JP2008246462A - Pretreatment apparatus for methane fermentation and methane fermentation treatment system using it - Google Patents

Pretreatment apparatus for methane fermentation and methane fermentation treatment system using it Download PDF

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JP2008246462A
JP2008246462A JP2007094959A JP2007094959A JP2008246462A JP 2008246462 A JP2008246462 A JP 2008246462A JP 2007094959 A JP2007094959 A JP 2007094959A JP 2007094959 A JP2007094959 A JP 2007094959A JP 2008246462 A JP2008246462 A JP 2008246462A
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methane fermentation
tank
drum screen
waste
solubilized
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JP4712752B2 (en
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Nobuyuki Ukai
展行 鵜飼
Takehiro Kato
雄大 加藤
Masayoshi Kaga
正悦 加賀
Hiroshi Mizutani
洋 水谷
Masamichi Asano
昌道 浅野
Masayuki Tabata
雅之 田畑
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Mitsubishi Heavy Industries Environmental Engineering Co Ltd
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    • 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
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a pretreatment apparatus for methane fermentation which improves efficiency of methane fermentation treatment, and a methane fermentation treatment system using it. <P>SOLUTION: The pretreatment apparatus for methane fermentation comprises first and second crusher 12-1, 12-2 for coarsely crushing garbage waste 11, a sorter 14 for sorting foreign materials 13, a solubilization tank 15 for solubilizing the garbage waste 11, a drum screen 16 for drawing solubilized liquid 18A from the vicinity of the tank bottom and removing the remaining foreign materials 13, a return line L3 for returning solubilized liquid 18B, from which the foreign materials 13 have been removed, to the solubilization tank, and a supply line L<SB>4</SB>for supplying solubilized liquid 19 for methane fermentation to a methane fermentation tank 20. The solubilization tank is divided into a front chamber and a rear chamber by a partition wall 15a. The solubilized liquid overflows the partition wall 15a, the solubilized liquid 18A is drawn from the bottom of the rear chamber to be supplied to the drum screen 16 side, and the solubilized liquid 18B of the return line L<SB>3</SB>is returned in a shower form from the upper part of the rear chamber through a shower nozzle 15b. <P>COPYRIGHT: (C)2009,JPO&INPIT

Description

本発明は、例えば生ごみ等の食品廃棄物をメタン発酵処理設備でリサイクルする際のメタン発酵前処理装置及びこれを用いたメタン発酵処理システムに関する。   The present invention relates to a methane fermentation pretreatment apparatus and a methane fermentation treatment system using the same, for example, when food waste such as garbage is recycled in a methane fermentation treatment facility.

従来、生ごみ、水産加工廃棄物、し尿、下水汚泥、浄化槽汚泥等の有機性廃棄物(以下、「廃棄物」という。)をメタン発酵処理する際においては、そのメタン発酵効率を向上させるために、所定の水分とする可溶化技術が各種提案されている(例えば特許文献1参照)。その一例として提案されるメタン発酵前処理装置を図2に示す。   Conventionally, when organic waste such as food waste, fishery processing waste, human waste, sewage sludge, septic tank sludge, etc. (hereinafter referred to as “waste”) is subjected to methane fermentation, in order to improve its methane fermentation efficiency In addition, various solubilization techniques using predetermined moisture have been proposed (see, for example, Patent Document 1). The methane fermentation pretreatment apparatus proposed as the example is shown in FIG.

