JP3131176B2 - Continuous carbide production equipment - Google Patents

Continuous carbide production equipment

Info

Publication number
JP3131176B2
JP3131176B2 JP28046097A JP28046097A JP3131176B2 JP 3131176 B2 JP3131176 B2 JP 3131176B2 JP 28046097 A JP28046097 A JP 28046097A JP 28046097 A JP28046097 A JP 28046097A JP 3131176 B2 JP3131176 B2 JP 3131176B2
Authority
JP
Japan
Prior art keywords
casing
waste
carbonization chamber
carbide
cylindrical
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.)
Expired - Fee Related
Application number
JP28046097A
Other languages
Japanese (ja)
Other versions
JPH11116367A (en
Inventor
昌洋 難波
Original Assignee
株式会社まさなみ鉄工
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 株式会社まさなみ鉄工 filed Critical 株式会社まさなみ鉄工
Priority to JP28046097A priority Critical patent/JP3131176B2/en
Publication of JPH11116367A publication Critical patent/JPH11116367A/en
Application granted granted Critical
Publication of JP3131176B2 publication Critical patent/JP3131176B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A40/00Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
    • Y02A40/10Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
    • Y02A40/20Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/78Recycling of wood or furniture waste

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、し尿処理汚泥、そ
の他食品製造業等の活性汚泥や、植物性廃棄物等からな
る有機質廃棄物から炭化物を連続して製造するための装
置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for continuously producing charcoal from human waste treatment sludge, other activated sludge from the food manufacturing industry, and organic waste such as vegetable waste.

【0002】[0002]

【従来の技術】有機質廃棄物の肥料化に関して既に多く
の例がみられる。し尿処理汚泥、その他食品製造業の活
性汚泥等については、それらを原料とする有機肥料が化
学肥料にない土壌改良作用によって野菜その他の農作物
に好結果を与えることが明らかとなっている。例えば特
開昭53-44363号には、汚泥を乾燥した後、有機物を添加
して好気性発酵を行ない肥料化する例がみられる。発酵
の際に水分調製は重要であるが、そのために例えば特開
昭55-85495号や特開昭63-195186号に木片チップを混合
する例もみられる。また、発酵の際に活性炭を添加する
ことにより発生する悪臭を吸着すると共に肥料としての
好結果を得ることも特開昭53-17154号や特開昭53-12716
4号に記載されている。
2. Description of the Related Art There are many examples of converting organic waste into fertilizer. It has been clarified that, for human waste treated sludge and other activated sludge of the food manufacturing industry, organic fertilizers using them as raw materials can give good results to vegetables and other agricultural crops by a soil improvement action not found in chemical fertilizers. For example, JP-A-53-44363 discloses an example in which sludge is dried and then added with an organic substance to perform aerobic fermentation to produce a fertilizer. Water content is important during fermentation. For this purpose, for example, Japanese Patent Application Laid-Open Nos. 55-85495 and 63-195186 disclose mixing wood chips. In addition, it is also possible to adsorb bad odors generated by adding activated carbon during fermentation and obtain good results as a fertilizer, as disclosed in JP-A-53-17154 and JP-A-53-12716.
It is described in No. 4.

【0003】[0003]

【発明が解決しようとする課題】し尿処理施設や排水処
理施設の規模は益々大きくなっており、そこから発生す
る汚泥処理が問題となっている。また、動植物由来の有
機質廃棄物も例えば建築廃材や家庭ゴミなど増加の一途
を辿っており、処理場問題等解決しなければならない課
題が多い。そこで、汚泥及び他の木片等植物性有機質廃
棄物について肥料化による再資源化を検討し、活性炭添
加によるコスト上昇を抑え、悪臭のない肥料の製造方法
を可能にするための炭化物製造装置を検討した。
The scale of human waste treatment facilities and wastewater treatment facilities is increasing, and the treatment of sludge generated therefrom has become a problem. In addition, the amount of organic wastes derived from animals and plants has been increasing steadily, for example, from construction waste materials and household waste, and there are many problems to be solved such as the problem of a treatment plant. Therefore, we are studying the recycling of sludge and other plant organic wastes such as wood chips by turning them into fertilizers, and examining a carbide production device that can suppress the increase in cost due to the addition of activated carbon and enable a method for producing fertilizers that do not have offensive odors. did.

