JPH11128995A - Device and process for bacteria mixing purification - Google Patents
Device and process for bacteria mixing purificationInfo
- Publication number
- JPH11128995A JPH11128995A JP31890097A JP31890097A JPH11128995A JP H11128995 A JPH11128995 A JP H11128995A JP 31890097 A JP31890097 A JP 31890097A JP 31890097 A JP31890097 A JP 31890097A JP H11128995 A JPH11128995 A JP H11128995A
- Authority
- JP
- Japan
- Prior art keywords
- mixing drum
- mixing
- sludge
- bacteria
- drum
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/40—Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse
Landscapes
- Processing Of Solid Wastes (AREA)
- Treatment Of Sludge (AREA)
- Mixers With Rotating Receptacles And Mixers With Vibration Mechanisms (AREA)
- Fertilizers (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、汚泥(本明細書中
において、し尿・生ゴミ・工場から排出される肉片等の
一般廃棄物及び汚泥・畜糞等の産業廃棄物を総称して
「汚泥」と呼ぶ)を菌の作用により発酵させて浄化処理
するための汚泥処理システムにおける菌混合浄化装置及
び菌混合浄化方法に関する。The present invention relates generally to sludge (in this specification, general waste such as human waste such as human waste, garbage and meat pieces discharged from factories, and industrial waste such as sludge and animal waste). The present invention relates to a bacteria-mixed purification apparatus and a bacteria-mixed purification method in a sludge treatment system for performing fermentation and purification treatment by the action of bacteria.
【0002】[0002]
【従来の技術】従来より汚泥を処理することが行われて
いる。この処理を大別すると、汚泥を微生物の分解力を
用いて浄化する「浄化処理」と、海洋に投棄する「海洋
投棄」とがある。2. Description of the Related Art Sludge has been conventionally treated. These treatments are roughly classified into "purification treatment" in which sludge is purified using the decomposing power of microorganisms, and "marine dumping" in which the sludge is dumped in the ocean.
【0003】このうち浄化処理としては、自然中の微生
物を利用した浄化処理と、意図的に加えた微生物を利用
した浄化処理とが提案されている。自然中の微生物を利
用する処理の例としては、汚泥を地中に埋めて微生物に
よる自然発酵・分解にて浄化するものが挙げられる。As the purification treatment, a purification treatment using microorganisms in nature and a purification treatment using microorganisms added intentionally have been proposed. As an example of a treatment using microorganisms in nature, there is a treatment in which sludge is buried in the ground and purified by natural fermentation and decomposition by microorganisms.
【0004】また意図的に加えた微生物を利用する処理
としては、好熱菌を利用した方法が提案されている。好
熱菌は通常の常温性微生物が増殖する温度範囲よりも高
い温度で増殖するものであり、単に有機物を分解するだ
けでなく、汚泥中の病原菌や有害な寄生虫卵を高温に曝
すことによって不活化することができるものである。具
体的な処理の過程としては、汚泥中に生息する様々な微
生物のうち比較的低温で増殖するバクテリア、真菌及び
放線菌等の細菌によって発酵が開始され、これらは堆肥
化過程進行に伴い急激に増殖し、これと同時に有機物の
分解熱によって温度が30〜60℃まで上昇する。この
とき温度に弱い酵母、カビ及び硝酸菌等は死滅する。温
度が上昇すると意図的に加えた好熱菌が増殖しはじめ、
さらに発酵熱が高まり、病原細菌、病虫卵、有害昆虫
卵、ウイルス、雑草種子等の大部分が不活化され、人畜
に無害なものになる。ここでの好熱菌として、通常の好
熱菌のみならず、バイオコロニー、バイオヒート(共に
バイオスペシャル社製)といった特に高温性な好熱菌を
も使用することにより、120℃前後の高温まで上昇さ
せて発酵させることが可能となる。このように好熱菌を
使用することでより高温での発酵処理が可能となり、し
たがって自然発酵に比べ処理時間を著しく短縮すること
ができ、また汚泥の浄化・安定化をより一層高めること
ができるといったメリットがある。As a treatment using a microorganism intentionally added, a method utilizing a thermophilic bacterium has been proposed. Thermophiles grow at temperatures higher than the temperature range at which normal room temperature microorganisms grow, and they not only degrade organic matter, but also expose pathogens and harmful parasite eggs in sludge to high temperatures. It can be inactivated. As a specific treatment process, fermentation is started by bacteria such as bacteria, fungi and actinomycetes that grow at relatively low temperature among various microorganisms inhabiting the sludge, and these are rapidly increased with the progress of the composting process. Proliferate, and at the same time, the temperature rises to 30 to 60 ° C. due to the heat of decomposition of organic matter. At this time, yeasts, molds, nitric acid bacteria, etc., which are sensitive to temperature, die. When the temperature rises, the thermophile added intentionally begins to grow,
Furthermore, the heat of fermentation increases, and most of pathogenic bacteria, diseased eggs, harmful insect eggs, viruses, weed seeds, and the like are inactivated and become harmless to humans and animals. By using not only normal thermophiles but also thermophiles with particularly high thermophilicity such as biocolonies and bioheats (both manufactured by Biospecial Co., Ltd.) It is possible to raise and ferment. By using thermophiles in this way, fermentation at higher temperatures becomes possible, and therefore the treatment time can be significantly reduced as compared to natural fermentation, and the purification and stabilization of sludge can be further enhanced. There is such a merit.
【0005】また、上記細菌として光栄養細菌を利用し
た方法もある。具体的には、細菌として光栄養細菌を担
体に固定させたものを対象物に添加したり(特開平5−
111694号)、当該細菌を担体に固定させたものを
パイプ状の処理管装置の内部に混入させて、対象物を処
理する装置(特開平8−224592号)等が挙げられ
る。ここで「光栄養細菌」とは、一般に光合成細菌(Ph
otosynthetic bacteria )と呼ばれている細菌のことを
いい、「Bergey's Manual of Determinative Bacteriol
ogy 8th edition (1974)」で確立された分類に従い、
光栄養細菌(Phototrophic bacteria )として開示され
るものを意味する。具体的には、特に限定はなく、ロド
スピリラム属、ロドシュードモナス属、及びロドミクロ
ビウム属を含むロドスピリ・ラーシエ科;クロマチウム
属等を含むクロマティ・アーシエ科;クロロビウム属等
を含むクロロビ・アーシエ科のうちを単独で又は2種以
上混合して用いることができる。There is also a method using a phototrophic bacterium as the above bacterium. Specifically, as a bacterium, a phototrophic bacterium which is immobilized on a carrier is added to a target object (Japanese Patent Laid-Open Publication No.
No. 111694), and a device for processing an object by mixing the bacteria immobilized on a carrier into a pipe-shaped processing tube device (Japanese Patent Application Laid-Open No. Hei 8-224592). Here, "phototrophic bacteria" generally refer to photosynthetic bacteria (Ph
Bacteria called otosynthetic bacteria) are described in Bergey's Manual of Determinative Bacteriol.
ogy 8th edition (1974) "
Means those disclosed as Phototrophic bacteria. Specific examples thereof include, but are not particularly limited to, Rhodospirillaceae including Rhodospirillum, Rhodopseudomonas, and Rhodomicrobium; Chromatiaceae including Chromatium; Chlorobiaceae including Chlorbium alone; Or a mixture of two or more.
【0006】なお上記光栄養細菌のみでは処理槽内で捕
食菌により捕食され、処理効率を所定のものに維持する
ためには、処理中に光栄養細菌の補充が必要となり不便
であるので、好ましい態様として、上記光栄養細菌をそ
の内部に固定するための「担体」を、該光栄養細菌に対
し、所定割合で添加して用いることができる。このよう
な「担体」としては、光栄養細菌の固定率が高いという
点より、多孔質粒子が好ましく、より具体的には、パー
ライト、バーミキュライト、珪藻土、活性炭、多孔質セ
ラミックス等が好ましく、上記多孔質粒子の他、内部に
固定化光栄養細菌を含む担体を充填したポリビニル製の
チューブや、アルギン酸ナトリウム及び/又はアルギン
酸カルシウム等の含水ゲル状担体をも好ましい担体とし
て用いることが可能である。The phototrophic bacteria alone are eaten by predators in the treatment tank, and in order to maintain the treatment efficiency at a predetermined level, replenishment of the phototrophic bacteria is required during the treatment, which is inconvenient. As an embodiment, a "carrier" for immobilizing the phototrophic bacterium therein can be used by adding it at a predetermined ratio to the phototrophic bacterium. As such a "carrier", porous particles are preferable in terms of a high fixation rate of phototrophic bacteria, and more specifically, perlite, vermiculite, diatomaceous earth, activated carbon, and porous ceramics are preferable. In addition to the porous particles, a polyvinyl tube filled with a carrier containing immobilized phototrophic bacteria or a hydrogel carrier such as sodium alginate and / or calcium alginate can also be used as a preferred carrier.
【0007】[0007]
【発明が解決しようとする課題】しかし、上記従来の浄
化処理のうち、自然中の微生物を利用する処理にあって
は浄化されるまで長期間を要し、また発酵臭も強い。さ
らに現代の都市型住宅では土に乏しいという実情もあ
る。生ゴミ以外のし尿や畜糞の浄化処理効率については
未だ十分でない。さらに、意図的に加えた微生物を利用
する処理は上記問題がなく新しい浄化処理方法として有
望視されているが、上述したようにその基本的な原理は
確立されているものの、該処理を効率良く簡易かつ迅速
に行うためのシステム及び装置は未だ提案されておら
ず、実用化には至っていない。特に、企業や自治体レベ
ルの大規模な処理だけでなく、比較的小規模な処理装置
の実用化も望まれている。また海洋投棄による処理にお
いては、該海洋投棄が近々全面禁止になることが決定し
ており、該処理に変わる処理方法の確立が強く要望され
ている。However, among the above-mentioned conventional purification treatments, the treatment using microorganisms in nature requires a long time to be purified and has a strong fermentation odor. There is also the fact that modern urban housing is scarce on the soil. The purification efficiency of human waste and feces other than garbage is not yet sufficient. Furthermore, treatment using intentionally added microorganisms is regarded as promising as a new purification treatment method without the above-mentioned problem. However, although the basic principle has been established as described above, the treatment can be performed efficiently. A system and an apparatus for performing the operation simply and quickly have not been proposed yet, and have not been put to practical use. In particular, not only large-scale processing at the company or local government level, but also practical use of a relatively small-scale processing apparatus is desired. In addition, in the processing by ocean dumping, it has been determined that the ocean dumping will be completely prohibited soon, and there is a strong demand for establishment of a processing method to replace the processing.
【0008】本発明は、従来のこのような問題点に鑑み
なされたもので、し尿、畜糞、生ゴミ等の廃棄物からな
る汚泥を浄化すると共に、堆肥化してその有効利用を図
り、また一連の処理を効率良く簡易かつ迅速に行うこと
ができる菌混合浄化装置及び菌混合浄化方法を提供する
ことを目的とする。The present invention has been made in view of the above-mentioned conventional problems, and purifies sludge composed of waste such as night soil, animal dung, garbage, and the like, and aims to effectively use the sludge by composting. It is an object of the present invention to provide a germ mixture purifying apparatus and a germ mixture purifying method which can efficiently, simply and quickly carry out the treatment of germs.
