물담체와 혐기성 미생물 담체를 순차적으로, 또 반복적으로 형성함으로써 폐수가 효과적으로 정화되도록 하였다.As described above, the present invention allows the wastewater to be effectively purified by sequentially and repeatedly forming an aerobic microbial carrier and an anaerobic microbial carrier effective for different pollutants.

또한 본 발명은 위로 올라갈 수록 직경이 줄어드는 수조를 최상단으로 부터 최하단까지 반복하여 적층함으로써 폐수처리장의 좁은 공간을 최대한 활용할 수 있도록 하는 효과를 갖는다.In addition, the present invention has the effect of maximizing the narrow space of the wastewater treatment plant by repeatedly stacking the water tank is reduced in diameter from the top to the bottom.

또 본 발명은 한번의 펌핑으로 최상단 수조 위에서 쏟아진 폐수가 위치에너지에 의해 하부에 있는 수조로 순차적으로 떨어지면서 호기성 미생물담체와 혐기성 미생물 담체에 의해 정화되도록 함으로써 에너지의 절감이 가능하도록 하는 매우 유용한 발명인 것이다.
In addition, the present invention is a very useful invention that enables the reduction of energy by allowing the wastewater poured on the top tank by one pump to be purified by aerobic microbial carrier and anaerobic microbial carrier while sequentially falling into the bottom tank by potential energy. .

도 1은 최상단 수조를 보이기 위한 분리 사시도.
도 2는 도 1의 결합된 상태의 사시도.
도 3은 본 발명 폐수처리장치의 단면도.
도 4는 본 발명의 폐수처리상태를 참고도.1 is an exploded perspective view for showing the top tank.
2 is a perspective view of the combined state of FIG.
3 is a cross-sectional view of the wastewater treatment apparatus of the present invention.
4 is a reference to the wastewater treatment state of the present invention.

이에 본 발명의 구성을 첨부된 도면에 의하여 당업자가 용이하게 이해하고 재현할 수 있도록 상세하게 설명하면 다음과 같다.Accordingly, the configuration of the present invention will be described in detail with reference to the accompanying drawings so that those skilled in the art can easily understand and reproduce.

도 1은 최상단 수조를 보이기 위한 분리 사시도이고, 도 2는 도 1의 결합된 상태의 사시도이며, 도 3은 본 발명 폐수처리장치의 단면도이고, 도 4는 본 발명의 폐수처리상태를 참고도로써, 본 발명은 배수관(1410)를 구비하는 외부수조(1400)와, 상기 외부수조(1400) 내측 중앙에 형성되며 외부수조(1400)보다는 직경이 작은 최하단 수조(1300)와, 상기 최하단 수조(1300)의 중앙 상부에 지지대(1340)에 의해 지지되어 형성되며 최하단 수조(1300) 보다는 직경이 작은 중간 수조(1200)와, 상기 중간 수조(1200)의 중앙 상부에 지지대(1140)에 의해 지지되어 형성되며 중간 수조(1200) 보다는 직경이 작은 최상단 수조(1100)와, 상기 최상단 수조(1100) 상부에 형성되는 폐수공급관(100)으로 이루어지되, 상기 각각 적층되어 배치되는 다수개의 수조(1100,1200,1300)는 중간에 일정간격으로 배수구멍(1102,1202,1302)이 천공되고, 상부 내측에 형성된 걸림턱(1101,1201,1301)에는 하부에 호기성 미생물 담체(1120,1220,1320)가 현수된 물분배판(1110,1210,1310)이 얹히도록 하며, 상기 배수구멍(1102,1202,1302) 아래, 즉 수조(1100,1200,1300)의 하부에는 혐기성 미생물담체(1130,1230,1330)가 채워져 폐수가 유입되면 폐수 속을 유동하면서 폐수를 정화할 수 있도록 구성되어 진다.1 is an exploded perspective view for showing the top tank, Figure 2 is a perspective view of the combined state of Figure 1, Figure 3 is a cross-sectional view of the wastewater treatment apparatus of the present invention, Figure 4 is a wastewater treatment state of the present invention with reference to In the present invention, the outer tank 1400 having a drain pipe 1410, the outer tank 1400 is formed in the inner center and the lowermost tank 1300 having a smaller diameter than the outer tank 1400, and the lowest tank 1300 Is formed by being supported by the support 1340 at the center of the upper support and is supported by the support 1140 at the center of the middle tank 1200, the middle tank 1200 having a smaller diameter than the lowest tank 1300 And a top water tank 1100 having a smaller diameter than the middle water tank 1200, and a waste water supply pipe 100 formed on the top water tank 1100, wherein the plurality of water tanks 1100,1200, 1300) ships at regular intervals The water holes 1110, 1210, 1310 are perforated and the abutments 1101, 1201, 1301 formed inside the upper part are provided with water distribution plates 1110, 1220, 1320 suspended therein. ) And the anaerobic microbial carriers (1130, 1230, 1330) are filled under the drain holes (1102, 1202, 1302), that is, the lower parts of the tanks (1100, 1200, 1300). It is configured to purify waste water.

