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JP4101945B2 - Decomposition accelerator for organic waste - Google Patents
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JP4101945B2 - Decomposition accelerator for organic waste - Google Patents

Decomposition accelerator for organic waste Download PDF

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JP4101945B2
JP4101945B2 JP24978798A JP24978798A JP4101945B2 JP 4101945 B2 JP4101945 B2 JP 4101945B2 JP 24978798 A JP24978798 A JP 24978798A JP 24978798 A JP24978798 A JP 24978798A JP 4101945 B2 JP4101945 B2 JP 4101945B2
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organic waste
decomposition
microorganisms
acid
decomposition accelerator
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JP2000070909A (en
JP2000070909A5 (en
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稔彦 竹花
遼 武井
建文 小栗
耕平 宇野
守 本間
博和 松井
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Adeka Corp
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Adeka Corp
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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
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A40/00Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
    • Y02A40/10Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
    • Y02A40/20Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
    • 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
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/40Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse

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  • Micro-Organisms Or Cultivation Processes Thereof (AREA)
  • Processing Of Solid Wastes (AREA)
  • Treatment Of Sludge (AREA)
  • Fertilizers (AREA)

Description

【0001】
【発明の属する技術分野】
本発明は、レストラン、ホテル、飲食店、結婚式場、給食施設等の外食産業から排出される生ごみや、食品工場より排出される有機性廃棄物等を好気的発酵処理する際に使用される分解促進剤及び分解促進方法、並びに好気的発酵処理過程におけるpH調整方法に関する。
【0002】
【従来の技術】
微生物を利用した好気的発酵処理による有機性廃棄物の堆肥化は、農業の現場において古くより行われてきた技術である。この原理を工学的に応用した、高速堆肥化施設やバイオ式生ゴミ処理装置は、現在広く普及している。特に、バイオ式生ゴミ処理装置は、従来の大規模な回収一括集中処理に代わり、有機性廃棄物をその発生場所において速やかに処理するといった個別分散処理を可能にした。この個別分散処理は、有機性廃棄物の回収までの保管場所の衛生改善、回収運搬コストの削減、他の資源ゴミの回収効率の向上に大きく貢献している。このような微生物を利用した好気的発酵処理は、ランニングコストが低廉で、エネルギー消費量の少ない省資源的な方法であるばかりでなく、発酵処理物を堆肥として土壌に還元することができ、有機性廃棄物の再利用を可能にした。
