JP2002336825A - Method for recycling organic waste - Google Patents
Method for recycling organic wasteInfo
- Publication number
- JP2002336825A JP2002336825A JP2001147144A JP2001147144A JP2002336825A JP 2002336825 A JP2002336825 A JP 2002336825A JP 2001147144 A JP2001147144 A JP 2001147144A JP 2001147144 A JP2001147144 A JP 2001147144A JP 2002336825 A JP2002336825 A JP 2002336825A
- Authority
- JP
- Japan
- Prior art keywords
- solid
- garbage
- crushed
- separated
- solubilized
- 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
Links
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
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/10—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
- Y02A40/20—Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
-
- 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
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P60/00—Technologies relating to agriculture, livestock or agroalimentary industries
- Y02P60/80—Food processing, e.g. use of renewable energies or variable speed drives in handling, conveying or stacking
- Y02P60/87—Re-use of by-products of food processing for fodder production
-
- 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
- Y02W30/40—Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は有機性廃棄物のリサ
イクル方法に関し、汚泥再処理センター、食品廃棄物リ
サイクル施設等における生ごみ、高濃度有機性排水の処
理技術に係るものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for recycling organic waste, and more particularly to a technique for treating garbage and high-concentration organic wastewater in a sludge reprocessing center, a food waste recycling facility, and the like.
【0002】[0002]
【従来の技術】従来、生ごみをメタン発酵する際の前処
理装置としては、一軸もしくは二軸の粗破砕機と圧縮分
別機を組み合わせたシステムにおいて、夾雑物を含む生
ごみを一軸もしくは二軸の粗破砕機で粗破砕した後に粗
破砕物を圧縮分別機でペースト化するとともに粗破砕物
中の夾雑物を分別除去するものがある。2. Description of the Related Art Conventionally, as a pretreatment device for methane fermentation of garbage, a system combining a single-shaft or two-shaft coarse crusher and a compression separation machine is used to process garbage containing impurities in one or two shafts. There is a method in which a coarsely crushed material is coarsely crushed and then the coarsely crushed material is pasteurized by a compression fractionator and impurities in the coarsely crushed material are separated and removed.
【0003】また、一軸もしくは二軸の粗破砕機と可溶
化と固液分離を組み合わせたシステムにおいて、夾雑物
を含む生ごみを一軸もしくは二軸の粗破砕機で粗破砕し
た後に粗破砕物を可溶化し、可溶化処理物を固液分離す
るものがある。あるいは、トロンメル型の装置で夾雑物
を含む生ごみを粗破砕するとともに生ごみと夾雑物の分
別を行うものがある。Further, in a system combining a solubilization and a solid-liquid separation with a uniaxial or biaxial coarse crusher, garbage containing impurities is roughly crushed by a monoaxial or biaxial coarse crusher, and then the coarse crushed material is removed. In some cases, the solubilized material is solubilized and solid-liquid separated. Alternatively, there is a method in which garbage containing impurities is roughly crushed by a trommel-type apparatus and the garbage is separated from the impurities.
【0004】[0004]
【発明が解決しようとする課題】ところで、一軸もしく
は二軸の粗破砕機と圧縮分別機を組み合わせたシステム
では圧縮分別機においてペースト化しない夾雑物が全て
排出されるが、排出された夾雑物中には再資源化が困難
なビニル類と骨、野菜の繊維分などコンポスト化して資
源として利用可能なものとが混在する状態で夾雑物とし
て排出されてしまうので、利用可能な物の再利用が困難
である。By the way, in a system in which a single-shaft or twin-shaft coarse crusher and a compression separator are combined, all the non-paste impurities in the compression separator are discharged. In some cases, compostable materials such as vinyl and bone and vegetable fibers that are difficult to recycle are discharged as contaminants in a mixed state. Have difficulty.
【0005】一軸もしくは二軸の粗破砕機と可溶化を組
み合わせたシステムでは可溶化工程の可溶化処理物がビ
ニル類を含んでいるので、固液分離により可溶化処理物
から除去した夾雑物はビニル類を含みコンポスト化によ
る再利用は困難である。In a system in which a solubilization process is combined with a single-shaft or twin-shaft coarse crusher, since the solubilized product in the solubilization process contains vinyls, impurities removed from the solubilized product by solid-liquid separation are It contains vinyls and is difficult to reuse by composting.
