JP2002263699A - Digester - Google Patents

Digester

Info

Publication number
JP2002263699A
JP2002263699A JP2001069012A JP2001069012A JP2002263699A JP 2002263699 A JP2002263699 A JP 2002263699A JP 2001069012 A JP2001069012 A JP 2001069012A JP 2001069012 A JP2001069012 A JP 2001069012A JP 2002263699 A JP2002263699 A JP 2002263699A
Authority
JP
Japan
Prior art keywords
sludge
digested
tank
digested sludge
containing liquid
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
Application number
JP2001069012A
Other languages
Japanese (ja)
Inventor
Hisato Takeda
久人 竹田
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.)
Sumitomo Heavy Industries Ltd
Original Assignee
Sumitomo Heavy Industries 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 Sumitomo Heavy Industries Ltd filed Critical Sumitomo Heavy Industries Ltd
Priority to JP2001069012A priority Critical patent/JP2002263699A/en
Publication of JP2002263699A publication Critical patent/JP2002263699A/en
Pending 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
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel

Landscapes

  • Processing Of Solid Wastes (AREA)
  • Treatment Of Sludge (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a digester which is capable of surely digesting organic matters containing a hardly biodegradable material and has high treatment capability. SOLUTION: Filtering means 5 for compartmentalizing the sludge-containing liquid in a chamber 1 is installed between a material-to-be-treated introducing port 3 and a digested sludge discharge port 2 and the organic matter, such as the hardly biodegradable material, which is larger than a prescribed size and takes time to be digested is held in the sludge-containing liquid on the material-to-be-treated introducing port 3 side and is sufficiently digested and is prevented from moving to the digested sludge discharge port 2 side until its size is made smaller than the prescribed size. As a result, the organic matters, such as the hardly biodegradable material, larger than the prescribed size is prevented from being discharged together with the digested sludge while the organic matter is kept undigested in discharging the digested sludge from the digested sludge discharge port 2. The hardly biodegradable material increases its surface area and exhibits a function as a carrier of digesting bacterial as the digestion progresses and therefore the contact efficiency of the organic matters and the digesting bacteria in the sludge-containing liquid is improved and the digestion rate of the organic matter is improved.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、生物難分解性物質
を含む有機物質を消化するための消化装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a digester for digesting organic substances including a substance that is hardly biodegradable.

【0002】[0002]

【従来の技術】農業や林業等において、稲わら、剪定枝
あるいは樹皮などの木質系物質が大量に廃棄されてい
る。これらの木質系の有機性廃棄物は生物難分解性であ
るため、現在のところ大部分が焼却あるいは堆肥化され
ているが、近年の環境意識の高まりとともにこれらの木
質系物質等の生物難分解性物質から効率的にエネルギー
を回収することが望まれている。
2. Description of the Related Art In agriculture, forestry, and the like, a large amount of woody substances such as rice straw, pruned branches, and bark are discarded. These woody organic wastes are hardly biodegradable, so most of them are incinerated or composted at present. However, with the increasing environmental awareness in recent years, these woody materials are hardly biodegradable. There is a demand for efficient recovery of energy from volatile substances.

【0003】有機性廃棄物からの効率的なエネルギー回
収法としては、有機性廃棄物を嫌気性条件下でメタン発
酵し可燃性ガスであるメタンガスを回収する消化処理法
が知られており、従来より、汚泥や生ごみ等の有機性廃
棄物からエネルギーがメタンガスとして効率的に回収さ
れている。
As an efficient energy recovery method from organic waste, a digestion treatment method in which methane fermentation of organic waste under anaerobic conditions to recover methane gas as a combustible gas is known. Energy is more efficiently recovered as methane gas from organic waste such as sludge and garbage.