【0003】
【発明が解決しようとする課題】
しかし、微生物を利用した好気的発酵処理法は、有機物の分解反応の主体である微生物が活発に生育可能な環境条件下でのみ機能し得る。従って、不適当な環境条件下においては、環境条件の調整が必要になる。発酵処理過程で関与する微生物の多くは、中性から弱アルカリ性に生育の至適pHを持つため、酸性環境下ではその増殖活性が低下し、pH4〜5以下では、全く増殖を示さなくなるものが多い。このため発酵処理過程でpHの低下が生じると分解反応速度が低下し、処理過程の大幅な遅延や停止を引き起こすことがある。
【0004】
こうした発酵処理過程におけるpHの低下は、主として有機性廃棄物に由来する有機酸等の酸性物質の生成とその蓄積に起因する。この有機酸生成は、有機性廃棄物の急速な分解反応時に、酸素の濃度が低下して嫌気的な状態になると起こりやすく、停電等の不慮の事故により攪拌や切り返し等の操作が停止し、酸素の供給が不足した場合にも同様の現象が起こる。
こうした酸性物質を中和してpHを調整するために、有機物処理装置に測定器を用いて発酵物質のpHを測定する機構や、pH値が適正範囲を外れた場合に消石灰等のアルカリ剤を投入する機構を搭載させていた(特開昭55−113688号公報、特開平1−145388号公報)。しかし、処理装置にpHを測定する機構やアルカリ剤を投入する機構を搭載すると、装置が複雑になりコストも高くなり、ことに装置が小規模であるバイオ式生ゴミ処理装置による個別分散処理に適用することは難しい。又、固相反応系である発酵処理物の正確なpH測定は困難であり、アルカリ剤の供給が不足すれば効果が得られないばかりか、過剰のアルカリ剤の供給によりpHが上昇し過ぎて逆に微生物の活性低下を引き起こす等の問題があった。
【0005】
又、有機物処理装置の発酵槽内に、水素イオン濃度を中性から弱アルカリ性に保つpH調整剤及び有機物を分解する微生物を固定した水分調整剤を充填することで、有機物を高速発酵させる方法が提案された(特開平7−303871号公報)。しかしこの水分調節剤は作成に1週間以上の日数を要し、製造コストが高くなるという問題があった。
有機性廃棄物の発酵処理過程で、pHを低下させる要因は、有機酸の蓄積であるが、逆にpHを高める要因はアンモニアの発生である。良好な発酵処理が進行すると、タンパク質の分解によって生じたアンモニアは、水に溶解し水酸化アンモニウムとなりpHを上昇させる。ある程度pHが上昇すると、アンモニアがアンモニアガスとして揮散するため、発酵に障害を与えるほどpHが上昇することはない。本発明では、こうした有機性廃棄物に含まれるタンパク質の分解にともなうpHの改善効果に着目し、酸性環境下においても十分な増殖活性を有する耐酸性微生物を利用することで本発明を完成させた。
【0006】
即ち本発明は、(1)χ-プロテオバクテリア エスピ−MB8(寄託番号FERM P−16948)又はブルクホルデリア エスピーMB11(寄託番号FERM P−16949)から選択される耐酸性のタンパク質資化性微生物からなる有機性廃棄物の分解促進剤であって、該有機性廃棄物が厨芥である、該分解促進剤、(2)(1)に記載の分解促進剤を使用する、有機性廃棄物の分解処理方法であって、該有機廃棄物が厨芥である、該分解処理方法、および(3)(1)に記載の分解促進剤を使用する、有機性廃棄物の発酵処理過程におけるpH調整方法であって、該有機廃棄物が厨芥である、該pH調整方法である。
【0007】
【発明の実施の形態】
本発明は、耐酸性を有する微生物を分解促進剤として使用することによって、酸性化した有機性廃棄物を好気的に発酵処理することができる。
本発明で使用する耐酸性を有する微生物は、pH2〜5の酸性範囲において良好に増殖する好酸性微生物、或いはpH2〜7の酸性から中性付近まで増殖可能な耐酸性微生物の何れでも良い。例えば、Bacillus属、Pseudomonas属等のバクテリア、Actinomyces属、Streptomyces属等の放線菌、Saccharomyces属、Hansenula属、Candida属等の酵母、及びAspergillus属、Penicillium属、Mucor属等の糸状菌等にこのような耐酸性を有する微生物の存在が知られている。又、本発明の耐酸性微生物の産生する酵素(好ましくはプロテアーゼ)の至適pHが2.0〜4.0、好ましくは3.0〜4.0、より好ましくは3.0〜3.5であるような微生物が好ましい。
【0008】
