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JP4019209B2 - Water purification system - Google Patents

Water purification system Download PDF

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Publication number
JP4019209B2
JP4019209B2 JP2000238952A JP2000238952A JP4019209B2 JP 4019209 B2 JP4019209 B2 JP 4019209B2 JP 2000238952 A JP2000238952 A JP 2000238952A JP 2000238952 A JP2000238952 A JP 2000238952A JP 4019209 B2 JP4019209 B2 JP 4019209B2
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Japan
Prior art keywords
carrier
conduit
sewage
bacteria
purification system
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP2000238952A
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Japanese (ja)
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JP2002045878A (en
Inventor
務 板屋
Original Assignee
株式会社ソナー
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
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Priority to JP2000238952A priority Critical patent/JP4019209B2/en
Priority to PCT/JP2001/011175 priority patent/WO2003053866A1/en
Publication of JP2002045878A publication Critical patent/JP2002045878A/en
Application granted granted Critical
Publication of JP4019209B2 publication Critical patent/JP4019209B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/02Aerobic processes
    • C02F3/04Aerobic processes using trickle filters
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/02Aerobic processes
    • C02F3/06Aerobic processes using submerged filters
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological 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)
  • Biological Treatment Of Waste Water (AREA)
  • Apparatus Associated With Microorganisms And Enzymes (AREA)
  • Immobilizing And Processing Of Enzymes And Microorganisms (AREA)
  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)

