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JPH10291877A - Production method of organic sludge fertilizer - Google Patents

Production method of organic sludge fertilizer

Info

Publication number
JPH10291877A
JPH10291877A JP9104419A JP10441997A JPH10291877A JP H10291877 A JPH10291877 A JP H10291877A JP 9104419 A JP9104419 A JP 9104419A JP 10441997 A JP10441997 A JP 10441997A JP H10291877 A JPH10291877 A JP H10291877A
Authority
JP
Japan
Prior art keywords
sludge
fertilizer
component
dryer
org
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
JP9104419A
Other languages
Japanese (ja)
Inventor
Masahito Fujita
雅人 藤田
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.)
Takuma Co Ltd
Original Assignee
Takuma 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 Takuma Co Ltd filed Critical Takuma Co Ltd
Priority to JP9104419A priority Critical patent/JPH10291877A/en
Publication of JPH10291877A publication Critical patent/JPH10291877A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A40/00Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
    • Y02A40/10Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
    • Y02A40/20Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses

Landscapes

  • Treatment Of Sludge (AREA)
  • Fertilizers (AREA)

Abstract

PROBLEM TO BE SOLVED: To produce an org. fertilizer containing a desired component from an org. waste at a low cost. SOLUTION: An org. sludge fertilizer is produced by dehydrating an org. sludge to make a dehydrated sludge having a 50-85 wt.% (wet base) water content, charging the obtained dehydrated sludge to a dryer 4 having simultaneously a mixing function and a granulating function, also charging zeolite, an additional fertilizer component, a pH adjusting component, a deodorant and/or a soil conditioner as an additional component, mixing the hydrated sludge and the additional components in the dryer 4, drying and granulating the mixture. An working temp. in a drying operation is suitably within the range of 60-80 deg.C.

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は、下水汚泥、農村集
落排水汚泥、浄化槽汚泥、し尿汚泥などの有機系の汚泥
から有機汚泥肥料を製造する方法に関する。なお、以下
の説明において含水率は湿量基準の重量%を意味する。
The present invention relates to a method for producing an organic sludge fertilizer from organic sludge such as sewage sludge, rural settlement drainage sludge, septic tank sludge, human waste sludge, and the like. In the following description, the water content means% by weight on a wet basis.

【0002】[0002]

【従来の技術】前記の有機系汚泥は、従来から脱水ケー
キ、乾燥ケーキ、コンポストなどの形態で肥料に利用さ
れていた。しかし、脱水ケーキは水分を多く含んでかさ
ばり、また付着性が強くて扱いにくかった。乾燥ケーキ
は含水率が低く扱いやすいが乾燥時に臭気発生防止の問
題があり、コンポストは微生物の発酵作用により製造さ
れ肥料として優れるが加工コストが大きいなど、それぞ
れに問題があった。また、共通して肥料三要素のバラン
スを調整しにくい欠点があった。
2. Description of the Related Art The above-mentioned organic sludge has been conventionally used as a fertilizer in the form of a dewatered cake, a dried cake, compost or the like. However, the dehydrated cake was bulky and rich in moisture, and was difficult to handle due to its strong adhesion. The dried cake has a low water content and is easy to handle, but has a problem of preventing generation of odor during drying. The compost is produced by fermentation of microorganisms and is excellent as a fertilizer, but has a problem in that the processing cost is large. In addition, there was a disadvantage that it was difficult to adjust the balance of the three elements of fertilizer in common.

【0003】そこで、前記の問題を解決するために、ゼ
オライトなどを有機系汚泥に添加して所要の固形有機汚
泥肥料に加工することが提案されている。たとえば、特
公平3−69600号公報には、浄化槽などの汚泥にゼ
オライトを、さらに生石灰を加え、攪拌混合し、しかる
後に乾燥、造粒する汚泥処理方法が記載されている。ま
た、特開昭62−167281号公報や特開昭64−6
1380号公報には汚泥を乾燥し、または堆肥に加工し
た後、ゼオライトなどを添加する肥料組成物の製造方法
が記載されている。
In order to solve the above problem, it has been proposed to add zeolite or the like to organic sludge and process it into a required solid organic sludge fertilizer. For example, Japanese Patent Publication No. 3-69600 describes a sludge treatment method in which zeolite and quick lime are added to sludge in a septic tank or the like, further mixed with stirring, and then dried and granulated. Also, Japanese Patent Application Laid-Open Nos. Sho 62-167281 and
No. 1380 describes a method for producing a fertilizer composition in which sludge is dried or processed into compost and then zeolite or the like is added.

