JP3549001B2 - Organic waste treatment system - Google Patents

Organic waste treatment system Download PDF

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JP3549001B2
JP3549001B2 JP2002121120A JP2002121120A JP3549001B2 JP 3549001 B2 JP3549001 B2 JP 3549001B2 JP 2002121120 A JP2002121120 A JP 2002121120A JP 2002121120 A JP2002121120 A JP 2002121120A JP 3549001 B2 JP3549001 B2 JP 3549001B2
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conveyor
organic waste
decomposition
chips
tank
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JP2003311245A (en
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和行 鶴見
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株式会社湯浅産業
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    • 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
    • Y02A50/00TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/20Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
    • 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

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  • Mixers With Rotating Receptacles And Mixers With Vibration Mechanisms (AREA)
  • Accessories For Mixers (AREA)
  • Treating Waste Gases (AREA)
  • Processing Of Solid Wastes (AREA)
  • Combined Means For Separation Of Solids (AREA)
  • Treatment Of Sludge (AREA)

Description

【0001】
【発明の属する技術分野】
本発明は、有機質廃棄物(有機質汚泥など)をバクテリアにより分解処理する有機質廃棄物処理システムに関する。
【0002】
【従来の技術】
特開2001−334239号公報には、発酵処理での水分調整と通気性確保のために木片チップを用いる生ごみ等の発酵処理装置が開示されている。この装置では、生ごみ等の有機質廃棄物を破砕機で破砕してから、円形の発酵槽(乾式分解処理槽)内に圧送して投入し、発酵槽内で木片チップと共に撹拌機で撹拌して発酵させる。この撹拌機は、多数の撹拌羽根を有する縦型無端コンベアを循環させながら全体を旋回させることで、生ごみ等の有機質廃棄物と木片チップとを撹拌して混合しながら発酵槽の中心部へ徐々に移動させる。発酵槽の中心部まで移動してきた混合物を、発酵槽の底部の搬出用コンベアにより搬出し、篩い器で粉粒状の処理物(分解処理した有機質廃棄物)と木片チップとに篩い分ける。篩い分けた木片チップは、還元コンベアによって発酵槽に戻して循環使用する。
【0003】
【発明が解決しようとする課題】
しかし、この発酵処理装置は、木片チップを用いるものの、これは、発酵処理での水分調整と通気性を確保することが目的であり、しかもこれを発酵槽内で有機質廃棄物と共に撹拌することで混合している。従って、発酵(分解処理)に長時間を要し、また木片チップは、発酵熱で加熱されるとしても、多量の水分を吸水してそれ自体も発酵するので、劣化が激しく、水分調整と通気性の確保を安定して行うためには、多量の木片チップを補充しなければならず、ランニングコストが高くなる。また、篩い器で木片チップを篩い分ける場合、木片チップは腐敗しているので、分解処理して粉粒状となった有機質廃棄物との篩い分けが難しいとともに、篩い器で目詰まりを起こす等の問題がある。更に、発酵槽内で篩い分ける場合、槽内の温度が高く、処理物の含水率が高い上に発酵菌自体の水分も高いため、分離が困難である。
【0004】
本発明の目的は、このような従来技術に鑑み、多量(例えば、一日当たり10トン以上)の有機質廃棄物を、消滅菌にて分解率高く経済的に分解消滅処理できる有機質廃棄物処理システムを提供することにある。
【0005】
【課題を解決するための手段】
