JP3764812B2 - 厨 芥 Wastewater treatment equipment - Google Patents

厨 芥 Wastewater treatment equipment Download PDF

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Publication number
JP3764812B2
JP3764812B2 JP35511497A JP35511497A JP3764812B2 JP 3764812 B2 JP3764812 B2 JP 3764812B2 JP 35511497 A JP35511497 A JP 35511497A JP 35511497 A JP35511497 A JP 35511497A JP 3764812 B2 JP3764812 B2 JP 3764812B2
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Prior art keywords
tank
wastewater
aerobic
solids
treatment
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JPH11179389A (en
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俊男 山根
秀磨 古村
泰祐 能勢
知 輿水
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Taisei Corp
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Taisei Corp
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

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Description

【0001】
【発明の属する技術分野】
本発明は、食品加工工場、レストラン、住宅等においてディスポーザ等の厨芥粉砕機により発生する厨芥排水の処理装置に関する。
【0002】
【従来の技術】
近年、厨房から発生する生ごみ(以下、厨芥と称する)を粉砕処理するディスポーザが普及している。
【0003】
ディスポーザは、厨芥を粉砕しながら厨房排水とともに排出する電化製品で、厨芥の保管・収集・搬送などの日常の煩わしさを一気に解消できるものとして消費者のあいだで好評を得ている。しかし、環境に与えるインパクトや既存の排水処理設備の処理能力を上回る負荷の増大などの点から、厨芥排水を垂れ流しにするディスポーザの単独使用は自粛しているのが現状である。
【0004】
このため、厨芥排水を発生点で処理できる方法や装置の開発が盛んに行われている。
【0005】
一例として、特開昭58−20291号公報には、沈殿作用とばっ気作用を兼ね備えた処理装置が開示されているが、これによれば、有機固形物のみを処理対象として溶解性汚濁物質の処理は考慮されていない。
【0006】
【発明が解決しようとする課題】
しかしながら本発明者等の知見によれば、有機性固形物含有排水には処理対象とすべき溶解性汚濁物質も含有するのが一般的であるから、上記公報の如く固形物だけを処理対象とするのは実情にそぐわず、開示された排水処理装置は、厨芥排水の処理には適さない。
【0007】
また、この公報には、沈殿作用により固形物を効果的に除去する点が記載されているが、厨芥中の有機性固形物には繊維のような難分解性物質を含む場合が多く、沈殿作用を利用した場合、これら難分解性物質が蓄積してしまい、運転中に汚泥の抜き出し作業が必要になるという問題があった。
【0008】
そこで、本出願人は、分離装置によって厨芥排水を固形物濃縮排水と分離排水に分離して、固形物濃縮排水を処理する好気性消化槽と、分離排水を処理する接触ばっ気槽からなる構成にて、各槽の容量の適正化をはかりつつ消化槽に攪拌手段を設けることにより、槽内における汚泥の増加・蓄積を阻止することができる処理装置などを検討してきた。
【0009】
ところで、厨芥には、例えば野菜に付着した土砂、鶏卵の殻、鳥獣や魚の骨、貝殻など、生物処理で分解困難な無機性固形物が絶えず混入している。この無機性固形物は、比重の大きさ、粒径の大きさゆえに好気性消化槽の槽内において、十分に攪拌しようとすれば過大な動力が必要なる。
【0010】
一方、好気性消化槽で有機性固形物の分解にともなって発生する汚泥は、有機物を資化した微生物が主成分であり、その比重は水に近く、また攪拌効果によって微生物フロックの解体も行うために粒径が小さくなることから、比較的小さな攪拌動力で槽底部に沈殿させず槽内液を混合できる。
【0011】
従って、余剰汚泥の抜き出しのみを不要とする場合、攪拌動力は小さくて済むが、余剰汚泥に加えて無機性固形物の抜き出しをも不要にする場合、無機性固形物を沈殿させないための過大な攪拌動力が必要になる。
【0012】
ここで、厨芥排水は、一部の特殊な食品排水を除いて、無機性固形物の厨芥排水における含有量が少ない場合が一般的であることから、無機性固形物に対する過大な攪拌動力は採算上無視される可能性が大きい。このような場合、見掛け上は少ない動力で、厨芥排水の圧倒的主成分である有機性固形物を処理し、余剰汚泥の抜き出し不要は達成できるものの、実際には、槽底部に無機性固形物が少量づつ蓄積していく。