【0004】[0004]

【発明が解決しようとする課題】しかし、特公平3−6
9600号公報記載の汚泥処理方法では最終処理物の含
水率が高く55〜70%もあり(全国農業協同組合中央
会が推奨する下水汚泥肥料水分率基準は30%以下)、
また多量の生石灰を使用するので反応生成物である消石
灰の含有量が高く所望の成分構成を取り難い。また、特
開昭62−167281号公報や特開昭64−6138
0号公報記載の肥料組成物の製造方法は、加工汚泥の含
水率が低すぎて添加成分と成形、一体化が行いにくく、
別途、造粒機などの諸設備を要し高コスト化の傾向があ
る。本発明は、主原料の有機系汚泥に必要な添加成分を
加えて所要の構成通りに調合し、主原料および各添加成
分間の一体化をはかり、成形しやすく均質で使い勝手の
よい有機汚泥肥料を、容易に低コストで製造する方法を
研究した結果、完成したものである。
[Problems to be solved by the invention]
In the sludge treatment method described in No. 9600, the water content of the final treated product is as high as 55 to 70% (the sewage sludge fertilizer moisture content standard recommended by the National Agricultural Cooperative Association of Japan is 30% or less),
Further, since a large amount of quicklime is used, the content of slaked lime, which is a reaction product, is high, and it is difficult to obtain a desired component composition. Also, JP-A-62-167281 and JP-A-64-1138.
The production method of the fertilizer composition described in No. 0 publication has a problem that the water content of the processed sludge is too low and the additive component is not easily formed and integrated,
Separately, various equipment such as a granulator is required, and the cost tends to be high. The present invention relates to an organic sludge fertilizer which is prepared by adding a required additive component to an organic sludge as a main raw material, mixing the main raw material and each of the additional components, and forming a uniform and easy-to-use homogeneous sludge. Was completed as a result of studying a method for easily manufacturing the same at low cost.

【0005】[0005]

【課題を解決するための手段】すなわち本発明は、前記
の課題を解決するために、有機系の汚泥を含水率が50
〜85重量%(湿量基準)に脱水して脱水汚泥とし、得
られた脱水汚泥を混合、造粒機能を併有する乾燥機に投
入するとともに添加成分としてゼオライト、追加肥料成
分、pH調整成分、脱臭剤、および/または土質改良剤
を投入し、乾燥機内において脱水汚泥と添加成分とを混
合し、乾燥し、造粒することを特徴とする有機汚泥肥料
の製造方法を提供する。本発明の製造方法において、乾
燥操作の温度は60ないし80℃の範囲内が好適であ
る。
That is, the present invention provides an organic sludge having a water content of 50 to solve the above-mentioned problems.
Dewatered sludge by dewatering to ~ 85% by weight (wet amount basis), and mixing the obtained dewatered sludge into a dryer having both a granulating function and adding zeolite, an additional fertilizer component, a pH adjusting component, Provided is a method for producing an organic sludge fertilizer, which comprises adding a deodorant and / or a soil conditioner, mixing a dehydrated sludge and an additive component in a dryer, drying, and granulating. In the production method of the present invention, the temperature of the drying operation is preferably in the range of 60 to 80 ° C.

