JPH02102793A - Apparatus for treating filthy water - Google Patents
Apparatus for treating filthy waterInfo
- Publication number
- JPH02102793A JPH02102793A JP63256677A JP25667788A JPH02102793A JP H02102793 A JPH02102793 A JP H02102793A JP 63256677 A JP63256677 A JP 63256677A JP 25667788 A JP25667788 A JP 25667788A JP H02102793 A JPH02102793 A JP H02102793A
- Authority
- JP
- Japan
- Prior art keywords
- membrane
- water
- aeration tank
- tank
- pressure
- 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.)
- Granted
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 22
- 239000012528 membrane Substances 0.000 claims abstract description 43
- 238000005273 aeration Methods 0.000 claims abstract description 23
- 238000000926 separation method Methods 0.000 claims abstract description 20
- 239000010865 sewage Substances 0.000 claims description 15
- 239000007788 liquid Substances 0.000 claims description 7
- 238000005192 partition Methods 0.000 claims description 3
- 238000007664 blowing Methods 0.000 abstract description 2
- 238000005406 washing Methods 0.000 abstract 2
- 238000004140 cleaning Methods 0.000 description 14
- 238000000034 method Methods 0.000 description 7
- 239000000126 substance Substances 0.000 description 7
- 238000010586 diagram Methods 0.000 description 3
- 230000001105 regulatory effect Effects 0.000 description 3
- 238000009434 installation Methods 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- 239000005708 Sodium hypochlorite Substances 0.000 description 1
- 239000003599 detergent Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- SUKJFIGYRHOWBL-UHFFFAOYSA-N sodium hypochlorite Chemical compound [Na+].Cl[O-] SUKJFIGYRHOWBL-UHFFFAOYSA-N 0.000 description 1
- 238000004065 wastewater treatment 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
- Activated Sludge Processes (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、汚水の曝気処理と膜分離処理とを組み合わせ
た汚水処理装置に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a sewage treatment device that combines aeration treatment and membrane separation treatment of sewage.
従来のこの種の装置としては、曝気槽の外に膜分離槽を
設置する形式のものが知られている。例えば、第4図及
び第5図に示したように、スクリーン程度で前処理した
汚水lをブロアー2の空気を空気配管3で圧送し、散気
装置4から吹き出す機構を持らた曝気槽5に投入し、微
生物処理しながら循環加圧ポンプ6で曝気槽5内の混合
液7を循環配管8を通して膜分離槽9に投入し、圧力調
整弁10で膜分離槽9の圧力を調整して液体の膜分離処
理を行い、循環配管11を通して曝気槽5に戻り、さら
に加圧された混合液は駆動装置13の動力でスプロケッ
トホイール14とチェーン15等により回転される中空
軸16に固定された回転円板膜17で口過され、中空軸
16より処理水12を引き出す構成の装置が知られてい
る。As a conventional device of this type, one in which a membrane separation tank is installed outside the aeration tank is known. For example, as shown in FIGS. 4 and 5, an aeration tank 5 has a mechanism in which the air from a blower 2 is forced through an air pipe 3 and blown out from an aeration device 4. The mixed liquid 7 in the aeration tank 5 is introduced into the membrane separation tank 9 through the circulation piping 8 using the circulation pressure pump 6 while being treated with microorganisms, and the pressure in the membrane separation tank 9 is adjusted with the pressure regulating valve 10. The liquid was subjected to membrane separation treatment, returned to the aeration tank 5 through the circulation pipe 11, and the pressurized mixed liquid was fixed to a hollow shaft 16 that was rotated by a sprocket wheel 14, a chain 15, etc. with the power of a drive device 13. An apparatus is known in which treated water 12 is filtered through a rotating disc membrane 17 and drawn out from a hollow shaft 16.
しかしながら、曝気槽の外に膜分離槽を設置する従来の
形式の装置では、設置面積及び体積が大きくなり、また
、膜分離槽は耐圧容器でなければならず、高価であり、
さらに圧力調整弁10は汚泥の詰まり等によって、一定
圧に調整するのが困難であるという欠点がある。However, in the conventional type of equipment in which a membrane separation tank is installed outside the aeration tank, the installation area and volume are large, and the membrane separation tank must be a pressure-resistant container, which is expensive.