本発明においては、このような耐酸性の微生物を使用することによりpHの低い酸性領域で有機性廃棄物の処理を行うことができるが、耐酸性微生物としてタンパク質資化性微生物を使用することが特に好ましい。このタンパク質資化性微生物を使用した場合は、有機物の分解反応を行わせるとともに、同時にタンパク質の分解によりアンモニアが発生することによって酸性化した有機性廃棄物のpHを上昇させることができ、その結果多くの好気的発酵が活発に行われる中性又は弱アルカリ性の環境条件を整えることができるので特に好ましい。このような耐酸性のタンパク質資化性微生物は、χ‐Proteobacteria属、Burkholderia属、Bacillus属、Xanthomonas属、Pseudomonas属等に存する。これらの中で最も好ましい菌株は、それぞれχ‐プロテオバクテリア エスピ−(χ‐Proteobacteria sp.)MB8(寄託番号FERM P−16948)及びブルクホルデリア エスピー(Burkholderia sp.)MB11(寄託番号FERM P−16949)であり、それぞれ前記の寄託番号にて工業技術院生命工学工業技術研究所に寄託した。
【0009】
又、本発明の分解促進剤或いは分解方法では、好気的発酵処理に関与する他の微生物の添加を排除するものではない。このような微生物は中性から弱アルカリ性に生育の至適pHを持つものが多く、本発明の分解促進剤の効果によりpHが酸性から中性側にシフトするとともにその活性を回復し、活発な分解反応を行うようになる。併用することができる微生物としては、Bacillus属等の中温性及び好熱性微生物製剤が挙げられる。
本発明の分解処理の対象である有機性廃棄物とは、微生物の好気的発酵により分解される廃棄物であれば特に限定されないが、例えば厨房から排出される生ごみのような厨芥の他、コーヒー粕、酒粕、汚泥、更には食品工場から排出される食品残渣等が挙げられる。
【0010】
本発明の分解促進剤の使用時期、使用量は特に限定されない。一般的には、何らかの理由で、発酵処理物のpHが低下した時に速やかに適当量添加すればよい。しかし、タンパク質資化性の耐酸性微生物を使用した場合は、発酵処理開始時より、本発明の分解促進剤を他の耐酸性を持たない微生物と共存させることにより、発酵処理物のpH低下を防止し、発酵処理を安定したものとすることも可能である。一般に、外食産業から排出される有機性廃棄物は弱酸性であることが多い。又、酸性を呈する有機性廃棄物は、これまでは中和処理を施さなければ円滑な発酵処理を行うことは困難であったが、本発明の分解促進剤を利用して、このような酸性の有機性廃棄物に対するpH調整を行うことにより速やかにpHが改善され、引き続く発酵処理における発酵が促進される。
【0011】
又、本発明の分解促進剤は、有機性廃棄物の分解を促進するために添加される他の化合物との併用を妨げるものではない。本発明の分解促進剤は、有機性廃棄物のpHを弱酸性から弱アルカリ性に維持する緩衝作用を有する塩類、窒素を含有する粉体上の物質等と併用することができる。例えば、リン酸ナトリウム塩類、リン酸カリウム塩類、硫酸アンモニウム、尿素等が挙げられる。
本発明においては、処理物の性状によっては(N源が不足しているような場合)、N源の添加が必要となる。そこで有機性廃棄物のC/N比を改善する目的で添加されるアンモニウム塩、尿素等の添加が必要になることもあるが、可能であれば、窒素源に富む他の有機性廃棄物と混合して処理されることが最も望ましい。
【0012】
【実施例】
以下、実施例により本発明を更に具体的に説明する。尚、以下の実施例中、部及び%は特に記載が無い限り重量基準である。
(実施例1)
まず、本発明に好適に使用することができる微生物であるχ‐プロテオバクテリア エスピ−MB8(寄託番号FERM P−16948)及びブルクホルデリア エスピーMB11(寄託番号FERM P−16949)が、タンパク質の分解にともなって、pHを上昇させる効果について実証した。下記の組成のACS培地(Soil Biol. Biochem. 7巻、345頁、1975年をもとに改変)により標記菌株を30℃で5日間培養し、菌体の生育、培地のpH、及びタンパク質分解の指標として、反応の第1段階で働くキーエンザイムであるプロテアーゼ活性を測定した。
【0013】
[ACS培地の組成]
スターチ:1%、カゼイン:0.3%、 NaCl:0.2%、
MgSO4・7H2O:0.005%、 CaCO3:0.002%、
FeSO4・7H2O:0.001%、 KH2PO4:0.3%、
尚、培地のpHは4.5であった。
【0014】
[菌体の生育測定法]
菌体の生育は、アデノシン3リン酸濃度(ATP濃度)を測定しその指標とした。ATP濃度の測定は、ATP測定用試薬キット ルシフェールLU(キッコーマン(株)社製)を使用し、ルミノメーター(ルミテスター K−100、キッコーマン(株)社製)により測定した発光計測値をもとに相対値を算出した。
