JP2005144262A - Methane fermentation method of solid organic waste containing foreign matter - Google Patents
Methane fermentation method of solid organic waste containing foreign matter Download PDFInfo
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- JP2005144262A JP2005144262A JP2003382567A JP2003382567A JP2005144262A JP 2005144262 A JP2005144262 A JP 2005144262A JP 2003382567 A JP2003382567 A JP 2003382567A JP 2003382567 A JP2003382567 A JP 2003382567A JP 2005144262 A JP2005144262 A JP 2005144262A
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- 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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
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- 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
- Y02W30/00—Technologies for solid waste management
- Y02W30/20—Waste processing or separation
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Abstract
Description
本発明は、夾雑物を含む固形有機性廃棄物をメタン発酵槽でメタン発酵処理しメタンガスを回収する方法に関する。 The present invention relates to a method for recovering methane gas by subjecting solid organic waste containing impurities to methane fermentation treatment in a methane fermentation tank.
従来、固形有機性廃棄物を有効利用する方法として、収集された可燃ごみを破砕装置により破砕し、この破砕した可燃ごみを分離選別装置により生ごみ(固形有機性廃棄物)とそれ以外の夾雑物とに分離選別し、この分離選別した生ごみをメタン発酵槽でメタン発酵処理しメタンガスを回収する方法が知られている(例えば、特許文献1参照)。
しかしながら、上記分離選別された生ごみには、実際には、夾雑物であるプラスチック片等の異物やコルク栓、割り箸、剪定枝等の低分解率の固形有機物が所定の割合で残る。このため、メタン発酵槽にあっては、撹拌強度を上げても、上記プラスチック片等の異物が消化汚泥に対して分離し、又、コルク栓、割り箸、剪定枝等の低分解率の固形有機物が未分解の状態で消化汚泥に対して分離し、これらの夾雑物がスカムとして液表面に堆積したり、槽内壁に堆積する結果、有効発酵槽容積が減少すると共に槽内の撹拌が不十分となり、所望にメタンガスを回収できないという問題がある。 However, in the separated and sorted garbage, in reality, foreign matters such as plastic pieces, which are contaminants, and solid organic substances having a low decomposition rate such as cork stoppers, chopsticks, and pruning branches remain at a predetermined ratio. For this reason, in the methane fermentation tank, even if the stirring strength is increased, foreign matters such as the above plastic pieces are separated from the digested sludge, and solid organic substances having a low decomposition rate such as corks, chopsticks and pruned branches Is separated from digested sludge in an undegraded state, and these contaminants accumulate on the liquid surface as scum or accumulate on the inner wall of the tank, resulting in a decrease in effective fermenter volume and insufficient agitation in the tank. Thus, there is a problem that methane gas cannot be recovered as desired.
ここで、このような問題を解消すべく、分離選別装置による生ごみと夾雑物との分離選別にあって、分離選別を徹底することが考えられるが、イニシャルコストやランニングコストが高くなる。また、このようなイニシャルコスト増やランニングコスト増を無くすには、夾雑物の混入率の低い生ごみを対象とする必要があり、対象が限定されてしまう。 Here, in order to solve such a problem, it is conceivable to thoroughly separate and sort garbage and garbage by the separation and sorting device, but the initial cost and running cost become high. Further, in order to eliminate such an increase in initial cost and running cost, it is necessary to target garbage with a low contamination rate, and the target is limited.
本発明は、このような課題を解決するために成されたものであり、イニシャルコストやランニングコスト等のコスト増の抑止及び対象範囲の拡大を図りつつ、所望にメタンガスを回収する方法を提供することを目的とする。 The present invention has been made to solve such a problem, and provides a method for recovering methane gas as desired while suppressing increase in costs such as initial cost and running cost and expanding the target range. For the purpose.
本発明による夾雑物を含む固形有機性廃棄物のメタン発酵方法は、夾雑物を含む固形有機性廃棄物をメタン発酵槽でメタン発酵処理しメタンガスを回収する方法において、メタン発酵槽のTS(Total Solid:全固形分)濃度を、夾雑物が消化汚泥に対して分離堆積しない所定のTS濃度に設定したことを特徴としている。 The method of methane fermentation of solid organic waste containing impurities according to the present invention is a method of performing methane fermentation treatment of solid organic waste containing impurities in a methane fermenter and recovering methane gas. Solid: the total solid content) concentration is set to a predetermined TS concentration at which impurities do not separate and accumulate on the digested sludge.
