JPS5931358Y2 - Sewage treatment equipment using rotating cylinder - Google Patents

Sewage treatment equipment using rotating cylinder

Info

Publication number
JPS5931358Y2
JPS5931358Y2 JP1979120819U JP12081979U JPS5931358Y2 JP S5931358 Y2 JPS5931358 Y2 JP S5931358Y2 JP 1979120819 U JP1979120819 U JP 1979120819U JP 12081979 U JP12081979 U JP 12081979U JP S5931358 Y2 JPS5931358 Y2 JP S5931358Y2
Authority
JP
Japan
Prior art keywords
treatment
sewage
aerobic
cylinder
rotating cylinder
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
Application number
JP1979120819U
Other languages
Japanese (ja)
Other versions
JPS5639199U (en
Inventor
稔 大久保
Original Assignee
積水化学工業株式会社
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.)
Filing date
Publication date
Application filed by 積水化学工業株式会社 filed Critical 積水化学工業株式会社
Priority to JP1979120819U priority Critical patent/JPS5931358Y2/en
Publication of JPS5639199U publication Critical patent/JPS5639199U/ja
Application granted granted Critical
Publication of JPS5931358Y2 publication Critical patent/JPS5931358Y2/en
Expired legal-status Critical Current

Links

Classifications

    • 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

Landscapes

  • Biological Treatment Of Waste Water (AREA)
  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)

Description

【考案の詳細な説明】 本考案は工場廃水等の汚水を回転筒によって生物学的に
処理する装置に関し、殊に汚水に対して好気性処理と嫌
気性処理との相異なった2種の処理を行なうことのでき
る装置に関する。
[Detailed description of the invention] The present invention relates to a device for biologically treating wastewater such as factory wastewater using a rotating cylinder, and in particular, it uses two different types of treatment for wastewater: aerobic treatment and anaerobic treatment. The present invention relates to a device capable of performing the following steps.

この種回転筒による処理装置の処理方式としては従来よ
り、回転筒の外周面を汚水に接触させる外浸型、内周面
を汚水に接触させる内浸型、及び回転筒を金網等多孔体
で形成し、外周面と内周面を同時に汚水に接触させる外
浸、内浸並存型の3種類がある。
Conventional treatment methods for this type of treatment equipment using a rotating cylinder include an external immersion type in which the outer peripheral surface of the rotating cylinder is brought into contact with wastewater, an internal immersion type in which the inner peripheral surface is brought into contact with wastewater, and a rotary cylinder in which a porous material such as a wire mesh is used. There are three types: external immersion type and internal immersion type, in which the outer peripheral surface and inner peripheral surface are brought into contact with wastewater at the same time.

前二者の外浸型、・内浸型の処理方式ではいずれも好気
性処理或いは嫌気性処理の一方しか行なうことができず
、両方の処理を行なうためには、好気性処理装置の後に
嫌気性処理装置を付加し或いは嫌気性処理装置の後に好
気性処理装置を付加しなければならず、壱のため占有空
間の大きな大損りな装置となり据付場所の選定に著しい
不便を来すことが多いものである。
The former two types of treatment methods, external immersion type and internal immersion type, can only perform either aerobic treatment or anaerobic treatment; in order to perform both treatments, anaerobic treatment must be performed after the aerobic treatment equipment It is necessary to add an aerobic treatment device or an aerobic treatment device after an anaerobic treatment device, which is a big waste of space and often causes significant inconvenience in selecting the installation location. It is.

一方外浸、内浸並存型の処理方式においてもやはり好気
性処理か嫌気性処理のいずれか一方に限られるので事情
は同じであるが、特にこの方式においては使用中に網目
が目詰まりを起すことがあり、その場合は筒内が相対的
に嫌気性状態となって、好気性処理と嫌気性処理とを一
台の装置にて行なえるが如き状態が現出する。
On the other hand, the situation is the same for external immersion and internal immersion coexistence type treatment methods as it is limited to either aerobic treatment or anaerobic treatment, but especially in this method, the meshes become clogged during use. In this case, the inside of the cylinder becomes relatively anaerobic, resulting in a situation where aerobic treatment and anaerobic treatment can be performed in one device.

しかし、この方式においては好気性バクテリヤと嫌気性
バクテリヤとが共存するため、相互に干渉しあって両者
とも適性生存条件が悪化し、処理効率の著しい低下を来
すものである。
However, in this method, since aerobic bacteria and anaerobic bacteria coexist, they interfere with each other, deteriorating the suitable survival conditions for both, and causing a significant drop in treatment efficiency.