【0015】
[酵素活性測定法]
Muraoらの方法(J. Biol. Chem. 268巻、349頁、1993年)により、ヘモグロビンを基質として、pH:3.0、37℃の条件で酵素反応を行った。反応液1mlあたり毎分1マイクログラムのチロシン相当量の酸可溶性ペプチドを生成する酵素量を1単位(1U)とした。
【0016】
以上の条件及び測定方法によって得られた、菌体の生育、培地中に分泌されたプロテアーゼ活性、及び培地のpH値の経時変化を図1〜図3に示した。以上の結果によれば、菌体の生育によってプロテアーゼが産生されるとともに培地のpH値が中性付近にまで上昇していることが分かった。培地中のプロテアーゼ活性とpH値の関係をプロットたものを図4に示す。この結果から、産生したプロテアーゼによるタンパク質の分解が起こるとpH値が明らかに中性側にシフトしていることが示された。
【0017】
(実施例2)
次に、実際に外食産業より排出された厨芥を用いて本発明による分解反応促進効果について検証を行った。ここで用いた厨芥は、含水率77.6%、pH4.76、C/N比12.4とごく一般的な性状を示しているものである。容量3リットルの発酵槽内に、通気性改良材、水分調整材として機能する150g(乾重量)の反応媒体(スギオガクズ)を充填後、食堂の厨房より排出された厨芥200g(湿重量)にそれぞれχ‐プロテオバクテリア エスピ−MB8株又はブルクホルデリア エスピーMB11株のいづれかを接種した二つの試験区を設け、これを媒体と攪拌しながら発酵処理を行った。発酵槽内の初期水分含有率は55%に調節した。厨芥を投入した後、発酵槽下部より0.5リットル/分の速度で空気を通気した。発酵処理過程における、発酵槽内温度、及び排気ガス中の二酸化炭素濃度を連続的にモニタリングし、発酵処理状況を解析した。又、比較例として、バシルスサブチリス(Bacillus subtilis)BN1001(明治製菓社製、寄託番号FERM P−11132)を接種した試験区を同様にして設けた。この菌株は、有機物の発酵過程に関与する一般的な種であるが、耐酸性は有していない。これを比較例1とする。
【0018】
発酵処理過程における排気ガス中の二酸化炭素濃度、及び発酵槽内温度の経時変化を図5〜図6に示す。χ‐プロテオバクテリア エスピ−MB8株又はブルクホルデリア エスピーMB11株を接種した試験区では、これらを接種していない比較例1と比べ明らかな分解促進効果が現れており、有機物の分解により発生する二酸化炭素濃度、分解熱ともに高い値を示していることが分かる。
【0019】
【発明の効果】
厨房から発生する生ごみのような酸性化した有機性廃棄物の分解処理に当たり、耐酸性の微生物、特に耐酸性のタンパク質資化性微生物からなる本発明の分解促進剤によって特別な手段を用いずに効率的に分解処理することができる。本発明によれば、単に酸性状態で活性があるだけでなく、タンパク質の分解により自動的にpHが中性から欠くアルカリ性に調整され、その他の微生物の作用も活発化し、効率的な処理が可能となる。
【図面の簡単な説明】
【図1】χ‐プロテオバクテリア エスピ−MB8株とブルクホルデリア エスピーMB11株について、培養時間とATP濃度の関係を示すグラフである。
【図2】MB8株とMB11株について、培養時間とプロテアーゼ活性の関係を示すグラフである。
【図3】MB8株とMB11株について、培養時間とpHの関係を示すグラフである。
【図4】MB8株とMB11株について、培地pHとプロテアーゼ活性の関係を示すグラフである。
【図5】MB8株、MB11株及びバシルスサブチリスBN1001株について、発酵時間と二酸化炭素濃度の関係を示すグラフである。
【図6】MB8株、MB11株及びバシルスサブチリスBN1001株について、発酵時間と発酵槽内温度の関係を示すグラフである。
[0001]
BACKGROUND OF THE INVENTION
The present invention is used for aerobic fermentation treatment of food waste discharged from the restaurant industry such as restaurants, hotels, restaurants, wedding halls, and lunch facilities, and organic waste discharged from food factories. The present invention relates to a decomposition accelerator, a decomposition acceleration method, and a pH adjustment method in an aerobic fermentation treatment process.
