JP2001181077A - Method for fermentative treatment of organic waste and product made by making use of the resultant fermentatively treated product - Google Patents

Method for fermentative treatment of organic waste and product made by making use of the resultant fermentatively treated product

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Publication number
JP2001181077A
JP2001181077A JP36918299A JP36918299A JP2001181077A JP 2001181077 A JP2001181077 A JP 2001181077A JP 36918299 A JP36918299 A JP 36918299A JP 36918299 A JP36918299 A JP 36918299A JP 2001181077 A JP2001181077 A JP 2001181077A
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JP
Japan
Prior art keywords
fermentation
product
treated
organic waste
resultant
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.)
Granted
Application number
JP36918299A
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Japanese (ja)
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JP3499484B2 (en
Inventor
Hidetaka Hori
秀隆 堀
Kenichi Iwabuchi
健一 岩淵
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Individual
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Individual
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Priority to JP36918299A priority Critical patent/JP3499484B2/en
Priority to TW90102460A priority patent/TW548244B/en
Publication of JP2001181077A publication Critical patent/JP2001181077A/en
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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
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/20Sludge processing
    • 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

Landscapes

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

Abstract

PROBLEM TO BE SOLVED: To provide a method for the high-speed fermentative treatment of organic wastes including organic sludge, livestock dung and garbage, and to provide a means for utilizing the resultant fermentatively treated product. SOLUTION: This method for fermentative treatment of organic wastes comprises the following process: organic wastes are mixed with waste paper under agitation and a water content adjustment for the resultant mixture is performed, the mixture is then charged into a closed-type fermentation vessel (fermentation tank 1) equipped with an inner double-bottomed section 3 and a blower 4, and an aerobic fermentation is conducted while forcedly feeding the vessel with a large quantity of air for a specified period of time to bring the object to be treated to such a viscosity as to be pressure-moldable.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、有機質汚泥(食品産業
廃棄汚泥、屎尿汚泥、下水汚泥)、蓄糞、厨芥(生ゴ
ミ)等多量の水分を含んだ有機性廃棄物の高速処理手法
並びに再利用手段に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a high-speed processing method for organic waste containing a large amount of water, such as organic sludge (food industry waste sludge, human waste sludge, sewage sludge), feces storage, kitchen waste (garbage), and the like. It relates to the reuse means.

【0002】[0002]

【従来技術及び発明が解決しようとする課題】各種産業
からの有機性廃棄物である汚泥は、例えば食品有機質汚
泥のように水分が80%以上であるにもかかわらず、高
タンパク質並びに炭水化物に富み、発酵処理によって肥
料とすると、廃棄物の有効利用となる。そこで発酵の阻
害要因である高水分含有にたいして、有機性廃棄物の発
酵処理に際しては、従前より、稲わら、籾殻、オガコ等
の水分調整材を添加し、全体の水分含量を55%〜60
%に低下させて発酵させコンポスト化を図っていた。
BACKGROUND OF THE INVENTION Sludge, which is an organic waste from various industries, is rich in high protein and carbohydrates, even though it has a water content of more than 80%, such as organic sludge of food. If fertilizer is made by fermentation, waste can be effectively used. In view of the high water content, which is a factor inhibiting fermentation, in the fermentation treatment of organic waste, a water regulating material such as rice straw, rice husk, sawdust has been added, and the total water content has been reduced to 55% to 60%.
% And fermented to achieve composting.

【0003】しかし前記の水分調整材を添加しての発酵
処理は、基本的に嫌気的発酵で、発酵温度が低い。もと
もと木材、モミガラなどに含まれるリグニン、珪酸分を
含んだモミガラの木質部などは非常に難分解性のもの
で、而も嫌気的な発酵で且つ低温発酵であるため、全重
量の30%以上も大量に存在するこれら添加物を分解す
るには、12日程度の1次発酵に続き約2ヶ月ほどの2
次発酵が必要である。更に2次発酵を終了しても籾殻や
オガクズが完全に分解することはなく、生成した肥料に
は汚泥の固形分とこれら残存の水分調整剤が共存する。
有機質汚泥の80%は水分であり、発酵の過程で蒸発
し、肥料中の有機汚泥の固形分は最大20%を占めるに
すぎない。およそ30%の水分調整材が残れば有機質汚
泥の持つ高い窒素分、燐酸などの成分の含有率は非常に
少なくされることになる。
[0003] However, the fermentation treatment with the addition of the water conditioning material is basically an anaerobic fermentation, and the fermentation temperature is low. Originally, lignin contained in wood, peach and so on, and the woody part of peach containing silicic acid are very hard to decompose and are anaerobic fermentation and low-temperature fermentation. In order to decompose these additives present in large amounts, the primary fermentation for about 12 days followed by about 2 months for 2 days
Next fermentation is required. Further, even after the secondary fermentation is completed, the rice husks and sawdust do not completely decompose, and the solid content of sludge and the remaining moisture regulator coexist in the fertilizer produced.
Eighty percent of the organic sludge is water, which evaporates during the fermentation process, and only up to 20% solids of the organic sludge in the fertilizer. If about 30% of the water conditioning material remains, the content of components such as high nitrogen content and phosphoric acid of the organic sludge will be extremely reduced.

