JPH09208354A - Rapid composting by utilization of medium for promoting oxidation and degradation - Google Patents

Rapid composting by utilization of medium for promoting oxidation and degradation

Info

Publication number
JPH09208354A
JPH09208354A JP3899896A JP3899896A JPH09208354A JP H09208354 A JPH09208354 A JP H09208354A JP 3899896 A JP3899896 A JP 3899896A JP 3899896 A JP3899896 A JP 3899896A JP H09208354 A JPH09208354 A JP H09208354A
Authority
JP
Japan
Prior art keywords
oxidation
composting
raw material
decomposition
promoting
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
JP3899896A
Other languages
Japanese (ja)
Inventor
Nobuyoshi Morikawa
信義 森川
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.)
Mitsubishi Nagasaki Machinery Mfg Co Ltd
Original Assignee
Mitsubishi Nagasaki Machinery Mfg Co 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 Mitsubishi Nagasaki Machinery Mfg Co Ltd filed Critical Mitsubishi Nagasaki Machinery Mfg Co Ltd
Priority to JP3899896A priority Critical patent/JPH09208354A/en
Publication of JPH09208354A publication Critical patent/JPH09208354A/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
    • 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)

Abstract

PROBLEM TO BE SOLVED: To provide a method for rapidly composting a raw material by the utilization of media for promoting the oxidation and degradation of the raw material, capable of promoting the oxidation, the degradation and the fermentation to shorten a composting period by dispersing and mixing the media for promoting the oxidation and the degradation with the raw material to be composted, continuously supplying oxygen or air into the mixture from the lower side and intermittently stirring the mixture. SOLUTION: The media for promoting the oxidation and the degradation of a raw material are made by binding a resin fiber-like material or plant stems into tortoise-shaped scrubbing brush-like articles, and have a height of approximately 50mm and diameters of approximately 30mm. When it is required to deodorize the composted product, a porous material (e.g. an artificial carbonization product) is used. The media having various kinds of shapes such as a cross shape and a spherical shape can be used. The four side surfaces and bottom surface of the composting tank shown in the figure are surrounded with concrete walls 1, and a longitudinally transferable stirrer 2 is disposed on the upper surface to till the raw material to be composted. The media 6 for promoting the oxidation and the decomposition are dispersed and mixed in an amount of >=20vol.%. Air-releasing nozzles 5 are disposed on an air-charging pipe 4, and the raw material is brought into contact with and oxidized with air or oxygen. A weight-selecting machine, etc., is used for removing the media for promoting the oxidation and the degradation.

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】この発明は、し尿、下水道、
各種水処理場等から発生する汚液、牛、鶏、豚等の糞、
及び野菜屑、木葉、樹木等の植物樹葉等の有機物を含有
する被堆肥化原料を酸化、分解及び発酵により堆肥化す
る技術に係り、特に、被堆肥化原料中に酸化・分解促進
媒介物を分散混入することにより、堆肥化への期間を早
めるようにした酸化・分解促進媒介物を利用した早期堆
肥化方法に関するものである。
TECHNICAL FIELD The present invention relates to human waste, sewer,
Sewage generated from various water treatment plants, feces from cows, chickens, pigs, etc.
In addition, the present invention relates to a technology for composting a composting raw material containing organic matter such as vegetable waste, tree leaves, and plant leaves such as trees by oxidizing, decomposing, and fermenting. The present invention relates to an early composting method using an oxidative / decomposition-promoting mediator that accelerates the period of composting by dispersing and mixing.

【0002】[0002]

【従来の技術】し尿、下水道、各種水処理場等から発生
する汚液、牛、鶏、豚等の糞、及び野菜屑、木葉、樹木
等の植物樹葉等の有機物を含有する物質を酸化、分解及
び発酵をさせて肥料として農地へ還元することが行われ
ている。
2. Description of the Related Art Sewage, sewerage, sewage generated from various water treatment plants, feces from cows, chickens, pigs, etc., and substances containing organic substances such as vegetable scraps, leaves, and plant leaves such as trees are oxidized, It is decomposed and fermented and returned to farmland as fertilizer.

