JP3408199B2 - Organic wastewater treatment apparatus and assembling method thereof - Google Patents
Organic wastewater treatment apparatus and assembling method thereofInfo
- Publication number
- JP3408199B2 JP3408199B2 JP18198899A JP18198899A JP3408199B2 JP 3408199 B2 JP3408199 B2 JP 3408199B2 JP 18198899 A JP18198899 A JP 18198899A JP 18198899 A JP18198899 A JP 18198899A JP 3408199 B2 JP3408199 B2 JP 3408199B2
- Authority
- JP
- Japan
- Prior art keywords
- tank
- treatment
- treatment tank
- biological treatment
- reaction tank
- 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 - Fee Related
Links
- 238000004065 wastewater treatment Methods 0.000 title claims description 13
- 238000000034 method Methods 0.000 title claims description 11
- 238000011282 treatment Methods 0.000 claims description 205
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 75
- 238000006243 chemical reaction Methods 0.000 claims description 70
- 239000010865 sewage Substances 0.000 claims description 53
- 239000012528 membrane Substances 0.000 claims description 38
- 238000000926 separation method Methods 0.000 claims description 37
- 239000002351 wastewater Substances 0.000 claims description 33
- 239000010802 sludge Substances 0.000 claims description 27
- 238000005273 aeration Methods 0.000 claims description 12
- 238000007599 discharging Methods 0.000 claims description 8
- 238000005276 aerator Methods 0.000 claims description 5
- 238000000638 solvent extraction Methods 0.000 claims description 3
- 238000009434 installation Methods 0.000 description 5
- 238000010276 construction Methods 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- 239000003899 bactericide agent Substances 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 238000013019 agitation Methods 0.000 description 1
- 230000000844 anti-bacterial effect Effects 0.000 description 1
- 230000001276 controlling effect Effects 0.000 description 1
- 239000000645 desinfectant Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000003028 elevating effect Effects 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 238000011328 necessary treatment Methods 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
Classifications
-
- 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
Landscapes
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
- Activated Sludge Processes (AREA)
- Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
Description
【0001】[0001]
【発明の属する技術分野】本発明は、有機性汚水の処理
装置及びその組立方法に関し、構造が簡単で、かつ、設
置工事を短期間で行うことができるようにした、特に、
小規模な汚水処理場等に好適な有機性汚水の処理装置及
びその組立方法に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a device for treating organic wastewater and a method for assembling the same, which has a simple structure and enables installation work in a short period of time.
The present invention relates to an organic sewage treatment apparatus suitable for a small sewage treatment plant and the like, and an assembling method thereof.
【0002】[0002]
【従来の技術】従来、下水等の有機性の汚水(本明細書
において、単に「汚水」という。)は、原水から篩渣を
分離し、汚水処理場に設置された生物処理反応槽等の複
数の処理槽において、硝化、脱窒等の必要な処理を行っ
た後、河川等に放流するようにしている。2. Description of the Related Art Conventionally, organic sewage such as sewage (herein, simply referred to as "sewage") is used to separate a sieve residue from raw water and remove it from a biological treatment reaction tank installed in a sewage treatment plant. After performing necessary treatments such as nitrification and denitrification in a plurality of treatment tanks, they are discharged into a river or the like.
【0003】[0003]
【発明が解決しようとする課題】ところで、従来の汚水
処理場に設置される有機性汚水の処理設備は、大形で、
基本的には、汚水処理場において構築されるものである
ため、設置工事に専門的な技術を必要とするとともに、
工期が長くかかるという問題があった。特に、小規模な
汚水処理場の場合にも、有機性汚水の処理設備の構築に
は、中規模以上の汚水処理場と同様の構築方法が採用さ
れているため、設備の構築コストが上昇するという問題
があった。By the way, the conventional organic sewage treatment facility installed in the conventional sewage treatment plant is large in size,
Basically, it is constructed at a sewage treatment plant, so specialized technology is required for installation work, and
There was a problem that the construction period was long. In particular, even in the case of a small-scale sewage treatment plant, the construction method for organic sewage treatment facilities is the same as that for medium-sized or larger sewage treatment plants, so the construction cost of the facilities will increase. There was a problem.
【0004】本発明は、上記従来の汚水処理場における
有機性汚水の処理設備の有する問題点に鑑み、構造が簡
単で、かつ、設置工事を短期間で行うことができ、特
に、小規模な汚水処理場等に好適に用いることができる
有機性汚水の処理装置及びその組立方法を提供すること
を目的とする。The present invention has a simple structure and can be installed in a short period of time in view of the problems of the conventional organic sewage treatment equipment in the above-mentioned conventional sewage treatment plant, and in particular, it is a small scale. An object of the present invention is to provide an organic sewage treatment apparatus that can be suitably used in a sewage treatment plant and the like, and an assembly method thereof.
【0005】[0005]
【課題を解決するための手段】上記目的を達成するた
め、本発明の有機性汚水の処理装置は、流入する原水か
ら篩渣を分離し、汚水と篩渣とを個別に貯留する汚水貯
留槽及び篩渣等貯留槽を備えた第1処理槽と、膜分離ユ
ニットを配設した無終端周回水路からなる生物処理反応
槽を備えた第2処理槽とを、独立して配置するととも
に、第1処理槽と第2処理槽とを、汚水供給管を介して
接続するようにしたことを特徴とする。In order to achieve the above object, an organic wastewater treatment apparatus of the present invention is a wastewater storage tank for separating sieve residue from inflowing raw water and separately storing the wastewater and the sieve residue. And a first treatment tank having a storage tank for sieve residue and the like, and a second treatment tank having a biological treatment reaction tank consisting of an endless circulating water channel in which a membrane separation unit is arranged, and It is characterized in that the first treatment tank and the second treatment tank are connected via a waste water supply pipe.
