JPS5845796A - Anaerobic digestion of highly-concentrated organic waste water - Google Patents
Anaerobic digestion of highly-concentrated organic waste waterInfo
- Publication number
- JPS5845796A JPS5845796A JP56145720A JP14572081A JPS5845796A JP S5845796 A JPS5845796 A JP S5845796A JP 56145720 A JP56145720 A JP 56145720A JP 14572081 A JP14572081 A JP 14572081A JP S5845796 A JPS5845796 A JP S5845796A
- Authority
- JP
- Japan
- Prior art keywords
- vessel
- digesting
- concentrated
- liquid
- highly
- 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
Classifications
-
- Y02W10/12—
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
Description
【発明の詳細な説明】
この発明は、し尿のような高濃度有機性廃水を嫌気性消
化反応する方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for anaerobic digestion of highly concentrated organic wastewater such as human waste.
高濃度有機性廃水に対して適用される嫌気性消化法では
、加温、攪拌によって1質と嫌気性細菌とを接触させ、
基質の分解とメタンガス等の代謝生産物の生成を促す作
用と、嫌気性細菌を多重に含有する汚泥と脱離液とを分
離する作用とによって所定のも理が行われる。この消化
汚泥と脱離液との分離は、従来の方法で°は静置による
。沈降分離作用によっているため、その分離効果は、長
い滞留時間をかけても充分でない場合が多く、脱離波と
ともに多重の固形物が流出するという欠点がある。とく
に被処理液中の基質力馬雌分解性で嫌気性細菌の増殖速
度が遅くなる場合C:は、細菌の脱離液への流出は消化
処理の過負荷状態を招き、消化効率の低下の原因となる
。また細菌の流出を防止するために沈降分離時間!いた
ずらに長くすると、スカム発生頻度を高めてガス発生を
抑制したり、被処理液中に混入している砂などの固形物
が沈積して槽の有効容積を縮小する等の別の欠点が生じ
る。In the anaerobic digestion method applied to highly concentrated organic wastewater, one substance is brought into contact with anaerobic bacteria by heating and stirring.
A predetermined process is carried out by the action of promoting the decomposition of the substrate and the production of metabolic products such as methane gas, and the action of separating the desorbed liquid from the sludge containing multiple anaerobic bacteria. The separation of the digested sludge and the desorbed liquid is carried out by a conventional method, in which case the sludge is allowed to stand still. Because it relies on sedimentation separation, the separation effect is often not sufficient even after a long residence time, and there is a drawback that multiple solids flow out together with desorption waves. In particular, when the growth rate of anaerobic bacteria slows down due to the decomposition of the substrate in the liquid to be treated (C), the flow of bacteria into the desorbed liquid will lead to overload of the digestion process, resulting in a decrease in digestion efficiency. Cause. Sedimentation separation time to also prevent bacteria from flowing out! If the length is unnecessarily long, other drawbacks will occur, such as increasing the frequency of scum generation and suppressing gas generation, and reducing the effective volume of the tank due to the sedimentation of solids such as sand mixed in the liquid to be treated. .
この発明は、上記のような欠点を伴なわずに、嫌気性消
化反応の効率を高め、後続の処理の負荷を低減させるこ
とができる嫌気性消化方法を提供することt目的として
いる。An object of the present invention is to provide an anaerobic digestion method that can increase the efficiency of the anaerobic digestion reaction and reduce the burden of subsequent processing without the above-mentioned drawbacks.
つぎにこの発明方法の工程の一例を図面にしたがって説
明する。第1図に・・おいて、し尿のような高濃度有機
性廃水は、まず消化槽1に導入され、嫌気性条件のもと
で消化処理されることζ二よってノ!ン発酵を行う。そ
して消化液は、限外r過装置2に送られて圧力差により
濾過される。P液は脱離液として後続の2次処理工程に
送られ、−縮液の一部は消化槽1に返送され、残部は命
剰汚泥として排iされる。なお濃縮液は全量消化槽1に
返送し、消化槽1より直接奈剰汚泥を排出してもよい。Next, an example of the steps of the method of this invention will be explained with reference to the drawings. In Figure 1, highly concentrated organic wastewater such as human waste is first introduced into the digestion tank 1 and digested under anaerobic conditions. Fermentation is carried out. The digestive fluid is then sent to the ultrafiltration device 2 and filtered by the pressure difference. The P liquid is sent to the subsequent secondary treatment process as a desorbed liquid, a part of the condensed liquid is returned to the digestion tank 1, and the remainder is discharged as dead sludge. Incidentally, the entire concentrated liquid may be returned to the digestion tank 1, and the raw sludge may be directly discharged from the digestion tank 1.
また限外濾過装置2は、消化槽1内に直接に収容させて
もよい。この場合には、消化槽1内のメタン発酵による
ガス圧や、消化槽混合液の水位圧が濾過圧の一部として
利用できるので効率的となる。Further, the ultrafiltration device 2 may be housed directly within the digestion tank 1. In this case, the gas pressure caused by methane fermentation in the digestion tank 1 and the water level pressure of the mixed liquid in the digestion tank can be used as part of the filtration pressure, which is efficient.
