JP2006223976A - Method for fermentation of organic waste and product using it - Google Patents
Method for fermentation of organic waste and product using it Download PDFInfo
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- JP2006223976A JP2006223976A JP2005039983A JP2005039983A JP2006223976A JP 2006223976 A JP2006223976 A JP 2006223976A JP 2005039983 A JP2005039983 A JP 2005039983A JP 2005039983 A JP2005039983 A JP 2005039983A JP 2006223976 A JP2006223976 A JP 2006223976A
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/10—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
- Y02A40/20—Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/20—Sludge processing
Abstract
Description
本発明は、有機質汚泥等の有機性廃棄物の発酵処理方法、並びに前記処理方法で製出される固形資材及び液体資材に関するものである。 The present invention relates to a fermentation treatment method for organic waste such as organic sludge, and a solid material and a liquid material produced by the treatment method.
各種産業からの有機性廃棄物である汚泥等は、例えば食品有機質汚泥の水分が80%以上であるが、高タンパク質並びに炭水化物に富み、発酵処理により肥料とすると、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対して、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。 Sludge and the like, which are organic wastes from various industries, have a water content of food organic sludge of 80% or more, but are rich in high proteins and carbohydrates. If fertilizer is obtained by fermentation treatment, waste is effectively used. Therefore, for the high moisture content which is a factor inhibiting fermentation, in the fermentation treatment of organic waste, conventionally, moisture adjusting materials such as rice straw, rice husk and sawdust are added, and the total moisture content is 55% to It was reduced to 60% and fermented for composting.
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、発酵温度が低く、効率的な処理とはいえない。そこで先に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を提案した(特許文献1:特公平7−91140号、同7−112958号、同8−18892号)。 However, the fermentation treatment with the addition of the moisture adjusting material is basically anaerobic fermentation, the fermentation temperature is low, and cannot be said to be an efficient treatment. In view of this, as means for fermenting organic sludge, means for aerobic fermentation by mixing paper strips in a disturbed state have been proposed (Patent Document 1: Japanese Patent Publication Nos. 7-91140 and 7-112958, 8-18892).
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所謂横型パドル式発酵装置による発酵処理を行っていたもので、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。 The fermentation treatment adds about 5% weight ratio of paper slender cut to about 80-90% water-containing organic sludge, and secures a micro space in a disturbed state of the paper long cut, It expands the air contact area of sludge and enables aerobic fermentation. The specific means of fermentation is to perform a fermentation process using a so-called horizontal paddle fermenter in which a processing object stored in a pool-shaped open fermenter is supplied with air and stirred back with a stirring blade. However, depending on the difference in the object to be treated, it took 2-3 weeks to complete the fermentation.
また前記の細長裁断紙を使用して汚泥発酵処理は、食品産業廃棄汚泥にしばしば見受けられる高い脂質を含有している汚泥の場合には、発酵処理が比較的困難であった。なぜならば古紙混合によって汚泥中に送風空気の自由な流路ができることが高速発酵のための条件であるが、汚泥の脂質含量が高い場合には、導入した裁断古紙が脂肪分を吸収し互いに密着し、あたかも一層の膜を形成するようになり、自由な空気の流通を妨げ、発酵を著しく遅延させ、且つ一部は嫌気発酵となってしまう。また、古紙混合汚泥の水分含量が多い場合にも、同様なことが想定される。 In addition, the sludge fermentation treatment using the above-mentioned long cut paper is relatively difficult in the case of sludge containing high lipids often found in food industry waste sludge. This is because it is a condition for high-speed fermentation that a free air flow path can be created in the sludge by mixing waste paper, but when the sludge has a high lipid content, the introduced cut waste paper absorbs fat and adheres to each other. However, as if a single layer of film was formed, free air flow was hindered, fermentation was remarkably delayed, and partly anaerobic fermentation. The same is also assumed when the waste paper mixed sludge has a high water content.
