JP2003039039A - Treatment system for organic waste - Google Patents

Treatment system for organic waste

Info

Publication number
JP2003039039A
JP2003039039A JP2001230140A JP2001230140A JP2003039039A JP 2003039039 A JP2003039039 A JP 2003039039A JP 2001230140 A JP2001230140 A JP 2001230140A JP 2001230140 A JP2001230140 A JP 2001230140A JP 2003039039 A JP2003039039 A JP 2003039039A
Authority
JP
Japan
Prior art keywords
methane fermentation
fermentation tank
organic waste
treatment system
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.)
Pending
Application number
JP2001230140A
Other languages
Japanese (ja)
Inventor
Takeshi Matsushiro
代 武 士 松
Kazuo Shibazaki
崎 和 夫 柴
Tetsuya Mine
哲 哉 峰
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.)
Toshiba Corp
Original Assignee
Toshiba Corp
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 Toshiba Corp filed Critical Toshiba Corp
Priority to JP2001230140A priority Critical patent/JP2003039039A/en
Publication of JP2003039039A publication Critical patent/JP2003039039A/en
Pending 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

  • Processing Of Solid Wastes (AREA)
  • Treatment Of Sludge (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a treatment system for organic wastes whereby the inhibition of a methane fermentation action by ammoniac nitrogen can be avoided. SOLUTION: The treatment system is provided with a methane fermentation tank 3 that treats organic wastes by mesophilic methanogenic bacteria and a pump that feeds diluting water into the tank 3. The ammoniac nitrogen concentration in the tank 3 is detected with an ammoniac nitrogen concentration detecting part 4. Diluting water is fed into the tank 3 by the pump 6 according to a signal from the detecting part 4.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、有機性廃棄物をメ
タン発酵により処理する有機性廃棄物の処理システムに
関する。
TECHNICAL FIELD The present invention relates to an organic waste treatment system for treating organic waste by methane fermentation.

【0002】[0002]

【従来の技術】メタン発酵により有機性廃棄物を処理す
るシステムを制御する場合、測定項目としてガス発生速
度、ガス組成、液相pH、揮発性有機酸(以下、VFA
と略称する)濃度、アンモニア濃度などが用いられる。
2. Description of the Related Art When controlling a system for treating organic waste by methane fermentation, the measurement items include gas generation rate, gas composition, liquid phase pH, volatile organic acid (hereinafter referred to as VFA).
Abbreviated as “) concentration, ammonia concentration, etc. are used.

【0003】生ごみ等のメタン発酵において、たんぱく
質の分解にともないアンモニアが高濃度に蓄積し、メタ
ン発酵に阻害を及ぼす可能性がある。
In methane fermentation of food waste and the like, there is a possibility that ammonia is accumulated at a high concentration as the protein is decomposed and the methane fermentation is inhibited.

【0004】[0004]

【発明が解決しようとする課題】生ごみのメタン発酵で
広く利用されている高温メタン菌はアンモニア性窒素濃
度が2500mg/L以上になるとメタン生成活性が低下
するという報告があり、中温メタン菌の方がアンモニア
性窒素に対する耐性が高いとされている。生ごみを無希
釈処理した場合、メタン槽内のアンモニア性窒素濃度は
およそ3,000〜8,000mg/Lとなる。高温メ
タン菌ではアンモニア阻害のため処理が困難であるた
め、2倍程度の希釈が必要となり、システム全体が大型
化するという問題がある。
[Problems to be Solved by the Invention] It has been reported that thermophilic methane bacteria, which are widely used in methane fermentation of food waste, have a reduced methanogenic activity when the concentration of ammonia nitrogen exceeds 2500 mg / L. It is said that the one with higher resistance to ammonia nitrogen. When the raw garbage is treated without dilution, the concentration of ammonia nitrogen in the methane tank becomes about 3,000 to 8,000 mg / L. Since it is difficult to treat ammonia in high temperature methane bacteria due to the inhibition of ammonia, it is necessary to dilute the bacterium by about twice, and there is a problem that the entire system becomes large.

【0005】また、特開2000−93192にあるよ
うに、遊離アンモニア濃度を検出してメタン発酵の阻害
を未然に防止する発明もあるが、高価な分析機器や熟練
した技術者が必要となる問題がある。
Further, as disclosed in Japanese Patent Application Laid-Open No. 2000-93192, there is an invention for detecting the concentration of free ammonia to prevent the inhibition of methane fermentation in advance, but there is a problem that expensive analytical equipment and a skilled technician are required. There is.

