JP2003211134A - Fermentation method for organic waste - Google Patents

Fermentation method for organic waste

Info

Publication number
JP2003211134A
JP2003211134A JP2002012956A JP2002012956A JP2003211134A JP 2003211134 A JP2003211134 A JP 2003211134A JP 2002012956 A JP2002012956 A JP 2002012956A JP 2002012956 A JP2002012956 A JP 2002012956A JP 2003211134 A JP2003211134 A JP 2003211134A
Authority
JP
Japan
Prior art keywords
fermentation
days
treatment
organic waste
mixture
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP2002012956A
Other languages
Japanese (ja)
Inventor
Fumiya Kitauchi
文哉 北内
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Unitika Ltd
Original Assignee
Unitika Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Unitika Ltd filed Critical Unitika Ltd
Priority to JP2002012956A priority Critical patent/JP2003211134A/en
Publication of JP2003211134A publication Critical patent/JP2003211134A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • 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

Landscapes

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

Abstract

<P>PROBLEM TO BE SOLVED: To provide a fermentation method capable of producing good quality compost having high application safety which does no harm to plants when it is applied to green farmland in a shorter fermentation period compared with a conventional method, downsizing a fermentation tank and facility and realizing reduction of a running cost. <P>SOLUTION: The fermentation method for organic waste is a method for fermenting a mixture of organic waste and chaff. The first fermentation first process 2 in which fermentation lasts for 3-10 days is carried out. All the obtained processed materials are transferred to the second fermentation process 3 in which fermentation lasts for 3-10 days. All the obtained processed materials are transferred to the third fermentation process 4 fermentation lasts for is not more than 30 days. <P>COPYRIGHT: (C)2003,JPO

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は、汚泥や、家畜糞
尿、生ごみ等の有機性廃棄物の発酵処理方法に関するも
のである。
TECHNICAL FIELD The present invention relates to a method for fermenting and treating sludge, organic waste such as livestock manure, and garbage.

【0002】[0002]

【従来の技術】従来、下水、し尿、産業廃水などの廃水
処理に伴って発生する汚泥や、家畜糞尿、生ごみ等の有
機性廃棄物は、焼却・埋立といった処分形態を取ってき
た。しかしながら、近年、地球温暖化の防止や燃料費の
抑制、ダイオキシン発生問題、最終処分地の確保が困難
等の社会的事情によって、コンポストとしての再利用が
注目されている。
2. Description of the Related Art Conventionally, sludge generated by treatment of wastewater such as sewage, human waste, industrial wastewater, and organic waste such as livestock excrement and garbage have been disposed of by incineration or landfill. However, in recent years, due to social circumstances such as prevention of global warming, reduction of fuel cost, the problem of dioxin generation, and difficulty in securing a final disposal site, re-use as compost has attracted attention.

【0003】コンポストは有機性廃棄物を微生物によっ
て分解処理することにより作製され、緑農地に還元でき
有効に再利用される理想的な処理処分方法である。しか
しながら、有機物の分解処理が不十分なコンポストを緑
農地に施用した場合、土壌中でのコンポストの分解速度
が速すぎ、土壌中の酸素や窒素が欠乏して植物に害を与
える問題がある。
Compost is an ideal treatment and disposal method that is produced by decomposing organic waste with microorganisms and can be effectively reused by being returned to green agricultural land. However, when compost with insufficient decomposition treatment of organic matter is applied to green agricultural land, there is a problem that the decomposition rate of compost in soil is too fast, and oxygen and nitrogen in the soil are deficient, which damages plants.

【0004】この様な不良質のコンポストの流通を避け
るため、コンポストの製造指針が設けられている。例え
ば、下水汚泥資源利用協議会発行の「下水汚泥コンポス
トの指標(その2)」では、下水汚泥コンポストの製造
規準として、発酵期間が10〜14日の1次発酵、およ
び発酵期間が1〜3ヶ月以上の2次発酵を定めている。
この様な製造指針に沿った発酵処理を行うことで、施用
した際に植物に害を及ぼす可能性の低い、すなわち施用
安全性の高いコンポストが作製される。
In order to avoid the distribution of such defective compost, a manufacturing guideline for compost is provided. For example, in the "Indicator of sewage sludge compost (Part 2)" issued by the Sewage Sludge Resource Utilization Council, as the production criteria of sewage sludge compost, the fermentation period is 10 to 14 days, and the primary fermentation period is 1 to 3 days. The second fermentation of more than a month is specified.
By carrying out the fermentation treatment in accordance with such a production guideline, a compost having a low possibility of damaging a plant when applied, that is, a highly safe application is produced.

【0005】[0005]

【発明が解決しようとする課題】しかしながら、この様
な製造指針に沿って施設を建設した場合、発酵槽の容量
が膨大になり、大きなスペースの敷地確保が必要となる
と共に、通気や切り返しなどに必要な運転コストが高い
といった問題がある。
[Problems to be Solved by the Invention] However, when a facility is constructed in accordance with such a manufacturing guideline, the capacity of the fermenter becomes enormous, and it is necessary to secure a large space site, as well as ventilation and turning back. There is a problem that the required operating cost is high.

