JP2008284417A - Organic waste treating agent and method for manufacturing the same - Google Patents

Organic waste treating agent and method for manufacturing the same Download PDF

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JP2008284417A
JP2008284417A JP2007129059A JP2007129059A JP2008284417A JP 2008284417 A JP2008284417 A JP 2008284417A JP 2007129059 A JP2007129059 A JP 2007129059A JP 2007129059 A JP2007129059 A JP 2007129059A JP 2008284417 A JP2008284417 A JP 2008284417A
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organic
organic waste
treatment agent
pieces
waste treatment
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Hodo Yakushiji
芳堂 薬師寺
Kuniyasu Numazawa
邦晏 沼澤
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BIOSELENT CO Ltd
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BIOSELENT CO Ltd
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/78Recycling of wood or furniture waste

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

Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for manufacturing an organic waste treating agent which produces better economical effects such as reduction in production costs and an improvement in productivity, as compared with the conventional ones, by eliminating the humidity control process and the process of immersing in an enzyme aqueous solution after pH adjustment, and which increases decomposition capability of the organic waste, and to provide an organic waste treating agent in which breeding and cultivation of microbial decomposition bacteria are accelerated and in which the decomposition capability is drastically improved since activation of the microbial decomposition bacteria is enhanced by immersing the compound pieces in an organic acid solution. <P>SOLUTION: The method possesses the process of processing organic raw chips by cutting wood chips to a predetermined length so that a sufficient strength and a shape holding property are obtained, the process of achieving a predetermined carbonization ratio by heating the organic row chips processed in the above process and by burning under predetermined conditions after sufficient drying, the process of adjusting pH of the compound chips treated in the above process with an organic acid, and the process of carrying the microbial decomposition bacteria on the compound chips treated in the above process. <P>COPYRIGHT: (C)2009,JPO&INPIT

Description

本発明は、有機廃棄物処理剤及び有機廃棄物処理剤の製造方法に関し、特に有機質としての保水性と揮発性及び強度と保形性等を有し、微生物分解菌の担体及び繁殖媒体として、有機廃棄物を分解化する有機廃棄物処理剤及び有機廃棄物処理剤の製造方法に関すものである。   The present invention relates to an organic waste treatment agent and a method for producing an organic waste treatment agent, and in particular, has water retention, volatility, strength, shape retention and the like as organic matter. The present invention relates to an organic waste treatment agent for decomposing organic waste and a method for producing the organic waste treatment agent.

一般に糞尿は、下水道がない地域では、バキューム車で回収して、処理施設に運搬して処理する。この場合、糞尿の水分は、凝集沈殿・濾過・活性炭処理・脱窒素処理等が行われた後に、河川等に放流される。
このため、糞尿の水分の処理には、大規模なプラントを設置するのに多くの費用を必要とすると共に、処理を行うための人件費等が負担となる。また、蓄糞尿は、堆肥に加工する場合には、厩舎の周囲に悪臭が発生し、井戸水・地下水等の汚染が問題になる。
In general, manure is collected in a vacuum car in an area where there is no sewerage system, transported to a processing facility, and processed. In this case, the water of manure is discharged into rivers and the like after being subjected to coagulation sedimentation, filtration, activated carbon treatment, denitrification treatment, and the like.
For this reason, the treatment of the water of manure requires a large amount of cost for installing a large-scale plant, and a labor cost for performing the treatment becomes a burden. In addition, when manure is processed into compost, a bad odor is generated around the stable and contamination of well water and groundwater becomes a problem.

また、一般家庭・食品加工業等から排出する生ごみ等の有機廃棄物は、地上に投棄すると、悪臭・腐敗等の原因となるので、衛生上・環境上等の社会問題が発生した。このため、乾燥装置等で乾燥した肥料に加工したり、海上に投棄する方法等が採用されていた。しかし、肥料として利用量には限度があり、また、海洋投棄には、環境汚染・費用等に問題がある。
さらに、一般家庭・食品加工業等から排出する生ごみ等の有機廃棄物を焼却炉で処理した場合には、有害物質及び悪臭の発生で環境汚染の社会問題がなる。
In addition, organic waste such as food waste discharged from general households and food processing industries, when dumped on the ground, causes bad odors and decay, resulting in social problems such as hygiene and environment. For this reason, the method etc. which were processed into the fertilizer dried with the drying apparatus etc. or dumped on the sea were employ | adopted. However, the amount of fertilizer used is limited, and ocean dumping has problems with environmental pollution and costs.
Furthermore, when organic waste such as garbage discharged from general households and food processing industries is treated in an incinerator, the generation of harmful substances and foul odors causes a social problem of environmental pollution.

