JP2003094010A - Heat treating equipment of bio-waste and heat treatment method - Google Patents

Heat treating equipment of bio-waste and heat treatment method

Info

Publication number
JP2003094010A
JP2003094010A JP2001296723A JP2001296723A JP2003094010A JP 2003094010 A JP2003094010 A JP 2003094010A JP 2001296723 A JP2001296723 A JP 2001296723A JP 2001296723 A JP2001296723 A JP 2001296723A JP 2003094010 A JP2003094010 A JP 2003094010A
Authority
JP
Japan
Prior art keywords
hot air
heat treatment
air dryer
hopper
biological waste
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.)
Withdrawn
Application number
JP2001296723A
Other languages
Japanese (ja)
Inventor
Yokichi Oku
要吉 奥
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.)
OKUGUMI KK
Original Assignee
OKUGUMI KK
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 OKUGUMI KK filed Critical OKUGUMI KK
Priority to JP2001296723A priority Critical patent/JP2003094010A/en
Publication of JP2003094010A publication Critical patent/JP2003094010A/en
Withdrawn legal-status Critical Current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

  • Fodder In General (AREA)
  • Incineration Of Waste (AREA)
  • Processing Of Solid Wastes (AREA)
  • Fertilizers (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a heat treating equipment and a heat treatment method for regenerating bio-waste, in particular exotic fish such as black bass, into feedstuff and a fertilizer. SOLUTION: The heat treating equipment 10 comprises a hopper 12 for feeding a material to be treated, a hot air dryer 14 for heat treating the material, a crusher 16 for crushing the material, a cyclone 18 for separating finely ground substances contained in exhaust from the hot air dryer 14, a deodorizing equipment 20 for burning the exhaust from the cyclone 18, and a chimney 22 for exhausting the exhaust from the deodorizing equipment 20. The material is crushed after heat drying treatment with the hot air of not lower than 500 deg.C and not higher than 700 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、ブルーギルなどの
有害な外来魚を、飼料や肥料に再生するのに特に適し
た、生物系廃棄物の加熱処理装置及び加熱処理方法に関
する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a heat treatment apparatus and a heat treatment method for biological waste, which are particularly suitable for regenerating harmful foreign fish such as bluegill into feed and fertilizer.

【0002】[0002]

【発明が解決しようとする課題】近年、琵琶湖などにお
いては、従来の貴重な資源であるモロコ、フナ、アユな
どが、ブルーギルやブラックバスなどの外来魚の繁殖に
よって激減している。これらの外来魚は食用に適さない
ためわざわざ捕獲されることがなく、また、天敵も少な
いため野放図に繁殖している現状である。このため、食
用を奨励するための料理レシピーの開発などが試みられ
ているが、満足な結果が得られていない。
In recent years, in Lake Biwa and the like, moroko, crucian carp, ayu, etc., which are traditionally valuable resources, are drastically reduced due to the breeding of exotic fish such as bluegill and black bass. Since these exotic fish are not suitable for food, they are not bothered to be caught, and because there are few natural enemies, they are now breeding in the wild map. Therefore, attempts have been made to develop cooking recipes to encourage edible foods, but satisfactory results have not been obtained.

【0003】したがって、当面できることは、捕獲して
駆除に努めることだけであるが、捕獲した外来魚の処理
方法が大きな課題になっている。土中に埋めるには広い
土地が必要になるし、なによりも、腐敗に伴なう異臭の
発生が問題である。あるいは、飼料や肥料に再生するに
しても、従来の技術では、品質的にもコスト的にも満足
できなかった。
Therefore, the only thing that can be done for the time being is to try to exterminate them by extermination, but the method of treating the exotic fish that has been entrapped has become a major issue. A large amount of land is required to bury it in the soil, and above all, the offensive odor caused by decay is a problem. Alternatively, even if it is regenerated into feed or fertilizer, the conventional techniques have not been satisfactory in terms of quality and cost.

【0004】そこで本発明者は、ブルーギルなどの有害
な外来魚を、大量かつ効率的に、良質な飼料や肥料に再
生する熱処理装置及び熱処理方法を提供するべく鋭意検
討を重ねた結果、本発明に至ったのである。
Therefore, the present inventor has conducted extensive studies to provide a heat treatment apparatus and a heat treatment method for regenerating harmful foreign fish such as bluegill into a high-quality feed or fertilizer in a large amount and efficiently, and as a result, the present invention was found. Was reached.