【0004】このメタン発酵は、メタン発酵槽内温度が
38℃前後に保たれる中温発酵と、55℃前後に保たれ
る高温発酵とに大別され、メタン発酵槽の容量は、一般
的に、中温発酵では投入される有機物量の30日分以
上、高温発酵では15日分以上とすることが多く、比較
的大きな装置が必要となる。これは、一般的な酸生成菌
と比較してメタン生成菌の増殖速度が遅く、良好にメタ
ン発酵を行うためには非常に長い滞留時間を確保する必
要があるからである。
[0004] The methane fermentation is roughly classified into a medium-temperature fermentation in which the temperature in the methane fermentation tank is maintained at around 38 ° C and a high-temperature fermentation in which the temperature in the methane fermentation tank is maintained at around 55 ° C. For medium-temperature fermentation, the amount of organic substances to be fed is often 30 days or more, and for high-temperature fermentation, it is often 15 days or more, and a relatively large apparatus is required. This is because the growth rate of the methanogen is slower than that of a general acid-producing bacterium, and it is necessary to secure an extremely long residence time in order to perform methane fermentation satisfactorily.

【0005】そこで、近年になって、メタン発酵を効率
よく行ってメタン発酵槽の容積あたりの処理量を増加す
ることができる消化装置として、メタン発酵槽内にガラ
ス繊維担体を設け、この担体にメタン生成菌を付着させ
てメタン発酵を行う消化装置が開発されている。
Therefore, in recent years, a glass fiber carrier is provided in a methane fermentation tank as a digester capable of efficiently performing methane fermentation and increasing the throughput per volume of the methane fermentation tank. Digestion devices that perform methane fermentation by attaching methanogens have been developed.

【0006】[0006]

【発明が解決しようとする課題】しかし、上述のような
消化装置に汚泥や生ごみ等とともに木質系物質のような
生物難分解性物質を投入しても、例えば、木質系物質の
主成分であるセルロースやヘミセルロースの消化速度は
生ごみ等の有機性廃棄物と比べて非常に遅く、特に比較
的大きめの木質系物質等はほとんど消化されずに消化汚
泥とともに未消化のまま消化装置から排出されてしまう
という問題があった。
However, even when sludge, garbage, and the like and a biorefractory substance such as a wood-based substance are put into the digester as described above, for example, the main component of the wood-based substance is The digestion rate of certain cellulose and hemicellulose is much slower than organic waste such as garbage, and especially relatively large woody substances are hardly digested and are discharged from the digester as undigested with digested sludge. There was a problem that would.

【0007】本発明は、上記課題に鑑みてなされたもの
であり、生物難分解性物質を含む有機物質を確実に消化
可能であるとともに高い処理能力を備える消化装置を提
供することを目的とする。
SUMMARY OF THE INVENTION The present invention has been made in view of the above problems, and has as its object to provide a digester capable of reliably digesting an organic substance containing a biodegradable substance and having a high processing capability. .

【0008】[0008]

【課題を解決するための手段】本発明に係る消化装置
は、有機物質を嫌気性消化して消化汚泥にする消化装置
であって、汚泥含有液が収容される槽と、生物難分解性
物質を含む有機物質を槽内に導入する被処理物導入口
と、消化汚泥を槽内から排出する消化汚泥排出口と、被
処理物導入口と消化汚泥排出口との間で槽内の汚泥含有
液を区画するように設置され、所定の大きさよりも小さ
い物質のみを通過させる濾過手段とを備えることを特徴
とする。
A digestion apparatus according to the present invention is an digestion apparatus for anaerobically digesting organic substances into digested sludge, comprising a tank containing a sludge-containing liquid, and a biodegradable substance. Of sludge in the tank between the inlet for introducing the organic substance containing methane into the tank, the outlet for digesting sludge discharging the digested sludge from the tank, and the inlet for introducing the sludge and the outlet for digesting sludge. A filter installed to partition the liquid and allowing only a substance smaller than a predetermined size to pass therethrough.