【0004】この様にコンポストの肥料性が低くされ、
しかも2ヶ月以上の二次発酵を必要とすることが、現在
の有機汚泥処理方法の最大の弱点である。このことが依
然として発生汚泥量のおよそ1%以下が処理されるに過
ぎない現状を生んでいる元凶である。
[0004] Thus, the fertilizer properties of compost are reduced,
Moreover, the need for secondary fermentation for two months or more is the greatest weakness of the current organic sludge treatment method. This is the cause of the current situation where only about 1% or less of the generated sludge is treated.

【0005】また高水分含有の有機質汚泥の発酵処理手
段として、紙の細長裁断体を攪乱状態で混合して好気発
酵させる手段が提案されている(特公平7−91140
号、同7−112958号、同8−18892号)。
As a means of fermenting organic sludge having a high water content, there has been proposed a means for aerobic fermentation by mixing slender pieces of paper in a disturbed state (Japanese Patent Publication No. 7-91140).
Nos. 7-112958 and 8-18892).

【0006】前記発酵処理は、80〜90%程度の水分
含有の有機質汚泥に対して、約5%重量比程度の紙の細
長裁断体を加え、紙の細長裁断体の攪乱状態での微小空
間確保によって、汚泥の空気接触面積を拡大し、好気発
酵可能としたものである。そして発酵の具体的手段は、
プール状のオープン発酵槽に収納した処理対象物に、空
気供給を行い乍ら、攪拌羽根による攪拌切り返しを行う
ようにしたもので、処理対象物の相違にもよるが、発酵
終了まで、2〜3週間を要した。
[0006] In the fermentation treatment, a slender paper body of about 5% by weight is added to an organic sludge containing about 80 to 90% of water, and the minute slender paper body is disturbed in a minute space. By securing, the air contact area of sludge is expanded, and aerobic fermentation is possible. And the specific means of fermentation is
The processing target stored in the pool-shaped open fermentation tank is subjected to stirring and switching by the stirring blade while supplying air. Depending on the difference in the processing target, the processing target is 2 to 2 times. It took three weeks.

【0007】そして前記発行終了物はコンポストとして
使用されるものであるが、発酵途中の切り返しによりセ
ルロースが細かく裁断されることになり、他のコンポス
ト同様に、粉末の散布用肥料としての使用手段しかな
い。
[0007] The end of issuance is used as compost, but cellulose is finely cut by cutting back during fermentation, and like other composts, only powder is used as a fertilizer for spraying. Absent.

【0008】そこで本発明は、コンポスト自体に所定の
成形性を備えさせることで、利用価値の高いコンポスト
を得ることができる発酵方法並びにその利用品自体を提
案したものである。
Therefore, the present invention proposes a fermentation method capable of obtaining a highly useful compost by providing the compost itself with a predetermined formability, and a product itself.

【0009】[0009]

【課題を解決する手段】本発明に係る有機性廃棄物の発
酵処理方法は、有機質汚泥、蓄糞、生ゴミ等の処理対象
物たる有機性廃棄物に古紙を混合撹拌して水分調整を行
い、底方からの空気供給可能で、且つ所定の断熱構造を
備えた密閉型発酵容器内に収納し、所定期間強制大量空
気供給を行い乍ら好気発酵を行い、処理対象物を加圧成
形可能な粘度にすることを特徴とするものである。
The method for fermenting organic waste according to the present invention comprises adjusting the water content by mixing and stirring used paper with organic waste to be treated, such as organic sludge, feces storage, garbage and the like. It is housed in a closed fermentation vessel that can supply air from the bottom and has a predetermined heat insulation structure, performs aerobic fermentation while supplying a large amount of forced air for a predetermined period, and press-molds the object to be treated. It is characterized by having a possible viscosity.