【0009】[0009]
【課題を解決するための手段】上記目的を達成するため
請求項1記載の本発明は、汚泥を投入して粉砕し菌を混
合するための筒状の混合ドラムを回転支持装置にて回転
自在に支持してなり、この混合ドラムの両側面には側面
板を面接触状に取付けると共に、この側面板は支持機構
により混合ドラムの側面に非回転状に支持されてなり、
上記混合ドラムの筒の外周壁部側に入出開口を設けて汚
泥を取入れ又は取出し自在とし、上記混合ドラムの内周
壁部には掬上げフィンを設けてあって混合ドラムの回転
によって汚泥を上方に掬上げ自在としてなり、上記混合
ドラムは上記投入された汚泥を均一に粉砕して上記菌と
均一に混合させることにより均一な発酵を促進させるた
めの粉砕混合機構を備えるもので、この粉砕混合機構は
側面板を介在して回転自在に軸支された回転駆動軸と、
この回転駆動軸に取付けられた回転羽と、回転駆動軸を
回転させる駆動装置とから構成され、上記掬上げフィン
によって上部に掬上げられた汚泥を上記回転羽にて細か
く粉砕して菌を混合自在としてなることを特徴として構
成される。According to the first aspect of the present invention, there is provided a cylindrical mixing drum for feeding sludge, crushing and mixing bacteria with a rotary support device. A side plate is attached to both sides of the mixing drum in a surface contact manner, and the side plate is non-rotatably supported on a side surface of the mixing drum by a support mechanism.
An inlet / outlet opening is provided on the outer peripheral wall side of the mixing drum cylinder so that sludge can be taken in or taken out, and a scooping fin is provided on the inner peripheral wall of the mixing drum, and the sludge is moved upward by the rotation of the mixing drum. The mixing drum is equipped with a pulverizing and mixing mechanism for promoting uniform fermentation by uniformly pulverizing the input sludge and uniformly mixing with the bacteria. Is a rotary drive shaft rotatably supported via a side plate,
It consists of a rotary wing attached to this rotary drive shaft and a drive device for rotating the rotary drive shaft, and the sludge scooped up by the scooping fins is finely pulverized by the rotary wings to mix bacteria. It is configured to be free.
【0010】また請求項2記載の本発明は、上記請求項
1記載の発明において、上記混合ドラムを上記入出開口
の開口部分が上方に移動する方向で回転させて汚泥を菌
混合処理し、上記混合ドラム内で菌混合処理し又は発酵
処理した内容物を上記混合時の回転に対して逆方向に上
記混合ドラムを回転させることにより上記入出開口から
外部へ適量にて取出自在とすることを特徴として構成さ
れる。According to a second aspect of the present invention, in the first aspect of the present invention, the mixing drum is rotated in a direction in which an opening portion of the inlet / outlet opening moves upward to mix the sludge with bacteria. By rotating the mixing drum in a direction opposite to the rotation at the time of mixing the bacteria-mixed or fermented content in the mixing drum, the content can be taken out from the inlet / outlet to the outside in an appropriate amount. The feature is constituted.
【0011】また請求項3記載の本発明は、上記請求項
1又は2記載の発明において、上記回転羽を取付けた回
転駆動軸は混合ドラムの回転中心の上部側方である回転
上り側位置であって上記掬上げられた汚泥が落下される
位置に偏心させて取付けてあることを特徴として構成さ
れる。According to a third aspect of the present invention, in the first or the second aspect of the present invention, the rotary drive shaft to which the rotary wing is attached is located at a rotation-up position on the upper side of the rotation center of the mixing drum. The sludge thus scooped is mounted eccentrically at the position where it is dropped.
【0012】また請求項4記載の本発明は、上記請求項
1乃至3記載の発明において、上記側面板に空気供給口
を設けて上記混合ドラム内に空気を混入自在とすると共
に、上記側面板に空気抜口を設けることにより上記菌混
合処理した汚泥を混合ドラム内にて発酵処理させる際に
発生する蒸気や臭気を上記空気抜口から外部に排出自在
とすることを特徴として構成される。According to a fourth aspect of the present invention, in the first to third aspects of the present invention, an air supply port is provided in the side plate so that air can be freely mixed into the mixing drum, and By providing an air vent, steam or odor generated when the sludge mixed with the bacteria is fermented in the mixing drum can be discharged to the outside through the air vent.
【0013】また請求項5記載の本発明は、上記請求項
1乃至3記載の発明において、上記側面板に空気供給口
及び空気抜口を設けると共に、該空気抜口から外部へ排
出された蒸気又は該蒸気を凝縮させた水を再度上記空気
供給口へ導くための配管を備え、該配管の途中に上記蒸
気を凝縮させるための凝縮機を備えてなることを特徴と
して構成される。According to a fifth aspect of the present invention, in the first to third aspects of the present invention, the side plate is provided with an air supply port and an air vent, and the steam discharged from the air vent to the outside is provided. Alternatively, a pipe for guiding water condensed with the steam to the air supply port again is provided, and a condenser for condensing the steam is provided in the middle of the pipe.
【0014】また請求項6記載の本発明は、上記請求項
4又は5記載の発明において、上記混合ドラム内に送風
機構を備え、該送風機構が多数の送風板と該送風板を軸
支する一対の支軸管とから構成され、該支軸管には上記
空気供給口が上記側面板を介在して連通状に結合され、
上記送風板の内部には支軸管に連通状に継合させた多数
の細管を形成させ、上記空気供給口、支軸管及び細管を
通じて混合ドラム内に送風自在としてなることを特徴と
して構成される。According to a sixth aspect of the present invention, in the fourth or fifth aspect of the present invention, a blower mechanism is provided in the mixing drum, and the blower mechanism supports a number of blowers and the blowers. A pair of support pipes, the air supply port is connected to the support pipe in a communication manner via the side plate,
A large number of small tubes connected to the spindle tube are formed in the inside of the blower plate, and the air can be freely blown into the mixing drum through the air supply port, the spindle tube, and the small tube. You.
【0015】また請求項7記載の本発明は、上記請求項
1乃至6記載の発明において、上記混合ドラムの周壁が
外周壁部と内周壁部との二重壁にて形成されており、該
二重壁の間に温湯を循環させるための昇温用配管を備え
てなることを特徴として構成される。According to a seventh aspect of the present invention, in the first to sixth aspects, the peripheral wall of the mixing drum is formed by a double wall of an outer peripheral wall and an inner peripheral wall. It is characterized by comprising a heating pipe for circulating hot water between the double walls.
【0016】また請求項8記載の本発明は、汚泥を投入
して粉砕し菌を混合するための筒状の混合ドラムを回転
支持装置にて回転自在に支持し、この混合ドラムの両側
面に側面板を面接触状に取付け、この側面板を支持機構
により混合ドラムの側面に非回転状に支持し、上記混合
ドラムの筒の外周壁部側に入出開口を設けると共に、そ
の内周壁部に掬上げフィンを設け、上記混合ドラムに粉
砕混合機構を備え、この粉砕混合機構が側面板を介在し
て回転自在に軸支された回転駆動軸と、この回転駆動軸
に取付けられた回転羽と、回転駆動軸を回転させる駆動
装置とから構成され、上記入出開口から混合ドラムに汚
泥を取入れ、上記混合ドラムを上記入出開口の開口部分
が上方に移動する方向で所定時間回転させて汚泥を菌と
混合して処理し、上記菌混合処理した菌混合汚泥を所定
時間静止状態を保持して発酵処理し、次いで、上記混合
時の回転に対して逆方向に上記混合ドラムを回転させる
ことにより上記発酵処理した発酵処理済内容物を上記入
出開口から外部へ適量にて取出すことを特徴として構成
される。According to the present invention, a cylindrical mixing drum for charging sludge, mixing, and mixing bacteria is rotatably supported by a rotary support device, and is provided on both side surfaces of the mixing drum. The side plate is attached in a face contact manner, the side plate is non-rotatably supported on the side surface of the mixing drum by a support mechanism, and an inlet / outlet opening is provided on the outer peripheral wall side of the cylinder of the mixing drum, and on the inner peripheral wall thereof. A scooping fin is provided, the mixing drum is provided with a pulverizing / mixing mechanism, and the pulverizing / mixing mechanism is rotatably supported rotatably with a side plate interposed therebetween, and a rotatable blade attached to the rotatable driving shaft. And a driving device for rotating a rotary drive shaft. Sludge is taken into the mixing drum from the inlet / outlet opening, and the mixing drum is rotated for a predetermined time in a direction in which the opening portion of the inlet / outlet opening moves upward, and the sludge is removed. Is mixed with bacteria and processed, The bacteria-mixed sludge subjected to the bacteria-mixing process is fermented while being kept stationary for a predetermined time, and then the fermentation-processed content obtained by performing the fermentation process by rotating the mixing drum in a direction opposite to the rotation during the mixing. The apparatus is characterized in that an object is taken out from the inlet / outlet to the outside in an appropriate amount.
【0017】また請求項9記載の本発明は、上記請求項
8記載の発明において、上記静止状態を所定時間保持し
て発酵処理をした後、上記混合ドラムの回転による菌混
合処理を再度行い、次いで静止状態を所定時間保持して
発酵処理を繰返すことを特徴として構成される。According to a ninth aspect of the present invention, in accordance with the eighth aspect of the present invention, the fermentation treatment is performed while the stationary state is maintained for a predetermined time, and then the bacteria mixing treatment by rotating the mixing drum is performed again. Next, the stationary state is maintained for a predetermined time, and the fermentation process is repeated.
【0018】また請求項10記載の本発明は、汚泥を投
入して粉砕し菌を混合するための筒状の混合ドラムを回
転支持装置にて回転自在に支持し、この混合ドラムの両
側面に側面板を面接触状に取付け、この側面板を支持機
構により混合ドラムの側面に非回転状に支持し、上記混
合ドラムの筒の外周壁部側に入出開口を設けると共に、
その内周壁部に掬上げフィンを設け、上記混合ドラムに
粉砕混合機構を備え、この粉砕混合機構が側面板を介在
して回転自在に軸支された回転駆動軸と、この回転駆動
軸に取付けられた回転羽と、回転駆動軸を回転させる駆
動装置とから構成され、上記入出開口から混合ドラムに
汚泥を取入れ、上記混合ドラムを上記入出開口の開口部
分が上方に移動する方向で所定時間回転させて汚泥を菌
と混合して処理し、かつ上記菌混合処理した菌混合汚泥
を上記混合ドラムを回転させながら発酵処理し、次い
で、上記混合時の回転に対して逆方向に上記混合ドラム
を回転させることにより上記発酵処理した発酵処理済内
容物を上記入出開口から外部へ適量にて取出すことを特
徴として構成される。According to a tenth aspect of the present invention, a cylindrical mixing drum for introducing sludge, crushing and mixing bacteria is rotatably supported by a rotary support device, and is provided on both side surfaces of the mixing drum. The side plate is attached in a surface contact manner, the side plate is non-rotatably supported on the side surface of the mixing drum by a support mechanism, and an inlet / outlet is provided on the outer peripheral wall side of the cylinder of the mixing drum,
A scooping fin is provided on the inner peripheral wall thereof, and the mixing drum is provided with a pulverizing / mixing mechanism. The pulverizing / mixing mechanism is rotatably supported via a side plate, and is attached to the rotatable driving shaft. And a driving device for rotating a rotary drive shaft. Sludge is taken into the mixing drum from the inlet / outlet opening, and the mixing drum is moved in a predetermined direction in which the opening of the inlet / outlet opening moves upward. The sludge is mixed with bacteria by rotating for a time to be treated, and the bacteria-mixed sludge subjected to the bacteria-mixing treatment is fermented while rotating the mixing drum, and then the mixing is performed in a direction opposite to the rotation during the mixing. By rotating the drum, the fermented contents obtained by the fermentation treatment are taken out from the inlet / outlet in an appropriate amount by an appropriate amount.