このような夾雑物を含む固形有機性廃棄物のメタン発酵方法によれば、メタン発酵槽のTS濃度が所定のTS濃度に設定され、これにより、消化汚泥に対して夾雑物が分離し堆積するということが無くされる。従って、前段での固形有機性廃棄物と夾雑物との分離選別の精度を高めること無く且つ夾雑物の低混入率の固形有機性廃棄物を選択すること無く、所定の有効発酵槽容積が確保されると共に槽内が十分に撹拌されてメタン発酵が行われる。 According to the method for methane fermentation of solid organic waste containing such impurities, the TS concentration of the methane fermenter is set to a predetermined TS concentration, whereby impurities are separated and deposited from the digested sludge. That is lost. Therefore, a certain effective fermenter volume can be secured without increasing the accuracy of separation and sorting of solid organic waste and contaminants in the previous stage and without selecting solid organic waste with a low contamination rate. At the same time, the inside of the tank is sufficiently stirred to perform methane fermentation.
ここで、メタン発酵槽のTS濃度を所定のTS濃度とする具体的な方法としては、メタン発酵槽の前段に、夾雑物を含む固形有機性廃棄物を水分と混合し混合物をメタン発酵槽に供給する混合槽を備え、メタン発酵槽のTS濃度が所定のTS濃度となるように、混合槽に対する水分供給量を設定する方法が挙げられる。 Here, as a specific method of setting the TS concentration of the methane fermenter to a predetermined TS concentration, solid organic waste containing impurities is mixed with moisture in the previous stage of the methane fermenter, and the mixture is put into the methane fermenter. There is a method of providing a mixing tank to be supplied and setting the amount of water supply to the mixing tank so that the TS concentration of the methane fermentation tank becomes a predetermined TS concentration.
また、メタン発酵槽のTS濃度を所定のTS濃度とする具体的な他の方法としては、メタン発酵槽の前段に、夾雑物を含む固形有機性廃棄物を水分と混合し混合物をメタン発酵槽に供給する混合槽を備え、この混合槽にメタン発酵槽の消化汚泥を戻す方法が挙げられる。 In addition, as another specific method for setting the TS concentration of the methane fermentation tank to a predetermined TS concentration, solid organic waste containing impurities is mixed with moisture in the previous stage of the methane fermentation tank, and the mixture is mixed with the methane fermentation tank. And a method of returning the digested sludge of the methane fermentation tank to the mixing tank.
ここで、本発明者らの実験によると、所定のTS濃度を7〜20%とすると、夾雑物の消化汚泥に対する分離が効果的に防止される。 Here, according to experiments by the present inventors, when the predetermined TS concentration is 7 to 20%, separation of contaminants from digested sludge is effectively prevented.
このように本発明による夾雑物を含む固形有機性廃棄物のメタン発酵方法によれば、固形有機性廃棄物と夾雑物との分離選別の精度を高めること無く且つ夾雑物の低混入率の固形有機性廃棄物を選択すること無く、所定の有効発酵槽容積が確保されると共に槽内が十分に撹拌されてメタン発酵が行われるため、イニシャルコストやランニングコスト等のコスト増の抑止及び対象範囲の拡大を図りつつ、所望にメタンガスを回収することが可能となる。 As described above, according to the method for methane fermentation of solid organic waste containing contaminants according to the present invention, the solid organic waste and contaminants can be solidified without increasing the accuracy of separation and sorting of the solid organic waste and contaminants. Without selecting organic waste, a certain effective fermenter volume is secured and the inside of the tank is sufficiently stirred to perform methane fermentation, so that the initial cost and running cost are prevented from increasing and the target range It is possible to recover methane gas as desired while expanding the range.