【0006】トロンメル型の装置は分別能力が低く、分
別した夾雑物中にもメタン発酵の原料となる生ごみ中に
もビニル類が多く混入している。本発明は上記した課題
を解決するものであり、生ごみ、し尿、浄化槽汚泥等の
有機性廃棄物から利用可能物を効率良く回収することが
できる有機性廃棄物のリサイクル方法を提供することを
目的とする。[0006] The trommel-type apparatus has a low separation ability, and a large amount of vinyl is mixed in the separated contaminants and the garbage used as a raw material for methane fermentation. The present invention solves the above-mentioned problems, and provides an organic waste recycling method capable of efficiently collecting usable materials from organic waste such as garbage, human waste, and septic tank sludge. Aim.
【0007】[0007]
【課題を解決するための手段】上記課題を解決するため
に、請求項1に係る本発明の有機性廃棄物のリサイクル
方法は、生ごみを遠心型破砕分別機で粗破砕分別して生
ごみ破砕物と夾雑物とに分別し、生ごみ破砕物を可溶化
し、この可溶化処理物を固液分離装置で固液分離した液
状分をメタン発酵の原料とし、固形分を再資源化原料と
するものである。According to a first aspect of the present invention, there is provided a method of recycling organic waste, comprising the steps of crushing garbage by roughly crushing and separating garbage with a centrifugal crusher / separator. And the contaminants, solubilize the garbage crushed material, and subject the solubilized product to solid-liquid separation with a solid-liquid separator to use the liquid as a raw material for methane fermentation, and use the solid as a raw material for recycling. Is what you do.
【0008】上記した構成により、遠心型破砕分別機は
破砕物を遠心力によって分別するので利用困難なビニル
類等の夾雑物と利用可能な生ごみ破砕物とをほぼ完全に
分離することができ、可溶化工程にビニル類等の利用困
難な夾雑物が流入せず、可溶化槽の容量を減少させるこ
とができ、可溶化槽において攪拌を行うポンプがビニル
類で閉塞せず、攪拌機の負荷増加を防止でき、以後の工
程にもビニル類等が含まれなくなる。[0008] With the above-described configuration, the centrifugal crushing and sorting machine separates the crushed material by centrifugal force, so that it is possible to almost completely separate difficult-to-use impurities such as vinyls from the available garbage crushed material. In addition, difficult-to-use impurities such as vinyls do not flow into the solubilization process, so that the capacity of the solubilization tank can be reduced. An increase can be prevented, and vinyls and the like are not included in subsequent steps.
【0009】可溶化工程では生ごみの可溶化分が可溶化
して液状分となり、骨、繊維分などは可溶化しないで固
形分として残る。このため可溶化工程の可溶化処理物を
固液分離装置で固液分離することでメタン発酵に利用可
能な液状分とコンポスト化や飼料化等の再資源化原料と
して利用可能な固形分とに分離する。[0009] In the solubilization step, the solubilized portion of the garbage is solubilized into a liquid portion, and the bone and the fiber portion remain as a solid portion without being solubilized. Therefore, by solid-liquid separation of the solubilized product in the solubilization process with a solid-liquid separation device, the liquid content can be used for methane fermentation and the solid content can be used as a raw material for recycling such as composting and feed. To separate.
【0010】この固液分離によって骨、繊維分のみが特
異的に脱水ケーキとして得られるので、コンポスト化や
飼料化を行った場合に後段での分別工程がいらなくな
る。脱水ケーキにはカルシウム分、繊維分を多く含有す
るので、コンポスト、飼料が高品質な製品となる。コン
ポスト化、飼料化の工程で高温となるので雑菌は死滅し
衛生的である。[0010] Since only bones and fibers are specifically obtained as a dehydrated cake by the solid-liquid separation, a composting or feed conversion step is not required in the subsequent stage. Since the dehydrated cake contains a large amount of calcium and fiber, compost and feed are high quality products. Since the temperature rises during the composting and feed conversion processes, various bacteria are killed and sanitary.
