JPS5852720B2 - Fermentation treatment equipment for sewage sludge, etc. - Google Patents

Fermentation treatment equipment for sewage sludge, etc.

Info

Publication number
JPS5852720B2
JPS5852720B2 JP54107418A JP10741879A JPS5852720B2 JP S5852720 B2 JPS5852720 B2 JP S5852720B2 JP 54107418 A JP54107418 A JP 54107418A JP 10741879 A JP10741879 A JP 10741879A JP S5852720 B2 JPS5852720 B2 JP S5852720B2
Authority
JP
Japan
Prior art keywords
main body
fermentation
chevron
sludge
sewage sludge
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
Application number
JP54107418A
Other languages
Japanese (ja)
Other versions
JPS5631499A (en
Inventor
栄一 武藤
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.)
Hitachi Kiden Kogyo Ltd
Original Assignee
Hitachi Kiden Kogyo Ltd
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 Hitachi Kiden Kogyo Ltd filed Critical Hitachi Kiden Kogyo Ltd
Priority to JP54107418A priority Critical patent/JPS5852720B2/en
Publication of JPS5631499A publication Critical patent/JPS5631499A/en
Publication of JPS5852720B2 publication Critical patent/JPS5852720B2/en
Expired 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

Landscapes

  • Treatment Of Sludge (AREA)
  • Fertilizers (AREA)

Description

【発明の詳細な説明】 本発明は家畜糞、下水処理場などより回収されるスクリ
ーン渣、下水汚泥、都市とみ等を好気性の微生物によっ
て発酵分解し、堆肥化する下水汚泥等の発酵処理装置に
関するものである。
Detailed Description of the Invention The present invention is a fermentation treatment device for sewage sludge, etc., which ferments and decomposes livestock manure, screen sludge collected from sewage treatment plants, sewage sludge, urban sludge, etc. using aerobic microorganisms and turns it into compost. It is related to.

本発明の目的とするところは一つの発酵槽内に投入され
る発酵処理をすべき下水汚泥等が圧密されることなく、
且揺動装置が使用されることなく充分に空気と接触し、
発酵処理を効果的に行なわんとするもので、以下本発明
を図示の実施例に基づいて詳細に説明する。
The purpose of the present invention is to prevent sewage sludge, etc. to be subjected to fermentation treatment, which is introduced into one fermentation tank, from becoming compacted.
In addition, sufficient contact with air is achieved without using a rocking device,
The present invention is intended to effectively carry out fermentation treatment, and the present invention will be described in detail below based on illustrated embodiments.

図に於て1は発酵処理装置の本体で、これは一度に下水
汚泥等を発酵処理できる容量を有すると共に上部2の形
状を山形とし、安息角以上のテーパ角を有し、その頂部
より供給コンベア等5にて装置全体に均一になるように
して下水汚泥等を供給するようになす。
In the figure, 1 is the main body of the fermentation treatment equipment, which has a capacity to ferment sewage sludge, etc. at one time, and has a chevron-shaped upper part 2, with a taper angle greater than the angle of repose, and is supplied from the top. Sewage sludge, etc. is supplied uniformly to the entire device by a conveyor or the like 5.

又該本体1の下部3の形状を上部形状と全く逆になるよ
う逆M字形とし、底部中央が上方に突出し、両側がくぼ
んだ形状とすると共にこの両側外壁に発酵処理済の堆肥
となった下水汚泥等を取り出す排出口4を設ける。
In addition, the shape of the lower part 3 of the main body 1 is made into an inverted M-shape, which is completely opposite to the shape of the upper part, with the center of the bottom protruding upward and both sides concave, and fermented compost is formed on the outer walls of both sides. A discharge port 4 is provided to take out sewage sludge, etc.

また本体1内には山形をした規制板6を水平方向に所要
の間隔をおいて多数配列すると共にこの規制板6を本体
の上下方向にも複数段設置する。
Further, a large number of chevron-shaped regulating plates 6 are arranged in the main body 1 at required intervals in the horizontal direction, and a plurality of regulating plates 6 are also installed in a plurality of stages in the vertical direction of the main body.

この時上下方向の規制板6は千鳥状とし、上段側より落
下してくる被発酵物は下段側の山形をした規制板上に落
下し、これにて分散されほぐされるようになす。
At this time, the regulation plates 6 in the vertical direction are arranged in a staggered manner, so that the fermented material falling from the upper stage falls onto the chevron-shaped regulation plate on the lower stage, thereby being dispersed and loosened.

この各段の規制板の山形をした内側には給気管7を配設
し、本体外より発酵に必要な空気あるいは加温空気を供
給する。
An air supply pipe 7 is arranged inside the chevron-shaped regulation plate of each stage to supply air or heated air necessary for fermentation from outside the main body.