【0003】従来の肥料化の方法においては、堆肥化槽
内に被堆肥化原料を入れて堆積し、その下部より酸素又
は空気を連続的に供給する一方、断続的に又は連続的に
攪拌機にて接触酸化を行って、被堆肥化原料の酸化、分
解及び発酵を促して堆肥化を行っている。
In the conventional method for fertilization, the raw material to be composted is put into a composting tank and accumulated, and oxygen or air is continuously supplied from the lower part thereof, while it is intermittently or continuously supplied to a stirrer. Contact oxidation is carried out to promote the oxidation, decomposition and fermentation of the material to be composted, thereby composting.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、前記の
従来の方法では被堆肥化原料の酸化、分解に長時間を要
し、堆肥化に時間がかかるという課題があった。
However, the above-mentioned conventional methods have a problem that it takes a long time to oxidize and decompose the material to be composted, and it takes a long time to compost.

【0005】特に、被堆肥化原料が家畜糞尿等の場合に
は、酸化時分解熱による昇温のため、被堆肥化原料が流
動性の半液状となり充分な酸化ができず、堆肥化が困難
になるという課題があった。
In particular, when the material to be composted is livestock excrement or the like, the temperature is raised by decomposition heat during oxidation, so that the material to be composted becomes liquid semi-liquid and cannot be sufficiently oxidized, so that composting is difficult. There was a problem of becoming.

【0006】また、被堆肥化原料の酸化、分解時にはア
ンモニア系、硫化系等の悪臭が発生するが、悪臭に関し
てはそのまま大気放出か又は別途脱臭施設を付備して処
理する必要があった。
Further, when the raw material to be composted is oxidized and decomposed, an offensive odor such as ammonia or sulfide is generated. However, the offensive odor needs to be released into the air as it is or treated with a separate deodorizing facility.

【0007】この発明は、上記のような課題に鑑み、そ
の課題を解決すべく創案されたものであって、その目的
とするところは、被堆肥化原料中に酸化・分解促進媒介
物を分散混入することにより、堆肥化への期間を早め、
また、脱臭が必要な場合には酸化・分解促進媒介物に多
孔質材を使用することにより、堆肥化時に発生する悪臭
を吸着脱臭することも可能な酸化・分解促進媒介物を利
用した早期堆肥化方法を提供することにある。
The present invention was made in view of the above problems and was devised to solve the problems. The object of the present invention is to disperse an oxidation / decomposition promoting medium in a composting raw material. By mixing it, the period for composting is shortened,
In addition, when deodorization is required, a porous material is used as an oxidation / decomposition accelerating agent, so that the bad odor generated during composting can be adsorbed and deodorized. It is to provide a method of computerization.

【0008】[0008]

【課題を解決するための手段】以上の目的を達成するた
めに、この発明は、有機物を含有する被堆肥化原料を堆
肥化槽に入れて堆積させ、その下部より酸素又は空気を
連続的に供給する一方、断続的に又は連続的に攪拌機に
て接触酸化を行って堆肥化を図る堆肥化方法において、
前記被堆肥化原料中に容積割合で少なくとも20%の酸
化・分解促進媒介物を分散混入し、分散混入した酸化・
分解促進媒介物によって、前記被堆肥化原料の通気性を
よくすると共に酸化接触面積を増すことにより酸化、分
解及び分解菌の活動エリアを増殖し易い環境を作り出
し、早期酸化、分解、発酵をならしめて、堆肥化への期
間を早めるようにした手段よりなるものである。
[Means for Solving the Problems] In order to achieve the above-mentioned object, the present invention puts a composting raw material containing an organic substance in a composting tank and deposits it, and oxygen or air is continuously supplied from the lower part thereof. While supplying, in the composting method for performing composting by performing contact oxidation with an agitator intermittently or continuously,
At least 20% by volume of an oxidative / decomposition promoting agent is dispersed and mixed in the raw material for composting, and the oxidized / oxidized mixture is mixed.
The decomposition promoting agent improves the air permeability of the material to be composted and increases the oxidation contact area to create an environment in which the active areas of oxidation, decomposition and degrading bacteria can easily grow, and promotes early oxidation, decomposition and fermentation. At the very least, it consists of means designed to accelerate the period for composting.

【0009】ここで、酸化・分解促進媒介物に多孔質材
を使用して、堆肥化時に発生する悪臭を吸着脱臭するよ
うにするのが好ましい。
Here, it is preferable to use a porous material as a medium for promoting oxidation / decomposition so as to adsorb and deodorize a bad odor generated during composting.