【0004】[0004]

【課題を解決するための手段】上記課題を検討した結
果、有機質廃棄物を分別し植物性残渣を炭化物にする工
程と、前記炭化物を有機質廃棄物に混合する工程と、
化物混合後の有機質廃棄物を発酵させて肥料化する工程
からなる有機質廃棄物の肥料化方法を開発した。有機質
廃棄物も例えば建築廃材や家庭ゴミや、排水処理場やし
尿処理場から発生する汚泥等である。この有機質廃棄物
に前記炭化物を混合する工程で木片を添加し、発酵後に
該木片を回収して再使用するとよい。木片は水分調製、
空気連通による発酵促進と一部肥料化に役立つ。
Means for Solving the Problems] As a result of studying the above problems, a step of fractionation and plant residue organic waste into carbides, and mixing the carbide organic waste, coal
We developed a method for converting organic waste into fertilizer, which consists of fermenting organic waste after compounding into fertilizer. Organic waste is also, for example, construction waste, household waste, or sludge generated from a wastewater treatment plant or a human waste treatment plant. The organic waste the carbide added piece of wood in the step of mixing into, may be recovered and reused to the wood pieces after fermentation. Wood pieces are prepared for moisture,
Useful for promoting fermentation and making some fertilizers through air communication.

【0005】有機質廃棄物の肥料化装置は、有機質廃棄
物のうちの植物性廃棄物を炭化物とするための炭化物
造装置と、有機質廃棄物に前記炭化物を混合する混合部
と、混合後の有機質廃棄物を発酵させる発酵槽とからな
る。混合後の有機質廃棄物を発酵させる発酵槽の後に
は、発酵後の肥料から木片を回収して前記混合装置へフ
ィードバックさせるための木片回収装置を設けるとよ
い。炭化物製造装置は密閉可能な炉で、空気の入りを制
限しながら熱分解させる機能を有する。また、木片回収
装置は、振動篩(ふるい)方式により肥料を下方に落し、
木片と分別する機能を有する。
[0005] The apparatus for converting organic waste into fertilizer comprises a carbide producing apparatus for converting vegetable waste of organic waste into carbide, and a mixing section for mixing the organic waste with the carbide. And a fermenter for fermenting the mixed organic waste. After the fermenter for fermenting the mixed organic waste, it is preferable to provide a wood chip collection device for collecting the wood chips from the fermented fertilizer and feeding it back to the mixing device. The carbide production device is a furnace that can be sealed and has a function of performing thermal decomposition while restricting the entry of air. In addition, the wood chip recovery device drops the fertilizer downward by the vibrating sieve (sieve) method,
It has the function of separating from wood chips.

【0006】炭化物連続製造装置の具体例は次のようで
ある。すなわち、上部に植物性廃棄物を供給するホッパ
ーと空気孔を備え下部がテーパ状の縦型筒状ケーシング
と、前記ケーシングのテーパ部に設けられた分解開始着
火用穴の外周の着火用バーナ加熱室と、ケーシング下方
に連続して設けた円筒状炭化室と、該円筒状炭化室内部
の螺旋排出スクリューと、該円筒状炭化室外部の冷却水
ジャケットとケーシング内から排煙を吸引する排気ファ
ンとからなり、ケーシング上方のホッパーから投入され
着火用バーナの炎が前記分解開始着火用の穴から入って
着火されて燃焼部で分解の始まった植物性廃棄物を燃焼
部の下端部に設けた円筒状の炭化室へ螺旋排出スクリュ
ーで送り、冷却水ジャケットで冷却される炭化室壁面と
螺旋排出スクリューにより形成された密閉空間内で炭化
されて得られた炭化物を炭化室下部の取出し口より連続
的に取り出すようにした装置が挙げられる。
A specific example of the continuous carbide producing apparatus is as follows. That is, a vertical cylindrical casing having an upper portion provided with a hopper for supplying vegetable waste and an air hole and having a tapered lower portion, and an ignition burner for heating an outer periphery of a decomposition start ignition hole provided in a tapered portion of the casing. Chamber, a cylindrical carbonization chamber provided continuously below the casing, a spiral discharge screw inside the cylindrical carbonization chamber, a cooling water jacket outside the cylindrical carbonization chamber, and an exhaust fan for sucking smoke from the casing. The flammable burner flame is injected from the hopper above the casing, and the flame of the ignition burner enters through the hole for the decomposition start ignition, is ignited, and the vegetable waste which is decomposed in the combustion part is provided at the lower end of the combustion part. feeding spiral discharge screw into a cylindrical coking chamber, the carbide obtained is carbonized in a sealed space formed by the carbonization chamber wall and the spiral discharge screw which is cooled by the cooling water jacket Reduction chamber include apparatus to extract from the continuous lower portion of the outlet.