また汚泥の脱水工程(ケーキ化)から発酵処理工程への移行に際して、前記した特許手法に採用されている紙の細裁断片を攪乱状態にして使用する手段では、紙攪乱体に汚泥を少しづつ加えながらの攪拌作業や、逆に攪拌している状態を継続している汚泥に、細裁断片の攪乱体を加える必要があり、発酵工程開始時の作業が非常に煩雑である。即ち単に紙の裁断片を脱水汚泥(汚泥ケーキ)に混入したとしても、紙片は直ぐに吸水状態となり、汚泥内での空気流通路を形成せずに、好気発酵とならない。更に紙の細長裁断片は、攪乱作業時や汚泥混入作業に際して、軽量のために直ぐに飛散し、種々機器への付着侵入等の問題があり、発酵自動化(水分調整剤投入、発酵装置への搬入)に際しての障害要因となるなどの課題を有していた。 In addition, when shifting from the sludge dehydration process (making cake) to the fermentation process, the paper shredded fragment used in the above-mentioned patent method is used in a disturbed state, and sludge is gradually added to the paper disturbing body. It is necessary to add a disturbing body of the shredded fragments to the agitating operation while adding or to the sludge that is continuously agitating, and the work at the start of the fermentation process is very complicated. That is, even if a piece of paper is simply mixed with dewatered sludge (sludge cake), the paper piece immediately becomes a water-absorbing state, does not form an air flow passage in the sludge, and does not undergo aerobic fermentation. In addition, paper strips are scattered quickly due to their light weight during disturbance work and sludge mixing work, causing problems such as adhesion and intrusion into various equipment. Fermentation automation (moisture adjustment agent input, transport to fermentation equipment) ) Had problems such as becoming an obstacle factor.
そこで紙製ペレット体を採用すると、汚泥への混入作業等の発酵自動化に対応でき、且つ水分調整も容易であると共に、高脂質含有汚泥に対しても効果的な発酵がなされ、且つ発酵効率も良いことを知見し、2〜5mm径・2〜10mm長の紙製ペレット体とした水分調整材を混合して水分調整を行い、前記混合物に所定の空気供給を行いながら好気発酵させて処理する手段を提案した(特許文献2:特開2002−263622号)。 Therefore, if paper pellets are used, it can be used for fermentation automation such as mixing into sludge, it is easy to adjust the water content, effective fermentation is also performed for high-fat sludge, and fermentation efficiency is also high. Knowing that it is good, adjust the moisture by mixing the moisture adjusting material in the form of paper pellets of 2-5mm diameter and 2-10mm length, and perform the aerobic fermentation while supplying predetermined air to the mixture The means to do was proposed (patent document 2: Unexamined-Japanese-Patent No. 2002-263622).
またパルプスラッジの処理手段として、特許文献3(特公昭57−35153号)に、パルプスラッジと余剰活性汚泥の混合発酵処理手段が開示されている。前記の処理は、パルプスラッジと余剰活性汚泥のC/N比が20〜45になるように(パルプスラッジの割合が85〜75%程度)に混合し、更に全体を水分75%以下に脱水したものを好気発酵させてなるものである。 As a pulp sludge treatment means, Patent Document 3 (Japanese Patent Publication No. 57-35153) discloses a mixed fermentation treatment means of pulp sludge and excess activated sludge. In the above treatment, the pulp sludge and surplus activated sludge are mixed so that the C / N ratio is 20 to 45 (the ratio of pulp sludge is about 85 to 75%), and the whole is dehydrated to 75% or less of moisture. It is made by aerobic fermentation of things.
近年古紙の需要が高まり、前記した細長裁断古紙を使用した有機質汚泥の発酵処理がコストの面で問題があり、また同様に紙製ペレット体を採用することも、紙製ペレット自体のコストを要することから、有機質汚泥の発酵処理における好気条件を確保する低コスト部材が求められている。 In recent years, the demand for waste paper has increased, and the fermentation treatment of organic sludge using the above-mentioned slender cut waste paper has a problem in terms of cost. Similarly, adopting a paper pellet body also requires the cost of the paper pellet itself Therefore, a low-cost member that ensures aerobic conditions in fermentation treatment of organic sludge is demanded.
