JPH05194071A - System for producing fertilizer - Google Patents

System for producing fertilizer

Info

Publication number
JPH05194071A
JPH05194071A JP4031561A JP3156192A JPH05194071A JP H05194071 A JPH05194071 A JP H05194071A JP 4031561 A JP4031561 A JP 4031561A JP 3156192 A JP3156192 A JP 3156192A JP H05194071 A JPH05194071 A JP H05194071A
Authority
JP
Japan
Prior art keywords
fertilizer
dried
hot air
organic
chemical
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP4031561A
Other languages
Japanese (ja)
Other versions
JP2519623B2 (en
Inventor
Tsuguo Suzuki
嗣生 鈴木
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP4031561A priority Critical patent/JP2519623B2/en
Publication of JPH05194071A publication Critical patent/JPH05194071A/en
Application granted granted Critical
Publication of JP2519623B2 publication Critical patent/JP2519623B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime 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

Abstract

PURPOSE:To obtain an excellent fertilizer provided only with the advantages of both a chemical fertilizer and an organic substance fertilizer, extremely mild for the roots of plants and free from pollution of rivers by making the chemical fertilizer chemically adsorbed on an organic waste to moderate the generation of the fertilizing effect and retard the dissolution time of the fertilizer in water, and further, on the production of the fertilizer, to enhance a heat exchange rate by a continuous drying treatment and on the application of the fertilizer, to enable the mechanical scattering of the fertilizer and save the labor by shaping the fertilizer into a pellet-like shape. CONSTITUTION:A mixture of an organic waste with a chemical fertilizer is aerobically fermented, and the produced organic fertilizer is brought into contact with hot air in the turbulent state with a baffle, while being stirred with stirring projections disposed in an oven 12 and controlled in the rotation. The dried fertilizer is shaped into a pellet-like shape with a pellet mill through a grinder, and subsequently cooled and solidified in a cooling machine.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は産業廃棄物の一種である
有機質廃棄物の有効利用を図ると共に、有機質肥料と化
学肥料との中間的特性を具有する肥料を製造する肥料製
造システムに関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a fertilizer manufacturing system for effectively utilizing organic waste, which is a type of industrial waste, and for producing a fertilizer having intermediate characteristics between organic fertilizer and chemical fertilizer. is there.

【0002】[0002]

【従来の技術】従来、産業廃棄物である有機質廃棄物と
しては、牛、豚、鶏等の畜糞尿、ビールカス、コヒーカ
ス、オカラ、オガクズ等の動物性廃棄物、植物性廃棄物
の種々のものが存在しているも、かかる有機質廃棄物は
それぞれの製造業者毎に個別に廃棄処理しているのが現
状であって、土壌改良剤としての複合機能を有する肥料
としては全くなく、有機質廃棄物を有効的に処理する方
法が望まれている。
2. Description of the Related Art Conventionally, various organic wastes such as cattle, pigs and chickens, animal wastes such as beer dregs, cohesives, okara and sawdust, and plant wastes have been conventionally used as organic wastes. However, such organic waste is currently disposed of separately by each manufacturer, and it is not a fertilizer with a combined function as a soil conditioner. What is desired is a method of effectively treating

【0003】又、ゴルフ場におけるフェアーウエー、テ
ィーグランド等の芝用に使用される肥料としては、窒素
肥料、リン酸肥料等の化学肥料が使用されているも、然
しながら化学肥料は速効性を有している反面、水に溶け
て流れて損失しやすいため、必要以上使用する結果とな
り、このため窒素、リン酸分等がゴルフ場に隣接する河
川に流れ込み汚染すると共に、ヘドロ状となって蓄積し
て公害の原因となる欠点を有していた。
Further, as fertilizers used for turf such as fairways and tee grounds at golf courses, chemical fertilizers such as nitrogen fertilizers and phosphoric acid fertilizers are used. However, chemical fertilizers have a rapid effect. On the other hand, since it dissolves in water and easily flows and is lost, it results in excessive use, and as a result, nitrogen and phosphoric acid, etc. flow into the river adjacent to the golf course and contaminate it, and accumulate as sludge. Then, it had the drawback of causing pollution.

【0004】[0004]

【発明が解決しようとする課題】本発明は有機質廃棄物
と化学肥料とを化学的に吸着させて有機化し、肥効を緩
徐にして根に優しい肥料にすると共に、水に溶ける時間
を遅延させ、河川の環境汚染等を未然に無くし、化学肥
料と有機質肥料との利点のみを兼ね備えた優れた肥料と
し、又製造時においては熱交換率を高くし、高い効率に
て連続乾燥処理出来、又施肥時においてはペレット状に
成形して機械散布を可能にし、省力化を図る肥料を製造
可能とした肥料製造システムを提供せんとするものであ
る。
DISCLOSURE OF THE INVENTION According to the present invention, organic wastes and chemical fertilizers are chemically adsorbed to be organically adsorbed, the fertilization effect is slowed to be a root-friendly fertilizer, and the time to dissolve in water is delayed. , It is an excellent fertilizer that eliminates environmental pollution of rivers and has only the advantages of chemical fertilizers and organic fertilizers. It also has a high heat exchange rate at the time of production and can be continuously dried with high efficiency. It is intended to provide a fertilizer production system capable of producing fertilizers which are manufactured into pellets at the time of fertilization so that they can be mechanically sprayed to save labor.

【0005】[0005]

【課題を解決するための手段】本発明は上記従来技術に
基づく有機質廃棄物の個別廃棄処理、化学肥料による公
害の原因等の課題に鑑み、有機質廃棄物と化学肥料とを
化学的に吸着させて一体的に有機化した肥料を、一貫し
た製造工程により製造し、肥料としての高付加価値を具
有させると共に、有機質廃棄物の有効利用を図ることを
要旨とする肥料製造システムを提供して上記欠点を解消
せんとしたものである。
SUMMARY OF THE INVENTION The present invention chemically adsorbs an organic waste and a chemical fertilizer in view of the problems such as the individual disposal treatment of the organic waste based on the above-mentioned conventional technique and the cause of pollution by the chemical fertilizer. Providing a fertilizer manufacturing system that manufactures integrated and organically fertilizers through a consistent manufacturing process, has high added value as fertilizer, and effectively utilizes organic waste. It does not eliminate the drawbacks.

【0006】以下本発明の肥料製造システムは、醗酵さ
せて肥料化し、乾燥処理し、成形し、しかる後冷却固化
して肥料を製造する。
In the fertilizer production system of the present invention, the fertilizer is produced by fermenting to fertilize, drying and molding, and then cooling and solidifying.

