JPS63248787A - Equipment for manufacturing organic fertilizer - Google Patents

Equipment for manufacturing organic fertilizer

Info

Publication number
JPS63248787A
JPS63248787A JP62084333A JP8433387A JPS63248787A JP S63248787 A JPS63248787 A JP S63248787A JP 62084333 A JP62084333 A JP 62084333A JP 8433387 A JP8433387 A JP 8433387A JP S63248787 A JPS63248787 A JP S63248787A
Authority
JP
Japan
Prior art keywords
raw material
fertilizer
evaporative
mixed
raw materials
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
JP62084333A
Other languages
Japanese (ja)
Inventor
坂下 常雄
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 JP62084333A priority Critical patent/JPS63248787A/en
Publication of JPS63248787A publication Critical patent/JPS63248787A/en
Pending legal-status Critical Current

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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

  • Fertilizers (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、有機質肥料の製造装置に関し、特に鶏糞や養
豚場廃棄物、その他の家畜の糞尿を原料として有機質肥
料を製造するのに適した装置に関する。
[Detailed Description of the Invention] (Field of Industrial Application) The present invention relates to an organic fertilizer manufacturing device, and is particularly suitable for manufacturing organic fertilizer using chicken manure, pig farm waste, and other livestock manure as raw materials. Regarding equipment.

(従来の技術) 鶏糞等の家畜の糞尿を醗酵させて有機質肥料とし、これ
を農地に還元することは一部で以前から行なわれている
(Prior Art) Fermenting livestock manure such as chicken manure to make organic fertilizer, which is then returned to farmland, has been practiced in some areas for some time.

上記従来の有機質肥料は、家畜の糞尿を数か月間自然醗
酵させて得られている。
The above-mentioned conventional organic fertilizers are obtained by naturally fermenting livestock manure for several months.

また、本出願人は醗酵機構の研究解明を行ない、肥料成
分に富んだ有機質肥料を短期間で効果的に1qることを
特開昭61−232286および同61−232287
で提案した。
In addition, the applicant has conducted research and elucidation of the fermentation mechanism, and has found that 1 q of organic fertilizer rich in fertilizer components can be effectively produced in a short period of time using JP-A-61-232286 and JP-A-61-232287.
I proposed it.

これら先の提案においては、鶏糞等の有機質肥料原料(
以下「原料」という)に複数種の細菌を含む混合培養菌
を添加し、醗酵を効率好く行なわせることができるとと
もに、上記混合培養菌の他に無機質材料を添加して醗酵
させることにより、バランスのとれた有機質肥料を得る
ことができる。
In these previous proposals, organic fertilizer raw materials such as chicken manure (
By adding a mixed culture containing multiple types of bacteria to the "raw material" (hereinafter referred to as "raw material"), fermentation can be carried out efficiently, and by adding inorganic materials in addition to the above mixed culture, You can get a balanced organic fertilizer.

(発明が解決しようとする問題点) しかしながら、上記従来の有機質肥料の製造にあたって
は、特に以前からの製造方法では、数か月間という長期
間必要とするため、設備が大きくなるという欠点があり
、また、本出願人が先に提案した製造方法においても、
極めて短期間で有用な有機質肥料が得られるという利益
があるが、よりコンパクトで簡単な肥料製造装置が望ま
れていた。なぜならば、原料は含水率が高いため、前処
理として遠心弁iI!を機おるいはベル1−プレス型脱
水機等の高価な装置を必要とするとともに、−貫したプ
ロセスからなる肥料製造装置がなかったためである。
(Problems to be Solved by the Invention) However, in producing the above-mentioned conventional organic fertilizer, especially in the conventional production method, there is a drawback that it requires a long period of several months and the equipment becomes large. Also, in the manufacturing method previously proposed by the applicant,
Although there is an advantage in that useful organic fertilizer can be obtained in a very short period of time, a more compact and simple fertilizer manufacturing device has been desired. This is because the raw material has a high moisture content, so as a pre-treatment process, the centrifugal valve iI! This is because, in addition to requiring expensive equipment such as a Bell 1-press type dewatering machine, there was no fertilizer manufacturing equipment that involved a complete process.