【0013】
また、好気性消化槽にはその底部に散気装置が配置されており、無機性固形物が槽底部に蓄積していくと、長期的には散気装置の開孔部を詰まらせ散気装置の寿命を著しく早める結果となる。
【0014】
これらの点を回避するには、無機性固形物の抜き出し作業を定期的に実行すればよいが、大容量の好気性消化槽から槽容量に比して小容量の無機物を取り出すという作業は経費・手間とも無駄が多い。
【0015】
本発明はこのような実情に鑑みてなされたもので使用する上で、厨芥排水中に含まれる有機性固形物と溶解性汚濁物質を除去する前に、生物処理が困難な無機性固形物を系外に除いておくことで、過大な攪拌動力を必要とせず、かつ、排水中に含まれる難分解性物質や無機性固形物による悪影響が及ぶことがなく、しかも微生物由来の大量の余剰汚泥の抜き出し作業を不要とし得る、厨芥排水の処理装置を提供することを目的とする。
【0017】
【課題を解決するための手段】
上記の目的を達成するため、本発明の厨芥排水の処理装置は、図2に例示するように、無機性固形物を沈降分離する沈砂槽21と、無機性固形物を除いた厨芥排水211を処理する好気性消化槽23と、この好気性消化槽23の内部液を、濃縮された有機性固形物及び汚泥と、分離排水221に分離する沈殿槽22と、分離排水221をさらに好気的生物処理する排水処理槽(接触ばっ気槽)24を備え、その好気的生物処理を行う排水処理槽24に、前記好気性消化槽23内の処理水231を導くように構成さているとともに、好気性消化槽23に槽内の処理水を攪拌する手段(散気装置232)を設けていることによって特徴づけられる。
<作用>
本発明の処理装置によれば、厨芥排水中に含まれる無機性固形物を沈砂槽21で系外に除去するので、無機性固形物を拡散するための過大な攪拌動力を必要とせず、さらに無機性固形物を専用の沈砂槽21に貯留しているので、その抜き出し作業を、大容量の好気性消化槽から無機性固形物を抜き出す場合に比して、簡単かつ低コストで行うことができる。
【0018】
しかも、好気性消化槽23において有機性固形物の分解に要する時間よりも水理学的滞留時間を大きく設定することが可能となり、これにより流入排水に含まれる有機性固形物を十分に分解できる。また、好気性消化槽23に攪拌手段を設けているので、槽内の処理水を常時攪拌することができ、好気性微生物による固形物の分解作用を高めることができる。
【0019】
さらに、攪拌状態の槽内処理水231を流出させることによって槽内の汚泥濃度を常に一定の平衡状態に維持することが可能となり、その結果として、好気性消化槽23内で汚泥の増加・蓄積が発生することがなくなる。
【0020】
なお、発明の処理装置において、沈砂槽に、空気を槽内に供給する散気装置を設けておけば、内容物の腐敗・腐臭を防ぐことができてさらに好都合である。
【0021】
【発明の実施の形態】
本発明の実施の形態を、以下、図面に基づいて説明する。
【0022】
図1は厨芥排水の処理装置の実施の形態の構成を示すブロック図である。
この図1に示す処理装置1は、例えば下水道整備地域の戸建て住宅から発生する厨芥排水の処理に利用する装置で、沈砂槽11、沈殿槽12、好気性消化槽13及び接触ばっ気槽14によって主に構成されている。
【0023】
沈砂槽11は、厨芥排水から無機性固形物を沈殿分離して貯留する装置で、戸建て住宅の流し台で発生するディスポーザ排水(厨芥排水)と厨房排水をまとめて流すための排水管110が接続される。
【0024】
この沈砂槽11で無機性固形物を除いた厨芥排水111は沈殿槽12に流入する。
【0025】
沈殿槽12は、無機性固形物が除かれた厨芥排水111を、有機性固形物濃縮排水121と分離排水122とに分離する装置で、この沈殿槽12で分離された固形物は周囲の液体とともに好気性消化槽13に、固形物濃縮排水121としてエアリフトポンプ16によって移送される。
【0026】
好気性消化槽13は、槽底部に設けた散気装置132から噴出する空気によって槽内を好気的雰囲気に保持する装置で、好気性微生物の働きによって有機性固形物を主に分解する。また好気性消化槽13には、槽内の処理水を常時攪拌するための送液ポンプ15が設けられている。
【0027】
一方、沈殿槽12で分離された分離排水122は、接触ばっ気槽14に導かれる。この接触ばっ気槽14も好気性消化槽13と同様に、槽底部の散気装置142から噴出する空気によって槽内を好気的雰囲気に保持する構造で、溶解性汚濁物質を分解する。
【0028】
また、接触ばっ気槽14には、上記した分離排水122に加えて、好気性消化槽13からオーバーフローした流出水131が流入する。
【0029】
次に、図1に示す実施の形態の作用を述べる。
まず、排水管110を通じてディスポーザ排水と厨房排水が沈砂槽11に流入し、この沈砂槽11において沈殿分離作用によって、沈降性の大なる無機性固形物が除去され、この無機性固形物が除去された厨芥排水及び厨房排水111が沈殿槽12に導かれる。
【0030】
沈殿槽12で分離された固形物濃縮排水121がエアリフトポンプ16によって好気性消化槽13に移送され、ここで有機性固形物が好気性微生物の生物酸化によって分解される。
【0031】