Furthermore, the pressure regulating valve 10 has a drawback in that it is difficult to adjust the pressure to a constant level due to clogging with sludge or the like.
したがって、本発明は、前記の従来技術の欠点を解消し
、耐圧容器を必要とせず、容易に一定圧に調整できる、
コンパクトで安価な汚水処理装置を提供することを課題
とする。Therefore, the present invention eliminates the drawbacks of the prior art described above, does not require a pressure-resistant container, and can easily adjust to a constant pressure.
The objective is to provide a compact and inexpensive sewage treatment device.
本発明は、曝気槽を上下に仕切り、その上部に膜モジュ
ールを設置し、圧力調整を容易にするため加圧方式でな
く、減圧方式に構成することによって前記の課題を解決
したものである。The present invention solves the above-mentioned problems by dividing the aeration tank into upper and lower parts, installing a membrane module on the upper part, and configuring the tank to be a depressurization system instead of a pressurization system to facilitate pressure adjustment.
すなわち、本発明の汚水処理装置は、曝気槽の中間部に
開閉可能な蓋を設け、該蓋より上部に液体分離用膜モジ
ュールと透過水集水バイブを有する膜分離装置を設置し
、該透過水集水パイプには真空ポンプで負圧にしうる真
空タンクを結合したことを特徴とする。That is, in the sewage treatment apparatus of the present invention, a lid that can be opened and closed is provided in the middle part of the aeration tank, and a membrane separation device having a membrane module for liquid separation and a permeated water collection vibrator is installed above the lid, and the permeated water The water collection pipe is characterized by a vacuum tank that can be used to create negative pressure using a vacuum pump.
次に、図面に示した実施例に基づいて本発明をさらに詳
述する。Next, the present invention will be explained in further detail based on embodiments shown in the drawings.
第1図は本発明の一実施例を示す汚水処理装置の系統図
、第2図は第1図の処理装置の上部の膜分離区画の断面
図である。FIG. 1 is a system diagram of a sewage treatment apparatus showing an embodiment of the present invention, and FIG. 2 is a sectional view of the membrane separation section in the upper part of the treatment apparatus of FIG.
この実施例においては、曝気槽18は、その中間部で開
閉可能なM19で仕切られている。この蓋19の上部に
は、透過水集水パイプとして宍能する中空軸16に多数
の回転円板膜17が固定され、駆動装置13の動力でス
プロケットホイール14とチェーン15により中空軸1
6を回転させることによって回転円板膜17も回転する
。この装置で処理を行う場合には、汚水lを曝気槽18
に注入し、曝気槽18の底部の散気装置4がら空気を吹
き込み、汚水を曝気処理するとともに、上部に設置した
回転円板膜17によって膜分離処理を行い、透過水は処
理水ライン20から真空ポンプ21により負圧にできる
圧力調整弁22を有する真空タンク23に引き出され、
さらに処理水移送ポンプ24によって移送される。In this embodiment, the aeration tank 18 is partitioned in the middle by an openable/closable M19. A large number of rotary disc membranes 17 are fixed to a hollow shaft 16 which functions as a permeated water collection pipe on the upper part of the lid 19.
By rotating 6, the rotating disc membrane 17 also rotates. When processing with this device, wastewater is transferred to the aeration tank 18.
The wastewater is aerated by blowing air through the aeration device 4 at the bottom of the aeration tank 18, and membrane separation is performed using the rotating disc membrane 17 installed at the top. It is drawn out to a vacuum tank 23 having a pressure regulating valve 22 that can be made negative pressure by a vacuum pump 21,
The treated water is further transferred by the treated water transfer pump 24.
第1図に示した処理装置で長期間処理を実施すると、膜
面にゲル層が形成し、膜が目詰まりを起こすことがある
。これを防止するため、膜を洗浄する必要がある。膜を
洗浄する際には、M19を閉じることにより曝気槽18
を上下に仕切り、上部区画において膜の洗浄を行う。例
えば、次亜塩素酸ナトリウム、洗剤などを用いる薬品洗
浄を行い、洗浄完了後、洗浄薬液を排液装置(図示せず
)によって排出した後、蓋19を開放し、再び、汚水処
理を開始する。If the treatment is carried out for a long period of time using the treatment apparatus shown in FIG. 1, a gel layer may be formed on the membrane surface, which may cause the membrane to become clogged. To prevent this, it is necessary to clean the membrane. When cleaning the membrane, the aeration tank 18 is closed by closing M19.
