KR200368250Y1 - Coagulating and Precipitating Apparatus for Sewage and Wastewater Treatment System - Google Patents

Coagulating and Precipitating Apparatus for Sewage and Wastewater Treatment System Download PDF

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KR200368250Y1
KR200368250Y1 KR20-2004-0024741U KR20040024741U KR200368250Y1 KR 200368250 Y1 KR200368250 Y1 KR 200368250Y1 KR 20040024741 U KR20040024741 U KR 20040024741U KR 200368250 Y1 KR200368250 Y1 KR 200368250Y1
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tank
coagulation
treatment system
sewage
sedimentation
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KR20-2004-0024741U
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Korean (ko)
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이상배
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베올리아워터시스템즈코리아 주식회사
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D21/00Separation of suspended solid particles from liquids by sedimentation
    • B01D21/0003Making of sedimentation devices, structural details thereof, e.g. prefabricated parts
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D21/00Separation of suspended solid particles from liquids by sedimentation
    • B01D21/02Settling tanks with single outlets for the separated liquid
    • B01D21/08Settling tanks with single outlets for the separated liquid provided with flocculating compartments
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D21/00Separation of suspended solid particles from liquids by sedimentation
    • B01D21/24Feed or discharge mechanisms for settling tanks
    • B01D21/245Discharge mechanisms for the sediments
    • 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
    • C02F1/52Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (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)
  • Separation Of Suspended Particles By Flocculating Agents (AREA)

Abstract

본 고안은 응결조 내의 침전물 침적현상을 제거함으로써 처리수의 수질을 양호하게 유지할 수 있도록 하는 하폐수 처리시스템의 고속응집침전 처리장치에 관한 것이다. 하폐수 처리시스템의 고속응집침전 처리장치는 일측으로 원수가 공급되는 원수 유입구가 형성되고 내부에 제 1교반기가 설치된 응집조와, 응집조와 연결되고 내부에 제 2교반기가 설치된 혼화조와, 혼화조와 연결되고 내부에 제 3교반기가 설치된 응결조와, 응결조와 연결되고 바닥면에 슬러지 수집 호퍼가 형성된 침전조를 포함한다. 응결조와 침전조를 구획하는 벽의 하부에는 응결조내에 침적될 수 있는 침전물이 응결조로부터 침전조 내로 원활하게 유출되도록 하기 위한 다수의 침전물 배출공이 복수의 행과 열을 이루며 형성되어 있다.The present invention relates to a high-speed flocculation sedimentation treatment apparatus of a sewage treatment system that can maintain the water quality of the treated water by removing the sediment deposition phenomenon in the coagulation tank. The high speed flocculation sedimentation treatment device of the sewage water treatment system has a raw water inlet for supplying raw water to one side and a coagulation tank having a first stirrer inside thereof, a mixing tank connected with a cohesion tank and having a second stirrer inside thereof, And a settling tank having a third stirrer installed therein, and a settling tank connected to the settling tank and having a sludge collection hopper formed at the bottom thereof. In the lower part of the wall partitioning the coagulation tank and the settling tank, a plurality of sediment discharge holes are formed in a plurality of rows and columns to allow the sediment which can be deposited in the coagulation tank to smoothly flow out from the coagulation tank.

Description

하폐수 처리시스템의 고속응집침전 처리장치{Coagulating and Precipitating Apparatus for Sewage and Wastewater Treatment System}Coagulating and Precipitating Apparatus for Sewage and Wastewater Treatment System

본 고안은 하폐수 처리시스템의 고속응집침전 처리장치에 관한 것으로, 더욱 상세하게는 응결조 내의 침전물 침적현상을 제거하여 유지보수가 원활히 이루어지도록 하면서 처리수의 수질을 양호하게 유지할 수 있도록 하는 하폐수 처리시스템의 고속응집침전 처리장치에 관한 것이다.The present invention relates to a high speed flocculation sedimentation treatment device of a sewage water treatment system, and more particularly, to remove sediment deposits in a condensing tank so that maintenance can be performed smoothly while maintaining the quality of treated water well. It relates to a high speed flocculation sedimentation treatment apparatus.

일반적으로, 고속응집침전 처리장치는 응집 및 침전의 원리를 이용하여 하폐수내의 유기물 및 부유물질 등을 제거하기 위한 것으로, 정수 및 공장 폐수, 축산물 폐수, 생활하수 등을 정화하는데 널리 사용되고 있다.In general, the high-speed flocculation sedimentation treatment apparatus is used to remove organic matter and suspended matter in sewage water using the principle of flocculation and sedimentation, and is widely used to purify purified water and factory wastewater, livestock wastewater, and domestic sewage.