なお、好気性消化槽13では、送液ポンプ15により槽内の固形物を常時攪拌しているので、好気性微生物による分解作用が効果的に行われ、固形物を十分に分解することができる。しかも攪拌状態の槽内処理水131を流出させることにより、好気性消化槽13内の汚泥濃度が常に一定の平衡状態に維持されるので、槽内で汚泥が増加することもなくなる。
【0032】
そして、好気性消化槽13内で、固形物が十分に分解された処理水131は、槽内への固形物濃縮排水121の流入時にオーバーフローによって槽外に流出する。この流出水131は接触ばっ気槽14に導かれる。
【0033】
一方、沈殿槽11で有機性固形物が除かれた分離排水122は接触ばっ気槽14内に流入し、槽内で好気性微生物の生物酸化により溶解性汚濁物質が分解され、その処理水141が、オーバーフローによって槽外に放流される。
【0034】
以上のように、図1に示す実施の形態では、沈砂槽11によって厨芥排水から沈降性の大なる無機性固形物を除去し、次に好気性消化槽13と接触ばっ気槽14によって、有機性固形物と溶解性汚濁物質をそれぞれ別々に処理するので、各処理槽の容量及び攪拌動力の適正化をはかることができる。
【0035】
しかも、無機性固形物を専用の沈砂槽11に貯留しているので、大容量の好気性消化槽から無機性固形物を抜き出すよりも経費が少なくて済み、また作業性も良くなる。
【0036】
なお、図1に示す実施の形態の構成に加えて、沈砂槽11に、槽内に空気を供給する散気装置を設けておけば、内容物の腐敗・腐臭を防ぐことができる。
【0037】
ここで、図1に示す実施の形態では、好気性消化槽13及び接触ばっ気槽14をそれぞれ単一の槽としているが、本発明はこれに限られることなく、その各処理槽として複数の槽を接続したものを用いてもよい。
【0038】
また、好気性消化槽13及び接触ばっ気槽14の付帯手段としての散気装置、移流方式、放流方式、並びに攪拌手段等は、図1に示した構成のものに限られることなく、上述した内容と同様な作用を得ることのできる方式であれば、どのような方式を採用してもよい。
【0039】
図2は発明の実施の形態の構成を示すブロック図である。
この実施の形態の処理装置2は、集合住宅から発生する厨芥排水の処理に利用する装置で、主に沈砂槽21、沈殿槽22、好気性消化槽23及び接触ばっ気槽24によって構成されている。
【0040】
沈砂槽21は、厨芥排水から無機性固形物を沈殿分離し貯留する装置で、各住宅の流し台で発生するディスポーザ排水と厨房排水をまとめて流すための排水管210が接続される。
【0041】
この沈砂槽21で無機性固形物を除いた厨芥排水211は好気性消化槽23へ流入する。なお、沈砂槽21には適当な水深に散気装置212に設けてある。
【0042】
好気性消化槽23は、槽底部に設けた散気装置232から噴出する空気によって槽内を好気的雰囲気に保持する構造で、有機性固形物を主に分解する。この好気性消化槽23に設けた散気装置232は、槽内の処理水を常時攪拌するための攪拌動力も兼ねる。
【0043】
また、好気性消化槽23には、内部液を沈殿槽22と流通できる経路26が設けられている。
【0044】
沈殿槽22は、沈殿分離作用により処理水を、濃縮された有機性固形物及び汚泥と分離排水221に分離する槽で、槽底部が、好気性消化槽23への経路26に向けて傾斜する形状に加工されている。
【0045】
そして、好気性消化槽23内の処理水231は適当な水深から送液ポンプ25によって、接触ばっ気槽24へ移送される。
【0046】
一方、沈殿槽22で分離された分離排水221は、接触ばっ気槽24に導かれる。この接触ばっ気槽24も好気性消化槽23と同様に、槽底部に散気装置242から噴出する空気によって槽内を好気的雰囲気に保持する構造で、溶解性汚濁物質を分解する。
【0047】
また、沈殿槽22で濃縮された有機性固形物及び汚泥は、経路26を通じて好気性消化槽23に戻りさらに分解・攪拌を受ける。
【0048】
次に、図2に示す実施の形態の作用を述べる。
まず、排水管210を通じてディスポーザ排水と厨房排水が沈砂槽21に流入し、この沈砂槽21で沈殿分離作用によって、沈降性の大なる無機性固形物が除かれ、この無機性固形物が除去された厨芥排水及び厨房排水211が好気性消化槽23に導かれる。
【0049】
なお、好気性消化槽23では、攪拌動力を兼ねた散気装置232により槽内の固形物を常時攪拌しているので、好気性微生物による分解作用が効果的に行われ、固形物を十分に分解することができる。しかも攪拌状態の槽内処理水231を送液ポンプ25で流出させることにより、好気性消化槽23内の汚泥濃度が常に一定の平行状態に維持されるので、槽内で汚泥が増加することもなくなる。
【0050】
好気性消化槽23の内部液は、沈殿槽22において傾斜を利用した沈殿分離作用により、濃縮された有機性固形物及び汚泥と、分離排水221とに分離され、その濃縮された有機性固形物及び汚泥は、経路26を通じて好気性消化槽23に戻って、さらに攪拌・分解される。
【0051】
そして、好気性消化槽23の流出水231は接触ばっ気装置24に導かれ、また沈殿槽22で分解された分離排水221は、好気性消化槽23への流入水211の流入時にオーバーフローによって接触ばっ気槽24に移送される。
【0052】
接触ばっ気槽24では、好気性微生物の生物酸化により溶解性汚濁物質が分解され、その処理水241が、オーバーフローによって槽外に放流される。
【0053】