図2に示すように、従来のメタン発酵前処理装置100は、有機性廃棄物である生ごみを破砕して生ごみ破砕物101とした後、貯蓄槽102に送られ、ここで、攪拌混合され、次いで、この貯蓄槽102の攪拌手段103で混合攪拌された一部を循環手段107にて前記貯蓄槽に循環させるとともに、残りの一部をメタン発酵槽でメタン発酵処理するものであり、そのメタン発酵の前処理の際に、前記循環手段107にて前記生ごみ101を循環させて、この生ごみの含水率が85%〜90%程度となるように水を添加して可溶化させるとともに、この生ごみから夾雑物除去手段105により前記夾雑物を除去した後に、水供給手段108から水108aが添加されて夾雑物が除去された前記有機性廃棄物を前記貯留槽102で再び攪拌混合して調質し、調質物104を得ている。符号106は洗浄水である。   As shown in FIG. 2, the conventional methane fermentation pretreatment apparatus 100 crushes raw garbage, which is an organic waste, into a crushed garbage 101, which is then sent to a storage tank 102 where stirring and mixing are performed. Then, a part mixed and stirred by the stirring means 103 of the storage tank 102 is circulated to the storage tank by the circulation means 107, and the remaining part is subjected to methane fermentation treatment in the methane fermentation tank. In the pretreatment of the methane fermentation, the garbage 101 is circulated by the circulation means 107, and water is added and solubilized so that the moisture content of the garbage becomes about 85% to 90%. At the same time, after removing the contaminants from the garbage by the contaminant removal means 105, the organic waste from which the contaminants have been removed by adding water 108a from the water supply means 108 is stirred again in the storage tank 102. Mixed Reforming to tone, to obtain a tone pledge 104. Reference numeral 106 denotes washing water.

また、循環の際には、攪拌混合されている有機性廃棄物を貯留槽102の下部から引き抜いて新たな有機性廃棄物が投入される前記貯留槽の上部に返送するようにしている。   In circulation, the organic waste that has been stirred and mixed is withdrawn from the lower part of the storage tank 102 and returned to the upper part of the storage tank into which new organic waste is introduced.

特許第3710938号公報Japanese Patent No. 3710938

しかしながら、特許文献1に係る装置では、以下のような問題がある。
1)生ごみ破砕物101から夾雑物を夾雑物除去手段105で除去する際には、固形状の生ごみが夾雑物と同時に除去され、夾雑物発生量の増加となると共に、本来処理する生ごみが除去される結果、メタン発酵槽でのメタンガス発生量の低下が生ずる、という問題がある。
However, the apparatus according to Patent Document 1 has the following problems.
1) When removing the contaminants from the crushed garbage 101 by the contaminant removal means 105, the solid garbage is removed at the same time as the contaminants, increasing the amount of contaminants generated and the raw food to be originally processed. As a result of the removal of garbage, there is a problem that the amount of methane gas generated in the methane fermentation tank is reduced.

2)また、夾雑物除去手段105における沈殿分離により夾雑物を除去する方法では、沈殿しない夾雑物、例えば軽質な夾雑物(ビニール、繊維等)を除去することが全くできない、という問題がある。
特に、破砕された生ごみから夾雑物を除去する選別手段においても、前記ビニールや繊維状物等は、選別手段によっても完全には選別されずに、生ごみ中に残留するので、これらを積極的に除去することも切望されている。
2) Further, the method of removing contaminants by precipitation separation in the contaminant removing means 105 has a problem that impurities that do not precipitate, such as light impurities (vinyl, fibers, etc.) cannot be removed at all.
In particular, even in the sorting means for removing impurities from the crushed garbage, the vinyl and fibrous materials remain in the garbage without being completely sorted by the sorting means. It is also eager to remove it.

3)また、夾雑物除去手段105の槽下部から沈殿物引抜く場合、重質な夾雑物(沈砂等
)の除去は、可能であるものの、軽質な夾雑物(例えばビニール、繊維等)は液面にスカムとして浮上するため、その除去が困難である、という問題がある。
3) Also, when the sediment is pulled out from the bottom of the tank of the contaminant removal means 105, heavy contaminants (such as sand) can be removed, but light contaminants (such as vinyl and fiber) are liquids. Since it floats as a scum on the surface, there is a problem that its removal is difficult.

本発明は、前記問題に鑑み、メタン発酵処理の効率を低減することなくしかも夾雑物を除去ことができると共に、その夾雑物に依存する処理設備の悪影響を未然防止できるメタン発酵前処理装置及びこれを用いたメタン発酵処理システムを提供することを課題とする。   In view of the above problems, the present invention is capable of removing impurities without reducing the efficiency of the methane fermentation treatment, and can prevent the adverse effects of the treatment equipment depending on the impurities, and the methane fermentation pretreatment device. It is an object to provide a methane fermentation treatment system using the above.