(発明が解決しようとする問題点) 本発明は上記問題点に鑑みてなされたものであって、鶏
糞等の家畜糞尿を受け入れる原料ホッパと、 上記原料ホッパからの原料と混合培養菌を混合して混合
原料を得るための混合攪拌機と、上記混合攪拌機からの
混合原料を受け入れて、混合原料を醗酵させるとともに
混合原料中の水分の一部を蒸発させて肥料原料を得るた
めの蒸発醗酵槽と、 上記蒸発醗酵槽からの肥料原料を破砕するための破砕機
と、 上記破砕機で処理した肥料原料を篩で選別し有機質肥料
を得るための篩機とからなることを特徴とするものであ
る。
(Problems to be Solved by the Invention) The present invention has been made in view of the above-mentioned problems, and includes a raw material hopper that receives livestock manure such as chicken manure, and a mixture of mixed culture bacteria with the raw material from the raw material hopper. an evaporative fermentation tank for receiving the mixed raw material from the mixing agitator, fermenting the mixed raw material, and evaporating part of the water in the mixed raw material to obtain a fertilizer raw material; , a crusher for crushing the fertilizer raw material from the evaporative fermentation tank, and a sieve for sorting the fertilizer raw material processed by the crusher with a sieve to obtain organic fertilizer. .

(作用) 本発明は、上述のように構成されるため、ホッパに受け
入れられた原料は、混合攪拌機で混合培養菌と均一に混
合されるとともに、原料中の臭気成分が分解され、その
後、この混合物は蒸発醗酵槽において余分な水分を蒸発
しながら醗酵作用を受けて有機質肥料原料となり、ざら
にこの肥料原料は破砕されてから篩分けされて有機質肥
料が調製される。
(Function) Since the present invention is configured as described above, the raw material received in the hopper is uniformly mixed with the mixed culture bacteria by the mixing agitator, and the odor components in the raw material are decomposed. The mixture undergoes fermentation in an evaporative fermentation tank while evaporating excess water to become an organic fertilizer raw material, and this fertilizer raw material is roughly crushed and sieved to prepare an organic fertilizer.

(実施例の説明) 以下本発明の実施例を図面に基づいて説明する。(Explanation of Examples) Embodiments of the present invention will be described below based on the drawings.

第1図は、本発明のフローシートを示すもので、1は原
料ホッパで、これに畜舎等から家畜11iが受け入れら
れる。
FIG. 1 shows a flow sheet of the present invention. Reference numeral 1 denotes a raw material hopper into which livestock 11i are received from a livestock shed or the like.

2は混合攪拌機であって、ホッパ1からの原料を受け入
れるとともに、混合培養菌および後述の篩機より(ワら
れた肥料(以下「返送肥料」という)を混合撹拌する。
Reference numeral 2 denotes a mixer and agitator, which receives the raw materials from the hopper 1 and also mixes and agitates the mixed culture bacteria and the sieved fertilizer (hereinafter referred to as "return fertilizer") from the sieve machine described below.

なお、混合培養菌は、本出願人が先に提案した特開昭6
1−232286および同61−232287に開示し
たものと同一なので、重複を避けるために詳しい説明を
省略するが、シュウドモナス系、ストレプトミセス系、
ミクメコックス系。
The mixed culture bacteria is based on the method proposed by the applicant in JP-A No. 6.
1-232286 and No. 61-232287, so a detailed explanation will be omitted to avoid duplication, but Pseudomonas series, Streptomyces series,
Mikmecox type.

ミコバクテリウム系、ビブリオ系、ノカルヂア系。Mycobacterium, Vibrio, and Nocardia.

アクロモバクタ−系、フラボバクテリウム系、エアロバ
クター系またはニトロバクタ−系の菌糸から選択される
少なくとも2種の系以上の混合培養菌である。この混合
培養菌は調整槽3で水に添加され所定濃度に調整後、混
合攪拌8!2に添加される。
It is a mixed culture of at least two types of fungi selected from Achromobacter, Flavobacterium, Aerobacter, and Nitrobacter mycelia. This mixed cultured bacteria is added to water in the adjustment tank 3, adjusted to a predetermined concentration, and then added to the mixing agitator 8!2.

混合攪拌機2は原料、混合培養菌および返送肥料を均一
に混合攪拌して原料混合物を作るとともに、原料中の臭
気成分を混合培養菌および返送肥料により速やかに生物
脱臭する。
The mixer 2 uniformly mixes and stirs the raw materials, mixed culture bacteria, and returned fertilizer to form a raw material mixture, and quickly biologically deodorizes odor components in the raw materials using the mixed culture bacteria and returned fertilizer.

次いでこの原料混合物は蒸発醗酵槽4に送られ、醗酵と
蒸発作用を受ける。
This raw material mixture is then sent to the evaporative fermentation tank 4, where it is subjected to fermentation and evaporation.