以上のように、図2に示す実施の形態においても、沈砂槽21によって厨芥排水の中に含まれる無機性固形物を系外に除去しているので、各処理槽の容量及び攪拌動力の適正化をはかることができる。しかも、無機性固形物を専用の沈砂槽21に貯留しているので、大容量の好気性消化槽から無機性固形物を抜き出すよりも経費が少なくて済み、また作業性も良くなる。
【0054】
ここで、図2に示す実施の形態では、好気性消化槽23及び接触ばっ気槽24をそれぞれ単一の槽としているが、本発明はこれに限られることなく、その各処理槽として複数の槽を接続したものを用いてもよい。
【0055】
また、好気性消化槽23及び接触ばっ気槽24の付帯手段としての散気装置、移流方式、放流方式、並びに攪拌手段等は、図2に示した構成のものに限られることなく、上述した内容と同様な作用を得ることのできる方式であれば、どのような方式を採用してもよい。
【0056】
【発明の効果】
以上説明したように、発明の厨芥排水の処理装置によれば、厨芥排水中に含まれる無機性固形物を系外へ除去し、有機性固形物と溶解性汚濁物質をそれぞれ個別に処理するので、各処理槽の容量及び攪拌動力の適正化をはかることができ、これにより処理装置の維持管理を簡単かつ安価に行うことができるとともに、装置全体をコンパクトにまとめることができる。
【0057】
また、消化槽内部に余剰汚泥が増加することなく、これにより槽内の汚泥濃度を一定の平衡状態に維持することができる。さらに、消化槽底部に無機性固形物がたまらないので付帯装置の故障を減らすことができる。
【図面の簡単な説明】
【図1】請求項1に記載の発明の実施の形態の構成を示すブロック図
【図2】請求項3に記載の発明の実施の形態の構成を示すブロック図
【符号の説明】
1 処理装置
11 沈砂槽
12 沈殿槽(分離装置)
13 好気性消化槽
14 接触ばっ気槽(排水処理槽)
15 送液ポンプ
16 エアリフトポンプ
110 排水管
111 無機性固形物を除いた厨芥排水
121 固形物濃縮排水
122 分離排水
131 好気性消化槽の処理水
132 散気装置
141 処理装置の処理水
142 散気装置
2 処理装置
21 沈砂槽
22 沈殿槽
23 好気性消化槽
24 接触ばっ気槽(排水処理槽)
25 送液ポンプ
26 経路
210 排水管
211 無機性固形物を除いた厨芥排水
212 散気装置
221 分離排水
231 好気性消化槽の処理水
232 散気装置
241 処理装置の処理水
242 散気装置
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a treatment device for waste water generated by a waste grinder such as a disposer in a food processing factory, a restaurant, a house, or the like.
[0002]
[Prior art]
2. Description of the Related Art In recent years, a disposer for pulverizing garbage generated from a kitchen (hereinafter referred to as cocoon) has become widespread.
[0003]
Disposers are electrical appliances that pulverize potatoes and discharge them together with kitchen wastewater, and have gained popularity among consumers as they can eliminate everyday troubles such as storage, collection, and transportation of potatoes. However, in view of the impact on the environment and the increase in load exceeding the capacity of existing wastewater treatment facilities, the current situation is that the use of a disposer for dredging dredged wastewater is self-sufficient.
[0004]
For this reason, development of the method and apparatus which can treat dredged wastewater at the generation | occurrence | production point is performed actively.
[0005]
As an example, Japanese Patent Application Laid-Open No. 58-20291 discloses a treatment apparatus having both a precipitation action and an aeration action. According to this, only organic solids are treated as a soluble pollutant. Processing is not considered.