【0006】本発明は、前述した従来技術の問題点を解
決し、短い発酵期間であっても施用安全性の高いコンポ
ストを作製する発酵処理方法を提供することを目的とす
る。
An object of the present invention is to solve the above-mentioned problems of the prior art and to provide a fermentation treatment method for producing compost having high application safety even in a short fermentation period.

【0007】[0007]

【課題を解決するための手段】本発明者は、上記課題を
解決するために鋭意検討した結果、発酵処理工程を完全
に2工程または3工程に区切り、各工程間、混合物をバ
ッチ移送させることにより、発酵期間を短くしても施用
安全性の高いコンポストが得られることを見出し、本発
明に到達した。
Means for Solving the Problems As a result of intensive studies to solve the above problems, the present inventor has completely divided the fermentation treatment step into two or three steps, and batch-transfers the mixture between the steps. According to the present invention, it was found that a compost with high application safety can be obtained even if the fermentation period is shortened, and the present invention has been completed.

【0008】すなわち、本発明は、有機性廃棄物とモミ
ガラの混合物を発酵処理する方法であって、発酵処理日
数が3〜10日間である発酵第1工程を行い、得られた
処理物の全量を発酵処理日数が3〜10日間である発酵
第2工程に移すことを特徴とする有機性廃棄物の発酵処
理方法を要旨とするものであり、好ましくは発酵第2工
程で得られた処理物の全量をさらに発酵処理日数が30
日以内である発酵第3工程に移すことを特徴とするもの
である。また、好ましくは、仕切によって上下2段に仕
切られた発酵槽の上段で発酵第1工程を行い、次いで発
酵槽の下段で発酵第2工程の発酵処理を行う前記の発酵
処理方法であり、さらに有機性廃棄物が、廃水処理施設
から排出された有機性汚泥である前記の発酵処理方法で
ある。
That is, the present invention is a method for fermenting a mixture of organic waste and rice husks, wherein the fermentation first step in which the number of days of fermenting treatment is 3 to 10 days is performed, and the total amount of the obtained treated product is obtained. Is a fermentation treatment method for an organic waste, characterized in that the fermentation treatment is carried out for 3 to 10 days, and preferably the treated product obtained in the fermentation second step The total amount of the
It is characterized in that it is transferred to the fermentation third step which is within a day. Further, preferably, the fermentation treatment method, wherein the fermentation first step is performed in the upper stage of the fermentation tank divided into upper and lower two stages by a partition, and then the fermentation second step is performed in the lower stage of the fermentation tank. In the above fermentation treatment method, the organic waste is organic sludge discharged from the wastewater treatment facility.

【0009】[0009]

【発明の実施の形態】以下に、本発明を詳細に説明す
る。本発明における有機性廃棄物とは、下水、し尿、産
業廃水などの廃水処理に伴って発生する汚泥、それらの
汚泥を脱水した脱水ケーキ、家畜糞尿、生ごみ、剪定
枝、刈草および各種有機性産業廃棄物等の、主成分が微
生物によって分解可能な有機物から構成された廃棄物を
指す。
BEST MODE FOR CARRYING OUT THE INVENTION The present invention is described in detail below. The organic waste in the present invention, sewage, human waste, sludge generated by the treatment of wastewater such as industrial wastewater, dehydrated cake obtained by dehydrating those sludge, livestock excreta, garbage, pruned branches, cut grass and various organic It refers to industrial wastes and other wastes whose main components are organic substances that can be decomposed by microorganisms.

【0010】これらの有機性廃棄物は、水分調整と通気
性の改良のためモミガラを混合した混合物として発酵処
理する。使用するモミガラの性状は特に限定するもので
なく、籾摺り時に発生する生モミガラ、生モミガラをハ
ンマーミル等で乾式粉砕した乾式粉砕モミガラ、生モミ
ガラに注水してスクリューミル等で湿式粉砕した湿式粉
砕モミガラ等が好適に用いられる。
These organic wastes are subjected to fermentation treatment as a mixture in which chaffs are mixed in order to control water content and improve air permeability. The properties of the chaff used are not particularly limited, and raw chaffs generated during hulling, dry chaffs that are dry-smashed with a hammer mill, etc. Etc. are preferably used.

【0011】また、有機性廃棄物とモミガラの混合時
に、発酵処理を終了した発酵処理物あるいは発酵処理途
中の発酵処理物を混合することもできる。このような発
酵処理物を混合することで、モミガラ添加量が削減で
き、発酵菌の種付けにもなる。
Further, when the organic waste and the rice husks are mixed, it is also possible to mix the fermented product after the fermentation process or the fermented product during the fermentation process. By mixing such a fermented product, the amount of rice husk added can be reduced and seeding of fermenting bacteria can be achieved.

【0012】有機性廃棄物、モミガラおよび発酵処理物
の混合量は、混合後の含水率が40〜80%となるよう
に混合するのが好ましく、含水率50〜70%がさらに
好ましい。含水率が40%未満の時、発酵途中で含水率
が低くなりすぎて、良好な発酵反応が進行しなくなるた
め好ましくない。また、含水率が80%を超える時、良
好な高温好気発酵が進行しない場合があるため好ましく
ない。
[0012] The organic waste, rice husk and fermented product are preferably mixed so that the water content after mixing is 40 to 80%, more preferably 50 to 70%. When the water content is less than 40%, the water content becomes too low during fermentation, and a good fermentation reaction does not proceed, which is not preferable. Further, when the water content exceeds 80%, good high temperature aerobic fermentation may not proceed, which is not preferable.