【0005】[0005]

【課題を解決するための手段】本発明に係わる生物系廃
棄物の加熱処理装置の要旨とするところは、処理物を供
給するためのホッパーと、処理物を加熱処理するための
熱風乾燥機と、被処理物を粉砕するための粉砕機と、熱
風乾燥機の排気に含まれる微粉粒物を分離するためのサ
イクロンと、サイクロンからの排気を燃焼する脱臭装置
と、脱臭装置から排気するための煙突とを含んで構成さ
れたことにある。
The gist of the heat treatment apparatus for biological waste according to the present invention is to provide a hopper for supplying the treatment object and a hot air dryer for heat treating the treatment object. , A crusher for crushing the object to be treated, a cyclone for separating fine powder particles contained in the exhaust of the hot air dryer, a deodorizing device for burning the exhaust from the cyclone, and a device for exhausting from the deodorizing device It is configured to include a chimney.

【0006】さらに、かかる生物系廃棄物の加熱処理装
置において、ホッパーから熱風乾燥機へ処理物を搬送す
るための処理物搬送手段が備えられたことにある。
Further, the heat treatment apparatus for such biological waste is provided with a treated product conveying means for conveying the treated product from the hopper to the hot air dryer.

【0007】またさらに、かかる生物系廃棄物の加熱処
理装置において、貯蔵タンクと、熱風乾燥機から貯蔵タ
ンクへ被処理物を搬送する被処理物搬送手段と、貯蔵タ
ンクの取り出し口下に設けられた粉砕機とが備えられた
ことにある。
Further, in such a biological waste heat treatment apparatus, a storage tank, an object transfer means for transferring an object to be processed from a hot air dryer to the storage tank, and a take-out port of the storage tank are provided. It was equipped with a crusher.

【0008】またさらに、かかる生物系廃棄物の加熱処
理装置において、熱風乾燥機の熱風発生炉とホッパーと
の間に、ホッパーから吸気して熱風発生炉に送気する吸
送気手段が備えられたことにある。
Further, in such a heat treatment apparatus for biological waste, an intake / intake means for inhaling air from the hopper and supplying it to the hot air generating furnace is provided between the hot air generating furnace of the hot air dryer and the hopper. There is something.

【0009】またさらに、かかる生物系廃棄物の加熱処
理装置において、熱風乾燥機に攪拌破砕用の回転翼が備
えられたことにある。
Furthermore, in such a biological waste heat treatment apparatus, the hot air dryer is provided with a rotary blade for stirring and crushing.

【0010】またさらに、かかる生物系廃棄物の加熱処
理装置において、被処理物搬送手段がバケットコンベヤ
とされたことにある。
Further, in the biological waste heat treatment apparatus, the object convey means is a bucket conveyor.

【0011】また、本発明に係わる生物系廃棄物の加熱
処理方法の要旨とするところは、500℃以上700℃
以下の熱風で加熱乾燥処理した後、粉砕することにあ
る。
Further, the gist of the heat treatment method for biological waste according to the present invention is 500 ° C. to 700 ° C.
It is to pulverize after heating and drying with the following hot air.

【0012】[0012]

【発明の実施の形態】次に、本発明に係わる生物系廃棄
物の加熱処理装置及び加熱処理方法の実施態様につい
て、図面に基づいて詳しく説明する。
BEST MODE FOR CARRYING OUT THE INVENTION Next, embodiments of the heat treatment apparatus and heat treatment method for biological waste according to the present invention will be described in detail with reference to the drawings.

【0013】図1と図2は、本発明に係わる生物系廃棄
物の加熱処理装置の一例を示し、図3は、本加熱処理装
置10によって、生物系廃棄物が加熱乾燥処理される流
れを示している。加熱処理装置10は、処理物を供給す
るためのホッパー12と、処理物を熱処理するための熱
風乾燥機14と、ホッパー12から熱風乾燥機14へ処
理物を搬送するための処理物搬送手段24と、貯蔵タン
ク28と、熱風乾燥機14から貯蔵タンク28へ被処理
物を搬送する被処理物搬送手段26と、貯蔵タンク28
の取り出し口下に設けられた粉砕機16と、また、熱風
乾燥機14の排気に含まれる微粉粒物を分離するための
サイクロン18と、サイクロン18からの排気を燃焼す
る脱臭装置20と、脱臭装置20から排気するための煙
突22とで主に構成されている。
1 and 2 show an example of a heat treatment apparatus for biological waste according to the present invention, and FIG. 3 shows a flow of heat drying treatment of biological waste by the heat treatment apparatus 10. Shows. The heat treatment apparatus 10 includes a hopper 12 for supplying a processed product, a hot air dryer 14 for heat-treating the processed product, and a processed product conveying means 24 for transferring the processed product from the hopper 12 to the hot air dryer 14. A storage tank 28, an object transfer means 26 for transferring an object from the hot air dryer 14 to the storage tank 28, and a storage tank 28.
A pulverizer 16 provided under the outlet of the cyclone 18, a cyclone 18 for separating fine powder particles contained in the exhaust of the hot air dryer 14, a deodorizing device 20 for burning the exhaust from the cyclone 18, and a deodorizing device. It is mainly configured with a chimney 22 for exhausting from the device 20.