【0006】[0006]

【発明の実施の形態】本発明を図面を参照し実施形態例
をあげて具体的に説明する。図1は本発明の一実施形態
例を示すフローシートである。肥料の原料である下水汚
泥、農村集落排水汚泥、浄化槽汚泥、し尿汚泥などの有
機系原料汚泥を脱水して脱水汚泥とし、脱水汚泥ホッパ
1に貯留する。脱水汚泥の含水率は50〜85%が好適
である。含水率が低すぎれば脱水汚泥と添加成分として
添加するゼオライト、追加肥料成分、pH調整成分、脱
臭剤、および/または土質改良剤とを均一に混合するこ
とが難くなって、成形、一体化が行いにくくなり好まし
くない。含水率が高すぎると混合機に付着して操作が難
しくなりエネルギー消費量が増大する。脱水方法にとく
に制限はなく、有機系原料汚泥の特性や操業環境などに
より最適な手段を選択、実施することができる。貯留し
た脱水汚泥は、脱水汚泥ホッパ1下部に設置したスクリ
ューフィーダ2を用い、プロセスに応じて連続的または
間欠的に所要量を抜き取られ、抜き取られた脱水汚泥は
脱水汚泥供給ポンプ3により混合・造粒機能を有する乾
燥機4に供給される。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be specifically described with reference to the drawings and embodiments. FIG. 1 is a flow sheet showing an embodiment of the present invention. Organic raw material sludge, such as sewage sludge, rural settlement drainage sludge, septic tank sludge, human waste sludge, etc., which is a raw material of fertilizer, is dehydrated into dewatered sludge and stored in the dewatered sludge hopper 1. The water content of the dewatered sludge is preferably 50 to 85%. If the water content is too low, it is difficult to uniformly mix the dehydrated sludge with the zeolite, the additional fertilizer component, the pH adjusting component, the deodorant, and / or the soil conditioner to be added as an additional component, and molding and integration are difficult. It is not preferable because it is difficult to perform. If the water content is too high, it will adhere to the mixer, making the operation difficult and increasing the energy consumption. There is no particular limitation on the dehydration method, and an optimal means can be selected and implemented depending on the characteristics of the organic raw material sludge, the operating environment, and the like. A required amount of the stored dewatered sludge is continuously or intermittently extracted according to a process using a screw feeder 2 installed below the dehydration sludge hopper 1. It is supplied to a dryer 4 having a granulating function.

【0007】乾燥機4として、付着性のある固体の混
合、乾燥および造粒の操作を合わせて行うことのできる
装置であれば、連続式でも回分式でも設置条件により適
宜に選択することができる。とくに、減圧下に60ない
し80℃の範囲で操作できる乾燥機を好ましく用いるこ
とができる。この温度範囲では、汚泥中の蛋白質の変性
を避けつつ、殺菌効果を奏するからである。減圧操作
は、乾燥効率を向上しエネルギー消費を節減する利点が
ある。具体的に混合造粒乾燥機として、加熱ジャケット
付横軸パドル式混合機などの容器固定型の攪拌式固体混
合機、もしくは容器回転型の傾斜式縦軸攪拌混合機が好
ましく用いられるが、これらに限られるものではない。
[0007] The dryer 4 can be appropriately selected depending on the installation conditions, whether it is a continuous type or a batch type, as long as it is a device capable of performing operations of mixing, drying and granulation of adherent solids. . In particular, a dryer that can be operated at a temperature of 60 to 80 ° C. under reduced pressure can be preferably used. This is because in this temperature range, a sterilizing effect is achieved while preventing denaturation of proteins in the sludge. The decompression operation has the advantage of improving drying efficiency and reducing energy consumption. Specifically, as a mixing granulation dryer, a container fixed type stirring type solid mixer such as a horizontal axis paddle type mixing machine with a heating jacket, or a container rotating type inclined vertical type stirring mixer is preferably used. It is not limited to.

【0008】脱水汚泥供給ポンプ3の吐出側配管には流
量計あるいは積算流量計5を取り付け、脱水汚泥を連続
供給する場合には脱水汚泥供給ポンプ3の回転数制御に
より時間当たりの供給量を調整し、バッチ運転の場合に
は所定供給量に達すればポンプ3を停止する。さらに、
いずれの場合にも脱水汚泥ホッパ1中の汚泥量を操作可
能範囲内に保てるように、たとえば脱水汚泥ホッパ1に
レベル計を取り付けてスクリューフィーダ2の回転数を
調整できるようにしておくとよい。
A flow meter or an integrated flow meter 5 is attached to the discharge pipe of the dewatered sludge supply pump 3. When the dewatered sludge is continuously supplied, the supply amount per time is adjusted by controlling the rotation speed of the dewatered sludge supply pump 3. Then, in the case of batch operation, when the predetermined supply amount is reached, the pump 3 is stopped. further,
In any case, a level meter is preferably attached to the dewatered sludge hopper 1 so that the rotation speed of the screw feeder 2 can be adjusted so that the amount of sludge in the dewatered sludge hopper 1 can be kept within the operable range.