【0006】そして、この有機性汚水の処理装置は、流
入する原水を汚水と篩渣とに分離し、個別に貯留する汚
水貯留槽及び篩渣等貯留槽を備えた第1処理槽と、内部
に膜分離ユニットを配設した無終端周回水路からなる生
物処理反応槽を備えた第2処理槽とを、分離した状態
で、それぞれトレーラ等によって陸上輸送できる外寸法
に工場で製造するとともに、陸上輸送した第1処理槽及
び第2処理槽を設置後、第1処理槽と第2処理槽とを、
配管を介して接続することにより組み立てることができ
る。This organic wastewater treatment apparatus is provided with a first treatment tank provided with a wastewater storage tank and a storage tank for sieve residue, which separates the inflowing raw water into wastewater and sieve residue and stores them separately. The second treatment tank, which has a biological treatment reaction tank consisting of an endless circulating water channel in which the membrane separation unit is installed, is manufactured in a factory in an external size that can be transported by land by a trailer, etc. After installing the transported first processing tank and second processing tank, the first processing tank and the second processing tank are
It can be assembled by connecting through piping.
【0007】この有機性汚水の処理装置及びその組立方
法は、流入する原水から篩渣を分離し、汚水と篩渣とを
個別に貯留する汚水貯留槽及び篩渣等貯留槽を備えた第
1処理槽と、膜分離ユニットを配設した無終端周回水路
からなる生物処理反応槽を備えた第2処理槽とを、独立
して構成するようにしているため、構造が簡単で、か
つ、第1処理槽及び第2処理槽を分離した状態で、それ
ぞれトレーラ等によって陸上輸送できるため、工場にお
いて基本的な部分を製造することができ、設置工事に専
門的な技術を必要とせず、設置工事を短期間で、低コス
トに行うことができる。This organic sewage treatment apparatus and its assembling method are provided with a first sewage storage tank for separating the sieve residue from the inflowing raw water and separately storing the sewage and the sieve residue, and a storage tank for the sieve residue and the like. Since the treatment tank and the second treatment tank having the biological treatment reaction tank composed of the endless circulating water channel in which the membrane separation unit is arranged are independently configured, the structure is simple and Since the 1st treatment tank and the 2nd treatment tank can be transported by land with a trailer or the like separately, the basic parts can be manufactured at the factory, and no specialized technology is required for the installation work. Can be performed in a short period of time and at low cost.
【0008】この場合において、第1処理槽と第2処理
槽とを、余剰汚泥引抜管を介して接続し、第2処理槽の
生物処理反応槽の余剰汚泥を第1処理槽の篩渣等貯留槽
へ導入、貯留するようにすることができる。In this case, the first treatment tank and the second treatment tank are connected via a surplus sludge drawing pipe, and the surplus sludge of the biological treatment reaction tank of the second treatment tank is treated with the sieve residue of the first treatment tank or the like. It can be introduced and stored in a storage tank.
【0009】これにより、第2処理槽の生物処理反応槽
において発生する余剰汚泥の貯留及び処理を、簡易な機
構の装置によって、トータル的に行うことができる。As a result, the storage and treatment of the excess sludge generated in the biological treatment reaction tank of the second treatment tank can be totally performed by the device having a simple mechanism.
【0010】また、第1処理槽の汚水貯留槽及び篩渣等
貯留槽に曝気機構を配設することができる。Further, an aeration mechanism can be provided in the waste water storage tank and the sieve residue storage tank of the first treatment tank.
【0011】これにより、第1処理槽の汚水貯留槽から
第2処理槽の生物処理反応槽に導入される汚水の生物処
理を円滑に行うことができるとともに、篩渣等貯留槽に
導入、貯留される篩渣及び余剰汚泥を好気処理し、腐敗
を防止することができる。Thus, the biological treatment of the sewage introduced into the biological treatment reaction tank of the second treatment tank from the sewage storage tank of the first treatment tank can be smoothly performed, and at the same time, it is introduced into and stored in the storage tank such as sieve residue. The screen residue and excess sludge to be treated can be aerobically treated to prevent spoilage.
【0012】また、第2処理槽の生物処理反応槽には、
攪拌機及び曝気機構を配設したり、スクリュー式曝気機
を配設することができる。Further, in the biological treatment reaction tank of the second treatment tank,
A stirrer and an aeration mechanism may be provided, or a screw type aerator may be provided.
【0013】これにより、無終端周回水路からなる生物
処理反応槽内を間欠的(時間的又は位置的)に好気又は
嫌気状態にして、汚水の生物処理、すなわち、硝化、脱
窒を円滑に行うための循環水流の流速等の環境を容易に
整えることができる。As a result, the inside of the biological treatment reaction tank consisting of the endless circulating water channel is intermittently (temporally or positionally) aerobically or anaerobically made to smoothly perform biological treatment of wastewater, that is, nitrification and denitrification. The environment such as the flow velocity of the circulating water flow for performing can be easily adjusted.
【0014】また、第2処理槽の生物処理反応槽の中央
部に膜分離ユニットを配設して区画することにより、無
終端周回水路を形成することができる。Further, by arranging and partitioning the membrane separation unit in the center of the biological treatment reaction tank of the second treatment tank, it is possible to form an endless circulating water channel.
【0015】これにより、第2処理槽の生物処理反応槽
の無終端周回水路を簡易に形成することができる。Thus, the endless circulating water channel of the biological treatment reaction tank of the second treatment tank can be easily formed.
【0016】また、第2処理槽の生物処理反応槽の膜分
離ユニットから処理水を排出する処理水排出管の出口側
端部を、生物処理反応槽の水位より低い位置で開放水面
の位置を任意に調節可能な水位調整手段を配設した排水
調整槽に浸漬するようにすることができる。Further, the outlet side end of the treated water discharge pipe for discharging treated water from the membrane separation unit of the biological treatment reaction tank of the second treatment tank is set at a position lower than the water level of the biological treatment reaction tank and at the position of the open water surface. It can be immersed in a drainage adjusting tank provided with a water level adjusting means that can be adjusted arbitrarily.
【0017】これにより、第2処理槽の生物処理反応槽
の膜分離ユニットから処理水を、生物処理反応槽と排水
調整槽間の水頭差を利用して無動力で安定して排出する
ことができる。As a result, the treated water can be stably discharged from the membrane separation unit of the biological treatment reaction tank of the second treatment tank without power by utilizing the head difference between the biological treatment reaction tank and the drainage adjustment tank. it can.
【0018】また、第2処理槽の生物処理反応槽の膜分
離ユニットから処理水を排出する処理水排出管に吸引ポ
ンプを介在したバイパス管を並設することができる。Further, a bypass pipe having a suction pump may be provided in parallel with a treated water discharge pipe for discharging treated water from the membrane separation unit of the biological treatment reaction tank of the second treatment tank.