【0011】請求項2に係る本発明の有機性廃棄物のリ
サイクル方法は、生ごみを遠心型破砕分別機で粗破砕分
別して生ごみ破砕物と夾雑物とに分別し、生ごみ破砕物
を可溶化し、この可溶化処理物を固液分離装置で固液分
離した液状分を排水処理系へ有機炭素源もしくは水素供
与体として供給するものである。According to a second aspect of the present invention, there is provided a method for recycling organic waste, wherein the raw garbage is roughly crushed and separated by a centrifugal crushing / separating machine to separate crushed garbage and contaminants. The solubilized product, which is obtained by solid-liquid separation of the solubilized product by a solid-liquid separator, is supplied to a wastewater treatment system as an organic carbon source or a hydrogen donor.
【0012】上記した構成により、高濃度有機性排水を
生物学的脱窒素処理する場合などにおいてBOD源が不
足する時に、従来のアルコール等の投入に代えて可溶化
物の液状分を投入することで排水処理費用を低減でき
る。According to the above-mentioned structure, when the BOD source becomes insufficient in a case where a high-concentration organic wastewater is subjected to a biological denitrification treatment, a liquid component of a solubilized substance is introduced instead of the conventional introduction of alcohol or the like. Thus, wastewater treatment costs can be reduced.
【0013】請求項3に係る本発明の有機性廃棄物のリ
サイクル方法は、高濃度有機性排水を細目スクリーンに
通してし渣を分離し、分離したし渣を生ごみと同様に遠
心型破砕分別機で粗破砕分別するものである。According to a third aspect of the present invention, there is provided a method for recycling organic waste, wherein high-concentration organic waste water is passed through a fine screen to separate the residue, and the separated residue is centrifugally crushed in the same manner as garbage. It is to be roughly crushed and separated by a separator.
【0014】上記した構成により、し尿、浄化槽汚泥等
の高濃度有機性排水に含まれたし渣中の繊維分などの有
機物も有効利用する。請求項4に係る本発明の有機性廃
棄物のリサイクル方法は、細目スクリーンの前段におい
て高濃度有機性排水に凝集剤を添加してし渣のBOD/
N比を調整する。With the above-mentioned structure, organic matter such as fibers in the residue contained in high-concentration organic wastewater such as night soil and septic tank sludge is effectively used. According to a fourth aspect of the present invention, there is provided the method for recycling organic waste, wherein a coagulant is added to the high-concentration organic wastewater before the fine screen to remove the BOD /
Adjust N ratio.
【0015】上記した構成により、し渣のBOD/N比
を調整することで、後工程で高濃度有機性排水を生物学
的脱窒素処理する際のBOD必要量を確保するととも
に、余剰なBODをし渣とともに回収して有効利用す
る。By adjusting the BOD / N ratio of the residue by the above-described configuration, the amount of BOD required for the biological denitrification treatment of the high-concentration organic wastewater in the subsequent step is ensured, and the excess BOD is obtained. And collect it together with the residue for effective use.
【0016】[0016]
【発明の実施の形態】以下、本発明の実施の形態を図面
に基づいて説明する。図1において、生ごみは遠心型破
砕分別機1において粗破砕分別して生ごみ破砕物とビニ
ル類を含む夾雑物とに分別する。この遠心型破砕分別機
1は破砕物を遠心力によって分別するので利用困難なビ
ニル類等の夾雑物と利用可能な生ごみ破砕物とをほぼ完
全に分離することができ、次工程の可溶化工程2にビニ
ル類等の利用困難な夾雑物が流入しない。Embodiments of the present invention will be described below with reference to the drawings. In FIG. 1, garbage is roughly crushed and separated in a centrifugal crushing and separating machine 1 to separate crushed garbage and contaminants containing vinyls. Since the centrifugal crushing and sorting machine 1 separates the crushed material by centrifugal force, it is possible to almost completely separate the difficult-to-use impurities such as vinyls and the available garbage crushed material, solubilizing the next step. Difficult-to-use impurities such as vinyls do not flow into step 2.