上述した課題を解決するための本発明の第1の発明は、食品生ごみ廃棄物を粗破砕処理する第1の破砕機と、粗破砕処理後に微破砕する第2の破砕機と、破砕された廃棄物に混入している夾雑物を選別する選別機と、前記夾雑物が除去された食品生ごみ廃棄物を可溶化する可溶化槽と、前記可溶化槽の底部近傍から可溶化液を抜出し、該抜出した可溶化液中に残留する夾雑物を除去するドラムスクリーンと、前記ドラムスクリーンにより夾雑物が除去された可溶化液を再度可溶化槽に戻す戻しラインと、前記可溶化槽からメタン発酵槽にメタン発酵用可溶化液を供給する供給ラインを具備し、且つ前記可溶化槽が前室と後室とに隔壁により二分割されてなり、該隔壁を可溶化液が越流すると共に、前記前室の底部から可溶化液を抜出してドラムスクリーン側に供給すると共に、前記ドラムスクリーンからの戻しラインの可溶化液を前室の上部からシャワーノズルによりシャワー状で戻してなることを特徴とするメタン発酵前処理装置にある。   1st invention of this invention for solving the subject mentioned above is crushed with the 1st crusher which carries out rough crushing processing of the food waste waste, the 2nd crusher which carries out fine crushing after rough crushing processing, and A sorter that sorts out contaminants mixed in the waste, a solubilization tank that solubilizes food waste waste from which the contaminants have been removed, and a solubilizing solution from the bottom of the solubilization tank. A drum screen that removes the contaminants remaining in the extracted solubilized liquid, a return line that returns the solubilized liquid from which the contaminants have been removed by the drum screen to the solubilization tank, and the solubilization tank. A supply line for supplying a methane fermentation solubilizing solution to the methane fermentation tank is provided, and the solubilization tank is divided into a front chamber and a rear chamber by a partition wall, and the solubilizing solution overflows the partition wall. At the same time, the solubilized liquid is extracted from the bottom of the front chamber. Supplies to the screen side, in the methane fermentation pretreatment apparatus characterized by comprising back in a shower-like by the shower nozzle from the top of the front chamber lysate of return line from the drum screen.

第2の発明は、第1の発明において、前記ドラムスクリーンのスクリーン目幅が5mm〜10mmであることを特徴とするメタン発酵前処理装置にある。   A second invention is the pretreatment apparatus for methane fermentation according to the first invention, wherein the screen width of the drum screen is 5 mm to 10 mm.

第3の発明は、第1又は2の発明において、除去される夾雑物がビニール系の回収夾雑物であることを特徴とするメタン発酵前処理装置にある。   According to a third aspect of the present invention, there is provided the pretreatment apparatus for methane fermentation according to the first or second aspect, wherein the foreign matter to be removed is a vinyl-based recovered foreign matter.

第4の発明は、第1乃至3のいずれか一つのメタン発酵前処理装置と、前記メタン発酵前処理装置で前処理されたメタン発酵用可溶化液をメタン発酵処理するメタン発酵槽とを具備することを特徴とするメタン発酵処理システムにある。   4th invention comprises the methane fermentation pretreatment apparatus of any one of 1st thru | or 3, and the methane fermentation tank which performs the methane fermentation process of the solubilization liquid for methane fermentation pre-processed by the said methane fermentation pre-treatment apparatus. It is in the methane fermentation processing system characterized by doing.

本発明によれば、食品生ごみ廃棄物をメタン発酵で処理する際の処理効率を低減することなく、夾雑物を除去し、夾雑物に依存する悪影響を未然防止でき、食品生ごみリサイクルシステムに適用して良好なものとなる。   According to the present invention, without reducing the processing efficiency when processing food wastes by methane fermentation, it is possible to remove foreign substances and prevent adverse effects depending on the foreign substances, and to the food garbage recycling system. Apply to be good.