【0006】本発明はこのような点を考慮してなされた
ものであり、メタン菌として中温メタン菌を用いて、必
要最小限の希釈水によってメタン発酵に対するアンモニ
アによる阻害を回避することができる有機性廃棄物の処
理システムを提供することを目的とする。
The present invention has been made in view of the above points, and an organic methane bacterium which can prevent the inhibition of methane fermentation by ammonia by using a mesophilic methane bacterium as a methane bacterium with a minimum necessary dilution water. The purpose is to provide a treatment system for toxic waste.

【0007】[0007]

【課題を解決するための手段】本発明は、有機性廃棄物
を処理するメタン発酵槽と、メタン発酵槽へ水を供給す
る水供給部と、メタン発酵槽に設置されたアンモニア性
窒素濃度検出部と、アンモニア性窒素濃度検出部からの
信号に基づいて水供給部を制御してメタン発酵槽へ水を
供給し、メタン発酵槽を希釈する制御部と、を備えたこ
とを特徴とする有機性廃棄物の処理システムである。
The present invention is directed to a methane fermentation tank for treating organic waste, a water supply unit for supplying water to the methane fermentation tank, and an ammoniacal nitrogen concentration detection installed in the methane fermentation tank. And a control unit that controls the water supply unit based on a signal from the ammonia nitrogen concentration detection unit to supply water to the methane fermentation tank and dilute the methane fermentation tank. It is a treatment system for toxic waste.

【0008】本発明は、制御部はメタン発酵槽内のアン
モニア性窒素濃度が5000mg/L以下となるよう水供
給部を制御してメタン発酵槽を希釈することを特徴とす
る有機性廃棄物の処理システムである。
The present invention is characterized in that the control unit controls the water supply unit so that the concentration of ammonia nitrogen in the methane fermentation tank is 5000 mg / L or less and dilutes the methane fermentation tank. It is a processing system.

【0009】本発明は、メタン発酵槽に設置され、メタ
ン発酵槽から発生するバイオガスから水分を分離するミ
ストセパレータを更に備え、ミストセパレータに水供給
部が接続されていることを特徴とする有機性廃棄物の処
理システムである。
The present invention further comprises a mist separator installed in a methane fermentation tank for separating water from biogas generated from the methane fermentation tank, and a water supply unit is connected to the mist separator. It is a treatment system for toxic waste.

【0010】[0010]

【発明の実施の形態】以下、図面を参照して本発明の実
施形態について説明する。
BEST MODE FOR CARRYING OUT THE INVENTION Embodiments of the present invention will be described below with reference to the drawings.

【0011】図1は本発明による有機性廃棄物の処理シ
ステムを示す構成図である。
FIG. 1 is a block diagram showing an organic waste treatment system according to the present invention.

【0012】図1に示すように、有機性廃棄物の処理シ
ステムは、有機性廃棄物を貯留する原液槽1と、有機性
廃棄物を供給するポンプ2と、有機性廃棄物を中温メタ
ン菌によりメタン発酵処理するメタン発酵槽3と、メタ
ン発酵槽3に設置されメタン発酵槽3内のアンモニア性
窒素濃度を検出するアンモニア性窒素濃度検出部4と、
メタン発酵槽3に設置されメタン発酵槽3から発生する
バイオガス中の水分を分離するミストセパレータ5とを
備えている。
As shown in FIG. 1, the system for treating organic waste comprises a stock solution tank 1 for storing the organic waste, a pump 2 for supplying the organic waste, and a mesophilic methane bacterium for treating the organic waste. A methane fermentation tank 3 for performing methane fermentation treatment by means of the above, and an ammoniacal nitrogen concentration detecting unit 4 installed in the methane fermentation tank 3 for detecting the ammoniacal nitrogen concentration in the methane fermentation tank 3.
The methane fermentation tank 3 is provided with a mist separator 5 for separating water in biogas generated from the methane fermentation tank 3.