特許文献1は、本願の発明者等が開発した技術であり、この特許文献1の製造方法においては、第3工程において湿度調整をし、さらに、第6工程において酵素水溶液浸漬処理を行っていた。また、炭化率が40%〜60%の技術が開示されている。
また、特許文献2及び特許文献3においては、おが粉及び木材チップ等を使用すること等が提案されている。
特開2001−179226号公報 特開平8−1133号公報 特開平8−168744号公報
Patent Document 1 is a technique developed by the inventors of the present application. In the manufacturing method of Patent Document 1, humidity adjustment is performed in the third step, and further, an enzyme aqueous solution immersion treatment is performed in the sixth step. . Moreover, the technique whose carbonization rate is 40%-60% is disclosed.
Moreover, in patent document 2 and patent document 3, it is proposed to use sawdust and wood chips.
JP 2001-179226 A JP-A-8-1133 JP-A-8-168744

しかしながら、特許文献1に開示されている製造方法においては、第3工程の帯電処理条件として、電圧200V・電流50A〜100Aで12時間も通電するので、電気料金等のランニングコスト等の加算で生産コストが上昇する割合には、消臭等の効果が難しかった。
また、第6工程において高価なヨモギ科植物・笹の葉から抽出した酵素等で酵素水溶液浸漬処理をしていたが、生産コストが上昇する割合には、微生物分解菌だけの活動を活発化させる効果が難しかった。
さらに、炭化率が40%〜60%のため保形及び保水が低下して、有機廃棄物の分解率を向上させることが出来なかった。
さらにまた、特許文献2及び特許文献3に開示されている、おが粉は、生ごみ等の水分を吸収するため固結物を形成するので、表面積の減少により空隙も減少する。このため、生ごみの分解に有効な好気性微生物の繁殖が抑制されるので、微生物により分解能力が低下し、生ごみを効率的に分解が出来ない等、の問題がある。
However, in the manufacturing method disclosed in Patent Document 1, the charging process conditions in the third step are energized for 12 hours at a voltage of 200 V and a current of 50 A to 100 A. Effects such as deodorization were difficult at the rate of cost increase.
In addition, in the sixth step, the enzyme aqueous solution was immersed in an enzyme extracted from an expensive Artemisia plant / bamboo leaf, etc., but the activity of only microbial-degrading bacteria was activated to increase the production cost. The effect was difficult.
Furthermore, since the carbonization rate is 40% to 60%, the shape retention and water retention decreased, and the decomposition rate of organic waste could not be improved.
Furthermore, since the sawdust disclosed in Patent Document 2 and Patent Document 3 absorbs moisture such as food waste, it forms a consolidated product, and therefore the voids are reduced due to the reduction in surface area. For this reason, since the propagation of aerobic microorganisms effective for the decomposition of garbage is suppressed, there is a problem that the decomposition ability is lowered by the microorganisms and the garbage cannot be decomposed efficiently.

そこで本発明は、上記特許文献1に開示されている第3工程である湿度調整の処理工程及び第6工程における酵素水溶液浸漬処理工程を削除することにより、生産コストの低減及び製造時間の減少等により生産性の向上等による経済的効果を図ると共に、有機廃棄物の分解能力の向上を図ることを目的とする。   Therefore, the present invention eliminates the humidity adjustment treatment process and the enzyme aqueous solution immersion treatment process in the sixth process, which are the third processes disclosed in Patent Document 1, thereby reducing production costs and production time. The purpose of this is to improve the productivity of organic waste and to improve economic efficiency by improving productivity.