以下、この発明につき図面を参照しつつ詳細に説明する。なお、この実施例によりこの発明が限定されるものではない。また、下記実施例における構成要素には、当業者が容易に想定できるもの、あるいは実質的に同一のものが含まれる。   Hereinafter, the present invention will be described in detail with reference to the drawings. Note that the present invention is not limited to the embodiments. In addition, constituent elements in the following embodiments include those that can be easily assumed by those skilled in the art or those that are substantially the same.

本発明による実施例に係るメタン発酵前処理装置、メタン発酵処理システムについて、図面を参照して説明する。
図1は、実施例に係るメタン発酵前処理装置を示す概念図である。
図1に示すように、本実施例に係るメタン発酵前処理装置10は、食品生ごみ廃棄物11を粗破砕処理する第1の破砕機12−1と、粗破砕処理後に微破砕する第2の破砕機12−2と、破砕された廃棄物に混入している夾雑物(ビニール)13を選別する選別機14と、前記夾雑物が除去された食品生ごみ廃棄物を可溶化する可溶化槽15と、前記可溶化槽15の底部近傍から可溶化液18Aを抜出し、該抜出した可溶化液18A中に残留する夾雑物13を除去するドラムスクリーン16と、前記ドラムスクリーン16により夾雑物13が除去された可溶化液18Bを再度可溶化槽15に戻す戻しラインL3と、前記可溶化槽15からメタン発酵槽20にメタン発酵用可溶化液19を供給する供給ラインL4を具備し、且つ前記可溶化槽が前室15−1と後室15−2とに隔壁15aにより二分割されてなり、該隔壁15aを可溶化液が越流すると共に、前記前室15−1の底部から可溶化液18Aを抜出してドラムスクリーン16側に供給すると共に、前記ドラムスクリーンからの戻しラインL3の可溶化液18Bを前室の上部からシャワーノズル15bによりシャワー状で戻してなるものである。
A methane fermentation pretreatment device and a methane fermentation treatment system according to an embodiment of the present invention will be described with reference to the drawings.
Drawing 1 is a key map showing the methane fermentation pretreatment device concerning an example.
As shown in FIG. 1, the methane fermentation pretreatment apparatus 10 according to the present embodiment includes a first crusher 12-1 that roughly crushes food waste waste 11 and a second crusher that finely crushes after the coarse crushing process. Crusher 12-2, sorter 14 for sorting out contaminants (vinyl) 13 mixed in the crushed waste, and solubilization for solubilizing food waste waste from which the contaminants have been removed The tank 15, the solubilizing liquid 18 </ b> A is extracted from the vicinity of the bottom of the solubilizing tank 15, and the drum screen 16 for removing the impurities 13 remaining in the extracted solubilizing liquid 18 </ b> A, Is provided with a return line L 3 for returning the solubilized liquid 18B from the solubilizing tank 15 to the solubilizing tank 15 and a supply line L 4 for supplying the solubilizing liquid 19 for methane fermentation from the solubilizing tank 15 to the methane fermentation tank 20. And the solubilization tank is in front The chamber 15-1 and the rear chamber 15-2 are divided into two by a partition wall 15a. The solubilized liquid overflows the partition wall 15a, and the solubilized solution 18A is extracted from the bottom of the front chamber 15-1. supplies to the drum screen 16 side, is made back in the shower-like by the shower nozzle 15b from the upper portion of the front chamber lysate 18B of line L 3 return from the drum screen.