【0013】メタン発酵槽3には希釈水がポンプ(水供
給部)6により供給され、このポンプ6はアンモニア性
窒素濃度検出部4からの信号に基づいて制御部7により
制御される。なお、制御部7によりポンプ(水供給部)
6aを制御してミストセパレータ5内の希釈水をメタン
発酵槽3内へ循環させても良い。
Dilution water is supplied to the methane fermentation tank 3 by a pump (water supply unit) 6, and the pump 6 is controlled by a control unit 7 based on a signal from the ammonia nitrogen concentration detection unit 4. A pump (water supply unit) is controlled by the control unit 7.
The dilution water in the mist separator 5 may be circulated into the methane fermentation tank 3 by controlling 6a.

【0014】次に、このような構成からなる本実施の形
態の作用について説明する。
Next, the operation of this embodiment having such a configuration will be described.

【0015】原液槽1に貯留された有機性廃棄物は、ポ
ンプ2によりメタン発酵槽3へ送られる。有機性廃棄物
はこのメタン発酵槽3内で、中温メタン菌を用いたメタ
ン発酵により、メタンを主成分とするバイオガスに分解
される。メタン発酵槽3内のアンモニア性窒素濃度はア
ンモニア性窒素濃度検出部4で検出される。制御部4は
このアンモニア性窒素濃度の検出値が一定値、例えば後
述のように5000mg/Lを超えた場合、ポンプ6によ
って必要最小限の一定量の希釈水をメタン発酵槽3内へ
供給する。この場合、希釈水の供給量を削減するため
に、ミストセパレータ4で分離された水分をポンプ6a
によりメタン発酵槽3内へ送ってもよい。
The organic waste stored in the stock solution tank 1 is sent to the methane fermentation tank 3 by the pump 2. The organic waste is decomposed into biogas containing methane as a main component in the methane fermentation tank 3 by methane fermentation using mesophilic methane bacteria. The ammonia nitrogen concentration in the methane fermentation tank 3 is detected by the ammonia nitrogen concentration detector 4. When the detected value of this ammoniacal nitrogen concentration exceeds a constant value, for example, 5000 mg / L as described later, the control unit 4 supplies a required minimum amount of dilution water into the methane fermentation tank 3 by a pump 6. . In this case, in order to reduce the amount of dilution water supplied, the water separated by the mist separator 4 is pumped by the pump 6a.
May be sent to the methane fermentation tank 3.

【0016】図2および図3にアンモニア性窒素と揮発
性有機酸濃度の関係を示す。
2 and 3 show the relationship between ammoniacal nitrogen and the concentration of volatile organic acids.

【0017】ここで図2はアンモニア性窒素と、酢酸お
よびプロピオン酸(揮発性有機酸(VFA))との関係
を示す図である。また図3は、アンモニア性窒素と、酢
酸およびプロピオン酸(揮発性有機酸(VFA))との
関係を経過日数に対応させて示す図である。生ごみを無
希釈で処理した場合、メタン発酵槽3内のアンモニア性
窒素濃度は3000〜8000mg/Lとなる。このと
きメタン菌がアンモニア性窒素の馴養が十分でないと、
アンモニア性窒素濃度が5000mg/Lを超えた場
合、メタン発酵槽3内の酢酸およびプロピオン酸の濃度
が上昇し、メタン発酵槽3内のメタン発酵作用運転が困
難となる可能性がある(図2および図3)。
FIG. 2 is a diagram showing the relationship between ammoniacal nitrogen and acetic acid and propionic acid (volatile organic acid (VFA)). FIG. 3 is a diagram showing the relationship between ammoniacal nitrogen and acetic acid and propionic acid (volatile organic acid (VFA)) in association with the elapsed days. When the raw garbage is treated without dilution, the concentration of ammonia nitrogen in the methane fermentation tank 3 becomes 3000 to 8000 mg / L. At this time, if the methane bacteria are not acclimatized with ammoniacal nitrogen,
When the concentration of ammonia nitrogen exceeds 5000 mg / L, the concentrations of acetic acid and propionic acid in the methane fermentation tank 3 increase, which may make the methane fermentation operation in the methane fermentation tank 3 difficult (see FIG. 2). And FIG. 3).