【0010】即ち好気発酵用の供給空気に見合う自然排
気のみがなされる発酵槽内で、好気発酵可能な量の空気
供給を行うと、発酵処理対象物(有機性廃棄物と古紙の
混合物)内の古紙は、水分蒸発を行うと共に、有機性廃
棄物からの水分吸収を行うので、水分の蒸発がなされる
と同時に有機性廃棄物の好気発酵がなされ、更にこの発
酵による温度上昇は、断熱容器内のために放熱が制限さ
れ、発酵熱が効果的に水分蒸発に使用される。従って切
り返しを行わなくとも発酵を継続でき、速やかに発酵を
終了させることができる。而も混合した古紙のセルロー
スは裁断されることがないので、紙粘土状となり加圧成
形可能となる。
That is, when air is supplied in an amount capable of aerobic fermentation in a fermenter in which only natural exhaustion is performed in accordance with the supply air for aerobic fermentation, the fermentation target (a mixture of organic waste and waste paper) The waste paper in the parentheses) evaporates water and absorbs water from organic waste, so that water is evaporated and aerobic fermentation of organic waste is performed at the same time. The heat radiation is limited because of the inside of the heat insulation container, and the fermentation heat is effectively used for water evaporation. Therefore, the fermentation can be continued without turning over, and the fermentation can be terminated quickly. Since the mixed waste cellulose is not cut, it becomes a paper clay and can be pressure-formed.

【0011】また本発明に係る有機性廃棄物の発酵処理
物利用品は、前記の発酵方法で製出された発酵処理物
を、所定の形状に加圧成形乾燥してなることを特徴とす
るもので単なる散布用肥料ではなく、シート形状や杭形
状の肥料として使用できるし、また容器形状としての使
用も可能であり、その利用範囲は広い。
[0011] The product utilizing the fermented organic waste product according to the present invention is obtained by subjecting the fermented product produced by the above fermentation method to pressure molding and drying into a predetermined shape. It can be used not only as a fertilizer for spraying but as a sheet-shaped or pile-shaped fertilizer, and can also be used as a container-shaped fertilizer.

【0012】[0012]

【発明の実施の形態】次に本発明の発酵方法の実施形態
について説明する。実施形態に示した発酵方法に使用す
る発酵装置は、図1に例示する通り、適宜な断熱構造
(金属板製や薄い樹脂製ではない趣旨。例えば木製やコ
ンクリート製のような、内部の熱が外気に放出され難い
構造であれば充分である趣旨)の発酵槽1に密閉蓋体2
を被冠してなり、発酵槽1の内部には、通気口を多数穿
設した二重底となる内底部3を設け、内底部3の下方空
間に、送風ブロワー4を接続し、蓋体2に排気口並びに
排気口に接続した排気ブロワー5を付設し、更に内底面
3上に攪拌機構6を設けたものである。尚内底面3上に
収納した発酵処理対象物(有機性廃棄物と古紙の混合物
処理対象物)Aに対しては、中蓋7を被冠する。
Next, an embodiment of the fermentation method of the present invention will be described. As shown in FIG. 1, the fermentation apparatus used in the fermentation method shown in the embodiment has an appropriate heat insulation structure (in the sense that it is not made of metal plate or thin resin. A fermenter 1 having a structure that is hardly released into the outside air is sufficient.
The inside of the fermenter 1 is provided with an inner bottom 3 serving as a double bottom with a large number of ventilation holes, and a blower 4 is connected to a space below the inner bottom 3 to form a lid. 2 is provided with an exhaust port and an exhaust blower 5 connected to the exhaust port, and further, a stirring mechanism 6 is provided on the inner bottom surface 3. In addition, the inner lid 7 is covered with the fermentation processing target (organic waste and waste paper mixture processing target) A stored on the inner bottom surface 3.