【0017】分別した生ごみ破砕物は可溶化工程2にお
いて可溶化する。この可溶化工程2ではビニル類等の夾
雑物が流入しないので、可溶化槽の容量を減少させるこ
とができ、可溶化槽において攪拌を行うポンプがビニル
類で閉塞せず、攪拌機の負荷増加を防止でき、以後の工
程にもビニル類等が含まれなくなる。可溶化工程2では
生ごみの可溶化分が可溶化して液状分となり、骨、繊維
分などは可溶化しないで固形分として残る。The separated crushed food waste is solubilized in the solubilization step 2. In the solubilization step 2, impurities such as vinyls do not flow, so that the capacity of the solubilization tank can be reduced, and the pump for stirring in the solubilization tank is not blocked by vinyls, thereby increasing the load on the stirrer. It is possible to prevent such a situation, and the subsequent steps do not include vinyls and the like. In the solubilization step 2, the solubilized portion of the garbage is solubilized into a liquid portion, and bone, fiber, and the like remain as a solid portion without being solubilized.
【0018】この可溶化処理物を固液分離装置3で固液
分離する。固液分離装置3としてはスクリュープレス、
スクリーン、またはその組み合わせによって行うが、フ
ィルタープレス、遠心分離、ベルトプレスなども利用可
能である。この固液分離により可溶化処理物を液状分と
固形分とに分離し、液状分を膜型メタン発酵槽4へメタ
ン発酵の原料として供給するか、後述する生物学的脱窒
素処理槽7へ有機炭素源もしくは水素供与体として供給
し、固形分(脱水ケーキ)をコンポスト化・飼料化工程
5へ再資源化原料として供給する。The solubilized product is subjected to solid-liquid separation by a solid-liquid separation device 3. Screw press as solid-liquid separation device 3,
It is performed by a screen or a combination thereof, but a filter press, a centrifuge, a belt press, and the like can also be used. The solubilized product is separated into a liquid component and a solid component by the solid-liquid separation, and the liquid component is supplied to the membrane-type methane fermentation tank 4 as a raw material for methane fermentation, or is supplied to a biological denitrification treatment tank 7 described later. It is supplied as an organic carbon source or a hydrogen donor, and the solid content (dehydrated cake) is supplied to the composting / feed conversion step 5 as a raw material for recycling.
【0019】この固液分離によって骨、繊維分のみが特
異的に脱水ケーキとして得られるので、コンポスト化・
飼料化工程5の後段での分別工程がいらなくなり、脱水
ケーキはカルシウム分、繊維分を多く含有するので、コ
ンポスト、飼料が高品質な製品となる。By this solid-liquid separation, only the bone and the fiber can be specifically obtained as a dehydrated cake.
Since the separation step at the latter stage of the feed conversion step 5 is not required, and the dewatered cake contains a large amount of calcium and fiber, compost and feed are high-quality products.
【0020】コンポスト化・飼料化工程5は発酵型、乾
燥型、フライヤー型の装置を使用し、その工程で高温
(50〜130℃)となるので雑菌は死滅し衛生的であ
る。膜型メタン発酵槽4は膜分離装置を有しており、膜
型メタン発酵槽4でメタン発酵により発生するバイオガ
スは燃料等として利用し、発酵汚泥は脱水機機6で脱水
して固形分をコンポスト化・飼料化工程5の再資源化原
料として利用し、脱水ろ液を後述する生物学的脱窒素処
理槽7へ有機炭素源もしくは水素供与体として供給す
る。The composting / feed conversion step 5 uses a fermentation type, a drying type, and a fryer type apparatus, and the temperature is high (50 to 130 ° C.) in the step, so that various bacteria are killed and sanitary. The membrane-type methane fermentation tank 4 has a membrane separation device. Biogas generated by methane fermentation in the membrane-type methane fermentation tank 4 is used as a fuel or the like. Is used as a raw material for recycling in the composting / feed conversion step 5, and the dehydrated filtrate is supplied to a biological denitrification treatment tank 7 described later as an organic carbon source or a hydrogen donor.
【0021】し尿・浄化槽汚泥等の高濃度有機性排水は
凝集剤を添加して後に細目スクリーン8でし渣を分離
し、その後に生物学的脱窒素処理槽7で生物学的処理す
る。分離したし渣は生ごみと同様に遠心型破砕分別機1
で粗破砕分別する。The high-concentration organic wastewater such as human waste and septic tank sludge is added with a coagulant and then separated by a fine screen 8 to separate the residue, and then subjected to a biological treatment in a biological denitrification treatment tank 7. Separated residue is centrifugal crushing and sorting machine 1 like garbage.
And coarsely crushed.