【0018】すなわち図3に示すように、アンモニア性
窒素濃度が5000mg/Lを超えた場合、酢酸およびプ
ロピオン酸の濃度が上昇してメタン発酵作用に困難が生
じることがある。この場合、制御部4がポンプ6を制御
して一定量の希釈水をメタン発酵槽3内へ供給してメタ
ン発酵槽3内を希釈することにより、アンモニア性窒素
濃度を5000mg/L以下とすることができる。このこ
とにより酢酸およびプロピオン酸の濃度を低下させて、
メタン発酵作用を回復させることができる。
That is, as shown in FIG. 3, when the concentration of ammonia nitrogen exceeds 5000 mg / L, the concentration of acetic acid and propionic acid increases, which may cause difficulty in the methane fermentation action. In this case, the control unit 4 controls the pump 6 to supply a fixed amount of dilution water into the methane fermentation tank 3 to dilute the inside of the methane fermentation tank 3 so that the ammonia nitrogen concentration becomes 5000 mg / L or less. be able to. This reduces the concentration of acetic acid and propionic acid,
The methane fermentation action can be restored.

【0019】本実施の形態によれば、メタン発酵槽3内
のアンモニア性窒素濃度がある一定値を超えた場合、一
時的にメタン発酵槽3内へ必要最小限となる一定量の希
釈水を供給することによって、有機性廃棄物を希釈する
ことができる。このように有機性廃棄物を希釈すること
により、必要最小限とすることができ、このためアンモ
ニア性窒素によるメタン発酵作用に対する阻害を回避す
ることができる。
According to the present embodiment, when the concentration of ammonia nitrogen in the methane fermentation tank 3 exceeds a certain value, a fixed minimum amount of dilution water is temporarily supplied to the methane fermentation tank 3. By supplying, the organic waste can be diluted. By diluting the organic waste in this manner, it can be minimized, and thus the inhibition of the methane fermentation action by ammonia nitrogen can be avoided.

【0020】[0020]

【発明の効果】以上説明したように、本発明によれば、
メタン発酵槽内のアンモニア性窒素濃度が一定値を超え
た場合、一時的にメタン発酵槽内へ一定量の希釈水を供
給することによって、アンモニア性窒素によるメタン発
酵作用に対する阻害を回避することができる。
As described above, according to the present invention,
When the concentration of ammonia nitrogen in the methane fermentation tank exceeds a certain value, it is possible to avoid the inhibition of the methane fermentation action by ammonia nitrogen by temporarily supplying a certain amount of dilution water to the methane fermentation tank. it can.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明による有機性廃棄物の処理システムの実
施の形態を示す構成図。
FIG. 1 is a configuration diagram showing an embodiment of an organic waste treatment system according to the present invention.

【図2】アンモニア性窒素と、酢酸およびプロピオン酸
との関係を示す図。
FIG. 2 is a diagram showing a relationship between ammoniacal nitrogen and acetic acid and propionic acid.

【図3】アンモニア性窒素と、酢酸およびプロピオン酸
との関係を示す図。
FIG. 3 is a diagram showing a relationship between ammoniacal nitrogen and acetic acid and propionic acid.

【符号の説明】[Explanation of symbols]

1 原液槽 2 ポンプ 3 メタン発酵槽 4 濃度検出部 5 ミストセパレータ 6 ポンプ 6a ポンプ 7 制御部 1 stock solution tank 2 pumps 3 methane fermentation tank 4 Concentration detector 5 mist separator 6 pumps 6a pump 7 control unit

───────────────────────────────────────────────────── フロントページの続き (72)発明者 峰 哲 哉 東京都港区芝浦一丁目1番1号 株式会社 東芝本社事務所内 Fターム(参考) 4D004 AA01 AA03 BA03 CA18 CB04 CC07 DA01 DA02 DA10 4D059 AA07 BA12 BA22 EA20 EB11   ─────────────────────────────────────────────────── ─── Continued front page    (72) Inventor Tetsuya Mine             1-1 Shibaura, Minato-ku, Tokyo Co., Ltd.             Toshiba headquarters office F-term (reference) 4D004 AA01 AA03 BA03 CA18 CB04                       CC07 DA01 DA02 DA10                 4D059 AA07 BA12 BA22 EA20 EB11