上記の目的を達成するために、本発明に係わる有機廃棄物の処理剤は、有機廃棄物を分解する微生物分解菌の担体と繁殖媒体としての機能を有し、木質細片・セプター細片・竹細片・籾殻を加熱して使用し、加熱により硬度を向上させる材料を含浸した有機物原料片を、非酸化雰囲気下で加熱して有機酸と無機酸が混在した多孔質の複合片とし、有機質としての保水性と水分の揮発性及び無機性としての強度と保形性の機能を有することを特徴とする。   In order to achieve the above object, the organic waste treating agent according to the present invention has a function as a carrier and a propagation medium for microbial degrading bacteria that decompose organic waste, and has a function as a wood strip, a scepter strip, Bamboo strips and rice husks are heated and used, and the organic material pieces impregnated with a material that improves the hardness by heating are heated in a non-oxidizing atmosphere to form a porous composite piece in which organic and inorganic acids are mixed, It is characterized by having functions of water retention as organic matter, water volatility, and inorganic strength and shape retention.

さらに、上記本発明の有機廃棄物処理剤の製造方法は、有機廃棄物を分解する微生物分解菌の担体と繁殖媒体として機能する有機廃棄物処理剤の製造方法において、木質細片・セプター細片・竹細片・籾殻等を十分な強度及び保形性が得られるように所定の長さに裁断して有機物原料片を加工する工程と、この工程で加工された有機物原料を十分に乾燥後に加熱し所定の条件で焼成して所定の炭化率になるようにする工程と、この工程によって処理された複合片を有機酸によりpH調整する工程と、この工程によって処理された複合片に微生物分解菌を担持する工程とを有していることを特徴とする。   Furthermore, the method for producing an organic waste treatment agent of the present invention includes a method for producing an organic waste treatment agent that functions as a carrier and a propagation medium for microbial degrading bacteria that decompose organic waste.・ Processing organic raw material pieces by cutting bamboo strips, rice husks, etc. to a predetermined length so that sufficient strength and shape retention can be obtained, and after sufficiently drying the organic raw materials processed in this step A step of heating and firing under a predetermined condition so as to obtain a predetermined carbonization rate, a step of adjusting the pH of the composite piece treated by this step with an organic acid, and a microbial decomposition into the composite piece treated by this step And a step of supporting bacteria.

上述したように本発明の有機廃棄物処理剤の製造方法は、従来に比較して、湿度調整処理の工程及びpH調整後の酵素水溶液浸漬処理の工程を削除することで、生産コストの低減及び製造時間の減少等により生産性が向上するので、顕著な経済的効果を有する。   As described above, the method for producing an organic waste treatment agent of the present invention reduces the production cost and reduces the humidity adjustment treatment step and the enzyme aqueous solution immersion treatment step after pH adjustment, as compared with the conventional method. Since the productivity is improved by reducing the manufacturing time or the like, it has a remarkable economic effect.

さらに、本発明の有機廃棄物処理剤は、木質細片等を加熱により硬度の強化の向上を図ると共に、表面の一部を炭化することで、有機質と非酸化雰囲気の処理をした物質の混合体で構成することにより、木質細片の強度を向上させて腐食の防止を図ると共に、ポーラス(多孔質)の増加することにより、微生物が生息することが出来る環境の整備の向上を図ることが出来るので、有機廃棄物の分解能力が顕著に向上する。   Furthermore, the organic waste treatment agent of the present invention is a mixture of organic matter and a non-oxidizing atmosphere treated by carbonization of a part of the surface while improving the hardness by heating wood chips and the like. By constructing with the body, it is possible to improve the strength of the wood pieces to prevent corrosion, and to improve the environment where microorganisms can inhabit by increasing the porosity. As a result, the ability to decompose organic waste is significantly improved.

さらに、本発明の有機廃棄物処理剤は、木質細片等を加熱により硬度を向上させて、非酸化雰囲気で加熱して有機質と、非酸化雰囲気の処理をした物質が混在したポーラス(多孔質)の複合片を構成するので、有機質としての保水性と水分の揮発性、及び強度と保形性の各機能を有し、使用時における耐磨耗性の向上及び劣化を抑制することにより、微生物分解菌に対する担持力の向上及び有機廃棄物の分解能力を向上等、を図ることにより長期間にわたり有効に使用することが出来る。   Furthermore, the organic waste treatment agent of the present invention is a porous (porous material) in which wood chips and the like are heated to improve hardness and heated in a non-oxidizing atmosphere to mix organic and non-oxidizing atmosphere-treated substances. )), It has functions of water retention and moisture volatility as organic matter, strength and shape retention, and suppresses improvement and deterioration of wear resistance during use. It can be used effectively over a long period of time by improving the supporting ability against microbial degrading bacteria and improving the decomposing ability of organic waste.