【0014】そして、ホッパー12から熱風乾燥機14
に至る部分は、地面29から掘り下げた窪み42に据え
付けられており、トラックなどで搬入された処理物を、
そのままホッパー12に投下できるようにされている。
From the hopper 12 to the hot air dryer 14
Is installed in the recess 42 dug down from the ground 29, and the processed material carried in by a truck,
It can be dropped onto the hopper 12 as it is.

【0015】ホッパー12の下部はテーパー状に絞られ
処理物搬送手段24につながるが、このテーパー状の底
部では、投下された処理物が、いわゆるブリッジを起こ
して落下しなくなることがある。このため、ホッパー1
2の中程には粗い目の金網31が設けられており、処理
物が処理物搬送手段24に向かって徐々に落下するよう
にされている。
The lower part of the hopper 12 is tapered and connected to the processing object conveying means 24. At the bottom of the taper, the dropped processing objects may cause a so-called bridge and may not fall. Therefore, the hopper 1
A coarse wire mesh 31 is provided in the middle of 2, and the processed material is gradually dropped toward the processed material conveying means 24.

【0016】また、図4に示されるように、ホッパー1
2の上縁13は、下方が開放された下向きコの字状の案
内路15で縁取られている。そして、案内路15と熱風
乾燥機14の熱風発生炉30とが、吸引路40と吸引フ
ァン34と送気路44とからなる吸送気手段によって連
結されている。吸引ファン34は、案内路15を介して
ホッパー12入口付近の空気を吸引すると同時に、この
吸気を外気で希釈して熱風発生炉30に送気する役目を
担っている。
Further, as shown in FIG. 4, the hopper 1
The upper edge 13 of 2 is framed by a downward U-shaped guide path 15 having an open bottom. Further, the guide passage 15 and the hot air generating furnace 30 of the hot air dryer 14 are connected by the suction and air supply means including the suction passage 40, the suction fan 34, and the air supply passage 44. The suction fan 34 has a role of sucking the air near the inlet of the hopper 12 through the guide passage 15 and at the same time diluting the intake air with the outside air and sending the diluted air to the hot air generating furnace 30.

【0017】ホッパー12と熱風発生炉30との間に吸
送気手段を備えることによって、外来魚などの処理物か
ら生じる強い臭気を、ホッパー12から外部に放散させ
ることなく熱風発生炉30に送り込むことができるよう
になる。そして、フレッシュな外気で希釈されて熱風乾
燥機14に供給される。本例において、ホッパー12で
の吸気口はホッパー12の上縁13に設けられている
が、ホッパー12の中程や底部に設けられてもよい。
By providing the suction and air supply means between the hopper 12 and the hot air generating furnace 30, the strong odor generated from the processed material such as foreign fish is sent from the hopper 12 to the hot air generating furnace 30 without being diffused to the outside. Will be able to. Then, it is diluted with fresh outside air and supplied to the hot air dryer 14. In this example, the intake port of the hopper 12 is provided at the upper edge 13 of the hopper 12, but it may be provided in the middle or bottom of the hopper 12.

【0018】処理物搬送手段24は、熱風乾燥機14へ
の送り込み速度をコントロールできる、2軸スクリュー
などの強制的な搬送手段が好ましい。外来魚などの比較
的大きくて不揃いな固形物では、管壁などとの接触によ
って移動が妨げられやすい。モーターの動力を用いて強
制的に移動させることが好ましい。しかしながら本発明
は、処理物搬送手段24を省いて、ホッパー12から熱
風乾燥機14に直接処理物を投入されるようにされても
よい。
The processed material conveying means 24 is preferably a compulsory conveying means such as a twin screw which can control the feeding speed to the hot air dryer 14. For relatively large and uneven solid materials such as foreign fish, their movement is likely to be hindered by contact with the pipe wall. It is preferable to force the movement by using the power of the motor. However, in the present invention, the processed material conveying means 24 may be omitted, and the processed material may be directly fed from the hopper 12 to the hot air dryer 14.