この蒸発醗酵槽4は、3つの蒸発醗酵槽4a。This evaporative fermentation tank 4 includes three evaporative fermentation tanks 4a.

4b、4Gからなっていて、前述の原料混合物がこれら
3つの蒸発醗酵槽内を反転撹乱されながら直列に移動し
、この移動中に醗酵操作と水分蒸発作用を受けるように
なっている。
4b and 4G, and the above-mentioned raw material mixture moves in series in these three evaporative fermentation tanks while being reversed and agitated, and is subjected to fermentation operation and water evaporation action during this movement.

また、各蒸発醗酵槽4a、4b、4cは後述するように
内筒と外筒から構成され、このうち外筒にはボイラ5に
より暖められた温水により加温されるようになっている
。従って、蒸発醗酵槽内の温度は微生物が活動し易い3
5℃近辺に維持されるとともに、加温により水分の蒸発
が促進される。
Further, each of the evaporative fermentation tanks 4a, 4b, and 4c is composed of an inner cylinder and an outer cylinder, as will be described later, and the outer cylinder is heated by hot water heated by the boiler 5. Therefore, the temperature inside the evaporative fermentation tank is such that microorganisms are easily active3.
The temperature is maintained at around 5°C, and the evaporation of water is promoted by heating.

蒸発醗酵槽4で原料混合物が醗酵と蒸発作用を受けてB
OD成分が分解されるとともに、水分調整されて肥料原
料となり、この肥料原料は破砕機6により均等な粒径に
調製される。
In the evaporative fermentation tank 4, the raw material mixture undergoes fermentation and evaporation to produce B.
While the OD component is decomposed, the moisture content is adjusted to become a fertilizer raw material, and this fertilizer raw material is adjusted to a uniform particle size by a crusher 6.

この破砕機6は周知のものを用いることができる。例え
ば容器の内壁に多数の棒材を突出させ、この棒材間に多
数のビークを植設した回転軸を[−タにより回転させる
破砕機などである。
As this crusher 6, a known one can be used. For example, there is a crusher in which a large number of rods protrude from the inner wall of a container, and a rotary shaft with a large number of beaks installed between the rods is rotated by a rotor.

破砕機6で処理された肥料原料は、篩機7により粒径が
調製される。すなわち所定粒径以上のものは篩目を落下
することなく製品原料と1)で製品ホッパ7aに受り入
れられ、袋詰め等されて出荷される。
The fertilizer raw material processed by the crusher 6 has its particle size adjusted by a sieve 7. That is, particles having a predetermined size or more are received into the product hopper 7a together with the product raw materials (1) without falling through the sieve, packed in bags, etc., and shipped.

一方、粉状肥料は返送ホッパ7bに受け入れられ、ここ
から前述した混合攪拌機2に返送される。
On the other hand, the powdered fertilizer is received in the return hopper 7b, from which it is returned to the mixer agitator 2 described above.

なお、図において8は凝縮器であり、これは前記蒸発醗
酵槽4内で発生した水蒸気を凝縮させるもので、得られ
た凝縮水の一部は混合培養菌を調整するために調整槽3
に送られ、残部は排出されるようになっている。
In addition, in the figure, 8 is a condenser, which condenses the water vapor generated in the evaporative fermentation tank 4, and a part of the obtained condensed water is sent to the adjustment tank 3 in order to adjust the mixed culture bacteria.
and the remainder is discharged.

また、図中9は、混合攪拌機2に空気を送風するための
ブロワで、これにより混合攪拌機2内の原料混合物の醗
酵に必要な酵素が供給されるとともに、混合攪拌機2内
で発生した水蒸気は効率良く凝縮器8に送出される。
In addition, 9 in the figure is a blower for blowing air to the mixer and agitator 2, which supplies the enzyme necessary for fermentation of the raw material mixture in the mixer and agitator 2, and also removes the water vapor generated in the mixer and agitator 2. It is efficiently sent to the condenser 8.

なお、図において、原料ホッパ1.混合攪拌機2、蒸発
醗酵槽4.破砕機68よび篩機7の各間の原料、混合原
料または肥料原料の移送は、ベル1〜コンベア、チェー
ンコンベアあるいはスクリューコンベア等の公知の搬送
手段を用いることができる。
In addition, in the figure, raw material hopper 1. Mixing agitator 2, evaporative fermentation tank 4. To transfer the raw materials, mixed raw materials, or fertilizer raw materials between the crusher 68 and the sieve 7, known conveyance means such as a bell 1 to conveyor, a chain conveyor, or a screw conveyor can be used.