【0019】[0019]
【発明の実施の形態】以下、本発明の実施形態を図面に
沿って詳細に説明する。図1は本発明の第1実施例の外
周壁部方向から見た縦断面図、図2はその側面板方向か
ら見た縦断面図、図3はその側面板方向から見た側面図
をそれぞれ示している。また、図4は本発明の第2実施
例の側面板方向から見た縦断面図を示している。さら
に、図5は本発明の第3実施例の斜視図、図6はその側
面板方向から見た縦断面図をそれぞれ示している。Embodiments of the present invention will be described below in detail with reference to the drawings. FIG. 1 is a longitudinal sectional view of the first embodiment of the present invention viewed from the outer peripheral wall portion direction, FIG. 2 is a longitudinal sectional view of the first embodiment viewed from the side plate direction, and FIG. 3 is a side view of the first embodiment viewed from the side plate direction. Is shown. FIG. 4 is a longitudinal sectional view of the second embodiment of the present invention viewed from the side plate. FIG. 5 is a perspective view of a third embodiment of the present invention, and FIG. 6 is a longitudinal sectional view of the third embodiment viewed from the side plate.
【0020】まず、本発明の菌混合浄化装置として、図
1乃至3に示す第1実施例について説明する。すなわ
ち、本発明の第1実施例は、基本的に混合ドラム10を
基台30上に回転支持装置31を介して回転自在に支持
してなるもので、この混合ドラム10は直径約2m程度
の円筒状に形成されると共に、回転支持装置31によっ
て低速回転させるものである。上記混合ドラム10の両
側面には側面板12、12を面接触状に取付ける。この
側面板12、12は回転駆動軸22を介して支持アーム
21、21により支持されていると共に、支持機構とし
て上記支持アーム21、21に設けた押圧機構13、1
3により常時一定の圧力で混合ドラム10の側面に押圧
されて非回転状に支持されてなる。上記支持アーム2
1、21は混合ドラム10の両側面外側において門型状
に立設される。なお、上記支持機構は押圧機構13、1
3に限定されず、混合ドラム10の内部から側面板1
2、12を吸引する等の他の方法によって支持するよう
にしてもよい。First, a first embodiment of the present invention will be described with reference to FIGS. That is, in the first embodiment of the present invention, the mixing drum 10 is basically rotatably supported on the base 30 via the rotation support device 31, and the mixing drum 10 has a diameter of about 2 m. It is formed in a cylindrical shape and is rotated at a low speed by a rotation support device 31. Side plates 12, 12 are attached to both sides of the mixing drum 10 in a surface contact manner. The side plates 12, 12 are supported by support arms 21, 21 via a rotary drive shaft 22, and a pressing mechanism 13, 1 provided on the support arms 21, 21 as a support mechanism.
3, the pressure is constantly pressed against the side surface of the mixing drum 10 at a constant pressure and is supported non-rotatably. The above support arm 2
The reference numerals 1 and 21 are provided on the outside of both sides of the mixing drum 10 in a portal shape. The supporting mechanism is a pressing mechanism 13, 1
3, the side plate 1 from the inside of the mixing drum 10
The support may be performed by another method such as suctioning the second and the second.
【0021】上記側面板12と混合ドラム10の側面間
には、パッキング材14が介在されている。また、上記
混合ドラム10の筒の周壁は外周壁部11aと内周壁部
11bとの二重壁にて形成されており、内部の断熱性、
保温性を良好にしている。上記二重壁の間に温湯を循環
させるための昇温用の配管を通したり、また断熱材を詰
める等により断熱性、保温性をいっそう良好にさせても
よい。なお、上記混合ドラム10の筒の周壁は必ずしも
二重壁にする必要はなく、一重壁であってもよく、その
場合には混合ドラム内部の断熱性、保温性を保持するた
めに該壁の外側に断熱フィルム等の断熱材を巻き付ける
ようにしてもよい。A packing member 14 is interposed between the side plate 12 and the side surface of the mixing drum 10. The peripheral wall of the cylinder of the mixing drum 10 is formed by a double wall of an outer peripheral wall portion 11a and an inner peripheral wall portion 11b.
Good heat retention. The heat insulating property and the heat retaining property may be further improved by passing a heating pipe for circulating hot water between the double walls or by filling a heat insulating material. Note that the peripheral wall of the cylinder of the mixing drum 10 does not necessarily have to be a double wall, and may be a single wall. In this case, in order to maintain heat insulation and heat retention inside the mixing drum, the peripheral wall of the cylinder is A heat insulating material such as a heat insulating film may be wound around the outside.
【0022】上記外周壁部11a側には汚泥を取入れ又
は取出す入出開口18を形成してなる。該入出開口18
はその下面を上記外周壁部11a下面と一体的に連続し
てなり、後述する駆動ローラ32、32の間に位置して
混合ドラム10の長手方向に略幅広形状に形成されてな
る。この入出開口18には混合ドラム10内の蒸気や臭
気を外部に排出しないようその開口部分に入出弁19a
が設けられている。An inlet / outlet 18 for taking in or taking out sludge is formed on the outer peripheral wall 11a side. The access opening 18
Has a lower surface integrally continuous with the lower surface of the outer peripheral wall portion 11a, and is formed between drive rollers 32, 32, which will be described later, and has a substantially wide shape in the longitudinal direction of the mixing drum 10. An inlet / outlet valve 19a is provided at the inlet / outlet opening 18 so that the vapor and odor in the mixing drum 10 are not discharged to the outside.
Is provided.
【0023】上記混合ドラム10の内周壁部11bに
は、その長手方向に長尺の薄板片からなる多数の掬上げ
フィン15、15を設けており、回転上り側位置にて汚
泥を掬上げるように上記内周壁部11bに対してそれぞ
れ傾斜状に形成されている。そして、上記混合ドラム1
0の回転によって汚泥が上方に掬上げられる。なお、こ
の混合ドラム10は、円筒形状に形成したが、六角形や
八角形等の多角形の筒状に形成することもできる。The inner peripheral wall 11b of the mixing drum 10 is provided with a large number of scooping fins 15 and 15 made of long thin plates in the longitudinal direction thereof, so that the sludge is scooped up at the rotation-up side position. Are formed to be inclined with respect to the inner peripheral wall portion 11b. And the mixing drum 1
Sludge is scooped up by the rotation of zero. Although the mixing drum 10 is formed in a cylindrical shape, it may be formed in a polygonal cylindrical shape such as a hexagon or an octagon.
【0024】上記両側面板12、12に空気供給口1
6、16を設けて上記混合ドラム10内に両側面から空
気を混入自在とすると共に、一方の側面板12に空気抜
口17を設けて上記混合ドラム10内から空気を排出自
在としてある。上記空気供給口16、16から混合ドラ
ム10内に空気を混入して汚泥の発酵を促進させ、該発
酵処理により発生して充満する蒸気や臭気を上記空気抜
口17から外部に排出させるものである。また、上記混
合ドラム10内を外気圧に対してわずかに負圧にするこ
とにより、空気を自然に混入させまた自然に蒸気や臭気
を排出させることができる。上記混合ドラム10内に温
度センサーを設けることにより汚泥の発酵温度を常時測
定し、該発酵温度にあわせて気圧を調整して空気を出し
入れし、発酵温度を調節することができる。なお、上記
空気供給口16、16には逆止弁19b、19bを設け
て上記混合ドラム10内の汚泥及び空気が上記空気供給
口16、16を通じて逆流しないようにしている。ま
た、上記空気抜口17から外部へ排出された蒸気又は該
蒸気を凝縮させた水を再度上記空気供給口16へ導くた
めの配管50と、該配管50の途中に該蒸気を凝縮させ
るための凝縮機51を備えるような構成し、発酵時に発
生した蒸気を再度混合ドラム10内に循環させるように
すれば、該混合ドラム10内に発生する異臭を消臭する
ことができるため好ましい態様となる。The air supply port 1 is connected to the side plates 12, 12.
6 and 16 are provided so that air can be freely mixed into the mixing drum 10 from both side surfaces, and an air vent 17 is provided in one side plate 12 so that air can be freely discharged from the mixing drum 10. Air is mixed into the mixing drum 10 from the air supply ports 16 and 16 to promote fermentation of sludge, and steam and odor generated and filled by the fermentation process are discharged from the air vent 17 to the outside. is there. Further, by making the inside of the mixing drum 10 slightly negative pressure with respect to the outside air pressure, air can be naturally mixed and steam and odor can be naturally discharged. By providing a temperature sensor in the mixing drum 10, the fermentation temperature of the sludge is constantly measured, and the air pressure is adjusted according to the fermentation temperature so that air can be taken in and out to adjust the fermentation temperature. The air supply ports 16, 16 are provided with check valves 19b, 19b to prevent sludge and air in the mixing drum 10 from flowing back through the air supply ports 16, 16. A pipe 50 for guiding the steam discharged to the outside from the air vent 17 or the water condensed with the steam to the air supply port 16 again, and a pipe 50 for condensing the steam in the middle of the pipe 50. It is a preferable embodiment to provide the condenser 51 and to circulate the steam generated during the fermentation again in the mixing drum 10 since the odor generated in the mixing drum 10 can be eliminated. .
【0025】次に、上記混合ドラム10の内部には投入
された汚泥を均一に粉砕して上記菌と均一に混合させる
ことにより均一な発酵を促進させるための粉砕混合機構
20を備えており、この粉砕混合機構20は、上記回転
駆動軸22と、この回転駆動軸22に取付けられた回転
羽23と、上記回転駆動軸22の回転を円滑にするため
のフライホイール25、25と、上記回転駆動軸22を
高速で回転させる駆動装置24とから構成される。上記
回転駆動軸22は上記側面板12、12と上記フライホ
イール25、25とを介在して上記支持アーム21、2
1に回転自在に軸支される。また上記回転駆動軸22は
混合ドラム10の回転中心の上部側方である回転上り側
位置であって上記掬上げられた汚泥が落下される位置に
偏心させて取付けてあり、回転上り側にある掬上げフィ
ン15に近接している。Next, the mixing drum 10 is provided with a pulverizing and mixing mechanism 20 for uniformly pulverizing the introduced sludge and uniformly mixing the sludge with the bacteria to promote uniform fermentation. The pulverizing / mixing mechanism 20 includes the rotary drive shaft 22, a rotary blade 23 attached to the rotary drive shaft 22, flywheels 25 for smooth rotation of the rotary drive shaft 22, and the rotary drive shaft 22. And a driving device 24 for rotating the driving shaft 22 at high speed. The rotary drive shaft 22 has the side arms 12, 12 and the flywheels 25, 25 interposed therebetween, and the support arms 21, 2
1 to be rotatably supported. The rotary drive shaft 22 is eccentrically attached to a position where the scooped sludge is dropped, which is an upper position of the rotation center of the rotation center of the mixing drum 10 and a position where the scooped sludge falls. It is close to the scooping fins 15.