この給気管γは全段の規制板すべてに設けることも可能
であるが本体内全体に亘って給気が均一に行えると共に
給気が円滑となるよう給気と排気とを各段交互に行うこ
ともある。
Although it is possible to provide this air supply pipe γ on all the regulation plates of all stages, it is necessary to supply and exhaust air alternately at each stage so that the air can be supplied uniformly throughout the main body and the air supply is smooth. Sometimes.

さらに本体1内に設置する規制板6は伺段目毎あるいは
1〜2段毎に上段側の規制板と直交するように配列して
上方より順次規制板を経て落下する被処理物が本体内を
前後左右方向に拡散され混合攪拌がより一層行なわれ、
空気との接触効率を向上し、且被処理物が均一して発酵
できるようになすことも可能である。
Further, the regulation plates 6 installed in the main body 1 are arranged perpendicularly to the regulation plate on the upper stage for each step or every 1st or 2nd stage, so that the objects to be processed that fall from above sequentially through the regulation plates are placed inside the main body. The mixture is dispersed in the front, rear, left and right directions for even more mixing and agitation.
It is also possible to improve the efficiency of contact with air and to uniformly ferment the material to be treated.

尚図中8は排気管を示す。Note that 8 in the figure indicates an exhaust pipe.

而して上述の如く構成した発酵処理装置にて下水汚泥、
スクリーン渣、都市とみ等を発酵処理を行う場合、壕ず
発酵に必要な含水率に調速した後、本体1の上部より供
給用のコンベア5にて投入すると各段の山形をした規制
板に衝突しつつ且分散されつつ各段の規制板間を経て本
体1の底部に達する。
Then, sewage sludge,
When fermenting screen residue, urban waste, etc., after regulating the moisture content necessary for trenchless fermentation, it is fed into the feeding conveyor 5 from the top of the main body 1, and it is fed to the chevron-shaped regulation plate at each stage. It reaches the bottom of the main body 1 after passing between the regulating plates of each stage while colliding and being dispersed.

順次下水汚泥等を供給投入することによって本体内は充
填される。
The main body is filled by sequentially supplying sewage sludge, etc.

そしてこの汚泥等の供給とともKあるいは供給後、給気
を行う好気性雰囲気が形成されこれに含有された微生物
(好気性発酵菌)にて分解発酵される。
When the sludge and the like are supplied, an aerobic atmosphere is formed in which air is supplied, and the microorganisms (aerobic fermentation bacteria) contained in this atmosphere decompose and ferment.

この発酵は規制板の各段毎に行なわれ上部より下部に至
るに従いその発酵過程は進み、最下部に達する時所望の
発酵が完了され堆肥化されるようになす。
This fermentation is carried out at each stage of the regulating plate, and the fermentation process progresses from the top to the bottom, and when the bottom is reached, the desired fermentation is completed and the material is composted.

従って本体1の大きさ及び規制板の段数はこの発酵時間
等にて予じめ定められるものである。
Therefore, the size of the main body 1 and the number of stages of the regulating plates are determined in advance based on this fermentation time and the like.

そして発酵が完了した汚泥等は排出口4の下部に設けら
れた排出用コンベア9上に取り出し排出すると本体内の
発酵中の汚泥等は排出された量のみ順次上方より下方へ
移動し、この移動時に於て分散攪拌され、圧密化が防止
される。
When the fermented sludge, etc. is taken out and discharged onto the discharge conveyor 9 provided at the bottom of the discharge port 4, the sludge, etc. undergoing fermentation inside the main body is sequentially moved from the upper part to the lower part, and this movement Sometimes it is dispersed and stirred to prevent compaction.

このようにして本体内への給気と排気を連続的に行ない
有機物の発酵は促進され含水率も低減する。
In this way, air is continuously supplied and exhausted into the main body, thereby promoting the fermentation of organic matter and reducing the moisture content.

本体内上部に空間が生じると供給用コンベアを再び稼動
し下水汚泥等の供給を本体内に満ちる1で行う。
When a space is created in the upper part of the main body, the supply conveyor is operated again to supply sewage sludge, etc. to fill the main body.