【0007】又、肥料化については有機質廃棄物に所定
量の化学肥料を添加し、しかる後攪拌混合しながら好気
性醗酵させている。
For fertilization, a predetermined amount of chemical fertilizer is added to organic waste, and then aerobically fermented while mixing with stirring.

【0008】又、上記有機質廃棄物としては、牛、豚、
鶏等の畜糞尿、ビールカス、コヒーカス、オカラ、オガ
クズ、ゼオライト、卵殻、貝殻等の動物性廃棄物、植物
性廃棄物があり、又化学肥料(無機質肥料)としては、
窒素肥料、リン酸肥料、カリ肥料等があり、有機質廃棄
物の少なくとも一種以上適宜混合して主原料と成し、該
主原料に化学肥料の少なくとも一種以上を適宜割合にて
添加している。
[0008] The above organic waste includes cattle, pigs,
There are animal wastes such as chicken manure, beer dregs, cohesives, okara, sawdust, zeolite, eggshells, shells, and plant wastes, and as chemical fertilizers (inorganic fertilizers),
There are nitrogen fertilizers, phosphate fertilizers, potassium fertilizers, etc., and at least one or more kinds of organic waste are appropriately mixed to form a main raw material, and at least one or more chemical fertilizers are added to the main raw material in an appropriate ratio.

【0009】又、上記乾燥処理としては、回転制御され
る炉体内に設ける撹拌突条により前記肥料を攪拌させな
がら邪魔板により乱流状態と成した熱風に接触させて乾
燥処理している。
In the drying process, the fertilizer is stirred by a stirring ridge provided in a furnace body whose rotation is controlled, and is brought into contact with hot air in a turbulent state by a baffle plate to perform the drying process.

【0010】又、乾燥処理された肥料を粉砕機を介して
ペレットミルによりペレット状に成形し、しかる後冷却
機に投入して冷却して固化する様にしている。
Further, the dried fertilizer is shaped into pellets by a pellet mill through a crusher, and then put into a cooler to be cooled and solidified.

【0011】[0011]

【作用】本発明にあっては、好気性醗酵が進むにつれ、
高含水部分の小団塊も次第に乾燥し、醗酵後期には小団
塊も細粒化されると共に、微生物の働きにより有機質廃
棄物が醗酵した有機醗酵生成物と化学肥料とを化学吸着
させて一体的に有機化し、攪拌状態の肥料に乱流状態の
熱風を接触させて、高い熱交換率にて乾燥処理し、この
乾燥処理された肥料をペレット状に成形し、施肥時の取
扱を容易と成す肥料を一貫して連続生産する。
In the present invention, as aerobic fermentation progresses,
The small nodules in the high water content are gradually dried, and in the latter half of the fermentation, the small nodules are also finely granulated, and the organic fermentation products produced by the fermentation of organic waste by the action of microorganisms and the chemical fertilizer are chemically adsorbed into an integrated body. The fertilizer in organic form is mixed with turbulent hot air in contact with the fertilizer in the agitated state, and the fertilizer is dried at a high heat exchange rate. The dried fertilizer is molded into pellets to facilitate handling during fertilization. Consistent continuous production of fertilizer.

【0012】[0012]

【実施例】以下本発明の一実施例を図面に基づいて説明
すると、1は本発明に係る肥料製造システムであり、該
肥料製造システム1の起点には醗酵槽2を設け、かかる
醗酵槽2により原料を醗酵処理している。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below with reference to the drawings. 1 is a fertilizer manufacturing system according to the present invention, a fermenter 2 is provided at the starting point of the fertilizer manufacturing system 1, and the fermenter 2 The raw material is processed by fermentation.

【0013】この醗酵槽2は屋根3を採光性を有するガ
ラス、プラスチック等の材質にて囲まれる温室効果を具
有させる建屋4内に、該建屋4の原料搬入口5から肥料
排出口6にわたってコンクリート製等にて形成される側
壁7、7aを設けて上方開口する横型の槽本体8を形成
し、該槽本体8の原料搬入口5と肥料排出口6間を移動
自在と成す撹拌混合機9を設けている。
This fermenter 2 has a roof 3 surrounded by a material such as glass and plastic having a daylighting property, in a building 4 having a greenhouse effect, and from the raw material carry-in port 5 of the building 4 to a fertilizer discharge port 6 concrete. An agitating mixer 9 which is provided with side walls 7 and 7a formed by manufacturing, forms a horizontal tank main body 8 having an upward opening, and is movable between a raw material carry-in port 5 and a fertilizer discharge port 6 of the tank main body 8. Is provided.

【0014】尚、撹拌混合機9は槽本体8内の推積原料
Wを撹拌混合するスクリュー式、スクープ式等の適宜機
構を採用することも可能である。
The stirring and mixing machine 9 may employ an appropriate mechanism such as a screw type or a scooping type for stirring and mixing the raw material W to be deposited in the tank body 8.

【0015】又、槽本体8の底部からは空気を通気でき
る通気機構10を有し、通気によって好気性醗酵を促進さ
せている。
Further, from the bottom of the tank body 8 is provided a ventilation mechanism 10 capable of ventilating air to promote aerobic fermentation.

【0016】11は醗酵槽2により醗酵処理された肥料を
乾燥させる乾燥処理装置であり、該乾燥処理装置11は円
筒状の炉体12が水平方向に回転自在に設置され、かかる
炉体12の一端側に肥料投入口13を設けると共に、他端側
に乾燥肥料取出口14を設けている。
Reference numeral 11 denotes a drying treatment device for drying the fertilizer fermented by the fermentation tank 2. The drying treatment device 11 has a cylindrical furnace body 12 rotatably installed in the horizontal direction. A fertilizer inlet 13 is provided on one end side, and a dry fertilizer outlet 14 is provided on the other end side.

【0017】尚、本実施例では炉体12の他端側を適宜下
方と成す様に若干炉体12を傾斜させている。
In the present embodiment, the furnace body 12 is slightly inclined so that the other end side of the furnace body 12 is appropriately downward.

【0018】15、15a …は炉体12内に設ける撹拌突条で
あり、該撹拌突条15、15a …は炉体12の内壁16における
円周方向に所定間隔にて配列するものにして、炉体12の
軸方向にわたって多数条設けている。
Reference numerals 15 and 15a are stirring ridges provided in the furnace body 12, and the stirring ridges 15 and 15a are arranged at predetermined intervals in the circumferential direction on the inner wall 16 of the furnace body 12. A large number of lines are provided in the axial direction of the furnace body 12.