【0019】熱風乾燥は、所定温度で均一に効率よく乾
燥できる特徴がある。生物系廃棄物を飼料や肥料に再生
するためには、被処理物の品質を安定に確保することが
重要な問題であり、熱風を用いる乾燥が最も適してい
る。用いられる熱風乾燥機14の種類は特に限定されな
いが、攪拌破砕用の回転翼を内部に供えた熱風乾燥機1
4が特に好ましく用いられる。熱風乾燥機14内に送り
込まれた外来魚などの処理物は、回転翼によって攪拌さ
れ、また、一部は乾燥されやすい形に破砕されるので、
熱風発生炉30から供給される熱風によって効率よく均
一に乾燥されることになる。
The hot air drying is characterized in that it can be uniformly and efficiently dried at a predetermined temperature. In order to recycle biological waste into feed and fertilizer, it is an important issue to ensure the quality of the treated material, and drying using hot air is most suitable. The type of the hot air dryer 14 used is not particularly limited, but the hot air dryer 1 is provided with a rotary blade for stirring and crushing inside.
4 is particularly preferably used. The processed products such as foreign fish sent into the hot air dryer 14 are agitated by the rotor blades, and a part of them is crushed into a form that is easily dried.
The hot air supplied from the hot air generating furnace 30 allows efficient and uniform drying.

【0020】熱風乾燥機14には、処理物入口と被処理
物出口、及び、熱風入口と熱風出口が設けられており、
熱風乾燥は次ぎのようにして実施される。すなわち、所
定量の処理物が熱風乾燥機14内に供給されると、処理
物入口と被処理物出口が閉じられる。そして、回転翼で
攪拌しながら、熱風入口から熱風出口へ熱風を流すこと
によって行われる。熱処理の時間は、熱風の温度や処理
物の量によって異なる。
The hot air dryer 14 is provided with a processed product inlet and a processed product outlet, and a hot air inlet and a hot air outlet,
Hot air drying is performed as follows. That is, when a predetermined amount of the processed product is supplied into the hot air dryer 14, the processed product inlet and the processed product outlet are closed. Then, the hot air is flown from the hot air inlet to the hot air outlet while stirring with the rotary blades. The heat treatment time varies depending on the temperature of hot air and the amount of the processed material.

【0021】外来魚などから飼料や肥料を安定に得るに
は、加熱処理温度が適切に選定されることが重要であ
る。加熱処理温度は熱風温度によって左右されるが、熱
風温度が500℃以上700℃以下とされるのが好まし
い。500℃以下であれば、十分に乾燥した被処理物が
得られにくく、乾燥時間が長くなるので好ましくない。
また、700℃以上であれば、被処理物に炭化物が混入
するようになるので好ましくない。なお、熱風温度の測
定は、熱風乾燥機14入口の直前で定法によって行われ
る。
In order to stably obtain feed and fertilizer from foreign fish and the like, it is important to properly select the heat treatment temperature. The heat treatment temperature depends on the hot air temperature, but the hot air temperature is preferably 500 ° C. or higher and 700 ° C. or lower. If the temperature is 500 ° C. or less, it is difficult to obtain a sufficiently dried object to be treated and the drying time becomes long, which is not preferable.
Further, if the temperature is 700 ° C. or higher, carbides will be mixed into the object to be treated, which is not preferable. In addition, the measurement of the hot air temperature is performed by a conventional method immediately before the inlet of the hot air dryer 14.

【0022】熱風乾燥機14によって熱処理された被処
理物は、飼料や肥料に供するため適当な大きさに粉砕さ
れる。熱風乾燥機14の直後に粉砕機を配設して、熱風
乾燥機14から取り出された被処理物を直ちに粉砕する
こともできるが、粉砕の作業性を高めるために被処理物
を冷却すること、及び、熱風乾燥機14からの取り出し
速度と粉砕速度の差を補うことを目的に、被処理物をい
ったん貯蔵タンクに収容した後に粉砕することが好まし
い。
The object to be treated, which has been heat-treated by the hot air dryer 14, is crushed to an appropriate size for use as feed or fertilizer. It is possible to dispose a crusher immediately after the hot air dryer 14 to crush the object to be treated taken out from the hot air dryer 14 immediately, but to cool the object to be crushed in order to improve workability. For the purpose of compensating the difference between the take-out speed from the hot air dryer 14 and the crushing speed, it is preferable that the object to be treated is once stored in a storage tank and then crushed.