【0026】上記回転羽23は、多数の波状羽からな
り、これらの波状羽を上記回転駆動軸22に対して略垂
直に軸着して形成させる。また、一つの層につき3枚の
波状羽を放射状に軸着してスクリューを構成し、このス
クリューを軸方向に略重層状に多数重ねて形成させる。
さらに、上記回転羽23を多数の波状羽を螺旋状に並べ
て上記回転駆動軸22に軸着させて形成させてもよい。
上記波状羽の周囲は先端鋭利に形成され、上記回転駆動
軸22を上記駆動装置24により高速に回転させると上
記回転羽23が高速に回転し汚泥を切裂状に粉砕する。The rotating wings 23 are composed of a large number of wavy wings, and these wavy wings are axially mounted substantially perpendicularly to the rotation drive shaft 22. In addition, a screw is formed by radially attaching three wavy wings to one layer to form a screw, and a large number of such screws are formed in a layered manner in the axial direction.
Further, the rotating wings 23 may be formed by arranging a number of wavy wings in a spiral and attaching the rotating wings 23 to the rotation driving shaft 22.
The periphery of the wavy wing is formed with a sharp tip, and when the rotary drive shaft 22 is rotated at a high speed by the driving device 24, the rotary wing 23 rotates at a high speed to pulverize the sludge into a cut shape.
【0027】上記側面板12、12の外側にはそれぞれ
フライホイール25、25が取付けられる。該フライホ
イール25、25は上記粉砕混合機構20を構成する回
転駆動軸22の回転を円滑にして上記回転羽23により
投入された汚泥を切削する際の切削負荷を軽減するため
に設けられるものであり、本実施形態ではその中心を上
記回転駆動軸22により軸支され形成されているが、上
記回転羽23に十分な慣性力があれば必ずしも設けるこ
とを要しない。また、一方のフライホイール25の外側
には上記回転駆動軸22を回転させて上記粉砕混合機構
20を駆動させるための回転駆動装置24が取付けられ
る。Flywheels 25, 25 are mounted outside the side plates 12, 12, respectively. The flywheels 25, 25 are provided for smoothing the rotation of the rotary drive shaft 22 constituting the crushing and mixing mechanism 20 and reducing the cutting load when cutting the sludge supplied by the rotary wings 23. In the present embodiment, the center is pivotally supported by the rotary drive shaft 22. However, if the rotary wing 23 has a sufficient inertial force, it is not always necessary to provide the rotary wing 23. Further, a rotary drive device 24 for rotating the rotary drive shaft 22 to drive the crushing and mixing mechanism 20 is mounted outside the one flywheel 25.
【0028】上記の構成から、混合ドラム10の回転と
共に掬上げフィン15によって掬上げられた汚泥は、高
速で回転する回転羽23の上に落されて細かく粉砕され
るものである。さらに下方に落下した汚泥は、引続き掬
上げフィン15によって再度連続的に上方へ掬上げられ
回転羽23上に落されてより一層細かく粉砕される。With the above structure, the sludge scooped by the scooping fins 15 with the rotation of the mixing drum 10 is dropped on the rotating blades 23 rotating at a high speed and finely pulverized. The sludge that has fallen further downward is continuously scooped up again by the scooping fins 15 again, dropped on the rotating blades 23, and further pulverized.
【0029】次に、混合ドラム10の回転支持装置31
は以下のように構成される。すなわち基台30上におい
て駆動ローラ32、32によって混合ドラム10を回転
自在に支持すると共に、この駆動ローラ32はローラ駆
動装置33によってローラ回転軸34を介して回転駆動
するものである。上記駆動ローラ32は、混合ドラム1
0の外周壁部11aの下面部分に接触して摩擦駆動もし
くはギヤ駆動等によって混合ドラム10を低速で回転さ
せる。この回転速度は1分間に1〜10回転する程度の
速度とする。Next, the rotation supporting device 31 of the mixing drum 10
Is configured as follows. That is, the mixing drum 10 is rotatably supported on the base 30 by the driving rollers 32, 32, and the driving roller 32 is rotationally driven by the roller driving device 33 via the roller rotating shaft 34. The driving roller 32 is used for the mixing drum 1.
The mixing drum 10 is rotated at a low speed by friction drive or gear drive in contact with the lower surface portion of the outer peripheral wall portion 11a. This rotation speed is set to a speed of about 1 to 10 rotations per minute.
【0030】次に本実施例の作用について説明する。ま
ず、回転する混合ドラム10に対し、その外周壁部11
aに設けた入出開口18から処理対象の汚泥を投入す
る。この時、同時に前記した好熱菌を適量投入する。投
入量としては投入する汚泥の重量に対して例えば約50
0分の1の重量の好熱菌を投入する。なお、投入する菌
として本実施例においては好熱菌を用いるが、該好熱菌
に限定されるものではなく、上記光栄養細菌を投入する
こともでき、もしくは好熱菌及び光栄養細菌の双方を投
入してもよい。光栄養細菌を使用する場合は別途、光照
射装置を備えることが必要である。また、好熱菌を投入
する代わりに後述する発酵済内容物(菌混合汚泥を発酵
処理したものを発酵済内容物と呼ぶ。以下同様)の一部
を戻し材(発酵済内容物のうち、再度混合ドラム10内
に混入されるものを戻し材と呼ぶ。以下同様)として新
汚泥と略等分量を投入することもできる。すなわち、上
記発酵済内容物には好熱菌が十分に培養されていること
から、これを用いると新規な好熱菌の投入は不要とな
る。またこの戻し材を投入することにより新たに投入し
た汚泥中の水分を調整するための水分調整材としての役
割も果たすことができる。新たに投入した汚泥が発酵に
必要な水分を保持していない場合に特に有効である。さ
らに、汚泥の臭気を消すために上記空気供給口16から
消臭剤を注入してもよい。消臭剤としては発酵処理にお
いて発生した水蒸気を予め回収しておき、これを注入す
るのが効果的である。Next, the operation of this embodiment will be described. First, the outer peripheral wall 11 of the rotating mixing drum 10 is
The sludge to be treated is introduced from the inlet / outlet opening 18 provided at a. At this time, an appropriate amount of the thermophilic bacterium described above is added at the same time. The input amount is, for example, about 50 to the weight of the sludge to be input.
The thermophilic bacterium of 1/0 weight is injected. In this example, a thermophilic bacterium is used as a bacterium to be added. However, the bacterium is not limited to the thermophilic bacterium. You may throw in both. When using phototrophic bacteria, it is necessary to separately provide a light irradiation device. In addition, instead of adding thermophilic bacteria, a part of fermented contents described below (the fermented content of the fungus-mixed sludge is referred to as fermented contents. The same applies hereinafter) is used as a return material (of the fermented contents, What is mixed again into the mixing drum 10 is called a return material. The same applies to the following. That is, since thermophilic bacteria are sufficiently cultured in the fermented contents, the use of the thermophilic bacteria eliminates the necessity of introducing new thermophilic bacteria. Also, by introducing this returning material, it can also play a role as a moisture adjusting material for adjusting the moisture in the newly introduced sludge. This is particularly effective when newly introduced sludge does not hold the water required for fermentation. Further, a deodorant may be injected from the air supply port 16 in order to eliminate the odor of the sludge. As a deodorant, it is effective to collect in advance the steam generated in the fermentation treatment and inject it.
【0031】上記混合ドラム10の内周壁部11bに
は、薄板片からなる多数の掬上げフィン15、15を設
けてあり、混合ドラム10の回転によって、汚泥が上方
に掬上げられる。この際、上記入出開口18に向かって
汚泥を逆流させないように、入出開口18の開口部分側
の端部が上方に移動する方向で上記混合ドラム10を低
速で回転させる。そして、掬上げられた汚泥は高速で回
転する回転羽23の上に落下して細かく粉砕される。そ
してさらに下方に落下した汚泥は、引続き掬上げフィン
15によって再度連続的に上方へ掬上げられ再び回転羽
23上に落下してより一層細かく粉砕される。On the inner peripheral wall 11b of the mixing drum 10, a large number of scooping fins 15, 15 made of thin pieces are provided, and by the rotation of the mixing drum 10, the sludge is scooped upward. At this time, the mixing drum 10 is rotated at a low speed in a direction in which the end on the opening portion side of the inlet / outlet 18 moves upward so as to prevent the sludge from flowing back toward the inlet / outlet 18. Then, the scooped sludge falls on the rotating blades 23 rotating at a high speed and is finely crushed. Then, the sludge that has fallen further downward is continuously scooped up again by the scooping fins 15 again, falls again on the rotating blades 23, and is further finely pulverized.
【0032】このように細かく粉砕された汚泥には上記
した細菌が混合される。そして上記回転を停止し又は回
転させながら、菌混合汚泥(混合ドラム10内において
菌が混合された汚泥を菌混合汚泥と呼ぶ。以下同様)を
混合ドラム10内に置いたまま保持して発酵させる。The above-mentioned bacteria are mixed with the sludge finely ground in such a manner. While the rotation is stopped or rotated, the bacteria-mixed sludge (the sludge mixed with the bacteria in the mixing drum 10 is referred to as a bacteria-mixed sludge; the same applies hereinafter) is held and fermented while being kept in the mixing drum 10. .
【0033】上記混合ドラム10内を負圧にして上記空
気供給口16から空気を混入すると、上記混合ドラム1
0内の好気性が高まることにより発酵が促進される。な
お、上記混合ドラム10を回転させているとき既に発酵
は始まっているため、上記空気供給口16を通じて空気
を混入させて発酵を促進させるのは上記静止状態での養
生期間には限られず、常時混合ドラム10内を負圧にす
ることが望ましい。発酵処理において発生した蒸気や臭
気は上記の通り上記空気抜口17を利用して外部に排出
させ、必要に応じて該排出された蒸気等を再度上記空気
供給口16から投入させるようにする。When the inside of the mixing drum 10 is set to a negative pressure and air is mixed in from the air supply port 16, the mixing drum 1
Fermentation is promoted by increasing the aerobicity within zero. Since the fermentation has already started when the mixing drum 10 is being rotated, it is not limited to the curing period in the stationary state that the air is mixed through the air supply port 16 to promote the fermentation. It is desirable to make the inside of the mixing drum 10 a negative pressure. The steam and odor generated in the fermentation treatment are discharged to the outside using the air vent 17 as described above, and the discharged steam and the like are supplied again from the air supply port 16 as necessary.