【0009】本発明製造方法では、連続式であれば脱水
汚泥と同時に、回分式であれば脱水汚泥投入と同時、ま
たは脱水汚泥の投入前または後に、各添加成分の貯留ホ
ッパ6から、あるいは他の適当な手段を利用して各種の
添加成分、たとえば、ゼオライト、追加肥料成分、pH
調整成分、脱臭剤、および/または土質改良剤を乾燥機
4内に投入し、乾燥機4内において脱水汚泥と各投入成
分とを混合し、乾燥し、造粒する。本実施形態例では添
加成分の搬送にニューマチックコンベアが利用されてい
る。8はロータリーフィーダ、9は搬送気体供給用コン
プレッサ、10は搬送気体の排出口のバグフィルタであ
る。
In the production method of the present invention, a continuous type is used simultaneously with the dewatered sludge, a batch type is used simultaneously with the input of the dewatered sludge, or before or after the input of the dehydrated sludge, from the storage hopper 6 for each additive component, or Various suitable components such as zeolite, additional fertilizer component, pH
The adjusting component, the deodorant, and / or the soil conditioner are charged into the dryer 4, and the dewatered sludge is mixed with each component in the dryer 4, dried, and granulated. In this embodiment, a pneumatic conveyor is used to transport the additional components. 8 is a rotary feeder, 9 is a carrier gas supply compressor, and 10 is a bag filter at the outlet of the carrier gas.

【0010】前記の添加成分は、需要者の要求、品質向
上、処理操作の効率化の目的で適宜に選択され、必要量
が加えられる。添加成分として具体的には、ゼオライ
ト、生石灰、消石灰、微粉炭、塩化カリウム、リン酸ナ
トリウム、リン酸カリウム、粉末尿素などがあげられ
る。これらの添加成分のうち、ゼオライトは、カチオン
交換基を有しリンなどをイオン交換して長期間の施肥効
果を付与する。また、通気性などの土壌改良効果の他、
アンモニアなどの臭気成分を吸着するので施肥時および
施肥後の臭気対策にも効果的である。また、生石灰は、
酸性土壌用の肥料に使用されるが、水との発熱反応によ
り乾燥速度を増加する効果もある。消石灰を用いること
もできる。微粉炭はC/N比が小さい場合のカーボンの
補給および臭気対策に寄与することができる。また、塩
化カリウム、リン酸ナトリウム、リン酸カリウム、粉末
尿素などは、肥料成分の調整に利用される。
[0010] The above-mentioned additive components are appropriately selected for the purpose of demands of customers, quality improvement and efficiency of processing operations, and necessary amounts are added. Specific examples of the additional component include zeolite, quicklime, slaked lime, pulverized coal, potassium chloride, sodium phosphate, potassium phosphate, and powdered urea. Among these additional components, zeolite has a cation exchange group and ion-exchanges phosphorus or the like to provide a long-term fertilizing effect. In addition, other than soil improvement effects such as air permeability,
Since it absorbs odor components such as ammonia, it is also effective for odor control during and after fertilization. Also, quicklime is
Used as a fertilizer for acidic soils, it also has the effect of increasing the drying rate due to the exothermic reaction with water. Slaked lime can also be used. Pulverized coal can contribute to carbon replenishment and odor control when the C / N ratio is small. Potassium chloride, sodium phosphate, potassium phosphate, powdered urea and the like are used for adjusting fertilizer components.