ここで、ラインL1は前記選別機14で夾雑物13を除去した食品生ごみを可溶化槽15に送給する廃棄物ラインであり、L2は可溶化液18Aをドラムスクリーン16に抜出す抜出しラインであり、L3はドラムスクリーン16で残留夾雑物を除去した可溶化液18Bを可溶化槽15に戻す戻しラインであり、L1〜L3で可溶化液の循環ラインを構成している。 Here, the line L 1 is a waste line for feeding the food waste from which the impurities 13 have been removed by the sorter 14 to the solubilization tank 15, and L 2 is for extracting the solubilizing liquid 18 A to the drum screen 16. L 3 is an extraction line, and L 3 is a return line for returning the solubilized liquid 18B from which residual impurities have been removed by the drum screen 16 to the solubilizing tank 15, and L 1 to L 3 constitute a circulation line for the solubilized liquid. Yes.

前記生ごみ廃棄物11を破砕する破砕機は本実施例では2段階破砕としており、前記第1の破砕機12−1では破砕後の粒径が200mm以下、より好ましくは50mm以下となるようにし、その後更に細かく砕く第2の破砕機12−2では、その破砕後の粒径が50mm以下、より好ましくは25mm以下となるようにしている。なお、廃棄物の種類は雑多であるので、持ち込まれる廃棄物の形態により、破砕機の数、種類及び組合せを適宜選定するようにすればよい。   The crusher for crushing the garbage waste 11 is a two-stage crushing in this embodiment, and in the first crusher 12-1, the particle size after crushing is 200 mm or less, more preferably 50 mm or less. Then, in the second crusher 12-2 that is further finely crushed, the particle size after crushing is 50 mm or less, more preferably 25 mm or less. Since the types of waste are various, the number, type and combination of crushers may be appropriately selected according to the form of waste to be brought in.

例えば第1の破砕機12−1をカッター幅43mmとし、第2の破砕機12−2をカッター幅25mmの二段階で破砕することで、生ごみを包むビニール袋や、例えば弁当・ヨーグルト・レトルト食品等のプラスチック容器を効率的に破砕することができる。   For example, the first crusher 12-1 has a cutter width of 43 mm, and the second crusher 12-2 is crushed in two stages with a cutter width of 25 mm, so that a plastic bag that wraps food waste, such as a lunch box, yogurt, or retort, is used. A plastic container such as food can be efficiently crushed.

これにより、例えば容積100L以下のビニール袋入り生ごみや30cm四方以下の形状の上述したような食品廃棄物を効率的に破砕でき、第2の破砕機12−2の出口形状で25mm以下とすることができる。
これにより、ビニール袋又はプラスチック容器から生ごみ廃棄物(容器又は袋入りの食品廃棄物を含む)を効率的に取り出すことができる。
Thereby, for example, food waste in a plastic bag with a volume of 100 L or less or food waste as described above having a shape of 30 cm square or less can be efficiently crushed, and the outlet shape of the second crusher 12-2 is 25 mm or less. be able to.
Thereby, garbage waste (a food waste containing a container or a bag is included) can be efficiently taken out from a plastic bag or a plastic container.

また、前記夾雑物13を選別する選別機14としては、ドラムスクリーン16の円筒部分がパンチングメタルからなるものであり、その孔径は直径20mm程度としている。
また、円筒の回転による遠心力とパンチングメタル開孔部分にて、前述の破砕機で破砕された生ごみの内の重い部分、具体的には水分を含む生ごみが比重分離され、円筒の外部に排出される。
Moreover, as the sorter 14 which sorts out the said impurities 13, the cylindrical part of the drum screen 16 consists of punching metal, The hole diameter is about 20 mm in diameter.
In addition, the centrifugal force generated by the rotation of the cylinder and the punched metal opening portion separates the heavy portion of the garbage that has been crushed by the aforementioned crusher, specifically the garbage containing moisture, by the specific gravity, and the outside of the cylinder. To be discharged.

一方で軽量のビニールやプラスチックはドラムスクリーン16の円筒内部に残り、更に円筒の中心軸方向に流れるよう配置された風力手段(図示せず)により円筒の中心軸方向に移送され、外部に排出される。
この比重選別と風力選別を組み合わせることで、効率的に分離可能となり、選別機の容積を小さくすることができる。
On the other hand, lightweight vinyl or plastic remains inside the cylinder of the drum screen 16, and is further transported in the direction of the center axis of the cylinder by wind force means (not shown) arranged to flow in the direction of the center axis of the cylinder, and discharged to the outside. The
By combining this specific gravity sorting and wind sorting, it becomes possible to efficiently separate, and the volume of the sorter can be reduced.