【0010】[0010]

【作用】少なくとも20%の酸化・分解促進媒介物を分
散混入した被堆肥化物の堆積層の下部より酸素又は空気
を供給し、適温度と適時攪拌の環境を与えれば、分散混
入した酸化・分解促進媒介物の機能によって、被堆肥化
原料の通気性向上、酸化接触面積の増大に依り、酸化又
分解ガスの通気、分解菌の増殖等により、早期酸化、分
解、発酵が促進されて、堆肥化への期間を早める作用が
ある。
[Operation] Oxygen or air is supplied from the lower part of the sediment layer of the composted material in which at least 20% of the oxidative / decomposition-promoting medium is dispersed and mixed, and if an environment of appropriate temperature and appropriate stirring is provided, the oxidative / decomposition is dispersed and mixed. Due to the function of the facilitating medium, the air permeability of the material to be composted is improved, the oxidation contact area is increased, and the oxidation or decomposition gas is aerated and the decomposition bacteria are propagated to accelerate early oxidation, decomposition, and fermentation. It has the effect of accelerating the period to change.

【0011】脱臭が必要な場合には、酸化・分解促進媒
介物に多孔質材を使用して、多孔質媒介物の吸着作用に
より、被堆肥化原料の酸化、分解時に発生するアンモニ
ア系、硫化系の悪臭物質も吸着され、脱臭効果が増大さ
れる作用がある。
When deodorization is required, a porous material is used as an oxidative / decomposition-promoting medium, and the adsorbing action of the porous medium causes the ammonia-based and sulfide-based substances generated during the oxidation and decomposition of the raw material for composting. Malodorous substances in the system are also adsorbed, and the deodorizing effect is increased.

【0012】完熟製品化後、酸化・分解促進媒介物は例
えばトロンメル等にて堆肥化したものから分離除去分解
される。
After the product is matured, the oxidative / decomposition promoting medium is separated and decomposed from the composted product by, for example, trommel.

【0013】[0013]

【発明の実施の形態】以下、図面に記載の発明の実施の
形態に基づいて、この発明をより具体的に説明する。こ
こで、図1(A)〜(F)は無孔質の材料からなる酸化
・分解促進媒介物の形状図、図2(A)〜(C)は多孔
質の材料からなる酸化・分解促進媒介物の形状図、図3
は本発明実証テスト装置の概略側断面図、図4は本発明
実証テスト装置の概略正断面図である。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, the present invention will be described more specifically based on embodiments of the invention shown in the drawings. Here, FIGS. 1 (A) to 1 (F) are shape diagrams of an oxidation / decomposition promoting medium made of a non-porous material, and FIGS. 2 (A) to 2 (C) are oxidation / decomposition promoting substances made of a porous material. Figure of shape of medium, Figure 3
Is a schematic side sectional view of the present invention verification test device, and FIG. 4 is a schematic front sectional view of the present invention verification test device.

【0014】図1の(A)〜(F)は脱臭を必要としな
い場合に使用される各酸化・分解促進媒介物6の形状を
示したものであり、又その材質には無孔質の材料が用い
られている。無孔質の材料として下記以外にも天然鉱物
もある。
FIGS. 1A to 1F show the shape of each oxidative / decomposition promoting medium 6 used when deodorization is not required, and the material thereof is non-porous. Material is used. There are natural minerals other than the following as non-porous materials.

【0015】このうち、図1(A)(B)の酸化・分解
促進媒介物6は、レジン系糸状又は植物樹茎を結束した
ものである。図1(A)の酸化・分解促進媒介物6はレ
ジン系糸状又は植物樹茎を亀の子タワシ形状に結束した
ものであり、その大きさは、高さが約50mm、直径が約
30mm程度である。図1(B)の酸化・分解促進媒介物
6はレジン系糸状又は植物樹茎を栗形状に結束したもの
であり、その球系の大きさは直径が約40mm程度であ
る。
Of these, the oxidative / degradation promoting medium 6 in FIGS. 1 (A) and 1 (B) is a resin filament or a bundle of plant stems. The oxidative / degradation promoting agent 6 in FIG. 1 (A) is a resin-based filamentous or plant tree stem bundled in the shape of a tortoise scrubber, the size of which is about 50 mm in height and about 30 mm in diameter. Is. The oxidative / degradation promoting medium 6 in FIG. 1 (B) is a resin-based filamentous or plant tree stem bundled in a chestnut shape, and its spherical system has a diameter of about 40 mm.