【0009】本発明の消化装置によれば、所定の大きさ
以上で消化に時間のかかる生物難分解性物質等の有機物
質は濾過手段を通過することなく被処理物導入口側の汚
泥含有液中に保持され、十分消化されて所定の大きさよ
り小さくなるまで消化汚泥排出口側に移動しない。これ
によって、消化汚泥排出口から消化汚泥を排出する際に
所定の大きさ以上の生物難分解性物質等の有機物質が未
消化のまま消化汚泥とともに排出されることがない。
According to the digester of the present invention, the organic substance such as a biorefractory substance which is longer than a predetermined size and takes a long time for digestion does not pass through the filtration means without passing through the filtration means. It is retained inside and does not move to the digested sludge outlet side until it is sufficiently digested and smaller than a predetermined size. Thus, when the digested sludge is discharged from the digested sludge outlet, an organic substance such as a biorefractory substance having a predetermined size or more is not discharged together with the digested sludge without being digested.

【0010】また、生物難分解性物質は消化が進むにつ
れて比表面積が増加し消化菌の担体としての機能を発揮
するので、汚泥含有液中で有機物質と消化菌との接触効
率が向上して有機物質の消化速度が向上される。
[0010] In addition, since the biorefractory substance increases in specific surface area as digestion progresses and functions as a carrier for digestive bacteria, the efficiency of contact between organic substances and digestive bacteria in the sludge-containing liquid is improved. The digestion rate of organic substances is improved.

【0011】ここで、消化汚泥排出口側から当該濾過手
段を介して被処理物導入口側へ汚泥含有液を送出し、槽
内を攪拌する攪拌手段を備えることが好ましい。
Here, it is preferable to provide a stirring means for sending out the sludge-containing liquid from the digested sludge discharge port side to the treatment object introduction port side through the filtration means and stirring the inside of the tank.

【0012】この攪拌手段によって濾過手段に消化汚泥
排出口側から被処理物導入口側へ向かう流れが形成さ
れ、消化の十分でない生物難分解性物質等の有機物質が
この流れにより濾過手段から離脱させられるので、濾過
手段の全面的な閉塞が防止される。また、槽内の汚泥含
有液が攪拌されて汚泥濃度が均一化されるので、消化が
さらに効率よく行われる。
[0012] By this stirring means, a flow is formed in the filtration means from the digested sludge discharge port side to the treatment object introduction port side, and organic substances such as biorefractory substances which are not sufficiently digested are separated from the filtration means by this flow. As a result, the filter is prevented from being completely blocked. In addition, since the sludge-containing liquid in the tank is stirred to make the sludge concentration uniform, digestion is performed more efficiently.

【0013】[0013]

【発明の実施の形態】以下、添付図面を参照しながら、
本発明に係る消化装置の好適な実施形態について詳細に
説明する。なお、図面の説明において、同一または相当
要素には同一の符号を付し、重複する説明は省略する。
BRIEF DESCRIPTION OF THE DRAWINGS FIG.
A preferred embodiment of the digestion apparatus according to the present invention will be described in detail. In the description of the drawings, the same or corresponding elements will be denoted by the same reference characters, without redundant description.

【0014】図1は、第1実施形態の消化装置100を
示す断面模式図である。本実施形態の消化装置100
は、汚泥含有液を収容する槽1と、槽1内の汚泥含有液
を攪拌する攪拌装置(攪拌手段)15と、槽1内に水平
に設置されたスクリーン(濾過手段)5とを備える。
FIG. 1 is a schematic sectional view showing a digestion apparatus 100 according to a first embodiment. Digestion apparatus 100 of the present embodiment
Comprises a tank 1 for storing the sludge-containing liquid, a stirrer (stirring means) 15 for stirring the sludge-containing liquid in the tank 1, and a screen (filtering means) 5 installed horizontally in the tank 1.

【0015】槽1は、下側に突出する円錐状の底1a
と、円板でその外周に下向きのスカート部を備える天井
1cと、これら底1aおよび天井1cを連結する円筒状
の周壁1bとを備えている。そして、天井1cには、有
機物質を導入する被処理物導入口3および消化により生
じるメタン等のガスを排出するメタン排出口4を備える
とともに、底1aの円錐の下端には有機物質の消化によ
り生成する消化汚泥等を排出する消化汚泥排出口2を備
えている。
The tank 1 has a conical bottom 1a projecting downward.
And a ceiling 1c having a disk and having a downward skirt portion on the outer periphery thereof, and a cylindrical peripheral wall 1b connecting the bottom 1a and the ceiling 1c. The ceiling 1c is provided with an inlet 3 for introducing an organic substance and a methane outlet 4 for discharging gas such as methane generated by digestion. A digested sludge discharge port 2 for discharging generated digested sludge and the like is provided.