【0034】さらに汚泥に一様に細菌が混合されるよう
にするため、再度混合ドラム10を一定方向に回転させ
て混合処理を繰り返す。また、より発酵を促進させるた
めさらに菌を投入してもよい。この菌の投入量や混入す
る空気量を調整することにより発酵の促進度、発酵温度
等を調節する。発酵温度が高まるほど浄化は促進され
る。上記一連の処理を数度繰り返しながら約2日間の養
生期間を経て上記菌混合汚泥が浄化される。In order to uniformly mix the bacteria with the sludge, the mixing drum 10 is again rotated in a certain direction, and the mixing process is repeated. Further, bacteria may be further added to further promote fermentation. The degree of acceleration of fermentation, the fermentation temperature, and the like are adjusted by adjusting the amount of the bacteria and the amount of air to be mixed. Purification is promoted as the fermentation temperature increases. The bacteria-mixed sludge is purified through a curing period of about two days while repeating the above series of processes several times.
【0035】上記発酵処理を終えて浄化された発酵済内
容物は上記入出開口18から外部に取出すことができ
る。この場合、混合ドラム10の入出開口18に汚泥を
投入した側とは反対側に発酵済内容物を取込むためのケ
ースを置き、上記菌混合処理の時に回転させた方向とは
逆方向に回転させることにより、上記入出開口18を通
じてケース内に発酵済内容物が落下する。混合ドラム1
0内の内周壁部11bには多数の掬上げフィン15が取
付けられて内容物が塞止められるので、上記逆回転時に
大量にケースに落下することが防止され、適量ずつ取出
せることとなる。上記発酵済内容物は処理品(発酵済内
容物のうち堆肥化されて肥料として利用されるものを処
理品と呼ぶ。以下同様)として農作物の肥料に利用され
る他、上記した通り戻し材として混合ドラム10内に残
し又は汚泥に混合させることもできる。The fermented contents purified after the completion of the fermentation treatment can be taken out through the inlet / outlet opening 18. In this case, a case for taking in the fermented contents is placed on the side opposite to the side into which the sludge is introduced into the inlet / outlet opening 18 of the mixing drum 10, and rotated in a direction opposite to the direction rotated during the bacteria mixing process. By doing so, the fermented contents fall into the case through the inlet / outlet opening 18. Mixing drum 1
Since a large number of scooping fins 15 are attached to the inner peripheral wall portion 11b inside 0 and the contents are closed, it is possible to prevent a large amount from falling into the case during the reverse rotation and to take out a suitable amount. The fermented content is used as a processed product (the fermented content that is composted and used as a fertilizer is referred to as a processed product. The same applies to the following). It can be left in the mixing drum 10 or mixed with sludge.
【0036】次に、本発明の第2実施例において、図4
を参照して説明する。本実施例は基本的に上記第1実施
例と同様の構成となっているが、本実施例においては、
上記粉砕混合機構20を構成する回転羽23を略大径に
形成させ、該回転羽23を取付けた回転駆動軸22の下
方にて、上記回転羽23の下半部が上記混合ドラム10
内下部に堆積した汚泥に埋接するようにし、上記回転駆
動軸22の回転により上記回転羽23が直接粉砕するよ
うにしてある。この場合においても、上記回転駆動軸2
2は混合ドラム10の回転中心の上部側方である回転上
り側位置であって上記掬上げられた汚泥が落下される位
置に偏心させて取付けてあり、回転上り側にある掬上げ
フィン15に近接することとなる。Next, in the second embodiment of the present invention, FIG.
This will be described with reference to FIG. This embodiment has basically the same configuration as the first embodiment, but in this embodiment,
The rotating blades 23 constituting the crushing and mixing mechanism 20 are formed to have a substantially large diameter, and the lower half of the rotating blades 23 is positioned below the rotary drive shaft 22 to which the rotating blades 23 are attached.
The rotary blade 23 is directly crushed by the rotation of the rotary drive shaft 22 so as to be buried in the sludge accumulated in the lower portion. Also in this case, the rotation drive shaft 2
Numeral 2 is an eccentrically mounted position on the rotation ascending side, which is the upper side of the rotation center of the mixing drum 10, and is eccentrically attached to a position where the scooped sludge falls, and is attached to the scooping fin 15 on the rotation ascending side. It will be close.
【0037】また、基台30はその上部が開口し、該開
口の下方位置に堆肥取出機構35が設けられている。該
堆肥取出機構35は上部開口状に形成され、この開口に
堆肥を落下させて収納することができ、上記堆肥取出機
構35の側面側に設けた堆肥取出口35aから堆肥を適
量ずつ取出自在としている。The base 30 has an opening at the top, and a compost take-out mechanism 35 is provided below the opening. The compost take-out mechanism 35 is formed in an upper opening shape, and the compost can be dropped and stored in this opening, and a suitable amount of compost can be taken out from a compost take-out port 35a provided on the side surface of the compost take-out mechanism 35. I have.
【0038】次に本実施例の作用について説明する。本
実施例においては上記第1実施例と基本的に同様の作用
をなす。しかし、以下の点で第1実施例における作用と
は異なる。すなわち、本実施例における上記粉砕混合機
構20を構成する回転羽23を略大径に形成させている
ため、上記混合ドラム10内に堆積した汚泥に上記回転
羽23が埋没し、上記回転駆動軸22の回転と共に直接
汚泥を粉砕させることができ、よりいっそう効率良く粉
砕混合処理を行うことができるものである。Next, the operation of this embodiment will be described. In this embodiment, the operation is basically the same as that of the first embodiment. However, the operation differs from that of the first embodiment in the following points. That is, since the rotating blades 23 constituting the crushing and mixing mechanism 20 in this embodiment are formed to have a substantially large diameter, the rotating blades 23 are buried in the sludge accumulated in the mixing drum 10 and the rotary drive shaft The sludge can be directly crushed with the rotation of 22, and the crushing and mixing treatment can be performed more efficiently.
【0039】また、上記発酵処理を終えて浄化された発
酵済内容物は上記入出開口18から外部に取出すことが
できる。この場合、混合ドラム10を上記菌混合処理の
時に回転させた方向とは逆方向に回転させることによ
り、上記入出開口18を通じて堆肥取出機構35に発酵
済内容物が落下する。混合ドラム10内の内周壁部11
bには多数の掬上げフィン15が取付けられて内容物が
塞止められるので、上記逆回転時に大量に上記堆肥取出
機構35に落下することが防止される。また、堆肥取出
機構35に一定量の発酵済内容物を収納してから適量ず
つ取出すこともできる。上記発酵済内容物は処理品とし
て農作物の肥料に利用されるほか、上記した通り戻し材
として混合ドラム10内に残し又は汚泥に混合させるこ
ともできる。Further, the fermented contents that have been purified after the fermentation treatment can be taken out through the inlet / outlet opening 18. In this case, by rotating the mixing drum 10 in a direction opposite to the direction rotated during the bacteria mixing process, the fermented contents fall into the compost take-out mechanism 35 through the inlet / outlet opening 18. Inner peripheral wall portion 11 in mixing drum 10
Since a large number of scooping fins 15 are attached to b and the contents are closed, a large amount of falling to the compost take-out mechanism 35 during the reverse rotation is prevented. Alternatively, a certain amount of fermented contents can be stored in the compost take-out mechanism 35 and then taken out in an appropriate amount. The fermented content is used as a processed product in fertilizers of agricultural products, and can be left in the mixing drum 10 as a return material or mixed with sludge as described above.
【0040】次に、本発明の第3実施例において、図5
を参照して説明する。本実施例は基本的に上記第1実施
例と同様の構成となっており、混合ドラム10を基台3
0上に回転支持装置31を介して回転自在に支持してな
るもので、上記混合ドラム10の両側面に側面板12、
12を面接触状に取付け、該側面板12、12は支持ア
ーム21に設けた押圧機構13により常時一定の圧力で
混合ドラム10の側面に押圧されて非回転状に支持され
てなる。また、第1実施例と同様に上記混合ドラム10
内に多数の掬上げフィン15、15と粉砕混合機構20
とを設けており、汚泥が上記混合ドラム10の回転と共
に掬上げられ、上記粉砕混合機構20に落下して細かく
粉砕される。Next, in a third embodiment of the present invention, FIG.
This will be described with reference to FIG. This embodiment has basically the same configuration as that of the above-described first embodiment.
The mixing drum 10 is rotatably supported on a rotating support device 31. Side plates 12 are provided on both side surfaces of the mixing drum 10.
The side plates 12, 12 are pressed against the side surface of the mixing drum 10 at a constant pressure by a pressing mechanism 13 provided on a support arm 21 and are supported non-rotatably. Further, similarly to the first embodiment, the mixing drum 10
A large number of scooping fins 15, 15 and a crushing and mixing mechanism 20
The sludge is scooped up with the rotation of the mixing drum 10 and falls into the crushing / mixing mechanism 20 to be finely crushed.
【0041】一方、本実施例においては、上記掬上げフ
ィン15、15の端部をそれぞれ上向き鉤状に形成させ
ており、汚泥をいっそう効率良く掬上げて上記粉砕混合
機構20に落下させるようにしてある。上記粉砕混合機
構20を構成する回転羽23は多数の十字羽からなり、
これらの十字羽を上記回転駆動軸22に対して略垂直に
軸着して形成させる。また、この十字羽を軸方向に略重
層状に多数重ねると共に、各層の十字羽の放射角度を交
互に45度ずつずらして取付ける。On the other hand, in the present embodiment, the ends of the scooping fins 15 and 15 are each formed in an upward hook shape so that the sludge is scooped up more efficiently and dropped into the crushing and mixing mechanism 20. It is. The rotary wings 23 constituting the crushing and mixing mechanism 20 are composed of a large number of cross wings,
These cross feathers are formed so as to be pivoted substantially perpendicularly to the rotation drive shaft 22. In addition, a large number of the cruciforms are superimposed in the axial direction in a substantially layered manner, and the radiating angles of the cruciforms of each layer are alternately shifted by 45 degrees.
【0042】上記混合ドラム10内には送風機構40が
備えてあり、該送風機構40は一対の支軸管42、42
と多数の送風板41、41とから構成される。上記支軸
管42、42はそれぞれ混合ドラム10の内部において
長手方向に長尺状に形成され、上記混合粉砕機構の回転
駆動軸22と同じ高さで、かつ、上記混合ドラム10の
回転下り側に偏心して両端が側面板12、12に固定さ
れている。A blower mechanism 40 is provided in the mixing drum 10, and the blower mechanism 40 includes a pair of support pipes 42, 42.
And a number of blower plates 41, 41. Each of the support pipes 42 is formed in the mixing drum 10 to be elongated in the longitudinal direction, has the same height as the rotation drive shaft 22 of the mixing and crushing mechanism, and has a lower rotation side of the mixing drum 10. And both ends are fixed to the side plates 12 and 12.