【0019】これにより、装置の作動開始時、その他非
常時に、第2処理槽の生物処理反応槽から、膜分離ユニ
ットを介して、処理水を強制的に排出することができ
る。As a result, the treated water can be forcibly discharged from the biological treatment reaction tank of the second treatment tank via the membrane separation unit at the start of operation of the apparatus or in other emergency.
【0020】また、第1処理槽及び第2処理槽の外寸法
を、高さを3m以下、幅を2.5m以下、長さを6m以
下に形成することができる。The outer dimensions of the first and second processing baths can be formed so that the height is 3 m or less, the width is 2.5 m or less, and the length is 6 m or less.
【0021】これにより、第1処理槽及び第2処理槽を
分離した状態で、規制を受けることなく、それぞれトレ
ーラ等によって陸上輸送できる。As a result, the first processing tank and the second processing tank can be transported by land without a restriction by a trailer or the like in a separated state.
【0022】[0022]
【発明の実施の形態】以下、本発明の有機性汚水の処理
装置及びその組立方法の実施の形態を図面に基づいて説
明する。BEST MODE FOR CARRYING OUT THE INVENTION Embodiments of an organic sewage treatment apparatus and an assembling method thereof according to the present invention will be described below with reference to the drawings.
【0023】図1〜図3に、本発明の有機性汚水の処理
装置の第1実施例を示す。この有機性汚水の処理装置
は、汚水処理場に流入する原水から篩渣を分離し、汚水
と篩渣とを個別に貯留する汚水貯留槽A1及び篩渣等貯
留槽A2を備えた第1処理槽Aと、膜分離ユニット9を
配設した無終端周回水路からなる生物処理反応槽B1及
び開放水面の位置を任意に調節可能な水位調整手段12
を配設した排水調整槽B2を備えた第2処理槽Bとを、
独立して配置するとともに、第1処理槽Aと第2処理槽
Bとを、汚水供給管7及び余剰汚泥引抜管8を介して接
続するようにして構成するようにする。1 to 3 show a first embodiment of the organic sewage treatment apparatus of the present invention. This organic sewage treatment apparatus includes a sewage storage tank A1 that separates sieve residue from raw water flowing into a sewage treatment plant, and separately stores the sewage and the sieve residue, and a first treatment provided with a storage tank A2 such as a sieve residue. A tank A, a biological treatment reaction tank B1 composed of an endless circulating water channel in which a membrane separation unit 9 is arranged, and a water level adjusting means 12 capable of arbitrarily adjusting the positions of the open water surface
A second treatment tank B having a drainage adjusting tank B2 in which
The first treatment tank A and the second treatment tank B are arranged independently of each other and are connected to each other through the waste water supply pipe 7 and the excess sludge drawing pipe 8.
【0024】この第1処理槽Aと第2処理槽Bとは、図
5及び図6に示すように、分離した状態で、それぞれト
レーラT等によって陸上輸送できる外寸法に工場でユニ
ットとして製造するとともに、それぞれトレーラT等に
よって汚水処理場まで陸上輸送した第1処理槽A及び第
2処理槽Bを、汚水処理場に設置後、第1処理槽Aと第
2処理槽Bとを、汚水供給管7及び余剰汚泥引抜管8を
介して接続することにより、組み立てるようにする。こ
のトレーラにて搬入する場合を図5、図6に示している
が、他の搬送方法でも行える。そして、第1処理槽A及
び第2処理槽Bを分離した状態で、規制を受けることな
く、それぞれトレーラT等によって陸上輸送できるよう
に、第1処理槽A及び第2処理槽Bの外寸法を、高さを
3m以下、幅を2.5m以下、長さを6m以下に形成す
るようにする。As shown in FIGS. 5 and 6, the first processing tank A and the second processing tank B are manufactured as a unit in a factory in a separated state so that they can be transported by land by a trailer T or the like. At the same time, after installing the first treatment tank A and the second treatment tank B, which were respectively transported by land to the wastewater treatment plant by the trailer T or the like, at the wastewater treatment plant, the first treatment tank A and the second treatment tank B are supplied to the wastewater. The pipe 7 and the excess sludge drawing pipe 8 are connected to each other to be assembled. The case of carrying in with this trailer is shown in FIGS. 5 and 6, but other carrying methods can be used. The outer dimensions of the first processing tank A and the second processing tank B are separated so that the first processing tank A and the second processing tank B can be transported by land by a trailer T or the like without being regulated. To have a height of 3 m or less, a width of 2.5 m or less, and a length of 6 m or less.
【0025】第1処理槽Aは、汚水と篩渣とを個別に貯
留する汚水貯留槽A1及び篩渣等貯留槽A2を備え、汚
水処理場に流入する原水からスクリーン1により篩渣を
分離した汚水を汚水貯留槽A1に一時的に貯留し、第2
処理槽Bの生物処理反応槽B1に対する汚水供給管7を
介する汚水の供給量を調整するようにするとともに、ス
クリーン1により分離した篩渣及び余剰汚泥引抜管8を
介して導入される第2処理槽Bの生物処理反応槽B1か
らの余剰汚泥を篩渣等貯留槽A2に貯留するようにす
る。なお、汚水貯留槽A1と篩渣等貯留槽A2の容積比
は、一時的に貯留する汚水量並びに発生する篩渣量及び
余剰汚泥量等により適当に定められる。The first treatment tank A comprises a wastewater storage tank A1 for separately storing wastewater and sieve residue and a storage tank A2 for sieve residue etc., and the screen residue is separated by a screen 1 from the raw water flowing into the wastewater treatment plant. The wastewater is temporarily stored in the wastewater storage tank A1, and the second
The second treatment, in which the amount of sewage supplied through the sewage supply pipe 7 to the biological treatment reaction tank B1 of the treatment tub B is adjusted, and which is introduced through the screen residue separated by the screen 1 and the excess sludge drawing pipe 8. The surplus sludge from the biological treatment reaction tank B1 in the tank B is stored in the storage tank A2 such as sieve residue. The volume ratio between the waste water storage tank A1 and the sieve residue storage tank A2 is appropriately determined depending on the amount of waste water temporarily stored, the amount of generated sieve residue and the amount of excess sludge, and the like.