【0013】而して前記発酵装置を使用して、300〜
400kgの食品会社廃棄の含水率80%の汚泥に、重
量比5−10%の古紙を混合した処理対象物Aを発酵槽
1の内底面3上に収納し、毎分30〜40Lの空気(1
0℃の外気)をブロワー4から送り込み、更に毎分25
〜50Lの強制排気を行ったところ、3日後に対象物温
度は70℃に達しその後2日間高温が継続し、10日後
には発酵が終了したものと認められた(図2参照)。
Using the fermentation apparatus, 300 to
400 kg of sludge waste from a food company with a moisture content of 80% mixed with waste paper having a weight ratio of 5 to 10% is stored on the inner bottom surface 3 of the fermenter 1 and the air (30 to 40 L per minute) is stored. 1
0 ° C outside air) from the blower 4 and 25 min / min.
When forced exhaustion of 50 L was performed, it was recognized that the target temperature reached 70 ° C. three days later, the high temperature continued for two days, and the fermentation was completed ten days later (see FIG. 2).

【0014】更に前記の一次発酵物を5日間室温に放置
した後、送風排気を行ってて温度を観察した結果が図3
で、処理物温度は40℃にしか上昇しなかった。即ち二
次発酵処理を必要としないほど、一次発酵で充分な分解
処理がなされたと認められる。
Further, after the primary fermentation product was allowed to stand at room temperature for 5 days, air was exhausted and the temperature was observed.
Thus, the temperature of the processed product rose only to 40 ° C. That is, it is recognized that sufficient decomposition treatment was performed in the primary fermentation so that the secondary fermentation treatment was not required.

【0015】また汚泥の水分量が80%以上でも、5−
10%(重量比)の古紙を混合し含水量を75−80%
に低下した汚泥を、前記発酵槽1に投入して前記同一条
件で送風排気をおこなった場合に、処理対象物の温度
は、図4に示したとおりで、約10日後に50℃に達
し、約15日で一次発酵が終了した。このような高水分
含有状態でも発酵処理が可能であることが認められ
た。、
[0015] Even when the water content of the sludge is 80% or more, 5-
10% (weight ratio) waste paper is mixed and the water content is 75-80%
When the sludge which has been reduced to is fed into the fermenter 1 and blasted and exhausted under the same conditions, the temperature of the object to be treated reaches 50 ° C. after about 10 days as shown in FIG. The primary fermentation was completed in about 15 days. It was recognized that fermentation treatment was possible even in such a high water content state. ,

【0016】種々の試行錯誤の結果、送風排気の調整
で、48時間以内に70℃に上昇し、70℃を2日間以
上維持し、更に60℃以上を4日間維持すると、充分な
発酵がなされ、含水率が55%前後のコンポストが得ら
れることが確認された。従って従前の古紙混入発酵処理
手段に比較して、短期間による処理が可能となったもの
である。尚攪拌機構6は、処理対象物Aにおける通気箇
所の閉塞、通気箇所の固定化や偏在化等の通気障害対策
で、古紙のセルロースをバラバラに裁断しないように、
必要に応じてゆっくりとした攪拌を行うものである。ま
た中蓋7は、水分蒸発による処理対象物の減容に対し
て、処理対象物の保温効果と、処理対象物の減容によっ
て生ずる発酵槽1内部の上方空間における結露から処理
対象物を保護する効果を有する。
As a result of various trials and errors, if the temperature of the air is raised to 70 ° C. within 48 hours by adjusting the ventilation and exhaust air, and maintained at 70 ° C. for 2 days or more, and further maintained at 60 ° C. or more for 4 days, sufficient fermentation is performed. It was confirmed that compost having a water content of about 55% was obtained. Therefore, compared with the conventional waste paper mixed fermentation processing means, the processing can be performed in a shorter time. In addition, the stirring mechanism 6 is used to prevent the cellulose of the used paper from being cut apart in order to prevent the ventilation of the processing object A from blocking the ventilation part, fixing the ventilation part, or unevenly distributing the ventilation part.
Slow stirring is performed as needed. In addition, the inner lid 7 protects the processing target from the volume reduction of the processing target due to moisture evaporation and protects the processing target from dew condensation in the upper space inside the fermenter 1 caused by the reduction of the processing target. It has the effect of doing.