【0013】本発明は、この有機性廃棄物とモミガラの
混合物を発酵処理する方法であって、まず発酵第1工程
として、3〜10日間の発酵処理を行う。この発酵第1
工程では有機性廃棄物に含まれる易分解性の有機物が急
激に微生物分解されることにより、混合物が65℃以上
の高温となる。この高温環境によって病原菌、寄生虫
卵、植物種子等が死滅あるいは不活性化される。
The present invention is a method for fermenting a mixture of this organic waste and rice husk, and first, as the first step of fermentation, fermenting treatment is carried out for 3 to 10 days. This fermentation first
In the process, the easily decomposable organic matter contained in the organic waste is rapidly microbially decomposed, so that the temperature of the mixture becomes 65 ° C. or higher. This high temperature environment kills or inactivates pathogenic fungi, parasite eggs, plant seeds, and the like.

【0014】この発酵第1工程に要する発酵処理時間
は、原料となる有機性廃棄物によって異なるが、3〜1
0日間である。処理時間が3日間未満であると、易分解
性有機物を多く残したまま発酵第2工程に移行し、発酵
不十分で製品の品質が悪化するため採用できない。処理
時間が10日間を超えると、製品品質には影響ないが処
理槽容積が必要以上に大きくなり採用できない。
The fermentation treatment time required for the first fermentation step varies depending on the organic waste used as a raw material, but is 3 to 1
0 days. If the treatment time is less than 3 days, the process proceeds to the second step of fermentation while leaving a large amount of easily decomposable organic substances, and the fermentation is insufficient and the quality of the product deteriorates. If the treatment time exceeds 10 days, the product quality is not affected, but the treatment tank volume becomes unnecessarily large and it cannot be used.

【0015】発酵第1工程に用いる発酵処理方式は特に
限定するものではなく、堆積式、ロータリーキルン式、
オーガー式、立型多段式、サイロ式、ビン式等の方式が
好適に使用される。
The fermentation treatment method used in the first fermentation step is not particularly limited, and may be a sedimentation type, a rotary kiln type,
Auger type, vertical multistage type, silo type, bottle type and the like are preferably used.

【0016】これらの発酵処理方式を採用した発酵槽に
有機性廃棄物とモミガラの混合物を放置することで発酵
処理は進行するが、発酵反応の進行を促進する目的で、
撹拌や通気を行うことが好ましい。撹拌方法は特に限定
するものではなく、堆積式の場合はショベルカー、コン
ベア、クレーン等による撹拌、ロータリーキルン式の場
合は回転等による撹拌、オーガー式の場合はオーガー等
による撹拌、立型多段式の場合は回転軸に水平に突出さ
せた撹拌翼による撹拌や、レーキ、パドル、ゲート等の
撹拌手段と重力落下等による撹拌、サイロ式の場合はク
レーン、ピンミキサー、重力落下等による撹拌、ビン式
の場合はスクープやパドル等による撹拌が好適に用いら
れる。
Fermentation treatment proceeds by leaving a mixture of organic waste and rice husk in a fermentation tank employing these fermentation treatment methods, but for the purpose of promoting the progress of fermentation reaction,
It is preferable to perform stirring and aeration. The stirring method is not particularly limited, in the case of a stacking type, stirring by a shovel car, a conveyor, a crane, etc., in the case of a rotary kiln type, stirring by rotation, etc., in the case of an auger type, stirring by an auger, etc., a vertical multi-stage type In the case of agitating blades that are projected horizontally on the rotating shaft, or by means of agitation such as rake, paddle, gate, etc. and gravity drop, in the case of silo type, crane, pin mixer, agitation by gravity drop, bottle type, etc. In this case, stirring with a scoop or paddle is preferably used.

【0017】また、通気は混合物を好気状態に維持する
ためのもので、通気方法としては、混合物を貯留する発
酵槽内部に送気する、発酵槽内部から排気する、発酵槽
内部に対して送気および排気を行う等が好適に用いられ
る。通気量は処理する有機性廃棄物によって異なるが、
1m3の混合物に対し、1分あたり0.01〜2.0m3
の流量が好ましい。1分あたり0.01m3未満である
と混合物が良好な好気状態にならない場合があり、1分
あたり2.0m3を超えると混合物の発酵温度が低くな
る場合があり好ましくない。
Aeration is for maintaining the mixture in an aerobic state. As the aeration method, air is sent to the inside of the fermentation tank in which the mixture is stored, exhausted from the inside of the fermentation tank, or inside the fermentation tank. Air supply and exhaust are preferably used. The air flow rate depends on the organic waste to be treated,
Mixture of 1 m 3 to per minute 0.01~2.0M 3
Is preferred. If it is less than 0.01 m 3 per minute, the mixture may not be in a good aerobic state, and if it exceeds 2.0 m 3 per minute, the fermentation temperature of the mixture may be low, which is not preferable.