而して本発明による装置に於ては上述のようにして連続
的に汚泥等の発酵を本体内各段で行うが、山形をし、且
千鳥状に配した規制板にて上段より下段側に向って移動
する時、汚泥等の自重による圧密化は規制板により分散
した荷重を受けるようになっているため本体の高さが高
くなっても圧密化は防止でき、好気性雰囲気が維持され
るため発酵が促進され、又山形をした規制板内に給排気
管を設けるため汚泥中を空気が移動する距離が短かくな
り通気抵抗が少なくブロワ−の容量も少くて済み、動力
の低減化がはかれると共に各段の送気、排気の量を加減
して発酵程度に応じた通気が行え、さらに本体上部を山
形で、その角度を安息角以上とし、且底部を上部と逆と
なるようにしているため本体全体の汚泥等の移動が平均
して行なわれる等数々の利点がある。
In the apparatus according to the present invention, fermentation of sludge, etc. is carried out continuously in each stage within the main body as described above, but the regulation plates, which are chevron-shaped and arranged in a staggered manner, are used to separate the fermentation from the upper stage to the lower stage. As the sludge and other objects become compacted due to their own weight, the regulation plates receive a distributed load, which prevents compaction even if the height of the main body increases, and maintains an aerobic atmosphere. This promotes fermentation, and since the supply and exhaust pipes are installed inside the chevron-shaped regulation plate, the distance that air travels through the sludge is shortened, resulting in less ventilation resistance and the need for a smaller blower capacity, reducing power consumption. As well as adjusting the amount of air supplied and exhausted from each stage, ventilation can be performed according to the degree of fermentation.Furthermore, the upper part of the main body is shaped like a chevron, the angle of which is equal to or greater than the angle of repose, and the bottom part is opposite to the upper part. Because of this, sludge, etc. can be moved evenly throughout the main body, and has many advantages.

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

第1図は縦断正面図、第2図は同側面図、第3図は真如
たる実施例図である。 1・・・・・・本体、2・・・・・・上部、3・・・・
・・下部、4・・・・・・排出口、5・・・・・・供給
コンベア、6・・・・・・規制板、・7・・・・・・給
気管、8・・・・・・排気管、9・・・・・・排出用コ
ンベア。
FIG. 1 is a longitudinal sectional front view, FIG. 2 is a side view of the same, and FIG. 3 is a diagram of an actual embodiment. 1...Body, 2...Top, 3...
... Lower part, 4 ... Discharge port, 5 ... Supply conveyor, 6 ... Regulation plate, 7 ... Air supply pipe, 8 ... ...Exhaust pipe, 9...Discharge conveyor.

Claims (1)

【特許請求の範囲】[Claims] 1 上部より被発酵物を投入し、下部より発酵後の被発
酵物を取り出すようになした発酵処理装置の本体内に複
数段の山形をした規制板を横方向及び縦方向にも所要の
間隔をおいて配列すると共にこの上下段の規制板を千鳥
状とし、且規制板の山形内に給気管あるいは排気管を配
設し、本体内を好気性雰囲気となるようにし、さらに上
記本体上部を山形でその角度を安息角以上とし、底部を
その逆にして本体内全体に亘って均一に汚泥等の流下が
行えるようになしたことを特徴とする下水汚泥等の発酵
処理装置。
1. In the main body of the fermentation processing equipment, the fermented material is introduced from the upper part and the fermented material is taken out from the lower part, and a plurality of chevron-shaped regulation plates are installed at the required intervals in both the horizontal and vertical directions. At the same time, the upper and lower regulating plates are arranged in a staggered manner, and an air supply pipe or an exhaust pipe is arranged within the chevron shape of the regulating plate to create an aerobic atmosphere inside the main body. A fermentation treatment device for sewage sludge, etc., characterized in that the angle of the chevron is greater than the angle of repose, and the bottom is reversed so that sludge, etc. can flow down uniformly throughout the main body.
JP54107418A 1979-08-23 1979-08-23 Fermentation treatment equipment for sewage sludge, etc. Expired JPS5852720B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP54107418A JPS5852720B2 (en) 1979-08-23 1979-08-23 Fermentation treatment equipment for sewage sludge, etc.

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP54107418A JPS5852720B2 (en) 1979-08-23 1979-08-23 Fermentation treatment equipment for sewage sludge, etc.

Publications (2)

Publication Number Publication Date
JPS5631499A JPS5631499A (en) 1981-03-30
JPS5852720B2 true JPS5852720B2 (en) 1983-11-24

Family

ID=14458638

Family Applications (1)

Application Number Title Priority Date Filing Date
JP54107418A Expired JPS5852720B2 (en) 1979-08-23 1979-08-23 Fermentation treatment equipment for sewage sludge, etc.

Country Status (1)

Country Link
JP (1) JPS5852720B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5843297A (en) * 1981-09-07 1983-03-12 Asahi Eng Kk Method and device for preventing dew condensation in vertical fermenting tank
JPS5888192A (en) * 1981-11-18 1983-05-26 三菱化工機株式会社 Composting device

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5423184A (en) * 1977-07-18 1979-02-21 Mitsubishi Electric Corp Fermentor of organic waste

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5423184A (en) * 1977-07-18 1979-02-21 Mitsubishi Electric Corp Fermentor of organic waste

Also Published As

Publication number Publication date
JPS5631499A (en) 1981-03-30

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