さらにまた、本発明の有機廃棄物処理剤は、複合片を、有機酸溶液に浸漬して微生物分解菌の活動の活発化を向上させるので、微生物分解菌の繁殖培養が促進され、有機廃棄物の分解能力が顕著に向上する。   Furthermore, since the organic waste treatment agent of the present invention improves the activation of the activity of the microbial degrading bacteria by immersing the composite piece in the organic acid solution, the propagation culture of the microbial degrading bacteria is promoted, and the organic waste The decomposition ability of is significantly improved.

以下、本発明の実施の形態を説明する。   Embodiments of the present invention will be described below.

(第1実施例)
有機廃棄物処理剤の製造方法は、水溶性の樹液成分を除去した有機物原料片を、加熱により硬度を強化させる工程と、この工程によって処理された含浸後の有機物原料片を非酸化雰囲気下で加熱して、有機質と非酸化雰囲気で処理した物質が混在した複合片に転換させ所定の炭化率に処理する工程と、この工程によって処理された複合片を有機酸によりpH調整する工程と、この工程によって処理されたpH調整の複合片に微生物分解菌を担持する工程を有し、微生物分解菌の繁殖媒体として機能を有する有機廃棄物処理剤を製造する。
(First embodiment)
The method for producing an organic waste treatment agent comprises a step of strengthening hardness by heating an organic raw material piece from which water-soluble sap components have been removed, and an impregnated organic raw material piece treated by this step in a non-oxidizing atmosphere. A step of heating and converting to a composite piece in which a substance treated in an organic and non-oxidizing atmosphere is mixed and processing to a predetermined carbonization rate, a step of adjusting the pH of the composite piece processed by this step with an organic acid, An organic waste treatment agent having a step of supporting microbial degrading bacteria on the pH-adjusted composite piece treated by the process and having a function as a propagation medium of microbial degrading bacteria is produced.

上記の各工程を詳細に説明する。
(第1工程)
有機物原料片に樹木等の木質細片等を使用するのは、各種の処理において、所定の強度及び保水性が要求されてからで、特に樹木及び竹等が好適である。この樹木の種類としては、針葉樹・広葉樹・落葉樹・常緑樹等があり、特に針葉樹が好適である。
有機物原料片を加工して、微生物分解菌の担持又は繁殖体としての機能を有する有機廃棄物処理剤を製造すれば、強度及び保水性に優れた有機廃棄物処理剤が得られる。
Each of the above steps will be described in detail.
(First step)
The reason why the fine pieces of wood such as trees are used as the organic raw material pieces is that a predetermined strength and water retention are required in various treatments, and in particular, trees and bamboo are suitable. The types of trees include conifers, broadleaf trees, deciduous trees, evergreen trees, and coniferous trees are particularly suitable.
An organic waste treatment agent having excellent strength and water retention can be obtained by processing an organic raw material piece to produce an organic waste treatment agent having a function of supporting or propagating microorganisms.

有機物原料片の形状としては、木質細片・セプター細片・竹細片等の細片状にする。この場合、細片状に加工出来ること及び細片状としてもある程度の強度と保水性が要求されるので、表皮を除いた樹木の外径が約7cm以上の大きさが好適であり、竹の場合は、外径が5cm以上の大きさが好適である。このため、古損木・間引きされた植林等も使用することが出来る。
有機物原料片として使用される細片の長さは、1cm〜4cmが好適であるが、十分な強度及び保形性があれば、0.3cm〜3cmのおが屑も使用することが出来る。また、籾殻は、強度及び保形性が優れていると共に、細片化する手間が省略することが出来るので、有機物原料として利用することが出来る。さらに、使用する有機物原料片は、種々の材質からの木質細片・セプター細片・竹細片・籾殻等のいずれか1種類を選択して使用してもよく、また、いずれか2種類以上を組合わせて使用することも出来る。
The shape of the organic material raw material piece is a thin piece such as a woody piece, a scepter piece, or a bamboo piece. In this case, since it can be processed into a strip shape and a certain amount of strength and water retention is required even as a strip shape, the outer diameter of the tree excluding the epidermis is preferably about 7 cm or more. In this case, the outer diameter is preferably 5 cm or more. For this reason, old damaged trees and thinned tree plantations can also be used.
The length of the strip used as the organic material piece is preferably 1 cm to 4 cm, but 0.3 cm to 3 cm sawdust can also be used if it has sufficient strength and shape retention. In addition, rice husks are excellent in strength and shape retention, and can be used as an organic material since the labor of fragmentation can be omitted. Furthermore, the organic material pieces to be used may be selected and used from various materials such as wood strips, scepter strips, bamboo strips, rice husks, etc., or any two or more types Can also be used in combination.