【0043】上記多数の送風板41、41はそれぞれ略
四半円の薄板からなり、その円の中心に近傍する位置に
て上記支持管42、42が貫通し、該支持管42、42
により懸吊されるように送風板41、41が固定され
る。該送風板41、41はその円弧が混合ドラム10の
下部に堆積した汚泥に埋没し、かつ、混合ドラム10の
回転時に上記掬上げフィン15、15に接触しない程度
の長さにてなる。上記各送風板41、41は相互に等間
隔にて重層状に配置される。Each of the large number of blowers 41, 41 is formed of a substantially quarter-circle thin plate, and the support tubes 42, 42 penetrate at a position near the center of the circle.
The blower plates 41, 41 are fixed so as to be suspended. The blowers 41 have a length such that their arcs are buried in the sludge deposited on the lower part of the mixing drum 10 and do not come into contact with the scooping fins 15 when the mixing drum 10 rotates. The blowers 41, 41 are arranged in layers at equal intervals.
【0044】上記一方の側面板12には空気供給口16
及び空気抜口17が取付けられている。そして、空気供
給口16は上記一方の支持管42に連通している。ま
た、上記送風板41、41のそれぞれの内部に円の中心
近傍位置から放射状に一様に伸びる送風用の細管44、
44が多数設けられている。該細管44、44はそれぞ
れ上記支軸管42に継合されている。このように上記空
気供給口16と一方の支持管42と細管44、44が互
いに連通しており、上記空気供給口16から取り入れら
れた空気が一方の支持管42及び上記細管44、44を
通じ上記送風板41、41の円弧の端部から噴出し、堆
積した汚泥中に均等に空気を供給するものである。The one side plate 12 has an air supply port 16.
And an air vent 17. The air supply port 16 communicates with the one support pipe 42. In addition, in each of the blower plates 41, 41, a thin tube 44 for blower that extends uniformly radially from a position near the center of the circle,
A number 44 are provided. The thin tubes 44 are connected to the support tube 42, respectively. As described above, the air supply port 16, the one support pipe 42, and the thin tubes 44, 44 are in communication with each other, and the air taken in from the air supply port 16 passes through the one support pipe 42 and the thin tubes 44, 44. The air is supplied from the ends of the circular arcs of the blower plates 41 and 41 to uniformly supply air into the accumulated sludge.
【0045】一方、上記空気抜口17は混合ドラム10
内の蒸気や臭気を外部に排出するためのものであり、上
記空気供給口16の上部にて上記側面板12に取付けら
れる。なお、上記空気供給口16は上記側面板12を介
して上記一方の支軸管42と連通状に結合させるが、い
ずれの支軸管42と連通させてもよく、また双方の支軸
管42と連通させてもよい。この場合、上記細管44、
44は空気供給口16と連通するいずれかの又は双方の
支軸管42に連通することもちろんである。On the other hand, the air vent 17 is
This is for discharging steam and odor inside to the outside, and is attached to the side plate 12 above the air supply port 16. The air supply port 16 is connected to the one of the support pipes 42 through the side plate 12 in a communicating manner, but may be connected to any one of the support pipes 42. May be communicated with. In this case, the thin tube 44,
44 is, of course, in communication with one or both of the shaft pipes 42 communicating with the air supply port 16.
【0046】また、基台30は上記第2実施例と同様に
その上部が開口し、該開口の下方位置に堆肥取出機構3
5が設けられている。該堆肥取出機構35は上部開口状
に形成され、この開口に堆肥を落下させて収納すること
ができ、上記堆肥取出機構35の側面側に設けた堆肥取
出口35aから堆肥を適量ずつ取り出し自在としてい
る。The base 30 has an opening at the top thereof as in the second embodiment, and the compost take-out mechanism 3 is located below the opening.
5 are provided. The compost take-out mechanism 35 is formed in an upper opening shape, and the compost can be dropped and stored in this opening, and a suitable amount of compost can be taken out from a compost take-out port 35a provided on the side of the compost take-out mechanism 35. I have.
【0047】次に本実施例の作用について説明する。ま
ず、回転する混合ドラム10に対し、その外周壁部11
aに設けた入出開口18から処理対象の汚泥を投入す
る。この時、同時に前記した好熱菌を適量投入する。投
入量としては投入する汚泥の重量に対して例えば約50
0分の1の重量の好熱菌を投入する。なお、投入する菌
として本実施例においては好熱菌を用いるが、該好熱菌
に限定されるものではなく、上記光栄養細菌を投入する
こともでき、もしくは好熱菌及び光栄養細菌の双方を投
入してもよい。光栄養細菌を使用する場合は別途、光照
射装置を備えることが必要である。また、好熱菌を投入
する代わりに好熱菌が十分に培養された発酵済内容物の
一部を戻し材として新汚泥と略等分量を投入することも
できる。さらに、汚泥の臭気を消すために上記空気供給
口16から消臭剤を注入してもよい。消臭剤としては発
酵処理において発生した水蒸気を予め回収しておき、こ
れを注入するのが効果的である。Next, the operation of this embodiment will be described. First, the outer peripheral wall 11 of the rotating mixing drum 10 is
The sludge to be treated is introduced from the inlet / outlet opening 18 provided at a. At this time, an appropriate amount of the thermophilic bacterium described above is added at the same time. The input amount is, for example, about 50 to the weight of the sludge to be input.
The thermophilic bacterium of 1/0 weight is injected. In this example, a thermophilic bacterium is used as a bacterium to be added. However, the bacterium is not limited to the thermophilic bacterium. You may throw in both. When using phototrophic bacteria, it is necessary to separately provide a light irradiation device. Instead of adding the thermophilic bacterium, a part of the fermented contents in which the thermophilic bacterium has been sufficiently cultured can be used as a return material and an approximately equal amount of the new sludge can be used. Further, a deodorant may be injected from the air supply port 16 in order to eliminate the odor of the sludge. As a deodorant, it is effective to collect in advance the steam generated in the fermentation treatment and inject it.
【0048】上記混合ドラム10の内周壁部11bに
は、薄板片からなる多数の掬上げフィン15、15を設
けてあり、混合ドラム10の回転によって、汚泥が上方
に掬上げられる。この際、上記入出開口18に向かって
汚泥を逆流させないように、入出開口18の開口部分側
の端部が上方に移動する方向で上記混合ドラム10を低
速で回転させる。そして、掬上げられた汚泥は高速で回
転する回転羽23の上に落下して細かく粉砕される。そ
してさらに下方に落下した汚泥は、引続き掬上げフィン
15によって再度連続的に上方へ掬上げられ再び回転羽
23上に落下してより一層細かく粉砕される。The inner peripheral wall 11b of the mixing drum 10 is provided with a large number of scooping fins 15 and 15 made of thin plate pieces, and the sludge is scooped upward by the rotation of the mixing drum 10. At this time, the mixing drum 10 is rotated at a low speed in a direction in which the end on the opening portion side of the inlet / outlet 18 moves upward so as to prevent the sludge from flowing back toward the inlet / outlet 18. Then, the scooped sludge falls on the rotating blades 23 rotating at a high speed and is finely crushed. Then, the sludge that has fallen further downward is continuously scooped up again by the scooping fins 15 again, falls again on the rotating blades 23, and is further finely pulverized.
【0049】このように細かく粉砕された汚泥には上記
した細菌が混合される。そして上記回転を停止し又は回
転させながら、菌混合汚泥を混合ドラム10内に置いた
まま保持して発酵させる。上記混合ドラム10内を負圧
にして上記空気供給口16から空気を混入すると、上記
支軸管42及び上記細管44、44を通じて菌混合汚泥
中に均等に空気が混入される。このように汚泥中に空気
が混入され、また混合ドラム10内の好気性が高まるこ
とにより発酵が促進される。なお、上記混合ドラム10
を回転させているとき既に発酵は始まっているため、空
気を混入させて発酵を促進させるのは上記静止状態での
養生期間には限られず、常時混合ドラム10内を負圧に
することが望ましい。発酵処理において発生した蒸気や
臭気は上記の通り上記空気抜口17を利用して外部に排
出させ、必要に応じて該排出された蒸気等を再度上記空
気供給口16から投入させるようにする。The bacteria mentioned above are mixed with the sludge finely ground in this way. Then, while the rotation is stopped or rotated, the bacteria-mixed sludge is held in the mixing drum 10 and fermented. When air is mixed from the air supply port 16 by setting the inside of the mixing drum 10 to a negative pressure, the air is uniformly mixed into the bacteria-mixed sludge through the support tube 42 and the small tubes 44. As described above, air is mixed into the sludge, and the aerobicity in the mixing drum 10 is increased, thereby promoting fermentation. The mixing drum 10
Since the fermentation has already begun when is rotated, the promotion of fermentation by mixing air is not limited to the curing period in the above-mentioned stationary state, and it is preferable that the inside of the mixing drum 10 is always kept at a negative pressure. . The steam and odor generated in the fermentation treatment are discharged to the outside using the air vent 17 as described above, and the discharged steam and the like are supplied again from the air supply port 16 as necessary.
【0050】所定時間静止させた後、さらに汚泥に一様
に細菌が混合されるようにするため、再度混合ドラム1
0を一定方向に回転させて混合処理を繰り返す。また、
より発酵を促進させるためさらに菌を投入してもよい。
この菌の投入量や混入する空気量を調整することにより
発酵の促進度、発酵温度等を調節する。発酵温度が高ま
るほど浄化は促進される。上記一連の処理を数度繰り返
しながら約2日間の養生期間を経て上記菌混合汚泥が浄
化される。After standing still for a predetermined period of time, the mixing drum 1 is again used to uniformly mix the bacteria with the sludge.
0 is rotated in a certain direction, and the mixing process is repeated. Also,
Bacteria may be further added to further promote fermentation.
The degree of acceleration of fermentation, the fermentation temperature, and the like are adjusted by adjusting the amount of the bacteria and the amount of air to be mixed. Purification is promoted as the fermentation temperature increases. The bacteria-mixed sludge is purified through a curing period of about two days while repeating the above series of processes several times.
【0051】上記発酵処理を終えて浄化された発酵済内
容物は上記入出開口18から外部に取出すことができ
る。この場合、混合ドラム10を上記菌混合処理の時に
回転させた方向とは逆方向に回転させることにより、上
記入出開口18を通じて堆肥取出機構35に発酵済内容
物が落下する。混合ドラム10内の内周壁部11bには
多数の掬上げフィン15が取付けられて内容物が塞止め
られるので、上記逆回転時に大量に上記堆肥取出機構3
5に落下することが防止される。また、堆肥取出機構3
5に一定量の発酵済内容物を収納してから適量ずつ取出
すこともできる。上記発酵済内容物は処理品として農作
物の肥料に利用される他、上記した通り戻し材として混
合ドラム10内に残し又は汚泥に混合させることもでき
る。The fermented contents which have been purified after the fermentation treatment can be taken out through the inlet / outlet opening 18. In this case, by rotating the mixing drum 10 in a direction opposite to the direction rotated during the bacteria mixing process, the fermented contents fall into the compost take-out mechanism 35 through the inlet / outlet opening 18. Since a large number of scooping fins 15 are attached to the inner peripheral wall portion 11b in the mixing drum 10 to block the contents, a large amount of the compost take-out mechanism 3 is rotated during the reverse rotation.