[0006]
[Problems to be solved by the invention]
However, according to the knowledge of the present inventors, it is common for organic solid-containing wastewater to contain a soluble pollutant that should be treated, so only solids are treated as described above. It is not appropriate to do so, and the disclosed wastewater treatment device is not suitable for the treatment of dredged wastewater.
[0007]
In addition, this publication describes that solids are effectively removed by precipitation, but the organic solids in the soot often contain persistent substances such as fibers, When the action is used, these hardly decomposable substances accumulate, and there is a problem that it is necessary to extract sludge during operation.
[0008]
Therefore, the applicant of the present invention consists of an aerobic digester that separates dredged wastewater into solid concentrated wastewater and separated wastewater by a separation device and processes the solids concentrated wastewater, and a contact aeration tank that processes the separated wastewater. Therefore, a processing apparatus that can prevent increase and accumulation of sludge in the tank by providing a stirring means in the digestion tank while optimizing the capacity of each tank has been studied.
[0009]
By the way, the sardines are constantly mixed with inorganic solids that are difficult to decompose by biological treatment, such as earth and sand, chicken eggshells, birds and fish bones, and shells attached to vegetables. Since this inorganic solid has a large specific gravity and a large particle size, excessive power is required to sufficiently stir in the aerobic digester tank.
[0010]
On the other hand, sludge generated by the decomposition of organic solids in an aerobic digester is mainly composed of microorganisms that assimilate organic substances, the specific gravity is close to water, and microbial flocs are also disassembled by the stirring effect Therefore, since the particle size is reduced, the liquid in the tank can be mixed without being precipitated at the bottom of the tank with a relatively small stirring power.
[0011]
Therefore, if only the extraction of excess sludge is not required, the stirring power may be small, but if it is not necessary to extract the inorganic solid in addition to the excess sludge, it is excessive to prevent precipitation of the inorganic solid. Stirring power is required.
[0012]
Here, except for some special food wastewater, dredging wastewater is generally low in the amount of inorganic solids in dredging wastewater, so excessive stirring power for inorganic solids is profitable. There is a high possibility of being ignored. In such a case, it is possible to treat organic solids, which are the overwhelming main component of dredged wastewater, with no apparent power, and to eliminate the need to extract excess sludge. Will gradually accumulate.
[0013]
In addition, an aerobic digester is equipped with a diffuser at the bottom, and as inorganic solids accumulate at the bottom of the tank, it will clog the opening of the diffuser for a long time. This results in significantly shortening the life of the device.
[0014]
In order to avoid these points, the extraction work of inorganic solids may be carried out periodically, but the work of taking out a small amount of inorganic substance from a large volume aerobic digestion tank as compared with the tank capacity is costly. -There is a lot of waste.
[0015]
The present invention is made in view of such circumstances, and before removing organic solids and soluble pollutants contained in wastewater, inorganic solids that are difficult to biologically treat are removed. By removing it outside the system, excessive stirring power is not required, and there is no adverse effect caused by the hardly decomposable substances and inorganic solids contained in the wastewater, and a large amount of excess sludge derived from microorganisms An object of the present invention is to provide a dredging waste water treatment device that can eliminate the need for the extraction work.
[0017]
[Means for Solving the Problems]
In order to achieve the above object, the dredged wastewater treatment apparatus of the present invention includes a sand settling tank 21 for settling and separating inorganic solids and a dredged wastewater 211 excluding the inorganic solids as illustrated in FIG. The aerobic digester 23 to be processed, the settling tank 22 that separates the internal liquid of the aerobic digester 23 into concentrated organic solids and sludge, and separated wastewater 221, and the separated wastewater 221 are more aerobic. comprising a wastewater treatment tank (contact aeration tank) 24 for biological treatment, the waste water treatment tank 24 for the aerobic biological treatment, with and configured to direct treated water 231 of the aerobic digestion tank 23, It is characterized by providing the aerobic digestion tank 23 with a means (aeration device 232) for stirring the treated water in the tank.
<Action>
According to the treatment apparatus of the present invention, since the inorganic solids contained in the wastewater are removed from the system by the sand settling tank 21, excessive stirring power for diffusing the inorganic solids is not required. Since the inorganic solids are stored in the dedicated sand settling tank 21, the extraction work can be performed easily and at a lower cost than when the inorganic solids are extracted from a large-capacity aerobic digestion tank. it can.
[0018]
In addition, the hydraulic residence time can be set longer than the time required for the decomposition of the organic solids in the aerobic digestion tank 23 , whereby the organic solids contained in the inflow drainage can be sufficiently decomposed. Moreover, since the aerobic digestion tank 23 is provided with a stirring means, the treated water in the tank can be constantly stirred, and the action of decomposing solid matter by aerobic microorganisms can be enhanced.