(第2工程)
十分に乾燥された有機物原料片を、ドラム式回転加熱炉に投入して蓋を密閉して、ガスバーナを点火して、ガスバーナに送る空気量調整と、ドラム式回転加熱炉のダンパ開閉度とを調整して加熱を開始する。この場合、ドラム式回転加熱炉内は、当初は空気が存在しているため、酸素雰囲気であるが、加熱が進むにつれて酸素が消費されるので、非酸化雰囲気に変化する。また、ダンパの開閉度の調整で、煙を大気中に放出させながら、ドラム式回転加熱炉内の圧力を、大気中の圧力より常に高く設定しておくと、加熱炉への空気の進入を防止するので、非酸化雰囲気を保持することが出来る。
このようにして、非酸化雰囲気を保持して、ドラム式回転加熱炉を、非雰囲気温度で100℃〜1000℃で加熱して、30分〜10時間で焼成する。
(Second step)
Thoroughly dry organic raw material pieces are put into a drum type rotary heating furnace, the lid is sealed, the gas burner is ignited, the amount of air sent to the gas burner is adjusted, and the damper open / close degree of the drum type rotary heating furnace is adjusted. Adjust and start heating. In this case, since the air is initially present in the drum type rotary heating furnace, the atmosphere is an oxygen atmosphere. However, since oxygen is consumed as heating proceeds, the atmosphere changes to a non-oxidizing atmosphere. Also, if the pressure in the drum-type rotary heating furnace is always set higher than the pressure in the atmosphere while adjusting the degree of opening and closing of the damper to release smoke into the atmosphere, air will enter the heating furnace. Therefore, a non-oxidizing atmosphere can be maintained.
In this way, the non-oxidizing atmosphere is maintained, and the drum-type rotary heating furnace is heated at 100 to 1000 ° C. at a non-atmospheric temperature and fired in 30 minutes to 10 hours.

非酸化雰囲気での焼成条件(温度・時間)は、有機物原料片の材質・形状等により変化するが、温度100℃〜600℃及び30分〜10時間の焼成で、有機物原料片は、その表層部分が炭化して、内部に入るにつれて有機質部分の含有量が増加すると、有機質と非酸化雰囲気で処理された物質が混在した複合片に転換する。
有機質原料片を、完全炭化(炭化率100%)させると、磨耗率の増加により強度及び保形性が劣化するので、有機廃棄物処理剤としての微生物分解菌の担体及び繁殖媒体の機能が低下させるので好ましくない。
各種試験から、炭化率20%以内の特性として優れた微生物分解菌の担体及び繁殖媒体が得られる。このため、非酸化雰囲気下の焼成条件は、炭化率20%以内になるように設定する必要がある。
有機物原料片に含浸され加熱により硬度が向上された材料は、非酸化雰囲気下の焼成により無機質に転換し、複合片の主な表層部分に処理された炭化質部分は、強度と保形性を向上させると共に、木質細片の内部は、有機質部分が炭化せずに保持されているので、保水性及び揮発性を有する。
The firing conditions (temperature and time) in the non-oxidizing atmosphere vary depending on the material and shape of the organic material piece, but the organic material piece is the surface layer by firing at a temperature of 100 to 600 ° C. for 30 minutes to 10 hours. When the portion is carbonized and the content of the organic portion increases as it enters the inside, it is converted into a composite piece in which organic matter and a substance treated in a non-oxidizing atmosphere are mixed.
If the organic raw material piece is completely carbonized (carbonization rate 100%), the strength and shape retention will deteriorate due to the increase in wear rate, so the function of the carrier and propagation medium for microbial degrading bacteria as organic waste treatment agent will be reduced. This is not preferable.
From various tests, a carrier and propagation medium of microbial degrading bacteria excellent in characteristics with a carbonization rate of 20% or less can be obtained. For this reason, it is necessary to set the firing conditions in a non-oxidizing atmosphere so that the carbonization rate is within 20%.
The material that has been impregnated into the organic material piece and improved in hardness by heating is converted to inorganic material by firing in a non-oxidizing atmosphere, and the carbonized part treated on the main surface layer part of the composite piece has strength and shape retention. While improving, since the organic part is hold | maintained without carbonizing, the inside of a wood strip has water retention and volatility.