本発明は、多量の有機質廃棄物(汚泥)を分解処理するような場合、脱水ケーキにして持ち込まれることが多いことに鑑み、脱水ケーキにされた有機質廃棄物を原料として、これに、消滅菌を担持したバクテリアチップを混合してから、分解処理槽で撹拌して消滅菌で分解処理し、その処理に供したバクテリアチップは、分解処理された有機廃棄物と篩い分けして循環使用するようにしたものである。
【0006】
すなわち、本発明の有機質廃棄物処理システムは、プッシャを内蔵するとともに、上下に循環するスクレーパコンベアを一端に備え、脱水ケーキにして投入された有機質廃棄物をプッシャで押圧してスクレーパコンベアで下側に一定量ずつ送り出す原料ホッパと、消滅菌を担持したバクテリアチップをコンベアにより搬出するチップホッパと、原料ホッパから送り出されてきた有機質廃棄物とチップホッパから搬出されてきたバクテリアチップとをそれぞれ一定量ずつ混合機搬入用コンベアにより搬入して混合する混合機と、この混合機で混合された混合物を分解処理槽搬入用コンベアにより上部から搬入し、撹拌しながら消滅菌にて分解処理する屋根付きの分解処理槽と、この分解処理槽から排出されてくる処理物を導入して、分解処理有機物とバクテリアチップとに篩い分けする篩い分け機と、篩い分けられたバクテリアチップをチップホッパへ返送するチップ返送用コンベアとを備えてなるものである。
【0007】
分解処理槽としては、多数の撹拌羽根を有する縦型無端コンベアを循環させながら全体を旋回させることで混合物を撹拌しながら移動させる撹拌機と、分解処理槽搬入用コンベアにより上部から搬入されてくる混合物を分配撒布する分配コンベアと、外気を底部から送気する送気装置と、処理物を底部から搬出する搬出用コンベアとを内蔵したものが良い。
【0008】
また、チップホッパとしては、送り出しコンベアを内蔵するとともに、上下に循環するスクレーパコンベアを一端に備え、バクテリアチップを送り出しコンベアで搬送してスクレーパコンベアで下側に一定量ずつ送り出すものが良い。
【0009】
分解処理槽からの排気については、分解処理槽からの排気を酸洗中和塔で酸性シャワー水に接触させてアンモニアを中和させた後、該酸洗中和塔から吸気した臭気を更に土壌脱臭装置にて土壌脱臭すると良い。
【0010】
原料ホッパ及びチップホッパのそれぞれにおいて、スクレーパコンベアの回転速度を調整することにより下側へ一定量ずつ送り出すので、混合比を常に一定にできる。
【0011】
【発明の実施の形態】
次に、本発明の実施の形態を図面に基づいて詳細に説明する。
【0012】
図1に、本発明による有機質廃棄物処理システムの構成とその処理の流れを示す。この有機質廃棄物処理システムは、主要構成部として、原料ホッパ1とチップホッパ2と混合機3と分解処理槽4と酸洗中和塔5と土壌脱臭装置6と篩い分け機7とを備えている。
【0013】
原料ホッパ1は、脱水ケーキにしてトラック8にて運搬されてきた有機質廃棄物を、トラック8からそのまま投入できるように、地表より低いところに構築され、またチップホッパ2も、トラック9にて運搬されてきたバクテリアチップ(消滅菌担持体)を、トラック9からそのまま投入できるように、同様に地表より低いところに構築されている。
【0014】
原料ホッパ1は、プッシャ10を内蔵するとともに、上下に循環するスクレーパコンベア11を一端に具備し、上蓋12を開けて投入口から投入された有機質廃棄物(脱水ケーキ)を、プッシャ10で押圧してスクレーパコンベア11で下側に掻き出すようになっている。この原料ホッパ1の処理重量は例えば18トン/日である。掻き出された有機質廃棄物は、混合機搬入用コンベアであるスクリューコンベア13にて混合機3に投入される。プッシャ10の推進速度とスクリューコンベア13の回転速度を調整することにより、脱水ケーキである有機質廃棄物を一定量ずつ送り出すことができる。
【0015】
チップホッパ2は、送り出しコンベア(ベルトコンベア)14を下部に内蔵するとともに、上下に循環するスクレーパコンベア15を一端に備え、上蓋16を開けて投入口から投入されたバクテリアチップを送り出しコンベア14で搬送してスクレーパコンベア15で下側に掻き出す。このチップホッパ2の処理重量も原料ホッパ1と同じく例えば18トン/日である。掻き出されたバクテリアチップは、混合機搬入用コンベアであるスクリューコンベア17にて混合機3に投入される。送り出しコンベア14の搬送速度とスクリューコンベア17のの回転速度を調整することにより、バクテリアチップを一定量ずつ送り出すことができる。
【0016】
バクテリアチップは、樹脂やセラミック等の発酵しない材質のチップに消滅菌を担持したもので、繰り返し使用できる。
【0017】
混合機3は、スクリューコンベア13・17から投入された有機質廃棄物とバクテリアチップとを、ほぼ等重量の割合で混合して排出する。その排出された混合物は、分解処理槽搬入用コンベア18にて上昇搬送され、分解処理槽4内へその上部から搬入される。
【0018】
分解処理槽4は、二重円筒壁のドーム型(屋根付き)円形槽で、上部に分配コンベア19、それより下方に撹拌機20、底部に送気装置21及び搬出用コンベア22を内蔵している。この分解処理槽4の仕様の一例を示すと、直径20m程度、有効内容積565mで、消滅菌の発酵熱による最高温度65〜80℃である。このため、分解処理槽4の中央まで送られたときには含水率が20〜30%となり、その後の篩い分けを容易に行える。
【0019】
分配コンベア19は、分解処理槽搬入用コンベア18により上部から搬入されてくる混合物を、分解処理槽4の半径方向に分配して撒布する。
【0020】