【0023】したがって、貯蔵タンク28と、これに被
処理物を搬送するための被処理物搬送装置26とが好ま
しく備えられるが、図1と図2に例示された加熱処理装
置10では、縦型の貯蔵タンク28が高所に設けられ、
その底部にある取り出し口下に、粉砕機16が備えられ
ている。そして、粉砕された被処理物はトラックなどの
上で受け、荷造りされて直ちに出荷できるようにされて
いて、本発明の特に好ましい実施態様である。高所に設
けられた貯蔵タンク28に被処理物を搬送するには、バ
ケットコンベヤが特に便利である。バケットコンベヤに
よれば、ほぼ垂直方向に被処理物を効率よく運べるの
で、設置面積を格別に小さくできる。
Therefore, the storage tank 28 and the workpiece transporting device 26 for transporting the workpiece are preferably provided in the storage tank 28. However, in the heat treatment apparatus 10 illustrated in FIGS. Storage tank 28 of is installed at a high place,
A crusher 16 is provided below the outlet on the bottom of the crusher 16. The crushed object to be processed is received on a truck or the like, packed, and ready to be shipped, which is a particularly preferred embodiment of the present invention. A bucket conveyor is particularly convenient for transporting an object to be processed to a storage tank 28 provided at a high place. According to the bucket conveyor, the object to be processed can be efficiently carried in a substantially vertical direction, so that the installation area can be made extremely small.

【0024】次ぎに排気系について説明するが、加熱処
理に用いられた後、熱風乾燥機14から排出される排気
は、サイクロン18に導かれ、熱風乾燥機14から伴な
ってきた微紛粒物が分離・回収される。サイクロンの型
式は特に限定されず、通常用いられるものの中から、流
量や微紛粒物の性状などを考慮して選択される。
Next, the exhaust system will be explained. The exhaust gas discharged from the hot air dryer 14 after being used for the heat treatment is guided to the cyclone 18 and the fine powder particles accompanied by the hot air dryer 14 are introduced. Are separated and collected. The type of cyclone is not particularly limited, and it is selected from among those usually used in consideration of the flow rate and the properties of the fine powder particles.

【0025】サイクロン18からの排気は、脱臭装置2
0にて脱臭され、煙突22から大気中に排出される。脱
臭装置20では、排気中に含まれる油分などの有機物が
バーナー33によって燃やされ、臭気の元となった諸成
分が焼失して脱臭される。
Exhaust gas from the cyclone 18 is discharged from the deodorizing device 2
It is deodorized at 0 and discharged into the atmosphere from the chimney 22. In the deodorizing device 20, organic substances such as oil contained in the exhaust gas are burned by the burner 33, and the various components causing the odor are burned off and deodorized.

【0026】以上、本発明に係わる生物系廃棄物の加熱
処理装置及び加熱処理方法について詳細に説明してきた
が、本発明は上述の引用・例示に限定されず、加熱処理
装置の構成や、ホッパー、熱風乾燥機、粉砕機、サイク
ロン、脱臭装置、煙突などの種類や形状、加熱処理条件
等々につき、本発明の趣旨を逸脱しない範囲で、当業者
の知識に基づき種々なる改良、修正、変化を加えた態様
で実施し得るものである。
Although the biological waste heat treatment apparatus and the heat treatment method according to the present invention have been described above in detail, the present invention is not limited to the above-mentioned citations and examples, and the constitution of the heat treatment apparatus and the hopper. , Hot air dryer, crusher, cyclone, deodorizer, chimney, etc. types and shapes, heat treatment conditions, etc., within the scope not departing from the spirit of the present invention, various improvements, modifications, changes based on the knowledge of those skilled in the art. It can be implemented in an added mode.

【0027】次ぎに、本発明の実施例を詳しく説明す
る。
Next, examples of the present invention will be described in detail.

【0028】実施例1図1及び図2に示されるのと同様
の加熱処理装置10を用いて、琵琶湖で捕獲したブラッ
クバスとブルーギルの混合物を熱処理した。両者の混合
割合は4対6であった。この処理物500kgを熱風乾
燥機14に入れ、螺旋状の翼を備えた回転翼で攪拌しな
がら、約650℃の熱風を3時間流して加熱処理した。
そして、いったん貯蔵タンク28に収容して冷却した後
に粉砕し、粉末状の被処理物を得た。
Example 1 Using a heat treatment apparatus 10 similar to that shown in FIGS. 1 and 2, a mixture of black bath and bluegill captured in Lake Biwa was heat treated. The mixing ratio of both was 4 to 6. This treated product (500 kg) was put into the hot air dryer 14, and was heated by flowing hot air at about 650 ° C. for 3 hours while stirring with a rotary blade having a spiral blade.
Then, it was once housed in the storage tank 28, cooled, and then pulverized to obtain a powdery object to be treated.