[0002]
[Prior art]
Composting organic waste by aerobic fermentation using microorganisms is a technique that has long been performed in the field of agriculture. High-speed composting facilities and bio-type garbage processing devices that apply this principle in engineering are now widely used. In particular, the bio-type garbage processing apparatus has made it possible to perform individual distributed processing, such as quickly processing organic waste at the place where it is generated, instead of the conventional large-scale collective batch concentration processing. This individual dispersion process greatly contributes to improving the hygiene of the storage area until the collection of organic waste, reducing the collection and transportation costs, and improving the collection efficiency of other resource garbage. Such an aerobic fermentation process using microorganisms is not only a resource-saving method with low running cost and low energy consumption, but also can reduce the fermented product to soil as compost, It enabled reuse of organic waste.
[0003]
[Problems to be solved by the invention]
However, the aerobic fermentation treatment method using microorganisms can function only under environmental conditions in which microorganisms that are the main components of organic matter decomposition reactions can actively grow. Therefore, adjustment of the environmental conditions is necessary under inappropriate environmental conditions. Many of the microorganisms involved in the fermentation process have an optimum pH for growth from neutral to weakly alkaline, so that their growth activity is reduced in an acidic environment, and at pH 4-5 or lower, no growth is shown at all. Many. For this reason, when the fall of pH arises in a fermentation process, a decomposition reaction rate will fall and it may cause the substantial delay and stop of a process.
[0004]
Such a decrease in pH during the fermentation process is mainly caused by the generation and accumulation of acidic substances such as organic acids derived from organic waste. This organic acid generation is likely to occur when the oxygen concentration is lowered and becomes anaerobic during the rapid decomposition reaction of organic waste, and operations such as agitation and reversal stop due to an unexpected accident such as a power failure, A similar phenomenon occurs when the supply of oxygen is insufficient.
In order to neutralize these acidic substances and adjust the pH, a mechanism for measuring the pH of the fermented substance using a measuring device in an organic matter treatment apparatus, or an alkaline agent such as slaked lime when the pH value is outside the appropriate range A mechanism for loading was mounted (Japanese Patent Laid-Open Nos. 55-11368 and 1-145388). However, when a mechanism for measuring pH or a mechanism for introducing an alkaline agent is installed in the processing apparatus, the apparatus becomes complicated and expensive, and in particular, for individual distributed processing by a bio-type garbage processing apparatus with a small scale. It is difficult to apply. In addition, it is difficult to accurately measure the pH of a fermented product that is a solid phase reaction system, and if the supply of the alkaline agent is insufficient, the effect cannot be obtained, and the pH increases excessively due to the supply of the excessive alkaline agent. Conversely, there were problems such as causing a decrease in the activity of microorganisms.
[0005]
In addition, there is a method of fermenting organic matter at high speed by filling a fermenter of an organic matter processing apparatus with a pH adjuster that maintains the hydrogen ion concentration from neutral to weakly alkaline and a moisture regulator that fixes microorganisms that decompose organic matter. It has been proposed (Japanese Patent Laid-Open No. 7-303871). However, this moisture regulator has a problem that it takes a week or more for preparation and the production cost is increased.