【0019】17、17a …は炉体12内に設ける弓形状に形
成した邪魔板であり、該邪魔板17、17a …は炉体12の内
壁16における軸方向に所定間隔にて配列するものにし
て、炉体12の軸方向に移行するに従って円周方向に所定
角度順次変位させる様に、邪魔板17、17a …の円弧側を
内壁16に固定し、かかる多数の邪魔板17、17a …の弦側
にて炉体12内の軸方向に多角状の熱風通路Lを形成して
いる。
Numerals 17, 17a are arcuate baffle plates provided in the furnace body 12, and the baffle plates 17, 17a are arranged in the inner wall 16 of the furnace body 12 at predetermined intervals in the axial direction. The arc side of the baffles 17, 17a is fixed to the inner wall 16 so that the furnace body 12 is displaced in the circumferential direction by a predetermined angle in sequence as it moves in the axial direction, and the baffles 17, 17a. A polygonal hot air passage L is formed in the axial direction in the furnace body 12 on the chord side.

【0020】18は乾燥肥料取出口14に設ける開閉扉であ
り、該開閉扉18は乾燥肥料取出口14の上下に設けるガイ
ド部材19、19a に扉体20をスライド自在に設け、該扉体
20にシリンダー等の駆動源21を連結し、該駆動源21によ
って扉体20をスライド開閉作動させ、乾燥肥料取出口14
の開閉度合を調整制御している。
Reference numeral 18 denotes an opening / closing door provided at the dry fertilizer outlet 14. The opening / closing door 18 is provided with guide members 19, 19a provided above and below the dry fertilizer outlet 14, and a door body 20 is slidably provided.
A drive source 21 such as a cylinder is connected to the drive source 20, and the door body 20 is slid by the drive source 21 to open and close the dry fertilizer outlet 14
The degree of opening and closing is adjusted and controlled.

【0021】又、乾燥肥料取出口14には、該乾燥肥料取
出口14より排出された乾燥した肥料を他に搬送する搬送
コンベア22を設けている。
Further, the dry fertilizer outlet 14 is provided with a conveyor 22 for transporting the dried fertilizer discharged from the dry fertilizer outlet 14 to another.

【0022】尚、乾燥肥料取出口14の開閉度合に応じて
外部へ排出される乾燥した肥料の排出量を測定する適宜
なる排出量測定装置23を設けることも可能である。
It is also possible to provide an appropriate discharge amount measuring device 23 for measuring the discharge amount of the dried fertilizer discharged to the outside according to the opening / closing degree of the dry fertilizer outlet 14.

【0023】24は原料投入ホッパーであり、該原料投入
ホッパー24は炉体12の肥料投入口13に連設すると共に、
肥料を肥料投入口13より炉体12内に投入する手段である
適宜モーター等の駆動源25によって作動する移送スクリ
ュー26を設け、該移送スクリュー26によりシューター27
を介して肥料を炉体12内に投入する様にしている。
Reference numeral 24 is a raw material charging hopper, and the raw material charging hopper 24 is connected to the fertilizer charging port 13 of the furnace body 12 and
A transfer screw 26 that is operated by a drive source 25 such as a motor, which is a means for charging fertilizer into the furnace body 12 through the fertilizer charging port 13, is provided.
The fertilizer is introduced into the furnace body 12 via the.

【0024】又、シューター27の入口側には開閉自在な
るシャッター27a が設けられ、このシャッター27a は後
述する熱風供給装置29にて送給される熱風によって閉鎖
し、原料投入ホッパー24より移送スクリュー26を介して
送られる肥料によって開口される。
A shutter 27a which can be opened and closed is provided on the entrance side of the shooter 27, and the shutter 27a is closed by hot air sent by a hot air supply device 29, which will be described later. It is opened by fertilizer that is sent through.

【0025】尚、肥料投入口13より炉体12内に投入され
る投入量を測定する投入量測定装置28を肥料投入口13に
関連する位置に設けることも可能である。
It is also possible to provide an input amount measuring device 28 for measuring the input amount into the furnace body 12 from the fertilizer input port 13 at a position related to the fertilizer input port 13.

【0026】29は熱風供給装置であり、該熱風供給装置
29は炉体12の他端側に設けられた熱風導入口30に接続さ
れ、上記邪魔板17、17a …にて形成された多角状の熱風
通路Lに熱風を送給している。
29 is a hot air supply device,
Reference numeral 29 is connected to a hot air inlet 30 provided on the other end side of the furnace body 12 and supplies hot air to the polygonal hot air passage L formed by the baffles 17, 17a.

【0027】又、熱風供給装置29は炉体12内の他端側に
高温温度センサー31を設けると共に、一端側には低温温
度センサー32を設け、熱風導入口30側では約200℃以
上、肥料投入口13側では外気温度より高く、水の沸騰点
より低くなる様に熱風の送給量を制御している。
Further, the hot air supply device 29 is provided with a high temperature sensor 31 on the other end side of the furnace body 12 and a low temperature sensor 32 on one end side thereof. At the inlet 13 side, the hot air supply amount is controlled so that it is higher than the outside air temperature and lower than the boiling point of water.

【0028】尚、本実施例では肥料投入口13側の温度は
約70℃程度にて制御している。
In this embodiment, the temperature on the fertilizer inlet 13 side is controlled at about 70 ° C.

【0029】33は集塵装置であり、該集塵装置33は炉体
12の一端側に排気ダクト34を設け、該排気ダクト34を外
部に設けた集塵処理塔35の中間部位に接続し、炉体12内
と集塵処理塔35内とを連通させている。
Reference numeral 33 is a dust collector, and the dust collector 33 is a furnace body.
An exhaust duct 34 is provided on one end side of 12, and the exhaust duct 34 is connected to an intermediate portion of a dust collection treatment tower 35 provided outside to communicate the inside of the furnace body 12 and the inside of the dust collection treatment tower 35.

【0030】又、集塵処理塔35内の適宜上方部位には水
を噴霧若しくはシャワー状に、該集塵処理塔35の内壁36
側へ向かって噴出させる拡散ノズル37を設け、一方集塵
処理塔35の適宜下方部位には内壁36に付着し、流下する
スラリー状の廃棄物を受承する様に排出コンベア38を連
設している。
Further, the inner wall 36 of the dust collection treatment tower 35 is sprayed or showered with water at an appropriate upper portion in the dust collection treatment tower 35.
A diffusion nozzle 37 for ejecting toward the side is provided, and on the other hand, a discharge conveyor 38 is continuously provided so as to adhere to the inner wall 36 at an appropriately lower portion of the dust collection processing tower 35 and receive the flowing slurry-like waste. ing.

【0031】尚、排出コンベア22より後述する粉砕機39
への乾燥した肥料の搬送過程において、必要に応じてカ
ルシウム、カリウム、鉄、マンガン、コバルト、ヨウ素
等のミネラルを所定量添加しても良く、又微生物(醗酵
菌)若しくは三菱商事株式会社製のヒューマス活植源
(商標)を必要に応じて所定量添加しても良い。
A crusher 39 which will be described later from the discharge conveyor 22
In the process of transporting the dried fertilizer to, if necessary, a predetermined amount of minerals such as calcium, potassium, iron, manganese, cobalt and iodine may be added, or a microorganism (fermentation bacterium) or Mitsubishi Corporation A certain amount of Humus Active Plant Source (trademark) may be added if necessary.