【0016】また、図1(C)(D)の酸化・分解促進
媒介物6は、その材質が人工セラミックス系からなる。
図1(C)の酸化・分解促進媒介物6は、人工セラミッ
クス系の材質を厚みのある十字型状に形成したものであ
り、その大きさは、十字型の直径が各々約50mm、十字
型の長さが約50mm、十字型の厚みが約20mm程度であ
る。図1(D)の酸化・分解促進媒介物6は、人工セラ
ミックス系の材質を歯車型状に形成したものであり、そ
の大きさは、歯車の直径が各々約60mm、歯車の長さが
約50mm程度であり、歯車の中央には直径約20mm程度
の孔が長さ方向に形成されている。
The material of the oxidation / decomposition promoting medium 6 shown in FIGS. 1C and 1D is made of artificial ceramics.
The oxidization / decomposition promoting medium 6 in FIG. 1 (C) is made of artificial ceramic material in the shape of a thick cross, and the size of the cross is about 50 mm and the cross is about 50 mm. Has a length of about 50 mm and a cross-shaped thickness of about 20 mm. The oxidation / decomposition promoting medium 6 in FIG. 1 (D) is made of an artificial ceramic material in the shape of a gear. The size of the gear is about 60 mm, and the length of the gear is about 60 mm. The gear has a diameter of about 50 mm, and a hole having a diameter of about 20 mm is formed in the center of the gear in the length direction.

【0017】また、図1(E)(F)の酸化・分解促進
媒介物6は、その材質が溶融スラグを硬化剤にて結合し
たものからなる。図1(E)の酸化・分解促進媒介物6
は、溶融スラグを硬化剤で球状に結合したものであり、
その大きさは、球の直径が約30mm程度である。図1
(F)の酸化・分解促進媒介物6は、溶融スラグを硬化
剤で板状に結合したものであり、その大きさは、幅が約
30mm、長さが約50mm、厚みが約10mm程度である。
The oxidizing / decomposing promoting medium 6 shown in FIGS. 1 (E) and 1 (F) is made of a material in which molten slag is bonded with a curing agent. Oxidation / degradation promoting medium 6 in FIG. 1 (E)
Is a molten slag bonded in a spherical shape with a curing agent,
The size is such that the diameter of the sphere is about 30 mm. FIG.
The oxidization / decomposition promoting medium 6 of (F) is formed by combining molten slag in a plate shape with a curing agent, and its size is about 30 mm in width, about 50 mm in length, and about 10 mm in thickness. is there.

【0018】図2の(A)〜(C)は脱臭を必要とする
場合に使用される各酸化・分解促進媒介物6の形状を示
したものであり、又その材質には多孔質の材料が用いら
れている。多孔質の材料として下記以外にも活性炭や人
工炭化物もある。
2A to 2C show the shape of each oxidative / decomposition promoting medium 6 used when deodorization is required, and the material thereof is a porous material. Is used. In addition to the following, activated carbon and artificial carbide are also available as porous materials.

【0019】このうち、図2(A)の酸化・分解促進媒
介物6は、木炭屑を硬化剤で球状に結合したものであ
り、その大きさは、球の直径が約30mm程度であり、ま
た、隙間は約 0.5〜2mm程度である。
Of these, the oxidation / decomposition promoting medium 6 in FIG. 2 (A) is formed by combining charcoal scraps in a spherical shape with a hardening agent, and the size thereof is about 30 mm in diameter, The gap is about 0.5 to 2 mm.

【0020】また、図2(B)(C)の酸化・分解促進
媒介物6は、その材質がゼオライト系からなる。図2
(B)の酸化・分解促進媒介物6は、ゼオライト系の材
質を球状に形成したものであり、その大きさは、球の直
径が約30mm程度であり、また、隙間は約20μ〜 0.5
mm程度である。図2(C)の酸化・分解促進媒介物6
は、ゼオライト系の材質を多角溝形状に形成したもので
あり、その大きさは、直径が約50mm、長さが30mm程
度であり、また、隙間は約20μ〜 0.5mm程度である。
The material for the oxidation / decomposition promoting medium 6 shown in FIGS. 2B and 2C is made of zeolite. FIG.
The oxidization / degradation promoting medium 6 in (B) is formed by spherically forming a zeolite-based material, and the size is such that the diameter of the sphere is about 30 mm and the gap is about 20 μ to 0.5 μm.
mm. Oxidation / degradation promoting agent 6 in FIG. 2 (C)
Is a zeolite-based material formed in the shape of polygonal grooves, and its size is about 50 mm in diameter and about 30 mm in length, and the gap is about 20 μ to 0.5 mm.