【0029】被処理物を飼料に供するための分析結果を
表1に、肥料に供するための分析結果を表2に示す。飼
料又は肥料として適性であることが確認された。なお、
分析方法は下記の通りである。 水分:常圧加熱乾燥法 粗たんぱく質:ケルダール法 粗脂肪:ジエチルエーテル抽出法 粗繊維:ろ過法 粗灰分:直接灰化法 カルシウム:過マンガン酸カリウム容量法 窒素全量:硫酸法 リン酸全量:バナドモリブデン酸アンモニウム法 カリ全量:原子吸光測定法 可消化粗たんぱく質、可消化養分総量、代謝エネルギ
ー:日本標準飼料成分表、 一般組成と消化率動物質飼料の魚粉(CP60%)牛に
よる。
Table 1 shows the analytical results for feeding the treated material to feed, and Table 2 shows the analytical results for feeding fertilizer. It was confirmed to be suitable as feed or fertilizer. In addition,
The analysis method is as follows. Moisture: Normal pressure heating drying method Crude protein: Kjeldahl method Crude fat: Diethyl ether extraction method Crude fiber: Filtration method Crude ash: Direct ashing method Calcium: Potassium permanganate volume method Nitrogen amount: Sulfuric acid Phosphoric acid amount: Banado Ammonium molybdate method Potassium total amount: Atomic absorption measurement method Digestible crude protein, total digestible nutrients, Metabolizable energy: Japanese standard feed ingredient table, general composition and digestibility Fish meal (CP60%) of animal feed.

【0030】[0030]

【表1】 [Table 1]

【0031】[0031]

【表2】 [Table 2]

【0032】実施例2 実施例1と同様に、琵琶湖の藻700kgに対し、20
0〜500℃の熱風を 4.5時間流して加熱処理した。
飼料に供するための分析結果を表3に、肥料に供するた
めの分析結果を表4に示す。琵琶湖の藻に対しても、飼
料又は肥料に再生できることが確認された。
Example 2 As in Example 1, 20 kg per 700 kg of algae in Lake Biwa
Hot air from 0 to 500 ° C It heat-processed by flowing for 4.5 hours.
Table 3 shows the results of the analysis for feeding.
Table 4 shows the results of the analysis. Even for algae in Lake Biwa,
It was confirmed that it can be regenerated into feed or fertilizer.

【0033】[0033]

【表3】 [Table 3]

【0034】[0034]

【表4】 [Table 4]

【0035】[0035]

【発明の効果】本発明に係わる生物系廃棄物の加熱処理
装置によれば、熱風乾燥機による加熱処理を行うので、
所定の温度で均一に乾燥することができ、飼料や肥料に
適した被処理物を安定かつ効率的に得ることができる。
また、サイクロンによって微粉粒が除かれ、脱臭装置に
よって有機物が燃焼されて排気されるので、有害物や臭
気がほとんど無い排気となり、周辺の環境を汚したり乱
したりしない。
According to the heat treatment apparatus for biological wastes of the present invention, since the heat treatment by the hot air dryer is performed,
It is possible to uniformly dry at a predetermined temperature, and it is possible to stably and efficiently obtain an object to be treated suitable for feed and fertilizer.
In addition, since the fine particles are removed by the cyclone and the organic matter is burned by the deodorizing device and exhausted, the exhaust gas is substantially free of harmful substances and odors and does not pollute or disturb the surrounding environment.

【0036】そして特に、ホッパーと熱風乾燥機の熱風
発生炉との間に吸送気手段が備えられれば、生物系処理
物をホッパーへ投入する時の臭気拡散を防止できる。
Further, in particular, if the suction air supply means is provided between the hopper and the hot air generating furnace of the hot air dryer, it is possible to prevent the odor from being diffused when the biological material is introduced into the hopper.

【0037】また特に、ホッパーから熱風乾燥機へ処理
物を搬送するための処理物搬送手段が備えられれば、外
来魚などの比較的大きい処理物も、熱風乾燥機に安定に
送り込むことができる。
Further, in particular, if a processed product conveying means for transferring the processed product from the hopper to the hot air dryer is provided, relatively large processed products such as foreign fish can be stably fed to the hot air dryer.

【0038】また特に、貯蔵タンクと、熱風乾燥機から
貯蔵タンクへ被処理物を搬送する被処理物搬送手段と、
貯蔵タンクの取り出し口下に設けられた粉砕機とが備え
られれば、被処理物を十分に冷却してから粉砕できるよ
うになり、熱風乾燥機からの排出速度に拘束されず、粉
砕速度を自由に選択できるようになる。そして、粉砕さ
れた被処理物をトラックなどの上で受け、荷造りして直
ちに出荷できるようになる。
Further, in particular, a storage tank, and an object transfer means for transferring an object from the hot air dryer to the storage tank,
If a crusher provided below the outlet of the storage tank is provided, it will be possible to sufficiently cool the object to be crushed before it can be crushed without being restricted by the discharge speed from the hot air dryer. You will be able to choose. Then, the crushed object to be processed can be received on a truck or the like, packed, and immediately shipped.