Description

【0001】
【発明の属する技術分野】
この発明は、下水等の有機性の汚濁物質を含む汚水を浄化するために用いられる水の浄化システムに関する。
【0002】
【従来の技術】
従来、有機性の汚濁物質を含む汚水の浄化には、バクテリアによって汚濁物質を分解させる方法が広く用いられており、その代表的なものとして活性汚泥法、生物膜法等がある。
【0003】
【発明が解決しようとする課題】
これら従来の方法は、処理槽、配管等からなる複雑な設備と広いスペースとを必要とし、しかも曝気を継続的に行わなければならないのでランニングコストが高くつくという問題があった。このような事情から、簡単な設備で安価に汚水を浄化するこのできる方法の開発が望まれている。
【0004】
【課題を解決するための手段】
そこで、本出願人は次のような水の浄化システムを開発した。すなわち、本発明に係る水の浄化システムは、螺旋の中心軸が鉛直方向を向くように配置された螺旋状導管にバクテリアを含浸させた粒状の担体を充填し、当該導管の一方端から汚水を入れ他方端から取り出すように構成された水の浄化システムにおいて、前記螺旋状導管の内部を有孔プレートによって、ほぼ等間隔に複数の充填室に区切るとともに、当該複数の充填室に充填する前記担体の粒径を上流側の充填室から下流側の充填室にかけて順次小さくなるようにし、各充填室の上流側には担体投入口を設け、下流側には担体取出口を設け、これら投入口及び取出口には水密性を有する開閉扉を設けたことを特徴としている。
【0005】
導管の一方端から汚水を入れると、汚水は導管内の担体と担体の隙間を通って、導管の他方端側へ流れる。この間に、汚水に混じっている固定の汚濁物質が担体に濾し取られると共に、汚水に溶け込んでいる有機物等の汚濁物質はバクテリアによって分解される。これにより、導管の他方端からは、浄化された清浄な水が取り出される。
【0006】
導管が螺旋状であると、必要長さの導管を狭いスペースに配設することができ、しかも汚水の流れが円滑で澱みが生じないので、汚濁物質の濾過や分解が良好に行われる。また、螺旋の中心軸が鉛直方向を向くように導管を配置すると、汚水が自重で導管を流れるので、汚水を流すためのポンプが不要である。
【0007】
前記担体を、浄化しようとする汚水の採取現場で生じた汚泥を原料とする多孔質の焼成物で成形すると、バクテリアが成育増殖する環境として好条件が得られて好ましい。
【0008】
【発明の実施の形態】
以下、図面に表された実施の形態に基づき、本発明を具体的に説明する。
図1は本発明による水の浄化システムの設置状態を示す図であり、中心軸O−Oが鉛直方向を向く姿勢で螺旋状の導管1が設けられ、この導管1の上端開口部に汚水供給管2が接続され、下端開口部に排水管3が接続されている。
【0009】
導管1の内側には上流側から下流側にかけてほぼ等間隔の位置に3個の有孔プレート4が設けられており、導管1の内部はA,B,C,Dの4室に仕切られている。そして、各室にバクテリアを含浸させた粒状の担体5が充填されている。担体5の粒径は、最上流のA室のものが最も大きく、以下B室、C室、D室の順に小さくなっている。各有孔プレート4の孔径は、水は通すが担体5は通さないようになっている。また、各室A,B,C,Dに対応して、担体5を投入する投入口6a,6b,6c,6dと担体5を取り出す取出口7a,7b,7c,7dとがそれぞれ設けられている。これら投入口及び取出口には、水密性を有する開閉扉が付けられている。
【0010】
担体5は、浄化しようとする汚水の採取現場で生じた汚泥を原料とするセラミック、ゼオライト等の焼成物であって、図2の拡大断面図に示すような多孔質の構造している。このため、担体5にバクテリア溶液を含浸させると、バクテリアが担体5の空孔5aに入り込んで、担体5がバクテリアの良好な増殖床となる。担体5は浄化しようとする汚水の採取現場で生じた汚泥を原料としているので、バクテリアが成育増殖する環境として好条件である。また、汚泥を利用することで、汚泥の量を減少させ、汚泥の処理を軽減させるのにも役立つ。なお、担体5にバクテリア溶液を含浸するのは、バクテリアの活力を維持するために、使用する直前に行うのがよい。
【0011】
担体5に含浸させるバクテリアの種類は、処理する水に含まれる汚染物質の種類に応じて適当なものを選択するとよい。例えば、好気性のバクテリアと嫌気性のバクテリアとを併用すると効果的である。その場合、担体5が多孔質の構造であると、好気性のバクテリアは担体5の表面部や空孔5aの入口付近で生息し、嫌気性のバクテリアは空孔5aの奥深くで生息するというように棲み分けが得られるので好都合である。また、有機物以外の特性物質、例えば環境ホルモンやダイオキシンを分解するバクテリアを使用してもよい。
【0012】
バクテリアを含浸させた担体5を導管1に充填して、汚水供給管2より導管1に汚水を供給すると、汚水はA室、B室、C室、D室を順に通過し、その間に汚水に混じっている固定の汚濁物質が担体5に濾し取られる。また、汚水に溶け込んでいる有機物等の汚濁物質はバクテリアによって分解される。これにより、排水管3には、浄化された清浄な水が取り出される。濾し取った固定の汚濁物質や担体5の表面から剥離したバクテリアの膜等によって充填されている担体5が目詰まりの状態となれば、投入口6a,6b,6c,6d及び取出口7a,7b,7c,7dを利用して新しい担体5と交換すればよい。
【0013】
また、上記実施の形態では、中心軸O−Oが鉛直方向を向く姿勢で螺旋状の導管1を配置して、汚水が自重で導管を流れるようにすることで、汚水を流すためのポンプを不要にしているが、中心軸O−Oが水平方向よりも僅かに傾く姿勢で導管1を配置してもよく、この場合は傾斜度合いに応じてゆっくりと汚水の処理を行うことができる。
【0014】
【発明の効果】
以上に説明したように、本発明にかかる水の浄化システムは、螺旋状導管の一方端から汚水を入れると、汚水は有孔プレートで区切られた各充填室を順に通過し、当該充填室に充填する担体の粒径を上流側の充填室から下流側の充填室にかけて順次小さくなるようにしているので、その間に汚水に混じっている固定の汚濁物質が大きいものから順次担体に濾し取られる。また、汚水に溶け込んでいる有機物等の汚濁物質はバクテリアによって分解され、排水管には、浄化された清浄な水が取り出されるという機能を発揮する。濾し取った固定の汚濁物質や担体の表面から剥離したバクテリアの膜等によって充填されている担体が目詰まりの状態となれば、投入口及び取出口を利用して新しい担体と容易に交換することができる。しかも導管が螺旋状であるため、必要長さの導管を狭いスペースに配設することができ、汚水の流れが円滑で澱みが生じないので、汚濁物質の濾過や分解が良好に行われ、また、螺旋の中心軸が鉛直方向を向いているため、汚水が自重で導管を流れ、汚水を流すためのポンプが不要であり曝気が必要でなくなり、設備が簡単で、狭くスペースに設置することができ、しかも維持費があまりかからないシステムとなる。
【図面の簡単な説明】
【図1】水の浄化システムの設置状態を示す図である。
【図2】担体の拡大断面図である。
【符号の説明】
1 導管
2 汚水供給管
3 排水管
5 担体
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a water purification system used for purifying sewage containing organic pollutants such as sewage.
[0002]
[Prior art]
Conventionally, methods for decomposing pollutants by bacteria have been widely used to purify wastewater containing organic pollutants, and representative examples include an activated sludge method and a biofilm method.
[0003]
[Problems to be solved by the invention]
These conventional methods have a problem in that they require complicated equipment including a processing tank, piping and the like and a large space, and the aeration needs to be performed continuously, so that the running cost is high. Under such circumstances, development of a method capable of purifying sewage at low cost with simple equipment is desired.
[0004]
[Means for Solving the Problems]