【0022】このことにより、し尿、浄化槽汚泥に含ま
れたし渣中の繊維分などの有機物もコンポスト化もしく
はメタン発酵の原料として有効利用する。高濃度有機性
排水に凝集剤を添加してし渣のBOD/N比を調整する
ことで、高濃度有機性排水を生物学的脱窒素処理する際
のBOD必要量を確保するとともに、余剰なBODをし
渣とともに回収してコンポスト化もしくはメタン発酵の
原料として有効利用する。生物学的脱窒素処理槽7で発
生する余剰汚泥は膜型メタン発酵槽4へ供給するか、脱
水機6へ直接に供給する。As a result, organic substances such as human waste and fibers contained in the sediment contained in the septic tank sludge are effectively used as composting or methane fermentation raw materials. By adding a coagulant to the high-concentration organic wastewater and adjusting the BOD / N ratio of the residue, the necessary amount of BOD for the biological denitrification treatment of the high-concentration organic wastewater is secured, and excess The BOD is collected together with the residue, and is effectively used as a raw material for composting or methane fermentation. Excess sludge generated in the biological denitrification treatment tank 7 is supplied to the membrane methane fermentation tank 4 or supplied directly to the dehydrator 6.
【0023】[0023]
【発明の効果】以上のように本発明によれば、生ごみを
遠心型破砕分別機で破砕分別することで利用困難なビニ
ル類等の夾雑物と利用可能な生ごみ破砕物とをほぼ完全
に分離することができるので、可溶化工程および以後の
工程にビニル類等の利用困難な夾雑物が流入せず、可溶
化槽の容量を減少させることができ、可溶化槽において
攪拌を行うポンプがビニル類で閉塞せず、攪拌機の負荷
増加を防止できる。可溶化処理物をメタン発酵もしくは
排水処理に利用可能な液状分とコンポスト化や飼料化等
の再資源化原料として利用可能な固形分とに固液分離す
ると、骨、繊維分のみが特異的に脱水ケーキとして得ら
れるので、コンポスト化や飼料化を行った場合に後段で
の分別工程がいらなくなり、カルシウム分、繊維分を多
く含有する高品質なコンポスト、飼料の製品を得ること
ができる。As described above, according to the present invention, garbage is hardly crushed and separated by the centrifugal crushing and separating machine, so that the difficult-to-use impurities such as vinyls and the crushed garbage can be almost completely separated. Pump that does not enter difficult-to-use impurities such as vinyls into the solubilization step and the subsequent steps, reduces the capacity of the solubilization tank, and performs stirring in the solubilization tank. Is not clogged with vinyls, thereby preventing an increase in load on the stirrer. Solid-liquid separation of the solubilized product into a liquid component that can be used for methane fermentation or wastewater treatment and a solid component that can be used as a raw material for recycling, such as composting and feed conversion, yields only bone and fiber components. Since it is obtained as a dehydrated cake, when composting or feed conversion is performed, a separation step in the subsequent stage is not required, and a high-quality compost or feed product containing a large amount of calcium and fiber can be obtained.
【0024】し尿、浄化槽汚泥等の高濃度有機性排水に
含まれたし渣中の繊維分などの有機物も有効利用するこ
とができ、凝集剤を添加してし渣のBOD/N比を調整
することで、後工程で高濃度有機性排水を生物学的脱窒
素処理する際のBOD必要量を確保するとともに、余剰
なBODをし渣とともに回収して有効利用することがで
きる。Organic matter such as fibers contained in high-concentration organic wastewater such as human waste and septic tank sludge can be effectively used, and the coagulant is added to adjust the BOD / N ratio of the residual. By doing so, it is possible to secure the required amount of BOD when biologically denitrifying high-concentration organic wastewater in a subsequent step, and to collect and effectively use excess BOD together with the residue.
【図1】本発明の実施の形態における有機性廃棄物のリ
サイクル方法を示す模式図である。FIG. 1 is a schematic diagram showing a method for recycling organic waste according to an embodiment of the present invention.