そこで本考案は、単一の処理装置という占有空間の少な
い一槽式の構成をとりつつ、好気性処理ゾーンと嫌気性
処理ゾーンとを明確に分けて両者ともに高い処理効率に
維持することのできる新規有用な技術を提案することを
目的とする。
Therefore, the present invention adopts a single-tank configuration with a single treatment device that occupies less space, while clearly separating the aerobic treatment zone and anaerobic treatment zone and maintaining high treatment efficiency in both. The purpose is to propose new and useful technologies.

次に本考案の実施例を図面に基づいて説明する。Next, embodiments of the present invention will be described based on the drawings.

第1図はその一実施例を示し、1は好気性雰囲気中(大
気中章に置かれた処理槽で、−側に未処理汚水を供給
る供給口としての供給パイプ2が設けられ、他側に処理
された汚水を槽外に流出する流出口としての排出パイプ
3が連結しである。
Figure 1 shows an example of this. 1 is a treatment tank placed in an aerobic atmosphere (in the atmosphere), and untreated sewage is supplied to the - side.
A supply pipe 2 serving as a supply port is provided, and a discharge pipe 3 serving as an outlet for discharging treated wastewater out of the tank is connected to the other side.

また該処理槽1の底部には排出弁4付きの排出管5が連
結してあり、底部に堆積した汚泥を適宜排出するように
しである。
Further, a discharge pipe 5 with a discharge valve 4 is connected to the bottom of the treatment tank 1, so that the sludge accumulated at the bottom can be appropriately discharged.

6は、外周面6aが前記処理槽1に貯留された汚水Aに
半水没状態で浸漬された中空の回転筒で、両端に固定さ
れた中空の回転軸7,8に摺動自在にシール9,10を
挿通することによって該筒6内を密封し、嫌気性雰囲気
に保っている。
6 is a hollow rotary cylinder whose outer peripheral surface 6a is semi-submerged in the wastewater A stored in the treatment tank 1, and has seals 9 slidably attached to hollow rotary shafts 7 and 8 fixed at both ends. , 10, the inside of the cylinder 6 is sealed and maintained in an anaerobic atmosphere.

またこの回転筒6内には前記シール9,10を貫通して
汚水の供給口としての供給パイプ11及び流出口として
の排出パイプ12が挿通しである。
In addition, a supply pipe 11 as a sewage supply port and a discharge pipe 12 as an outlet are inserted through the rotary cylinder 6 through the seals 9 and 10.

そして両者の供給パイプ11は前記処理槽1の排出パイ
プ3とポンプ13を介して連結されている○尚、前記回
転筒6は塩化ビニール等の合成樹脂材或いはステンレス
鋼等の不錆性金属から形成されており、かつ内部の点検
、保守の便のために2つ割りできるように構成されてい
る。
The supply pipe 11 of both is connected to the discharge pipe 3 of the treatment tank 1 via a pump 13.The rotating cylinder 6 is made of synthetic resin material such as vinyl chloride or rust-proof metal such as stainless steel. It is constructed so that it can be divided into two for convenient internal inspection and maintenance.

また図中、14は回転駆動軸で、その端部のギヤー15
を前記回転軸8に取着されたギヤー16と噛合させて回
転筒6に回転動力を伝達している。
In the figure, 14 is a rotary drive shaft, and a gear 15 at the end thereof.
is meshed with a gear 16 attached to the rotating shaft 8 to transmit rotational power to the rotating cylinder 6.

17は排出ポンプ18は排気管で、筒6内で発生した分
解窒素ガスを排出するのみし、筒6内に空気が流入しな
いように逆止弁19が連結してである。
Reference numeral 17 denotes an exhaust pump 18, which only discharges the decomposed nitrogen gas generated within the cylinder 6, and is connected to a check valve 19 to prevent air from flowing into the cylinder 6.

この構成によれば汚水は供給パイプ2→処理槽1→排出
パイプ3→ポンプ13→供給パイプ11→回転筒6内→
排出パイプ12という順序で流され、この間に処理槽1
と回転筒6内で異なった生物学的処理を受ける。
According to this configuration, the wastewater is supplied from the supply pipe 2 → the treatment tank 1 → the discharge pipe 3 → the pump 13 → the supply pipe 11 → the inside of the rotating cylinder 6 →
During this time, the treatment tank 1
and undergo different biological treatments within the rotating cylinder 6.