【0018】本発明では、発酵第1工程の発酵処理中に
新たな混合物が追加投入され混合されることなく、完全
に所定時間の処理がなされ、発酵第1工程終了後は、混
合物の全量を発酵第2工程にバッチ移送する。ゆえに発
酵処理時間が所定時間より短い混合物の第2工程への移
行、すなわちショートパスを生じないため、安定した品
質となる。
According to the present invention, a new mixture is not added and mixed during the fermentation process of the first fermentation step, and the mixture is completely treated for a predetermined period of time. After the first fermentation step, the total amount of the mixture is changed. Batch transfer to the second fermentation step. Therefore, the fermentation process time does not shift to the second step of the mixture, which is shorter than the predetermined time, that is, the short pass does not occur, and the quality is stable.

【0019】本発明における発酵第2工程では発酵第1
工程と同様に3〜10日間処理する。この発酵第2工程
では有機性廃棄物に含まれる比較的分解され易い有機物
が微生物により分解、安定化される。
In the second fermentation step of the present invention, the first fermentation step is used.
It is treated for 3 to 10 days in the same manner as the process. In the second fermentation step, the organic substances contained in the organic waste, which are relatively easily decomposed, are decomposed and stabilized by the microorganisms.

【0020】この発酵第2工程に要する発酵処理時間
は、原料となる有機性廃棄物によって異なるが、3〜1
0日間である。処理時間が3日間未満であると、有機物
の分解、安定化が不十分となり製品の品質が悪化するた
め採用できない。処理時間が10日間を超えると、製品
品質には影響ないが処理槽容積が必要以上に大きくなり
採用できない。
The fermentation treatment time required for the second fermentation step varies depending on the organic waste used as a raw material, but it is 3 to 1
0 days. If the treatment time is less than 3 days, decomposition and stabilization of organic substances will be insufficient and the quality of the product will be deteriorated, so that it cannot be used. If the treatment time exceeds 10 days, the product quality is not affected, but the treatment tank volume becomes unnecessarily large and it cannot be used.

【0021】発酵第2工程に用いる発酵処理方式は、発
酵第1工程と同様、特に限定するものではない。また、
発酵第1工程と同様、発酵反応の進行を促進する目的
で、撹拌や通気を行うことが好ましい。
The fermentation treatment system used in the second fermentation step is not particularly limited as in the first fermentation step. Also,
As in the first fermentation step, stirring and aeration are preferably performed for the purpose of promoting the progress of the fermentation reaction.

【0022】本発明では、発酵第2工程の発酵処理中に
被処理時間の異なる混合物同士が混じり合うことがない
ので、完全に所定時間の処理がなされ、発酵第2工程終
了後は、混合物の全量を発酵第3工程にバッチ移送す
る。ゆえに発酵処理時間が所定時間より短い混合物の発
酵第3工程への移行、すなわちショートパスを生じない
ため、安定した品質となる。
In the present invention, since the mixtures having different treatment times do not mix with each other during the fermentation process of the second fermentation step, the treatment is completely performed for a predetermined time, and after the second fermentation step is completed, The whole amount is batch-transferred to the fermentation third step. Therefore, a transition to the third step of fermentation of the mixture, that is, a short pass does not occur in the mixture in which the fermentation treatment time is shorter than a predetermined time, so that the quality is stable.

【0023】本発明における発酵第1工程および発酵第
2工程は、俗に1次発酵処理と呼ばれる処理時期に相当
する。これらの工程の反応場となる発酵槽は、前述した
通り、特に限定されるものでないが、これらの工程を仕
切によって上下2段に仕切られた発酵槽、すなわち立型
2段式発酵槽で行うことは、得に好ましい。立型2段式
発酵槽は立型ゆえに設置スペースが小さく、密閉箱型で
あるため、発酵熱の外部への放散を抑止できると共に、
発酵反応の際に発生する強い臭気を外部に漏らさずに捕
集できる。捕集した臭気を脱臭処理装置に導入して脱臭
処理することで、作業環境や施設周辺環境を良好に保持
できる。
The first fermentation step and the second fermentation step in the present invention correspond to the treatment period commonly called the primary fermentation treatment. As described above, the fermenter serving as a reaction field of these steps is not particularly limited, but these steps are performed in a fermenter divided into upper and lower two stages by a partition, that is, a vertical two-stage fermentor. Is especially preferable. The vertical two-stage fermenter has a small installation space because it is a vertical type, and because it is a closed box type, it is possible to suppress the dissipation of fermentation heat to the outside,
The strong odor generated during the fermentation reaction can be collected without leaking to the outside. By introducing the collected odor into the deodorization processing device and performing deodorization processing, the work environment and the environment around the facility can be maintained well.

【0024】本発明における発酵第3工程は、俗に2次
発酵処理と呼ばれるもので、本発明ではこの2次発酵処
理時間を30日以内とする。発酵第3工程では有機性廃
棄物に含まれる比較的分解され難い有機物やモミガラ由
来の有機物が微生物により分解される。
The third fermentation step in the present invention is so-called secondary fermentation treatment, and in the present invention, the secondary fermentation treatment time is within 30 days. In the third fermentation step, microorganisms decompose the organic substances contained in the organic waste that are relatively difficult to decompose and the organic substances derived from rice husk.