In the process of fermentation of organic waste, the factor that lowers the pH is the accumulation of organic acid, but the factor that raises the pH is the generation of ammonia. As a good fermentation process proceeds, ammonia produced by protein degradation dissolves in water and becomes ammonium hydroxide, raising the pH. When pH rises to some extent, ammonia volatilizes as ammonia gas, so the pH does not rise so as to hinder fermentation. In the present invention, the present invention has been completed by using an acid-resistant microorganism having sufficient growth activity even in an acidic environment, paying attention to the effect of improving the pH accompanying the degradation of proteins contained in such organic waste. .
[0006]
That is, the present invention relates to (1) an acid-resistant protein-assimilating microorganism selected from χ-proteobacteria Esp-MB8 (deposit number FERM P-16948) or Burkholderia sp. MB11 (deposit number FERM P-16949). a decomposition accelerator for the organic waste composed, organic waste is garbage, the decomposition accelerator, using a decomposition accelerator according to (2) (1), the decomposition of organic waste A method for adjusting the pH in the fermentation process of organic waste, wherein the decomposition method is the soot, and the decomposition accelerator according to (3) (1) is used. The method for adjusting pH, wherein the organic waste is soot.
[0007]
DETAILED DESCRIPTION OF THE INVENTION
In the present invention, acidified organic waste can be aerobically fermented by using an acid-resistant microorganism as a decomposition accelerator.
The acid-resistant microorganism used in the present invention may be either an acidophilic microorganism that grows well in the acidic range of pH 2 to 5, or an acid-resistant microorganism that can grow from acidic pH 2 to about neutral. For example, bacteria such as Bacillus genus, Pseudomonas genus, actinomyces genus, Streptomyces genus actinomycetes, Saccharomyces genus, Hansenula genus, Candida genus yeast, and Aspergillus genus, Penicillium genus, Mucor genus fungi, etc. The existence of microorganisms with good acid resistance is known. In addition, the optimum pH of the enzyme (preferably protease) produced by the acid-resistant microorganism of the present invention is 2.0 to 4.0, preferably 3.0 to 4.0, more preferably 3.0 to 3.5. Such microorganisms are preferred.
[0008]
In the present invention, organic waste can be treated in an acidic region having a low pH by using such acid-resistant microorganisms. However, protein-assimilating microorganisms can be used as acid-resistant microorganisms. Particularly preferred. When this protein assimilating microorganism is used, the decomposition of the organic matter is performed, and at the same time, the pH of the acidified organic waste can be raised by the generation of ammonia by the decomposition of the protein. This is particularly preferable because neutral or weak alkaline environmental conditions in which many aerobic fermentations are actively performed can be adjusted. Such acid-resistant protein-assimilating microorganisms exist in the χ-Proteobacteria genus, Burkholderia genus, Bacillus genus, Xanthomonas genus, Pseudomonas genus and the like. The most preferred strains of these are respectively χ-Proteobacteria sp. MB8 (deposit number FERM P-16948) and Burkholderia sp. MB11 (deposit number FERM P-16949). And deposited at the Institute of Biotechnology, National Institute of Technology.
[0009]
In addition, the degradation accelerator or degradation method of the present invention does not exclude the addition of other microorganisms involved in the aerobic fermentation treatment. Many of these microorganisms have an optimum pH for growth from neutral to weakly alkaline, and the pH is shifted from acidic to neutral due to the effect of the degradation accelerator of the present invention, and its activity is restored and active. Decomposition reaction begins. Examples of microorganisms that can be used in combination include mesophilic and thermophilic microorganism preparations such as Bacillus.
The organic waste subject to the decomposition treatment of the present invention is not particularly limited as long as it is a waste decomposed by aerobic fermentation of microorganisms. For example, the waste other than kitchen waste discharged from kitchens. , Coffee lees, sake lees, sludge, and food residues discharged from food factories.