[0019]
Furthermore, by allowing the treated water 231 in the tank to flow out, the sludge concentration in the tank can always be maintained at a constant equilibrium state. As a result, the increase and accumulation of sludge in the aerobic digestion tank 23 is achieved. Will not occur.
[0020]
In the processing apparatus of the present invention, it is more convenient to provide an air diffuser for supplying air into the sand settling tank so that the contents can be prevented from decaying or odor.
[0021]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, embodiments of the present invention will be described with reference to the drawings.
[0022]
FIG. 1 is a block diagram showing a configuration of an embodiment of a wastewater treatment apparatus .
The processing apparatus 1 shown in FIG. 1 is an apparatus used for processing dredging drainage generated from a detached house in a sewerage maintenance area, for example, and includes a sand settling tank 11, a settling tank 12, an aerobic digestion tank 13, and a contact aeration tank 14. It is mainly composed.
[0023]
The sand settling tank 11 is a device that separates and stores inorganic solids from dredged wastewater, and is connected to a drainage pipe 110 for flowing together the disposer drainage (spider drainage) and kitchen drainage generated in the sink of a detached house. The
[0024]
The dredged waste water 111 from which the inorganic solid matter is removed in the sand settling tank 11 flows into the settling tank 12.
[0025]
The sedimentation tank 12 is a device that separates the dredged waste water 111 from which inorganic solids have been removed into an organic solids concentrated waste water 121 and a separated waste water 122, and the solids separated in the precipitation tank 12 are the surrounding liquid. At the same time, it is transferred to the aerobic digester 13 by the air lift pump 16 as the solid concentrate drainage 121.
[0026]
The aerobic digestion tank 13 is an apparatus that keeps the inside of the tank in an aerobic atmosphere by the air ejected from the diffuser 132 provided at the bottom of the tank, and mainly decomposes organic solids by the action of aerobic microorganisms. The aerobic digestion tank 13 is provided with a liquid feed pump 15 for constantly stirring the treated water in the tank.
[0027]
On the other hand, the separated waste water 122 separated in the settling tank 12 is guided to the contact aeration tank 14. Similar to the aerobic digestion tank 13, the contact aeration tank 14 has a structure in which the inside of the tank is maintained in an aerobic atmosphere by the air blown from the air diffuser 142 at the bottom of the tank, and decomposes the soluble pollutant.
[0028]
In addition to the separated drainage 122 described above, the effluent 131 overflowed from the aerobic digestion tank 13 flows into the contact aeration tank 14.
[0029]
Next, the operation of the embodiment shown in FIG. 1 will be described.
First, the disposer waste water and the kitchen waste water flow into the sand settling tank 11 through the drain pipe 110. In the sand settling tank 11, an inorganic solid matter having a large sedimentation property is removed by the precipitation separating action, and this inorganic solid matter is removed. The culm drainage and kitchen drainage 111 are guided to the settling tank 12.
[0030]
The solid-concentrated waste water 121 separated in the settling tank 12 is transferred to the aerobic digestion tank 13 by the air lift pump 16, where the organic solid is decomposed by biooxidation of aerobic microorganisms.
[0031]
In the aerobic digestion tank 13, since the solid matter in the tank is constantly stirred by the liquid feed pump 15, the decomposition action by the aerobic microorganism is effectively performed, and the solid matter can be sufficiently decomposed. . Moreover, since the in-tank treated water 131 is allowed to flow out, the sludge concentration in the aerobic digestion tank 13 is always maintained in a constant equilibrium state, so that sludge does not increase in the tank.
[0032]
Then, the treated water 131 in which the solid matter is sufficiently decomposed in the aerobic digestion tank 13 flows out of the tank due to overflow when the solid matter concentrated waste water 121 flows into the tank. The effluent 131 is guided to the contact aeration tank 14.
[0033]
On the other hand, the separated waste water 122 from which the organic solid matter has been removed in the sedimentation tank 11 flows into the contact aeration tank 14, and the dissolved pollutants are decomposed in the tank by the biooxidation of aerobic microorganisms, and the treated water 141. Is discharged out of the tank due to overflow.
[0034]
As described above, in the embodiment shown in FIG. 1, the sedimentary tank 11 is used to remove inorganic solids having a large sedimentation property from the wastewater, and then the aerobic digestion tank 13 and the contact aeration tank 14 are used to organically Since the solid material and the soluble pollutant are separately treated, the capacity and stirring power of each treatment tank can be optimized.
[0035]
In addition, since the inorganic solid matter is stored in the dedicated sand settling tank 11, the cost is lower than extracting the inorganic solid matter from the large-capacity aerobic digestion tank, and the workability is improved.