【0017】前記の発酵処理物(コンポスト)は、含水
率が55%前後であり、セルロースが細かく裁断されず
に、そのまま長繊維状態で存在し、且つ紙のような絡ま
った状態を維持しているので、そのまま押し固め、含水
率20%に乾燥した2×2×7cmの試験片を、RdD
社製RTC−1225AS型試験機で、引張試験を行っ
たところ、引張強さは117kg/平方cmであり、特
別なバインダーを必要とせずに充分な保形性を有するも
のである。即ち前記の有機性廃棄物の発酵処理方法を採
用することよって、任意の大きさの粒状体やそのほか所
望の形状のコンポストを得ることができ、その利用範囲
は広がるものである。
The above-mentioned fermented product (compost) has a water content of about 55%, cellulose is not finely cut, exists in a long fiber state as it is, and maintains a tangled state like paper. Therefore, a 2 × 2 × 7 cm test piece, which was compacted as it was and dried to a moisture content of 20%, was subjected to RdD
When a tensile test was carried out using an RTC-1225AS type tester manufactured by the company, the tensile strength was 117 kg / cm 2, and it had sufficient shape retention without requiring a special binder. That is, by adopting the above-mentioned organic waste fermentation treatment method, it is possible to obtain granules having an arbitrary size and compost having a desired shape, and the range of use thereof can be expanded.

【0018】そこで本発明は、更に前記発酵方法で製出
したコンポストを利用した物品を提案したもので、その
実施形態は、図5(第一実施例)に示すように、板状に
加圧成形し、含水率35〜40%程度まで乾燥させる
と、板状固形肥料10として使用できる。更に同図
(ロ)に示すように、前記板状固形肥料10の加圧成形
に際して、種子20を混合する、種子含有の肥料板が形
成され、そのまま圃場に埋設し灌水を施すと、コンポス
トは含水して肥効成分を流出させ、種子の発芽並びに繁
殖を無施肥で実現することができる。以下コンポスト利
用品は全て同様の効果を備える。
Therefore, the present invention further proposes an article utilizing the compost produced by the fermentation method. In the embodiment, as shown in FIG. When molded and dried to a moisture content of about 35 to 40%, it can be used as the plate-shaped solid fertilizer 10. Further, as shown in FIG. 2 (b), when the plate-shaped solid fertilizer 10 is press-formed, a seed-containing fertilizer plate for mixing the seeds 20 is formed. The fertilizer can be hydrated to allow the fertilizer to flow out, and germination and propagation of the seed can be realized without fertilization. Hereinafter, all the composting products have the same effect.

【0019】また板状とせずに、図6(イ)に示すよう
に棒状体肥料(第二実施例)11に形成しても良い。こ
の棒状体肥料11は、圃場30の栽培植物21の周囲に
差し込むことで、所望の施肥を行うことができる。
Instead of a plate-shaped material, a bar-shaped fertilizer (second embodiment) 11 may be formed as shown in FIG. By inserting the rod-shaped fertilizer 11 around the cultivated plant 21 in the field 30, desired fertilization can be performed.

【0020】また図7に示すように、多数の小凹部を備
えた苗床体(第三実施例)12に形成し、凹部内に培土
31と種子22を充填すると、コンポスト製品は苗床体
として使用することができる。特に発芽時には、発芽に
必要な培土31を備え、幼苗の圃場への植え替えに際し
ては、苗床体12と共に行うと、苗床体12自体が肥効
成分を備えているものであるから、植え替えと施肥が同
時に行われることになる。
Further, as shown in FIG. 7, when a seedbed body (third embodiment) 12 having a number of small recesses is formed and the soil is filled with seeds 31 and seeds 22, the compost product is used as a seedbed body. can do. In particular, at the time of germination, the cultivation soil 31 necessary for germination is provided, and when the seedlings are replanted in the field, when the seedlings 12 are used together with the nursery body 12, the nursery body 12 itself has a fertilizing component. Fertilization will be performed simultaneously.

【0021】更に図8は、散布体(第四実施例)13と
したもので、内部が空洞で、およそソフトボール大の球
状で、上部に適当な大きさの開口部131を持つ成型品
である。この散布体13は、内底部分に種子23と培土
32を充填し、特に充填物(種子23及び培土32)が
散布体13の内部で移動しない様な処置例えば押し固め
る等の処置を施しておく。そうすると、散布体13は、
起きあがり小法師的機能を備えることになるので、充填
状態のまま散布すると、開口部131が上方に向いて散
布されることになる。
FIG. 8 shows a dispersion body (fourth embodiment) 13 which is a molded product having a hollow inside, a spherical shape of about a softball size, and having an opening 131 of an appropriate size at the top. is there. The scattered body 13 is filled with seeds 23 and cultivated soil 32 in the inner bottom portion, and in particular, is subjected to a treatment such that the filler (seed 23 and cultivated soil 32) does not move inside the scattered body 13, for example, a treatment such as compacting. deep. Then, the spreading body 13
Since it has the function of getting up, it is sprayed in the filled state, so that the opening 131 is sprayed upward.