Therefore, the present applicant has developed the following water purification system. That is, in the water purification system according to the present invention, a spiral conduit arranged so that the central axis of the spiral is oriented in the vertical direction is filled with a granular carrier impregnated with bacteria, and sewage is discharged from one end of the conduit. In the water purification system configured to be taken out from the other end, the carrier is divided into a plurality of filling chambers at approximately equal intervals by a perforated plate and filled in the plurality of filling chambers. The particle diameter of each of the filling chambers gradually decreases from the upstream filling chamber to the downstream filling chamber, and a carrier inlet is provided on the upstream side of each filling chamber, and a carrier outlet is provided on the downstream side. The outlet is characterized by providing a watertight door.
[0005]
When sewage is introduced from one end of the conduit, the sewage flows through the gap between the carrier in the conduit and the other end of the conduit. During this time, the fixed pollutant mixed in the sewage is filtered by the carrier, and the pollutant such as organic matter dissolved in the sewage is decomposed by bacteria. Thereby, the purified clean water is taken out from the other end of the conduit.
[0006]
When the conduit is spiral, the conduit having the required length can be disposed in a narrow space, and the flow of sewage is smooth and does not cause stagnation, so that the contaminants are filtered and decomposed satisfactorily. In addition, when the conduit is arranged so that the central axis of the spiral is oriented in the vertical direction, the sewage flows through the conduit under its own weight, so that a pump for flowing the sewage is unnecessary.
[0007]
Forming the carrier with a porous fired product made from sludge generated at the site of collecting the sewage to be purified is preferable because favorable conditions can be obtained as an environment in which bacteria grow and proliferate.
[0008]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, the present invention will be described in detail based on the embodiments shown in the drawings.
FIG. 1 is a diagram showing an installation state of a water purification system according to the present invention, in which a spiral conduit 1 is provided with a central axis OO oriented in a vertical direction, and sewage is supplied to an upper end opening of the conduit 1. A pipe 2 is connected, and a drain pipe 3 is connected to the lower end opening.
[0009]
Inside the conduit 1, three perforated plates 4 are provided at substantially equal intervals from the upstream side to the downstream side, and the interior of the conduit 1 is partitioned into four chambers A, B, C, and D. Yes. Each chamber is filled with a granular carrier 5 impregnated with bacteria. The particle size of the carrier 5 is the largest in the uppermost A chamber, and the smaller the B chamber, the C chamber, and the D chamber. The hole diameter of each perforated plate 4 allows water to pass but not the carrier 5. Corresponding to each of the chambers A, B, C and D, there are provided inlets 6a, 6b, 6c and 6d for inserting the carrier 5 and outlets 7a, 7b, 7c and 7d for taking out the carrier 5, respectively. Yes. These inlets and outlets are provided with watertight doors.
[0010]
The carrier 5 is a fired product of ceramic, zeolite, or the like made from sludge generated at the collection site of the sewage to be purified, and has a porous structure as shown in the enlarged sectional view of FIG. For this reason, when the carrier 5 is impregnated with the bacterial solution, the bacteria enter the pores 5a of the carrier 5, and the carrier 5 becomes a good growth bed of bacteria. Since the carrier 5 is made of sludge generated at the site of collecting the sewage to be purified, it is a favorable condition as an environment in which bacteria grow and proliferate. Moreover, by using sludge, the amount of sludge is reduced and it is useful also to reduce the treatment of sludge. The carrier 5 is preferably impregnated with a bacterial solution immediately before use in order to maintain the vitality of the bacteria.