前記可溶化槽15は、破砕及び選別された生ごみ廃棄物を元々入っている可溶化液と混合し、温度を例えば20〜80℃、好ましくは30〜60℃又は35〜55℃としている。これはメタン発酵槽20での発酵処理温度に略合致させることでエネルギーロスの低減を図るようにしている。また、この可溶化槽15での生ごみ廃棄物の含水率は85%〜90%程度となるように水を添加して可溶化させるようにしており、滞留時間2日間程度で固体状の生ごみを液状に可溶化するようにしている。
ここで、可溶化されない夾雑物13は、軽量物は槽内の可溶化液表面の全体に浮遊し、重量物は槽底部に沈殿物17として沈積する。
The solubilization tank 15 is mixed with a solubilized liquid originally containing crushed and sorted garbage waste, and the temperature is set to, for example, 20 to 80 ° C., preferably 30 to 60 ° C. or 35 to 55 ° C. This is intended to reduce the energy loss by substantially matching the fermentation treatment temperature in the methane fermentation tank 20. In addition, water is added and solubilized so that the water content of the garbage waste in the solubilization tank 15 is about 85% to 90%. Garbage is solubilized in liquid form.
Here, as for the impurities 13 which are not solubilized, the light weight thing floats on the whole surface of the solubilization liquid in a tank, and a heavy thing deposits as the deposit 17 in the tank bottom part.

本発明では、可溶化槽15の底部から立設してなる隔壁15aを設け、槽内部を前室15−1と後室15−2とに隔壁15aを介して二分割されてなり、該隔壁15aを可溶化液が越流水18Cとして越流するようにしている。
このように槽内部を二分割することで、前室15−1は、夾雑物13が混入する部分とすると共に、後室15−2は越流した可溶化液から構成されるので、重い夾雑物は前室15−1において既に沈殿物17として分離されたものとなり、夾雑物13の混入割合が低下されるものとなる。
これにより、メタン発酵槽20に供給するメタン発酵用可溶化液中に、浮遊物及び夾雑物が極力少ないものとなり、この結果メタン発酵効率の更なる向上を図ることができる。
In the present invention, a partition wall 15a standing from the bottom of the solubilization tank 15 is provided, and the inside of the tank is divided into a front chamber 15-1 and a rear chamber 15-2 through the partition wall 15a. 15a is made to overflow the solubilized liquid as overflow water 18C.
By dividing the inside of the tank into two in this manner, the front chamber 15-1 is made a part into which the contaminants 13 are mixed, and the rear chamber 15-2 is composed of a solubilized liquid that has overflowed. A thing will already be isolate | separated as the precipitate 17 in the front chamber 15-1, and the mixing rate of the contaminant 13 will fall.
Thereby, in the solubilization liquid for methane fermentation supplied to the methane fermentation tank 20, suspended matter and contaminants are reduced as much as possible, and as a result, further improvement in methane fermentation efficiency can be achieved.

また、可溶化液をドラムスクリーン16に引抜く引抜ラインとして、可溶化槽15の底部から可溶化液18Aとして引抜くことで、沈積した夾雑物13からなる沈殿物17を効率的に引抜くことができる。   Further, as a drawing line for drawing the solubilized liquid to the drum screen 16, the sediment 17 consisting of the deposited contaminants 13 can be efficiently pulled out by pulling out the solubilized liquid 18 </ b> A from the bottom of the solubilizing tank 15. Can do.

本発明のドラムスクリーン16は、ワイヤーメッシュを用いることで、長細いビニール片のすり抜けを少なくし、効率的に分離しやすくしている。よって、例えばウェッジワイヤ等のスリットからなるスクリーンでは前記スリットの間をすり抜けることがあるが、ワイヤーメッシュを用いることでこのような不具合が解消される。   The drum screen 16 of the present invention uses a wire mesh to reduce the slipping of long and thin vinyl pieces and to facilitate efficient separation. Therefore, for example, a screen made of a slit such as a wedge wire may pass through the slit, but such a problem is solved by using a wire mesh.

