JPH01210100A - Anaerobic digestion of sludge - Google Patents

Anaerobic digestion of sludge

Info

Publication number
JPH01210100A
JPH01210100A JP63025667A JP2566788A JPH01210100A JP H01210100 A JPH01210100 A JP H01210100A JP 63025667 A JP63025667 A JP 63025667A JP 2566788 A JP2566788 A JP 2566788A JP H01210100 A JPH01210100 A JP H01210100A
Authority
JP
Japan
Prior art keywords
sludge
anaerobic digestion
treatment
high voltage
voltage pulse
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
Application number
JP63025667A
Other languages
Japanese (ja)
Other versions
JPH0438477B2 (en
Inventor
Yoshio Oshima
大嶋 吉雄
Noboru Nonoyama
野々山 登
Teruo Nakagawa
中川 輝雄
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Minister for Public Works for State of New South Wales
Fujita Corp
National Research and Development Agency Public Works Research Institute
Original Assignee
Minister for Public Works for State of New South Wales
Fujita Corp
Public Works Research Institute Ministry of Construction
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 Minister for Public Works for State of New South Wales, Fujita Corp, Public Works Research Institute Ministry of Construction filed Critical Minister for Public Works for State of New South Wales
Priority to JP63025667A priority Critical patent/JPH01210100A/en
Publication of JPH01210100A publication Critical patent/JPH01210100A/en
Publication of JPH0438477B2 publication Critical patent/JPH0438477B2/ja
Granted 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
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel

Landscapes

  • Treatment Of Sludge (AREA)
  • Water Treatment By Electricity Or Magnetism (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、活性汚泥法による下水処理場において発生す
る余剰汚泥のように、主として微生物からなる汚泥の嫌
気性消化を、効率よく行う方法に関するものである。
[Detailed Description of the Invention] [Field of Industrial Application] The present invention relates to a method for efficiently performing anaerobic digestion of sludge mainly composed of microorganisms, such as surplus sludge generated in a sewage treatment plant using an activated sludge method. It is something.

〔従来の技術〕[Conventional technology]

一般的な活性汚泥法による下水処理においては、多量の
初沈汚泥および余剰汚泥を発生する。これらの汚泥は非
常に含水率が高く、濾過による脱水も困難であるから、
そのままでは廃棄も利用も困難である。そこで、微生物
を利用して生化学的に汚泥を分解することにより固形物
をなるべく少なくするとともに発生するメタンガスを有
効に利用するいわゆる嫌気性消化処理を行うことが多い
。しかしながら、従来の嫌気性消化は、標準的な中温消
化すなわち消化温度37℃程度、滞留日数約30日でも
、VS(有機物)分解率は50〜55%程度であり、非
常に効率が悪い。嫌気性消化で特に分解しにくいのは、
主として微生物からなる余剰汚泥である。
In sewage treatment using the general activated sludge method, a large amount of initial settled sludge and surplus sludge are generated. These sludges have extremely high water content and are difficult to dewater by filtration.
As it is, it is difficult to dispose of or use it. Therefore, so-called anaerobic digestion treatment is often performed, which uses microorganisms to biochemically decompose the sludge to reduce the amount of solid matter as much as possible, and to effectively utilize the methane gas generated. However, conventional anaerobic digestion has a VS (organic matter) decomposition rate of about 50 to 55%, which is very inefficient, even with standard mesophilic digestion, that is, the digestion temperature is about 37° C. and the residence time is about 30 days. What is particularly difficult to break down in anaerobic digestion is
This is surplus sludge mainly composed of microorganisms.

効率の悪い汚泥の嫌気性消化法の改良は種々試みられて
いる。その代表的なものは、嫌気性消化に先立ち汚泥に
何らかの前処理を施して汚泥中機生物の細胞壁を破壊す
るものであって、たとえば超音波処理を施す方法(特開
昭58−76200号)、メタンガスによる加圧に続く
減圧処理を施す方法(特開昭56−40497号)など
がある。
Various attempts have been made to improve the inefficient anaerobic digestion of sludge. A typical method is to perform some kind of pretreatment on the sludge prior to anaerobic digestion to destroy the cell walls of organisms in the sludge, such as ultrasonic treatment (Japanese Patent Application Laid-open No. 76200/1983). , a method in which pressurization with methane gas is followed by depressurization treatment (Japanese Unexamined Patent Publication No. 56-40497).

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

本発明の目的は、上記従来の前処理法のいずれとも拠な
る新規な手段により改良された、効率のよい汚泥嫌気性
消化法を提供することにある。
An object of the present invention is to provide an efficient sludge anaerobic digestion method that is improved by new means that are based on any of the above-mentioned conventional pretreatment methods.

〔課題を解決するための手段〕[Means to solve the problem]

本発明が提供する嫌気性消化法は、嫌気性消化処理に先
立って汚泥に高電圧パルスを印加する処理を施すことを
特徴とするものである。
The anaerobic digestion method provided by the present invention is characterized by applying a high voltage pulse to sludge prior to the anaerobic digestion treatment.