[0011]
The type of bacteria impregnated in the carrier 5 may be selected appropriately depending on the type of contaminant contained in the water to be treated. For example, it is effective to use aerobic bacteria and anaerobic bacteria together. In that case, if the carrier 5 has a porous structure, aerobic bacteria live near the surface of the carrier 5 and near the entrance of the holes 5a, and anaerobic bacteria live deep inside the holes 5a. This is convenient because it can be divided into two categories. Moreover, you may use the characteristic substances other than organic substance, for example, bacteria which decompose | disassemble environmental hormones and dioxin.
[0012]
When the carrier 5 impregnated with bacteria is filled in the conduit 1 and the sewage is supplied to the conduit 1 from the sewage supply pipe 2, the sewage passes through the A chamber, the B chamber, the C chamber, and the D chamber in that order. The mixed fixed contaminants are filtered out on the carrier 5. In addition, pollutants such as organic matter dissolved in the sewage are decomposed by bacteria. Thereby, the purified water which was purified is taken out to the drain pipe 3. If the carrier 5 filled with the fixed contaminants filtered out or the bacterial film peeled off from the surface of the carrier 5 becomes clogged, the inlets 6a, 6b, 6c, 6d and the outlets 7a, 7b 7c, 7d may be replaced with a new carrier 5.
[0013]
Moreover, in the said embodiment, the pump for flowing sewage is arrange | positioned by arrange | positioning the helical conduit | pipe 1 with the attitude | position in which the central axis OO faces a perpendicular direction, and letting sewage flow through a conduit | pipe with dead weight. Although not required, the conduit 1 may be arranged in a posture in which the central axis OO is slightly inclined with respect to the horizontal direction. In this case, wastewater can be treated slowly according to the degree of inclination.
[0014]
【The invention's effect】
As described above, in the water purification system according to the present invention, when sewage is introduced from one end of the spiral conduit, the sewage sequentially passes through the respective filling chambers partitioned by the perforated plate, and enters the filling chamber. Since the particle size of the carrier to be filled is gradually reduced from the upstream filling chamber to the downstream filling chamber, the fixed contaminants mixed in the sewage during that period are sequentially filtered from the largest to the carrier. Moreover, pollutants such as organic matter dissolved in the sewage are decomposed by bacteria, and the drainage pipe has a function of taking out purified clean water. If the carrier filled with fixed contaminants filtered out or bacterial membranes peeled off from the surface of the carrier becomes clogged, it can be easily replaced with a new carrier using the inlet and outlet. Can do. Moreover, since the conduit is spiral, the required length of conduit can be arranged in a narrow space, and the flow of sewage is smooth and does not cause stagnation, so that contaminants are filtered and decomposed well. Because the central axis of the spiral is in the vertical direction, sewage flows through the conduit by its own weight, no pump is required to flow the sewage, aeration is not required, equipment is simple, and it can be installed in a narrow space This is a system that does not require much maintenance costs.
[Brief description of the drawings]
FIG. 1 is a diagram showing an installation state of a water purification system.
FIG. 2 is an enlarged cross-sectional view of a carrier.
[Explanation of symbols]
1 Conduit 2 Sewage supply pipe 3 Drain pipe 5 Carrier