【0016】スクリーン5は、所定の目幅を有しその目
幅より小さい物質を選択的に透過させる網であり、槽1
の底1aと周壁1bとの境界部分に槽1内の汚泥含有液
を被処理物導入口3側と消化汚泥排出口2側とに区画す
るように水平設置されている。なお、このスクリーン5
の目幅の大きさは、投入する木質系物質等の有機物質の
大きさ等に基づいて設定されるが、消化装置100の後
段での消化汚泥の移送を容易にするため20mm以下と
することが好ましい。
The screen 5 is a net having a predetermined mesh width and selectively transmitting a substance smaller than the mesh width.
The sludge-containing liquid in the tank 1 is horizontally installed at the boundary between the bottom 1a and the peripheral wall 1b so as to partition the liquid into the treatment object introduction port 3 and the digestion sludge discharge port 2. This screen 5
The size of the mesh width is set based on the size of an organic substance such as a wood-based substance to be charged, etc., but should be 20 mm or less in order to facilitate the transfer of digested sludge in the subsequent stage of the digester 100. Is preferred.

【0017】攪拌装置15は、槽1内の汚泥含有液を攪
拌するものであり、天井1c側に軸支されて下方に延在
するとともにスクリーン5を貫通する回転軸12と、こ
の回転軸12の上下方向に互いに離間して設置され、汚
泥含有液に浸漬する複数の攪拌翼13a,13b,13
cと、天井1cの上に設置され回転軸12を回転させる
駆動装置11とを備えている。下段の攪拌翼13aはス
クリーン5と消化汚泥排出口2との間に位置し、消化汚
泥排出口2側の汚泥含有液をかきあげてスクリーン5の
中心近傍およびその周辺を透過させ、中段および上段の
攪拌翼13b,13cは周壁1bの中心軸近傍およびそ
の周辺の汚泥含有液を上方にかきあげるものである。
The agitating device 15 is for agitating the sludge-containing liquid in the tank 1. The agitating device 15 is rotatably supported by the ceiling 1 c side, extends downward, and penetrates through the screen 5. A plurality of agitating blades 13a, 13b, 13 which are installed vertically apart from each other and immersed in a sludge-containing liquid.
c, and a driving device 11 installed on the ceiling 1c to rotate the rotating shaft 12. The lower agitating blade 13a is located between the screen 5 and the digested sludge discharge port 2, and lifts up the sludge-containing liquid on the digested sludge discharge port 2 side to pass through the vicinity of the center of the screen 5 and the periphery thereof. The agitating blades 13b, 13c are used to lift up the sludge-containing liquid in the vicinity of the central axis of the peripheral wall 1b and in the vicinity thereof.

【0018】つぎに、第1実施形態の消化装置100の
作用について述べる。
Next, the operation of the digester 100 according to the first embodiment will be described.

【0019】まず、消化装置100の槽1内に酸生成菌
およびメタン発酵菌等の消化菌を含む汚泥含有水を仕込
んで消化可能な状態とする。つぎに、被処理物導入口3
から、有機物質として、稲わら、剪定枝、樹皮等の木質
系物質および生ごみや汚泥等を槽1内に投入する。そし
て、攪拌装置15の駆動装置11を駆動して攪拌翼13
a,13b,13cによって有機物質を含む汚泥含有液
を攪拌し、スクリーン5上での堆積を防止しつつ有機物
質の消化を行う一方、消化により生成する消化汚泥を適
宜消化汚泥排出口2から排出する。
First, sludge-containing water containing digestive bacteria such as acid-producing bacteria and methane-fermenting bacteria is charged into the tank 1 of the digester 100 so as to be in a digestible state. Next, the processing object inlet 3
Then, woody materials such as rice straw, pruned branches, bark, and the like, as well as garbage and sludge, are charged into the tank 1 as organic substances. Then, the driving device 11 of the stirring device 15 is driven to drive the stirring blades 13.
The sludge-containing liquid containing an organic substance is stirred by a, 13b, and 13c to digest the organic substance while preventing deposition on the screen 5, while appropriately discharging the digested sludge generated by the digestion from the digested sludge discharge port 2. I do.