【0032】粉砕機39は乾燥した肥料を粉砕するボール
ミル、ロッドミル等の適宜機構からなるものにして、粉
砕機39の入口側を排出コンベア22に連設すると共に、出
口側は粉砕中に発生する粉塵を除去する集塵機40を介し
て粉砕した肥料を収容する粉砕肥料ホッパー41に連設し
ている。
The crusher 39 is made up of an appropriate mechanism such as a ball mill or a rod mill for crushing dried fertilizer, the inlet side of the crusher 39 is connected to the discharge conveyor 22, and the outlet side is generated during crushing. A dust collector 40 for removing dust is connected to a crushed fertilizer hopper 41 for storing crushed fertilizer.

【0033】尚、粉砕機39より粉砕肥料ホッパー41への
粉砕した肥料の搬送過程において、必要に応じて加水す
ると共に、土壌菌(好気性有効菌)を添加している。
In addition, in the process of transporting the crushed fertilizer from the crusher 39 to the crushed fertilizer hopper 41, water is added if necessary and soil bacteria (aerobic effective bacteria) are added.

【0034】42は粉砕肥料ホッパー41より供給される粉
砕した肥料をペレット状に造粒するペレットミルであ
り、該ペレットミル42のスクリューフィダー43における
下流側に粉砕肥料ホッパー41の出口側を連設すると共
に、後述する冷却機44にて発生する粉塵をスクリューフ
ィダー43における上流側に適宜搬送手段を介して供給
し、更に後述する選別機45により規格外品のペレット状
の固形肥料をペレットミル42のスクリューフィダー43に
おける中流側に適宜搬送手段を介して供給している。
Reference numeral 42 is a pellet mill for granulating the pulverized fertilizer supplied from the pulverized fertilizer hopper 41 into pellets. The outlet side of the pulverized fertilizer hopper 41 is connected to the downstream side of the screw feeder 43 of the pellet mill 42. In addition, the dust generated in the cooler 44 described later is supplied to the upstream side of the screw feeder 43 through an appropriate conveying means, and further, the sorting machine 45 described below pellets the solid fertilizer in a nonstandard product into a pellet mill 42. It is supplied to the middle stream side of the screw feeder 43 of FIG.

【0035】尚、粉砕肥料ホッパー41よりペレットミル
42のスクリューフィダー43へ粉砕した肥料を供給する過
程において、所定量の木酢液を添加し施肥した際にミミ
ズ、コガネ虫等の発生を未然に防止させている。
The crushed fertilizer hopper 41 is used for pellet milling.
In the process of supplying the crushed fertilizer to the screw feeder 43 of 42, when a predetermined amount of wood vinegar is added and fertilized, the generation of earthworms, chafers and the like is prevented in advance.

【0036】尚、ペレットミル42のスクリューフィダー
43には適宜なるセンサー(図示せず)を設け、スクリュ
ーフィダー43に先行して投入されるリサイクルされた冷
却機44からの粉塵、選別機45からの規格外品との投入量
を測定し、ペレットミル42の処理能力に対し粉砕肥料ホ
ッパー41より供給される粉砕した肥料の供給量を制御
し、ペレットミル42の過負荷を防止している。
The screw feeder of the pellet mill 42
43 is provided with an appropriate sensor (not shown) to measure the amount of dust from the recycled cooler 44 that is charged prior to the screw feeder 43 and the amount of nonstandard products from the sorter 45, The overload of the pellet mill 42 is prevented by controlling the supply amount of the pulverized fertilizer supplied from the pulverized fertilizer hopper 41 with respect to the processing capacity of the pellet mill 42.

【0037】又、ペレットミル42にて造粒する際に加水
する水分中には必要に応じて土壌菌(好気性有効菌)を
添加してもよい。
If necessary, soil bacteria (aerobic effective bacteria) may be added to the water to be added when granulating with the pellet mill 42.

【0038】尚、ペレットミル42としては、円筒の外周
に多数の成形孔があり、円筒の内壁に沿って回転しなが
ら回るロールによってその成形孔から材料を押し出すも
の(図示せず)、又円筒に詰められた材料をプランジャ
ーで成形孔から材料を押し出すもの(図示せず)等適宜
機構のものであれば良い。
The pellet mill 42 has a large number of forming holes on the outer circumference of the cylinder, and the material is extruded from the forming holes by a roll that rotates while rotating along the inner wall of the cylinder (not shown). Any material may be used as long as it has a proper mechanism, such as a material (not shown) in which the material packed in the above is pushed out from a molding hole by a plunger.

【0039】又、冷却機44は空気等の冷却媒体に固形肥
料を接触させて所定温度まで冷却するものにして、その
入口側はペレットミル42の出口側に連設すると共に、冷
却処理中にて発生する粉塵を集塵し、かかる粉塵をペレ
ットミル42のスクリューフィダー43における上流側に供
給している。
The cooler 44 is designed to bring the solid fertilizer into contact with a cooling medium such as air to cool it to a predetermined temperature. The inlet side of the cooler 44 is connected to the outlet side of the pellet mill 42, and during cooling treatment. The dust generated is collected, and the dust is supplied to the upstream side of the screw feeder 43 of the pellet mill 42.

【0040】又、選別機45はペレットミル42により成形
された固形肥料を規格品と規格外品とに選別する振動フ
ルイ等からなるものにして、そのフルイ網46の上方には
遠赤外線を放射する加熱器47を設けると共に、規格外品
をペレットミル42のスクリューフィダー43における中流
側に適宜搬送手段を介して供給している。
Further, the sorting machine 45 is made of a vibrating screen or the like for sorting the solid fertilizer formed by the pellet mill 42 into standard products and nonstandard products, and emits far infrared rays above the screening screen 46. In addition to providing the heater 47, the nonstandard product is appropriately supplied to the midstream side of the screw feeder 43 of the pellet mill 42 through the conveying means.

【0041】又、選別機45によりふるい分けされた規格
品の固形肥料は10キロ詰めの小袋詰器48と、20キロ
詰めの大袋詰器49へと選択分離供給され、その後はロボ
ットパレタイザー50を介してパレット(図示せず)上に
所定量載置される。
The standard solid fertilizer screened by the sorting machine 45 is selectively separated and supplied to a small bag packing machine 48 of 10 kg and a large bag packing machine 49 of 20 kg, and then through a robot palletizer 50. A predetermined amount is placed on a pallet (not shown).