5 is prevented. In addition, compost removal mechanism 3
5, a certain amount of fermented contents can be stored and then taken out in an appropriate amount. The fermented contents are used as fertilizers for agricultural products as processed products, and can also be left in the mixing drum 10 as a return material as described above or mixed with sludge.
【0052】[0052]
【発明の効果】以上のように本発明によれば、粉砕混合
機構を備えて回転自在に支持された混合ドラムの外周に
汚泥の入出開口を設けると共に、その内周に多数の掬上
げフィンを設け、一定方向に上記混合ドラムを回転させ
て菌混合処理をした後所定時間置いて発酵処理をする構
成としたことから、簡易な装置で汚泥を浄化できると共
に、浄化処理時間を大幅に短縮させることができるとい
う効果がある。As described above, according to the present invention, a sludge inlet / outlet is provided on the outer periphery of a rotatably supported mixing drum provided with a pulverizing / mixing mechanism, and a large number of scooping fins are provided on the inner periphery thereof. Since the fermentation treatment is performed after a predetermined time has elapsed after the bacteria mixing treatment by rotating the mixing drum in a certain direction, the sludge can be purified with a simple device, and the purification treatment time is greatly reduced. There is an effect that can be.
【0053】回転自在に支持された混合ドラムの筒の外
周壁部側に突出状の汚泥の入出開口を形成したことか
ら、上記混合ドラムを一定方向に回転させて汚泥の逆流
をなくし、その一方で上記混合ドラムを上記混合時の回
転とは逆方向に回転させることにより上記入出開口から
菌混合汚泥又は発酵済内容物を外部へ取出すことができ
るという効果がある。また、上記混合ドラム内の内周壁
部には掬上げフィンが多数設けられて内容物が塞止めら
れるので、上記逆回転時に大量に排出されることを防止
し、適量ずつ取出すことができるという効果がある。Since the projecting sludge inlet / outlet opening is formed on the outer peripheral wall side of the rotatably supported mixing drum cylinder, the mixing drum is rotated in a certain direction to eliminate the backflow of sludge. By rotating the mixing drum in a direction opposite to the rotation during mixing, there is an effect that the bacteria-mixed sludge or the fermented contents can be taken out from the inlet / outlet opening. Further, since a large number of scooping fins are provided on the inner peripheral wall portion in the mixing drum and the contents are closed, it is possible to prevent a large amount from being discharged at the time of the reverse rotation and to take out an appropriate amount. There is.
【0054】上記多数の波状羽からなる回転羽を高速に
回転させてなる粉砕混合機構を設けたことから、投入し
た汚泥を均一に粉砕し菌を均一に混合させることがで
き、均一な発酵と完全な浄化処理が図られると共に、処
理品としてもより良質な肥料にすることができるという
効果がある。また、上記回転羽を取付けた回転駆動軸を
混合ドラムの回転中心の上部側方である回転上り側位置
であって上記掬上げられた汚泥が落下される位置に偏心
させて取付ける構成としたことから、粉砕混合機構が混
合ドラムの内周壁部の回転上り側に近傍することとな
り、掬上げフィンにより掬上げられた汚泥を漏らさず効
率良く粉砕混合機構に落下させることができるという効
果がある。Since the crushing / mixing mechanism is provided by rotating the rotating wings composed of the large number of wavy wings at a high speed, the sludge introduced can be crushed uniformly and the bacteria can be uniformly mixed. There is an effect that a complete purification treatment can be achieved, and a higher quality fertilizer can be obtained as a treated product. In addition, the rotary drive shaft to which the rotating blades are attached is eccentrically attached to a position where the scooped sludge falls at a rotation ascending position which is an upper side of the rotation center of the mixing drum. Therefore, the pulverizing / mixing mechanism is located near the rotation-up side of the inner peripheral wall of the mixing drum, and the sludge scooped up by the scooping fins can be efficiently dropped into the pulverizing / mixing mechanism without leaking.
【0055】上記側面板に空気供給口を設けて上記混合
ドラム内に空気を混入可能とすると共に、上記側面板に
空気抜口を設けて上記混合ドラム内から空気を排出可能
としたことから、上記菌混合処理した汚泥に酸素を供給
して好気的にし発酵を促進させることができると共に、
発生した蒸気や臭気を上記空気抜口から外部に排出させ
ることができるという効果がある。また、上記空気抜口
から外部へ排出された蒸気又は該蒸気を凝縮させた水を
再度上記空気供給口へ導くための配管を備え、該配管の
途中に該蒸気を凝縮させるための凝縮機を備えてなるこ
ととしたことから、混合ドラム内での汚泥発酵時に発生
する異臭を効果的に消臭することができるいう効果があ
る。An air supply port is provided in the side plate so that air can be mixed into the mixing drum, and an air vent is provided in the side plate so that air can be discharged from the mixing drum. While supplying oxygen to the sludge mixed with the bacteria and aerobically to promote fermentation,
There is an effect that generated steam and odor can be discharged to the outside through the air vent. Further, a pipe for guiding the steam discharged from the air vent to the outside or water condensed with the steam to the air supply port again is provided, and a condenser for condensing the steam is provided in the middle of the pipe. Since it is provided, there is an effect that an odor generated during sludge fermentation in the mixing drum can be effectively deodorized.
【0056】上記混合ドラム内に多数の送風板と一対の
支軸管とからなる送風機構を設け、この送風板を等間隔
に重層状に形成させ、その内部に一方の上記支軸管に継
合させた多数の細管を設ける構成としたことから、混合
ドラム内に堆積する汚泥中に均等に酸素を供給して効率
良く発酵を促進することができるという効果がある。ま
た、他方の支軸管を通じて混合ドラム内の蒸気や臭気を
均等に外部へ排出することができるという効果がある。An air blowing mechanism comprising a large number of air blowing plates and a pair of shaft pipes is provided in the mixing drum, and the air blowing plates are formed in a layered manner at equal intervals, and connected to one of the shaft pipes therein. Since a large number of combined thin tubes are provided, there is an effect that the fermentation can be efficiently promoted by uniformly supplying oxygen to the sludge deposited in the mixing drum. Further, there is an effect that the steam and the odor in the mixing drum can be uniformly discharged to the outside through the other spindle tube.
【図1】本発明の第1実施例の外周壁部方向から見た縦
断面図である。FIG. 1 is a longitudinal sectional view of a first embodiment of the present invention as viewed from a direction of an outer peripheral wall portion.
【図2】本発明の第1実施例の側面板方向から見た縦断
面図である。FIG. 2 is a longitudinal sectional view of the first embodiment of the present invention as viewed from a side plate.
【図3】本発明の第1実施例の側面板方向から見た側面
図である。FIG. 3 is a side view of the first embodiment of the present invention as viewed from a side plate.
【図4】本発明の第2実施例の側面板方向から見た縦断
面図である。FIG. 4 is a longitudinal sectional view of a second embodiment of the present invention as viewed from a side plate.
【図5】本発明の第3実施例の斜視図である。FIG. 5 is a perspective view of a third embodiment of the present invention.
【図6】本発明の第3実施例の側面板方向から見た縦断
面図である。FIG. 6 is a longitudinal sectional view of a third embodiment of the present invention as viewed from a side plate.
10 混合ドラム 11a 外周壁部 11b 内周壁部 12 側面板 13 押圧機構 14 パッキング材 15 掬上げフィン 16 空気供給口 17 空気抜口 18 入出開口 19a 入出弁 19b 逆止弁 20 粉砕混合機構 21 支持アーム 22 回転駆動軸 23 回転羽 24 駆動装置 25 フライホイール 30 基台 31 回転支持装置 32 駆動ローラ 33 ローラ駆動装置 34 ローラ回転軸 35 堆肥取出機構 35a 取出口 40 送風機構 41 送風板 42 支軸管 44 細管 50 配管 51 凝縮機 Reference Signs List 10 mixing drum 11a outer peripheral wall 11b inner peripheral wall 12 side plate 13 pressing mechanism 14 packing material 15 scooping fin 16 air supply port 17 air vent 18 inlet / outlet opening 19a inlet / outlet valve 19b check valve 20 pulverizing / mixing mechanism 21 support arm 22 Rotary drive shaft 23 Rotary wing 24 Drive device 25 Flywheel 30 Base 31 Rotation support device 32 Drive roller 33 Roller drive device 34 Roller rotation shaft 35 Compost take-out mechanism 35a Outlet 40 Blow mechanism 41 Blow plate 42 Support tube 44 Narrow tube 50 Piping 51 Condenser
Claims (10)
の筒状の混合ドラムを回転支持装置にて回転自在に支持
してなり、この混合ドラムの両側面には側面板を面接触
状に取付けると共に、この側面板は支持機構により混合
ドラムの側面に非回転状に支持されてなり、上記混合ド
ラムの筒の外周壁部側に入出開口を設けて汚泥を取入れ
又は取出し自在とし、 上記混合ドラムの内周壁部には掬上げフィンを設けてあ
って混合ドラムの回転によって汚泥を上方に掬上げ自在
としてなり、 上記混合ドラムは上記投入された汚泥を均一に粉砕して
上記菌と均一に混合させることにより均一な発酵を促進
させるための粉砕混合機構を備えるもので、この粉砕混
合機構は側面板を介在して回転自在に軸支された回転駆
動軸と、この回転駆動軸に取付けられた回転羽と、回転
駆動軸を回転させる駆動装置とから構成され、上記掬上
げフィンによって上部に掬上げられた汚泥を上記回転羽
にて細かく粉砕して菌を混合自在としてなることを特徴
とする菌混合浄化装置。1. A cylindrical mixing drum for mixing sludge into sludge by pouring sludge therein is rotatably supported by a rotary support device, and a side plate is brought into surface contact with both side surfaces of the mixing drum. The side plate is supported non-rotatably on the side surface of the mixing drum by a support mechanism, and an inlet / outlet opening is provided on the outer peripheral wall side of the cylinder of the mixing drum so that sludge can be taken in or taken out, A scooping fin is provided on the inner peripheral wall portion of the mixing drum so that the sludge can be scooped up by the rotation of the mixing drum, and the mixing drum uniformly crushes the input sludge and the bacteria. It is equipped with a pulverizing and mixing mechanism to promote uniform fermentation by mixing uniformly, and this pulverizing and mixing mechanism includes a rotary drive shaft rotatably supported via a side plate, and a rotary drive shaft. Mounted The rotating blades and the driving device for rotating the rotary drive shaft are constituted, and the sludge scooped up by the scooping fins is finely pulverized by the rotating blades to mix bacteria. Bacteria mixed purification device.
分が上方に移動する方向で回転させて汚泥を菌混合処理
し、 上記混合ドラム内で菌混合処理し又は発酵処理した内容
物を上記混合時の回転に対して逆方向に上記混合ドラム
を回転させることにより上記入出開口から外部へ適量に
て取出自在とすることを特徴とする請求項1記載の菌混
合浄化装置。2. The mixing drum is rotated in a direction in which the opening portion of the inlet / outlet moves upward to mix bacteria with sludge, and the content mixed or mixed with bacteria in the mixing drum is subjected to fermentation. 2. The apparatus for purifying and mixing bacteria according to claim 1, wherein the mixing drum is rotated in a direction opposite to the rotation at the time of mixing so that a suitable amount can be taken out from the inlet / outlet to the outside.