また、ドラムスクリーン16であるワイヤーメッシュの目幅を5〜10mmとすることで、夾雑物としてビニール・プラスチックの他に、木質の繊維や大型の貝殻、種、割箸や串、骨などを効率的に除去できる。ドラムスクリーンとすることで、夾雑物から生ごみの溶けた可溶化液、比較的柔らかくなっている生ごみはスクリーンを通過し、夾雑物を効率的に分離することができる。   Also, by setting the mesh width of the wire mesh that is the drum screen 16 to 5 to 10 mm, it is possible to efficiently use wood fibers, large shells, seeds, disposable chopsticks, skewers, bones, etc. in addition to vinyl and plastic as impurities. Can be removed. By using the drum screen, the solubilized solution in which the garbage is dissolved from the contaminants and the relatively soft garbage pass through the screen, and the impurities can be efficiently separated.

また、可溶化槽15に可溶化液18Bを戻す戻しラインL3においては、ドラムスクリーン16で夾雑物13の多くが除去された可溶化液18Bを可溶化槽15の上部より槽内に返送し、ここでシャワーノズル15bによりシャワー状に降らせることで、可溶化槽15内の液面にスカムが形成されることを防止するようにしている。これにより、可溶化液中に浮遊している軽量の夾雑物を混合させるようにしており、再度循環する際に、夾雑物13としてドラムスクリーン16で分離して外部は排出するようにしている。 In the return line L 3 for returning the solubilized liquid 18B to the solubilizing tank 15, the solubilized liquid 18B from which most of the impurities 13 have been removed by the drum screen 16 is returned from the upper part of the solubilized tank 15 into the tank. In this case, the scum is prevented from being formed on the liquid surface in the solubilization tank 15 by being lowered into a shower shape by the shower nozzle 15b. Thereby, the lightweight foreign substance floating in the solubilized liquid is mixed, and when circulating again, it is separated as the foreign substance 13 by the drum screen 16 and discharged to the outside.

また、前述した前記メタン発酵前処理装置10で前処理されたメタン発酵用可溶化液19をメタン発酵処理するメタン発酵槽20とを具備するメタン発酵処理システムとすることで、本来処理する食品生ごみ廃棄物中の夾雑物が効率的に除去される結果、メタン発酵槽でのメタンガス発生量が低下するのを防止することができる。この結果、メタン発酵槽で得られるメタンガスを例えば燃料として利用する際の利用効率の低下を防止することができる。   Moreover, the food raw material which is originally processed is made into the methane fermentation processing system which comprises the methane fermentation solubilization liquid 20 which carries out the methane fermentation process of the solubilization liquid 19 for methane fermentation pre-processed by the said methane fermentation pre-processing apparatus 10 mentioned above. As a result of efficiently removing impurities in the waste waste, it is possible to prevent a decrease in the amount of methane gas generated in the methane fermentation tank. As a result, it is possible to prevent a decrease in utilization efficiency when the methane gas obtained in the methane fermentation tank is used as fuel, for example.

以上のように、本発明に係るメタン発酵前処理装置及びメタン発酵処理システムによれば、例えば生ごみ等の有機性廃棄物をメタン発酵で処理する際の処理効率を低減することなく、夾雑物を除去し、夾雑物に依存する悪影響を未然防止でき、食品生ごみ廃棄物のリサイクルシステムに用いて適している。   As described above, according to the methane fermentation pretreatment device and the methane fermentation treatment system according to the present invention, for example, impurities are reduced without reducing the treatment efficiency when treating organic waste such as garbage with methane fermentation. It is suitable for use in food waste recycling systems, because it can prevent adverse effects that depend on foreign substances.