이때 상기 호기성 미생물 담체가 현수된 물분배판은 최상단 수조(1100)만 제외하고 모두 상부에 위치하는 수조의 배수구멍(1102,1202,1302) 보다 항상 아래에 위치하도록 한다. 이는 상부에 위치한 수조의 배수구멍을 통해 배수된 폐수가 다시 하부에 위치한 수조의 호기성 미생물 담체에 의해 정화된 뒤 혐기성 미생물담체에 의해 정화되도록 하기 위해 필요한 구성이다.At this time, the water distribution plate in which the aerobic microbial carrier is suspended is always positioned below the drainage holes 1102, 1202 and 1302 of the tank except for the uppermost tank 1100. This is necessary to allow the wastewater drained through the drain hole of the upper tank to be purified by the anaerobic microbial carrier after being purified by the aerobic microbial carrier of the lower tank.

상기 물분배판(1110,1210,1310)에는 다수개의 통수공(1111)이 형성되며, 상기 물분배판(1110,1210,1310)의 저부에는 호기성 미생물담체(1120,1220,1320)가 현수되어지되, 상기 호기성 미생물담체(1120,1220,1320)의 상단은 물분배판(1110,1210,1310)의 저면으로 부터 일정간격 이격되도록 형성함과 동시에 호기성 미생물담체(1120,1220,1320)의 상단 중심은 물분배판(1110,1210,1310)의 통수공(1111) 중심과 동일한 수직선상에 위치하도록 구성됨이 바람직하다.A plurality of water holes 1111 are formed in the water distribution plates 1110, 1210 and 1310, and aerobic microbial carriers 1120, 1220 and 1320 are suspended in the bottom of the water distribution plates 1110, 1210 and 1310. The upper end of the aerobic microbial carriers (1120, 1220, 1320) is formed so as to be spaced apart from the bottom of the water distribution plates (1110, 1210, 1320) at the same time and the center of the upper end of the aerobic microbial carriers (1120, 1220, 1320) It is preferable to be configured to be located on the same vertical line as the center of the through hole 1111 of the back plate (1110, 1210, 1310).

이때 일정간격이라 함은 통수공(1111)이 호기성 미생물담체(1120,1220,1320)에 의해 막히지 않고 또 폐수의 찌꺼기가 호기성 미생물담체(1120,1220,1320) 위에 쌓이더라도 통수공(1111)을 막지는 않을 정도의 거리를 말하며, 폐수의 상태와 폐수처리용량에 따라 다를수는 있지만 약 2mm~20cm정도의 범위가 될 것이다.In this case, the constant interval means that the water hole 1111 is not blocked by the aerobic microbial carriers 1120, 1220, 1320, and the waste water is accumulated on the aerobic microbial carriers 1120, 1220, 1320. It is a distance that will not be blocked, and may vary depending on the condition of the wastewater and the capacity of the wastewater, but will be in the range of about 2 mm to 20 cm.