消化槽1内でメタン発酵を効率よく行わせるためには、
槽内の微生物―度を高水準に保つこと、−嫌気性条件を
確実に保つこと%およびよく攪拌することが重要である
。この発明によれば、消化槽1内で生じた消化液は、限
外濾過装置2の作用で脱離液を除去する゛ことによって
濃縮されるので、消化槽1内での処理能力を高く維持で
きるほか。In order to efficiently carry out methane fermentation in the digestion tank 1,
It is important to maintain a high level of microorganisms in the tank, to ensure that anaerobic conditions are maintained, and to mix well. According to this invention, the digestive juice produced in the digestion tank 1 is concentrated by removing the desorbed liquid by the action of the ultrafiltration device 2, so that the processing capacity in the digestion tank 1 can be maintained at a high level. In addition to being able to.
濃縮液が空気と接触することはないのでメタン菌の活性
を損うことがない。Since the concentrated liquid does not come into contact with air, the activity of methane bacteria is not impaired.
以上のようにこの発明艦=よれば、消化槽内における嫌
気性消化処理によって生じた消化液は、限外濾過装置に
よって濃縮され、P液だけが脱離液として、2次処理工
程に送られる。したがって嫌気性消化処巡の処理能力を
高め、2次処理工程の負萄の薯減を達成できる。さらに
消化槽内における沈降分離機能を軽減し、もしくは不要
とすることができるので、消化槽総容積を小さくできる
。しかも限外濾過の濃縮液は大気と接触することなく循
環されるので、メタン菌の活性を損うことがない。また
消化液を限外濾過装置にポンプで圧送する場合には、濃
縮液の排圧を消化槽内の攪拌に利用することも可能であ
る。なお、上記実施例では消化液を直接限外1遇するこ
とのみ記載したが、消化液を沈殿処理、マイクロストレ
ーナ、砂濾過機などで一度固液分離して得られた処理水
を限外濾過処理してもよい。、As described above, according to this inventor, the digestive fluid produced by anaerobic digestion in the digestion tank is concentrated by the ultrafiltration device, and only the P solution is sent to the secondary treatment process as the desorbed fluid. . Therefore, the throughput of the anaerobic digestion process can be increased and the burden of the secondary treatment process can be reduced. Furthermore, since the sedimentation separation function within the digestion tank can be reduced or eliminated, the total volume of the digestion tank can be reduced. Moreover, since the ultrafiltrated concentrate is circulated without coming into contact with the atmosphere, it does not impair the activity of methane bacteria. Furthermore, when the digestive fluid is pumped to the ultrafiltration device, the exhaust pressure of the concentrated fluid can be used for stirring inside the digestion tank. In addition, in the above example, only the direct ultrafiltration of the digestive fluid was described, but the treated water obtained by solid-liquid separation of the digestive fluid by precipitation treatment, a micro strainer, a sand filter, etc., may be subjected to ultrafiltration. May be processed. ,
図はこの発明方法の工程の一例を示す、フローシートで
ある。The figure is a flow sheet showing an example of the steps of the method of this invention.
Claims (1)
化液を限外濾過装置によって限外濾過し、濃縮液の少な
くとも一部は上記消化槽に返送し、r液は脱離液として
外部に取出すことを特徴とする高一度有機性廃水の嫌気
性消化方法。Highly concentrated organic wastewater is anaerobically digested in a digestion tank, this digestive fluid is ultrafiltered by an ultrafiltration device, at least a part of the concentrated liquid is returned to the digestion tank, and the r liquid is used as a desorbed liquid. A method for anaerobic digestion of high-temperature organic wastewater, characterized by taking it out to the outside.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP56145720A JPS5845796A (en) | 1981-09-16 | 1981-09-16 | Anaerobic digestion of highly-concentrated organic waste water |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP56145720A JPS5845796A (en) | 1981-09-16 | 1981-09-16 | Anaerobic digestion of highly-concentrated organic waste water |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5845796A true JPS5845796A (en) | 1983-03-17 |
JPH0318955B2 JPH0318955B2 (en) | 1991-03-13 |
Family
ID=15391564
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP56145720A Granted JPS5845796A (en) | 1981-09-16 | 1981-09-16 | Anaerobic digestion of highly-concentrated organic waste water |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5845796A (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS62273100A (en) * | 1986-05-22 | 1987-11-27 | Kubota Ltd | Treatment of sewage |
JPS63305997A (en) * | 1987-06-05 | 1988-12-13 | Ebara Infilco Co Ltd | Process for treating sewage and wastes |
JPH03199A (en) * | 1989-05-25 | 1991-01-07 | Ebara Infilco Co Ltd | Methane fermentation treatment |
JP2010017614A (en) * | 2008-07-08 | 2010-01-28 | Kurita Water Ind Ltd | Method and apparatus for treating organic wastewater |
JP2014008431A (en) * | 2012-06-28 | 2014-01-20 | Swing Corp | Method and apparatus for anaerobic digestion treatment of organic wastewater |