【0020】このとき、スクリーン5の目幅よりも小さ
く、汚泥中の酸生成菌やメタン発酵菌等によって容易に
消化される有機物質はスクリーン5を通過して槽1内を
循環しつつさらに消化されて消化汚泥となる。
At this time, organic substances smaller than the mesh width of the screen 5 and easily digested by acid-producing bacteria or methane-fermenting bacteria in the sludge pass through the screen 5 and circulate in the tank 1 to be further digested. It becomes digested sludge.

【0021】一方、スクリーン5の目幅以上の大きさを
有し消化に長時間を要する木質系物質等の有機物質は被
処理物導入口3側の汚泥含有液中に保持され、攪拌され
つつ消化が行われる。これによって、消化汚泥排出口2
から消化汚泥が抜き出される際に、このスクリーン5の
目幅以上の木質系物質等の有機物質が未消化のまま消化
汚泥とともに排出されることが防止されている。
On the other hand, an organic substance such as a wood-based substance having a size larger than the mesh width of the screen 5 and requiring a long time for digestion is retained in the sludge-containing liquid on the side of the treatment object introduction port 3 and stirred. Digestion takes place. As a result, the digestion sludge outlet 2
When the digested sludge is extracted from the mash, organic substances such as wood-based substances and the like that are larger than the mesh width of the screen 5 are prevented from being discharged together with the digested sludge without being digested.

【0022】このように被処理物導入口3側の汚泥含有
液中に保持されている木質系物質は、消化が進むにつれ
て表面の凸凹が多くなって比表面積が増加し消化菌の担
体としての機能を発揮して消化菌の濃度が増加するの
で、汚泥含有液中で有機物質とメタン菌等との接触効率
が向上して有機物質の消化速度が向上され、木質系物質
を含む有機性物質が好適に消化処理される。特に、高温
での発酵にあっては、木質系物質が未消化のまま排出さ
れることが防止されるのに加えて、この木質系物質が、
特許2708087号公報に開示された消化装置におい
て槽内に設置されるガラス繊維担体と同様の作用効果を
一層発揮し、小さな槽の容量で高負荷処理が可能になる
とともに、木質系物質自身の分解速度も早くされる。
As described above, the woody substance held in the sludge-containing liquid on the inlet side of the material to be treated 3 has more irregularities on the surface as the digestion proceeds, and the specific surface area increases. It functions to increase the concentration of digestive bacteria, so the efficiency of contact between organic substances and methane bacteria in the sludge-containing liquid is improved, and the digestion rate of organic substances is increased, and organic substances including wood-based substances Is suitably digested. In particular, in the case of fermentation at high temperatures, in addition to preventing the emission of undigested woody substances, in addition to this woody substance,
In the digestion apparatus disclosed in Japanese Patent No. 2708087, the same effect as the glass fiber carrier installed in the tank is further exhibited, a high load treatment can be performed with a small tank capacity, and decomposition of the woody substance itself is performed. Speed is also increased.

【0023】そして、スクリーン5の目幅以上の木質系
物質等の有機物質が被処理物導入口3側で十分消化され
てスクリーン5の目幅よりも小さくなると、スクリーン
5を透過して自由に槽1内を循環しつつさらに消化され
るようになり、消化汚泥となって消化汚泥排出口2から
抜き出される。
When the organic substance such as a woody substance or the like having a width equal to or larger than the mesh width of the screen 5 is sufficiently digested at the treatment object inlet 3 side and becomes smaller than the mesh width of the screen 5, the organic material penetrates the screen 5 and freely passes through the screen 5. It is further digested while circulating in the tank 1, and is extracted as digested sludge from the digested sludge outlet 2.