【0042】次に本発明に係る肥料製造システムによる
製造方法の各工程について説明すると、先ず、建屋4に
おける槽本体8の原料搬入口5より有機質廃棄物と所定
量の化学肥料を添加した原料を推積し、かかる推積原料
Wを撹拌混合機9により順次槽本体8の終端側である肥
料排出口6まで撹拌と混合を繰り返し処理させながら、
適度な空気を通気機構10より供給すると共に、腐植物質
(土壌菌)が含まれる水を加えて微生物である好気性菌
(活性菌)によって所定期間醗酵させて肥料と成すので
ある。
Next, each step of the manufacturing method by the fertilizer manufacturing system according to the present invention will be described. First, the organic waste and a raw material to which a predetermined amount of chemical fertilizer is added are introduced from the raw material inlet 5 of the tank body 8 in the building 4. While being piled up, the piled up raw material W is repeatedly stirred and mixed by the stirrer / mixer 9 up to the fertilizer discharge port 6 which is the terminal side of the tank body 8,
A proper amount of air is supplied from the aeration mechanism 10, water containing humic substances (soil fungi) is added, and fermented by aerobic bacteria (active bacteria) which are microorganisms for a predetermined period to form fertilizer.

【0043】又、上記有機質廃棄物としては、牛、豚、
鶏等の畜糞尿、ビールカス、コヒーカス、オカラ、オガ
クズ、ゼオライト、卵殻、貝殻等の動物性廃棄物、植物
性廃棄物があり、又化学肥料(無機質肥料)としては、
窒素肥料、リン酸肥料、カリ肥料等があり、有機質廃棄
物の少なくとも一種以上適宜混合して主原料と成し、該
主原料に化学肥料の少なくとも一種以上を適宜割合にて
添加して推積原料Wと成している。
As the organic waste, cattle, pigs,
There are animal wastes such as chicken manure, beer dregs, cohesives, okara, sawdust, zeolite, eggshells, shells, and plant wastes, and as chemical fertilizers (inorganic fertilizers),
There are nitrogen fertilizers, phosphate fertilizers, potash fertilizers, etc., and at least one or more kinds of organic waste are appropriately mixed to form a main raw material, and at least one or more chemical fertilizers are added to the main raw material at an appropriate ratio to obtain a raw material for deposition. It's W.

【0044】上記の様に撹拌混合し所定の醗酵処理が終
了した肥料としては、槽本体8内にて好気性醗酵が進む
につれ、高含水部分の小団塊も次第に乾燥し、醗酵後期
には小団塊も細粒化されると共に、微生物の働きにより
有機質廃棄物が醗酵し細粒化した有機醗酵生成物と化学
肥料とを化学吸着させて一体的に有機化させるのであ
る。
As the fertilizer which has been agitated and mixed as described above and the predetermined fermentation treatment is completed, as the aerobic fermentation progresses in the tank body 8, the small nodules in the high water content portion are gradually dried, and in the latter half of the fermentation, the small agglomerates are gradually dried. The nodule is also finely granulated, and the organic waste is fermented by the action of microorganisms, and the finely granulated organic fermentation product and the chemical fertilizer are chemically adsorbed to be integrally organized.

【0045】そして、上記有機化した肥料は適宜搬送手
段を介して乾燥処理装置11に搬入され乾燥処理される。
Then, the above-mentioned organized fertilizer is carried into the drying treatment device 11 through a conveying means and dried.

【0046】即ち、熱風供給装置29にて所定の温度に加
熱された熱風を炉体12の熱風導入口30より送給すると共
に、炉体12を所定回転速度にて回転させた状態で、原料
投入ホッパー24に有機化された肥料を投入すると、駆動
源25にて作動される移送スクリュー26にて炉体12の肥料
投入口13より連続的若しくは間歇的に順次肥料をシュー
ター27を介して炉体12内に投入する。
That is, while the hot air heated to a predetermined temperature by the hot air supply device 29 is fed from the hot air inlet 30 of the furnace body 12 and the furnace body 12 is rotated at a predetermined rotation speed, When the organic fertilizer is fed into the feeding hopper 24, the fertilizer is continuously or intermittently fed through the shooter 27 from the fertilizer feeding port 13 of the furnace body 12 by the transfer screw 26 operated by the driving source 25. Put into the body 12.

【0047】尚、肥料中には不純物(例えば金属、石
等) が存在しているため、この不純物を分離装置によっ
て除去分離している。
Since impurities (for example, metals, stones, etc.) are present in the fertilizer, these impurities are removed and separated by a separator.

【0048】そして、投入された肥料は、順次乾燥肥料
取出口4側へと移動する過程において、熱風により乾燥
させられ、そして乾燥肥料取出口14より順次搬送コンベ
ア22にて粉砕機39へと搬送される。
Then, the fed fertilizer is dried by hot air in the process of sequentially moving to the dry fertilizer take-out port 4 side, and then sequentially conveyed from the dry fertilizer take-out port 14 to the crusher 39 by the conveyer conveyor 22. To be done.

【0049】又、上記乾燥過程については、炉体12が回
転していることにより、投入された原料が撹拌突条15、
15a …によって掻き上げられ、所定位置にて落下されて
撹拌処理されながら、乾燥肥料取出口14へと移動する過
程で、熱風通路Lを通過する熱風に接触して順次水分が
除去され、而も邪魔板17、17a …が変位して設けられて
いることより、熱風が単純に直線的に熱風通路Lを通過
せずに、各邪魔板17、17a …に衝突して内部にて撹拌乱
流状態と成りながら熱風が排気ダクト34へと移動するこ
ととなり、高い熱交換率で乾燥させるのである。
In addition, in the above-mentioned drying process, since the furnace body 12 is rotating, the charged raw materials are agitated with the stirring ridges 15,
In the process of moving to the dried fertilizer outlet 14 while being scraped up by the 15a, dropped at a predetermined position and stirred, the hot air passing through the hot air passage L is contacted to sequentially remove water, and Since the baffle plates 17, 17a ... Are provided so as to be displaced, the hot air does not simply linearly pass through the hot air passage L but collides with each baffle plate 17, 17a. While being in the state, hot air moves to the exhaust duct 34 and is dried at a high heat exchange rate.

【0050】又、高温温度センサー31、低温温度センサ
ー32により検出された夫々の温度は常に熱風供給装置29
に内装される制御装置(図示せず)に入力され、炉体12
内の原料の量に関係なく常に乾燥肥料取出口14側では約
200℃以上と成すと共に、肥料投入口13側では約70
℃程度と成る様に制御している。
Further, the respective temperatures detected by the high temperature sensor 31 and the low temperature sensor 32 are always hot air supply device 29.
Input to a control device (not shown) installed inside the furnace body 12
Regardless of the amount of raw material inside, the dry fertilizer outlet 14 side always achieves a temperature of approximately 200 ° C or higher, and the fertilizer inlet 13 side approximately 70 ° C.
The temperature is controlled so that it becomes about ℃.