그러나, 종래의 고속응집침전 처리장치는 응결조 내에 침전물이 바닥에 점차 침적되는 문제로 인하여 처리수의 체류시간이 짧아지는 문제점이 있었다. 따라서, 시간이 지남에 따라 하폐수 처리효율이 저하되므로, 정기적으로 응결조를 비우고 청소를 해야 하는 번거로움이 있었고, 상시 가동되어야 하는 하수처리장의 경우에는 청소작업이 매우 어려운 문제점이 있었다.However, the conventional high speed flocculation sedimentation treatment device has a problem in that the residence time of the treated water is shortened due to the problem that the precipitate gradually accumulates in the bottom of the coagulation tank. Therefore, the wastewater treatment efficiency is lowered over time, and there is a problem of emptying the condensing tank and cleaning regularly, and in the case of a sewage treatment plant that needs to be operated at all times, the cleaning operation is very difficult.

본 고안은 이러한 종래기술의 문제점을 해결하기 위한 것으로서, 본 고안의 목적은 응결조 내의 침전물 침적현상을 제거하여 유지보수가 원활히 이루어지도록 하면서 처리수의 수질을 양호하게 유지할 수 있도록 하는 하폐수 처리시스템의 고속응집침전 처리장치를 제공하는 것이다.The present invention is to solve the problems of the prior art, an object of the present invention is to remove the sediment deposition phenomenon in the condensate tank to maintain the water quality of the treated water while maintaining a smooth maintenance of the wastewater treatment system It is to provide a high speed flocculation sedimentation treatment device.

상기 목적을 달성하기 위한 본 고안에 따른 하폐수 처리시스템의 고속응집침전 처리장치는 하폐수내의 유기물 및 부유물질을 제거하기 위해 순차적으로 연결되어 설치되는 응집조, 혼화조, 응결조 및 응결조로부터 유입되는 처리수로부터 슬러지를 침전시키기 위한 침전조를 포함하고, 응결조와 침전조를 구획하는 벽의 하부에는 응결조내의 침전물이 응결조로부터 침전조 내로 배출되도록 하기 위한 다수의 침전물 배출공이 복수의 행과 열을 이루며 형성되어 있다.The high speed flocculation sedimentation treatment apparatus of the sewage treatment system according to the present invention for achieving the above object is introduced from a coagulation tank, a mixing tank, a coagulation tank and a coagulation tank installed in order to remove organic matter and suspended matter in the waste water. A sedimentation tank for sedimentation of the sludge from the treated water, and a plurality of sediment discharge holes are formed in a plurality of rows and columns at the lower part of the wall partitioning the condensation tank and the sedimentation tank so that the sediment in the condensation tank is discharged from the condensing tank into the sedimentation tank. It is.

도 1은 본 고안에 따른 하폐수 처리시스템의 고속응집침전 처리장치를 개략적으로 보인 평면도,1 is a plan view schematically showing a high speed flocculation sedimentation treatment apparatus of a sewage treatment system according to the present invention,

도 2는 본 고안에 따른 하폐수 처리시스템의 고속응집침전 처리장치의 내부구조를 개략적으로 보인 부분단면도,Figure 2 is a partial cross-sectional view schematically showing the internal structure of the high speed flocculation sedimentation treatment apparatus of the sewage treatment system according to the present invention,

도 3은 본 고안에 따른 하폐수 처리시스템의 고속응집침전 처리장치의 침전물 배출공을 보인 도면.Figure 3 is a view showing a sediment discharge hole of the high speed flocculation sedimentation treatment apparatus of a wastewater treatment system according to the present invention.

<도면의 주요 부분에 대한 부호의 설명><Explanation of symbols for the main parts of the drawings>

10: 응집조10: flocculation tank

12: 제 1교반기12: first stirrer

14: 원수 유입구14: raw water inlet

20: 혼화조20: mixing tank

22: 제 2교반기22: second stirrer

30: 응결조30: Condensation

32: 제 3교반기32: 3rd stirrer

34: 벽34: wall

36: 배출공36: discharge hole

40: 침전조40: sedimentation tank

44: 경사판44: inclined plate

46: 처리수 월류 웨어 수로부46: Processing water overflow wear channel

48: 처리수 배출구48: treated water outlet

이하에서는 첨부된 도면을 참조하여 본 고안에 대한 바람직한 실시예를 상세하게 설명한다.Hereinafter, with reference to the accompanying drawings will be described in detail a preferred embodiment of the present invention.