【0026】第1処理槽Aの汚水貯留槽A1及び篩渣等
貯留槽A2には、槽底部に、曝気機構としての散気管
2,3を配設し、ブロア4からの送気にて曝気を行うよ
うにする。これにより、第1処理槽Aの汚水貯留槽A1
から第2処理槽Bの生物処理反応槽B1に導入される汚
水の生物処理を円滑に行うことができるとともに、篩渣
等貯留槽B2に導入、貯留される篩渣及び余剰汚泥を好
気処理し、腐敗を防止することができる。In the wastewater storage tank A1 and the screen residue storage tank A2 of the first treatment tank A, air diffusers 2 and 3 as an aeration mechanism are provided at the bottom of the tank, and aeration is carried out from the blower 4. To do. Thereby, the wastewater storage tank A1 of the first treatment tank A
The biological treatment of sewage introduced into the biological treatment reaction tank B1 of the second treatment tank B can be smoothly performed, and the sieve residue and excess sludge introduced and stored in the storage tank B2 for a sieve residue are aerobically treated. And prevent corruption.
【0027】また、第1処理槽Aの汚水貯留槽A1内に
は、流量調整ポンプ5を1台又は2台以上(本実施例に
おいては2台)設置し、この流量調整ポンプ5にて揚水
された汚水を、定流量計量槽6を介在した汚水供給管7
を介して、第2処理槽Bの生物処理反応槽B1に供給す
るようにする。この場合、第2処理槽Bの生物処理反応
槽B1の水位が一定に保たれ、生物処理が円滑に行われ
るように、定流量計量槽6を制御しながら、汚水を供給
するようにする。これにより、汚水処理場に流入する原
水の流入量の変動を吸収し、第2処理槽Bの生物処理反
応槽B1における生物処理を円滑に行うことができるも
のとなる。Further, in the wastewater storage tank A1 of the first treatment tank A, one or two or more (two in this embodiment) flow rate adjusting pumps 5 are installed, and the flow rate adjusting pumps 5 pump water. The collected sewage is supplied to a sewage supply pipe 7 with a constant flow rate measuring tank 6 interposed.
To the biological treatment reaction tank B1 of the second treatment tank B via. In this case, sewage is supplied while controlling the constant flow rate measurement tank 6 so that the water level of the biological treatment reaction tank B1 of the second treatment tank B is kept constant and biological treatment is smoothly performed. This makes it possible to absorb fluctuations in the amount of raw water flowing into the sewage treatment plant and smoothly perform biological treatment in the biological treatment reaction tank B1 of the second treatment tank B.
【0028】第2処理槽Bの生物処理反応槽B1におい
て発生する余剰汚泥は、余剰汚泥引抜弁15を備えた余
剰汚泥引抜管7を介して、第1処理槽Aの篩渣等貯留槽
A2に導入するようにする。これにより、第2処理槽B
の生物処理反応槽B1において発生する余剰汚泥を引き
抜き、生物処理反応槽B1の汚泥濃度を適正値に調整し
て、生物処理を連続的に安定して行うことができるとと
もに、引き抜いた汚泥を、篩渣等貯留槽A2に導入、貯
留するとともに、余剰汚泥を好気処理することができ
る。Excess sludge generated in the biological treatment reaction tank B1 of the second treatment tank B is passed through a surplus sludge drawing pipe 7 equipped with a surplus sludge drawing valve 15 to store a sieve residue etc. tank A2 of the first processing tank A. To be introduced into. As a result, the second processing tank B
The excess sludge generated in the biological treatment reaction tank B1 is removed, the sludge concentration in the biological treatment reaction tank B1 is adjusted to an appropriate value, and the biological treatment can be continuously and stably performed. The excess sludge can be aerobically treated while being introduced and stored in the storage tank A2 such as sieve residue.
【0029】第2処理槽Bは、膜分離ユニット9を配設
した無終端周回水路からなる生物処理反応槽B1及び開
放水面の位置を任意に調節可能な水位調整手段12を配
設した排水調整槽B2を備え、第1処理槽Aの汚水貯留
槽A1から導入される汚水を、オキシデーションディッ
チとなる無終端周回水路として形成した生物処理反応槽
B1において生物処理を行うようにするとともに、生物
処理反応槽B1に配設した膜分離ユニット9により汚泥
を除去した処理水を、処理水排出管14を介して、生物
処理反応槽B1と排水調整槽B2間の水頭差を利用して
無動力で排水調整槽B2に排出するようにする。The second treatment tank B comprises a biological treatment reaction tank B1 consisting of an endless circulating water channel in which the membrane separation unit 9 is arranged and a water level adjusting means 12 in which the position of the open water surface can be arbitrarily adjusted. A biological treatment reaction tank B1 that is equipped with a tank B2 and is formed as an endless circulating water channel that serves as an oxidation ditch is used to perform biological treatment of the sewage introduced from the sewage storage tank A1 of the first treatment tank A. The treated water from which sludge has been removed by the membrane separation unit 9 arranged in the treatment reaction tank B1 is non-powered through the treated water discharge pipe 14 by utilizing the head difference between the biological treatment reaction tank B1 and the drainage adjustment tank B2. To be discharged into the drainage adjusting tank B2.
【0030】生物処理反応槽B1は、特に限定されるも
のではないが、生物処理反応槽B1の中央部に膜分離ユ
ニット9を配設し、膜分離ユニット9の中央側の周壁9
1の上端部が水面上に位置し、下端部が生物処理反応槽
B1の底部に接するように膜分離ユニット9を形成する
ことにより、生物処理反応槽B1の中央部を区画し、こ
れによりより、無終端周回水路を簡易に形成することが
できる。The biological treatment reaction tank B1 is not particularly limited, but the membrane separation unit 9 is arranged in the central portion of the biological treatment reaction tank B1, and the peripheral wall 9 on the central side of the membrane separation unit 9 is disposed.
By forming the membrane separation unit 9 so that the upper end of 1 is located on the water surface and the lower end is in contact with the bottom of the biological treatment reaction tank B1, the central portion of the biological treatment reaction tank B1 is partitioned, and The endless circulating water channel can be easily formed.