【0007】[0007]

【発明の実施の形態】図1は有機質廃棄物の肥料化方法
を実施する装置の平面図、図2は正面図である。図示し
た有機質廃棄物の肥料化装置はほぼ中央に平坦面を三方
の壁で囲った混合部1があり、その脇に本発明の炭化物
製造装置2がある。炭化物製造装置2には植物性廃棄物
を供給するための供給機3を設けている。有機質廃棄物
の中から分別され供給機3に供給された植物性廃棄物
は、コンベア4で炭化物製造装置2の中へ投入されて
化物になる。この炭化物は他の有機質廃棄物残渣及び必
要に応じて木片と混合部1で混合される。混合部1での
混合は人による混合作業でもよいし、撹拌羽根を設けた
原動機付撹拌機を用いてもよい。混合比の好ましい例
は、汚泥1に対して木片0〜0.4、炭化物0.1〜0.3、最
も好ましいのは汚泥1に対して木片0.3、炭化物0.2であ
る。木片が0の場合は有機質廃棄物残渣の水分調製を必
要としないような場合である。
DESCRIPTION OF THE PREFERRED EMBODIMENTS FIG. 1 is a plan view of an apparatus for carrying out a method for converting organic waste into fertilizer, and FIG. 2 is a front view. In the illustrated organic waste fertilizer, there is a mixing section 1 having a flat surface surrounded by three walls at almost the center, and a carbide producing apparatus 2 of the present invention beside the mixing section 1. The charcoal production device 2 is provided with a supply device 3 for supplying vegetable waste. Vegetable waste fed to the feeder 3 is separated from the organic waste is turned into a carbide production apparatus 2 in the conveyor 4 charcoal
Become a monster . This carbide is mixed with other organic waste residues and, if necessary, wood chips in the mixing section 1. The mixing in the mixing section 1 may be a mixing operation by a person, or a motor-driven stirrer provided with a stirring blade may be used. Preferred examples of the mixing ratio are wood chips 0 to 0.4 and carbides 0.1 to 0.3 for sludge 1, and most preferably wood chips 0.3 and carbides 0.2 for sludge 1. The case where the wood piece is 0 is a case where it is not necessary to adjust the water content of the organic waste residue.

【0008】本発明の炭化物製造装置2の詳細な構造は
図3に示すように、植物性廃棄物を連続的に収容する予
熱室5の内部に撹拌フレーム6があり、予熱室5の下部
にテーパ状の燃焼部7がある。燃焼部7の外周には周囲
を加熱するバーナ加熱室7aがあって、バーナ加熱室7aの
炎の一部が燃焼部7テーパの下部に設けた穴7bから入っ
て植物性廃棄物を加熱して分解を開始させる。分解が始
まった植物性廃棄物は燃焼部7の下端部に設けた円筒状
の密閉炭化室8へ螺旋排出スクリュー8aで送られる。密
閉炭化室8の外周には冷却水で冷却するためのジャケッ
ト8bが設けられている。この炭化物製造装置2は炭化物
を高能率で連続して製造することができる特徴がある。
外方に設けた排気ファン36に接続された煙道(ダクト)31
がバーナ加熱室7aに連結されている。そこで、排気ファ
ン36を回転させると全体が減圧され、予熱室5の上部に
設けた空気孔5aから空気が予熱室5、燃焼部7へと供給
される。
[0008] As shown in FIG. 3, a detailed structure of the carbide producing apparatus 2 of the present invention is provided with a stirring frame 6 inside a preheating chamber 5 for continuously storing vegetable waste, and at a lower portion of the preheating chamber 5. There is a tapered combustion section 7. There is a burner heating chamber 7a for heating the periphery on the outer periphery of the combustion section 7, and a part of the flame of the burner heating chamber 7a enters through a hole 7b provided below the taper of the combustion section 7 to heat the vegetable waste. To start disassembly. The decomposed vegetable waste is sent by a spiral discharge screw 8a to a cylindrical closed carbonization chamber 8 provided at the lower end of the combustion section 7. A jacket 8b for cooling with cooling water is provided on the outer periphery of the closed carbonization chamber 8. This carbide producing apparatus 2 has a feature that carbide can be continuously produced with high efficiency.
Flue (duct) 31 connected to an exhaust fan 36 provided outside
Are connected to the burner heating chamber 7a. Therefore, when the exhaust fan 36 is rotated, the pressure is reduced as a whole, and air is supplied to the preheating chamber 5 and the combustion section 7 from the air holes 5 a provided in the upper part of the preheating chamber 5.