汚泥に高電圧パルスを印加すると、電気エネルギーの大
半が汚泥中の微生物の細胞壁に印加され、機械的な膜圧
縮エネルギーに変換されて細胞壁を破壊する。
When a high voltage pulse is applied to sludge, most of the electrical energy is applied to the cell walls of microorganisms in the sludge and is converted into mechanical membrane compression energy, destroying the cell walls.

それにより、主として細胞質からなる可溶性タンパク質
、糖、核酸などが細胞外に溶出し、速やかに嫌気性消化
を受けるようになる。
As a result, soluble proteins, sugars, nucleic acids, etc., which mainly consist of the cytoplasm, are eluted out of the cells and rapidly undergo anaerobic digestion.

上述のような微生物細胞壁の破壊を生じさせるのに必要
な(あるいは好適な)高電圧パルスの特性は、処理する
汚泥の微生物濃度、共存する無機電解質の濃度等によっ
て異なるが、おおむね次の範囲にある。。
The characteristics of the high voltage pulse necessary (or suitable) to cause the destruction of microbial cell walls as described above vary depending on the microbial concentration of the sludge to be treated, the concentration of coexisting inorganic electrolytes, etc., but generally fall within the following range. be. .

被処理汚泥中における電界強度:5〜50KV/e+a
パルス幅:100μSee以上 (好ましくは200〜1000μSeeまたはそれ以上
)パルス波形は方形でお一4ニーとが望ましいが、これ
に限定されるわけではない。なお、高電圧パルスの印加
条件によっては汚泥の電気分解を生じる得るが、それは
消費電力を大きくするだけであって、細胞壁破壊のため
には無意味であるから、電気分解を招く連続通電に等し
いようなパルスの印加は避けることが望ましい。
Electric field strength in sludge to be treated: 5 to 50 KV/e+a
Pulse width: 100 μSee or more (preferably 200 to 1000 μSee or more) The pulse waveform is preferably rectangular and about 14 knees, but is not limited to this. Note that depending on the application conditions of high voltage pulses, electrolysis of sludge may occur, but this only increases power consumption and is meaningless for destroying cell walls, so it is equivalent to continuous energization that causes electrolysis. It is desirable to avoid applying such pulses.

汚泥に高電圧パルスを印加する方法としては、撹拌装置
を付属させた汚泥容器中に電極板を挿入し、微生物細胞
が電極板間に入り込んだとき高電圧パルスを受けるよう
にする方法、電極板間に汚泥を連続的または間欠的に流
して高電圧パルスを受けさせる方法、などがある。パル
ス印加時間は、パルス印加の方法および条件に応じて、
汚泥中の実質的にすべての微生物細胞が少なくとも1回
(好ましくは数回)のパルスを受けるように設定する。
A method of applying high voltage pulses to sludge is to insert an electrode plate into a sludge container equipped with a stirring device so that microbial cells receive a high voltage pulse when they enter between the electrode plates. There is a method in which sludge is passed continuously or intermittently and subjected to high voltage pulses. The pulse application time depends on the pulse application method and conditions.
The arrangement is such that substantially all microbial cells in the sludge receive at least one (preferably several) pulses.

高電圧パルス処理を終わった汚泥は、適量の種汚泥と混
合して、常法により嫌気性消化処理する。
After the high voltage pulse treatment, the sludge is mixed with an appropriate amount of seed sludge and subjected to anaerobic digestion using a conventional method.

〔実施例〕〔Example〕

都市下水処理場から採取した標準活性汚泥の余剰汚泥を
、その有機物(VS)濃度が1.0%になるように濃度
調整した後、2,0OOCCの容器にとり、撹拌しなが
ら、下記の条件で20分間高電圧パルス処理した。
After adjusting the concentration of surplus sludge from standard activated sludge collected from a municipal sewage treatment plant so that its organic matter (VS) concentration was 1.0%, it was placed in a 2,000 OOCC container and stirred under the following conditions. High voltage pulse treatment was performed for 20 minutes.

処理液量:1,500cc 電極二二重円形電極(電極間隔4 am)  2印加電
圧:10,0OOV   電界強度: 25 KV/c
+aパルス幅: 5001ec     パルス間隔:
0.l5ec剋理後、汚泥に2倍量の嫌気性消化済み汚
泥を種汚泥として加え、20日間、中温嫌気性消化させ
た。
Processing liquid volume: 1,500 cc Electrode Double circular electrode (electrode spacing 4 am) 2 Applied voltage: 10,0 OOV Electric field strength: 25 KV/c
+a Pulse width: 5001ec Pulse interval:
0. After 15 ec digestion, twice the amount of anaerobically digested sludge was added to the sludge as seed sludge, and the sludge was subjected to mesophilic anaerobic digestion for 20 days.