【0011】[0011]

【実施例】本発明を実施例により具体的に説明する。下
水汚泥をベルトプレスを用いて、含水率が76.7%の
脱水汚泥にした。この脱水汚泥35kgをゼオライト
(日東ゼオライト2号:日東粉化工業(株)製)ととも
に、混合・造粒機能を有する乾燥機として利用した減圧
バッチ式乾燥機(R08vac:日本アイリッヒ(株)
製)に投入し、粒径4mmの芝生用肥料を造粒目標に混
合、乾燥、造粒した。混合物の含水率は58.3%であ
った。乾燥機内容物の温度を60℃、圧力600mmb
arに維持し、2.05時間、混合、乾燥、造粒操作を
行い、有機汚泥肥料を製造した。得られた有機汚泥肥料
は26.18kgであって、粒径4mm以上が42.9
重量%、4mm以下が57.1%、かさ密度は0.66
であった。また、これらの操作中、乾燥機減圧ポンプ吐
出側で3点比較式臭気袋法(平成4年環境庁告示第92
号の記載による)により測定した排気の臭気濃度は、1
740であった。
EXAMPLES The present invention will be specifically described with reference to examples. The sewage sludge was converted into dehydrated sludge having a water content of 76.7% using a belt press. 35 kg of this dewatered sludge was used together with zeolite (Nitto Zeolite No. 2: manufactured by Nitto Powder Chemical Co., Ltd.) together with a vacuum batch dryer (R08vac: Nippon Eirich Co., Ltd.) which was used as a dryer having a mixing and granulating function.
Manufactured), and a lawn fertilizer having a particle size of 4 mm was mixed, dried and granulated for the purpose of granulation. The water content of the mixture was 58.3%. The temperature of the contents of the dryer is 60 ° C and the pressure is 600 mmb.
The mixture was maintained at ar and mixed, dried and granulated for 2.05 hours to produce an organic sludge fertilizer. The obtained organic sludge fertilizer was 26.18 kg and had a particle diameter of 4 mm or more of 42.9.
Weight%, 47.1% or less 57.1%, bulk density 0.66
Met. In addition, during these operations, a three-point comparison odor bag method (notified by the Environment Agency in 92
The odor concentration of the exhaust gas measured according to
740.

【0012】[0012]

【発明の効果】本発明では脱水汚泥と各添加成分との混
合、乾燥、造粒を同時に行う。各成分が適度の含水率の
もと、同一条件で効率的かつ十分に混合されて乾燥され
るので、得られる製品は均質である。また各成分が相互
になじんで混じり合い一体化して乾燥、成形されている
ので、相乗的な施肥効果を期待できる。本発明製造方法
では、特別の理由のない限り、任意の所要添加成分を任
意の割合で添加することができる。たとえばゼオライト
は、さらに操業中の臭気発散を抑制する効果も奏する。
多機能装置を利用し各操作が適度の含水率で行われるの
で、製造工程で装置などに脱水汚泥が付着して操作を困
難にすることはなく、混合物の見掛上の含水率が低下
し、スラリー状にならないため伝熱面が増加し、乾燥効
率が増加するので、エネルギー消費量を節減することが
できる。肥料として使用先の条件や要求に応じた成分を
汚泥と同時に混合、乾燥および造粒を行うので、経済的
で付加価値の高い汚泥肥料を得ることができる。
According to the present invention, mixing, drying and granulation of the dehydrated sludge and each additive component are performed simultaneously. The resulting product is homogeneous because each component is efficiently and thoroughly mixed and dried under the same conditions and with a moderate moisture content. In addition, since the components are mixed with each other, mixed, dried and molded, a synergistic fertilizing effect can be expected. In the production method of the present invention, any necessary additive components can be added in any ratio unless there is a special reason. For example, zeolite also has the effect of suppressing odor emission during operation.
Since each operation is performed with an appropriate water content using a multi-function device, dewatered sludge does not adhere to the device during the manufacturing process, making operation difficult, and the apparent water content of the mixture decreases. Since the slurry does not form a slurry, the heat transfer surface increases, and the drying efficiency increases, so that the energy consumption can be reduced. As the fertilizer mixes, dries and granulates the components according to the conditions and requirements of the place of use, sludge fertilizer can be obtained economically and with high added value.