【0025】発酵第3工程に要する処理時間は、原料と
なる有機性廃棄物の種類によって異なる。比較的分解に
時間の要する油脂分を多く含んだ有機性廃棄物や、分解
性有機物比率が高く安定化に時間を要する有機性廃棄物
等は長めの処理時間を設定する必要がある。一方、比較
的分解安定化されやすい、例えば、廃水処理施設から排
出された有機性汚泥等の場合、発酵第3工程を0日、す
なわち省略して製品化工程に移行してもよい。
The processing time required for the third fermentation step depends on the type of organic waste used as a raw material. It is necessary to set a long treatment time for organic wastes containing a large amount of fats and oils, which require a relatively long time to decompose, or organic wastes having a high degradable organic matter ratio and requiring a long time for stabilization. On the other hand, in the case of, for example, organic sludge discharged from the wastewater treatment facility that is relatively easily decomposed and stabilized, the third fermentation step may be skipped on day 0, that is, the production step may be performed.

【0026】発酵第3工程に用いる発酵処理方式は、発
酵第1工程および発酵第2工程と同様、特に限定するも
のではなく、また、発酵第1工程および発酵第2工程と
同様、発酵反応の進行を促進する目的で、撹拌や通気を
行うことが好ましい。
The fermentation treatment method used in the fermentation third step is not particularly limited as in the fermentation first step and the fermentation second step, and in the same manner as the fermentation first step and the fermentation second step, the fermentation reaction It is preferable to carry out stirring and aeration for the purpose of promoting the progress.

【0027】発酵第3工程で所定の時間処理された混合
物は、取り出され、製品化される。製品化の際、使用者
の要求を考慮して、コンポストとして取り扱いやすい含
水率にまで水分を除去する乾燥処理やペレターザー等に
よる造粒化処理を行うこともできる。
The mixture treated in the third fermentation step for a predetermined time is taken out and commercialized. At the time of commercialization, in consideration of the user's request, it is possible to carry out a drying treatment for removing water to a water content which is easy to handle as compost or a granulating treatment by a pelletizer or the like.

【0028】本発明によって生産された製品、すなわち
コンポストの品質は、従来の発酵処理方法で60日以上
処理された製品の品質に匹敵し、緑農地に施用した際、
植物の生長に害を及ぼす恐れがない。
The quality of the product produced according to the present invention, namely compost, is comparable to the quality of the product treated for more than 60 days by the conventional fermentation treatment method, and when applied to green farmland,
There is no fear of damaging the growth of plants.

【0029】以下、本発明の実施態様の一例を図1を参
照しながら説明する。図1は本発明の有機性廃棄物の発
酵処理方法のプロセスの一例を示す図である。まず、有
機性廃棄物とモミガラを混合工程1で混合した後、混合
物を発酵第1工程2に移送する。発酵第1工程2で所定
時間の発酵処理終了後、混合物の全量を発酵第2工程3
にバッチ移送する。発酵第2工程3で所定時間の発酵処
理終了後、混合物の全量を発酵第3工程4にバッチ移送
する。発酵第3工程4で所定時間の発酵処理を終えた混
合物は製品化工程5で製品化される。また、各発酵工程
から次工程への移送時や製品化工程5において、混合物
の一部を混合工程1に返送ライン6を通して返送するこ
ともできる。
An example of the embodiment of the present invention will be described below with reference to FIG. FIG. 1 is a diagram showing an example of a process of a method for fermenting an organic waste according to the present invention. First, organic waste and rice husks are mixed in the mixing step 1, and then the mixture is transferred to the first fermentation step 2. After completion of fermentation treatment for a predetermined time in the first fermentation step 2, the whole amount of the mixture is fermented in the second step 3
Batch transfer to. After completion of the fermentation treatment for a predetermined time in the second fermentation step 3, the entire amount of the mixture is batch-transferred to the third fermentation step 4. The mixture that has undergone the fermentation treatment for a predetermined time in the third fermentation step 4 is commercialized in the commercialization step 5. Further, at the time of transfer from each fermentation process to the next process or in the commercialization process 5, a part of the mixture can be returned to the mixing process 1 through the return line 6.

【0030】[0030]