【0021】そして、図1又は図2に示すような形状と
粗成からなる酸化・分解促進媒介物6を、図3、図4に
示すような堆肥化槽に入れて堆積させた被堆肥化原料3
中に容積割合で少なくとも20%を分散混入し、その下
部より酸素又は空気を連続的に供給する一方、断続的に
又は連続的に攪拌機にて接触酸化を行って早期の堆肥化
を図るのである。
Then, the oxidation / decomposition promoting medium 6 having a shape and coarse formation as shown in FIG. 1 or 2 is placed in a composting tank as shown in FIGS. Raw material 3
At least 20% by volume is dispersed and mixed into the inside, and oxygen or air is continuously supplied from the lower part, while intermittent or continuous catalytic oxidation is carried out with a stirrer for early composting. .

【0022】図3、図4に示すような堆肥化槽は、四側
面及び底面がコンクリート壁1で囲まれ、上面が開口さ
れた長方体型の形状を有し、その開口された上面には長
手方向に移動自在に攪拌機2が2基並設されている。
The composting tank as shown in FIGS. 3 and 4 has a rectangular parallelepiped shape in which the four side surfaces and the bottom surface are surrounded by the concrete wall 1 and the upper surface is opened. Two agitators 2 are arranged side by side so as to be movable in the longitudinal direction.

【0023】各攪拌機2は下向きに取り付けられてい
て、この攪拌機2が連続的又は断続的に耕転して、コン
クリート壁1で囲まれた内側に堆積された被堆肥化原料
3及び該被堆肥化原料3中に少なくとも20%が分散混
入された酸化・分解促進媒介物6を攪拌し、空気放出ノ
ズル5から供給される空気又は酸素との接触酸化を行っ
ている。
Each stirrer 2 is mounted downward, and the stirrer 2 is continuously or intermittently cultivated, and the composting raw material 3 and the composted fertilizer 3 accumulated inside the concrete wall 1 are accumulated. The oxidation / decomposition promoting medium 6 in which at least 20% is dispersed and mixed in the chemical conversion raw material 3 is stirred, and contact oxidation with the air or oxygen supplied from the air discharge nozzle 5 is performed.

【0024】被堆肥化原料3が堆積された底部には空気
導入管4が配管されており、空気導入管4には空気放出
ノズル5が分岐して取り付けられている。各空気放出ノ
ズル5は底部に幅方向及び長手方向に等間隔で配管され
ており、底部から空気又は酸素を堆積された被堆肥化原
料3に連続的に供給できるようになっている。
An air introducing pipe 4 is provided at the bottom of the raw material 3 to be composted, and an air discharging nozzle 5 is branched and attached to the air introducing pipe 4. Each of the air discharge nozzles 5 is arranged at the bottom portion at equal intervals in the width direction and the longitudinal direction, and air or oxygen can be continuously supplied from the bottom portion to the deposited composting raw material 3.

【0025】被堆肥化原料3中に容積割合で少なくとも
20%の酸化・分解促進媒介物6を分散混入することに
よって、被堆肥化原料3の堆積状態での通気度合を良く
すると共に酸化接触面積を多くする。また、熱による流
動粘性状の密度の高い被堆肥化原料3の通気度合及び酸
化接触面積を多くする。そして、分解菌の活動エリアの
増殖し易い環境を作り出す。
By dispersing and mixing at least 20% by volume of the oxidization / decomposition promoting medium 6 in the composting raw material 3, the ventilation degree in the piled state of the composting raw material 3 is improved and the oxidation contact area is increased. To increase. Further, the air permeability and the oxidation contact area of the composting raw material 3 having a high flow viscosity due to heat and having a high density are increased. Then, it creates an environment in which the activity area of the degrading bacteria easily grows.

【0026】酸化・分解促進媒介物6の混入容積度合は
被堆肥化原料3に対して、分解熱にても難粘物であれ
ば、最低20%、粘性物であれば最低30%程度は必要
となる。
The mixing volume of the oxidative / decomposition promoting medium 6 is at least 20% with respect to the raw material 3 to be composted if it is difficult to be decomposed by heat of decomposition, and at least 30% if it is viscous. Will be needed.