【0009】ホッパー5bから連続的に供給される植物性
廃棄物は燃焼部7で燃焼分解を開始する。しかし、螺旋
排出スクリュー8aで密閉炭化室8へ送られて空気がほと
んど供給されない状態の分解となって炭化物となる。燃
焼部7に設けた温度センサ37による温度測定結果をみな
がら螺旋排出スクリュー8aによる送りを調節する。燃焼
部7で生じる煙は煙道31によって排出されるが、煙道31
は途中が冷却水槽32の中へU字状に曲げて浸漬されてい
る。その最下部へ廃液口33を設けて排煙中の悪臭を除去
し、木酢を回収して、肥料原料中に混ぜることもできる
し、他の用途に使うこともできるようにしている。そこ
で、排気ガスが周囲の環境に悪影響を与えないようにし
ている。また、連続的に取出し口35から排出される炭化
はスクリュコンベア34によって図1に示す混合部1へ
送るようになっている。本装置によると、予熱室5の直
径を1.2mとし、密閉炭化室8までの長さを3mに製作
した場合、この装置の最上部に供給されたそば殻とコー
ヒー粕の1:1の混合物の例では20分経過後には炭化物
となって取出し口35から排出された。
The plant waste continuously supplied from the hopper 5b starts burning and decomposing in the combustion section 7. However, it is sent to the closed carbonization chamber 8 by the helical discharge screw 8a, and is decomposed into a state in which almost no air is supplied, and becomes a carbide . The feed by the spiral discharge screw 8a is adjusted while observing the temperature measurement result by the temperature sensor 37 provided in the combustion section 7. The smoke generated in the combustion section 7 is exhausted by the flue 31,
Is bent and immersed into the cooling water tank 32 in a U-shape. A waste liquid port 33 is provided at the bottom to remove the bad smell in the flue gas, and the wood vinegar can be collected and mixed with the fertilizer raw material, or used for other purposes. Therefore, the exhaust gas is prevented from adversely affecting the surrounding environment. In addition, the carbonized gas continuously discharged from the outlet 35
The articles are sent to the mixing section 1 shown in FIG. 1 by a screw conveyor 34. According to this apparatus, when the diameter of the preheating chamber 5 is 1.2 m and the length to the closed carbonization chamber 8 is 3 m, a 1: 1 mixture of buckwheat husk and coffee grounds supplied to the top of the apparatus is used. In the example of Example 2, after 20 minutes passed, it was discharged from the outlet 35 as carbide .