【実施例】以下、本発明を実施例により具体的に説明す
る。 実施例1 下水処理場から排出された脱水汚泥、モミガラおよび発
酵処理を終了した発酵処理物を混合した混合物を、上下
2段に仕切られた円筒立型2段式発酵槽の上段に投入し
て、本発明の方法に準じて、上段で6日間処理(発酵第
1工程)した後、全量を下段に移送し、下段で6日間の
発酵処理(発酵第2工程)を行った。上段および下段発
酵槽の通気は、外気を1m3の混合物に対し1分あたり
0.1m3送気して行った。また攪拌は、垂直方向回転
軸に水平に突出させた撹拌翼を15分間で1回転するこ
とで行った。所定時間の発酵処理終了後、発酵処理物の
全量を取り出し、さらに堆積式発酵槽で30日間処理
(発酵第3工程)した。堆積式発酵槽の通気は、外気を
1m3の混合物に対し1分あたり0.1m3送気して行っ
た。またショベルを用いて10日毎に1回切り返しを行
った。
EXAMPLES The present invention will be specifically described below with reference to examples. Example 1 A mixture obtained by mixing dehydrated sludge discharged from a sewage treatment plant, rice husk and fermented material after fermentation treatment was put into the upper stage of a cylindrical vertical two-stage fermenter partitioned into upper and lower stages. According to the method of the present invention, after the upper stage was treated for 6 days (fermentation first step), the whole amount was transferred to the lower stage, and the lower stage was subjected to fermentation treatment for 6 days (fermentation second step). Venting of the upper and lower fermentor outside air was carried out 0.1 m 3 air per minute to a mixture of 1 m 3. The stirring was performed by rotating the stirring blade horizontally projected on the vertical rotating shaft once for 15 minutes. After completion of the fermentation treatment for a predetermined time, the whole amount of the fermented product was taken out and further treated in a sedimentary fermenter for 30 days (fermentation third step). Venting the deposition type fermenter, outside air was carried out 0.1 m 3 air per minute to a mixture of 1 m 3. Moreover, it cut back once every 10 days using a shovel.

【0031】計42日間の発酵処理により得られた発酵
処理物を含水率35%にまで乾燥した後、強熱減量、p
H、硝酸性窒素、全窒素、BODおよびコマツナ発芽指
数を測定した。なお、これらの測定項目は「下水汚泥コ
ンポストの指標(その2)」(下水汚泥資源利用協議会
発行、1985年)における、腐熟コンポストの品質規
準を定める項目である。強熱減量、pH、硝酸性窒素、
全窒素、BODの測定は「下水汚泥分析法」(下水汚泥
資源利用協議会発行、1996年)あるいは「肥料分析
法」(養賢堂発行、1988年)に準じて行った。コマ
ツナ発芽指数の測定は以下の方法で行った。
The fermented product obtained by the fermentation treatment for a total of 42 days was dried to a water content of 35%, and then the ignition loss, p
H, nitrate nitrogen, total nitrogen, BOD and Komatsuna germination index were measured. In addition, these measurement items are the items that determine the quality standard of the sewage sludge compost in "Indicator of sewage sludge compost (Part 2)" (published by Sewage Sludge Resource Utilization Council, 1985). Loss on ignition, pH, nitrate nitrogen,
Total nitrogen and BOD were measured according to the “Sewage Sludge Analysis Method” (issued by the Sewage Sludge Resource Utilization Council, 1996) or the “Fertilizer Analysis Method” (issued by Yokendo, 1988). The Komatsuna germination index was measured by the following method.

【0032】コマツナ発芽指数測定方法:乾燥重量1g
に相当する発酵処理物に対し、蒸留水20mlを添加し
て、60℃、3時間の抽出処理を行った。この抽出液を
ガーゼでろ過した後、ろ液10mlを2枚のろ紙を敷い
たシャーレ内に注入した。このろ紙の上にコマツナ種子
50粒を播き、シャーレの蓋をした後、室温、光照射な
し条件下で栽培した。また対照区として、蒸留水を用い
て同様の栽培を行った。栽培3日目の種子の発芽数を測
定して、対照区の値を100とした場合の相対値(発芽
指数:%)で評価した。測定結果を表1に示す。
Komatsuna germination index measuring method: Dry weight 1 g
20 ml of distilled water was added to the fermented product corresponding to and the extraction treatment was performed at 60 ° C. for 3 hours. After filtering this extract with gauze, 10 ml of the filtrate was poured into a petri dish lined with two filter papers. 50 Komatsuna seeds were sown on the filter paper, covered with a Petri dish, and then cultivated at room temperature without light irradiation. As a control, the same cultivation was performed using distilled water. The germination number of the seeds on the 3rd day of cultivation was measured and evaluated by the relative value (germination index:%) when the value of the control was 100. The measurement results are shown in Table 1.

【0033】[0033]

【表1】 [Table 1]

【0034】実施例2 実施例1と同一の混合物を、実施例1と同一の立型2段
式発酵槽の上段に投入して、本発明の方法に準じて、上
段で6日間処理(発酵第1工程)した後、全量を下段に
移送し、下段で6日間の発酵処理(発酵第2工程)を行
った。通気および攪拌条件は実施例1と同様に行った。
計12日間の発酵処理により得られた発酵処理物を含水
率35%にまで乾燥した後、強熱減量、pH、硝酸性窒
素、全窒素、BODおよびコマツナ発芽指数を測定し
た。測定方法は実施例1と同じである。測定結果を表1
に示す。
Example 2 The same mixture as in Example 1 was added to the upper stage of the same vertical two-stage fermentation tank as in Example 1 and treated for 6 days in the upper stage (fermentation according to the method of the present invention). After the first step), the whole amount was transferred to the lower stage, and the fermentation treatment (fermentation second step) was performed for 6 days in the lower stage. Aeration and stirring conditions were the same as in Example 1.
The fermented product obtained by the fermentation treatment for a total of 12 days was dried to a water content of 35%, and then the loss on ignition, pH, nitrate nitrogen, total nitrogen, BOD and komatsuna germination index were measured. The measuring method is the same as that of the first embodiment. Table 1 shows the measurement results
Shown in.