JP2015157291A (en) * | 2015-06-10 | 2015-09-03 | 株式会社神鋼環境ソリューション | Water treatment method and apparatus |
US10781119B2 (en) | 2013-02-22 | 2020-09-22 | Bl Technologies, Inc. | Membrane assembly for supporting a biofilm |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4840971A (en) * | 1971-10-01 | 1973-06-15 | ||
JPS54102056A (en) * | 1978-01-27 | 1979-08-11 | Ebara Infilco Co Ltd | Process for high-speed treatment of waste water |
JPS55149681A (en) * | 1979-05-10 | 1980-11-21 | Kuraray Co Ltd | Disposal method for waste water disposed with activated sludge |
-
1981
- 1981-09-16 JP JP56145720A patent/JPS5845796A/en active Granted
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4840971A (en) * | 1971-10-01 | 1973-06-15 | ||
JPS54102056A (en) * | 1978-01-27 | 1979-08-11 | Ebara Infilco Co Ltd | Process for high-speed treatment of waste water |
JPS55149681A (en) * | 1979-05-10 | 1980-11-21 | Kuraray Co Ltd | Disposal method for waste water disposed with activated sludge |
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS62273100A (en) * | 1986-05-22 | 1987-11-27 | Kubota Ltd | Treatment of sewage |
JPS63305997A (en) * | 1987-06-05 | 1988-12-13 | Ebara Infilco Co Ltd | Process for treating sewage and wastes |
JPH0325238B2 (en) * | 1987-06-05 | 1991-04-05 | Ebara Infuiruko Kk | |
JPH03199A (en) * | 1989-05-25 | 1991-01-07 | Ebara Infilco Co Ltd | Methane fermentation treatment |
JPH0567358B2 (en) * | 1989-05-25 | 1993-09-24 | Ebara Infilco | |
JP2010017614A (en) * | 2008-07-08 | 2010-01-28 | Kurita Water Ind Ltd | Method and apparatus for treating organic wastewater |
JP2014008431A (en) * | 2012-06-28 | 2014-01-20 | Swing Corp | Method and apparatus for anaerobic digestion treatment of organic wastewater |
US10781119B2 (en) | 2013-02-22 | 2020-09-22 | Bl Technologies, Inc. | Membrane assembly for supporting a biofilm |
US11724947B2 (en) | 2013-02-22 | 2023-08-15 | Bl Technologies, Inc. | Membrane assembly for supporting a biofilm |
JP2015157291A (en) * | 2015-06-10 | 2015-09-03 | 株式会社神鋼環境ソリューション | Water treatment method and apparatus |
Also Published As
Publication number | Publication date |
---|---|
JPH0318955B2 (en) | 1991-03-13 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JPS5845796A (en) | Anaerobic digestion of highly-concentrated organic waste water | |
JP3152357B2 (en) | Anaerobic treatment method and apparatus for high-concentration organic wastewater containing organic suspended matter | |
JP5801769B2 (en) | Method and apparatus for anaerobic digestion treatment of organic wastewater | |
JP5873736B2 (en) | Organic wastewater treatment method and treatment apparatus | |
CN109574395B (en) | Method for purifying and deodorizing wastewater generated in production process of fermented cordyceps sinensis powder | |
JP3846138B2 (en) | Method and apparatus for anaerobic treatment of liquid containing starch particles | |
JPH05277493A (en) | Method for treatment of waste water containing oil | |
JP2000070908A (en) | Method for anaerobically digesting organic waste | |
JPH04131199A (en) | Concurrent disposal of night soil and septic tank sludge | |
JPH05253594A (en) | Anaerobic treatment of waste water | |
JPS60150896A (en) | Treatment of sludge | |
CN112062366A (en) | Coal-fired power plant desulfurization wastewater comprehensive treatment system and method | |
US3300401A (en) | Process for dewatering organic sludge which has been separated during treatment of waste water | |
JPH1119696A (en) | Treatment of sludge waste water and water purifier | |
JP4010733B2 (en) | Organic wastewater treatment method and apparatus | |
JP2002224686A (en) | Anaerobic treatment method and equipment for starch particle-containing liquid | |
CN217103495U (en) | Waste acid liquid treatment system | |
CN220745633U (en) | Nanofiltration concentrated water COD removal system | |
CN210287073U (en) | Diamond wire section wastewater treatment system | |
CN210559934U (en) | Pure oxygen aeration system for wastewater treatment | |
CN215924819U (en) | Sweet potato protein extraction and separation device | |
JP3759055B2 (en) | Organic wastewater treatment apparatus and method | |
CN114477529B (en) | Treatment method of acidic wastewater containing nitrogen, phosphorus and fluorine | |
KR20190000157A (en) | The method and apparatus for treatment of livestock manure, livestock wastewater or livestock washing water using ceramic membrane | |
CN212655638U (en) | Fermentation wastewater treatment reclaimed water recycling and sterilizing device |