도 1 및 도 2는 각각 본 고안에 따른 하폐수 처리시스템의 고속응집침전 처리장치를 개략적으로 보인 평면도 및 부분단면도이고, 도 3은 침전물 배출공을 보인 도면이다.1 and 2 are a plan view and a partial cross-sectional view schematically showing a high-speed coagulation sedimentation treatment apparatus of the sewage treatment system according to the present invention, respectively, Figure 3 is a view showing the discharge hole of the sediment.

도시된 바와 같이, 본 고안에 따른 하폐수 처리시스템의 고속응집침전 처리장치는 일측으로 원수가 공급되는 원수 유입구(14)가 형성되고 그 내부에 제 1교반기(12)가 설치된 응집조(10)와, 응집조(10)와 직렬로 연결되고 내부에 제 2교반기(22)가 설치된 혼화조(20)와, 혼화조(20)와 직렬로 연결되고 내부에 제 3교반기(32)가 설치된 응결조(30)와, 응결조(30)와 직렬로 연결되고 바닥면에 슬러지 수집 호퍼(42)가 형성되며 일측에 처리수 배출구(48)가 형성되는 침전조(40)를 포함한다.As shown, the high speed flocculation sedimentation treatment apparatus of the sewage treatment system according to the present invention is formed with a coagulation tank 10 in which a raw water inlet 14 for supplying raw water to one side and a first stirrer 12 is installed therein; , A mixing tank 20 connected in series with the coagulation tank 10 and having a second stirrer 22 installed therein, and a coagulation tank having a third stirrer 32 connected in series with the mixing tank 20 and installed therein 30 and the settling tank 40 is connected in series with the condensation tank 30, the sludge collection hopper 42 is formed on the bottom surface and the treated water outlet 48 is formed on one side.

응결조(30)와 침전조(40)를 구획하는 벽(34)의 하부에는 도 3에 도시된 바와 같이, 응결조(30)내에 침적될 수 있는 침전물이 응결조(30)로부터 침전조(40) 내로 원활히 유출되도록 하기 위한 다수의 침전물 배출공(36)이 복수의 행과 열을 이루며 형성되어 있다. 바람직하게는, 각 침전물 배출공(36)의 직경은 1.3㎝ 내지 1.7㎝이고, 상호 이웃하는 두 침전물 배출공(36) 사이의 간격은 8㎝ 내지 12㎝로 설정된다.In the lower portion of the wall 34 partitioning the coagulation tank 30 and the precipitation tank 40, as shown in FIG. 3, sediment which can be deposited in the coagulation tank 30 is settled from the coagulation tank 30. A plurality of sediment discharge holes 36 are formed to form a plurality of rows and columns to smoothly flow out into the inside. Preferably, the diameter of each precipitate discharge hole 36 is 1.3 cm to 1.7 cm, and the spacing between two neighboring precipitate discharge holes 36 is set to 8 cm to 12 cm.

침전조(40)의 상부 일측에는 일정한 간격으로 경사지게 배치된 복수의 경사판(44)이 설치되고, 경사판(44)의 상부에는 경사판(44)을 통과한 처리수를 배출하기 위한 처리수 월류 웨어 수로부(46)가 설치된다. 경사판(44)은 수평면과 대략 50°~70°범위의 각도를 이루며, 중간영역이 소정각도로 절곡될 수 있고, 경사판(44)의 면은 일정한 간격으로 사다리꼴 형태를 갖추고 있다.A plurality of inclined plates 44 disposed to be inclined at regular intervals are installed at one upper side of the settling tank 40, and a treated water overflow wear channel for discharging the treated water passing through the inclined plate 44 at an upper portion of the inclined plate 44. 46 is installed. The inclined plate 44 forms an angle in the range of approximately 50 ° to 70 ° with the horizontal plane, the intermediate region may be bent at a predetermined angle, and the surface of the inclined plate 44 has a trapezoidal shape at regular intervals.