【0035】比較例1 実施例1と同一の混合物を、1日に1回の混合物の取り
出し、および新たな混合物の投入を行うサイロ式発酵槽
に投入して、12日間の発酵処理を行った。通気条件は
実施例1と同様に行い、攪拌は1日1回の取り出し時に
ピンミキサーの回転によって行った。この方式は、本発
明の方法と異なり、発酵槽内で被処理時間の異なる混合
物同士が混じり合う。取り出した混合物は、さらに実施
例1と同一の堆積式発酵槽で60日間処理した。
Comparative Example 1 The same mixture as in Example 1 was placed in a silo fermenter in which the mixture was taken out once a day and a new mixture was placed, and a fermentation treatment was carried out for 12 days. . The aeration conditions were the same as in Example 1, and the stirring was performed by rotating the pin mixer at the time of taking out once a day. This method is different from the method of the present invention in that the mixtures having different treatment times are mixed in the fermenter. The mixture taken out was further treated in the same sedimentary fermenter as in Example 1 for 60 days.

【0036】計72日間の発酵処理によって得られた発
酵処理物を含水率35%にまで乾燥した後、強熱減量、
pH、硝酸性窒素、全窒素、BODおよびコマツナ発芽
指数を測定した。測定方法は実施例1と同じである。測
定結果を表1に示す。
After the fermented product obtained by the fermenting process for a total of 72 days was dried to a water content of 35%, the loss on ignition,
pH, nitrate nitrogen, total nitrogen, BOD and komatsuna germination index were measured. The measuring method is the same as that of the first embodiment. The measurement results are shown in Table 1.

【0037】比較例2 実施例1と同一の混合物を、比較例1と同一のサイロ式
発酵槽に投入して、12日間の発酵処理を行った。通気
は実施例1と同様に、攪拌は比較例1と同様に行った。
計12日間の発酵処理により得られた発酵処理物を含水
率35%にまで乾燥した後、強熱減量、pH、硝酸性窒
素、全窒素、BODおよびコマツナ発芽指数を測定し
た。測定方法は実施例1と同じである。測定結果を表1
に示す。
Comparative Example 2 The same mixture as in Example 1 was put into the same silo type fermenter as in Comparative Example 1 to carry out fermentation treatment for 12 days. Aeration was performed as in Example 1, and stirring was performed as in Comparative Example 1.
The fermented product obtained by the fermentation treatment for a total of 12 days was dried to a water content of 35%, and then the loss on ignition, pH, nitrate nitrogen, total nitrogen, BOD and komatsuna germination index were measured. The measuring method is the same as that of the first embodiment. Table 1 shows the measurement results
Shown in.

【0038】実施例1(本発明の方法による42日間処
理)の発酵処理物、および実施例2(本発明の方法によ
る12日間処理)の発酵処理物の性状は、全ての項目に
おいて、比較例1(本発明の方法と異なる一般的な発酵
方法による72日間処理)の発酵処理物と同程度であ
り、腐熟は十分であると判断された。一方、比較例2
(本発明の方法と異なる一般的な発酵方法による12日
間処理)の発酵処理物の性状は、特にpH、BOD、コ
マツナ発芽指数が、実施例1,実施例2および比較例1
の発酵処理物に劣り、腐熟は不十分であると判断され
た。
The properties of the fermented product of Example 1 (42 days treated by the method of the present invention) and the fermented product of Example 2 (12 days treated by the method of the present invention) are comparative examples in all items. It was judged that the ripening was sufficient as it was about the same as the fermented product of No. 1 (72-day treatment by a general fermentation method different from the method of the present invention). On the other hand, Comparative Example 2
The properties of the fermented product (treated for 12 days by a general fermentation method different from the method of the present invention) are, in particular, pH, BOD and Komatsuna germination index in Example 1, Example 2 and Comparative Example 1.
It was judged to be inferior to the fermented product of No. 1, and the ripening was insufficient.

【0039】[0039]

【発明の効果】本発明によると、従来の方法に比べ短い
発酵期間で、緑農地に施用した際、植物に害を与えるこ
とのない、すなわち施用安全性の高い良質のコンポスト
を作製することができ、発酵槽や施設のコンパクト化、
さらには運転コストの低減が図れる。
EFFECTS OF THE INVENTION According to the present invention, it is possible to produce a high-quality compost that does not harm plants when applied to green agricultural land in a shorter fermentation period as compared with conventional methods, that is, has high application safety. It is possible to make fermentation tanks and facilities compact,
Furthermore, the operating cost can be reduced.

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

【図1】本発明の有機性廃棄物の発酵処理方法のプロセ
スの一例を示す図である。
FIG. 1 is a diagram showing an example of a process of a fermentation treatment method for organic waste of the present invention.