【0027】脱臭が必要な場合には、被堆肥化原料3中
に分散混入する酸化・分解促進媒介物6の材質に多孔質
材を使用することによって、多孔質媒介物の吸着作用に
より、被堆肥化原料3の酸化、分解時に発生する分解ガ
ス7に含まれるアンモニア系、硫化系の悪臭物質も吸着
され、脱臭効果が増大する。
When deodorization is required, by using a porous material as the material of the oxidation / decomposition promoting medium 6 dispersed and mixed in the composting raw material 3, the adsorption of the porous medium causes Ammonia-based and sulfide-based malodorous substances contained in the decomposition gas 7 generated during the oxidation and decomposition of the composting raw material 3 are also adsorbed, and the deodorizing effect is increased.

【0028】酸化・分解促進媒介物6の機能によって、
被堆肥化原料3から早期に堆肥化へ図られた後において
は、堆肥製品から酸化・分解促進媒介物6を分離除去す
る必要があり、この場合には、例えばトロンメル、重力
選別機、風力選別機等が使用される。また、分離除去し
た酸化・分解促進媒介物6の再利用する場合には、これ
を洗浄する洗浄装置等が必要となり、例えば高圧洗浄
水、オートクレーブ、炭化再生機等が使用される。
By the function of the oxidation / degradation promoting medium 6,
After the material 3 to be composted is converted into the compost early, it is necessary to separate and remove the oxidation / decomposition promoting medium 6 from the compost product. In this case, for example, trommel, gravity sorter, wind sorter, etc. Machines are used. Further, when the separated / removed oxidation / decomposition promoting medium 6 is reused, a washing device or the like for washing this is required, and for example, high-pressure washing water, an autoclave, a carbonization regenerator or the like is used.

【0029】[0029]

【実施例】図3、図4の実証プラントにて表1に示す被
原料2種類をテストした。その結果を表1に示す。
EXAMPLE Two kinds of raw materials shown in Table 1 were tested in the demonstration plant shown in FIGS. Table 1 shows the results.

【0030】[0030]

【表1】 [Table 1]

【0031】〔実施例1〕脱水し尿汚液含水率73%を
原料とし、乾物含水率27%、酸化・分解促進媒介物の
図1(A)のタイプの形状を20%混入した場合と、酸
化・分解促進媒介物なしの原料から完熟までの日数を比
較した。尚エアーの供給料は槽平面積当たり、毎分当た
り0.8m3 、又ロータリー攪拌機にての耕転は6時間
毎一定し比較した。その結果は119日対43日と約1
/3の日数効果を得た。
Example 1 A case where dehydrated urine wastewater 73% was used as a raw material, dry matter water content was 27%, and the shape of the type of oxidation / degradation promoting medium of 20% was mixed, The number of days from raw material without oxidization / decomposition promoting medium to full maturity was compared. The air supply rate was 0.8 m 3 per minute per square meter of the tank, and the rotary agitation was fixed every 6 hours for comparison. The result was 119 days vs. 43 days, about 1
/ 3 days effect was obtained.

【0032】〔実施例2〕鶏糞含水分89%を原料と
し、乾物含水分30%までの分解、発酵を前記の実験例
1と同様比較して、その効果を確認した。酸化・分解促
進媒介物は図2(A)のタイプの形状を対容積比40%
混入した。結果は159日対87日で約1/2の期間に
短縮、又脱臭効果も一次酸化、分解時期2週間目位で、
最高アンモニアが890ppm から120ppm に減少し、
硫化水素も38ppm から6ppm に減少し、大幅な脱臭効
果も得られた。
[Example 2] Using 89% water content of chicken manure as a raw material, decomposition and fermentation up to 30% water content of dry matter were compared in the same manner as in Experimental Example 1 above, and the effect was confirmed. The oxidative / decomposition promoting medium has the shape of the type shown in FIG.
Mixed. The result was shortened to about 1/2 period from 159 days to 87 days, and the deodorizing effect was primary oxidation and the decomposition time was about 2 weeks.
Maximum ammonia decreased from 890ppm to 120ppm,
Hydrogen sulfide was also reduced from 38 ppm to 6 ppm, and a significant deodorizing effect was obtained.

【0033】上記の分解時媒介物なしは最高被物温度は
89℃にも達し、粘性が流動化密度も増し、酸化、分解
に悪影響を与えた。媒介物有りは最高温度68℃と粘性
は多少大きくなったが、その差ははっきり示された。
Without the above-mentioned mediator during decomposition, the maximum object temperature reached 89 ° C., the viscosity and the fluidization density increased, and the oxidation and decomposition were adversely affected. With the medium, the maximum temperature was 68 ° C, and the viscosity became slightly large, but the difference was clearly shown.