【0031】膜分離ユニット9は、膜分離ユニット9と
生物処理反応槽B1の底部との間に形成された隙間92
から流入する汚水を、膜分離により濾過することによ
り、汚泥を含まない状態の処理水を、処理水排出管14
を介して排水調整槽B2に排出することができるように
したもので、膜分離ユニット9と生物処理反応槽B1の
底部との間に形成された隙間92には、散気管10を配
設して、ブロア4から送気することにより、膜分離ユニ
ット9の膜面洗浄と曝気を行うようにする。The membrane separation unit 9 has a gap 92 formed between the membrane separation unit 9 and the bottom of the biological treatment reaction tank B1.
The sewage flowing in from the sewage is filtered by membrane separation, so that the treated water without sludge is treated as a treated water discharge pipe 14
The air diffuser 10 is disposed in the gap 92 formed between the membrane separation unit 9 and the bottom of the biological treatment reaction tank B1. Then, air is blown from the blower 4 so that the membrane surface of the membrane separation unit 9 is cleaned and aerated.
【0032】この膜分離ユニット9は、ユニット化して
構成し、生物処理反応槽B1の容量、膜分離ユニット9
の処理能力等に応じて、1台又は2台以上(本実施例に
おいては2台)設置するようにする。The membrane separation unit 9 is constructed as a unit, and the capacity of the biological treatment reaction tank B1 and the membrane separation unit 9 are
Depending on the processing capacity and so on, one unit or two or more units (two units in this embodiment) are installed.
【0033】この膜分離ユニット9によって濾過された
処理水を排出する処理水排出管14は、その出口側端部
を、生物処理反応槽B1の水位より低い位置で開放水面
の位置を任意に調節可能な水位調整手段12を配設した
排水調整槽B2に浸漬するようにする。この水位調整手
段12は、本実施例においては、排水調整槽B2内に有
底の水位調整用タンク13を、任意の昇降機構(図示省
略)によって昇降可能に配設し、この水位調整用タンク
13内に、処理水排出管14の出口側端部を挿入、浸漬
するようにする。この場合、処理水排出管14の出口側
端部が、生物処理反応槽B1の水面位置よりも低くなる
ようにし、これにより、生物処理反応槽B1の膜分離ユ
ニット9によって濾過された処理水を、生物処理反応槽
9の水面位置と排水調整槽B2の水位調整用タンク13
の水面位置間の水頭差△hを利用して無動力で安定して
排出することができるようにする。The treated water discharge pipe 14 for discharging the treated water filtered by the membrane separation unit 9 has its outlet end portion adjusted to a position lower than the water level of the biological treatment reaction tank B1 and the position of the open water surface arbitrarily. It is soaked in a drainage adjusting tank B2 provided with a possible water level adjusting means 12. In this embodiment, the water level adjusting means 12 has a bottomed water level adjusting tank 13 in a drainage adjusting tank B2 which is vertically movable by an arbitrary elevating mechanism (not shown). The outlet side end of the treated water discharge pipe 14 is inserted into 13 and immersed therein. In this case, the outlet side end of the treated water discharge pipe 14 is made lower than the water surface position of the biological treatment reaction tank B1, whereby the treated water filtered by the membrane separation unit 9 of the biological treatment reaction tank B1 can be treated. , The water surface position of the biological treatment reaction tank 9 and the water level adjusting tank 13 of the drainage adjusting tank B2
By using the water head difference Δh between the water surface positions, it is possible to stably discharge without power.
【0034】この水位調整手段12としては、図4に示
す本発明の第2実施例の有機性汚水の処理装置のよう
に、可動堰19等、任意の方法を採用することができ
る。そして、可動堰19により排水調整槽B2の水面位
置を任意に調節するようにした場合には、排水調整槽B
2に処理水排出管14の出口側端部を直接挿入、浸漬す
るようにする。As the water level adjusting means 12, an arbitrary method such as a movable weir 19 can be adopted as in the organic wastewater treatment apparatus of the second embodiment of the present invention shown in FIG. When the water surface position of the drainage adjusting tank B2 is arbitrarily adjusted by the movable weir 19, when the drainage adjusting tank B2 is adjusted.
The end portion on the outlet side of the treated water discharge pipe 14 is directly inserted into and immersed in 2.
【0035】また、膜分離ユニット9によって濾過され
た処理水を排出する処理水排出管14に、吸引ポンプ1
1を介在したバイパス管21を並設するようにする。こ
れにより、装置の作動開始時、その他非常時に、第2処
理槽Bの生物処理反応槽B1から、膜分離ユニット9を
介して、処理水を強制的に排出することができる。The suction pump 1 is attached to the treated water discharge pipe 14 for discharging the treated water filtered by the membrane separation unit 9.
Bypass pipes 21 with 1 interposed are arranged side by side. As a result, the treated water can be forcibly discharged from the biological treatment reaction tank B1 of the second treatment tank B via the membrane separation unit 9 at the start of operation of the apparatus or in other emergency.
【0036】そして、排水調整槽B2から排出された処
理水は、殺菌剤添加槽20に導入され、殺菌剤添加器2
0aから必要量の殺菌剤を供給して基準値まで殺菌した
後、河川等に放流する。この場合、処理水排出管14
に、殺菌剤添加器14aを接続することもできる。Then, the treated water discharged from the drainage adjusting tank B2 is introduced into the bactericidal agent adding tank 20, and the bactericidal agent adding device 2
The necessary amount of bactericide is supplied from 0a to sterilize to a standard value, and then discharged into a river or the like. In this case, the treated water discharge pipe 14
It is also possible to connect the sterilizer addition device 14a.