침전조(40)의 하측 외부에는 슬러지 수집 호퍼(42)와 연통하는 슬러지 재순환 파이프(52)가 연결되며, 슬러지 재순환 파이프(52)는 혼화조(20)의 상측으로 연장형성된다. 재순환 파이프(52)의 중도에는 재순환 펌프(54)가 설치되고, 혼화조(20)의 상측으로 연장되는 슬러지 재순환 파이프(52)의 단부에는 사이클론 분리기(56)가 설치된다.The sludge recycle pipe 52 communicating with the sludge collection hopper 42 is connected to the lower outer side of the settling tank 40, and the sludge recycle pipe 52 extends above the mixing tank 20. A recirculation pump 54 is installed in the middle of the recirculation pipe 52, and a cyclone separator 56 is installed at the end of the sludge recirculation pipe 52 extending upward of the mixing tank 20.

이하에서는, 상기와 같이 구성된 본 고안에 따른 하폐수 처리시스템의 고속응집침전 처리장치의 작동을 설명하기로 한다.Hereinafter, the operation of the high speed flocculation sedimentation treatment apparatus of the wastewater treatment system according to the present invention configured as described above will be described.

원수 유입구(14)를 통해 응집조(10)내로 원수가 유입되고, 응집조(10)에 응집제(FeCl3)를 주입하고 제 1교반기(12)에 의해 급속교반을 실시하여 음전하를 띄고 있는 부유물질의 표면을 중화시키고, 원수중에 포함되어 있는 인(PO4 3-)을 불용성의 인산염화(FePO4)시킨다. 혼화조(20)내에 폴리머(음이온계)를 주입하여 응집조(10)에서 응결된 미세플록(floc)을 응집시키고, 마이크로샌드(microsand)를 주입하여 응집효과를 증대시킨다. 이후, 응결조(30)내에서 제 3교반기(32)에 의한 완속교반을 통해서 거대플록으로 형성시킨 후, 침전조(40)에서 침전시킨다. 응결조(30)내에서의 반응공정 중 침전물이 발생하게 되는데, 이러한 침전물은 응결조(30)와 침전조(40)를 구획하는 벽(34)에 구비되어 있는 다수의 배출공(36)을 통해 침전조(40)내로 배출됨으로써, 응결조(30)내에서의 침적현상을 방지한다.Raw water flows into the coagulation tank 10 through the raw water inlet 14, injects coagulant (FeCl 3 ) into the coagulation tank 10, and rapidly stirs by the first stirrer 12 to give a negative charge. The surface of the material is neutralized and phosphorus (PO 4 3- ) contained in raw water is insoluble phosphate (FePO 4 ). A polymer (anionic) is injected into the mixing tank 20 to agglomerate the floc condensed in the agglomeration tank 10, and microsand is injected to increase the agglomeration effect. Thereafter, after forming into a large floc through slow stirring by the third stirrer 32 in the condensation tank 30, it is precipitated in the settling tank (40). Precipitates are generated during the reaction process in the condensation tank 30, and the precipitates are formed through a plurality of discharge holes 36 provided in the wall 34 partitioning the condensing tank 30 and the settling tank 40. By being discharged into the settling tank 40, deposition phenomenon in the condensing tank 30 is prevented.

침전조(40)내로 유입된 처리수는 경사판(44)을 통해 올라가면서 침전된 고형물은 경사판(44)을 타고 아래로 흘러내려 침전된다. 이러한 경사판(44)은 침전높이를 낮추고, 침전면적을 증가시켜 보다 빠른 침전속도를 가지게 한다. 경사판(44)을 빠져나온 처리수는 처리수 월류 웨어 수로부(46)로 월류한 후 처리수 배출구(48)를 통해 외부로 배출되게 된다.The treated water introduced into the settling tank 40 goes up through the inclined plate 44, and the precipitated solids flow down the inclined plate 44 to settle down. This inclined plate 44 lowers the settling height, and increases the settling area to have a faster settling speed. The treated water exiting the inclined plate 44 is discharged to the outside through the treated water outlet 48 after flowing through the treated water overflow wear channel 46.

한편, 침전된 마이크로샌드와 슬러지 혼합물은 침전조(40)의 바닥에서 수집되어 원심 슬러지 펌프(54)에 의해 사이클론 분리기(56)로 이송되고, 압송된 힘에의해 사이클론 분리기(56) 내부에서 슬러지와 마이크로샌드가 분리된다. 분리된 마이크로샌드는 사이클론 분리기(56)의 하부에서 혼화조(20) 내로 주입되어 재사용되고, 상대적으로 가벼운 슬러지는 사이클론 분리기(56)의 상부에서 농축이나 최종처분을 위하여 이송된다.On the other hand, the precipitated microsands and sludge mixture is collected at the bottom of the settling tank 40 and transferred to the cyclone separator 56 by the centrifugal sludge pump 54, and the sludge and the sludge inside the cyclone separator 56 by the forced force. Microsands are separated. The separated microsands are injected into the mixing tank 20 at the bottom of the cyclone separator 56 and reused, and the relatively light sludge is transferred for concentration or final disposal at the top of the cyclone separator 56.