【0034】乾物化後、酸化・分解促進媒介物は図示し
ないトロンメル装置にて、堆肥製品と分別した。
After being dried, the oxidative / decomposition promoting medium was separated from the compost product by a trommel apparatus (not shown).

【0035】[0035]

【発明の効果】以上の記載より明らかなように、この発
明に係る酸化・分解促進媒介物を利用した早期堆肥化方
法によれば、特に高含水原料、及び60〜80℃にて粘
性が大きくなる被堆肥化原料を早期堆肥化するにあた
り、従来の方式の被堆肥化原料に対して、早期酸化、分
解を助ける通気性の問題と分解菌の増殖活動エリアの良
い環境作りとを促進させる酸化・分解促進媒介物を少な
くと20%分散混入することによって、大幅な日程短縮
を図ることができる。
As is apparent from the above description, according to the method for early composting using the oxidative / decomposition promoting medium according to the present invention, the viscosity is particularly high at high water content and at 60 to 80 ° C. In the case of early composting of the material to be composted, the conventional method of oxidizing the material to be composted is promoted to promote the early oxidation and aeration problems that help decomposition and the creation of a good environment for the growth activity area of decomposing bacteria. -By incorporating at least 20% of the decomposition accelerating agent, it is possible to significantly shorten the schedule.

【0036】また、脱臭が必要な場合には、酸化・分解
促進媒介物に多孔質材を使用することによって、堆肥化
時に発生する悪臭を吸着脱臭することができ、大幅な日
程短縮と脱臭効果も得られる等、極めて新規的有益なる
効果を奏するものである。
When deodorization is required, the use of a porous material as an oxidation / decomposition promoting medium makes it possible to adsorb and deodorize a bad odor generated during composting, resulting in a significant reduction in schedule and deodorizing effect. It also has an extremely new and beneficial effect.

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

【図1】(A)〜(F)はこの発明の実施の形態を示す
無孔質の材料からなる酸化・分解促進媒介物の形状図で
ある。
1 (A) to 1 (F) are shape diagrams of an oxidation / degradation promoting medium made of a non-porous material showing an embodiment of the present invention.

【図2】(A)〜(C)はこの発明の実施の形態を示す
多孔質の材料からなる酸化・分解促進媒介物の形状図で
ある。
2 (A) to (C) are shape diagrams of an oxidation / decomposition promoting medium made of a porous material, showing an embodiment of the present invention.

【図3】この発明の実施の形態を示す本発明実証テスト
装置の概略側断面図である。
FIG. 3 is a schematic side sectional view of a verification test apparatus of the present invention showing an embodiment of the present invention.

【図4】この発明の実施の形態を示す本発明実証テスト
装置の概略正断面図である。
FIG. 4 is a schematic front sectional view of a verification test apparatus of the present invention showing an embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1 壁 2 攪拌機 3 被堆肥化原料 4 空気導入管 5 空気放出ノズル 6 酸化・分解促進媒介物 7 分解ガス 1 Wall 2 Stirrer 3 Raw material for composting 4 Air introduction pipe 5 Air discharge nozzle 6 Oxidation / decomposition promoting medium 7 Decomposition gas

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 有機物を含有する被堆肥化原料を堆肥化
槽に入れて堆積させ、その下部より酸素又は空気を連続
的に供給する一方、断続的に又は連続的に攪拌機にて接
触酸化を行って堆肥化を図る堆肥化方法において、前記
被堆肥化原料中に容積割合で少なくとも20%の酸化・
分解促進媒介物を分散混入し、分散混入した酸化・分解
促進媒介物によって、前記被堆肥化原料の通気性をよく
すると共に酸化接触面積を増すことにより酸化、分解及
び分解菌の活動エリアを増殖し易い環境を作り出し、早
期酸化、分解、発酵をならしめて、堆肥化への期間を早
めるようにしたことを特徴とする酸化・分解促進媒介物
を利用した早期堆肥化方法。
1. A material to be composted containing an organic matter is placed in a composting tank to be deposited, and oxygen or air is continuously supplied from the lower part thereof, while intermittent or continuous catalytic oxidation is carried out by a stirrer. In the method for composting by carrying out composting, at least 20% by volume of the composting raw material is oxidized and
Disperse and mix the decomposition promoting mediator, and improve the air permeability of the raw material to be composted and increase the oxidation contact area by the oxidation and decomposition promoting media that are dispersed and mixed. An early composting method using an oxidative / decomposition-promoting medium, characterized in that an easy-to-use environment is created, and early oxidation, decomposition, and fermentation are smoothed to accelerate the period for composting.
【請求項2】 酸化・分解促進媒介物に多孔質材を使用
して、堆肥化時に発生する悪臭を吸着脱臭するようにし
た請求項1記載の酸化・分解促進媒介物を利用した早期
堆肥化方法。
2. An early composting process using an oxidation / decomposition promoting medium according to claim 1, wherein a porous material is used as the oxidation / decomposition promoting medium so that a malodor generated during composting is adsorbed and deodorized. Method.
JP3899896A 1996-01-31 1996-01-31 Rapid composting by utilization of medium for promoting oxidation and degradation Pending JPH09208354A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3899896A JPH09208354A (en) 1996-01-31 1996-01-31 Rapid composting by utilization of medium for promoting oxidation and degradation