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】有機性廃棄物を処理するメタン発酵槽と、 メタン発酵槽へ水を供給する水供給部と、 メタン発酵槽に設置されたアンモニア性窒素濃度検出部
と、 アンモニア性窒素濃度検出部からの信号に基づいて水供
給部を制御してメタン発酵槽へ水を供給し、メタン発酵
槽を希釈する制御部と、を備えたことを特徴とする有機
性廃棄物の処理システム。
1. A methane fermentation tank for treating organic waste, a water supply unit for supplying water to the methane fermentation tank, an ammonia nitrogen concentration detection unit installed in the methane fermentation tank, and an ammonia nitrogen concentration detection unit. A system for treating organic waste, comprising: a control unit that controls a water supply unit based on a signal from the unit to supply water to the methane fermentation tank and dilute the methane fermentation tank.
【請求項2】制御部はメタン発酵槽内のアンモニア性窒
素濃度が5000mg/L以下となるよう水供給部を制御
してメタン発酵槽を希釈することを特徴とする請求項1
記載の有機性廃棄物の処理システム。
2. The control unit controls the water supply unit to dilute the methane fermentation tank so that the concentration of ammonia nitrogen in the methane fermentation tank becomes 5000 mg / L or less.
The described organic waste treatment system.
【請求項3】メタン発酵槽に設置され、メタン発酵槽か
ら発生するバイオガスから水分を分離するミストセパレ
ータを更に備え、 ミストセパレータに水供給部が接続されていることを特
徴とする請求項1記載の有機性廃棄物の処理システム。
3. A mist separator installed in a methane fermentation tank, for separating water from biogas generated from the methane fermentation tank, further comprising a water supply unit connected to the mist separator. The described organic waste treatment system.
JP2001230140A 2001-07-30 2001-07-30 Treatment system for organic waste Pending JP2003039039A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001230140A JP2003039039A (en) 2001-07-30 2001-07-30 Treatment system for organic waste

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001230140A JP2003039039A (en) 2001-07-30 2001-07-30 Treatment system for organic waste

Publications (1)

Publication Number Publication Date
JP2003039039A true JP2003039039A (en) 2003-02-12

Family

ID=19062390

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2001230140A Pending JP2003039039A (en) 2001-07-30 2001-07-30 Treatment system for organic waste

Country Status (1)

Country Link
JP (1) JP2003039039A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007117948A (en) * 2005-10-31 2007-05-17 Ebara Corp Method and apparatus for treating high-concentration organic waste liquid
JP2007237055A (en) * 2006-03-07 2007-09-20 Toshiba Corp Organic waste water treatment method and arrangement
EP2151279A1 (en) 2008-08-04 2010-02-10 Zweckverband Abfallbehandlung Kahlenberg Method for operating a mechanical-biological waste treatment assembly with a process water circuit
JP2010069417A (en) * 2008-09-18 2010-04-02 Fuji Electric Holdings Co Ltd Methane fermentation apparatus

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH09192696A (en) * 1996-01-25 1997-07-29 Meidensha Corp Monitor controller of anaerobic digestion tank
JPH11309438A (en) * 1998-05-01 1999-11-09 Ataka Constr & Eng Co Ltd Waste treating method
JP2000015231A (en) * 1998-07-06 2000-01-18 Kubota Corp Method for methane fermentation of organic waste
JP2000070908A (en) * 1998-08-31 2000-03-07 Kubota Corp Method for anaerobically digesting organic waste
JP2001162298A (en) * 1999-12-06 2001-06-19 Ishikawajima Harima Heavy Ind Co Ltd Waste water treating reactor

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH09192696A (en) * 1996-01-25 1997-07-29 Meidensha Corp Monitor controller of anaerobic digestion tank
JPH11309438A (en) * 1998-05-01 1999-11-09 Ataka Constr & Eng Co Ltd Waste treating method
JP2000015231A (en) * 1998-07-06 2000-01-18 Kubota Corp Method for methane fermentation of organic waste
JP2000070908A (en) * 1998-08-31 2000-03-07 Kubota Corp Method for anaerobically digesting organic waste
JP2001162298A (en) * 1999-12-06 2001-06-19 Ishikawajima Harima Heavy Ind Co Ltd Waste water treating reactor

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007117948A (en) * 2005-10-31 2007-05-17 Ebara Corp Method and apparatus for treating high-concentration organic waste liquid
JP4642635B2 (en) * 2005-10-31 2011-03-02 荏原エンジニアリングサービス株式会社 High concentration organic waste liquid treatment method and apparatus
JP2007237055A (en) * 2006-03-07 2007-09-20 Toshiba Corp Organic waste water treatment method and arrangement
EP2151279A1 (en) 2008-08-04 2010-02-10 Zweckverband Abfallbehandlung Kahlenberg Method for operating a mechanical-biological waste treatment assembly with a process water circuit
JP2010069417A (en) * 2008-09-18 2010-04-02 Fuji Electric Holdings Co Ltd Methane fermentation apparatus

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