【符号の説明】[Explanation of symbols]

1 混合工程 2 発酵第1工程 3 発酵第2工程 4 発酵第3工程 5 製品化工程 6 返送ライン 1 mixing process 2 Fermentation first step 3 Second fermentation process 4 Fermentation 3rd process 5 Commercialization process 6 Return line

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 有機性廃棄物とモミガラの混合物を発酵
処理する方法であって、発酵処理日数が3〜10日間で
ある発酵第1工程を行い、得られた処理物の全量を発酵
処理日数が3〜10日間である発酵第2工程に移すこと
を特徴とする有機性廃棄物の発酵処理方法。
1. A method of fermenting a mixture of organic waste and rice husk, which comprises performing a fermentation first step in which the number of days of fermenting treatment is 3 to 10 days, and the total amount of the obtained treated product is the number of days of fermenting treatment. The method for fermentation treatment of organic waste, comprising transferring to a second fermentation step for 3 to 10 days.
【請求項2】 有機性廃棄物とモミガラの混合物を発酵
処理する方法であって、発酵処理日数が3〜10日間で
ある発酵第1工程を行い、得られた処理物の全量を発酵
処理日数が3〜10日間である発酵第2工程に移し、得
られた処理物の全量を発酵処理日数が30日以内である
発酵第3工程に移すことを特徴とする有機性廃棄物の発
酵処理方法。
2. A method of fermenting a mixture of organic waste and rice husk, which comprises performing a fermentation first step in which the number of days of fermentation treatment is 3 to 10 days, and the total amount of the obtained treated product is determined by the number of days of fermentation treatment. Is transferred to the second fermentation step, which is 3 to 10 days, and the entire amount of the obtained processed product is transferred to the third fermentation step, which has a fermentation processing time of 30 days or less. .
【請求項3】 仕切によって上下2段に仕切られた発酵
槽の上段で発酵第1工程を行い、次いで発酵槽の下段で
発酵第2工程の発酵処理を行う請求項1又は2記載の発
酵処理方法。
3. The fermentation treatment according to claim 1, wherein the fermentation first step is performed in the upper stage of the fermentation tank divided into upper and lower two stages by the partition, and then the fermentation second step is performed in the lower stage of the fermentation tank. Method.
【請求項4】 有機性廃棄物が、廃水処理施設から排出
された有機性汚泥である請求項1ないし3のいずれかに
記載の発酵処理方法。
4. The fermentation treatment method according to claim 1, wherein the organic waste is organic sludge discharged from a wastewater treatment facility.
JP2002012956A 2002-01-22 2002-01-22 Fermentation method for organic waste Pending JP2003211134A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2002012956A JP2003211134A (en) 2002-01-22 2002-01-22 Fermentation method for organic waste

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2002012956A JP2003211134A (en) 2002-01-22 2002-01-22 Fermentation method for organic waste

Publications (1)

Publication Number Publication Date
JP2003211134A true JP2003211134A (en) 2003-07-29

Family

ID=27650029

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2002012956A Pending JP2003211134A (en) 2002-01-22 2002-01-22 Fermentation method for organic waste

Country Status (1)

Country Link
JP (1) JP2003211134A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2015013779A (en) * 2013-07-05 2015-01-22 中部エコテック株式会社 Compost, and method for manufacturing the compost

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2015013779A (en) * 2013-07-05 2015-01-22 中部エコテック株式会社 Compost, and method for manufacturing the compost

Similar Documents

Publication Publication Date Title
US6200475B1 (en) Method of converting organic waste by thermophilic fermentation
Sharma et al. Bioconversion of flowers waste: Composting using dry leaves as bulking agent
JP2015167912A (en) Livestock excreta treating system
KR200389525Y1 (en) Fermentation equipment of animals-excretions
KR100479836B1 (en) Fermentation equipment of animals-excretions and method therefor
JP2008050248A (en) Grass-derived organic fermentation fertilizer and its manufacturing method
CN210394109U (en) Earthworm reactor
Choi Optimal operating parameters in the composting of swine manure with wastepaper
JP2002143896A (en) Method for treating organic waste and sewage sludge or animal feces, or sewage sludge and animal feces
JPH10174582A (en) Active microbial mixture and its use
KR101976009B1 (en) Composition for treating solid organic wastes, treatment method of solid organic waste using thereof and compost manufactured by the same
JP2003211134A (en) Fermentation method for organic waste
Dincă et al. Recovery of organic waste through composting process
JP2000143375A (en) Compost
JPS5830274B2 (en) New composting method for organic waste
JP2021127400A (en) Soil improvement agent, fertilizer and soil improvement method
JP2008037718A (en) Low odor composting treatment method
JPH0585874A (en) Production of soil conditioner
KR102502684B1 (en) Organic sludge treatment method with reduced odor
JP3809782B2 (en) Garbage disposal method
JP3054355B2 (en) Three-dimensional multi-stage multipurpose fermenter
JPH1053481A (en) Treatment of shellfish or the like, treatment apparatus for shellfish or the like or treating material for shellfish or the like
JPH0645515B2 (en) How to treat shochu waste liquid
KR101784953B1 (en) Microorganism product with mixed microbe and evaporative pig excrements processing method using it
JPH107481A (en) Production of soil improver and its storing method

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20050119

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20070126

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20070206

A02 Decision of refusal

Free format text: JAPANESE INTERMEDIATE CODE: A02

Effective date: 20070605