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3899896A JPH09208354A (en) 1996-01-31 1996-01-31 Rapid composting by utilization of medium for promoting oxidation and degradation

Publications (1)

Publication Number Publication Date
JPH09208354A true JPH09208354A (en) 1997-08-12

Family

ID=12540808

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3899896A Pending JPH09208354A (en) 1996-01-31 1996-01-31 Rapid composting by utilization of medium for promoting oxidation and degradation

Country Status (1)

Country Link
JP (1) JPH09208354A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1134196A1 (en) * 2000-03-14 2001-09-19 Masaru Hazaka Method for treating organic waste matter in a fermentation container
US6316246B1 (en) 1999-02-08 2001-11-13 Masaru Hazaka Method for treating organic waste matter
CN112753588A (en) * 2020-12-25 2021-05-07 青海裕福畜牧业发展有限公司 Conveniently-treated excrement collecting device for live pig breeding and using method thereof

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6316246B1 (en) 1999-02-08 2001-11-13 Masaru Hazaka Method for treating organic waste matter
EP1134196A1 (en) * 2000-03-14 2001-09-19 Masaru Hazaka Method for treating organic waste matter in a fermentation container
EP1777199A1 (en) * 2000-03-14 2007-04-25 Masaru Hazaka Method for treating organic waste matter in a fermentation container
CN112753588A (en) * 2020-12-25 2021-05-07 青海裕福畜牧业发展有限公司 Conveniently-treated excrement collecting device for live pig breeding and using method thereof

Similar Documents

Publication Publication Date Title
KR101870797B1 (en) Sewage sludge treatment methods to remove biological drying and odor utilizing high temperature aerobic microorganisms
DE19916857A1 (en) Disposal of an organic waste involves preparing material with bacteria on sterile carriers, introducing the material into a fermenting tank and feeding food waste, mixing, and operating a temperature regulator
JPH09208354A (en) Rapid composting by utilization of medium for promoting oxidation and degradation
KR19980079280A (en) Oni reforming method
JP2004275949A (en) Excreta decomposing treating agent and decomposing treating method for excreta by activation of microorganism
DE2423744A1 (en) Composting of settled sludge - particularly from activated sludge plants in aerating silos
JP3487399B2 (en) Final treatment of excess sludge
EP0658153B1 (en) Method of neutralizing and recovering of gases released from wet composting of domestic animal manure and/or sewage mud
JP2007330928A (en) Waste treatment device
KR20020005023A (en) Process and apparatus for utilizing animal excrement
JPH021558B2 (en)
JPH0810792A (en) Garbage-containing sewage treating device
JPH0667519B2 (en) Method of treating feces, urine, organic sludge, sewage, etc.
JP2003210931A (en) Method for deodorization treatment
JP4953513B2 (en) Garbage disposal agent and high temperature garbage disposal method
JP3192408B2 (en) Garbage processing equipment
JPH04250893A (en) Bioreaction device for treating sludgy and solid organic waste
JP2003225531A (en) Biological deodorizing method and biological deodorizing device
JP2001163689A (en) Deodorizing apparatus for composting device of livestock excrement
JP2000024628A (en) Production of microorganism base material for treating sewage, and microorganism base material
JPH10323652A (en) Method and device for treating raw garbage
JP2823506B2 (en) Porous filler for deodorizing device and deodorizing device using the same
KR101477549B1 (en) Process for purifying highly concentrated malicious organic waste
JP2003117341A (en) Method for treating gas containing ammonia and device therefor
Shimko et al. Biochemical methods of freeing gas-air mixtures from sulfur containing compounds