The membrane is divided into upper and lower sections, and the membrane is washed in the upper section. For example, chemical cleaning using sodium hypochlorite, detergent, etc. is performed, and after completion of cleaning, the cleaning chemical solution is discharged by a drainage device (not shown), and then the lid 19 is opened and wastewater treatment is started again. .
第3図に示した汚水処理装置は、洗浄工程の間にも汚水
処理工程を停止せずに連続運転することができるように
構成した実施例である。この実施例では、曝気槽25の
上部は仕切壁26によって2個の区画に仕切られており
、各区間の底部には開閉可能な蓋27が設けられ、各区
間内には多数の回転円板膜17が設けられている。この
処理装置において、膜を洗浄する場合には、洗浄すべき
回転円板膜17を含む区画を蓋27の閉鎖に車って閉鎖
し、この区画内の混合液を隣の区画に・移し、空になっ
た区画内に洗浄薬液導入管28より洗浄薬液を注入する
。The sewage treatment apparatus shown in FIG. 3 is an embodiment configured so that the sewage treatment process can be continuously operated without stopping the sewage treatment process even during the cleaning process. In this embodiment, the upper part of the aeration tank 25 is divided into two sections by a partition wall 26, the bottom of each section is provided with an openable and closable lid 27, and each section has a large number of rotating disks. A membrane 17 is provided. In this processing apparatus, when cleaning the membrane, the compartment containing the rotating disk membrane 17 to be cleaned is closed by closing the lid 27, and the mixed liquid in this compartment is transferred to the next compartment. A cleaning chemical solution is injected into the empty compartment from the cleaning chemical solution introduction pipe 28.
上記のように他方の区画へ混合液を移すことによって閉
鎖したM21に背圧が生じ、より完全な密封が可能とな
り、洗浄薬液が曝気槽にもれることはない。By transferring the liquid mixture to the other compartment as described above, a back pressure is created in the closed M21, allowing a more complete seal so that the cleaning chemical solution does not leak into the aeration tank.
洗浄完了後には、洗浄薬液を排水管29から排出する。After the cleaning is completed, the cleaning chemical solution is discharged from the drain pipe 29.
このように、第3図に示した装置では、洗浄工程の間、
他方の区画では蓋27を開放しておき、膜分離処理を続
行することができる。処理水は処理水ライン20から取
り出される。Thus, in the apparatus shown in FIG. 3, during the cleaning process,
In the other compartment, the membrane separation process can be continued with the lid 27 open. Treated water is taken out from treated water line 20.
本発明の汚水処理装置は、従来のこの種の装置に比べて
設置面積及び体積が著しく縮小され、また、耐圧容器を
必要とせず、安価である。さらに本発明の処理装置は、
加圧方式でなく、減圧方式に構成されているので、圧力
調整が容易であり、容易に一定圧に維持することができ
る。The sewage treatment device of the present invention has a significantly smaller installation area and volume than conventional devices of this type, does not require a pressure container, and is inexpensive. Furthermore, the processing device of the present invention includes:
Since the pressure reduction method is used instead of the pressurization method, the pressure can be easily adjusted and maintained at a constant pressure.
さらに、本発明の処理装置においては、膜モジュールを
取り外すことなく洗浄することができ、曝気槽の上部を
二個以上の区画に仕切り、各々の区画に膜モジュール及
び蓋を設けることにより、膜分離処理を停止することな
く、洗浄を行うことができる。Furthermore, in the processing apparatus of the present invention, the membrane module can be cleaned without removing it, and the upper part of the aeration tank is partitioned into two or more compartments, and each compartment is provided with a membrane module and a lid. Cleaning can be performed without stopping the process.