【0039】また特に、被処理物搬送手段がバケットコ
ンベヤとされれば、高所にあるホッパーまでほぼ垂直方
向に被処理物を効率よく運べるし、設置面積を格別に小
さくできて設備コストが低減される効果がある。
Further, in particular, if the object conveying means is a bucket conveyor, the object can be efficiently conveyed in a substantially vertical direction to a hopper located at a high place, and the installation area can be made particularly small to reduce the equipment cost. Is effective.

【0040】また特に、攪拌破砕用の回転翼が備えられ
た熱風乾燥機が用いることによって、加熱処理の効率を
高め、被処理物の均一性を向上させることができる。
Further, in particular, by using a hot-air dryer equipped with a rotary blade for stirring and crushing, the efficiency of heat treatment can be increased and the uniformity of the object to be treated can be improved.

【0041】また、本発明に係わる生物系廃棄物の加熱
処理方法によれば、500℃以上700℃以下の熱風で
加熱処理した後に粉砕するので、炭化物などが混入せず
に十分に乾燥されて、飼料や肥料に適した良質の被処理
物が得られる。
Further, according to the method for heat treatment of biological waste according to the present invention, since it is heat-treated with hot air of 500 ° C. or more and 700 ° C. or less and then pulverized, it is sufficiently dried without inclusion of carbides and the like. , Good quality products suitable for feed and fertilizer can be obtained.

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

【図1】本発明に係わる熱風乾燥機の一例を示す側面図
である。
FIG. 1 is a side view showing an example of a hot air dryer according to the present invention.

【図2】本発明に係わり、図1に示される熱風乾燥機の
平面図である。
FIG. 2 is a plan view of the hot air dryer shown in FIG. 1 according to the present invention.

【図3】本発明に係わり、図1と図2に示される熱風乾
燥機による熱処理の流れを示すブロック図である。
FIG. 3 is a block diagram showing a flow of heat treatment by the hot air dryer shown in FIGS. 1 and 2 according to the present invention.

【図4】本発明に係わり、ホッパーの上縁付近を拡大し
て示す縦断面図である。
FIG. 4 is a vertical cross-sectional view showing an enlarged vicinity of an upper edge of a hopper according to the present invention.

【符号の説明】[Explanation of symbols]

10:加熱処理装置 12:ホッパー 13:ホッパーの上縁 14:熱風乾燥機 15:案内路 16:粉砕機 18:サイクロン 20:脱臭装置 22:煙突 24:処理物搬送手段 26:被処理物搬送手段 28:貯蔵タンク 29:地面 30:熱風発生炉 31:金網 32、33:バーナー 34:吸引ファン 36:燃料タンク 38:誘引ファン 40:吸引路 42:窪み 44:送気路 10: Heat treatment device 12: Hopper 13: Upper edge of hopper 14: Hot air dryer 15: Guideway 16: Crusher 18: Cyclone 20: Deodorizing device 22: Chimney 24: Processed material conveying means 26: Transporting means for processed material 28: Storage tank 29: Ground 30: Hot air generator 31: Wire mesh 32, 33: Burner 34: Suction fan 36: Fuel tank 38: Attraction fan 40: suction path 42: hollow 44: Airway

フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) C05F 1/02 B09B 3/00 303M F23G 7/06 ZAB Fターム(参考) 2B150 AE02 BA04 BD01 BD06 BE01 CD15 3K078 AA05 AA08 BA06 BA23 CA04 CA09 CA25 4D004 AA04 AB01 AC04 BA04 CA04 CA08 CA42 CA48 CB13 CB36 CB45 DA02 DA03 DA06 4H061 AA02 AA03 CC31 GG16 GG18 GG19 GG67 GG70 LL02 Front page continuation (51) Int.Cl. 7 Identification code FI theme code (reference) C05F 1/02 B09B 3/00 303M F23G 7/06 ZAB F term (reference) 2B150 AE02 BA04 BD01 BD06 BE01 CD15 3K078 AA05 AA08 BA06 BA23 CA04 CA09 CA25 4D004 AA04 AB01 AC04 BA04 CA04 CA08 CA42 CA48 CB13 CB36 CB45 DA02 DA03 DA06 4H061 AA02 AA03 CC31 GG16 GG18 GG19 GG67 GG70 LL02