以下、本発明による夾雑物を含む固形有機性廃棄物のメタン発酵方法の好適な実施形態について図1を参照しながら説明する。図1は、本発明の実施形態に係る、夾雑物を含む固形有機性廃棄物のメタン発酵方法を採用したメタン発酵処理システムを示すブロック構成図である。 Hereinafter, a preferred embodiment of a method for methane fermentation of solid organic waste containing impurities according to the present invention will be described with reference to FIG. FIG. 1 is a block configuration diagram showing a methane fermentation treatment system adopting a methane fermentation method for solid organic waste containing impurities according to an embodiment of the present invention.
この実施形態のシステムは、ごみ収集車より搬入された可燃ごみから固形有機性廃棄物である生ごみを分離選別し、この生ごみをメタン発酵処理してメタンガスを回収するものであり、前処理装置1と、メタン発酵槽2と、を備えている。 The system of this embodiment separates and sorts garbage, which is solid organic waste, from combustible waste carried from a garbage truck, and collects methane gas by subjecting this raw garbage to methane fermentation treatment, and pretreatment. The apparatus 1 and the methane fermentation tank 2 are provided.
前処理装置1は、袋詰めされて搬入された可燃ごみを破袋装置1aで破袋し、この破袋物を破砕装置1bで所定の大きさ以下に破砕し、この破砕物を分離選別装置としての例えばトロンメル等の篩及び風力選別装置1cで生ごみとそれ以外の夾雑物とに分離選別し、この分離選別装置1cで分離選別した生ごみを混合槽1dに導入し、当該混合槽1dで、供給水ラインLを通して供給される水と蒸気と撹拌混合し、生ごみを酸発酵させると共に所定に調質し且つ重量異物を沈殿除去し、この重量異物を除去した混合物をメタン発酵槽2に供給する。
The pretreatment device 1 breaks the combustible waste that has been packed into the bag with the bag breaking
メタン発酵槽2は、混合槽1dからの混合物を、例えば、機械的撹拌、又は、槽中心にドラフト管を設置し当該ドラフト管にガスを供給してのガス撹拌、又は、液を循環させる液撹拌等により所定期間所定の撹拌力で撹拌し、メタン発酵させる。 The methane fermentation tank 2 is a liquid which circulates the mixture from the mixing tank 1d, for example, mechanical stirring, or gas stirring by installing a draft pipe in the center of the tank and supplying gas to the draft pipe. The mixture is stirred with a predetermined stirring force for a predetermined period by stirring or the like, and is subjected to methane fermentation.
そして、このメタン発酵槽2の消化汚泥は当該メタン発酵槽2の底部から引き抜かれて所定の汚泥処理又は所定の汚泥利用設備に供され、一方、メタン発酵槽2の上部から排出されるバイオガス(メタンガス及び二酸化炭素の混合ガス)は後段でメタンガスが分離精製され例えば天然ガス自動車の燃料等として利用される。 And the digested sludge of this methane fermentation tank 2 is extracted from the bottom part of the said methane fermentation tank 2, and is used for a predetermined sludge process or a predetermined sludge utilization equipment, On the other hand, the biogas discharged | emitted from the upper part of the methane fermentation tank 2 The (methane gas and carbon dioxide mixed gas) is separated and purified at a later stage and used as, for example, a fuel for a natural gas vehicle.
ところで、分離選別装置1cで分離選別された生ごみには、実際には、夾雑物であるプラスチック片等の異物やコルク栓、割り箸、剪定枝等の低分解率の固形有機物が所定の割合で残っている。従って、メタン発酵槽2には、夾雑物である異物や低分解率の固形有機物を含む生ごみが導入される。
By the way, the garbage separated and sorted by the separation and sorting
そこで、本実施形態にあっては、メタン発酵槽2のTS(Total Solid:全固形分)濃度が、メタン発酵槽2に導入される夾雑物が消化汚泥に対して分離堆積しない所定のTS濃度に設定されている。この所定のTS濃度は、本実施形態では、7〜20%に設定されている。具体的には、混合槽1dへの供給水ラインLの供給水量を調整することで、メタン発酵槽2のTS濃度が上記所定のTS濃度とされている。なお、メタン発酵槽2のTS濃度を所定のTS濃度とする他の方法としては種々考えられるが、例えば、メタン発酵槽2の消化汚泥を混合槽1dに戻す方法が挙げられる。 Therefore, in the present embodiment, the TS (Total Solid) concentration of the methane fermentation tank 2 is a predetermined TS concentration at which impurities introduced into the methane fermentation tank 2 are not separated and deposited on the digested sludge. Is set to This predetermined TS concentration is set to 7 to 20% in this embodiment. Specifically, the TS concentration of the methane fermentation tank 2 is set to the predetermined TS concentration by adjusting the amount of water supplied from the supply water line L to the mixing tank 1d. Various other methods for setting the TS concentration of the methane fermentation tank 2 to a predetermined TS concentration are conceivable. For example, there is a method of returning the digested sludge of the methane fermentation tank 2 to the mixing tank 1d.
