JPS6233594A - Biological wastewater treatment method - Google Patents
Biological wastewater treatment methodInfo
- Publication number
- JPS6233594A JPS6233594A JP60174666A JP17466685A JPS6233594A JP S6233594 A JPS6233594 A JP S6233594A JP 60174666 A JP60174666 A JP 60174666A JP 17466685 A JP17466685 A JP 17466685A JP S6233594 A JPS6233594 A JP S6233594A
- Authority
- JP
- Japan
- Prior art keywords
- water
- treated
- reaction tank
- reaction vessel
- flow
- 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
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- Biological Treatment Of Waste Water (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
この発明は、微生物、即ち生体触媒を使用して廃水の浄
化を行なう生物学的廃水処理方法に関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a biological wastewater treatment method for purifying wastewater using microorganisms, that is, biocatalysts.
生物学的廃水処理方法においては、反応槽の容量あたり
の生体触媒濃度を高濃度に維持することによって反応槽
のコンパクト化、固液分離性の改善、余剰汚泥の発生量
を少なくすることなどが可能である。このため、生体触
媒を無機担体へ吸着させたり、また、生体触媒を有機担
体によって包括したり、あるいは生体触媒を無機担体へ
吸着させた後、有機担体によって包括するなど、生体触
媒を固定化して生体触媒濃度を高濃度に維持することが
行なわれている。さらに、反応槽の容量あたりの生体触
媒濃度を高くするために、担体に固定化する生体触媒量
を増加させたり、反応槽内の担体充填率を増加させるこ
とも知られている。In biological wastewater treatment methods, by maintaining a high biocatalyst concentration per reactor capacity, it is possible to make the reactor more compact, improve solid-liquid separation, and reduce the amount of surplus sludge generated. It is possible. For this reason, it is possible to immobilize the biocatalyst by adsorbing the biocatalyst onto an inorganic carrier, encapsulating the biocatalyst with an organic carrier, or adsorbing the biocatalyst onto an inorganic carrier and then encapsulating it with an organic carrier. The biocatalyst concentration is maintained at a high concentration. Furthermore, in order to increase the biocatalyst concentration per volume of the reaction tank, it is also known to increase the amount of biocatalyst immobilized on the carrier or to increase the carrier filling rate in the reaction tank.
ところで、従来、反応槽内に上昇管を立設し、反応槽内
の底部の被処理水を上昇流によって上昇管内を上昇せし
め、反応槽内の上部に上昇せしめた被処理水を下降流に
よって上昇管の外壁と反虐槽の内壁みの間を下降せしめ
ることにより、被処理水を反応槽内において循環させて
、生体触媒と被処理水との接触効率を高める生物学的廃
水処理方法がある。By the way, conventionally, a riser pipe is installed in the reaction tank, and the water to be treated at the bottom of the reaction tank is caused to rise in the riser pipe by an upward flow, and the water to be treated that has risen to the top of the reaction tank is caused to flow downward. A biological wastewater treatment method is provided in which the water to be treated is circulated in the reaction tank by descending between the outer wall of the riser pipe and the inner wall of the reaction tank, thereby increasing the contact efficiency between the biocatalyst and the water to be treated. be.
しかしながら、この方法には、従来次のような問題点が
あった。即ち、反応槽内で被処理水を上昇流と下降流と
によって循環させた場合、下降流から上昇流へと流れの
方向が変わる反応槽の底部において、反応槽の底部内壁
周辺に死水域が形成される。このため、反応槽内の生体
触媒濃度を高(するために、固定化生体触媒を反応槽内
に充填しても、死水域での固定化生体触媒が充分に活動
せず、反応槽内における廃水の浄化に有効な固定化生体
触媒の充填率が充分に向上しないという問題があった。However, this method has conventionally had the following problems. In other words, when the water to be treated is circulated in the reaction tank by upward flow and downward flow, a dead area is created around the bottom inner wall of the reaction tank at the bottom of the reaction tank where the flow direction changes from downward flow to upward flow. It is formed. For this reason, even if the reaction tank is filled with immobilized biocatalyst to increase the biocatalyst concentration in the reaction tank, the immobilized biocatalyst in the dead area will not be sufficiently active, and the There has been a problem in that the filling rate of the immobilized biocatalyst, which is effective in purifying wastewater, is not sufficiently improved.
そこで、この発明は、反応槽内に死水域が形成され難い
循環式の生物学的廃水処理方法を提供しようとするもの
である。Therefore, it is an object of the present invention to provide a circulating biological wastewater treatment method in which a dead zone is unlikely to be formed in a reaction tank.