【0051】よって、乾燥肥料取出口14より排出される
乾燥した肥料は種子、病原菌等が殺菌された状態で排出
されるのである。
Therefore, the dried fertilizer discharged from the dried fertilizer outlet 14 is discharged in a state where seeds, pathogenic bacteria and the like are sterilized.

【0052】又、炉体2の温度制御を簡易にするために
肥料投入口13から投入する量と乾燥肥料取出口14から排
出する量を一定にすることも可能とし、即ちその方法と
しては乾燥肥料取出口14の開口度合に応じて決定される
排出量に対応した量と成る様に駆動源25の回転数を制御
して移送スクリュー26によって投入される投入量を一定
と成したり、又他の方法としては、乾燥肥料取出口14よ
り排出される量を排出量測定装置23により常に測定しな
がら、この測定値に対し所定の基準値となる様に制御す
る。
Further, in order to simplify the temperature control of the furnace body 2, it is possible to make constant the amount input from the fertilizer inlet 13 and the amount discharged from the dry fertilizer outlet 14, that is, the method is dry. The rotation amount of the drive source 25 is controlled so that the amount corresponds to the amount of discharge determined according to the opening degree of the fertilizer outlet 14, and the amount of charge input by the transfer screw 26 is made constant, or As another method, the amount discharged from the dried fertilizer outlet 14 is constantly measured by the discharge amount measuring device 23, and the measured value is controlled to be a predetermined reference value.

【0053】次に集塵装置33については、排気ダクト34
より排出される熱風は乾燥過程にて粉塵と成った廃棄物
が存在しており、ここでは拡散ノズル37により水を集塵
処理塔35の内壁36側若しくは下方へ噴霧(又はシャワー
状)することにより、この水と接触した粉塵は内壁36に
付着し、この付着した粉塵はスラリー状と成って下方へ
流動し、そして排出コンベア38により外部に排出される
ため、集塵処理塔35からは極めてクリーンな空気のみが
排出される結果となる。
Next, for the dust collector 33, the exhaust duct 34
The hot air discharged from the waste contains wastes that have become dust during the drying process, and here, the water is sprayed (or showered) by the diffusion nozzle 37 to the inner wall 36 side of the dust collection tower 35 or below. As a result, the dust that has come into contact with the water adheres to the inner wall 36, the adhered dust forms a slurry and flows downward, and is discharged to the outside by the discharge conveyor 38. The result is that only clean air is expelled.

【0054】尚、排出コンベア38は乾燥処理装置11にお
ける投入した肥料のオーバーフローを取り出すことも出
来る。
The discharge conveyor 38 can also take out the overflow of the fertilizer input in the drying processing device 11.

【0055】次に乾燥された肥料は粉砕機39に投入さ
れ、粉末状にして原材料の均一化を図って粉砕肥料ホッ
パー41へ供給され、該粉砕肥料ホッパー41よりペレット
ミル42に投入する過程において必要に応じて所定量の木
酢液を添加し、かかるペレットミル42に投入された粉末
状の肥料に対し水若しくは水蒸気等にて水分調整し、数
ミリ程度のペレット状に成形して固形肥料とする。
Next, the dried fertilizer is put into the crusher 39, made into a powder form and supplied to the crushed fertilizer hopper 41 with the aim of homogenizing the raw materials. If necessary, add a predetermined amount of wood vinegar, adjust the water content of the powdered fertilizer put into the pellet mill 42 with water or steam, and mold it into pellets of about several millimeters to obtain solid fertilizer. To do.

【0056】又、このペレットミル42に供給する原材料
は乾燥した肥料の他に、冷却工程にて発生した粉塵と成
った肥料、選別機45により選別された規格外品の固形肥
料をリサイクルして優先供給することにより、製造ライ
ン1における肥料の損失を著しく低減することが出来る
と共に、この優先供給している間は、粉砕肥料ホッパー
41への供給のための装置、例えば乾燥処理装置11、粉砕
機39を停止させることも出来る。
The raw materials to be supplied to the pellet mill 42 are, in addition to the dried fertilizer, the fertilizer formed into dust generated in the cooling process and the solid fertilizer of the nonstandard product selected by the selector 45. By preferentially supplying the fertilizer, the loss of fertilizer in the production line 1 can be remarkably reduced.
It is also possible to stop the device for supplying to 41, for example, the drying treatment device 11 and the crusher 39.

【0057】次に、ペレットミル42にて成形された固形
肥料は直ぐに冷却機44に投入され、該冷却機44を通過す
る過程にて空気等の冷却媒体と接触させて所定温度まで
冷却固化し、ペレット状に成形された固形肥料の形状の
安定化を図っている。
Next, the solid fertilizer formed by the pellet mill 42 is immediately put into the cooler 44, and in the process of passing through the cooler 44, it is brought into contact with a cooling medium such as air to be cooled and solidified to a predetermined temperature. , The shape of pelletized solid fertilizer is being stabilized.

【0058】その後、固形肥料を選別機45のフルイ網46
上に載せて振動を与えてふるい分けし、かかる選別機45
によりふるい分けされた規格品の固形肥料は小袋詰器48
により10キロ、大袋詰器49により20キロ程度に詰め
られ、その後はロボットパレタイザー50を介してパレッ
ト上に所定量載置される。
After that, the solid fertilizer is sorted by a screening machine 45 and a screening screen 46.
It is placed on top of it and vibrated to sort it.
The standard solid fertilizer screened by
10 kg, and about 20 kg by the large bag packer 49, and then a predetermined amount is placed on the pallet via the robot palletizer 50.

【0059】尚、ふるい分けする過程にて加熱器47より
遠赤外線を放射して適宜乾燥させることにより、フルイ
網46の網目に付着して閉鎖する付着物を無くし、選別時
の不具合を防止すると共に、固形肥料のイオン化傾向を
高めている。
In the sieving process, far infrared rays are radiated from the heater 47 to be appropriately dried, so that the deposits that adhere to the mesh of the sieve net 46 and are closed are eliminated, and the malfunction at the time of selection is prevented. , Increasing the ionization tendency of solid fertilizer.