このような本実施形態にあっては、メタン発酵槽2のTS濃度が上記所定のTS濃度に設定されているため、メタン発酵槽2にあっては、消化汚泥に対して夾雑物(プラスチック片等の異物や、コルク栓、割り箸、剪定枝等の低分解率の固形有機物)が分離し堆積するということが無くされている。これは、メタン発酵槽2のTS濃度を上記所定のTS濃度とすることで、汚泥の粘性が上がり固形分が巻き込まれ分離し難くなるからだと考えられる。 In this embodiment, since the TS concentration of the methane fermenter 2 is set to the predetermined TS concentration, in the methane fermenter 2, impurities (plastic pieces) Such as foreign substances such as cork stoppers, disposable chopsticks, pruned branches, etc.) are separated and deposited. This is thought to be because, by setting the TS concentration of the methane fermentation tank 2 to the above-mentioned predetermined TS concentration, the viscosity of the sludge increases and the solid content is entrained, making it difficult to separate.
従って、前段での生ごみと夾雑物との分離選別の精度を高めること無く(分離選別装置1cをさらに高選別能力の装置とすること無く)且つ夾雑物の低混入率の生ごみを選択すること無く(上記異物や低分解率の固形有機物の生ごみに対する混入を許容しつつ)、所定の有効発酵槽容積が確保されていると共に槽内が十分に撹拌されてメタン発酵が行われる。その結果、イニシャルコストやランニングコスト等のコスト増の抑止及び対象範囲の拡大を図りつつ、所望にメタンガスを回収することが可能とされている。
Therefore, it is possible to select the garbage with a low contamination rate without increasing the accuracy of separating and sorting the garbage and foreign substances in the previous stage (without making the separation and sorting
なお、本発明者らの実験によると、所定のTS濃度を前述した7〜20%とすることで、夾雑物の消化汚泥に対する分離を効果的に防止し得ることが確認された。因みに、従来のメタン発酵槽のTS濃度は一般的に3〜5%程度であり、このような低いTS濃度では、プラスチック片等の異物が消化汚泥に対して分離し、又、コルク栓、割り箸、剪定枝等の低分解率の固形有機物が未分解の状態で消化汚泥に対して分離してしまい、これらの夾雑物がスカムとして液表面に堆積したり、槽の内周壁に沿って環状に堆積することになる。 According to the experiments by the present inventors, it was confirmed that separation of impurities from digested sludge can be effectively prevented by setting the predetermined TS concentration to 7 to 20% as described above. Incidentally, the TS concentration of the conventional methane fermenter is generally about 3 to 5%, and at such a low TS concentration, foreign matters such as plastic pieces are separated from the digested sludge. The solid organic matter with a low decomposition rate such as pruned branches is separated from the digested sludge in an undecomposed state, and these contaminants accumulate on the liquid surface as scum or ring along the inner peripheral wall of the tank. Will be deposited.
以上、本発明をその実施形態に基づき具体的に説明したが、本発明は上記実施形態に限定されるものではなく、例えば、上記実施形態においては、生ごみを酸発酵させると共に所定に調質し且つ重量異物を沈殿除去すべく、夾雑物を含む生ごみを、混合槽1dに導入するようにしているが、混合槽1dを通すこと無く直接メタン発酵槽2に供給することも可能である。この場合には、メタン発酵槽2のTS濃度が上記所定のTS濃度となるように、例えばメタン発酵槽2に水を供給し供給水量を調整すれば良い。 As described above, the present invention has been specifically described based on the embodiment. However, the present invention is not limited to the above embodiment. For example, in the above embodiment, the food waste is acid-fermented and conditioned in a predetermined manner. In addition, in order to precipitate and remove heavy foreign substances, garbage containing foreign substances is introduced into the mixing tank 1d. However, it is also possible to directly supply the methane fermentation tank 2 without passing through the mixing tank 1d. . In this case, for example, water may be supplied to the methane fermentation tank 2 to adjust the amount of supplied water so that the TS concentration of the methane fermentation tank 2 becomes the predetermined TS concentration.