即ち処理槽1では好気性雰囲気中で筒外周面6aに増殖
した好気性バクテリヤと接触し、好気的な生物学的処理
を受け、回転筒6内では嫌気性雰囲気中で筒内周面6b
に増殖した嫌気性バクテリヤと接触することによって嫌
気的な生物学的処理を受ける。
That is, in the treatment tank 1, the aerobic bacteria grown on the cylinder outer circumferential surface 6a in an aerobic atmosphere are brought into contact and subjected to aerobic biological treatment, and in the rotary cylinder 6, the cylinder inner circumferential surface 6b is in an anaerobic atmosphere.
undergoes anaerobic biological treatment by coming into contact with anaerobic bacteria grown on

そしてこの場合、処理槽1と筒6内とは筒壁によって完
全に絶縁されているので、好気性バクテリヤと嫌気性バ
クテリヤとは隔離され、ともに干渉しない独自の高い処
理効率で汚水を処理するのである。
In this case, since the inside of the treatment tank 1 and the cylinder 6 are completely insulated by the cylinder wall, aerobic bacteria and anaerobic bacteria are separated, and the wastewater is treated with a unique high treatment efficiency that does not interfere with either. be.

尚、この構成では処理槽1を好気性雰囲気中におき、回
転筒6内を嫌気性雰囲気に保つようにしたが、本考案は
これに限定されるものではなく処理槽1を嫌気性雰囲気
中におき、一方回転筒6内を好気性雰囲気に保つように
しても良いものである。
In this configuration, the processing tank 1 is placed in an aerobic atmosphere and the inside of the rotating cylinder 6 is kept in an anaerobic atmosphere. However, the present invention is not limited to this, and the processing tank 1 is placed in an anaerobic atmosphere. However, the inside of the rotating cylinder 6 may be kept in an aerobic atmosphere.

また汚水を流す方向も、回転筒6内から処理槽1という
ように上記構成とは全く逆の方向としても良いものであ
る。
Furthermore, the direction in which the wastewater flows may be completely opposite to the above configuration, such as from the inside of the rotary tube 6 to the treatment tank 1.

その他、例えば回転筒6に対して第2図ないし第4図に
示すように、その外周面6aに円板20・・・を固着し
、或いは内周面6bにドーナツ状の仕切板21・・・を
固着し、更には外周面に円板20・・・を内周面6bに
仕切板21・・・をそれぞれ固着して、外周面6a又は
内周面6b或いは内外両周面の表面積を増大させ、処理
能力の増大を図るようにしても良い。
In addition, for example, as shown in FIGS. 2 to 4, a disk 20 is fixed to the outer circumferential surface 6a of the rotating cylinder 6, or a donut-shaped partition plate 21 is attached to the inner circumferential surface 6b.・Fix the disk 20... to the outer circumferential surface and the partition plate 21... to the inner circumferential surface 6b, respectively, to increase the surface area of the outer circumferential surface 6a, the inner circumferential surface 6b, or both the inner and outer circumferential surfaces. The processing capacity may be increased by increasing the processing capacity.

この場合、汚水の供給口のある回転軸8に近い側の仕切
板21・・・はど図示のようにその中央の穴の径を小さ
くしておけば、汚水は仕切板21・・・を溢流しつつ漸
時左方に移動するので更に好都合である。
In this case, if the diameter of the hole in the center of the partition plate 21 on the side near the rotating shaft 8 where the waste water supply port is made small as shown in the figure, the waste water will flow through the partition plate 21... This is even more convenient because it gradually moves to the left while overflowing.

また前記円板20・・・、仕切板21・・・に代えて、
第5図、第6図に示すように回転筒6の周部自身に凹部
22・・・と凸部23・・・を交互に形成して筒内外周
面の表面積を増大するようにしても良い。
Also, instead of the disk 20..., the partition plate 21...
As shown in FIGS. 5 and 6, recesses 22 and convex portions 23 may be alternately formed on the circumference of the rotary cylinder 6 to increase the surface area of the inner and outer peripheral surfaces of the cylinder. good.

そして特に第6図に示すように筒6内に横架した軸24
にリング25・・・を回転自在に設け、該リング25・
・・から鎖26・・・を凸部23・・・に向かって垂下
させれば、凸部22・・・内で増殖した余剰の生物膜に
よる目詰りが防止でき、更に好都合である。
In particular, as shown in FIG.
A ring 25... is rotatably provided in the ring 25...
If the chains 26 are allowed to hang down from the convex portions 23 toward the convex portions 23, it is possible to prevent the convex portions 22 from being clogged with excess biofilm that has grown, which is more convenient.