特許文献3には、パルプスラッジの処理手段として、余剰活性汚泥の混合処理が開示されているが、パルプスラッジの処理を主目的とするものであり、処理対象の汚泥量が少なく、また比較的乾燥脱水が容易であるパルプスラッジによって混合物の全体の水分を75%以下とするものであり、単に混合比率を変化させたとしても、高水分含有(85%程度)の有機質汚泥の効率処理はなされない。
そこで本発明は、脱水パルプスラッジが高水分含有の有機質汚泥の好気条件を確保する部材となることを見出し、新規な有機質汚泥の処理手段を提案したものである。 Therefore, the present invention has found that dehydrated pulp sludge serves as a member that ensures aerobic conditions for organic sludge having a high water content, and proposes a novel means for treating organic sludge.
本発明に係る有機性廃棄物の発酵処理方法は、有機質汚泥の脱水ケーキや畜糞、生ゴミ等の有機性廃棄物に、脱水乾燥して水分10%程度とした製紙汚泥を適宜量混合撹拌し、前記混合物を、底方からの空気供給が可能で、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、容器底方からの大量の空気供給を行うと共に、容器上方から強制排気を行い、混合物を好気発酵させてなることを特徴とするものである。 In the organic waste fermentation treatment method according to the present invention, an appropriate amount of paper sludge dehydrated and dried to about 10% water is mixed and stirred in organic waste such as dehydrated cake of organic sludge, livestock dung, and garbage. The mixture is stored in a closed fermentation vessel that can be supplied with air from the bottom and has a predetermined heat insulation structure, and supplies a large amount of air from the bottom of the vessel and forcibly exhausts from above the vessel. And the mixture is aerobically fermented.
混合物を収納した密閉容器内への空気供給並びに強制排気を行うことによって、微小ファイバーを多量に含んでいる製紙汚泥における前記微小繊維の絡まりが、空気通路を構成すると共に、脱水ケーキの空気接触面積を増大させることになって、空気を汚泥全体に容易に散在させることになり、確実な好気発酵がなされる。 By supplying air into the sealed container containing the mixture and forcibly exhausting, the entanglement of the fine fibers in the papermaking sludge containing a large amount of fine fibers constitutes an air passage and the air contact area of the dewatered cake As a result, air is easily scattered throughout the sludge, and a reliable aerobic fermentation is performed.
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、特に微小繊維が、所定の形状に維持する作用をなして、例えばシート形状や杭形状など所望形状の肥料として使用したり、また種子や培土等を混入し、直接散布による種まきが可能となる。 Further, the fermented processed product using organic waste according to the present invention is characterized in that the fermented processed product produced by the fermentation method is formed by pressure molding and drying into a predetermined shape, In particular, the microfibers act to maintain a predetermined shape, and can be used as fertilizers having a desired shape such as a sheet shape or a pile shape, or seeds or cultivated soil can be mixed and seeded by direct spraying.
又本発明に係る液体資材は、前記の発酵処理方法において、密閉容器からの排気を結露させて製出したもので、分析によって充分な肥効成分を含有しており、液肥等として利用できる。 Further, the liquid material according to the present invention is produced by condensing exhaust from the closed container in the fermentation treatment method, and contains sufficient fertilizing components by analysis, and can be used as liquid fertilizer or the like.
以上のように本発明は、有機質汚泥のような高含水有機性廃棄物に、水分調整材として製紙汚泥の乾燥物を混合し、前記混合物を好気発酵させる有機性廃棄物の発酵処理方法であり、焼却処分される製紙汚泥を有効利用できると共に、前記の発酵方法で製出された発酵処理物は、所定の形状に加圧成形乾燥することで、所望形状のコンポストとして提供でき、また発酵時に生ずる水蒸気を結露させて得られる液状物は、液肥等として利用できるものである。 As described above, the present invention is a method for fermenting organic waste, in which a high water content organic waste such as organic sludge is mixed with a dried product of paper sludge as a moisture adjusting material, and the mixture is subjected to aerobic fermentation. Yes, the papermaking sludge to be incinerated can be used effectively, and the fermented product produced by the fermentation method can be provided as a compost of a desired shape by being pressure-molded and dried into a predetermined shape. The liquid material obtained by dew condensation of water vapor that is sometimes generated can be used as liquid fertilizer or the like.