また、上記実施形態においては、特に効果的であるとして、固形有機性廃棄物を生ごみとしているが、例えば下水汚泥等の固形有機性廃棄物に対しても適用可能である。 Moreover, in the said embodiment, although it is effective, solid organic waste is made into garbage, However For example, it is applicable also to solid organic waste, such as a sewage sludge.
2…メタン発酵槽、L…供給水ライン。 2 ... Methane fermenter, L ... Supply water line.
Claims (4)
前記メタン発酵槽のTS濃度を、前記夾雑物が消化汚泥に対して分離堆積しない所定のTS濃度に設定したことを特徴とする夾雑物を含む固形有機性廃棄物のメタン発酵方法。 In a method of recovering methane gas by subjecting solid organic waste containing impurities to methane fermentation treatment in a methane fermentation tank,
A method for methane fermentation of solid organic waste containing contaminants, wherein the TS concentration of the methane fermentation tank is set to a predetermined TS concentration at which the contaminants are not separated and deposited with respect to digested sludge.
前記メタン発酵槽のTS濃度が前記所定のTS濃度となるように、前記混合槽に対する水分供給量を設定したことを特徴とする請求項1記載の夾雑物を含む固形有機性廃棄物のメタン発酵方法。 In the front stage of the methane fermentation tank, a mixing tank is provided that mixes solid organic waste containing the impurities with moisture and supplies the mixture to the methane fermentation tank.
The methane fermentation of solid organic waste containing impurities according to claim 1, wherein the amount of water supply to the mixing tank is set so that the TS concentration of the methane fermentation tank becomes the predetermined TS concentration. Method.
この混合槽に前記メタン発酵槽の消化汚泥を戻すことを特徴とする請求項1記載の夾雑物を含む固形有機性廃棄物のメタン発酵方法。 In the front stage of the methane fermentation tank, a mixing tank is provided that mixes solid organic waste containing the impurities with moisture and supplies the mixture to the methane fermentation tank.
The method for methane fermentation of solid organic waste containing impurities according to claim 1, wherein the digested sludge of the methane fermentation tank is returned to the mixing tank.
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007167782A (en) * | 2005-12-22 | 2007-07-05 | Nippon Steel Engineering Co Ltd | Waste treatment method |
JP2007216168A (en) * | 2006-02-17 | 2007-08-30 | Kurita Water Ind Ltd | Method and apparatus for treating organic waste |
WO2010002102A2 (en) * | 2008-07-02 | 2010-01-07 | Kim Tong-Ki | Method using food waste and human excrement |
JP2019177334A (en) * | 2018-03-30 | 2019-10-17 | Jfeエンジニアリング株式会社 | Pretreatment apparatus for dry methane fermentation treatment of waste |
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2003
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Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007167782A (en) * | 2005-12-22 | 2007-07-05 | Nippon Steel Engineering Co Ltd | Waste treatment method |
JP2007216168A (en) * | 2006-02-17 | 2007-08-30 | Kurita Water Ind Ltd | Method and apparatus for treating organic waste |
WO2010002102A2 (en) * | 2008-07-02 | 2010-01-07 | Kim Tong-Ki | Method using food waste and human excrement |
WO2010002102A3 (en) * | 2008-07-02 | 2010-03-11 | Kim Tong-Ki | Method using food waste and human excrement |
CN102015134A (en) * | 2008-07-02 | 2011-04-13 | 金栋基 | Method using food waste and human excrement |
JP2019177334A (en) * | 2018-03-30 | 2019-10-17 | Jfeエンジニアリング株式会社 | Pretreatment apparatus for dry methane fermentation treatment of waste |
JP7032696B2 (en) | 2018-03-30 | 2022-03-09 | Jfeエンジニアリング株式会社 | Pretreatment equipment for dry methane fermentation treatment of waste |
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