[0036]
In addition to the configuration of the embodiment shown in FIG. 1, if a sand diffuser 11 is provided with an air diffuser for supplying air into the tank, the contents can be prevented from decaying or odor.
[0037]
Here, in the embodiment shown in FIG. 1, each of the aerobic digestion tank 13 and the contact aeration tank 14 is a single tank, but the present invention is not limited to this, and a plurality of treatment tanks are provided. You may use what connected the tank.
[0038]
Further, the air diffuser, the advection method, the discharge method, the stirring means, and the like as ancillary means of the aerobic digestion tank 13 and the contact aeration tank 14 are not limited to those having the configuration shown in FIG. Any method may be adopted as long as it can obtain the same effect as the contents.
[0039]
FIG. 2 is a block diagram showing the configuration of the embodiment of the present invention.
The treatment apparatus 2 of this embodiment is an apparatus used for the treatment of dredged wastewater generated from an apartment house, and is mainly composed of a sand settling tank 21, a settling tank 22, an aerobic digestion tank 23, and a contact aeration tank 24. Yes.
[0040]
The sand settling tank 21 is a device that separates and stores inorganic solids from dredged wastewater, and is connected to a drain pipe 210 for flowing together the disposer wastewater and kitchen wastewater generated in the sink of each house.
[0041]
The dredged waste water 211 from which the inorganic solid matter is removed in the sand settling tank 21 flows into the aerobic digestion tank 23. In the sand settling tank 21, the air diffuser 212 is provided at an appropriate water depth.
[0042]
The aerobic digestion tank 23 has a structure in which the inside of the tank is maintained in an aerobic atmosphere by air ejected from an air diffuser 232 provided at the bottom of the tank, and mainly decomposes organic solids. The air diffuser 232 provided in the aerobic digestion tank 23 also serves as stirring power for constantly stirring the treated water in the tank.
[0043]
The aerobic digestion tank 23 is provided with a path 26 through which the internal liquid can be circulated with the precipitation tank 22.
[0044]
The settling tank 22 is a tank that separates treated water into concentrated organic solids and sludge and separated wastewater 221 by a settling action, and the bottom of the tank is inclined toward the path 26 to the aerobic digestion tank 23. It is processed into a shape.
[0045]
Then, the treated water 231 in the aerobic digestion tank 23 is transferred from a suitable depth to the contact aeration tank 24 by the liquid feed pump 25.
[0046]
On the other hand, the separated waste water 221 separated in the settling tank 22 is guided to the contact aeration tank 24. Similarly to the aerobic digestion tank 23, the contact aeration tank 24 has a structure in which the inside of the tank is maintained in an aerobic atmosphere by the air ejected from the air diffuser 242 to the bottom of the tank, and dissolves pollutants.
[0047]
Further, the organic solid and sludge concentrated in the sedimentation tank 22 are returned to the aerobic digestion tank 23 through the path 26 and further decomposed and stirred.
[0048]
Next, the operation of the embodiment shown in FIG. 2 will be described.
First, the disposer drainage and the kitchen drainage flow into the sand settling tank 21 through the drain pipe 210. In the sand settling tank 21, the sedimentary separation action removes the inorganic solid matter having a large sedimentation property, and the inorganic solid matter is removed. The kitchen wastewater and kitchen wastewater 211 are led to the aerobic digester 23.
[0049]
In the aerobic digestion tank 23, the solid matter in the tank is constantly stirred by the air diffuser 232 that also serves as the stirring power. Therefore, the decomposition action by the aerobic microorganisms is effectively performed, and the solid matter is sufficiently removed. Can be disassembled. In addition, by allowing the treated water 231 in the tank to flow out with the liquid feed pump 25, the sludge concentration in the aerobic digestion tank 23 is always maintained in a constant parallel state, so that sludge may increase in the tank. Disappear.
[0050]
The internal liquid of the aerobic digestion tank 23 is separated into concentrated organic solids and sludge and separated waste water 221 by the precipitation separation action using the gradient in the precipitation tank 22, and the concentrated organic solids. And sludge returns to the aerobic digester 23 through the path | route 26, and is further stirred and decomposed | disassembled.
[0051]
The outflow water 231 of the aerobic digestion tank 23 is guided to the contact aeration device 24, and the separated waste water 221 decomposed in the settling tank 22 is contacted by overflow when the inflow water 211 flows into the aerobic digestion tank 23. It is transferred to the aeration tank 24.
[0052]
In the contact aeration tank 24, the soluble pollutant is decomposed by biological oxidation of aerobic microorganisms, and the treated water 241 is discharged out of the tank by overflow.