【0060】[0060]

【発明の効果】要するに本発明は、有機質廃棄物に所定
量の化学肥料を添加し、しかる後攪拌混合しながら好気
性醗酵させて肥料化したので、好気性醗酵が進むにつ
れ、高含水部分の小団塊も次第に乾燥し、醗酵後期には
小団塊も細粒化され、これにより細粒化される有機醗酵
生成物と、細粒化された化学肥料とを化学的に吸着させ
て一体的に有機化した肥料を製造することが出来る。
EFFECTS OF THE INVENTION In summary, the present invention adds a predetermined amount of chemical fertilizer to organic waste, and then fermented it by aerobically fermenting while stirring and mixing, so as the aerobic fermentation proceeds, The small nodules also gradually dry, and in the latter half of fermentation, the small nodules are also atomized, and the organic fermentation products that are atomized by this and the atomized chemical fertilizer are chemically adsorbed and integrated. It is possible to produce organic fertilizer.

【0061】又、この肥料を土壌に散布すると、土壌中
の微生物によって化学吸着している有機醗酵生成物が無
機化され、その肥料成分を徐々に少量ずつ土壌中に放出
することが出来、化学肥料に比し肥効が緩徐であるため
植物の根に極めて優しい肥料となると共に、化学肥料と
有機醗酵生成物とを化学的に吸着させているため、化学
吸着されている有機醗酵生成物が無機化されるまで化学
肥料が水に溶ける時間を遅延させることが出来、化学肥
料のみを使用する場合に比し、河川の環境汚染等の公害
の原因を未然に無くすことが出来、よって化学肥料と有
機質肥料との利点のみを兼ね備えた優れた肥料を製造す
ることが出来る。
When this fertilizer is applied to the soil, the organic fermentation products chemically adsorbed by the microorganisms in the soil are mineralized, and the fertilizer components can be gradually released into the soil. Since the fertilizing effect is slower than fertilizer, it becomes a fertilizer that is extremely gentle to the roots of plants, and since the chemical fertilizer and the organic fermentation product are chemically adsorbed, the chemically adsorbed organic fermentation product is The time required for the chemical fertilizer to dissolve in water can be delayed until it is mineralized, and the cause of pollution such as environmental pollution of rivers can be eliminated in advance compared with the case of using only chemical fertilizer. It is possible to produce an excellent fertilizer having only the advantages of organic fertilizer.

【0062】次に回転制御される炉体12内に設ける撹拌
突条15、15a …により前記肥料を攪拌させながら邪魔板
17、17a …により乱流状態と成した熱風に接触させて乾
燥処理したので、回転する炉体12により投入された肥料
が撹拌突条15、15a …によって掻き上げられると共に落
下されて撹拌処理されながら、邪魔板17、17a …によっ
て撹拌乱流状態と成る熱風に接触して順次水分を除去さ
せて乾燥処理することが出来、又熱風は各邪魔板17、17
a …に衝突して内部にて撹拌乱流状態と成ることによ
り、熱交換率を高くし、高い効率にて連続乾燥処理する
ことが出来る。
Next, the baffle plate is provided while stirring the fertilizer by the stirring ridges 15, 15a ...
The fertilizer introduced by the rotating furnace body 12 was scraped up and dropped by the stirring ridges 15, 15a, because it was dried by being brought into contact with the hot air in a turbulent state by 17, 17a. However, the baffles 17, 17a ... Can be contacted with hot air in a turbulent agitated state to sequentially remove water and perform drying treatment.
By colliding with a ... and forming a stirring turbulent state inside, it is possible to increase the heat exchange rate and perform continuous drying processing with high efficiency.

【0063】又、熱風供給装置29から送給する熱風の温
度を乾燥肥料取出口14側では約200℃以上と成すこと
により、乾燥肥料取出口14より排出される乾燥した肥料
は種子、病原菌等を殺菌させた状態で排出することが出
来、このため施肥した後の雑草の発生を未然に防止する
ことが出来る。
Further, by setting the temperature of the hot air sent from the hot air supply device 29 to about 200 ° C. or more on the dry fertilizer outlet 14 side, the dried fertilizer discharged from the dry fertilizer outlet 14 can be seeds, pathogenic bacteria, etc. Can be discharged in a sterilized state, and thus weeds can be prevented from occurring after fertilization.

【0064】次にこの乾燥処理された肥料を粉砕機39を
介してペレットミル42によりペレット状に成形し、しか
る後冷却機44に投入して冷却固化する様にしたので、施
肥時に機械散布が出来ることにより、省力化を図ること
が出来、又乾燥処理された肥料に土壌菌(好気性有効
菌)を添加することにより、フェアーウエー、ティーグ
ランド等に生菌として働きサッチの分解を促進し、芝の
健全に発育させることが出来る等その実用的効果甚だ大
なるものである。
Next, this dried fertilizer was shaped into pellets by the pellet mill 42 through the crusher 39, and then put into the cooler 44 to be cooled and solidified. By doing so, it is possible to save labor, and by adding soil fungi (aerobic effective bacteria) to the dried fertilizer, it works as a live fungus on fairways, tea grounds, etc. to promote the decomposition of thatch. , The lawn can be grown soundly, and its practical effect is enormous.

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

【図1】本発明に係る肥料製造システムのフローシート
図である。
FIG. 1 is a flow sheet diagram of a fertilizer manufacturing system according to the present invention.

【図2】肥料の醗酵槽を有する建屋の概略正面図であ
る。
FIG. 2 is a schematic front view of a building having a fertilizer fermenter.

【図3】建屋の醗酵槽の概略側面図である。FIG. 3 is a schematic side view of the fermentation tank of the building.

【図4】乾燥処理装置の一部を破断した側面図である。FIG. 4 is a side view in which a part of the drying processing device is cut away.

【図5】乾燥処理装置の一部を示す拡大図である。FIG. 5 is an enlarged view showing a part of the drying processing apparatus.

【図6】乾燥処理装置の炉体内に設ける邪魔板の配設状
態を示す概略斜視図である。
FIG. 6 is a schematic perspective view showing a disposition state of baffle plates provided in the furnace of the drying processing apparatus.

【図7】図4のAーA一部省略断面図である。7 is a cross-sectional view of FIG. 4 taken along the line AA.

【図8】図4のBーB一部省略断面図である。FIG. 8 is a cross-sectional view of FIG. 4 taken along the line BB.

【図9】選別機の概略側面図である。FIG. 9 is a schematic side view of a sorter.