[0010]
There are no particular limitations on the timing and amount of use of the decomposition accelerator of the present invention. Generally, an appropriate amount may be quickly added when the pH of the fermented product is lowered for some reason. However, when protein-assimilable acid-resistant microorganisms are used, the pH of the fermentation-treated product can be lowered by allowing the degradation accelerator of the present invention to coexist with other microorganisms not having acid resistance from the start of the fermentation process. It is possible to prevent and make the fermentation process stable. In general, organic waste discharged from the food service industry is often weakly acidic. In addition, it has been difficult for organic wastes that exhibit acidity to be subjected to a smooth fermentation treatment unless they are neutralized. By adjusting the pH of the organic waste, the pH is quickly improved, and the fermentation in the subsequent fermentation treatment is promoted.
[0011]
Further, the decomposition accelerator of the present invention does not prevent the combined use with other compounds added to accelerate the decomposition of organic waste. The decomposition accelerator of the present invention can be used in combination with salts having a buffering action for maintaining the pH of organic waste from weakly acidic to weakly alkaline, substances on nitrogen-containing powders, and the like. For example, sodium phosphate salts, potassium phosphate salts, ammonium sulfate, urea and the like can be mentioned.
In the present invention, depending on the properties of the treated product (when the N source is insufficient), it is necessary to add the N source. Therefore, it may be necessary to add ammonium salt, urea, etc. added for the purpose of improving the C / N ratio of organic waste, but if possible, other organic waste rich in nitrogen sources Most preferably, they are processed in a mixed manner.
[0012]
【Example】
Hereinafter, the present invention will be described more specifically with reference to examples. In the following examples, parts and% are based on weight unless otherwise specified.
Example 1
First, microorganisms that can be preferably used in the present invention, χ-proteobacteria Esp-MB8 (deposit number FERM P-16948) and Burkholderia sp. MB11 (deposit number FERM P-16949) are used for protein degradation. Along with this, the effect of increasing the pH was demonstrated. The title strain is cultured for 5 days at 30 ° C. in an ACS medium (modified from Soil Biol. Biochem. 7, 345, 1975) with the following composition to grow the cell, pH of the medium, and proteolysis As an indicator, protease activity, a key enzyme acting in the first stage of the reaction, was measured.
[0013]
[Composition of ACS medium]
Starch: 1%, Casein: 0.3%, NaCl: 0.2%,
MgSO4 · 7H2O: 0.005%, CaCO3: 0.002%,
FeSO4 · 7H2O: 0.001%, KH2PO4: 0.3%,
The pH of the medium was 4.5.
[0014]
[Method for measuring growth of bacterial cells]
The growth of the bacterial cells was used as an indicator by measuring the adenosine triphosphate concentration (ATP concentration). The ATP concentration was measured using an ATP measurement reagent kit Lucifer LU (manufactured by Kikkoman Corporation) and based on luminescence measurement values measured by a luminometer (Lumitester K-100, manufactured by Kikkoman Corporation). The relative value was calculated.
[0015]
[Enzyme activity measurement method]
By the method of Murao et al. (J. Biol. Chem. 268, 349, 1993), the enzyme reaction was carried out under the conditions of pH: 3.0 and 37 ° C. using hemoglobin as a substrate. The amount of enzyme that produces 1 microgram of tyrosine-equivalent acid-soluble peptide per 1 ml of the reaction solution was defined as 1 unit (1 U).
[0016]
The changes over time in the growth of the bacterial cells, the protease activity secreted into the medium, and the pH value of the medium obtained by the above conditions and measurement method are shown in FIGS. According to the above results, it was found that protease was produced by the growth of the bacterial cells and the pH value of the medium was increased to near neutrality. A plot of the relationship between the protease activity in the medium and the pH value is shown in FIG. From this result, it was shown that the pH value was clearly shifted to the neutral side when protein degradation by the produced protease occurred.