[0053]
As described above, also in the embodiment shown in FIG. 2, since the inorganic solids contained in the dredged wastewater are removed from the system by the sand settling tank 21, the capacity and stirring power of each treatment tank are appropriate. Can be realized. In addition, since the inorganic solid matter is stored in the dedicated sand settling tank 21, the cost is lower than extracting the inorganic solid matter from the large-capacity aerobic digestion tank, and the workability is improved.
[0054]
Here, in the embodiment shown in FIG. 2, each of the aerobic digestion tank 23 and the contact aeration tank 24 is a single tank, but the present invention is not limited to this, and a plurality of treatment tanks are used. You may use what connected the tank.
[0055]
Further, the diffuser, the advection method, the discharge method, the stirring means, and the like as the auxiliary means of the aerobic digestion tank 23 and the contact aeration tank 24 are not limited to the one shown in FIG. Any method may be adopted as long as it can obtain the same effect as the contents.
[0056]
【The invention's effect】
As described above, according to the wastewater treatment apparatus of the present invention, the inorganic solids contained in the wastewater are removed from the system, and the organic solids and the soluble pollutants are individually treated. Therefore, it is possible to optimize the capacity of each treatment tank and the stirring power, whereby the maintenance and management of the treatment apparatus can be performed easily and inexpensively, and the entire apparatus can be made compact.
[0057]
Moreover, this can maintain the sludge density | concentration in a tank in a fixed equilibrium state, without an excess sludge increasing in a digestion tank. Furthermore, since the inorganic solid does not accumulate at the bottom of the digester, it is possible to reduce the failure of the incidental device.
[Brief description of the drawings]
FIG. 1 is a block diagram showing a configuration of an embodiment of the invention described in claim 1; FIG. 2 is a block diagram showing a configuration of an embodiment of the invention described in claim 3;
1 Processing device 11 Sand settling tank 12 Settling tank (separation device)
13 Aerobic digestion tank 14 Contact aeration tank (drainage treatment tank)
DESCRIPTION OF SYMBOLS 15 Liquid feed pump 16 Air lift pump 110 Drain pipe 111 The dredging drainage 121 except the solid inorganic substance 121 Solid matter concentration drainage 122 Separation wastewater 131 Treated water of an aerobic digester 132 Aeration apparatus 141 Treated water 142 Aeration apparatus 2 Processing device 21 Sand settling tank 22 Settling tank 23 Aerobic digestion tank 24 Contact aeration tank (drainage treatment tank)
25 Liquid feed pump 26 Channel 210 Drain pipe 211 Drainage drainage 212 excluding inorganic solid matter 212 Aeration device 221 Separation wastewater 231 Aerobic digester treated water 232 Aeration device 241 Treatment device treated water 242 Aeration device

Claims (2)

厨芥排水に含まれる有機性固形物の濃度を低くするのに用いられる装置であって、厨芥固形物のうち無機性固形物を分離する沈砂槽と、その無機性固形物を除いた厨芥排水を処理する好気性消化槽と、この好気性消化槽の内部液を、濃縮された有機性固形物及び汚泥と分離排水とに分離する沈殿槽と、この分離排水をさらに好気的生物処理する排水処理槽を備え、その好気的生物処理を行う排水処理槽に、前記好気性消化槽内の処理水を導くように構成されているとともに、上記好気性消化槽に槽内を攪拌する手段が設けられていることを特徴とする厨芥排水の処理装置。A device used to reduce the concentration of organic solids contained in dredging wastewater, a sand settling tank that separates inorganic solids from dredged solids, and dredging drainage that excludes the inorganic solids An aerobic digester to be treated, a settling tank for separating the internal liquid of the aerobic digester into concentrated organic solids and sludge and separated wastewater, and wastewater for further aerobic biological treatment of the separated wastewater comprising a treatment vessel, the waste water treatment tank to perform the aerobic biological treatment, the conjunction is configured to direct the treated water aerobic digestion tank, means for agitating the intracisternal to the aerobic digestion tank A wastewater treatment apparatus characterized by being provided. 上記沈砂槽には、空気を槽内に供給する散気装置が設けられていることを特徴とする請求項1に記載の厨芥排水の処理装置。  The apparatus for treating dredged wastewater according to claim 1, wherein the sand basin is provided with an air diffuser for supplying air into the tank.
JP35511497A 1997-12-24 1997-12-24 厨 芥 Wastewater treatment equipment Expired - Fee Related JP3764812B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP35511497A JP3764812B2 (en) 1997-12-24 1997-12-24 厨 芥 Wastewater treatment equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP35511497A JP3764812B2 (en) 1997-12-24 1997-12-24 厨 芥 Wastewater treatment equipment

Publications (2)

Publication Number Publication Date
JPH11179389A JPH11179389A (en) 1999-07-06
JP3764812B2 true JP3764812B2 (en) 2006-04-12

Family

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Family Applications (1)

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Country Link
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