撹拌機20は、多数の撹拌羽根を上下に間隔をおいて設けた縦型無端コンベア23を、循環させながら全体を旋回移動させることにより、分解処理槽4内の混合物を撹拌しながら徐々に底部の中央へ移動させる。その具体的構造については、本発明者が先に提案した特許第3194141号公報に説明されている。
【0021】
送気装置21は、外部のブロアー24からの新鮮な空気を、分解処理槽4内の底部のほぼ全域にわたり多数のノズルから上向きに平均に送気する。
【0022】
有機質廃棄物とバクテリアチップとの混合物は、このように外気を底部から送気されながら撹拌機20にて撹拌され、有機質廃棄物は、消滅菌により水分と二酸化炭素とアンモニアに分解される。
【0023】
本例の場合、撹拌機20は、その縦型無端コンベア23を循環させながら全体を順方向に旋回させることで、有機質廃棄物とバクテリアチップとの混合物を分解処理槽4の中央へと移動させる順方向送りと、全体を逆方向に旋回させることで、分解処理槽4の周壁部へと移動させる逆方向移動とを日交互に行い、これを数日間繰り返すことで、有機質廃棄物の大半が消滅したら、順方向送りのみを1日2回行って分解処理槽4の底部の中央へ集める。
【0024】
搬出用コンベア22は、分解処理槽4内の底部の下側に設置されており、上記のように分解処理槽4内の底部の中央へ集まったバクテリアチップを含む分解処理済み有機物を、分解処理槽4の外周部へ搬送してそこから外部へ搬出する。
【0025】
分解処理槽4から搬出されたバクテリアチップを含む分解処理済み有機物は、篩い分け機搬入用コンベア25にて篩い分け機7に搬入される。
【0026】
篩い分け機7は、分解処理済み有機物とバクテリアチップとを篩い分ける。篩い分けられたバクテリアチップは、密閉型バケットコンベア等のチップ返送用コンベア26にてチップホッパ2へ返送され、循環使用される。篩い分けられた分解処理済み有機物は、袋詰め装置27にて袋詰めされた後、搬送パレットに載置して保管場所へ保管される。篩い分け機7で篩い分けられなかった残滓は残滓ホッパ28により回収され、また篩い分け機7内で発生した塵粉は外部の集塵装置で集塵される。
【0027】
一方、分解処理槽4の天井部中央からの排気は、排気ダクト29を通じて酸洗中和塔5に吸気される。酸洗中和塔5は、本例の場合、同じもの2塔を2段に連結したもので、そのぞれぞれにおいて、硫酸タンク30からの硫酸を貯留タンク31に補給してPHコントローラにより酸性水とし、これをポンプ32にて酸性シャワー水として内部で散水しながら循環させることで、分解処理槽4からの排気中のアンモニアを中和させるようになっており、これを2塔の分解処理槽4にて2段階に行う。
【0028】
更に、脱臭用吸気ファン33にて分解処理槽4から吸気して土壌脱臭装置6へ送り、ここで土壌により脱臭を行う。土壌脱臭装置6は、土壌層34上にセラミック炭層36を形成したもので、ここで生じた汚水は汚水ピット36に貯留される。この汚水及び酸洗中和塔5での汚水は、汚水処理施設へ送られて別途処理される。
【0029】
【発明の効果】
以上説明したように、本発明は、脱水ケーキにされた有機質廃棄物を原料として、これを原料ホッパに投入し、原料ホッパ内でプッシャで押圧してスクレーパコンベアの回転速度を調整することにより一定量ずつ下側に送り出し、混合機に投入して消滅菌を担持したバクテリアチップと混合してから、分解処理槽で撹拌して消滅菌で分解処理し、その処理に供したバクテリアチップは、分解処理された有機廃棄物と篩い分けして循環使用するので、多量の有機質廃棄物を分解率高く経済的に分解処理できる。
【0030】
請求項2に係る発明は、有機質廃棄物とバクテリアチップとの混合物を、分解処理槽内において上から分配撒布し、これを撹拌機で撹拌しながらしかも送気装置にて下から送気しながら移動させ、分解処理槽の底部から搬出するので、分解処理を効率良く行える。
【0031】
請求項3に係る発明は、バクテリアチップを、チップホッパ内で送り出しコンベアで搬送してスクレーパコンベアで一定量ずつ下側に送り出すので、バクテリアチップを脱水ケーキである有機質廃棄物の送り出しと同期させながら、混合機に連続して投入して、所望の割合に混合できる。
【0032】
請求項4に係る発明は、分解処理槽からの排気を酸洗中和塔で酸性シャワー水に接触させてアンモニアを中和させた後、該酸洗中和塔から吸気した臭気を更に土壌脱臭装置にて土壌脱臭するので、脱臭処理も効率良く行える。
【図面の簡単な説明】
【図1】本発明による有機質廃棄物処理システムの構成とその処理の流れを示す図である。
【符号の説明】
1 原料ホッパ
2 チップホッパ
3 混合機
4 分解処理槽
5 酸洗中和塔
6 土壌脱臭装置
7 篩い分け機
8・9 トラック
10 プッシャ
11 スクレーパコンベア
12 上蓋
13 スクリューコンベア
14 送り出しコンベア
15 スクレーパコンベア
16 上蓋
17 スクリューコンベア
18 分解処理槽搬入用コンベア
19 分配コンベア
20 撹拌機
21 送気装置
22 搬出用コンベア
23 縦型無端コンベア
24 ブロアー
25 篩い分け機搬入用コンベア
26 チップ返送用コンベア
27 袋詰め装置
28 残滓ホッパ
29 排気ダクト
30 硫酸タンク
30 貯留タンク
32 ポンプ
33 脱臭用吸気ファン
34 土壌層
36 セラミック炭層
[0001]
TECHNICAL FIELD OF THE INVENTION