【0022】従って海岸の砂丘地33やその他広大な砂
漠地帯等では、前記充填物を有する散布体を広く散布
し、すぐに覆土34を施し、その後適宜な方法で灌水す
ることで内部の培土32が膨潤し、種子が発芽、幼苗2
4は無施肥で長時間生育できる。しかも散布体13の保
水力によって内部の水分の拡散を防ぎ、砂漠、砂丘地な
どの乾燥地帯での種子発芽に適したものである。
Therefore, in the sand dune area 33 and other large desert areas along the coast, the scattered body having the above-mentioned filling material is widely spread and immediately covered with soil 34 and then irrigated by an appropriate method, thereby cultivating the inner soil 32. Swells, seeds germinate, seedling 2
No. 4 can grow for a long time without fertilization. Moreover, the water retention of the spraying body 13 prevents the diffusion of water inside, and is suitable for seed germination in arid areas such as deserts and dunes.

【0023】また本発明の前記利用品は、製出したコン
ポストの肥料性が高く、かえって根傷害、窒素過多症等
を生じることもあるので、根傷害などを起こしやすい種
子を含んだ利用品を作製する場合は、セルロース性バイ
ンダー(たとえば粉砕オガコ、紛状古紙など)、無機物
性バインダー(シリカ、用土、バーミキュライト等)を
半量ほど加えたりし、その本来の肥料性を低くして用い
る。
Further, the above-mentioned use product of the present invention has high fertilizer properties of the produced compost, and may cause root damage, hypertrophy and the like. In the case of production, about half the amount of a cellulosic binder (for example, ground sawdust, powdery waste paper, etc.) and an inorganic binder (silica, soil, vermiculite, etc.) are added to reduce the original fertilizer properties.

【0024】[0024]

【発明の効果】以上のように本発明は、有機性廃棄物に
古紙を混合撹拌して水分調整を行い、底方からの空気供
給可能で、且つ所定の断熱構造を備えた密閉型発酵容器
内に収納し、所定期間強制大量空気供給を行い乍ら好気
発酵を行い、処理対象物を加圧成形可能な粘度にした有
機性廃棄物の発酵処理方法であり、また本発明は、前記
の発酵方法で製出された発酵処理物を、所定の形状に加
圧成形乾燥してなる有機性廃棄物の発酵処理物利用品
で、有機性廃物の発酵処理を短期間で実施でき、而も成
形可能なコンポストの提供並びに所定形状に形成したコ
ンポストの提供により、その利用範囲を広げることがで
きたものである。
As described above, the present invention relates to a closed fermentation vessel having a predetermined heat insulation structure, which is capable of adjusting the water content by mixing and stirring waste paper with organic waste, allowing air to be supplied from the bottom. The method is a method for fermenting an organic waste in which an aerobic fermentation is performed while a forced mass air supply is performed for a predetermined period, and the object to be treated is made into a viscosity that can be molded under pressure. The fermented product produced by the fermentation method of the above is a product utilizing an organic waste fermented product obtained by pressing and drying into a predetermined shape, and the fermentation treatment of the organic waste can be carried out in a short time. Also, by providing compost that can be molded and compost formed in a predetermined shape, the range of use can be expanded.

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

【図1】本発明方法に使用される発酵装置の説明図。FIG. 1 is an explanatory view of a fermentation apparatus used in the method of the present invention.

【図2】同装置による発酵処理の経過日−処理物温度の
グラフ(含水率80%汚泥)。
FIG. 2 is a graph of elapsed time of fermentation treatment by the same device-temperature of treated material (water content: 80% sludge).

【図3】同装置による発酵処理の経過日−処理物温度の
グラフ(二次発酵確認)。
FIG. 3 is a graph of elapsed time of fermentation treatment by the same apparatus-temperature of treated material (confirmation of secondary fermentation).

【図4】同装置による発酵処理の経過日−処理物温度の
グラフ(高含水率汚泥)
FIG. 4 is a graph of elapsed time of fermentation treatment by the same device-treated material temperature (high water content sludge).