【0037】また、第2処理槽Bの無終端周回水路から
なる生物処理反応槽B1内を間欠的(時間的又は位置
的)に好気又は嫌気状態にして、有機性汚水の生物処
理、すなわち、硝化、脱窒を円滑に行うための循環水流
の流速(例えば、生物処理反応槽B1の底部の流速:1
0cm/sec以上)等の環境を整えるようにするため
に、生物処理反応槽B1には、攪拌・曝気機構を配設す
るようにする。この攪拌・曝気機構は、図1〜図3に示
す第1実施例の有機性汚水の処理装置においては、生物
処理反応槽B1の底部に配設した攪拌機17及びブロア
4に接続された散気管16からなる曝気機構で以て構成
するようにしているが、これに限定されず、例えば、図
4に示す第2実施例の有機性汚水の処理装置のように、
スクリュー式曝気機22で以て構成することができる。Further, the inside of the biological treatment reaction tank B1 consisting of the endless circulating water channel of the second treatment tank B is intermittently (temporally or positionally) aerobically or anaerobically set to perform biological treatment of the organic wastewater, that is, , The flow velocity of the circulating water flow for smoothly performing nitrification and denitrification (for example, the flow velocity at the bottom of the biological treatment reaction tank B1: 1
In order to prepare an environment such as 0 cm / sec or more), the biological treatment reaction tank B1 is provided with a stirring / aeration mechanism. This agitation / aeration mechanism, in the organic wastewater treatment apparatus of the first embodiment shown in FIGS. 1 to 3, is an aeration pipe connected to an agitator 17 and a blower 4 arranged at the bottom of the biological treatment reaction tank B1. Although it is configured by the aeration mechanism consisting of 16, it is not limited to this, and, for example, like the organic wastewater treatment apparatus of the second embodiment shown in FIG.
It can be configured with a screw type aerator 22.
【0038】なお、第2実施例の有機性汚水の処理装置
のその他の構成は、上記第1実施例の有機性汚水の処理
装置と同様である。The other construction of the organic wastewater treatment apparatus of the second embodiment is the same as that of the organic wastewater treatment apparatus of the first embodiment.
【0039】[0039]
【発明の効果】本発明の有機性汚水の処理装置及びその
組立方法によれば、流入する原水から篩渣を分離し、汚
水と篩渣とを個別に貯留する汚水貯留槽及び篩渣等貯留
槽を備えた第1処理槽と、膜分離ユニットを配設した無
終端周回水路からなる生物処理反応槽を備えた第2処理
槽とを、独立して構成するようにしているため、構造が
簡単で、かつ、第1処理槽及び第2処理槽を分離した状
態で、それぞれトレーラ等によって陸上輸送できるた
め、工場において基本的な部分を製造することができ、
設置工事に専門的な技術を必要とせず、設置工事を短期
間で、低コストに行うことができ、特に、小規模な汚水
処理場等に好適な有機性汚水の処理装置及びその組立方
法を提供することができる。EFFECT OF THE INVENTION According to the apparatus for treating organic wastewater and the method for assembling the same of the present invention, a wastewater storage tank for separating the sieve residue from the inflowing raw water and separately storing the wastewater and the sieve residue, and the storage of the sieve residue, etc. Since the first treatment tank provided with the tank and the second treatment tank provided with the biological treatment reaction tank composed of the endless circulating water channel in which the membrane separation unit is arranged are independently configured, the structure is It is simple and can be transported by land with a trailer etc. in the state where the first treatment tank and the second treatment tank are separated, so that the basic parts can be manufactured at the factory.
The installation work does not require specialized technology, and the installation work can be performed in a short period of time and at low cost. Particularly, an organic sewage treatment apparatus and its assembling method suitable for a small sewage treatment plant are provided. Can be provided.
【0040】また、第1処理槽と第2処理槽とを、余剰
汚泥引抜管を介して接続し、第2処理槽の生物処理反応
槽の余剰汚泥を第1処理槽の篩渣等貯留槽へ導入、貯留
するようにすることにより、第2処理槽の生物処理反応
槽において発生する余剰汚泥の貯留及び処理を、簡易な
機構の装置によって、トータル的に行うことができる。Further, the first treatment tank and the second treatment tank are connected via a surplus sludge drawing pipe, and the surplus sludge of the biological treatment reaction tank of the second treatment tank is stored in a sieve residue of the first treatment tank. By introducing and storing the excess sludge in the biological treatment reaction tank of the second treatment tank, it is possible to totally store and treat the excess sludge by a device having a simple mechanism.
【0041】また、第1処理槽の汚水貯留槽及び篩渣等
貯留槽に曝気機構を配設することにより、第1処理槽の
汚水貯留槽から第2処理槽の生物処理反応槽に導入され
る汚水の生物処理を円滑に行うことができるとともに、
篩渣等貯留槽に導入、貯留される篩渣及び余剰汚泥を好
気処理し、腐敗を防止することができる。Further, by disposing the aeration mechanism in the wastewater storage tank of the first treatment tank and the storage tank such as sieve residue, the wastewater storage tank of the first treatment tank is introduced into the biological treatment reaction tank of the second treatment tank. The biological treatment of sewage can be performed smoothly,
The screen residue and excess sludge introduced and stored in a storage tank such as screen residue can be aerobically treated to prevent spoilage.
【0042】また、第2処理槽の生物処理反応槽には、
攪拌機及び曝気機構を配設したり、スクリュー式曝気機
を配設することにより、無終端周回水路からなる生物処
理反応槽内を間欠的(時間的又は位置的)に好気又は嫌
気状態にして、汚水の生物処理、すなわち、硝化、脱窒
を円滑に行うための循環水流の流速等の環境を容易に整
えることができる。In the biological treatment reaction tank of the second treatment tank,
By installing a stirrer and aeration mechanism, or by installing a screw type aerator, the biological treatment reaction tank consisting of endless circulating water channel is intermittently (temporally or positionally) made aerobic or anaerobic. The biological treatment of sewage, that is, the environment such as the flow velocity of the circulating water flow for smoothly performing nitrification and denitrification can be easily prepared.
【0043】また、第2処理槽の生物処理反応槽の中央
部に膜分離ユニットを配設して区画することにより、第
2処理槽の生物処理反応槽の無終端周回水路を簡易に形
成することができる。Further, by arranging and partitioning the membrane separation unit in the center of the biological treatment reaction tank of the second treatment tank, the endless circulating water channel of the biological treatment reaction tank of the second treatment tank can be easily formed. be able to.
【0044】また、第2処理槽の生物処理反応槽の膜分
離ユニットから処理水を排出する処理水排出管の出口側
端部を、生物処理反応槽の水位より低い位置で開放水面
の位置を任意に調節可能な水位調整手段を配設した排水
調整槽に浸漬するようにすることにより、第2処理槽の
生物処理反応槽の膜分離ユニットから処理水を、生物処
理反応槽と排水調整槽間の水頭差を利用して無動力で安
定して排出することができる。Further, the outlet side end of the treated water discharge pipe for discharging treated water from the membrane separation unit of the biological treatment reaction tank of the second treatment tank is set at a position lower than the water level of the biological treatment reaction tank and at the position of the open water surface. By immersing it in a drainage adjusting tank provided with a water level adjusting means that can be arbitrarily adjusted, treated water is discharged from the membrane separation unit of the biological processing reaction tank of the second treatment tank, and the biological treatment reaction tank and the drainage adjusting tank. It is possible to stably discharge without power using the head difference between the two.