이처럼 호기성 미생물담체(1120,1220,1320)의 상단 중심이 물분배판(1110,1210,1310)의 통수공(1111) 중심과 동일한 수직선상에 위치하게 됨으로써 통수공(1111)을 통과한 폐수는 정확하게 호기성 미생물담체(1120,1220,1320)의 중심으로 낙하하게 되고, 결국 폐수가 정확하게 호기성 미생물담체(1120,1220,1320)를 타고 흐르게 되므로 폐수의 정화효율이 높아지게 되는 것이다.As such, the upper center of the aerobic microbial carriers 1120, 1220 and 1320 is positioned on the same vertical line as the center of the through holes 1111 of the water distribution plates 1110, 1210 and 1310 so that the wastewater passing through the through holes 1111 is accurately The aerobic microbial carriers (1120, 1220, 1320) will fall to the center of the end, and the waste water will flow through the aerobic microbial carriers (1120, 1220, 1320) accurately, so that the purification efficiency of the waste water is increased.

이처럼 본 발명에 사용되는 호기성 미생물담체(1120,1220,1320)는 다양한 종류가 사용될 수 있으나 섬유상 미생물 담체를 사용함이 바람직하고, 혐기성 미생물담체(1130,1230,1330)은 세라믹 또는 플라스틱, 탄소섬유재질의 유동상 담체를 사용함이 바람직하다. As described above, various types of aerobic microbial carriers 1120, 1220 and 1320 used in the present invention may be used, but it is preferable to use a fibrous microbial carrier, and anaerobic microbial carriers 1130, 1230 and 1330 may be made of ceramic or plastic or carbon fiber material. Preference is given to using fluidized bed carriers.

또한 본 발명은 상기 혐기성 미생물담체(1130,1230,1330)의 유동성을 강화하고 혐기성 미생물담체(1130,1230,1330)의 상부에 위치한 호기성 미생물담체(1120,1220,1320)에 공기를 공급하기 위하여 공기공급관(1500)을 각 수조(1100,1200,1300)의 하단에 형성할 수도 있다. 이로 인해 수조(1100,1200,1300) 내부에 폐수가 폭기되면서 보다 활발한 정화작용이 이루어지게 된다.
In addition, the present invention to enhance the fluidity of the anaerobic microbial carriers (1130, 1230, 1330) and to supply air to the aerobic microbial carriers (1120, 1220, 1320) located on top of the anaerobic microbial carriers (1130, 1230, 1330) The air supply pipe 1500 may be formed at the lower ends of the respective tanks 1100, 1200, and 1300. As a result, the waste water is aerated in the water tanks 1100, 1200, and 1300, thereby purifying more actively.

이처럼 본 발명은 폐수가 최상부에 형성되는 폐수공급관(100)에 의해 최상단에 위치한 수조(1100)의 물분배판(1110)에 공급되는 구조이며, 상기 물분배판(1110)의 통수공(1111)을 통해 현수되어 있는 호기성 미생물담체(1120)를 따라 흘러 내려 수조(1100)의 하부에 채워지게 된다. 이때 폐수는 상기 호기성 미생물담체(1120)를 따라 흐르는 순간 호기성 미생물에 의해 오염물질이 양분으로 섭취되면서 정화된다.As such, the present invention is a structure in which the waste water is supplied to the water distribution plate 1110 of the water tank 1100 located at the top by the wastewater supply pipe 100 formed at the top thereof, and through the water hole 1111 of the water distribution plate 1110. It flows down along the suspended aerobic microbial carrier 1120 is filled in the lower portion of the water tank (1100). At this time, the wastewater is purified by ingesting contaminants as nutrients by the aerobic microorganisms as they flow along the aerobic microbial carrier 1120.

다음 수조(1100)의 하부에 채워진 폐수는 혐기성 미생물담체(1130)에 서식하고 있는 혐기성 미생물에 의해 오염물질이 양분으로 섭취되면서 정화된다.Next, the wastewater filled in the lower portion of the water tank 1100 is purified by ingesting contaminants as nutrients by anaerobic microorganisms inhabiting the anaerobic microbial carrier 1130.