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

【図1】本発明の一実施形態例を示すフローシートFIG. 1 is a flow sheet showing an embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1:脱水汚泥ホッパ 2:スクリューフィーダ 3:脱水汚泥供給ポンプ 4:混合・造粒機能を有す
る乾燥機 5:(積算)流量計 6:添加成分貯留ホッパ 7:乾燥機内減圧ポンプ 8:ロータリーフィーダ 9:搬送気体供給用コンプレッサ 10:バグフィル
1: Dewatered sludge hopper 2: Screw feeder 3: Dewatered sludge supply pump 4: Dryer having mixing / granulation function 5: (Integrated) flow meter 6: Additive component storage hopper 7: Dryer inside vacuum dryer 8: Rotary feeder 9 : Carrier gas supply compressor 10: Bag filter

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 FI C05G 3/04 C05G 3/04 5/00 5/00 ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 6 Identification code FI C05G 3/04 C05G 3/04 5/00 5/00

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】有機系の汚泥を含有水分率が50〜85重
量%(湿量基準)に脱水して脱水汚泥とし、得られた脱
水汚泥を混合、造粒機能を併有する乾燥機に投入すると
ともに添加成分としてゼオライト、追加肥料成分、pH
調整成分、脱臭剤、および/または土質改良剤を投入
し、乾燥機内において脱水汚泥と添加成分とを混合し、
乾燥し、造粒することを特徴とする有機汚泥肥料の製造
方法。
1. An organic sludge is dehydrated to a dewatered sludge having a water content of 50 to 85% by weight (wet amount basis), and the obtained dewatered sludge is mixed and poured into a dryer having a granulating function. Zeolite, additional fertilizer component, pH
The adjusting component, the deodorant, and / or the soil conditioner are added, and the dehydrated sludge and the additional component are mixed in the dryer,
A method for producing an organic sludge fertilizer, comprising drying and granulating.
【請求項2】乾燥操作を60ないし80℃の範囲内で実
施することを特徴とする請求項1または2記載の有機汚
泥肥料の製造方法。
2. The method for producing an organic sludge fertilizer according to claim 1, wherein the drying operation is carried out within a range of 60 to 80 ° C.
JP9104419A 1997-04-22 1997-04-22 Production method of organic sludge fertilizer Pending JPH10291877A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9104419A JPH10291877A (en) 1997-04-22 1997-04-22 Production method of organic sludge fertilizer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9104419A JPH10291877A (en) 1997-04-22 1997-04-22 Production method of organic sludge fertilizer

Publications (1)

Publication Number Publication Date
JPH10291877A true JPH10291877A (en) 1998-11-04

Family

ID=14380183

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9104419A Pending JPH10291877A (en) 1997-04-22 1997-04-22 Production method of organic sludge fertilizer

Country Status (1)

Country Link
JP (1) JPH10291877A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100320367B1 (en) * 1999-05-21 2002-01-15 이상배 Manufacturing method and apparatus of waste organic
WO2008053086A2 (en) * 2006-10-27 2008-05-08 Michel Mazon Method for treating domestic waste
JP2011046576A (en) * 2009-08-28 2011-03-10 Taiheiyo Cement Corp Fertilizer, method and apparatus for manufacturing the same
KR20190026495A (en) * 2017-09-05 2019-03-13 (주) 화이미제약 Food waste treatment appratus

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100320367B1 (en) * 1999-05-21 2002-01-15 이상배 Manufacturing method and apparatus of waste organic
WO2008053086A2 (en) * 2006-10-27 2008-05-08 Michel Mazon Method for treating domestic waste
WO2008053086A3 (en) * 2006-10-27 2008-07-03 Michel Mazon Method for treating domestic waste
JP2010507475A (en) * 2006-10-27 2010-03-11 ミシェル・マゾン General waste treatment methods
US8858671B2 (en) 2006-10-27 2014-10-14 Michel Mazon Method for treating domestic waste
JP2011046576A (en) * 2009-08-28 2011-03-10 Taiheiyo Cement Corp Fertilizer, method and apparatus for manufacturing the same
KR20190026495A (en) * 2017-09-05 2019-03-13 (주) 화이미제약 Food waste treatment appratus

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