이상에서 상세히 설명한 바와 같이, 본 고안에 따른 하폐수 처리시스템의 고속응집침전 처리장치에 있어서, 응결조 내에서 침적될 수 있는 침전물이 응결조와 침전조를 구획하는 벽에 형성된 다수의 배출공을 통해 침전조내로 배출됨으로써 처리수의 응결조내 체류시간을 극대화하여 처리효율을 양호하게 유지할 수 있을 뿐만 아니라, 정기적으로 응결조를 비우고 청소를 해야 하는 번거로움이 없어지는 효과가 있다.As described in detail above, in the high speed flocculation sedimentation treatment apparatus of the sewage treatment system according to the present invention, sediment which can be deposited in the coagulation tank is introduced into the sedimentation tank through a plurality of discharge holes formed in the wall separating the coagulation tank and the sedimentation tank. By discharging, it is possible not only to maximize the residence time of the treated water in the condensation tank to maintain the treatment efficiency well, but also to eliminate the hassle of emptying and cleaning the condensing tank regularly.

Claims (2)

하폐수내의 유기물 및 부유물질을 제거하기 위해 순차적으로 설치되는 응집조, 혼화조, 응결조 및 상기 응결조로부터 유입되는 처리수로부터 슬러지를 침전시키기 위한 침전조를 포함하는 하폐수 처리시스템의 고속응집침전 처리장치에 있어서,High-speed coagulation sedimentation treatment apparatus of sewage treatment system including a flocculation tank, a mixing tank, a condensation tank, and a settling tank for sedimentation of sludge from the treated water flowing from the coagulation tank are sequentially installed to remove organic matter and suspended matter in the sewage water. To 상기 응결조와 상기 침전조를 구획하는 벽의 하부에는 상기 응결조내의 침전물이 상기 응결조로부터 상기 침전조 내로 배출되도록 하기 위한 다수의 침전물 배출공이 복수의 행과 열을 이루며 형성되어 있는 것을 특징으로 하는 하폐수 처리시스템의 고속응집침전 처리장치.Sewage water treatment, characterized in that a plurality of sediment discharge holes formed in a plurality of rows and columns in the lower portion of the wall partitioning the coagulation tank and the sedimentation tank so that the sediment in the coagulation tank is discharged from the coagulation tank into the sedimentation tank. High speed flocculation sedimentation treatment system. 제 1항에 있어서, 상기 침전물 배출공의 직경은 1.3㎝ 내지 1.7㎝이고, 상호 이웃하는 두 침전물 배출공 사이의 간격은 8㎝ 내지 12㎝인 것을 특징으로 하는 하폐수 처리시스템의 고속응집침전 처리장치.According to claim 1, wherein the diameter of the sediment discharge hole is 1.3cm to 1.7cm, the spacing between two adjacent sediment discharge hole is 8cm to 12cm, high speed coagulation sedimentation treatment apparatus of the sewage treatment system .
KR20-2004-0024741U 2004-08-30 2004-08-30 Coagulating and Precipitating Apparatus for Sewage and Wastewater Treatment System KR200368250Y1 (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7903534B2 (en) 2006-11-17 2011-03-08 Samsung Electronics Co., Ltd. Optical recording medium, apparatus and method of manufacturing optical recording medium, and apparatus and method of recording/reproducing data of optical recording medium
KR101278230B1 (en) * 2010-05-31 2013-06-27 김남천 The method and Appuratus of removing total nitrogen and phosphate in sewage and wastewater using precipitation-agent of rapidity for coagulation an flocculation

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7903534B2 (en) 2006-11-17 2011-03-08 Samsung Electronics Co., Ltd. Optical recording medium, apparatus and method of manufacturing optical recording medium, and apparatus and method of recording/reproducing data of optical recording medium
KR101278230B1 (en) * 2010-05-31 2013-06-27 김남천 The method and Appuratus of removing total nitrogen and phosphate in sewage and wastewater using precipitation-agent of rapidity for coagulation an flocculation

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