ドラムの回転中心の上部側方である回転上り側位置であ
って上記掬上げられた汚泥が落下される位置に偏心させ
て取付けてあることを特徴とする請求項1又は2記載の
菌混合浄化装置。3. A rotary drive shaft to which the rotary blades are attached is mounted eccentrically at a rotational upside position which is an upper side of the rotation center of the mixing drum and at a position where the scooped sludge falls. 3. The apparatus for purifying and mixing bacteria according to claim 1, wherein:
合ドラム内に空気を混入自在とすると共に、上記側面板
に空気抜口を設けることにより上記菌混合処理した汚泥
を混合ドラム内にて発酵処理させる際に発生する蒸気や
臭気を上記空気抜口から外部に排出自在とすることを特
徴とする請求項1乃至3記載の菌混合浄化装置。4. An air supply port is provided on said side plate to allow air to be freely mixed into said mixing drum, and said side plate is provided with an air vent to allow said bacteria-mixed sludge to enter the mixing drum. The apparatus for purifying bacteria mixed with bacteria according to claim 1, wherein steam and odor generated during the fermentation treatment can be discharged to the outside through the air vent.
設けると共に、該空気抜口から外部へ排出された蒸気又
は該蒸気を凝縮させた水を再度上記空気供給口へ導くた
めの配管を備え、該配管の途中に上記蒸気を凝縮させる
ための凝縮機を備えてなることを特徴とする請求項1乃
至3記載の菌混合浄化装置。5. A pipe for providing an air supply port and an air vent on the side plate, and for guiding steam discharged from the air vent to the outside or water condensed to the steam to the air supply port again. The apparatus for purifying and mixing bacteria according to any one of claims 1 to 3, further comprising a condenser for condensing the vapor in the middle of the pipe.
送風機構が多数の送風板と該送風板を軸支する一対の支
軸管とから構成され、該支軸管には上記空気供給口が上
記側面板を介在して連通状に結合され、上記送風板の内
部には支軸管に連通状に継合させた多数の細管を形成さ
せ、上記空気供給口、支軸管及び細管を通じて混合ドラ
ム内に送風自在としてなることを特徴とする請求項4又
は5記載の菌混合浄化装置。6. A blower mechanism is provided in the mixing drum, and the blower mechanism is composed of a number of blower plates and a pair of support tubes for supporting the blower plates. The mouth is connected in a communicating manner with the side plate interposed therebetween, and inside the blower plate, a number of small tubes connected to the supporting tube are formed, and the air supply port, the supporting tube and the small tube are formed. The bacteria mixing and purifying apparatus according to claim 4, wherein air can be freely blown into the mixing drum through the passage.
壁部との二重壁にて形成されており、該二重壁の間に温
湯を循環させるための昇温用配管を備えてなることを特
徴とする請求項1乃至6記載の菌混合浄化装置。7. A peripheral wall of the mixing drum is formed by a double wall of an outer peripheral wall and an inner peripheral wall, and a heating pipe for circulating hot water is provided between the double walls. The apparatus for purifying and mixing bacteria according to any one of claims 1 to 6, wherein:
の筒状の混合ドラムを回転支持装置にて回転自在に支持
し、この混合ドラムの両側面に側面板を面接触状に取付
け、この側面板を支持機構により混合ドラムの側面に非
回転状に支持し、 上記混合ドラムの筒の外周壁部側に入出開口を設けると
共に、その内周壁部に掬上げフィンを設け、 上記混合ドラムに粉砕混合機構を備え、この粉砕混合機
構が側面板を介在して回転自在に軸支された回転駆動軸
と、この回転駆動軸に取付けられた回転羽と、回転駆動
軸を回転させる駆動装置とから構成され、 上記入出開口から混合ドラムに汚泥を取入れ、上記混合
ドラムを上記入出開口の開口部分が上方に移動する方向
で所定時間回転させて汚泥を菌と混合して処理し、上記
菌混合処理した菌混合汚泥を所定時間静止状態を保持し
て発酵処理し、 次いで、上記混合時の回転に対して逆方向に上記混合ド
ラムを回転させることにより上記発酵処理した発酵処理
済内容物を上記入出開口から外部へ適量にて取出すこと
を特徴とする菌混合浄化方法。8. A cylindrical mixing drum for throwing sludge into pulverized and mixed bacteria is rotatably supported by a rotary support device, and side plates are attached to both side surfaces of the mixing drum in a face contact manner. The side plate is non-rotatably supported on the side surface of the mixing drum by a support mechanism, an inlet / outlet opening is provided on the outer peripheral wall side of the mixing drum cylinder, and a scooping fin is provided on the inner peripheral wall thereof. A crushing / mixing mechanism is provided on the drum, and the crushing / mixing mechanism is rotatably supported via a side plate, a rotary drive shaft, a rotary wing attached to the rotary drive shaft, and a drive for rotating the rotary drive shaft. Sludge is taken into the mixing drum from the inlet / outlet opening, and the mixing drum is rotated for a predetermined time in a direction in which the opening portion of the inlet / outlet opening moves upward to mix the sludge with the bacterium for treatment. , The mixed bacterial soil treated The fermentation treatment is performed by keeping the mud stationary for a predetermined time and then fermenting the fermented contents by rotating the mixing drum in a direction opposite to the rotation during the mixing from the inlet / outlet opening. A method for purifying and mixing bacteria, which is taken out in an appropriate amount to the outside.
理をした後、上記混合ドラムの回転による菌混合処理を
再度行い、次いで静止状態を所定時間保持して発酵処理
を繰返すことを特徴とする請求項8記載の菌混合浄化方
法。9. After the fermentation treatment is performed while maintaining the stationary state for a predetermined time, the bacteria mixing processing is performed again by rotating the mixing drum, and then the fermentation processing is repeated while maintaining the stationary state for a predetermined time. The method for purifying and mixing bacteria according to claim 8.
めの筒状の混合ドラムを回転支持装置にて回転自在に支
持し、この混合ドラムの両側面に側面板を面接触状に取
付け、この側面板を支持機構により混合ドラムの側面に
非回転状に支持し、 上記混合ドラムの筒の外周壁部側に入出開口を設けると
共に、その内周壁部に掬上げフィンを設け、 上記混合ドラムに粉砕混合機構を備え、この粉砕混合機
構が側面板を介在して回転自在に軸支された回転駆動軸
と、この回転駆動軸に取付けられた回転羽と、回転駆動
軸を回転させる駆動装置とから構成され、 上記入出開口から混合ドラムに汚泥を取入れ、上記混合
ドラムを上記入出開口の開口部分が上方に移動する方向
で所定時間回転させて汚泥を菌と混合して処理し、かつ
上記菌混合処理した菌混合汚泥を上記混合ドラムを回転
させながら発酵処理し、 次いで、上記混合時の回転に対して逆方向に上記混合ド
ラムを回転させることにより上記発酵処理した発酵処理
済内容物を上記入出開口から外部へ適量にて取出すこと
を特徴とする菌混合浄化方法。10. A cylindrical mixing drum for throwing sludge and crushing and mixing bacteria is rotatably supported by a rotary support device, and side plates are attached to both side surfaces of the mixing drum in a face contact manner. The side plate is non-rotatably supported on the side surface of the mixing drum by a support mechanism, an inlet / outlet opening is provided on the outer peripheral wall side of the mixing drum cylinder, and a scooping fin is provided on the inner peripheral wall thereof. A crushing / mixing mechanism is provided on the drum, and the crushing / mixing mechanism is rotatably supported via a side plate, a rotary drive shaft, a rotary wing attached to the rotary drive shaft, and a drive for rotating the rotary drive shaft. Sludge is taken into the mixing drum from the inlet / outlet opening, and the mixing drum is rotated for a predetermined time in a direction in which the opening portion of the inlet / outlet opening moves upward to mix the sludge with the bacterium for treatment. , And a bacterium mixed and treated as described above The mixed sludge is subjected to fermentation processing while rotating the mixing drum, and then the fermentation-processed contents subjected to the fermentation processing by rotating the mixing drum in a direction opposite to the rotation during the mixing from the inlet / outlet opening. A method for purifying and mixing bacteria, which is taken out in an appropriate amount to the outside.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP31890097A JPH11128995A (en) | 1997-11-05 | 1997-11-05 | Device and process for bacteria mixing purification |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP31890097A JPH11128995A (en) | 1997-11-05 | 1997-11-05 | Device and process for bacteria mixing purification |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH11128995A true JPH11128995A (en) | 1999-05-18 |
Family
ID=18104234
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP31890097A Pending JPH11128995A (en) | 1997-11-05 | 1997-11-05 | Device and process for bacteria mixing purification |
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Country | Link |
---|---|
JP (1) | JPH11128995A (en) |
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CN109984312A (en) * | 2017-12-31 | 2019-07-09 | 宁波方太厨具有限公司 | A kind of fermentation machine |
KR102243513B1 (en) * | 2020-08-31 | 2021-04-22 | 주식회사 세명하이트 | Stirring Apparatus Of Activated Carbon For Filtering |
CN113289387A (en) * | 2021-04-26 | 2021-08-24 | 南京三美农业发展有限公司 | Solid-liquid separation device for preparing biological organic fertilizer and solid-liquid separation method thereof |
CN114590986A (en) * | 2022-03-31 | 2022-06-07 | 河北邯峰发电有限责任公司 | Coal fired power plant utilizes flue gas recirculation to mix and burns mud device |
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1997
- 1997-11-05 JP JP31890097A patent/JPH11128995A/en active Pending
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
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GB2507487A (en) * | 2012-10-30 | 2014-05-07 | Ashe Morris Ltd | Rotating flow reactor |
US10632449B2 (en) | 2012-10-30 | 2020-04-28 | Ashe Morris Ltd. | Method of mixing using an improved flow reactor |
CN105601081A (en) * | 2016-03-21 | 2016-05-25 | 华南理工大学 | Sludge wet wrapping dry mixing device and method |
CN109984312A (en) * | 2017-12-31 | 2019-07-09 | 宁波方太厨具有限公司 | A kind of fermentation machine |
CN109984312B (en) * | 2017-12-31 | 2023-11-17 | 宁波方太厨具有限公司 | Fermentation machine |
KR102243513B1 (en) * | 2020-08-31 | 2021-04-22 | 주식회사 세명하이트 | Stirring Apparatus Of Activated Carbon For Filtering |
CN113289387A (en) * | 2021-04-26 | 2021-08-24 | 南京三美农业发展有限公司 | Solid-liquid separation device for preparing biological organic fertilizer and solid-liquid separation method thereof |
CN114590986A (en) * | 2022-03-31 | 2022-06-07 | 河北邯峰发电有限责任公司 | Coal fired power plant utilizes flue gas recirculation to mix and burns mud device |
CN114590986B (en) * | 2022-03-31 | 2024-01-23 | 河北邯峰发电有限责任公司 | Device for mixing and burning sludge by utilizing flue gas recirculation in coal-fired power plant |
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