次に本発明の発酵方法の実施形態について説明する。実施形態は、処理対象物を密閉容器に収納して実施するもので、発酵装置は、図1に例示するとおり、適宜な断熱構造(金属板製や薄い樹脂製ではない趣旨で、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)の密閉形式の発酵槽1と、発酵槽1内に配置する中蓋体2と、発酵槽1に被冠する密閉蓋体3を備えてなり、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4を設け、内底部4の下方空間に、送風ブロワー5を接続し、蓋体3に排気口並びに排気口に接続した排気ブロワー6を付設し、排気ブロワー6に冷却部(結露装置)7、気水分離部(結露水貯留槽)8、脱臭部9を順次設けてなるものである。
Next, an embodiment of the fermentation method of the present invention will be described. The embodiment is carried out by storing the object to be processed in a sealed container, and the fermentation apparatus has an appropriate heat insulating structure (not a metal plate or a thin resin, as illustrated in FIG. A closed
また本発明においては、製紙汚泥の乾燥装置を必要とする。乾燥装置は、一般の乾燥装置と同様で乾燥槽内の底方から熱風を供給するようにしたもので、脱水した製紙汚泥を乾燥槽内に収納し、水分を10%前後まで乾燥させて使用する。 In the present invention, a paper sludge drying apparatus is required. The drying device is similar to a general drying device, and is designed to supply hot air from the bottom of the drying tank. The dewatered paper sludge is stored in the drying tank and the moisture is dried to around 10%. To do.
前記発酵装置を使用して有機質汚泥(食品会社廃棄800kg含水率80%の食品汚泥と、800kg含水率80%の下水汚泥の各々)に、乾燥装置で水分10%前後まで乾燥させた製紙汚泥200kgを、幅1.2m、奥行き1.7m、高さ1.35mの1トン型の発酵容器1内に収納し、送風ブロワー5で、発酵槽1に毎分160Lの常温空気を送り込み、更に排気ブロワーを毎分200Lの定格出力をもって強制排気を行った。
200kg of paper sludge dried to about 10% of moisture with a drying device to organic sludge (each of food sludge with 800kg water content 80% water content and 800kg water content 80% sewage sludge) using the fermenter Is stored in a 1-
前記の給排気を連続し、混合汚泥の発酵状態を確認するために、発酵槽1の底面から15cm、45cm、75cmの位置に温度センサー10を配置し、その測定結果が図2,3の表の通りである。
In order to confirm the fermentation state of the mixed sludge by continuously supplying and exhausting the temperature, the
測定結果から食品汚泥処理の場合には、上方から発酵が進行して、底方部分のピークが8日目となり、10日以降から全体の温度が下降して、発酵が終了したことが確認できる。また下水汚泥の場合には、上下の発酵進行状態が相違するが、10日程度で発酵が終了する。 In the case of food sludge treatment, it can be confirmed from the measurement results that fermentation has progressed from above, the peak at the bottom part is on the eighth day, and the entire temperature has fallen from the 10th day onward, thus ending the fermentation. . In the case of sewage sludge, the upper and lower fermentation progress states are different, but the fermentation is completed in about 10 days.
なお中蓋体2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。
The
発酵終了物は、60〜70%の水分を含んでおり、これを更に乾燥機で20%前後まで乾燥させ、280kg/平方cmの圧力で造粒すると、固形肥料となる。この固形肥料を小松菜の栽培に使用したところ充分な肥料効果を確認できた。 The fermented product contains 60 to 70% of moisture, and when this is further dried to about 20% with a dryer and granulated at a pressure of 280 kg / square cm, it becomes solid fertilizer. When this solid fertilizer was used for cultivation of Japanese mustard spinach, a sufficient fertilizer effect could be confirmed.