[0017]
(Example 2)
Next, it verified about the decomposition reaction promotion effect by this invention using the waste actually discharged | emitted from the restaurant industry. The soot used here has a water content of 77.6%, a pH of 4.76, and a C / N ratio of 12.4, showing very general properties. After filling a 3-liter fermenter with 150 g (dry weight) of the reaction medium (Sugiogakuzu), which functions as a breathability improver and moisture adjuster, 200 g (wet weight) discharged from the canteen kitchen Two test sections were inoculated with either χ-proteobacterial Esp-MB8 strain or Burkholderia sp. MB11 strain, and fermentation treatment was carried out while stirring this with the medium. The initial moisture content in the fermenter was adjusted to 55%. After introducing the koji, air was vented from the bottom of the fermenter at a rate of 0.5 l / min. During the fermentation process, the temperature in the fermenter and the carbon dioxide concentration in the exhaust gas were continuously monitored to analyze the status of the fermentation process. Further, as a comparative example, a test area inoculated with Bacillus subtilis BN1001 (manufactured by Meiji Seika Co., Ltd., deposit number FERM P-11132) was similarly provided. This strain is a general species involved in the fermentation process of organic matter, but does not have acid resistance. This is referred to as Comparative Example 1.
[0018]
The changes over time in the concentration of carbon dioxide in the exhaust gas and the temperature in the fermenter during the fermentation process are shown in FIGS. In the test plots inoculated with χ-proteobacterial Esp-MB8 strain or Burkholderia sp. It can be seen that both the carbon concentration and the heat of decomposition show high values.
[0019]
【The invention's effect】
In the decomposition treatment of acidified organic waste such as garbage generated from kitchens, no special means is used by the decomposition accelerator of the present invention consisting of acid-resistant microorganisms, particularly acid-resistant protein-utilizing microorganisms. Can be efficiently decomposed. According to the present invention, not only is it active in an acidic state, but also the pH is automatically adjusted from neutral to alkaline due to protein degradation, the action of other microorganisms is activated, and efficient treatment is possible It becomes.
[Brief description of the drawings]
FIG. 1 is a graph showing the relationship between culture time and ATP concentration for χ-proteobacterial Esp-MB8 strain and Burkholderia sp. MB11 strain.
FIG. 2 is a graph showing the relationship between culture time and protease activity for MB8 and MB11 strains.
FIG. 3 is a graph showing the relationship between culture time and pH for MB8 and MB11 strains.
FIG. 4 is a graph showing the relationship between medium pH and protease activity for MB8 and MB11 strains.
FIG. 5 is a graph showing the relationship between fermentation time and carbon dioxide concentration for MB8 strain, MB11 strain and Bacillus subtilis BN1001 strain.
FIG. 6 is a graph showing the relationship between fermentation time and fermenter temperature for MB8 strain, MB11 strain and Bacillus subtilis BN1001 strain.

Claims (3)

χ-プロテオバクテリア エスピ−MB8(寄託番号FERM P−16948)又はブルクホルデリア エスピーMB11(寄託番号FERM P−16949)から選択される耐酸性のタンパク質資化性微生物からなる有機性廃棄物の分解促進剤であって、該有機性廃棄物が厨芥である、該分解促進剤。  Decomposition promotion of organic waste consisting of acid-resistant protein-assimilating microorganisms selected from χ-proteobacteria ESPI-MB8 (deposit number FERM P-16948) or Burkholderia sp. MB11 (deposit number FERM P-16949) The decomposition accelerator, wherein the organic waste is soot. 請求項1に記載の分解促進剤を使用する、有機性廃棄物の分解処理方法であって、該有機廃棄物が厨芥である、該分解処理方法。An organic waste decomposition treatment method using the decomposition accelerator according to claim 1, wherein the organic waste is soot. 請求項1に記載の分解促進剤を使用する、有機性廃棄物の発酵処理過程におけるpH調整方法であって、該有機廃棄物が厨芥である、該pH調整方法。A method for adjusting pH in a fermentation treatment process of organic waste, wherein the decomposition accelerator according to claim 1 is used, wherein the organic waste is soot.
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