第1図は本発明の一実施例を示す汚水処理装置の系統図
、第2図は第1図の装置の膜分離区画の断面図、第3図
は本発明の別の実施例を示す汚水処理装置の系統図、第
4図は従来の汚水処理装置の系統図、第5図は第4図の
装置の膜分離槽の断面図である。
符号の説明
1・・・汚水、4・・・散気装置、5.18゜25・・
・曝気槽、9・・・膜分離槽、16・・・中空軸、17
・・・回転円板膜、19.27・・・蓋、20・・・処
理水ライン、21・・・真空ポンプ、22・・・圧力調
整弁、23・・・真空タンク、26・・・仕切壁、28
・・・洗浄薬液、29・・・排水管
第2図
第4図
第5Fig. 1 is a system diagram of a sewage treatment equipment showing one embodiment of the present invention, Fig. 2 is a sectional view of the membrane separation section of the equipment of Fig. 1, and Fig. 3 is a sewage water treatment equipment showing another embodiment of the present invention. FIG. 4 is a system diagram of a conventional sewage treatment device, and FIG. 5 is a sectional view of a membrane separation tank of the device shown in FIG. 4. Explanation of symbols 1...Sewage, 4...Diffuser, 5.18°25...
・Aeration tank, 9... Membrane separation tank, 16... Hollow shaft, 17
... Rotating disk membrane, 19.27 ... Lid, 20 ... Treated water line, 21 ... Vacuum pump, 22 ... Pressure adjustment valve, 23 ... Vacuum tank, 26 ... Partition wall, 28
...Cleaning chemical solution, 29...Drain pipe Figure 2 Figure 4 Figure 5
Claims (2)
上部に液体分離用膜モジュールと透過水集水パイプを有
する膜分離装置を設置し、該透過水集水パイプには真空
ポンプで負圧にしうる真空タンクを結合したことを特徴
とする汚水処理装置。(1) A lid that can be opened and closed is provided in the middle of the aeration tank, a membrane separation device having a membrane module for liquid separation and a permeated water collection pipe is installed above the lid, and the permeated water collection pipe has a vacuum A sewage treatment device that is equipped with a vacuum tank that can create negative pressure with a pump.
底部に開閉可能な仕切り蓋を設け、各区画内に膜分離装
置を設置した請求項1記載の汚水処理装置。(2) The sewage treatment apparatus according to claim 1, wherein the upper part of the aeration tank is partitioned into two or more compartments, a partition lid that can be opened and closed is provided at the bottom of each compartment, and a membrane separation device is installed in each compartment.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63256677A JPH02102793A (en) | 1988-10-12 | 1988-10-12 | Apparatus for treating filthy water |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63256677A JPH02102793A (en) | 1988-10-12 | 1988-10-12 | Apparatus for treating filthy water |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH02102793A true JPH02102793A (en) | 1990-04-16 |
JPH05117B2 JPH05117B2 (en) | 1993-01-05 |
Family
ID=17295934
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP63256677A Granted JPH02102793A (en) | 1988-10-12 | 1988-10-12 | Apparatus for treating filthy water |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH02102793A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0481697U (en) * | 1990-11-26 | 1992-07-16 | ||
FR2799391A1 (en) * | 1999-10-07 | 2001-04-13 | Degremont | Biological filter station for treatment of waste water and sewage has membranes supported by angled disks on rotating horizontal shaft with rising gas bubble stream to scour the membranes |
WO2011065520A1 (en) * | 2009-11-30 | 2011-06-03 | 株式会社クボタ | Organic wastewater treatment device and organic wastewater treatment method |
-
1988
- 1988-10-12 JP JP63256677A patent/JPH02102793A/en active Granted
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0481697U (en) * | 1990-11-26 | 1992-07-16 | ||
FR2799391A1 (en) * | 1999-10-07 | 2001-04-13 | Degremont | Biological filter station for treatment of waste water and sewage has membranes supported by angled disks on rotating horizontal shaft with rising gas bubble stream to scour the membranes |
WO2011065520A1 (en) * | 2009-11-30 | 2011-06-03 | 株式会社クボタ | Organic wastewater treatment device and organic wastewater treatment method |
JP2011110520A (en) * | 2009-11-30 | 2011-06-09 | Kubota Corp | Apparatus for treating organic waste water and method of treating organic waste water |
CN102630218A (en) * | 2009-11-30 | 2012-08-08 | 株式会社久保田 | Organic wastewater treatment device and organic wastewater treatment method |
CN102630218B (en) * | 2009-11-30 | 2014-05-07 | 株式会社久保田 | Organic wastewater treatment device and organic wastewater treatment method |
Also Published As
Publication number | Publication date |
---|---|
JPH05117B2 (en) | 1993-01-05 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
EXPY | Cancellation because of completion of term |