勿論発酵終了物については、造粒するほか、板状固形肥料として使用したり、前記板状固形肥料の加圧成形に際して種子を混合して、種子含有の肥料板を形成したり、或いは棒状体肥料に形成し、圃場の栽培植物の周囲に差し込むことで、所望の施肥を可能としたりするものである。その他所望の使用形態に対応して種々の形状に形成するのが可能である。 Of course, the fermented product is granulated, used as a plate-shaped solid fertilizer, mixed with seeds during pressure molding of the plate-shaped solid fertilizer to form a seed-containing fertilizer plate, or a rod-shaped body By forming it into a fertilizer and inserting it around the cultivated plant in the field, a desired fertilization is possible. In addition, it is possible to form in various shapes corresponding to a desired usage pattern.
また発酵槽1からの排気は、冷却部(結露装置)7を通過させることで、発酵時の水蒸気を結露させ、気水分離部(結露水貯留槽)8において前記結露水を貯留する。この結露水は、図4に例示するとおり肥効成分を含んでおり、液肥としても使用できるものである。
The exhaust from the
1 発酵槽
2 中蓋体
3 密閉蓋体
4 内底部
5 送風ブロワー
6 排気ブロワー
7 冷却部(結露装置)
8 気水分離部(結露水貯留槽)
9 脱臭部
10 温度センサー
DESCRIPTION OF
8 Air / water separation unit (condensate storage tank)
9
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PCT/JP2006/302819 WO2006088124A1 (en) | 2005-02-17 | 2006-02-17 | 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 |
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Cited By (4)
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JP2010069477A (en) * | 2008-08-22 | 2010-04-02 | Chubu Shiryo Kk | Fermentation apparatus for food residue |
JP2010124743A (en) * | 2008-11-27 | 2010-06-10 | Niigata Univ | Seedling raising method via tree cutting or herbaceous cutting |
CN101961724A (en) * | 2009-07-24 | 2011-02-02 | 岩渊健一 | Fermentation treatment method and device of an organic waste |
CN114956496A (en) * | 2022-01-18 | 2022-08-30 | 天科院环境科技发展(天津)有限公司 | Oil silt bioremediation processing apparatus |
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JPS6256392A (en) * | 1985-09-04 | 1987-03-12 | 寿和工業株式会社 | Manufacture of manure |
JP2001181077A (en) * | 1999-12-27 | 2001-07-03 | Hidetaka Hori | Method for fermentative treatment of organic waste and product made by making use of the resultant fermentatively treated product |
JP2003246693A (en) * | 2002-02-22 | 2003-09-02 | Naoharu Yamazaki | Method of recovering liquid manure from organic waste and apparatus for recovering liquid manure |
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2005
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JPS6256392A (en) * | 1985-09-04 | 1987-03-12 | 寿和工業株式会社 | Manufacture of manure |
JP2001181077A (en) * | 1999-12-27 | 2001-07-03 | Hidetaka Hori | Method for fermentative treatment of organic waste and product made by making use of the resultant fermentatively treated product |
JP2003246693A (en) * | 2002-02-22 | 2003-09-02 | Naoharu Yamazaki | Method of recovering liquid manure from organic waste and apparatus for recovering liquid manure |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
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JP2010069477A (en) * | 2008-08-22 | 2010-04-02 | Chubu Shiryo Kk | Fermentation apparatus for food residue |
JP2010124743A (en) * | 2008-11-27 | 2010-06-10 | Niigata Univ | Seedling raising method via tree cutting or herbaceous cutting |
CN101961724A (en) * | 2009-07-24 | 2011-02-02 | 岩渊健一 | Fermentation treatment method and device of an organic waste |
CN114956496A (en) * | 2022-01-18 | 2022-08-30 | 天科院环境科技发展(天津)有限公司 | Oil silt bioremediation processing apparatus |
CN114956496B (en) * | 2022-01-18 | 2023-12-15 | 天科院环境科技发展(天津)有限公司 | Oil sludge bioremediation processing apparatus |
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