(第3工程)
第2工程で得られた複合片から、リグニン・へミセルロース等を分解するために、酸性溶液に30分〜2時間浸漬して酸処理を行う。この酸処理に使用する酸は、有機酸・無機酸のいずれの酸でもよく、有機酸の場合はクエン酸、無機酸の場合は希硫酸等を使用する。この場合、クエン酸を使用するのが特に好ましいのは、生態系に安全で環境に優しいからである。
(3rd process)
In order to decompose lignin, hemicellulose and the like from the composite piece obtained in the second step, acid treatment is performed by immersing in an acidic solution for 30 minutes to 2 hours. The acid used for this acid treatment may be either an organic acid or an inorganic acid. In the case of an organic acid, citric acid is used, and in the case of an inorganic acid, diluted sulfuric acid is used. In this case, it is particularly preferred to use citric acid because it is ecologically safe and environmentally friendly.

(第4工程)
第3工程で得られた複合片を、有機酸を使用してpH調整する。ところで、有機廃棄物の処理では、有機廃棄物の内容・目的に対応してそれぞれ最適な微生物分解菌を選定する。
このようにして、選定された微生物分解菌は、それぞれ最適な活動環境とするために特定の有機酸を用いてpH値を調整する。例えば、微生物分解菌に乳酸を使用する場合には、複合片を乳酸溶液に20分〜80分間浸漬して、pH値を6.7〜7.8に調整する。
(4th process)
The pH of the composite piece obtained in the third step is adjusted using an organic acid. By the way, in the treatment of organic waste, the most suitable microbial degrading bacteria are selected according to the content and purpose of the organic waste.
In this way, the selected microbial degradation bacteria adjust the pH value using a specific organic acid in order to obtain an optimal activity environment. For example, when lactic acid is used for microbial degrading bacteria, the composite piece is immersed in a lactic acid solution for 20 to 80 minutes to adjust the pH value to 6.7 to 7.8.

(第5工程)
第4工程の処理で得られた複合片を、担持させる微生物分解菌が存在する水溶液に30分〜1時間、浸漬させる。この場合、水溶液の温度を、20℃〜40℃とし、水道水以外を使用する。
このように、水道水を使用しないのは、水道水に含まれている塩素が、微生物分解菌の繁殖を抑制するためである。微生物分解菌としては、バチルス系が好ましいが、有機廃棄物の内容・目的に対応して、乳酸菌等をも使用することが出来る。
(5th process)
The composite piece obtained by the treatment in the fourth step is immersed in an aqueous solution containing the microbial degrading bacteria to be supported for 30 minutes to 1 hour. In this case, the temperature of the aqueous solution is 20 ° C. to 40 ° C., and other than tap water is used.
Thus, tap water is not used because chlorine contained in tap water suppresses the growth of microbial-degrading bacteria. As a microbial degrading bacterium, a Bacillus type is preferable, but a lactic acid bacterium or the like can also be used according to the contents and purpose of organic waste.