第2,3図には、上記した混合攪拌機2の詳細が示され
ている。
2 and 3 show details of the above-mentioned mixer agitator 2.

すなわら、横断面がほぼ長円形状をした密閉状の箱体2
1の長手方向に、2本の回転軸22,23を設けるとと
もに、これらの回転軸22.23に複数の撹拌翼24,
25を溶接により植設しである。
In other words, a closed box body 2 whose cross section is approximately oval in shape.
Two rotating shafts 22, 23 are provided in the longitudinal direction of the 1, and a plurality of stirring blades 24, 23 are provided on these rotating shafts 22, 23.
25 is installed by welding.

これら攪拌’!24.25は長方形の板材からなってお
り、これら板材の短辺の一端を回転軸22゜23の回り
に、かつ回転軸の長手方向に所定間隔毎に放射状に延び
るように溶接して設けられている。しかも、攪拌翼の板
材の幅方向の向きが各回転軸22.23の軸心とが直交
以外の角をもって取り付けられ、その取り付は角度も各
撹拌翼24゜25で一様でなく、ランダムになっている
Stir these! 24 and 25 are made of rectangular plates, and one end of the short side of these plates is welded to extend radially around the rotating shaft 22°23 at predetermined intervals in the longitudinal direction of the rotating shaft. ing. Moreover, the direction of the plate material of the stirring blade in the width direction is installed at an angle other than perpendicular to the axis of each rotating shaft 22, 23, and the angle of installation is not uniform for each stirring blade 24° 25 and is random. It has become.

また、回転軸24に設けられている撹拌翼24の先端に
は、この撹拌翼24の板面と直交して爪24′が設けら
れている。
Furthermore, a claw 24' is provided at the tip of the stirring blade 24 provided on the rotating shaft 24 so as to be perpendicular to the plate surface of the stirring blade 24.

なお、回転軸23.24に設けられている各攪拌翼24
.25は互いの回転軸の回転翼間に位置して、互いの回
転を阻害しないように配置されている。
Note that each stirring blade 24 provided on the rotating shaft 23, 24
.. 25 is located between the rotary blades of each rotary shaft and arranged so as not to inhibit each other's rotation.

図中26.27は各回転@22,23に設けられている
歯車で、原動機28により回転移動されるようになって
いる。なお、各回転軸22.23の回転方向は互いに外
向きの逆回転になるようになっており、従って原動機2
8によって回転される歯車26は、中間歯車(図示せず
)を介して歯車27と連絡されている。
In the figure, reference numerals 26 and 27 are gears provided at each rotation @ 22 and 23, which are rotated by the prime mover 28. Note that the rotational directions of the respective rotating shafts 22 and 23 are such that they rotate outward in opposite directions, so that the motor 2
Gear 26 rotated by 8 is in communication with gear 27 via an intermediate gear (not shown).

なお、29は開閉蓋であって、混合攪拌時は閉じられ、
通常はボルトにより閉じられており、保守点検時に開け
られるようになっる。
In addition, 29 is an opening/closing lid, which is closed during mixing and stirring.
It is normally closed with bolts and can be opened for maintenance and inspection.

また、30aおよび30bは7ランジであって、30a
のフランジは原料、混合培養液および返送肥料投入用で
あり、30bの7ランジは混合物排出用である。
Further, 30a and 30b are 7 lunges, and 30a
The flange 30b is for inputting raw materials, mixed culture solution, and returned fertilizer, and the 7 lunges 30b are for discharging the mixture.

以上のように構成される混合撹拌機においては、フラン
ジ30aから投入された原料、混合培養液および返送肥
料が厳しく混合撹拌されて均一な混合原料となる。特に
、回転軸22.23への攪拌翼24.25が所定角度で
取り付けられており、また一方の攪拌翼24の先端に爪
24′が設けられているので、原料の一部が混合攪拌機
内で攪拌作用を受けずに静置されることがない。このた
め原料と混合培養菌および返送肥料が均一に混合される
ので、原料中の臭気成分かむらなく分解されるとともに
、原料の水分調整が効果的に行なわれる。
In the mixing agitator configured as described above, the raw material, mixed culture solution, and returned fertilizer introduced from the flange 30a are thoroughly mixed and agitated to form a uniform mixed raw material. In particular, since the stirring blades 24.25 are attached to the rotating shaft 22.23 at a predetermined angle, and the claw 24' is provided at the tip of one of the stirring blades 24, a part of the raw material is inside the mixing stirrer. It will not be allowed to stand still without being subjected to stirring action. Therefore, the raw material, mixed culture bacteria, and returned fertilizer are mixed uniformly, so that the odor components in the raw material are evenly decomposed, and the moisture content of the raw material is effectively adjusted.