以上要約すれば本考案に係る回転筒による汚水処理装置
は、好気性又は嫌気性雰囲気中におかれた処理槽と、外
周面が前記処理槽に半水没状態で浸漬され、中空内部が
前記処理槽とは異なった雰囲気に保たれ回転筒とを備え
、かつ前記処理槽の汚水供給口と回転筒内の汚水流出口
とを、或いは処理槽の汚水流出口と回転筒内の汚水供給
口とを直列に配管接続したため、汚水を配管を通じて流
すことによって、処理槽と回転筒内という同一装置内の
明確に分離された2つのゾーンで、好気性と嫌気性とい
う相反する生物学的処理を行なうことができる。
In summary, the sewage treatment device using a rotating cylinder according to the present invention includes a treatment tank placed in an aerobic or anaerobic atmosphere, an outer circumferential surface of which is immersed in the treatment tank in a semi-submerged state, and a hollow interior that is immersed in the treatment tank. A rotary cylinder maintained in an atmosphere different from that of the tank, and a sewage supply port of the treatment tank and a sewage outlet in the rotary cylinder, or a sewage outflow port of the treatment tank and a sewage supply port in the rotary cylinder. are connected in series, and by flowing wastewater through the pipes, aerobic and anaerobic biological treatments, which are contradictory to each other, can be performed in two clearly separated zones within the same device: the treatment tank and the rotary cylinder. be able to.

従って従来の外浸、内浸並存型の装置においてみられた
好気性バクテリヤと嫌気性バクテリヤとの共存という困
った事態は防止され、好気性処理、嫌気性処理とも独自
の高い処理効率で行なうことができる。
Therefore, the troublesome situation of coexistence of aerobic bacteria and anaerobic bacteria that was observed in conventional external immersion and internal immersion coexistence type equipment is prevented, and both aerobic treatment and anaerobic treatment can be performed with unique high processing efficiency. I can do it.

しかも、このような相反する処理を同一装置内で行なう
ものでありながら、単なる外浸型の処理装置と同程度の
空間しか占有しないものであるから空間的に限られた狭
い場所に対しても設置できるという利点ももつのである
Furthermore, although these contradictory processes are carried out within the same device, it occupies the same amount of space as a simple external immersion type processing device, so it can be used in narrow spaces with limited space. It also has the advantage of being easy to install.

【図面の簡単な説明】 図は本考案に係る回転筒による汚水処理装置を例示し、
第1図はその一実施例としての全体正面断面図、第2図
ないし第6図はそれぞれ本考案の他の各実施例を示した
正面断面図である01・・・・・・処理槽、2・・・・
・・供給口、3・・・・・・流出口、6・・・・・・回
転筒、11・・・・・・供給口、12・・・・・・流出
口。
[Brief explanation of the drawings] The figure illustrates a sewage treatment device using a rotating cylinder according to the present invention.
FIG. 1 is an overall front sectional view showing one embodiment of the invention, and FIGS. 2 to 6 are front sectional views showing other embodiments of the present invention. 2...
... Supply port, 3 ... Outlet, 6 ... Rotating tube, 11 ... Supply port, 12 ... Outlet.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 好気性又は嫌気性雰囲気中におかれた処理槽と、外周面
が前記処理槽に半水没状態で浸漬され、中空内部が前記
処理槽とは異なった雰囲気に保たれた回転筒とを備え、
かつ前記処理槽の汚水供給口と回転筒内の汚水流出口と
を、或いは処理槽の汚水流出口と回転筒内の汚水供給口
とを直列に配管接続してなる回転筒による汚水処理装置
comprising a processing tank placed in an aerobic or anaerobic atmosphere, and a rotating cylinder whose outer peripheral surface is immersed in the processing tank in a semi-submerged state and whose hollow interior is maintained in an atmosphere different from that of the processing tank,
A sewage treatment device using a rotary cylinder, in which the sewage supply port of the treatment tank and the sewage outlet in the rotary cylinder are connected in series, or the sewage outflow port of the treatment tank and the sewage supply port in the rotary cylinder are connected in series.
JP1979120819U 1979-08-31 1979-08-31 Sewage treatment equipment using rotating cylinder Expired JPS5931358Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1979120819U JPS5931358Y2 (en) 1979-08-31 1979-08-31 Sewage treatment equipment using rotating cylinder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1979120819U JPS5931358Y2 (en) 1979-08-31 1979-08-31 Sewage treatment equipment using rotating cylinder

Publications (2)

Publication Number Publication Date
JPS5639199U JPS5639199U (en) 1981-04-13
JPS5931358Y2 true JPS5931358Y2 (en) 1984-09-05

Family

ID=29352987

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1979120819U Expired JPS5931358Y2 (en) 1979-08-31 1979-08-31 Sewage treatment equipment using rotating cylinder

Country Status (1)

Country Link
JP (1) JPS5931358Y2 (en)

Also Published As

Publication number Publication date
JPS5639199U (en) 1981-04-13

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