【0024】このとき、排出に伴って槽1内の液が被処
理物導入口3側から消化汚泥排出口2側に向かって流れ
て被処理物導入口3側の未分解の木質系物質がスクリー
ン5の表面に堆積しようとするが、スクリーンの中心に
攪拌装置15によって上向流が形成されて未分解の木質
系物質がスクリーン5の表面から離脱させられるので、
スクリーンの全面的な閉塞が防止されている。また、こ
れにより槽1内の汚泥含有液の汚泥濃度が均一化される
ので、消化がさらに効率よく行われる。
At this time, the liquid in the tank 1 flows from the inlet 3 to the digested sludge outlet 2 along with the discharge, and the undecomposed woody substance at the inlet 3 is removed. Although an attempt is made to accumulate on the surface of the screen 5, an upward flow is formed at the center of the screen by the stirrer 15, and undecomposed wood-based material is separated from the surface of the screen 5.
The entire blockage of the screen is prevented. In addition, since the sludge concentration of the sludge-containing liquid in the tank 1 is made uniform, digestion is performed more efficiently.

【0025】このように、本実施形態の消化装置100
は、スクリーン5を設置することにより、所定の大きさ
以上で消化に時間のかかる木質系物質等の有機物質が被
処理物導入口3側の汚泥含有液中に保持され消化汚泥排
出口2から未消化のまま消化汚泥とともに排出されるこ
とが防止されているとともに、木質系物質が消化につれ
て消化菌の担体とされるため有機物質の消化速度が向上
される。したがって、木質系物質を含む有機性物質を確
実に消化可能であるとともに高い処理能力を備える消化
装置100を提供することが可能となっている。
As described above, the digestion apparatus 100 of the present embodiment is
By installing the screen 5, an organic substance such as a wood-based substance, which is longer than a predetermined size and takes a long time to digest, is retained in the sludge-containing liquid on the side of the treatment object introduction port 3, and is discharged from the digested sludge discharge port 2. It is prevented from being discharged together with digested sludge without being digested, and the digestion rate of organic substances is improved because the wood-based substance is used as a carrier for digestive bacteria as it is digested. Therefore, it is possible to provide the digestion apparatus 100 capable of reliably digesting organic substances including wood-based substances and having high processing capability.

【0026】つぎに、第2実施形態の消化装置200に
ついて図2を参照して説明する。本実施形態の消化装置
200が第1実施形態の消化装置100と違う点は、攪
拌翼13a〜13cを備えた攪拌装置15に代えて、消
化汚泥排出口2から排出された汚泥含有液を槽1内に戻
し、消化汚泥排出口2側からスクリーン5に向けて送出
して汚泥含有液を攪拌する攪拌装置(攪拌手段)25を
備えている点である。この攪拌装置25は、詳しくは、
消化汚泥排出口2側の汚泥含有液をラインL1を介して
吸引するとともにラインL2を介して再び槽1内の消化
汚泥排出口2側に対して送出するポンプ21と、送出さ
れる汚泥含有液を槽1内の消化汚泥排出口2側でスクリ
ーン5に向かって均一に吐出させる散水ノズル20とを
備えている。
Next, a digestion apparatus 200 according to a second embodiment will be described with reference to FIG. The digester 200 of the present embodiment is different from the digester 100 of the first embodiment in that the sludge-containing liquid discharged from the digested sludge discharge port 2 is replaced with a stirrer 15 having stirring blades 13a to 13c. 1 and is provided with a stirring device (stirring means) 25 for stirring the sludge-containing liquid by sending it toward the screen 5 from the digested sludge discharge port 2 side. This stirrer 25 is described in detail
A pump 21 for sucking the sludge-containing liquid on the digested sludge discharge port 2 side through the line L1 and sending it again to the digested sludge discharge port 2 side in the tank 1 via the line L2; And a sprinkling nozzle 20 for uniformly discharging the water toward the screen 5 on the digested sludge discharge port 2 side in the tank 1.

【0027】そして、このように構成しても第1実施形
態と同様な効果を得ることができるというのは言うまで
もない。
It is needless to say that the same effect as in the first embodiment can be obtained even with this configuration.