Claims (1)

螺旋の中心軸が鉛直方向を向くように配置された螺旋状導管にバクテリアを含浸させた粒状の担体を充填し、当該導管の一方端から汚水を入れ他方端から取り出すように構成された水の浄化システムにおいて、前記螺旋状導管の内部を有孔プレートによって、ほぼ等間隔に複数の充填室に区切るとともに、当該複数の充填室に充填する前記担体の粒径を上流側の充填室から下流側の充填室にかけて順次小さくなるようにし、各充填室の上流側には担体投入口を設け、下流側には担体取出口を設け、これら投入口及び取出口には水密性を有する開閉扉を設けたことを特徴とする水の浄化システム A helical conduit placed so that the central axis of the spiral is oriented in the vertical direction is filled with a granular carrier impregnated with bacteria, and sewage is introduced from one end of the conduit and water is configured to be taken out from the other end . In the purification system, the inside of the spiral conduit is divided into a plurality of filling chambers at almost equal intervals by a perforated plate, and the particle size of the carrier filled in the plurality of filling chambers is set downstream from the upstream filling chamber. The carrier inlet is provided on the upstream side of each filling chamber, the carrier outlet is provided on the downstream side, and a watertight door is provided at the inlet and outlet. purification system for water, characterized in that the
JP2000238952A 2000-08-07 2000-08-07 Water purification system Expired - Lifetime JP4019209B2 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
JP2000238952A JP4019209B2 (en) 2000-08-07 2000-08-07 Water purification system
PCT/JP2001/011175 WO2003053866A1 (en) 2000-08-07 2001-12-20 Water clarifying system

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP2000238952A JP4019209B2 (en) 2000-08-07 2000-08-07 Water purification system
PCT/JP2001/011175 WO2003053866A1 (en) 2000-08-07 2001-12-20 Water clarifying system

Publications (2)

Publication Number Publication Date
JP2002045878A JP2002045878A (en) 2002-02-12
JP4019209B2 true JP4019209B2 (en) 2007-12-12

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WO (1) WO2003053866A1 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4019209B2 (en) * 2000-08-07 2007-12-12 株式会社ソナー Water purification system
WO2005019119A1 (en) * 2003-08-23 2005-03-03 Moo-Won Byun Pipe type water treatment apparatus and water treatment system using the same
JP2011050902A (en) * 2009-09-03 2011-03-17 Toshiba Corp Water treatment system for sewage
CN102092839B (en) * 2010-12-07 2012-07-04 江苏苏净集团有限公司 Compact supporting filler
CN104529050B (en) * 2014-11-25 2016-11-30 浙江浙牌科技有限公司 Efficiently country sewage purifier

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6325198U (en) * 1986-07-31 1988-02-19
JPH078978A (en) * 1993-06-25 1995-01-13 Matsushita Electric Works Ltd Waste water treatment apparatus
JPH10137776A (en) * 1996-11-08 1998-05-26 Yamaguchi Yukio Sewage treating device and treated water storage tank
JP2001047077A (en) * 1999-08-16 2001-02-20 Matsushita Electric Ind Co Ltd Carbide biological filter bed, its production thereof and biological cleaning treatment apparatus using the carbide biological filter bed
JP4019209B2 (en) * 2000-08-07 2007-12-12 株式会社ソナー Water purification system
JP3082931U (en) * 2001-05-24 2002-01-11 宗一 前田 Soil purification material using useful microorganisms and porous sludge fired ceramics

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