なお、図示の混合攪拌機においては、一方の攪拌翼24
のみに爪を設けた例を示したが、他方の攪拌m25にも
設けても良い。ただし、この場合、互いの回転軸の回転
を邪魔しないように配慮する必要がある。
In addition, in the illustrated mixing agitator, one of the agitating blades 24
Although an example is shown in which a claw is provided only on the stirring m25, the other stirring m25 may also be provided with a claw. However, in this case, it is necessary to take care not to interfere with the rotation of each other's rotation axes.

ざらに、回転軸の回転は歯車を組合せて行なうようにし
たが、これをVベルトを用いて行なっても良く、この場
合互いの回転軸が逆回転となるように、たすき掛けとす
るようにする。
Generally speaking, the rotating shafts are rotated by a combination of gears, but this may also be done using a V-belt. do.

第4,5図には、上述した蒸発醗酵槽4の詳細が示され
ている。この蒸発醗酵槽4は、外筒41と内筒42から
主として構成されている。
4 and 5 show details of the evaporative fermentation tank 4 described above. This evaporative fermentation tank 4 is mainly composed of an outer cylinder 41 and an inner cylinder 42.

外筒41には、温水の通過する通路43が筒の長手方向
に複数段けられ、この通路43中を温水ボイラ5で作ら
れた温水が通路43の一方から入り、他端から流出した
温水は再び温水ボイラ5に戻るように配管されている(
第1図参照)。
The outer cylinder 41 has a plurality of passages 43 for hot water to pass through in the longitudinal direction of the cylinder, through which the hot water produced by the hot water boiler 5 enters from one side of the passage 43, and the hot water flows out from the other end. is piped to return to hot water boiler 5 again (
(See Figure 1).

他方、内筒42は、リング部材44を等間隔に配置し、
これらリング部材44に多数の棒材45を貫通させ、は
ぼ簾状体を作るとともに、この棒材45に棒材長さと同
じ長さを有する断面円弧状の掻上げ羽根46を溶接しで
ある。また、内筒42の両端には端板47a、47bが
設けられているとともに、ざらにその外方に内筒42と
同心状に歯車48a、48bが段けられている。従って
、この歯車48a、48bを回転させることにより、内
筒42を回転させることができる。
On the other hand, the inner cylinder 42 has ring members 44 arranged at equal intervals,
A large number of rods 45 are passed through these ring members 44 to form a curtain-like body, and raking blades 46 having an arcuate cross section and having the same length as the rods are welded to the rods 45. . In addition, end plates 47a and 47b are provided at both ends of the inner cylinder 42, and gears 48a and 48b are arranged concentrically with the inner cylinder 42 roughly outward from the end plates 47a and 47b. Therefore, by rotating the gears 48a and 48b, the inner cylinder 42 can be rotated.

なお、内筒の回転は各蒸発醗酵槽4a、4b。Note that the inner cylinder rotates in each evaporative fermentation tank 4a, 4b.

4Gの内筒についている一方の歯車48aをチェーンで
連絡し、これを駆動機49で駆動することにより行なわ
れ、また、内筒の回転を円滑に行なわせるために他方の
歯車48b同士をチェーンで連絡しである(第1図参照
)。
This is done by connecting one gear 48a attached to the 4G inner cylinder with a chain and driving this with a drive machine 49. Also, in order to ensure smooth rotation of the inner cylinder, the other gear 48b is connected with a chain. (See Figure 1).

また、図中508は前述の混合攪拌[2からの混合原料
を投入するための開口であり、50bは蒸発醗酵処理さ
れた肥料原料を次の蒸発醗酵槽または破砕機6へ送出す
るための開口である。
Further, in the figure, 508 is an opening for introducing the mixed raw material from the above-mentioned mixing/stirring [2], and 50b is an opening for sending the evaporative and fermented fertilizer raw material to the next evaporative fermentation tank or crusher 6. It is.

なお、図示しないが外筒41にはブロワ9からの空気取
入口と、上記を含んだ空気を凝縮器8に送出するための
排気口が設けられている。
Although not shown, the outer cylinder 41 is provided with an air intake port from the blower 9 and an exhaust port for sending the air containing the above to the condenser 8.