【0045】また、第2処理槽の生物処理反応槽の膜分
離ユニットから処理水を排出する処理水排出管に吸引ポ
ンプを介在したバイパス管を並設することにより、装置
の作動開始時、その他非常時に、第2処理槽の生物処理
反応槽から、膜分離ユニットを介して、処理水を強制的
に排出することができる。Further, by arranging a bypass pipe interposing a suction pump in parallel with the treated water discharge pipe for discharging treated water from the membrane separation unit of the biological treatment reaction tank of the second treatment tank, at the start of operation of the apparatus, etc. In an emergency, the treated water can be forcibly discharged from the biological treatment reaction tank of the second treatment tank through the membrane separation unit.
【0046】また、第1処理槽及び第2処理槽の外寸法
を、高さを3m以下、幅を2.5m以下、長さを6m以
下に形成することにより、第1処理槽及び第2処理槽を
分離した状態で、規制を受けることなく、それぞれトレ
ーラ等によって陸上輸送できる。The outer dimensions of the first processing tank and the second processing tank are formed such that the height is 3 m or less, the width is 2.5 m or less, and the length is 6 m or less. With the treatment tanks separated, they can be transported by land by trailers without restriction.
【図面の簡単な説明】[Brief description of drawings]
【図1】本発明の有機性汚水の処理装置の第1実施例を
示す説明図である。FIG. 1 is an explanatory diagram showing a first embodiment of an organic wastewater treatment apparatus of the present invention.
【図2】同正面断面図である。FIG. 2 is a front sectional view of the same.
【図3】同平面図である。FIG. 3 is a plan view of the same.
【図4】本発明の有機性汚水の処理装置の第2実施例を
示す説明図である。FIG. 4 is an explanatory diagram showing a second embodiment of the organic sewage treatment apparatus of the present invention.
【図5】第1処理槽をトレーラで搬送している状態を示
す説明図である。FIG. 5 is an explanatory diagram showing a state where the first processing tank is being transported by a trailer.
【図6】第2処理槽をトレーラで搬送している状態を示
す説明図である。FIG. 6 is an explanatory diagram showing a state where the second processing tank is being transported by a trailer.
A 第1処理槽 A1 汚水貯留槽 A2 篩渣等貯留槽 B 第2処理槽 B1 生物処理反応槽 B2 排水調整槽 T トレーラ 1 スクリーン 2 散気管 3 散気管 4 ブロア 5 流量調整ポンプ 6 定流量計量槽 7 汚水供給管 8 余剰汚泥引抜管 9 膜分離ユニット 10 散気管 11 吸引ポンプ 12 水位調整手段 13 水位調整用タンク 14 処理水排出管 15 余剰汚泥引抜弁 16 散気管 17 攪拌機 18 スクリュー式曝気機 19 可動堰 20 殺菌剤添加槽 21 バイパス管 A first treatment tank A1 wastewater storage tank A2 sieve residue storage tank B Second treatment tank B1 Biological treatment reactor B2 drainage adjustment tank T trailer 1 screen 2 Air diffuser 3 Air diffuser 4 Blower 5 Flow rate adjustment pump 6 constant flow metering tank 7 Sewage supply pipe 8 Excess sludge drawing pipe 9 Membrane separation unit 10 Air diffuser 11 Suction pump 12 Water level adjustment means 13 Water level adjustment tank 14 Treated water discharge pipe 15 Surplus sludge extraction valve 16 Air diffuser 17 Stirrer 18 screw type aerator 19 movable weir 20 Disinfectant addition tank 21 Bypass pipe
───────────────────────────────────────────────────── フロントページの続き (72)発明者 碓井 次郎 東京都港区赤坂6丁目1番20号 日本下 水道事業団内 (72)発明者 水田 耕市 兵庫県尼崎市下坂部3丁目11番1号 日 立機電工業株式会社内 (72)発明者 松岡 征夫 兵庫県尼崎市下坂部3丁目11番1号 日 立機電工業株式会社内 (72)発明者 浜田 英明 兵庫県尼崎市下坂部3丁目11番1号 日 立機電工業株式会社内 (56)参考文献 特開 平3−270791(JP,A) 特開 平10−151484(JP,A) 特開 平7−299485(JP,A) 特開 平6−490(JP,A) 特開 平3−15697(JP,A) (58)調査した分野(Int.Cl.7,DB名) C02F 3/12 C02F 3/14 - 3/18 C08F 3/34 101 C02F 3/00 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Jiro Usui 6-1-20 Akasaka, Minato-ku, Tokyo Within the Japan Sewer Works (72) Inventor Koichi Mizuta 3-11-1 Shimozakabe, Amagasaki City, Hyogo Prefecture No. Nitto Kiden Kogyo Co., Ltd. (72) Inventor Masao Matsuoka 3-11-1 Shimosaka, Amagasaki-shi, Hyogo Prefecture Nikko Ritsudenki Co., Ltd. (72) Hideaki Hamada 3-chome Shimozaka, Amagasaki, Hyogo No. 1 within Nitto Kiden Kogyo Co., Ltd. (56) Reference JP-A-3-270791 (JP, A) JP-A-10-151484 (JP, A) JP-A-7-299485 (JP, A) JP Flat 6-490 (JP, A) JP-A-3-15697 (JP, A) (58) Fields investigated (Int.Cl. 7 , DB name) C02F 3/12 C02F 3/14-3/18 C08F 3 / 34 101 C02F 3/00
Claims (10)
篩渣とを個別に貯留する汚水貯留槽及び篩渣等貯留槽を
備えた第1処理槽と、膜分離ユニットを配設した無終端
周回水路からなる生物処理反応槽を備えた第2処理槽と
を、独立して配置するとともに、第1処理槽と第2処理
槽とを、汚水供給管を介して接続するようにしたことを
特徴とする有機性汚水の処理装置。1. A first treatment tank having a waste water storage tank for separating the screen residue from the inflowing raw water and separately storing the waste water and the screen residue, and a membrane separation unit. A second treatment tank provided with a biological treatment reaction tank composed of an endless circulating water channel was arranged independently, and the first treatment tank and the second treatment tank were connected via a waste water supply pipe. An organic sewage treatment apparatus characterized by the above.