The present invention relates to an organic waste treatment system that decomposes organic waste (eg, organic sludge) with bacteria.
[0002]
[Prior art]
Japanese Patent Application Laid-Open No. 2001-334239 discloses a fermentation treatment apparatus for kitchen garbage and the like using wood chip chips for moisture adjustment and air permeability in the fermentation treatment. In this device, organic waste such as garbage is crushed by a crusher, and then fed into a circular fermentation tank (dry decomposition treatment tank) by pressure and stirred with a stirrer together with wood chip in the fermentation tank. Ferment. This stirrer, by circulating the whole while circulating a vertical endless conveyor having a large number of stirring blades, stirs and mixes organic waste such as garbage and wood chip with the center of the fermenter while mixing. Move slowly. The mixture that has moved to the center of the fermenter is carried out by a carry-out conveyor at the bottom of the fermenter, and is sieved by a sieve into powdery and granular processed materials (decomposed organic waste) and wood chip. The sieved wood chips are returned to the fermenter by a reduction conveyor and used for circulation.
[0003]
[Problems to be solved by the invention]
However, although this fermentation treatment apparatus uses wood chips, the purpose is to ensure moisture control and air permeability in the fermentation treatment, and furthermore, by stirring this together with organic waste in the fermentation tank. Mixed. Therefore, fermentation (decomposition processing) takes a long time, and even if the wood chip is heated by fermentation heat, it absorbs a large amount of water and ferment itself, so that it deteriorates violently. In order to stably maintain the properties, a large amount of wood chip chips must be replenished, which increases running costs. Also, when sieving wood chips with a sieving machine, the wood chips are decayed, so it is difficult to sieve with organic waste that has been decomposed and turned into powder and granules, and clogging occurs in the sieving machine. There's a problem. Furthermore, in the case of sieving in a fermentation tank, separation is difficult because the temperature in the tank is high, the water content of the processed product is high, and the moisture of the fermentation bacteria itself is high.