実施例1に係るメタン発酵前処理装置の概略図である。1 is a schematic view of a methane fermentation pretreatment apparatus according to Example 1. FIG. 従来技術に係るメタン発酵前処理装置の概略図である。It is the schematic of the methane fermentation pretreatment apparatus which concerns on a prior art.

符号の説明Explanation of symbols

10 メタン発酵前処理装置
11 食品生ごみ廃棄物
12−1 第1の破砕機
12−2 第2の破砕機
13 夾雑物
14 選別機
15 可溶化槽
16 ドラムスクリーン
18A、18B、18C 可溶化液
19 メタン発酵用可溶化液
20 メタン発酵槽
DESCRIPTION OF SYMBOLS 10 Methane fermentation pretreatment apparatus 11 Food waste waste 12-1 1st crusher 12-2 2nd crusher 13 Contamination 14 Sorting machine 15 Solubilization tank 16 Drum screen 18A, 18B, 18C Solubilization liquid 19 Solubilizing solution for methane fermentation 20 Methane fermentation tank

Claims (4)

食品生ごみ廃棄物を粗破砕処理する第1の破砕機と、
粗破砕処理後に微破砕する第2の破砕機と、
破砕された廃棄物に混入している夾雑物を選別する選別機と、
前記夾雑物が除去された食品生ごみ廃棄物を可溶化する可溶化槽と、
前記可溶化槽の底部近傍から可溶化液を抜出し、該抜出した可溶化液中に残留する夾雑物を除去するドラムスクリーンと、
前記ドラムスクリーンにより夾雑物が除去された可溶化液を再度可溶化槽に戻す戻しラインと、
前記可溶化槽からメタン発酵槽にメタン発酵用可溶化液を供給する供給ラインを具備し、且つ
前記可溶化槽が前室と後室とに隔壁により二分割されてなり、該隔壁を可溶化液が越流すると共に、
前記前室の底部から可溶化液を抜出してドラムスクリーン側に供給すると共に、前記ドラムスクリーンからの戻しラインの可溶化液を前室の上部からシャワーノズルによりシャワー状で戻してなることを特徴とするメタン発酵前処理装置。
A first crusher for roughly crushing food waste waste;
A second crusher for fine crushing after the rough crushing treatment;
A sorter that sorts out impurities mixed in the crushed waste;
A solubilization tank for solubilizing food waste waste from which the contaminants have been removed;
A drum screen for extracting the lysate from the vicinity of the bottom of the solubilization tank and removing impurities remaining in the extracted lysate;
A return line for returning the solubilized liquid from which the contaminants have been removed by the drum screen to the solubilization tank again;
A supply line for supplying a solubilizing solution for methane fermentation from the solubilization tank to the methane fermentation tank; and the solubilization tank is divided into a front chamber and a rear chamber by a partition wall, solubilizing the partition wall As the liquid overflows,
The solubilized liquid is extracted from the bottom of the front chamber and supplied to the drum screen side, and the solubilized liquid in the return line from the drum screen is returned from the top of the front chamber in a shower shape by a shower nozzle. Methane fermentation pretreatment equipment.
請求項1において、
前記ドラムスクリーンのスクリーン目幅が5mm〜10mmであることを特徴とするメタン発酵前処理装置。
In claim 1,
The screen width of the drum screen is 5 mm to 10 mm.
請求項1又は2において、
除去される夾雑物がビニール系の回収夾雑物であることを特徴とするメタン発酵前処理装置。
In claim 1 or 2,
A methane fermentation pretreatment device, wherein the foreign matter to be removed is a vinyl-based collected foreign matter.
請求項1乃至3のいずれか一つのメタン発酵前処理装置と、
前記メタン発酵前処理装置で前処理されたメタン発酵用可溶化液をメタン発酵処理するメタン発酵槽とを具備することを特徴とするメタン発酵処理システム。
A methane fermentation pretreatment device according to any one of claims 1 to 3,
A methane fermentation treatment system comprising: a methane fermentation tank for methane fermentation treatment of a solubilized solution for methane fermentation pretreated by the methane fermentation pretreatment device.
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