【0028】なお、本発明に係る消化装置は、上記実施
形態に限定されるものではなく、種々の変形態様をとる
ことが可能である。
The digestion apparatus according to the present invention is not limited to the above-described embodiment, but can take various modifications.

【0029】例えば、上記実施形態では、濾過手段とし
て網であるスクリーン5を用いているがこれに限られ
ず、例えば、格子、パンチングプレート等でも構わな
い。
For example, in the above embodiment, the screen 5 which is a net is used as the filtering means. However, the present invention is not limited to this. For example, a lattice, a punching plate, or the like may be used.

【0030】また、上記実施形態では、スクリーン5を
水平に備えているがこれに限られず、例えば、垂直等に
設置しても構わない。この場合は、例えば、スクリーン
によって区画される槽内の一方側に被処理物導入口を設
け、他方側に消化汚泥排出口を設ければよい。
Further, in the above embodiment, the screen 5 is provided horizontally, but is not limited to this. For example, the screen 5 may be installed vertically. In this case, for example, a treatment object introduction port may be provided on one side of the tank partitioned by the screen, and a digested sludge discharge port may be provided on the other side.

【0031】また、上記実施形態では、スクリーン5に
対して、攪拌装置15,25によって消化汚泥排出口2
側から被処理物導入口3側に向かう流れを形成している
がこれに限られず、スクリーン5の濾過面積が充分広い
場合等でスクリーン5の閉塞の可能性が低い場合はこれ
を備えなくても構わない。
In the above-described embodiment, the digested sludge outlet 2 is provided to the screen 5 by the stirring devices 15 and 25.
The flow is formed from the side to the treatment object inlet 3 side, but is not limited to this. If the filtration area of the screen 5 is sufficiently large and the likelihood of blocking of the screen 5 is low, this is not provided. No problem.

【0032】また、上記実施形態では、生物難分解性物
質として、稲わら等の木質系物質を採用しているが、こ
れに限られず、紙等他の生物難分解性物質でも構わな
い。
In the above embodiment, a wood-based substance such as rice straw is used as the biodegradable substance. However, the present invention is not limited to this, and other biodegradable substances such as paper may be used.

【0033】[0033]

【発明の効果】以上説明したように、本発明に係る消化
装置は、濾過手段を設置し、所定の大きさ以上で消化に
時間のかかる生物難分解性物質等の有機物質を濾過手段
によって被処理物導入口側の汚泥含有液中に保持し、十
分に消化させて所定の大きさより小さくなるまで消化汚
泥排出口側に移動させない。これによって、消化汚泥排
出口から消化汚泥を排出する際に所定の大きさ以上の生
物難分解性物質等の有機物質が未消化のまま消化汚泥と
ともに排出されない。また、生物難分解性物質は消化が
進むにつれて比表面積が増加し消化菌の担体としての機
能を発揮するので、汚泥含有液中で有機物質と消化菌と
の接触効率が向上して有機物質の消化速度が向上され
る。
As described above, the digestion apparatus according to the present invention is provided with the filtering means, and the organic substance such as the biologically hardly decomposable substance which is longer than a predetermined size and which is difficult to digest is covered by the filtering means. It is kept in the sludge-containing liquid on the treated material inlet side, and is not moved to the digested sludge outlet side until it is sufficiently digested and smaller than a predetermined size. Accordingly, when the digested sludge is discharged from the digested sludge discharge port, organic substances such as a biorefractory substance having a predetermined size or more are not discharged without digestion together with the digested sludge. In addition, since the biodegradable substance increases in specific surface area as digestion progresses and functions as a carrier for digestive bacteria, the contact efficiency between the organic substance and digestive bacteria in the sludge-containing liquid is improved, and Digestion speed is improved.

【0034】これらによって、生物難分解性物質を含む
有機性物質を確実に消化可能であるとともに高い処理能
力を備える消化装置を提供することが可能とされる。
[0034] Thus, it is possible to provide a digester capable of surely digesting organic substances including biodegradable substances and having a high processing ability.

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

【図1】本発明の消化装置の第1実施形態を示す断面模
式図である。
FIG. 1 is a schematic sectional view showing a first embodiment of a digestion apparatus of the present invention.