引抜管を介して接続し、第2処理槽の生物処理反応槽の
余剰汚泥を第1処理槽の篩渣等貯留槽へ導入、貯留する
ようにしたことを特徴とする請求項1記載の有機性汚水
の処理装置。2. The first treatment tank and the second treatment tank are connected via a surplus sludge drawing pipe, and the surplus sludge of the biological treatment reaction tank of the second treatment tank is a storage tank such as a sieve residue of the first treatment tank. The organic sewage treatment apparatus according to claim 1, wherein the organic sewage treatment apparatus is introduced into and stored in.
槽に曝気機構を配設したことを特徴とする請求項1又は
2記載の有機性汚水の処理装置。3. The apparatus for treating organic sewage according to claim 1 or 2, wherein an aeration mechanism is provided in the sewage storage tank and the sieve residue storage tank of the first treatment tank.
及び曝気機構を配設したことを特徴とする請求項1、2
又は3記載の有機性汚水の処理装置。4. The biological treatment reaction tank of the second processing tank is provided with a stirrer and an aeration mechanism.
Or the organic sewage treatment apparatus according to 3 above.
ュー式曝気機を配設したことを特徴とする請求項1、2
又は3記載の有機性汚水の処理装置。5. The screw type aerator is provided in the biological treatment reaction tank of the second treatment tank.
Or the organic sewage treatment apparatus according to 3 above.
膜分離ユニットを配設して区画することにより、無終端
周回水路を形成するようにしたことを特徴とする請求項
1、2、3、4又は5記載の有機性汚水の処理装置。6. The endless circulating water channel is formed by arranging and partitioning a membrane separation unit at the center of the biological treatment reaction tank of the second treatment tank. The organic sewage treatment apparatus according to 2, 3, 4 or 5.
ニットから処理水を排出する処理水排出管の出口側端部
を、生物処理反応槽の水位より低い位置で開放水面の位
置を任意に調節可能な水位調整手段を配設した排水調整
槽に浸漬するようにしたことを特徴とする請求項1、
2、3、4、5又は6記載の有機性汚水の処理装置。7. The outlet side end of the treated water discharge pipe for discharging treated water from the membrane separation unit of the biological treatment reaction tank of the second treatment tank is set at a position lower than the water level of the biological treatment reaction tank and at the position of the open water surface. 2. The apparatus is soaked in a drainage adjusting tank provided with an arbitrarily adjustable water level adjusting means.
The treatment apparatus for organic wastewater according to 2, 3, 4, 5 or 6.
ニットから処理水を排出する処理水排出管に吸引ポンプ
を介在したバイパス管を並設したことを特徴とする請求
項1、2、3、4、5、6又は7記載の有機性汚水の処
理装置。8. A bypass pipe having a suction pump interposed in parallel with a treated water discharge pipe for discharging treated water from the membrane separation unit of the biological treatment reaction tank of the second treatment tank. The treatment device for organic wastewater according to 3, 4, 5, 6 or 7.
高さを3m以下、幅を2.5m以下、長さを6m以下に
形成したことを特徴とする請求項1、2、3、4、5、
6、7又は8記載の有機性汚水の処理装置。9. The outer dimensions of the first treatment tank and the second treatment tank are
The height is 3 m or less, the width is 2.5 m or less, and the length is 6 m or less.
6. The organic sewage treatment apparatus according to 6, 7, or 8.
し、個別に貯留する汚水貯留槽及び篩渣等貯留槽を備え
た第1処理槽と、内部に膜分離ユニットを配設した無終
端周回水路からなる生物処理反応槽を備えた第2処理槽
とを、分離した状態で、それぞれトレーラ等によって陸
上輸送できる外寸法に工場で製造するとともに、陸上輸
送した第1処理槽及び第2処理槽を設置後、第1処理槽
と第2処理槽とを、配管を介して接続することを特徴と
する有機性汚水の処理装置の組立方法。10. A first treatment tank having a storage tank for separating the inflowing raw water into a waste water and a sieve residue and separately storing the waste water and a sieve residue, and a membrane separation unit disposed inside. The second treatment tank provided with the biological treatment reaction tank consisting of the terminal circulation water channel is manufactured in a factory in an external dimension that can be transported by land by a trailer or the like in a separated state, and the first treatment tank and the second treatment tank transported by land are used. After installing the treatment tank, the first treatment tank and the second treatment tank are connected via a pipe, and a method for assembling an organic wastewater treatment apparatus.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP18198899A JP3408199B2 (en) | 1999-06-28 | 1999-06-28 | Organic wastewater treatment apparatus and assembling method thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP18198899A JP3408199B2 (en) | 1999-06-28 | 1999-06-28 | Organic wastewater treatment apparatus and assembling method thereof |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JP2001009490A JP2001009490A (en) | 2001-01-16 |
| JP3408199B2 true JP3408199B2 (en) | 2003-05-19 |
Family
ID=16110368
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP18198899A Expired - Fee Related JP3408199B2 (en) | 1999-06-28 | 1999-06-28 | Organic wastewater treatment apparatus and assembling method thereof |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3408199B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103145252A (en) * | 2013-02-22 | 2013-06-12 | 国核电力规划设计研究院 | System and method for supplementing water to circulation cooling device of thermal power plant |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4336143B2 (en) * | 2003-05-27 | 2009-09-30 | ヤンマー株式会社 | Portable sewage treatment device and construction method of this portable sewage treatment device |
| JP2007275895A (en) * | 2007-07-30 | 2007-10-25 | Hitachi Plant Technologies Ltd | Nitrogen removal method and apparatus in membrane separation type oxidation ditch |
-
1999
- 1999-06-28 JP JP18198899A patent/JP3408199B2/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103145252A (en) * | 2013-02-22 | 2013-06-12 | 国核电力规划设计研究院 | System and method for supplementing water to circulation cooling device of thermal power plant |
Also Published As
| Publication number | Publication date |
|---|---|
| JP2001009490A (en) | 2001-01-16 |
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