【0010】混合部1で炭化物、有機質汚泥及び必要に
応じて水分調製のための木片あるいはそれにオガ屑が混
合された有機質肥料原料は第1発酵槽9へ移される。こ
の移送にはコンベア等の搬送装置、或いはシャベルロー
ダ(自走式シャベル機)を用いる。第1発酵槽9は第1槽
から第12槽まで区画されている。有機質肥料原料は第1
発酵槽9の第1槽から順次第12槽まで所定時間(通常24
時間)ごとに移動させていく。第1発酵槽9の第1槽か
ら順次第12槽までの総ての槽の底部に送風口が設けられ
ているので、有機質肥料原料中へ撹拌によって空気の供
給ができる。この撹拌によって発酵中の有機質肥料原料
は第1槽から順次第12槽まで所定時間ごとに移動させて
いく。その移動はコンベアでもよいが、この例では図5
右側にみられるようなシャベルローダ16による。
[0010] In the mixing section 1, the charcoal , the organic sludge, and, if necessary, the wood chips for adjusting the water content or the organic fertilizer raw material mixed with sawdust are transferred to the first fermenter 9. For this transfer, a transfer device such as a conveyor or a shovel loader (self-propelled shovel machine) is used. The first fermenter 9 is partitioned from a first tank to a twelfth tank. Organic fertilizer raw materials are first
Predetermined time (normally 24 hours) from the first tank to the twelfth tank of fermenter 9
Time). Since the air vents are provided at the bottom of all the tanks from the first tank to the twelfth tank of the first fermentation tank 9, air can be supplied to the organic fertilizer raw material by stirring. By this stirring, the organic fertilizer raw material being fermented is moved from the first tank to the twelfth tank sequentially at predetermined time intervals. The movement may be by conveyor, but in this example,
By shovel loader 16 as seen on the right.

【0011】一次発酵を終え半肥料化した有機質廃棄物
は搬送コンベアによって第2発酵槽19に送られる。第1
発酵槽9の第12槽の半肥料化した有機質廃棄物をコンベ
ア17へ載せるために図4に示すような供給機18を設けて
いる。この供給機18の特徴はホッパー18aの下方を上方
よりも広く形成した点にある。このことにより、送りロ
ール18b,18cによって下方へ落下させる半肥料化した有
機質廃棄物のコンベア18dへの供給の際に生じる詰まり
の問題を解決し、コンベア18dから搬送コンベアへ円滑
に載せられる。
The organic waste that has been converted into semi-fertilizer after the primary fermentation is sent to the second fermenter 19 by a conveyor. First
A feeder 18 as shown in FIG. 4 is provided for placing the semi-fertilized organic waste in the twelfth tank of the fermenter 9 on the conveyor 17. The feature of the feeder 18 is that the lower part of the hopper 18a is formed wider than the upper part. This solves the problem of clogging that occurs when the semi-fertilized organic waste dropped by the feed rolls 18b and 18c is supplied to the conveyor 18d, and the organic waste is smoothly loaded from the conveyor 18d to the transport conveyor.

【0012】第2発酵槽19の様子の詳細は図5の側面図
によって明らかであるが、第2発酵槽19の隔壁10の上部
に走行用レール11があり、その上に方形の台車12が載っ
ている。その上に直角方向の移動用レール13,13があ
る。この移動用レール13,13上に撹拌搬送機保持台車14
が載っている。撹拌搬送機保持台車14には斜めに撹拌搬
送機15が保持されている。撹拌搬送機15は上下のプーリ
間にエンドレスベルトが張架され、それに多数枚の板状
の撹拌用羽根が設けられており、台車12が走行用レール
11上を前進(図中左行き)しながら後方へ落下させて、有
機廃棄物から得られた肥料を撹拌及び取出し口方向へと
前進させる。撹拌位置の変更は撹拌搬送機保持台車14が
移動用レール13上を移動して位置変更する(図面に対面
して前後方向に撹拌搬送機保持台車14が移動する)。撹
拌搬送機15による進行方向後方へ第2発酵を終えた有機
廃棄物由来の肥料が送られて第2発酵槽19からの搬出が
可能となる。
The details of the state of the second fermenter 19 are apparent from the side view of FIG. 5, but the traveling rail 11 is provided above the partition 10 of the second fermenter 19, and the rectangular carriage 12 is provided thereon. It is listed. Above it is a right-angle moving rail 13,13. On the moving rails 13, 13, the carrier carrier holding carriage 14 is provided.
There is. The stirring transporter 15 is held diagonally on the stirring transporter holding carriage 14. The stirring transporter 15 has an endless belt stretched between upper and lower pulleys, and a number of plate-like stirring blades are provided thereon.
The fertilizer obtained from the organic waste is moved forward (to the left in the figure) while advancing (leftward in FIG. 11) to agitate and advance toward the outlet. To change the stirring position, the stirring carrier holding carriage 14 moves on the moving rail 13 to change the position (the stirring carrier holding carriage 14 moves in the front-back direction facing the drawing). The fertilizer derived from the organic waste after the second fermentation is sent rearward in the advancing direction by the agitation transporter 15 and can be carried out of the second fermenter 19.