【図2】本発明の消化装置の第2実施形態を示す断面模
式図である。
FIG. 2 is a schematic sectional view showing a second embodiment of the digestion apparatus of the present invention.

【符号の説明】[Explanation of symbols]

1…槽、2…消化汚泥排出口、3…被処理物導入口、5
…スクリーン(濾過手段)、15,25…攪拌装置(攪
拌手段)、100,200…消化装置。
1 ... tank, 2 ... digestion sludge outlet, 3 ... inlet for treated material, 5
... screen (filtration means), 15, 25 ... stirring device (stirring device), 100, 200 ... digestion device.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 有機物質を嫌気性消化して消化汚泥にす
る消化装置であって、 汚泥含有液が収容される槽と、 生物難分解性物質を含む有機物質を前記槽内に導入する
被処理物導入口と、 前記消化汚泥を前記槽内から排出する消化汚泥排出口
と、 前記被処理物導入口と前記消化汚泥排出口との間で前記
槽内の汚泥含有液を区画するように設置され、所定の大
きさよりも小さい物質のみを通過させる濾過手段と、 を備えることを特徴とする、消化装置。
1. A digestion apparatus for anaerobically digesting an organic substance into digested sludge, comprising: a tank for storing a sludge-containing liquid; and a container for introducing an organic substance containing a biodegradable substance into the tank. A treated material inlet, a digested sludge outlet for discharging the digested sludge from the inside of the tank, and a sludge-containing liquid in the tank between the treated object inlet and the digested sludge outlet. A filter installed to allow only a substance smaller than a predetermined size to pass therethrough.
【請求項2】 前記消化汚泥排出口側から当該濾過手段
を介して前記被処理物導入口側へ前記汚泥含有液を送出
し、前記槽内を攪拌する攪拌手段を備えることを特徴と
する、請求項1に記載の消化装置。
2. A stirring means for sending out the sludge-containing liquid from the digested sludge discharge port side to the treatment object introduction port side via the filtration means and stirring the inside of the tank, The digestion device according to claim 1.
JP2001069012A 2001-03-12 2001-03-12 Digester Pending JP2002263699A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001069012A JP2002263699A (en) 2001-03-12 2001-03-12 Digester

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001069012A JP2002263699A (en) 2001-03-12 2001-03-12 Digester

Publications (1)

Publication Number Publication Date
JP2002263699A true JP2002263699A (en) 2002-09-17

Family

ID=18927109

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2001069012A Pending JP2002263699A (en) 2001-03-12 2001-03-12 Digester

Country Status (1)

Country Link
JP (1) JP2002263699A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009028625A (en) * 2007-07-26 2009-02-12 Kurimoto Ltd Methane fermentation apparatus and method
WO2011013655A1 (en) * 2009-07-31 2011-02-03 Kobayashi Yoshio Water-withdrawal type methane fermentation method
CN102115256A (en) * 2010-12-14 2011-07-06 华中科技大学 Anaerobic treatment method for landfill leachate
JP2012183481A (en) * 2011-03-04 2012-09-27 Takuma Co Ltd Device for hydrogen/methane fermentation

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009028625A (en) * 2007-07-26 2009-02-12 Kurimoto Ltd Methane fermentation apparatus and method
WO2011013655A1 (en) * 2009-07-31 2011-02-03 Kobayashi Yoshio Water-withdrawal type methane fermentation method
JP4768881B2 (en) * 2009-07-31 2011-09-07 義雄 小林 Dehydrated methane fermentation
JPWO2011013655A1 (en) * 2009-07-31 2013-01-07 小林 義雄 Dehydrated methane fermentation
CN102115256A (en) * 2010-12-14 2011-07-06 华中科技大学 Anaerobic treatment method for landfill leachate
CN102115256B (en) * 2010-12-14 2012-05-09 华中科技大学 Anaerobic treatment method for landfill leachate
JP2012183481A (en) * 2011-03-04 2012-09-27 Takuma Co Ltd Device for hydrogen/methane fermentation

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