[0004]
SUMMARY OF THE INVENTION An object of the present invention is to provide an organic waste treatment system capable of economically dissolving large amounts (for example, 10 tons or more per day) of organic waste at a high decomposition rate by disinfection and economically in view of such conventional technology. To provide.
[0005]
[Means for Solving the Problems]
The present invention is based on the fact that when a large amount of organic waste (sludge) is decomposed, it is often brought into a dewatered cake. After mixing the bacterial chips carrying the same, the mixture is stirred in a decomposition treatment tank and disintegrated by sterilization, and the bacterial chips subjected to the treatment are sieved from the decomposed organic waste and recycled. It was made.
[0006]
That is, the organic waste treatment system of the present invention has a built-in pusher, a scraper conveyor that circulates up and down at one end, and pushes the organic waste input as a dewatered cake with the pusher and pushes the organic waste downward with the scraper conveyor. The raw material hopper that feeds a fixed amount to each of the raw materials, the chip hopper that transports the bacterial chips carrying sterilization by a conveyor, and the organic waste that is discharged from the raw material hopper and the bacterial chips that are transported from the chip hopper are mixed by a fixed amount. A mixing machine that carries in and mixes it with a conveyor for carrying in a machine, and a decomposition process with a roof in which the mixture mixed by this mixer is carried in from above by a conveyor for carrying in a decomposition treatment tank, and disintegrated by disinfection while stirring. The tank and the treated material discharged from this decomposition treatment tank are introduced, and And goods and bacteria chip and the sieving sieving machine is made and a chip return conveyor for returning the bacteria chips were sieved to Chippuhoppa.
[0007]
As the decomposition treatment tank, the vertical endless conveyor having a large number of stirring blades is circulated while being swirled to move the mixture while stirring, and the decomposition treatment tank is carried in from the top by a conveyor for carrying in the decomposition treatment tank. It is preferable to incorporate a distribution conveyor for distributing and dispersing the mixture, an air supply device for supplying outside air from the bottom, and a carry-out conveyor for carrying out the processed material from the bottom.
[0008]
Further, as the chip hopper, it is preferable to have a scraper conveyer built in at one end and a scraper conveyer circulating up and down at one end, to convey the bacterial chips by the conveyer and to send out a predetermined amount by the scraper conveyer downward.
[0009]
Regarding the exhaust gas from the decomposition tank, the exhaust gas from the decomposition tank was brought into contact with acidic shower water in a pickling neutralization tower to neutralize the ammonia, and then the odor sucked from the pickling neutralization tower was further removed from the soil. It is good to deodorize the soil with a deodorizer.
[0010]
In each of the raw material hopper and the chip hopper, a constant amount is sent downward by adjusting the rotation speed of the scraper conveyor, so that the mixing ratio can be always kept constant.
[0011]
BEST MODE FOR CARRYING OUT THE INVENTION
Next, embodiments of the present invention will be described in detail with reference to the drawings.
[0012]
FIG. 1 shows a configuration of an organic waste treatment system according to the present invention and a flow of the treatment. This organic waste treatment system includes, as main components, a raw material hopper 1, a chip hopper 2, a mixer 3, a decomposition tank 4, a pickling neutralization tower 5, a soil deodorizing device 6, and a sieving machine 7. .
[0013]
The raw material hopper 1 is constructed below the ground surface so that the organic waste, which has been transported by the truck 8 as a dehydrated cake, can be directly input from the truck 8, and the chip hopper 2 is also transported by the truck 9. Similarly, the bacteria chip (sterilized carrier) is constructed at a lower level than the ground surface so that it can be introduced from the truck 9 as it is.