이때 수조(1100)를 넘친 폐수는 배수구멍(1102)을 통해 외부로 배출되며, 이처럼 배출된 폐수는 다음 수조, 즉 중간 수조(1200)의 물분배판(1210)에 공급되며, 상기 물분배판(1210)의 통수공(1211)을 통해 역시 현수되어 있는 호기성 미생물담체(1220)를 따라 흘러 내리면서 정화된 다음, 수조(1200)의 하부에 채워져 다시 혐기성 미생물담체(1230)에 의해 정화된다.At this time, the wastewater overflowing the water tank 1100 is discharged to the outside through the drain hole 1102, the discharged waste water is supplied to the water distribution plate 1210 of the next tank, that is, the intermediate tank 1200, the water distribution plate 1210 Purified while flowing along the aerobic microbial carrier 1220, which is also suspended through the air hole 1211, and filled in the lower portion of the tank 1200, and is again purified by the anaerobic microbial carrier 1230.

이와 같이 반복되는 구조로 최하단 수조(1300)로 공급된 폐수는 역시 동일한 순서로 호기성 미생물담체(1320)와 혐기성 미생물담체(1330)에 의해 정화된 다음 배수구멍(1302)을 통해 외부수조(1400)로 정화된 폐수를 배출하게 되고 배수관(1410)를 통해 정화조(미도시)로 이동하게 된다.
The wastewater supplied to the lowermost tank 1300 in such a repeated structure is also purified by the aerobic microbial carrier 1320 and the anaerobic microbial carrier 1330 in the same order, and then the external tank 1400 through the drainage hole 1302. The purified wastewater is discharged to the septic tank (not shown) through the drain pipe 1410.

1: 본 발명 폐수처리장치 100: 폐수공급관
1100: 최상단 수조 1200: 중간수조
1300: 최하단 수조 1400: 외부수조
1500: 공기공급관
1101,1201,1301: 걸림턱
1102,1202,1302: 배수구멍
1110,1210,1310: 물분배판
1120,1220,1320: 호기성 미생물 담체
1130,1230,1330: 혐기성 미생물 담체1: the present invention wastewater treatment apparatus 100: wastewater supply pipe
1100: top tank 1200: middle tank
1300: lowest tank 1400: external tank
1500: air supply pipe
1101,1201,1301: Jamming jaw
1102,1202,1302: Drainage hole
1110,1210,1310: water distribution plate
1120,1220,1320: Aerobic Microbial Carriers
1130,1230,1330: anaerobic microbial carriers

Claims (4)