1 遠心型破砕分別機 2 可溶化工程 3 固液分離装置 4 膜型メタン発酵槽 5 コンポスト化・飼料化工程 6 脱水機 7 生物学的脱窒素処理槽 8 細目スクリーン DESCRIPTION OF SYMBOLS 1 Centrifugal crushing and sorting machine 2 Solubilization process 3 Solid-liquid separation device 4 Membrane methane fermentation tank 5 Composting and feed conversion process 6 Dehydrator 7 Biological denitrification treatment tank 8 Fine screen
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) B02C 23/16 C02F 11/14 A C02F 11/04 C05F 7/00 11/14 9/00 C05F 7/00 B09B 3/00 ZABC 9/00 D Z (72)発明者 師 正史 大阪府大阪市浪速区敷津東一丁目2番47号 株式会社クボタ内 (72)発明者 柴田 敏行 大阪府大阪市浪速区敷津東一丁目2番47号 株式会社クボタ内 Fターム(参考) 2B150 BA05 CD06 CD37 CD38 4D004 AA03 AC05 BA03 BA04 CA04 CA10 CA13 CA18 CB04 CB13 4D059 AA01 AA02 AA07 BA12 BA21 BE54 BF15 BK11 BK12 BK17 CC01 CC02 CC03 4D067 DD02 DD08 EE11 GA17 GA20 GB05 4H061 AA02 CC32 CC42 CC47 CC51 CC55 DD20 GG70 ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 7 Identification symbol FI Theme coat ゛ (Reference) B02C 23/16 C02F 11/14 A C02F 11/04 C05F 7/00 11/14 9/00 C05F 7/00 B09B 3/00 ZABC 9/00 DZ (72) Inventor Masafumi Shiki 2-47 47 Shizitsuhigashi, Naniwa-ku, Osaka-shi, Osaka Kubota Co., Ltd. (72) Toshiyuki Shibata Toshiyuki Shibata, Osaka-shi, Osaka 1-47 Tsuto F-term in Kubota Corporation (Reference) 2B150 BA05 CD06 CD37 CD38 4D004 AA03 AC05 BA03 BA04 CA04 CA10 CA13 CA18 CB04 CB13 4D059 AA01 AA02 AA07 BA12 BA21 BE54 BF15 BK11 BK12 BK17 CC01 CC02 CC03 DD08 EE11 GA17 GA20 GB05 4H061 AA02 CC32 CC42 CC47 CC51 CC55 DD20 GG70
Claims (4)
して生ごみ破砕物と夾雑物とに分別し、生ごみ破砕物を
可溶化し、この可溶化処理物を固液分離装置で固液分離
した液状分をメタン発酵の原料とし、固形分を再資源化
原料とすることを特徴とする有機性廃棄物のリサイクル
方法。Claims 1. A garbage is coarsely crushed and separated by a centrifugal crushing and separating machine to separate crushed garbage and contaminants, solubilize the crushed garbage, and subject the solubilized product to a solid-liquid separation device. A method for recycling organic waste, characterized in that a liquid component obtained by solid-liquid separation is used as a raw material for methane fermentation and a solid component is used as a raw material for recycling.
して生ごみ破砕物と夾雑物とに分別し、生ごみ破砕物を
可溶化し、この可溶化処理物を固液分離装置で固液分離
した液状分を排水処理系へ有機炭素源もしくは水素供与
体として供給することを特徴とする有機性廃棄物のリサ
イクル方法。2. The garbage is coarsely crushed and separated by a centrifugal crusher / separator to separate crushed garbage and contaminants. The crushed garbage is solubilized, and the solubilized product is separated by a solid-liquid separator. A method for recycling organic waste, comprising supplying a liquid fraction separated into solid and liquid to a wastewater treatment system as an organic carbon source or a hydrogen donor.
してし渣を分離し、分離したし渣を遠心型破砕分別機で
粗破砕分別することを特徴とする請求項1又は2に記載
の有機性廃棄物のリサイクル方法。3. The method according to claim 1, wherein the high-concentration organic wastewater is passed through a fine screen to separate the residue, and the separated residue is roughly crushed and separated by a centrifugal crushing and separating machine. How to recycle organic waste.
機性排水に凝集剤を添加してし渣のBOD/N比を調整
することを特徴とする請求項3に記載の有機性廃棄物の
リサイクル方法。4. The method for recycling organic waste according to claim 3, wherein a coagulant is added to the high-concentration organic wastewater before the fine screen to adjust the BOD / N ratio of the residue. .
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JP2006281095A (en) * | 2005-03-31 | 2006-10-19 | Kubota Corp | Method for treating organic waste |
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