[0014]
The raw material hopper 1 has a built-in pusher 10 and a scraper conveyor 11 that circulates up and down at one end. The upper lid 12 is opened, and the organic waste (dehydrated cake) input from the input port is pressed by the pusher 10. The scraper conveyor 11 scrapes it down. The processing weight of the raw material hopper 1 is, for example, 18 tons / day. The scraped organic waste is put into the mixer 3 by the screw conveyor 13 which is a conveyor for carrying the mixer. By adjusting the propulsion speed of the pusher 10 and the rotation speed of the screw conveyor 13, it is possible to send out a certain amount of organic waste as a dewatered cake.
[0015]
The chip hopper 2 has a built-in conveyor (belt conveyor) 14 at its lower part, and has a scraper conveyor 15 circulating up and down at one end. The upper lid 16 is opened, and the bacterial chip input from the inlet is fed out and conveyed by the conveyor 14. And scrape it down with a scraper conveyor 15. The processing weight of the chip hopper 2 is, for example, 18 tons / day, similarly to the raw material hopper 1. The scraped-out bacterial chips are introduced into the mixer 3 by the screw conveyor 17 which is a conveyor for carrying the mixer. By adjusting the transport speed of the feed conveyor 14 and the rotation speed of the screw conveyor 17, the bacterial chips can be sent out by a fixed amount.
[0016]
A bacterial chip is a chip made of a material that does not ferment, such as a resin or a ceramic, which is sterilized and can be used repeatedly.
[0017]
The mixing machine 3 mixes and discharges the organic waste and the bacterial chips input from the screw conveyors 13 and 17 at a substantially equal weight ratio. The discharged mixture is conveyed upward by the conveyor 18 for carrying in the decomposition treatment tank, and is carried into the decomposition treatment tank 4 from above.
[0018]
The decomposition processing tank 4 is a dome-shaped (with a roof) circular tank having a double cylindrical wall, and includes a distribution conveyor 19 at an upper portion, a stirrer 20 below the distribution conveyor 19, and an air supply device 21 and an unloading conveyor 22 at a bottom portion. I have. As an example of the specification of the decomposition treatment tank 4, the diameter is about 20 m, the effective internal volume is 565 m 3 , and the maximum temperature is 65 to 80 ° C. due to the heat of fermentation for disinfection. For this reason, when sent to the center of the decomposition treatment tank 4, the water content becomes 20 to 30%, and subsequent sieving can be easily performed.
[0019]
The distribution conveyor 19 distributes and distributes the mixture carried in from the upper part by the conveyor 18 for carrying out the decomposition treatment tank in the radial direction of the decomposition treatment tank 4.
[0020]
The stirrer 20 circulates a vertical endless conveyor 23 in which a number of stirring blades are provided at intervals vertically, while circulating the same so that the mixture in the decomposition treatment tank 4 is gradually stirred at the bottom. To the center of the The specific structure is described in Japanese Patent No. 3194141 previously proposed by the present inventor.
[0021]
The air supply device 21 sends the fresh air from the external blower 24 from a large number of nozzles in an upward direction over substantially the entire bottom of the decomposition treatment tank 4 in an average manner.
[0022]
The mixture of the organic waste and the bacterial chip is stirred by the stirrer 20 while the outside air is supplied from the bottom in this way, and the organic waste is decomposed into moisture, carbon dioxide, and ammonia by sterilization.
[0023]
In the case of this example, the stirrer 20 moves the mixture of the organic waste and the bacterial chips to the center of the decomposition treatment tank 4 by circulating the whole in the forward direction while circulating the vertical endless conveyor 23. The forward feeding and the reverse movement of moving the whole to the peripheral wall portion of the decomposition treatment tank 4 by turning the whole body in the reverse direction are alternately performed on a daily basis, and by repeating this for several days, most of the organic waste is reduced. When it disappears, only forward feeding is performed twice a day and collected in the center of the bottom of the decomposition treatment tank 4.
[0024]
The unloading conveyor 22 is installed below the bottom of the decomposition processing tank 4 and decomposes the organic matter that has been subjected to the decomposition processing including the bacterial chips collected at the center of the bottom of the decomposition processing tank 4 as described above. It is conveyed to the outer peripheral part of the tank 4 and is carried out therefrom.