【図5】本発明利用品の第一実施例の説明図で、(イ)
は板状固形肥料、(ロ)は種子含有板状固形肥料を示
す。
FIG. 5 is an explanatory view of a first embodiment of a product used in the present invention;
Indicates a plate-shaped solid fertilizer, and (b) indicates a seed-containing plate-shaped solid fertilizer.

【図6】同第二実施例の説明図で、(イ)は棒状肥料の
全体図、(ロ)は同使用状態を示す。
FIG. 6 is an explanatory view of the second embodiment, in which (a) shows an overall view of the bar-shaped fertilizer, and (b) shows the same use state.

【図7】同第三実施例の説明図で、(イ)は苗床体の斜
視図、(ロ)は同使用状態の一部断面図。
FIG. 7 is an explanatory view of the third embodiment, in which (a) is a perspective view of a nursery, and (b) is a partial cross-sectional view of the same use state.

【図8】同第四実施例の説明図で、(イ)は散布体の全
体図、(ロ)は同使用状態の断面図、(ハ)は同散布状
態の説明図。
8A and 8B are explanatory diagrams of the fourth embodiment, wherein FIG. 8A is an overall view of a spraying body, FIG. 8B is a sectional view of the same use state, and FIG.

【符号の説明】[Explanation of symbols]

1 発酵槽 2 密閉蓋体 3 内底部 4 送風ブロワー 5 排気ブロワー 6 攪拌機構 7 中蓋 10 板状固形肥料 11 棒状肥料 12 苗床体 13 散布体 20,22,23 種子 21 栽培植物 24 幼苗 30 圃場 31,32 培土 33 砂丘地 34 覆土 DESCRIPTION OF SYMBOLS 1 Fermenter 2 Closed lid 3 Inner bottom part 4 Blower blower 5 Exhaust blower 6 Stirring mechanism 7 Middle lid 10 Plate-shaped solid fertilizer 11 Rod-shaped fertilizer 12 Nursery bed 13 Scattered body 20, 22, 23 Seeds 21 Cultivated plant 24 Seedling 30 Field 31 , 32 Cultivation 33 Sand dune 34 Cover soil

フロントページの続き Fターム(参考) 4D004 AA02 AA12 BA04 CA04 CA14 CA19 CA42 CC02 DA02 DA09 4D059 AA01 AA02 AA03 AA07 BA03 BA45 BD01 CA08 CC01 4H061 AA01 AA02 CC36 CC51 CC55 DD20 EE42 EE61 FF06 GG15 GG19 GG25 GG49 KK09 Continued on front page F-term (reference) 4D004 AA02 AA12 BA04 CA04 CA14 CA19 CA42 CC02 DA02 DA09 4D059 AA01 AA02 AA03 AA07 BA03 BA45 BD01 CA08 CC01 4H061 AA01 AA02 CC36 CC51 CC55 DD20 EE42 EE61 FF06 GG15 GG19 GG19 GG25