【0013】第2発酵を終えた有機廃棄物由来の肥料は
第2発酵槽19から木片回収装置20へ送られる。木片を回
収しない場合には第2発酵槽から包装装置へ送って製品
として出荷する。木片回収装置20への移送はコンベアで
も良いし、シャベルローダ等種々の搬送装置を用いるこ
とができる。木片回収装置20は振動篩方式により肥料を
下方に落し、木片と分別する機能を有している。その構
造を図6〜図8に示す。供給機18からコンベア21によっ
て搬送された木片を含む有機廃棄物肥料は木片回収装置
20の振動可能なメッシュ部20aにおいて肥料が下方に落
ち、木片がメッシュ上に残って後部から排出され木片回
送コンベア22で第1発酵槽9へフィードバックされる。
発酵菌も木片に伴って第1発酵槽へ供給されるので、第
1発酵槽における発酵を早める効果がある。篩分けされ
た有機廃棄物肥料は木片回収装置20下部の搬送コンベア
23で木片回収装置20外にある製品秤量包装装置24へ送ら
れる。製品秤量包装装置24には大袋秤量器25と小袋秤量
器26があり、前記搬送コンベア23の進退によって大袋秤
量器25と小袋秤量器26のいずれかへ送る製品搬送コンベ
ア27,28へ有機廃棄物肥料が載るようになっている。大
袋秤量器25と小袋秤量器26はロードセル方式であり、所
定量(この例では1000Kgと20Kg)袋に充填されるとシール
機29で熱シールしてコンベア30で出荷位置へ送るように
なっている。
[0013] The fertilizer derived from the organic waste after the second fermentation is sent from the second fermenter 19 to the wood chip recovery device 20. If the wood chips are not collected, they are sent from the second fermenter to the packaging device and shipped as products. The transfer to the wood chip collection device 20 may be performed by a conveyor, or various transfer devices such as a shovel loader may be used. The wood chip collection device 20 has a function of dropping the fertilizer downward by the vibrating sieve method and separating it from the wood chips. The structure is shown in FIGS. Organic waste fertilizer including wood chips transported by the conveyor 21 from the feeder 18 is collected by a wood chip recovery device.
At the 20 vibrable mesh sections 20a, the fertilizer falls down, the wood pieces remain on the mesh, are discharged from the rear, and are fed back to the first fermenter 9 by the wood piece conveyor 22.
Since the fermentation bacteria are also supplied to the first fermentation tank along with the wood chips, there is an effect of speeding up the fermentation in the first fermentation tank. The sieved organic waste fertilizer is transferred to the conveyor below the wood chip recovery unit 20
At 23, the product is sent to a product weighing and packaging device 24 outside the wood chip collection device 20. The product weighing and packaging apparatus 24 has a large bag weighing device 25 and a small bag weighing device 26, and the organic waste is transferred to the product carrying conveyors 27 and 28, which are sent to either the large bag weighing device 25 or the small bag weighing device 26 by the reciprocation of the transfer conveyor 23. Fertilizers are now available. The large bag weighing device 25 and the small bag weighing device 26 are of a load cell type, and when a predetermined amount (1000 kg and 20 kg in this example) is filled in a bag, the bag is heat-sealed by a sealing machine 29 and sent to a shipping position by a conveyor 30. I have.

【0014】[0014]

【発明の効果】本発明によって、汚泥や木片等植物性有
機質廃棄物を植物性有機質廃棄物の一部を炭化物とし、
その炭化物を含む優れた肥料として再資源化を可能とし
た。炭化物添加により肥料製造工程の無臭化が可能にな
り、かつ、活性炭を別途入手しなくてもよくなり、有機
質肥料の製造コストの低下と、廃棄物処理の両者を同時
に可能とした。
According to the present invention, plant organic waste such as sludge and wood chips is converted into a part of vegetable organic waste as carbide ,
It is possible to recycle as an excellent fertilizer containing the carbide . The addition of carbides makes it possible to eliminate the odor in the fertilizer production process, and eliminates the need to separately obtain activated carbon, thereby simultaneously reducing both the production cost of organic fertilizers and waste disposal.