배수관(1410)를 구비하는 외부수조(1400)와, 상기 외부수조(1400) 내측 중앙에 형성되며 외부수조(1400)보다는 직경이 작은 최하단 수조(1300)와, 상기 최하단 수조(1300)의 중앙 상부에 지지대(1340)에 의해 지지되어 형성되며 최하단 수조(1300) 보다는 직경이 작은 중간 수조(1200)와, 상기 중간 수조(1200)의 중앙 상부에 지지대(1140)에 의해 지지되어 형성되며 중간 수조(1200) 보다는 직경이 작은 최상단 수조(1100)와, 상기 최상단 수조(1100) 상부에 형성되는 폐수공급관(100)으로 이루어지되, 상기 각각 적층되어 배치되는 다수개의 수조(1100,1200,1300)는 중간에 일정간격으로 배수구멍(1102,1202,1302)이 천공되고, 상부 내측에 형성된 걸림턱(1101,1201,1301)에는 하부에 호기성 미생물 담체(1120,1220,1320)가 현수된 물분배판(1110,1210,1310)이 얹히도록 하며, 상기 배수구멍(1102,1202,1302) 아래, 즉 수조(1100,1200,1300)의 하부에는 혐기성 미생물담체(1130,1230,1330)가 채워져 폐수가 유입되면 폐수 속을 유동하면서 폐수를 정화할 수 있도록 구성되어짐을 특징으로 하는 위치에너지를 이용한 다단식 폐수처리장치.
An outer tank 1400 having a drain pipe 1410, a lowermost tank 1300 formed in the inner center of the outer tank 1400 and having a smaller diameter than the outer tank 1400, and a central upper portion of the lower tank 1300. Is formed by being supported by the support 1340, the intermediate tank 1200 having a smaller diameter than the lowermost tank 1300, and is supported by the support 1140 formed on the center upper portion of the intermediate tank 1200, the intermediate tank ( The top tank 1100 having a smaller diameter than 1200, and the waste water supply pipe 100 formed on the top tank 1100, each of the plurality of tanks (1100, 1200, 1300) are stacked in the middle The drainage holes 1102, 1202 and 1302 are drilled at regular intervals, and the locking jaws 1101, 1201 and 1301 formed inside the upper part have water distribution plates 1110 suspended with aerobic microbial carriers 1120, 1220 and 1320 at the bottom. , 1210, 1310, and the drain holes (1102,1202,1302) In other words, the bottom of the tank (1100, 1200, 1300) is filled with anaerobic microbial carriers (1130, 1230, 1330) when the waste water flows into the waste water while flowing into the waste water, characterized in that it is configured to clean the waste water Multi-stage wastewater treatment device using.
제 1항에 있어서 상기 호기성 미생물 담체가 현수된 물분배판은 최상단 수조(1100)만 제외하고 모두 상부에 위치하는 수조의 배수구멍(1102,1202,1302) 보다 항상 아래에 위치하도록 구성되어짐을 특징으로 하는 위치에너지를 이용한 다단식 폐수처리장치.
According to claim 1, wherein the aerobic microbial carrier is suspended water distribution plate is configured to be always located below the drain holes (1102,1202,1302) of the tank located at the top except the top tank (1100). Multi-stage wastewater treatment device using potential energy to.
제 1항에 있어서 상기 물분배판(1110,1210,1310)에는 다수개의 통수공(1111)이 형성되며, 상기 물분배판(1110,1210,1310)의 저부에는 호기성 미생물담체(1120,1220,1320)가 현수되어지되, 상기 호기성 미생물담체(1120,1220,1320)의 상단은 물분배판(1110,1210,1310)의 저면으로 부터 일정간격 이격되도록 형성함과 동시에 호기성 미생물담체(1120,1220,1320)의 상단 중심은 물분배판(1110,1210,1310)의 통수공(1111) 중심과 동일한 수직선상에 위치하도록 구성되어짐을 특징으로 하는 위치에너지를 이용한 다단식 폐수처리장치.
The water distribution plate (1110, 1210, 1310) is formed with a plurality of through holes 1111, the bottom of the water distribution plate (1110, 1210, 1310) aerobic microbial carrier (1120, 1220, 1320) Is suspended, the upper end of the aerobic microbial carriers (1120, 1220, 1320) is formed so as to be spaced apart from the bottom of the water distribution plates (1110, 1210, 1310) at the same time aerobic microbial carriers (1120, 1220, 1320) The upper center of the multi-stage wastewater treatment apparatus using potential energy, characterized in that it is configured to be located on the same vertical line as the center of the water hole (1111) of the water distribution plate (1110, 1210, 1310).
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KR20100041132A 2010-04-30 2010-04-30 Apparatus for disposing waste water KR101003705B1 (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101368347B1 (en) 2013-04-02 2014-02-27 김일홍 Water treatment apparatus
CN107244759A (en) * 2017-07-19 2017-10-13 安徽云融信息技术有限公司 A kind of intermediate water reuse system and its method

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR200257981Y1 (en) 2001-09-12 2001-12-24 고명한 Fluidized Media having a potential of aerobic and anaerobic treatment
KR100959911B1 (en) 2009-09-14 2010-05-26 주식회사 세기종합환경 Floating body with a biofilm

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR200257981Y1 (en) 2001-09-12 2001-12-24 고명한 Fluidized Media having a potential of aerobic and anaerobic treatment
KR100959911B1 (en) 2009-09-14 2010-05-26 주식회사 세기종합환경 Floating body with a biofilm

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101368347B1 (en) 2013-04-02 2014-02-27 김일홍 Water treatment apparatus
CN107244759A (en) * 2017-07-19 2017-10-13 安徽云融信息技术有限公司 A kind of intermediate water reuse system and its method

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