以上のように構成される蒸発醗酵槽においては、開口5
0aから投入された混合原料は温水により適温に維持さ
れるとともに、掻上げ羽根46により反転攪拌されるの
で、充分に酵素を取込むことができ、効率良く醗酵作用
を受けることができる。
In the evaporative fermentation tank configured as described above, the opening 5
The mixed raw materials introduced from 0a are maintained at an appropriate temperature by hot water and are reversely stirred by the raking blades 46, so that enzymes can be sufficiently incorporated and the fermentation action can be carried out efficiently.

また混合原料中の水分が効果的に蒸発することができる
Moreover, water in the mixed raw materials can be effectively evaporated.

なお図示の蒸発醗酵槽4は3個の蒸発醗酵槽から構成さ
れてるが、これは原料の発生量等を考慮して、1または
2個でも良く、さらには4個以上としても良い。°ざら
に、蒸発醗酵槽の回転は、1つの駆動機49により、3
つの円筒42を回転させるようにしであるが、勿論、各
蒸発醗酵槽毎に駆動機を設けても良い。
Although the illustrated evaporative fermentation tank 4 is composed of three evaporative fermentation tanks, the number may be one or two, or even four or more, taking into consideration the amount of raw material generated. Roughly speaking, the rotation of the evaporative fermentation tank is controlled by one drive machine 49.
Although the two cylinders 42 are rotated, it is of course possible to provide a driving machine for each evaporative fermentation tank.

第6.7図には篩機7の詳細が示されており、両図にお
いて71は篩であって、全体形状は円筒の一部を形成し
ている。この@71の長手方向の両端は、高ざの低い支
持フレーム72と高さの高い支持フレーム73との間に
支持されている。また、これら支持フレーム72,73
には長孔74が設けられており、この長孔に1171の
フレーム71aに設けられた突起75が遊嵌されている
FIG. 6.7 shows details of the sieve 7, and in both figures 71 is a sieve whose overall shape forms part of a cylinder. Both ends of this @71 in the longitudinal direction are supported between a support frame 72 with a low height and a support frame 73 with a high height. In addition, these support frames 72, 73
is provided with a long hole 74, into which a protrusion 75 provided on the frame 71a of 1171 is loosely fitted.

ざらに、篩71のフレーム71aには、他端がモータ7
6により回転される回転偏心円板77に連結されている
リンク78の一端が、回動自在に連結されている。従っ
て、回転偏心円板77の回転により篩71が左右に揺動
できるようになっている(第7図矢印参照)。
Roughly speaking, the frame 71a of the sieve 71 has the motor 7 at the other end.
One end of a link 78 is rotatably connected to a rotary eccentric disk 77 rotated by a rotary eccentric disk 77 . Therefore, the sieve 71 can be swung left and right by the rotation of the rotating eccentric disk 77 (see arrows in FIG. 7).

なお、図中79は篩71の下部に設けられた案内板であ
り、篩71の目を通過した肥料をスクリューコンベア8
0に案内するようになっている。
In addition, 79 in the figure is a guide plate provided at the bottom of the sieve 71, and the fertilizer that has passed through the mesh of the sieve 71 is transferred to the screw conveyor 8.
It is designed to guide you to 0.

従って、この案内板は第1図の返送ホッパ7bに該当す
る。
Therefore, this guide plate corresponds to the return hopper 7b in FIG.

以上の構成からなるm機7においては、破砕機6から送
られてきた肥料原料をf!i71の上方で受け、1i7
1の傾斜と揺動により、肥料原料を下方へ移vJさせる
と、この移動中に粉状の肥料は篩目を通過して、スクリ
ューコンベア80により前述した混合攪拌機2に返送さ
れる。一方、篩上を下方へ移動した肥料は、製品の有機
質肥料として、図示しないが袋詰めされて出荷される。
In the m machine 7 having the above configuration, the fertilizer raw material sent from the crusher 6 is f! Received above i71, 1i7
When the fertilizer raw material is moved downward by the tilting and swinging of 1, the powdered fertilizer passes through the sieve mesh during this movement and is returned to the mixing agitator 2 described above by the screw conveyor 80. On the other hand, the fertilizer that has moved downward on the sieve is packaged in bags (not shown) and shipped as an organic fertilizer product.

以上の実施例においては、混合攪拌機2において原料ホ
ッパ1からの原料が調整槽3からの混合培養菌と混合さ
れることにより原料中の臭気成分は速やかに生物脱臭さ
れる。さらに、FJ機7からの返送肥料も混合されるこ
とにより、ざらにその脱臭効果が促進されるとともに、
原料中の水分調整も行なわれる。
In the above embodiment, the raw material from the raw material hopper 1 is mixed with the mixed culture bacteria from the adjustment tank 3 in the mixing agitator 2, so that odor components in the raw material are rapidly biologically deodorized. Furthermore, by mixing the fertilizer returned from FJ machine 7, the deodorizing effect is greatly promoted, and
Moisture adjustment in the raw materials is also carried out.