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

【図1】有機質廃棄物の肥料化方法を実施する装置に本
発明の炭化物製造装置を配置した例の平面図である。
FIG. 1 is a plan view of an example in which a carbide producing device of the present invention is arranged in a device for performing a method for converting organic waste into fertilizer.

【図2】同正面図である。FIG. 2 is a front view of the same.

【図3】本発明の炭化物製造装置の一部破断側面図であ
る。
FIG. 3 is a partially cutaway side view of the carbide manufacturing device of the present invention.

【図4】供給機の断面図である。FIG. 4 is a sectional view of a feeder.

【図5】第2発酵槽の断面図である。FIG. 5 is a sectional view of a second fermenter.

【図6】木片回収装置の平面図である。FIG. 6 is a plan view of the wood chip collecting device.

【図7】同装置の側面図である。FIG. 7 is a side view of the same device.

【図8】図6中A−A矢視図である。8 is a view taken in the direction of arrows AA in FIG. 6;

【符号の説明】[Explanation of symbols]

1 混合部 2 炭化物製造装置 3 供給機 4 コンベア 5 予熱室 6 撹拌フレーム 7 燃焼部 7a バーナ加熱室 7b 穴 8 密閉炭化室 8a 螺旋排出スクリュー 8b ジャケット 9 第1発酵槽 10 隔壁 11 走行用レール 12 台車 13 移動用レール 14 撹拌搬送機保持台車 15 撹拌搬送機 16 シャベルローダ 17 搬送コンベア 18 供給機 19 第2発酵槽 20 木片回収装置 24 製品秤量包装装置 29 シール機 31 煙道 33 廃液口 35 取出し口 36 排気ファン DESCRIPTION OF SYMBOLS 1 Mixing part 2 Carbide manufacturing apparatus 3 Feeder 4 Conveyor 5 Preheating chamber 6 Stirring frame 7 Combustion part 7a Burner heating chamber 7b Hole 8 Closed carbonization chamber 8a Spiral discharge screw 8b Jacket 9 First fermenter 10 Partition wall 11 Rail for traveling 12 truck 13 Rail for transportation 14 Carriage holding agitating and transporting machine 15 Agitating and transporting machine 16 Shovel loader 17 Conveyor 18 Feeder 19 Second fermenter 20 Wood chip collecting device 24 Product weighing and packaging device 29 Sealing machine 31 Flue 33 Waste liquid outlet 35 Discharge port 36 Exhaust fan

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI C05F 9/02 C05F 9/04 9/04 B09B 3/00 A (58)調査した分野(Int.Cl.7,DB名) C10B 53/00 C01B 31/02 101 B09B 3/00 C02F 11/02 ZAB C05F 9/02 C05F 9/04 ────────────────────────────────────────────────── ─── Continuation of front page (51) Int.Cl. 7 identification code FI C05F 9/02 C05F 9/04 9/04 B09B 3/00 A (58) Field surveyed (Int.Cl. 7 , DB name) C10B 53/00 C01B 31/02 101 B09B 3/00 C02F 11/02 ZAB C05F 9/02 C05F 9/04