Claims (7)

【特許請求の範囲】[Claims] 【請求項1】 生物系の処理物を供給するためのホッパ
ーと、 前記処理物を加熱乾燥処理するための熱風乾燥機と、 前記加熱乾燥処理された被処理物を粉砕するための粉砕
機と、 前記熱風乾燥機の排気に含まれる微粉粒物を分離するた
めのサイクロンと、 前記サイクロンからの排気を燃焼する脱臭装置と、 前記脱臭装置から排気するための煙突と、を含む、生物
系廃棄物の加熱処理装置。
1. A hopper for supplying a biologically processed product, a hot air dryer for heating and drying the processed product, and a crusher for crushing the heated and dried product to be processed. A cyclone for separating fine particles contained in the exhaust of the hot air dryer, a deodorizing device for burning the exhaust from the cyclone, and a chimney for exhausting from the deodorizing device, a biological waste Heat treatment equipment for objects.
【請求項2】 前記ホッパーから熱風乾燥機へ処理物を
搬送するための処理物搬送手段が備えられた、請求項1
に記載の生物系廃棄物の加熱処理装置。
2. A processed product transporting means for transporting a processed product from the hopper to the hot air dryer is provided.
The heat treatment device for biological waste according to [4].
【請求項3】 前記被処理物を貯蔵する貯蔵タンクと、 前記熱風乾燥機から貯蔵タンクへ被処理物を搬送する被
処理物搬送手段と、 貯蔵タンクの取り出し口下に設けられた粉砕機と、が備
えられた、請求項1又は請求項2に記載の生物系廃棄物
の加熱処理装置。
3. A storage tank for storing the object to be processed, an object transfer means for transferring the object to be processed from the hot air dryer to the storage tank, and a crusher provided below an outlet of the storage tank. The heat treatment apparatus for biological waste according to claim 1 or 2, further comprising:
【請求項4】 前記熱風乾燥機の熱風発生炉とホッパー
との間に、ホッパーから吸気して熱風発生炉に送気する
吸送気手段が備えられた、請求項1乃至請求項3のいず
れかに記載の生物系廃棄物の加熱処理装置。
4. The suction air feeding means for sucking air from the hopper and feeding the hot air to the hot air generating furnace, which is provided between the hot air generating furnace and the hopper of the hot air dryer. A heat treatment device for biological waste according to item 1.
【請求項5】 前記熱風乾燥機に、攪拌破砕用の回転翼
が備えられた、請求項1乃至請求項4のいずれかに記載
の生物系廃棄物の加熱処理装置。
5. The heat treatment apparatus for biological waste according to claim 1, wherein the hot air dryer is equipped with a rotary blade for stirring and crushing.
【請求項6】 前記被処理物搬送手段がバケットコンベ
ヤとされた、請求項3乃至請求項5のいずれかに記載の
生物系廃棄物の加熱処理装置。
6. The heat treatment apparatus for biological waste according to claim 3, wherein the object conveying means is a bucket conveyor.
【請求項7】 処理物を500℃以上700℃以下の熱
風で加熱乾燥処理した後被処理物を粉砕することを特徴
とする、生物系廃棄物の加熱処理方法。
7. A heat treatment method for biological waste, which comprises heat-drying the treated material with hot air at 500 ° C. or higher and 700 ° C. or lower and then pulverizing the treated material.
JP2001296723A 2001-09-27 2001-09-27 Heat treating equipment of bio-waste and heat treatment method Withdrawn JP2003094010A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001296723A JP2003094010A (en) 2001-09-27 2001-09-27 Heat treating equipment of bio-waste and heat treatment method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001296723A JP2003094010A (en) 2001-09-27 2001-09-27 Heat treating equipment of bio-waste and heat treatment method

Publications (1)

Publication Number Publication Date
JP2003094010A true JP2003094010A (en) 2003-04-02

Family

ID=19117914

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP2003094010A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100860351B1 (en) 2007-07-30 2008-09-25 안영근 Method for production of fertilizer made from micropterus salmoides and fertilizer thereof
WO2016090445A1 (en) * 2014-12-10 2016-06-16 Ecobrás Gestão De Royalties Ltda Simultaneous pulper and dryer for solids

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100860351B1 (en) 2007-07-30 2008-09-25 안영근 Method for production of fertilizer made from micropterus salmoides and fertilizer thereof
WO2016090445A1 (en) * 2014-12-10 2016-06-16 Ecobrás Gestão De Royalties Ltda Simultaneous pulper and dryer for solids

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