混合攪拌機2で処理された混合原料は蒸発醗酵槽4で加
温され、かつ内筒42に設けられた掻上げ羽根45によ
り反転攪拌されるので、水分が効果的に蒸発されるとと
もに、空気中の酸素を消費して醗酵が進行する。
The mixed raw materials processed by the mixer agitator 2 are heated in the evaporative fermentation tank 4, and are reversely agitated by the scraping blades 45 provided in the inner cylinder 42, so that water is effectively evaporated and water is removed from the air. Fermentation proceeds by consuming oxygen.

従って、この蒸発醗酵槽4で処理が終えたときには含水
率が低く、かつ原料中のBOD成分が分解された肥料成
分に富む有機質肥料が生成する。
Therefore, when the treatment is completed in this evaporative fermentation tank 4, an organic fertilizer is produced which has a low moisture content and is rich in fertilizer components in which the BOD components in the raw materials have been decomposed.

ただし、この蒸発醗酵槽4から得られる肥料原料は、塊
状を含む粒径が不均一な状態であるため、これを破砕機
6により破砕し、さらに@機7により粉状肥料を分離す
る調製がなされる。従って、篩機7で選別された肥料は
、粒状で含水率が低く、かつ取り扱いやすい肥料となる
However, since the fertilizer raw material obtained from this evaporative fermentation tank 4 is in a state where the particle size is uneven including lumps, it is necessary to crush it with the crusher 6 and further separate the powdered fertilizer with the @machine 7. It will be done. Therefore, the fertilizer sorted by the sieve 7 is granular, has a low moisture content, and is easy to handle.

この実施例装置で得た肥料の成分の一例を示せば、肥料
100g当たり水分13.3a、窒素2゜6(1,リン
酸(P2O3として>5.6(IIおよびカリウム(K
2Oとして)2.6oという低含水率で肥料成分に富ん
だものが得られる。
An example of the ingredients of the fertilizer obtained using this example device is as follows: per 100 g of fertilizer, moisture is 13.3 a, nitrogen is 2°6 (1), phosphoric acid (P2O3 is >5.6 (II) and potassium (K
A product rich in fertilizer components can be obtained with a low moisture content of 2.6o (as 2O).

(効果) 本発明は、原料に混合培養菌を添加して混合攪拌機によ
り混合攪拌して得られた混合原料を、蒸発醗酵槽で醗酵
および蒸発処理し、ざらに篩機で粒径を調製するように
構成したので、混合攪拌時に脱臭が行なわれ、また、醗
酵とともに水分調整も成されるので、別途に脱水機ある
いは脱臭機の設備が不要であり、また、II機で粒径の
調製が成されるので均一な有機質肥料が得られる。しか
も、この製造工程は原料の投入から製品の排出まで一員
して製造することができる利益がある。
(Effects) In the present invention, the mixed raw material obtained by adding mixed culture bacteria to the raw material and stirring it with a mixing agitator is fermented and evaporated in an evaporative fermentation tank, and the particle size is adjusted with a rough sieve machine. With this structure, deodorization is performed during mixing and stirring, and moisture adjustment is also performed at the same time as fermentation, so there is no need for separate dehydrator or deodorizer equipment, and the particle size can be adjusted using the II machine. Because the organic fertilizer is produced in a uniform manner, a uniform organic fertilizer can be obtained. What's more, this manufacturing process has the benefit of allowing everyone to work together from the input of raw materials to the discharge of the product.