(第2実施例)
まず、有機廃棄物処理剤に関して説明する。
有機廃棄物処理剤は、針葉樹原木から裁断機であるチョッパーを使用して裁断された0.3cm〜4cmの杉細片を、地下水に3時間〜6時間浸漬して水溶性水分を除去する。その後に、ドラム式回転混合機に投入して、シリカゾル水溶液を添加しながら1時間〜3時間混合して、杉細片をシリカゾル水溶液に湿潤させる。この杉細片を、シリカゾル水溶液に18時間〜36時間室温で浸漬して、シリカゾルを杉細片に含浸する。加熱により、硬度を向上させる材料としては、アルミナゾル等の酸化物のコロイド粒子の水溶液、水ガラス溶液、金属アルコキシド溶液等をも使用することが出来る。
前記シリカゾルを含浸した杉細片を、ドラム式回転加熱炉に投入し、雰囲気温度100℃〜600℃で3時間〜5時間焼成して、炭化率が20%以内の複合片を生産する。このようにして生産された杉細片の複合片は、金網で構成させている容器に入れて流水で洗浄後に、鉱泉等に浸漬する。
このように、表面の一部を炭化して、有機質と非酸化雰囲気の処理による物質の結合体を構成することで、木質細片の強度を向上させることで、腐蝕を防止し、また、ポーラス(多孔質)を増加することで、微生物が生息することが出来る環境整備の向上を図る。さらに、樹脂は、微生物に対して阻害因子であり活性化を抑制するので、加熱することにより樹脂を除去する。
(Second embodiment)
First, the organic waste treatment agent will be described.
The organic waste treatment agent removes water-soluble moisture by immersing a cedar strip of 0.3 cm to 4 cm cut from a softwood log using a chopper as a cutting machine in ground water for 3 to 6 hours. Thereafter, the mixture is put into a drum-type rotary mixer and mixed for 1 to 3 hours while adding the silica sol aqueous solution to wet the cedar strips in the silica sol aqueous solution. This cedar strip is immersed in an aqueous silica sol solution at room temperature for 18 hours to 36 hours to impregnate the cedar strip with the silica sol. As materials for improving the hardness by heating, an aqueous solution of oxide colloidal particles such as alumina sol, a water glass solution, a metal alkoxide solution, and the like can also be used.
The cedar strip impregnated with the silica sol is put into a drum-type rotary heating furnace and fired at an ambient temperature of 100 ° C. to 600 ° C. for 3 hours to 5 hours to produce a composite piece having a carbonization rate of 20% or less. The composite piece of cedar strips produced in this way is placed in a container made of wire mesh, washed with running water, and then immersed in a mineral spring.
In this way, part of the surface is carbonized to form a combined body of organic and non-oxidizing atmospheres, thereby improving the strength of the wood strip, thereby preventing corrosion, and porous. By increasing (porosity), improve the environment where microorganisms can live. Furthermore, since the resin is an inhibitor against microorganisms and suppresses activation, the resin is removed by heating.

次に生ごみ処理について説明する。
生ごみ80kg〜150kgと、前記有機廃棄物処理剤300kg〜1200kgを、ドラム式回転攪拌容器内に投入して、8日間〜12日間回転しながら生ごみを処理する。
上記の条件で処理する場合において、毎日の生ごみ処理量が100kgで、10日間の連続運転の場合について説明する。生ごみを100kg及び本発明に係わる前記有機廃棄物処理剤600kgを、前記ドラム式回転攪拌容器内に投入して、約24時間連続運転する。この約24時間の運転後の2日目に、新たに生ごみ100kgを、前記ドラム式回転攪拌容器内に投入して、約24時間連続運転する。このようにして、10日間にわたり毎日、100kgの生ごみを、前記ドラム式回転攪拌容器内に投入して、約24時間連続運転する。
Next, garbage disposal will be described.
80 kg to 150 kg of raw garbage and 300 kg to 1200 kg of the organic waste treatment agent are put into a drum-type rotary stirring vessel, and the garbage is processed while rotating for 8 to 12 days.
In the case of processing under the above conditions, a case where the daily garbage processing amount is 100 kg and continuous operation for 10 days will be described. 100 kg of garbage and 600 kg of the organic waste treatment agent according to the present invention are put into the drum-type rotary stirring vessel, and are continuously operated for about 24 hours. On the second day after the operation for about 24 hours, 100 kg of fresh garbage is newly put into the drum-type rotary stirring vessel and continuously operated for about 24 hours. In this way, 100 kg of garbage is put into the drum-type rotary stirring vessel every day for 10 days and continuously operated for about 24 hours.