[0025]
The decomposition-treated organic matter including the bacterial chips carried out from the decomposition treatment tank 4 is carried into the sieving machine 7 by the sieving machine carry-in conveyor 25.
[0026]
The sieving machine 7 sieves the decomposed organic matter and the bacterial chips. The sieved bacterial chips are returned to the chip hopper 2 by a chip return conveyor 26 such as a closed bucket conveyor, and are circulated. The sieved and decomposed organic matter is packed in a bag by the bag packing device 27, and then placed on a transport pallet and stored in a storage place. Residues that have not been sieved by the sieving machine 7 are collected by a residue hopper 28, and dust generated in the sieving machine 7 is collected by an external dust collector.
[0027]
On the other hand, the exhaust gas from the center of the ceiling of the decomposition tank 4 is sucked into the pickling neutralization tower 5 through the exhaust duct 29. In this example, the acid pickling neutralization tower 5 is composed of two identical towers connected in two stages. In each case, the sulfuric acid from the sulfuric acid tank 30 is supplied to the storage tank 31 and the storage tank 31 is supplied thereto by the PH controller. The acidic water is circulated while being sprinkled internally as acidic shower water by the pump 32, thereby neutralizing the ammonia in the exhaust gas from the decomposition treatment tank 4. The treatment is performed in two stages in the treatment tank 4.
[0028]
Further, the air is taken from the decomposition treatment tank 4 by the deodorizing intake fan 33 and sent to the soil deodorizing device 6, where the soil is deodorized. The soil deodorizing device 6 is a device in which a ceramic charcoal layer 36 is formed on a soil layer 34, and sewage generated here is stored in a sewage pit 36. The sewage and the sewage in the pickling neutralization tower 5 are sent to a sewage treatment facility to be separately treated.
[0029]
【The invention's effect】
As described above, the present invention uses an organic waste made into a dewatered cake as a raw material, puts it into a raw material hopper, and presses the raw material hopper with a pusher in the raw material hopper to adjust the rotation speed of the scraper conveyor to thereby maintain a constant value. Dispense by volume into a mixer, mix it with the sterilized bacterial chip, mix it in a digestion tank and disinfect it by sterilization. Since the treated organic waste is sieved and recycled, a large amount of organic waste can be economically decomposed at a high decomposition rate.
[0030]
The invention according to claim 2 is that the mixture of the organic waste and the bacterial chips is distributed and sprayed from above in the decomposition treatment tank, and the mixture is stirred by the stirrer and sent from below by the air supply device. Since it is moved and carried out from the bottom of the decomposition treatment tank, the decomposition treatment can be performed efficiently.
[0031]
The invention according to claim 3 is that the bacterial chips are conveyed in a chip hopper by a sending-out conveyor and sent downward by a fixed amount by a scraper conveyor, so that the bacterial chips are synchronized with the sending of the organic waste as a dehydrated cake, It can be continuously charged into a mixer and mixed at a desired ratio.
[0032]
The invention according to claim 4 is that, after the exhaust gas from the decomposition treatment tank is brought into contact with acidic shower water in a pickling neutralization tower to neutralize ammonia, the odor sucked from the pickling neutralization tower is further deodorized to soil. Since the soil is deodorized by the device, the deodorizing treatment can be performed efficiently.