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

図面は本発明に係る有機質肥料製造装置の一実施例を示
すもので、第1図はフローシート、第2゜3図は混合攪
拌機を示すものであって、第2図はその横断面図、第3
図は第2の■−■線断面図、第4,5図は蒸発醗酵槽を
示すものであって第4図はその側面図、第5図は第4図
のv−v線断面図、第6,7図は篩機を示すものであっ
て、第6図はその縦断面図および第7図は第6図の■−
VI線断面図である。 1・・・原料ホッパ 2・・・混合攪拌機 4・・・蒸発醗酵槽 6・・・破砕機 7・・・tgI機 し−%/71 特許庁長官 黒 1)明 雄 殿 1、事件の表示 特願昭62−84333号 2、発明の名称 有機質肥料製造装置 3、補正をする者 事件との関係  特許出願人 住 所  岩手県九ノ戸郡種市町第57地割13番地氏
名 坂下常雄 4、代理人〒101 住 所  東京都千代田区内神田1丁目15番16号7
、補正の内容 (1)明細書第7頁第15行目「混合攪拌機2」を「蒸
発醗酵槽4」に訂正する。 〈2)同頁筒17行目「酵素」を「酸素」に訂■する。
The drawings show an embodiment of the organic fertilizer production apparatus according to the present invention, in which Fig. 1 shows a flow sheet, Figs. 2-3 show a mixer, and Fig. 2 shows a cross-sectional view thereof. Third
The figure is a cross-sectional view taken along the line 2--■, Figures 4 and 5 are a side view of the evaporative fermentation tank, and Figure 5 is a cross-sectional view taken along the line v-v of Figure 4. Figures 6 and 7 show the sieving machine, with Figure 6 being a longitudinal sectional view and Figure 7 being the
It is a sectional view taken along VI line. 1... Raw material hopper 2... Mixing agitator 4... Evaporative fermentation tank 6... Crusher 7... TgI machine -%/71 Commissioner of the Patent Office Black 1) Akio Tono 1, Incident display Patent Application No. 62-84333 2, Name of the invention: Organic fertilizer manufacturing device 3, Relationship with the case of the person making the amendment Patent applicant address: 13, Lot 57, Taneichi-cho, Kunoto-gun, Iwate Name: Tsuneo Sakashita 4; Agent Address: 101 Address: 1-15-16-7 Uchikanda, Chiyoda-ku, Tokyo
, Contents of amendment (1) On page 7, line 15 of the specification, "mixing agitator 2" is corrected to "evaporative fermentation tank 4."<2) On the 17th line of the same page, ``enzyme'' is corrected to ``oxygen.''

Claims (1)

【特許請求の範囲】[Claims] (1)鶏糞等の家畜糞尿を受け入れる原料ホッパと、 上記原料ホッパからの原料と混合培養菌を混合して混合
原料を得るための混合攪拌機と、 上記混合攪拌機からの混合原料を受け入れて、混合原料
を醗酵させるとともに混合原料中の水分の一部を蒸発さ
せて肥料原料を得るための蒸発醗酵槽と、 上記蒸発醗酵槽からの肥料原料を破砕するための破砕機
と、 上記破砕機で処理した肥料原料を篩で選別し有機質肥料
を得るための篩機とからなることを特徴とする有機質肥
料製造装置。
(1) A raw material hopper that receives livestock manure such as chicken manure; A mixing agitator that mixes the raw material from the raw material hopper with mixed culture bacteria to obtain a mixed raw material; A mixing agitator that receives and mixes the mixed raw material from the mixing agitator. an evaporative fermentation tank for fermenting raw materials and evaporating part of the water in the mixed raw materials to obtain fertilizer raw materials; a crusher for crushing the fertilizer raw materials from the evaporative fermentation tank; 1. An organic fertilizer manufacturing apparatus comprising a sieve machine for sorting the fertilizer raw materials with a sieve to obtain organic fertilizer.
JP62084333A 1987-04-06 1987-04-06 Equipment for manufacturing organic fertilizer Pending JPS63248787A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62084333A JPS63248787A (en) 1987-04-06 1987-04-06 Equipment for manufacturing organic fertilizer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62084333A JPS63248787A (en) 1987-04-06 1987-04-06 Equipment for manufacturing organic fertilizer

Publications (1)

Publication Number Publication Date
JPS63248787A true JPS63248787A (en) 1988-10-17

Family

ID=13827581

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62084333A Pending JPS63248787A (en) 1987-04-06 1987-04-06 Equipment for manufacturing organic fertilizer

Country Status (1)

Country Link
JP (1) JPS63248787A (en)

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS537475A (en) * 1976-07-07 1978-01-23 Ebara Mfg Process for composting municipal refuses
JPS5767092A (en) * 1980-10-09 1982-04-23 Daiwa Engineering Kk Livestock excretions continuous fermentation treatment
JPS59184786A (en) * 1983-04-04 1984-10-20 日立機電工業株式会社 Fermentation treatment of organic waste

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS537475A (en) * 1976-07-07 1978-01-23 Ebara Mfg Process for composting municipal refuses
JPS5767092A (en) * 1980-10-09 1982-04-23 Daiwa Engineering Kk Livestock excretions continuous fermentation treatment
JPS59184786A (en) * 1983-04-04 1984-10-20 日立機電工業株式会社 Fermentation treatment of organic waste

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