このような条件の下で10日間の連続運転終了後に、生ごみ及び前記有機廃棄物処理剤の重量を計測すると、約600.5kgである。これは、前記有機廃棄物処理剤600kgは不変なので、10日間の生ごみ処理総量1000kgの内、約999.5kgが分解したことを意味する。
上記の結果から、本発明の有機廃棄物処理剤における有機廃棄物の分解率(%)=999.5kg÷1000kg≒99.9%である。
このように、本発明の有機廃棄物処理剤よる有機廃棄物の分解率は、非常に高くなっている。
Under these conditions, after the continuous operation for 10 days, the weight of the garbage and the organic waste treatment agent is measured, and it is about 600.5 kg. This means that since 99 kg of the organic waste treatment agent is unchanged, about 999.5 kg of the total amount of garbage treated for 10 days was decomposed.
From the above results, the decomposition rate (%) of organic waste in the organic waste treatment agent of the present invention = 999.5 kg ÷ 1000 kg≈99.9%.
Thus, the decomposition rate of organic waste by the organic waste treatment agent of the present invention is very high.

Claims (4)

有機廃棄物の処理剤において、有機廃棄物を分解する微生物分解菌の担体と繁殖媒体としての機能を有し、木質細片・セプター細片・竹細片・籾殻を加熱して使用し、加熱により硬度を向上させる材料を含浸した有機物原料片を、非酸化雰囲気下で加熱して有機酸と無機酸が混在した多孔質の複合片とし、有機質としての保水性と水分の揮発性及び無機性としての強度と保形性の機能を有することを特徴とする有機廃棄物処理剤。   In the organic waste treatment agent, it functions as a carrier and propagation medium for microbial degrading bacteria that decompose organic waste, heating and using wood strips, scepter strips, bamboo strips and rice husks. Organic material pieces impregnated with materials that improve hardness by heating in a non-oxidizing atmosphere to make porous composite pieces mixed with organic and inorganic acids, water retention as organic matter, moisture volatility and inorganicity Organic waste treatment agent characterized by having functions of strength and shape retention. 請求項1において、木質細片・セプター細片・竹細片・籾殻のいずれかを単独で使用することを特徴とする有機廃棄物処理剤。   2. The organic waste treatment agent according to claim 1, wherein any one of a wood strip, a scepter strip, a bamboo strip, and a rice husk is used alone. 請求項1において、木質細片・セプター細片・竹細片・籾殻のうち複数個の組合わせで使用することを特徴とする有機廃棄物処理剤。   2. The organic waste treatment agent according to claim 1, wherein the organic waste treatment agent is used in combination of a plurality of pieces of wood, scepter, bamboo, and rice husk. 有機廃棄物を分解する微生物分解菌の担体と繁殖媒体として機能する有機廃棄物処理剤の製造方法において、
木質細片・セプター細片・竹細片・籾殻等を十分な強度及び保形性が得られるように所定の長さに裁断して有機物原料片を加工する工程と、
この工程で加工された有機物原料片を十分に乾燥後に加熱炉で加熱し所定の条件で焼成して所定の炭化率になるようにする工程と、
この工程で所定の炭化率に処理された複合片を酸処理する工程と、
この工程によって酸処理された複合片を有機酸によりpH調整する工程と、
この工程でpH調整された複合片に微生物分解菌を担持する工程と、
を有していることを特徴とする有機廃棄物処理剤の製造方法。
In a method for producing an organic waste treatment agent that functions as a carrier and a propagation medium for microbial degrading bacteria that decompose organic waste,
Cutting the organic raw material pieces by cutting the wood pieces, scepter pieces, bamboo pieces, rice husks, etc. into a predetermined length so as to obtain sufficient strength and shape retention;
The organic raw material pieces processed in this step are sufficiently dried and then heated in a heating furnace and fired under predetermined conditions so as to have a predetermined carbonization rate,
A step of acid-treating the composite piece treated to a predetermined carbonization rate in this step;
Adjusting the pH of the composite piece acid-treated by this step with an organic acid;
A step of carrying microbial degrading bacteria on the composite piece adjusted in pH in this step;
The manufacturing method of the organic waste processing agent characterized by having.
JP2007129059A 2007-05-15 2007-05-15 Organic waste treating agent and method for manufacturing the same Pending JP2008284417A (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107089746A (en) * 2017-05-17 2017-08-25 四川省犍为凤生纸业有限责任公司 A kind of recycling method of true qualities bamboo pulp slurrying washes

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107089746A (en) * 2017-05-17 2017-08-25 四川省犍为凤生纸业有限责任公司 A kind of recycling method of true qualities bamboo pulp slurrying washes

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