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 有機質汚泥、蓄糞、生ゴミ等の処理対象
物たる有機性廃棄物に古紙を混合撹拌して水分調整を行
い、底方からの空気供給可能で、且つ所定の断熱構造を
備えた密閉型発酵容器内に収納し、所定期間強制大量空
気供給を行い乍ら好気発酵を行い、処理対象物を加圧成
形可能な粘度にすることを特徴とする有機性廃棄物の発
酵処理方法。
An organic waste, which is an object to be treated such as organic sludge, feces storage, garbage, etc., is mixed with a used paper to stir to adjust the water content, air can be supplied from the bottom, and a predetermined heat insulating structure is provided. Fermentation of organic waste, which is housed in a closed fermentation vessel equipped with it and aerobic fermentation is performed while supplying a large amount of forced air for a predetermined period of time, so that the object to be treated has a viscosity that enables pressure molding. Processing method.
【請求項2】 容器内に収納した処理対象物に断熱用被
覆体を被せ、処理対象物の発酵時の減容に対応して処理
対象物を断熱被覆可能とした中蓋を使用した請求項1記
載の有機性廃棄物の発酵処理方法。
2. A method according to claim 1, wherein the object to be treated housed in the container is covered with a heat insulating covering, and an inner lid is used which allows the object to be treated to be covered with heat in response to the volume reduction during fermentation of the object to be treated. The method for fermenting organic waste according to claim 1.
【請求項3】 請求項1又は2記載の発酵方法で製出さ
れた発酵処理物を、所定の形状に加圧成形乾燥してなる
ことを特徴とする発酵処理物利用品。
3. A product utilizing a fermentation product obtained by subjecting the fermentation product produced by the fermentation method according to claim 1 or 2 to pressure molding and drying into a predetermined shape.
【請求項4】 請求項1又は2記載の発酵方法で製出さ
れた発酵処理物に、粉砕、微細化した紙類、木材、無機
物等を加え、肥料成分の含有比率を少なくして加圧成形
乾燥してなることを特徴とする発酵処理物利用品。
4. A fermented product produced by the fermentation method according to claim 1 or 2 is added with pulverized and finely divided papers, wood, inorganic substances, and the like to reduce the content of fertilizer components and pressurize. A product utilizing a fermented product, which is formed and dried.
【請求項5】 容器形状に加圧成形乾燥した請求項3又
は4記載の利用品内に、培土と種子を充填してなること
を特徴とする発酵処理物利用品。
5. A product using a fermentation product, wherein the product is filled with cultivated soil and seeds in the product according to claim 3 which has been formed into a container by press forming and drying.
JP36918299A 1999-12-27 1999-12-27 Fermentation treatment method for organic waste and product using the fermentation treatment Expired - Fee Related JP3499484B2 (en)

Priority Applications (2)

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JP36918299A JP3499484B2 (en) 1999-12-27 1999-12-27 Fermentation treatment method for organic waste and product using the fermentation treatment
TW90102460A TW548244B (en) 1999-12-27 2001-02-06 Novel methods for composting of organic wastes and various usages of the compost resulted

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP36918299A JP3499484B2 (en) 1999-12-27 1999-12-27 Fermentation treatment method for organic waste and product using the fermentation treatment

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WO2006088124A1 (en) * 2005-02-17 2006-08-24 Kenichi Iwabuchi Method of treating paper industry sludge by fermentation, article comprising product of the fermentation treatment, method of treating organic waste by fermentation, and article comprising the product
JP2006223976A (en) * 2005-02-17 2006-08-31 Kenichi Iwabuchi Method for fermentation of organic waste and product using it
JP2006223977A (en) * 2005-02-17 2006-08-31 Kenichi Iwabuchi Method for fermenting paper sludge and fermented paper sludge-utilized article
JP2010124743A (en) * 2008-11-27 2010-06-10 Niigata Univ Seedling raising method via tree cutting or herbaceous cutting
JP2010124744A (en) * 2008-11-27 2010-06-10 Niigata Univ Biodegradable seedling-raising pot and seedling raising method
JP2020183328A (en) * 2019-05-07 2020-11-12 株式会社和田牧場 Block compost production method and block compost
CN112273190A (en) * 2020-07-29 2021-01-29 北京林业大学 Device for resource utilization of urban garden waste and urban sludge

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012139108A (en) * 2010-12-28 2012-07-26 Hanagokoro:Kk Culture soil

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006088124A1 (en) * 2005-02-17 2006-08-24 Kenichi Iwabuchi Method of treating paper industry sludge by fermentation, article comprising product of the fermentation treatment, method of treating organic waste by fermentation, and article comprising the product
JP2006223976A (en) * 2005-02-17 2006-08-31 Kenichi Iwabuchi Method for fermentation of organic waste and product using it
JP2006223977A (en) * 2005-02-17 2006-08-31 Kenichi Iwabuchi Method for fermenting paper sludge and fermented paper sludge-utilized article
JP2010124743A (en) * 2008-11-27 2010-06-10 Niigata Univ Seedling raising method via tree cutting or herbaceous cutting
JP2010124744A (en) * 2008-11-27 2010-06-10 Niigata Univ Biodegradable seedling-raising pot and seedling raising method
JP2020183328A (en) * 2019-05-07 2020-11-12 株式会社和田牧場 Block compost production method and block compost
JP7309145B2 (en) 2019-05-07 2023-07-18 株式会社和田牧場 Method for producing block compost and block compost
CN112273190A (en) * 2020-07-29 2021-01-29 北京林业大学 Device for resource utilization of urban garden waste and urban sludge

Also Published As

Publication number Publication date
JP3499484B2 (en) 2004-02-23
TW548244B (en) 2003-08-21

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