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 上部に植物性廃棄物を供給するホッパー
と空気孔を備え下部がテーパ状の縦型筒状ケーシング
と、前記ケーシングのテーパ部に設けられた分解開始着
火用穴の外周の着火用バーナ加熱室と、ケーシング下方
に連続して設けた円筒状炭化室と、該円筒状炭化室内部
の螺旋排出スクリューと、該円筒状炭化室外部の冷却水
ジャケットとケーシング内から排煙を吸引する排気ファ
ンとからなり、ケーシング上方のホッパーから投入され
着火用バーナの炎が前記分解開始着火用の穴から入って
着火されて燃焼部で分解の始まった植物性廃棄物を燃焼
部の下端部に設けた円筒状の炭化室へ螺旋排出スクリュ
ーで送り、冷却水ジャケットで冷却される炭化室壁面と
螺旋排出スクリューにより形成された密閉空間内で炭化
されて得られた炭化物を炭化室下部の取出し口より連続
的に取り出すようにしてなる炭化物連続製造装置。
1. A vertical cylindrical casing having an upper portion provided with a hopper for supplying vegetable waste and an air hole and having a tapered lower portion, and ignition of an outer periphery of a decomposition start ignition hole provided in a tapered portion of the casing. Suction smoke from the burner heating chamber, the cylindrical carbonization chamber continuously provided below the casing, the spiral discharge screw inside the cylindrical carbonization chamber, the cooling water jacket outside the cylindrical carbonization chamber, and the inside of the casing The lower end of the combustion portion is a waste fan that is turned on from the hopper above the casing, and the flame of the ignition burner enters through the hole for the decomposition start ignition and is ignited to start decomposing in the combustion portion. Carbide obtained by carbonization in the sealed space formed by the carbonization chamber wall and the spiral discharge screw cooled by the cooling water jacket and sent to the cylindrical carbonization chamber provided by the spiral discharge screw Carbide continuous manufacturing apparatus comprising as continuously removed from the coking chamber lower portion of the outlet.
JP28046097A 1997-10-14 1997-10-14 Continuous carbide production equipment Expired - Fee Related JP3131176B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP28046097A JP3131176B2 (en) 1997-10-14 1997-10-14 Continuous carbide production equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP28046097A JP3131176B2 (en) 1997-10-14 1997-10-14 Continuous carbide production equipment

Publications (2)

Publication Number Publication Date
JPH11116367A JPH11116367A (en) 1999-04-27
JP3131176B2 true JP3131176B2 (en) 2001-01-31

Family

ID=17625380

Family Applications (1)

Application Number Title Priority Date Filing Date
JP28046097A Expired - Fee Related JP3131176B2 (en) 1997-10-14 1997-10-14 Continuous carbide production equipment

Country Status (1)

Country Link
JP (1) JP3131176B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20030034312A (en) * 2001-10-22 2003-05-09 심연숙 automatic producing system of tablet type manure

Also Published As

Publication number Publication date
JPH11116367A (en) 1999-04-27

Similar Documents

Publication Publication Date Title
US5194069A (en) Method and apparatus for refinement of organic material
KR101295477B1 (en) Composting apparatus and method of organic waste
KR100372163B1 (en) Apparatus and method for producing fermentive feeds and composts from garbage
KR101113534B1 (en) Composting method of organic waste
CN1248792C (en) Organic waste material treatment process
KR101156250B1 (en) Composting apparatus and method of organic waste
CN1334152A (en) Process for treating city house refuse by wet decomposing method
US7052902B2 (en) Continuously operational biological reactor
US6056800A (en) Method of simultaneously composting anaerobic and aerobic material
CN1953826A (en) Refuse treatment apparatus
WO2014107791A1 (en) Method of aerobic treatment of poultry manure and apparatus for producing organic fertilizer
JP3131176B2 (en) Continuous carbide production equipment
CN213623900U (en) Kitchen waste aerobic composting equipment
JP2006026539A (en) Method for treating/reusing organic waste
JP3592622B2 (en) Method for producing carbonized fertilizer containing potassium component from organic waste
KR100427669B1 (en) Garbage disposal/lignite making system and manufacturing method of lignite using the same
KR100299069B1 (en) The methord and system of composting organic fertiliter with sewage sludge and food waste
JP3544646B2 (en) Garbage recycling system
JP3693910B2 (en) Method for producing carbonized product from organic waste
JP3549001B2 (en) Organic waste treatment system
KR20000031445A (en) Preparation of wet type feed using food garbage and apparatus thereof
KR102596533B1 (en) Composting fuel treated with sewage sludge and its treatment method and system
KR100321827B1 (en) Plant for processing kitchen refuge
NZ564496A (en) An apparatus and process for conversion of biomass/waste into bio-organic soil enricher & conditioner and fuel
JP3774791B2 (en) Used mushroom culture medium reprocessing equipment

Legal Events

Date Code Title Description
R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20081117

Year of fee payment: 8

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20091117

Year of fee payment: 9

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20101117

Year of fee payment: 10

LAPS Cancellation because of no payment of annual fees