【符号の説明】 12 炉体 15、15a … 撹拌突条 17、17a … 邪魔板 39 粉砕機 42 ペレットミル[Explanation of symbols] 12 Furnaces 15, 15a… Stirring ridges 17, 17a… Baffle plate 39 Crusher 42 Pellet mill

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 有機質廃棄物に所定量の化学肥料を添加
し、しかる後攪拌混合しながら好気性醗酵させて肥料化
し、次に回転制御される炉体内に設ける撹拌突条により
前記肥料を攪拌させながら邪魔板により乱流状態と成し
た熱風に接触させて乾燥処理し、次にこの乾燥処理され
た肥料を粉砕機を介してペレットミルによりペレット状
に成形し、しかる後冷却機に投入して冷却固化する様に
したことを特徴とする肥料製造システム。
1. A predetermined amount of a chemical fertilizer is added to organic waste, which is then agitated and mixed to be fermented by aerobic fermentation, and then the fertilizer is agitated by a stirrer bar provided in a furnace body whose rotation is controlled. While making it contact with hot air that has become turbulent due to the baffle plate, it is dried, then this dried fertilizer is molded into pellets by a pellet mill through a crusher, and then put into a cooler. A fertilizer manufacturing system characterized by being cooled and solidified.
JP4031561A 1992-01-21 1992-01-21 Fertilizer manufacturing method Expired - Lifetime JP2519623B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4031561A JP2519623B2 (en) 1992-01-21 1992-01-21 Fertilizer manufacturing method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4031561A JP2519623B2 (en) 1992-01-21 1992-01-21 Fertilizer manufacturing method

Publications (2)

Publication Number Publication Date
JPH05194071A true JPH05194071A (en) 1993-08-03
JP2519623B2 JP2519623B2 (en) 1996-07-31

Family

ID=12334593

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4031561A Expired - Lifetime JP2519623B2 (en) 1992-01-21 1992-01-21 Fertilizer manufacturing method

Country Status (1)

Country Link
JP (1) JP2519623B2 (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006335601A (en) * 2005-06-01 2006-12-14 Shiwa Hozen:Kk Fertilizer or soil conditioner, its producing method, and method for producing cultivation-type soil conditioner using the fertilizer or soil conditioner
JP2012071994A (en) * 2010-09-27 2012-04-12 Mc Ferticom Co Ltd Method for promoting phosphate absorption by crop using sludge-fermented fertilizer and method for producing material for promoting phosphate absorption
US8619227B2 (en) 2005-12-05 2013-12-31 Semiconductor Energy Laboratory Co., Ltd. Liquid crystal display device
WO2021230160A1 (en) * 2020-05-13 2021-11-18 株式会社クラシコ Rational method for producing artificial humic matter and method for using same
CN114887549A (en) * 2022-05-30 2022-08-12 安徽惠禾壮有机肥科技有限公司 Compound-feeding type organic fertilizer granulator and granulation method thereof
CN115096060A (en) * 2022-05-30 2022-09-23 高唐亚泰肥料有限公司 Agricultural planting fertilizer production device and production process thereof

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU186729U1 (en) * 2018-05-24 2019-01-30 Федеральное государственное бюджетное образовательное учреждение высшего образования "Южно-Уральский государственный аграрный университет" (ФГБОУ ВО Южно-Уральский ГАУ) PLANT FOR PRODUCING BIOGAS AND EFFLUENT DISINFECTION

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS49123852A (en) * 1973-04-16 1974-11-27
JPS5369971A (en) * 1976-12-04 1978-06-21 Asami Kimi Means for treating domestic animal waste
JPS59137212A (en) * 1983-01-26 1984-08-07 Nippon Denso Co Ltd Air cleaner and conditioner for automobile
JPH03126690A (en) * 1989-10-06 1991-05-29 Taki Chem Co Ltd Living bacterium-containing granular fertilizer

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS49123852A (en) * 1973-04-16 1974-11-27
JPS5369971A (en) * 1976-12-04 1978-06-21 Asami Kimi Means for treating domestic animal waste
JPS59137212A (en) * 1983-01-26 1984-08-07 Nippon Denso Co Ltd Air cleaner and conditioner for automobile
JPH03126690A (en) * 1989-10-06 1991-05-29 Taki Chem Co Ltd Living bacterium-containing granular fertilizer

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006335601A (en) * 2005-06-01 2006-12-14 Shiwa Hozen:Kk Fertilizer or soil conditioner, its producing method, and method for producing cultivation-type soil conditioner using the fertilizer or soil conditioner
US8619227B2 (en) 2005-12-05 2013-12-31 Semiconductor Energy Laboratory Co., Ltd. Liquid crystal display device
JP2012071994A (en) * 2010-09-27 2012-04-12 Mc Ferticom Co Ltd Method for promoting phosphate absorption by crop using sludge-fermented fertilizer and method for producing material for promoting phosphate absorption
WO2021230160A1 (en) * 2020-05-13 2021-11-18 株式会社クラシコ Rational method for producing artificial humic matter and method for using same
CN114887549A (en) * 2022-05-30 2022-08-12 安徽惠禾壮有机肥科技有限公司 Compound-feeding type organic fertilizer granulator and granulation method thereof
CN115096060A (en) * 2022-05-30 2022-09-23 高唐亚泰肥料有限公司 Agricultural planting fertilizer production device and production process thereof

Also Published As

Publication number Publication date
JP2519623B2 (en) 1996-07-31

Similar Documents

Publication Publication Date Title
CN101687720B (en) Process for treating sludge and manufacturing bioorganically-augmented high nitrogen-containing inorganic fertilizer
CN104326830B (en) A kind of compound organic and inorganic fertilizer and preparation method
CN108623348A (en) Biological organic fertilizer production system
CN103264042A (en) Household garbage recycling method
CN110317089A (en) A kind of livestock and poultry feces and agricultural crop straw blending prepare organic fertilizer apparatus and method
CN1181015C (en) Complete set of machines for preparing compund biologic organic fertilizer from solid waste
KR101822480B1 (en) Method for manufacturing organic fertilizerwithingredient made from waste having enhanced productivity
JP2519623B2 (en) Fertilizer manufacturing method
CN105646024A (en) Bio-organic fertilizer production line
KR200399083Y1 (en) an organic fertilizer and manufacturing apparatus of the same
CN103265343A (en) Method for treating domestic garbage by utilizing biotechnology
CN205590584U (en) Bio - organic fertilizer production line
KR101822476B1 (en) The manufacture device of pellet-type fertilizer
CN212610338U (en) Biogas residue aerobic fermentation organic fertilizer production system
CN101987800B (en) BB fertilizer production method and special device thereof
US3547612A (en) Production of granular fertilizers
KR100433010B1 (en) Pellet manure system production
CN101993285B (en) Production method of coated organic fertilizer and special equipment thereof
KR101822478B1 (en) The manufacture device of fertilizer having material pre-treating tank
CN212982826U (en) System for producing granular organic fertilizer by utilizing biogas residue aerobic fermentation material
JP2002248454A (en) Treating apparatus for organic waste
KR100684295B1 (en) An organic fertilizer and mafacturing method and apparatus of the same
CN209778681U (en) Automatic organic waste treatment system
CN1384081A (en) System of producing organic fertilizer with sludge
CN113912434A (en) Aerobic biological treatment and inactivation granulation cooperative system for antibiotic fungi residues