[Brief description of the drawings]
FIG. 1 is a diagram showing a configuration of an organic waste treatment system according to the present invention and a flow of the treatment.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Raw material hopper 2 Chip hopper 3 Mixer 4 Decomposition tank 5 Pickling neutralization tower 6 Soil deodorizer 7 Sieving machine 8.9 Truck 10 Pusher 11 Scraper conveyor 12 Top lid 13 Screw conveyor 14 Delivery conveyor 15 Scraper conveyor 16 Top lid 17 Screw Conveyor 18 Conveyor for disassembling treatment tank 19 Distribution conveyor 20 Stirrer 21 Air supply device 22 Conveyor for unloading 23 Vertical endless conveyor 24 Blower 25 Conveyor for sieving machine 26 Conveyor for chip return 27 Bagging device 28 Residue hopper 29 Exhaust Duct 30 Sulfuric acid tank 30 Storage tank 32 Pump 33 Deodorizing intake fan 34 Soil layer 36 Ceramic coal layer

Claims (4)

プッシャを内蔵するとともに、上下に循環するスクレーパコンベアを一端に備え、脱水ケーキにして投入された有機質廃棄物をプッシャで押圧してスクレーパコンベアで下側に一定量ずつ送り出す原料ホッパと、
消滅菌を担持したバクテリアチップをコンベアにより搬出するチップホッパと、
前記原料ホッパから送り出されてきた有機質廃棄物と前記チップホッパから搬出されてきたバクテリアチップとをそれぞれ一定量ずつ混合機搬入用コンベアにより搬入して混合する混合機と、
この混合機で混合された混合物を分解処理槽搬入用コンベアにより上部から搬入し、撹拌しながら消滅菌にて分解処理する屋根付きの分解処理槽と、
この分解処理槽から排出されてくる処理物を導入して、分解処理済み有機物とバクテリアチップとに篩い分けする篩い分け機と、
篩い分けられたバクテリアチップを前記チップホッパへ返送するチップ返送用コンベアとを備えてなることを特徴とする有機質廃棄物処理システム。
A raw material hopper that has a built-in pusher and a scraper conveyor that circulates up and down at one end, pushes organic waste input as a dewatered cake with a pusher, and sends out a fixed amount to the lower side with a scraper conveyor,
A chip hopper for carrying out the bacteria chips carrying sterilization by a conveyor,
A mixer that mixes the organic waste that has been sent out from the raw material hopper and the bacterial chips that have been unloaded from the chip hopper by a predetermined amount, respectively, by a mixer loading conveyor.
A decomposition treatment tank with a roof that carries the mixture mixed by this mixer from the upper part by a conveyor for carrying in the decomposition treatment tank and disintegrates by disinfection while stirring,
A sieving machine that introduces the treated material discharged from the decomposition treatment tank and sieves the decomposition-treated organic matter and the bacterial chips,
An organic waste treatment system comprising: a chip return conveyor for returning the sieved bacterial chips to the chip hopper.
分解処理槽は、多数の撹拌羽根を有する縦型無端コンベアを循環させながら全体を旋回させることで混合物を撹拌しながら移動させる撹拌機と、分解処理槽搬入用コンベアにより上部から搬入されてくる混合物を分配撒布する分配コンベアと、外気を底部から送気する送気装置と、処理物を底部から搬出する搬出用コンベアとを内蔵していることを特徴とする請求項1に記載の有機質廃棄物処理システム。The decomposition tank is a stirrer that moves while stirring the mixture by rotating the whole while circulating a vertical endless conveyor having a large number of stirring blades, and a mixture that is carried in from the top by a conveyor for carrying the decomposition processing tank. The organic waste according to claim 1, further comprising a distribution conveyor for distributing and dispersing the air, an air supply device for supplying outside air from the bottom, and a carry-out conveyor for carrying out the processed material from the bottom. Processing system. チップホッパは、送り出しコンベアを内蔵するとともに、上下に循環するスクレーパコンベアを一端に備え、バクテリアチップを送り出しコンベアで搬送してスクレーパコンベアで下側に一定量ずつ送り出すことを特徴とする請求項1又は2に記載の有機質廃棄物処理システム。The chip hopper has a built-in feeder conveyor, a scraper conveyor that circulates up and down at one end, and transports the bacterial chips by the feeder conveyor and sends out the bacteria chips by the scraper conveyor by a fixed amount. Organic waste treatment system according to 1. 分解処理槽からの排気を酸性シャワー水に接触させる酸洗中和塔と、該酸洗中和塔から吸気された臭気を土壌にて脱臭する土壌脱臭装置とを更に備えたことを特徴とする請求項1、2又は3に記載の有機質廃棄物処理システム。It further comprises a pickling neutralization tower for bringing the exhaust gas from the decomposition treatment tank into contact with the acidic shower water, and a soil deodorizing device for deodorizing the odor sucked from the pickling neutralization tower in the soil. The organic waste treatment system according to claim 1, 2 or 3.
JP2002121120A 2002-04-23 2002-04-23 Organic waste treatment system Expired - Fee Related JP3549001B2 (en)

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