比較のため、無処理の上記余剰汚泥についても、同様の
嫌気性消化処理を行なった。
For comparison, the untreated surplus sludge was also subjected to the same anaerobic digestion treatment.

その結果は表1に示したとおりで、高電圧パルス処理を
施すことにより消化効率が顕著に向上した。
The results are shown in Table 1, and the digestion efficiency was significantly improved by applying the high voltage pulse treatment.

表  1 測定項目      実施例   比較例有機物(VS
)分解率(%)   55    41ガス発生量(m
l、/VS−g) 58目        225   1301O日目 
       330   20015日目  8  
  375   24520日目  8    4jD
    290ガス組成(%) メタン         61   57C0,333
6 〔発明の効果〕 実施例の結果から明らかなように、本発明によれば余剰
汚泥の嫌気性消化をきわめて高速かつ効率よく行うこと
ができる。また、本発明の方法において汚泥の前処理手
段として採用した高電圧パルス処理は、純電気的な処理
であるから、電源装置さえ用意すれば汚泥の組成変動に
応じて容易に最適の処理条件を選択することができ、処
理装置も小型かつ簡単なもので済むという利点がある。
Table 1 Measurement items Example Comparative example Organic matter (VS
) Decomposition rate (%) 55 41 Gas generation amount (m
l, /VS-g) 58th day 225 1301Oth day
330 20015th day 8
375 24520th day 8 4jD
290 Gas composition (%) Methane 61 57C0,333
6 [Effects of the Invention] As is clear from the results of the Examples, according to the present invention, anaerobic digestion of excess sludge can be performed extremely quickly and efficiently. Furthermore, since the high voltage pulse treatment adopted as a pretreatment means for sludge in the method of the present invention is a purely electrical treatment, it is possible to easily adjust the optimum treatment conditions according to changes in the composition of the sludge as long as a power supply is provided. There are advantages in that the processing device can be selected and that the processing device can be small and simple.

Claims (1)

【特許請求の範囲】[Claims] 活性汚泥法による下水処理において発生する余剰汚泥等
主として微生物からなる汚泥を嫌気性消化処理するに当
たり、嫌気性消化処理に先立って汚泥に高電圧パルスを
印加する処理を施すことを特徴とする汚泥の嫌気性消化
法。
When anaerobically digesting sludge mainly composed of microorganisms, such as surplus sludge generated in sewage treatment by the activated sludge method, the sludge is treated by applying a high voltage pulse to the sludge prior to the anaerobic digestion treatment. Anaerobic digestion.
JP63025667A 1988-02-08 1988-02-08 Anaerobic digestion of sludge Granted JPH01210100A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63025667A JPH01210100A (en) 1988-02-08 1988-02-08 Anaerobic digestion of sludge

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63025667A JPH01210100A (en) 1988-02-08 1988-02-08 Anaerobic digestion of sludge

Publications (2)

Publication Number Publication Date
JPH01210100A true JPH01210100A (en) 1989-08-23
JPH0438477B2 JPH0438477B2 (en) 1992-06-24

Family

ID=12172138

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63025667A Granted JPH01210100A (en) 1988-02-08 1988-02-08 Anaerobic digestion of sludge

Country Status (1)

Country Link
JP (1) JPH01210100A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100492297B1 (en) * 2002-12-11 2005-06-02 (주)대우건설 Method and device for sludge treatment using high voltage pulse
US7001520B2 (en) 1995-11-02 2006-02-21 Opencel Llc. Method for treating waste-activated sludge using elecroporation
US7507341B2 (en) 1999-01-13 2009-03-24 Opencel Llc Method of and apparatus for converting biological materials into energy resources
US7572369B2 (en) 2007-02-16 2009-08-11 Opencel Llc System for supporting denitrification
CN105873862A (en) * 2013-11-06 2016-08-17 Arc阿罗马珀尔公司 Method comprising separation and high voltage pulse treatment before digestion or further purification

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7001520B2 (en) 1995-11-02 2006-02-21 Opencel Llc. Method for treating waste-activated sludge using elecroporation
US7645382B2 (en) 1995-11-02 2010-01-12 Opencell Llc Apparatus for converting biological materials into energy resources
US7507341B2 (en) 1999-01-13 2009-03-24 Opencel Llc Method of and apparatus for converting biological materials into energy resources
KR100492297B1 (en) * 2002-12-11 2005-06-02 (주)대우건설 Method and device for sludge treatment using high voltage pulse
US7572369B2 (en) 2007-02-16 2009-08-11 Opencel Llc System for supporting denitrification
US7695621B2 (en) 2007-02-16 2010-04-13 Opencel Llc Method of supporting denitrification
CN105873862A (en) * 2013-11-06 2016-08-17 Arc阿罗马珀尔公司 Method comprising separation and high voltage pulse treatment before digestion or further purification

Also Published As

Publication number Publication date
JPH0438477B2 (en) 1992-06-24

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