上記の問題点を解決するために、この発明は、上記のよ
うな反応槽”内において被処理水を下向流と上昇流とに
よって被処理水を循環せしめる生物学的廃水処理方法に
おいて、下向流の下端へ、廃水と共に処理水の一部を下
向流と同方向に流入させるものである。In order to solve the above problems, the present invention provides a biological wastewater treatment method in which water to be treated is circulated by a downward flow and an upward flow in a reaction tank as described above. A portion of the treated water along with the wastewater flows into the lower end of the counterflow in the same direction as the downward flow.
これにより、死水域が形成され易い反応槽の底部周辺の
固定化生体触媒と被処理水が強制的に流動化されるので
、反応槽内に死水域が形成されない。As a result, the immobilized biocatalyst and the water to be treated around the bottom of the reaction tank where a dead zone is likely to be formed are forcibly fluidized, so that a dead zone is not formed in the reaction tank.
以下、この発明の実施例を添付図面に基づいて説明する
。Embodiments of the present invention will be described below with reference to the accompanying drawings.
第1図は嫌気的処理を行なう装置の概略図である。この
ものは、密閉型の反応槽1内に、上昇管2を設けてあり
、溢流によって引き出した処理水。FIG. 1 is a schematic diagram of an apparatus for performing anaerobic treatment. This is a closed reaction tank 1 with a rising pipe 2, and the treated water is drawn out by overflow.
3を循環ポンプ4により反応槽1の底部に流入させて反
応槽1内に上昇流を形成し、これにより被処理水5が上
昇管2内を上昇し、反応槽1内の上部に上昇した被処理
水5が上昇管2の外壁と反応槽1の内壁との間を下降流
によって下降して循環するようになっている。そして、
循環ポンプ4によって循環される処理水3の一部を、原
水6と共に、下降流の下端部分に、下降流と同方向に流
入させて反応槽1の底部周辺の固定化生体触媒と被処理
水5を流動化させている。この際、処理水子の一部と原
水6とは、上昇管2の周囲に均等に流入させることが好
ましい。3 was caused to flow into the bottom of the reaction tank 1 by the circulation pump 4 to form an upward flow in the reaction tank 1, whereby the water to be treated 5 rose in the rising pipe 2 and rose to the upper part of the reaction tank 1. The water to be treated 5 is circulated by descending between the outer wall of the riser pipe 2 and the inner wall of the reaction tank 1 by a downward flow. and,
A part of the treated water 3 circulated by the circulation pump 4 is caused to flow into the lower end of the downward flow together with the raw water 6 in the same direction as the downward flow, and the immobilized biocatalyst around the bottom of the reaction tank 1 and the water to be treated are 5 is fluidized. At this time, it is preferable that a part of the treated water and the raw water 6 are allowed to flow evenly around the riser pipe 2 .
第2図も第1図と同様に嫌気性処理を行なう装置であり
、このものは嫌気性処理によって発生するCH,、Co
2等のガス8をコンプレッサー7によって反応槽1の底
部に吹き入れ、上昇流を形成している。そして、溢流に
よって引き出した処理水3と一部と原水6を、下降流の
下端部分に、下降流と同方向に流入させている。Figure 2 also shows a device that performs anaerobic treatment, similar to Figure 1, and this device is designed to reduce the amount of CH, Co, generated by anaerobic treatment.
A gas 8 such as No. 2 is blown into the bottom of the reaction tank 1 by a compressor 7 to form an upward flow. Then, the treated water 3 and part of the water drawn out by the overflow and the raw water 6 are made to flow into the lower end portion of the downward flow in the same direction as the downward flow.
次に、第3図のものは好気性処理を行なう装置であって
、反応槽1の底部から曝気用コンプレッサー9によって
空気が吹き込まれ、これによって反応槽1内に上昇流が
形成されるようになっている。そして、溢流によって引
き出した処理水の一部と原水6を、下降流の下端部分に
、下降流と同方向に流入させている。Next, the one in FIG. 3 is an apparatus for performing aerobic treatment, in which air is blown into the bottom of the reaction tank 1 by an aeration compressor 9, thereby forming an upward flow in the reaction tank 1. It has become. Then, a part of the treated water drawn out by the overflow and the raw water 6 are made to flow into the lower end portion of the downward flow in the same direction as the downward flow.
この発明は、以上の如きものであ、るがら、死水域が生
じ易い反応槽の底部周辺において、被処理水の流動が起
る。The present invention is as described above, however, the water to be treated flows around the bottom of the reaction tank where a dead area is likely to occur.
したがって、この発明によれば、反応槽内に死水域の形
成が防止されるので、反応槽内に充填された固定化生体
触媒がすべて有効に活動し、実質的に生体触媒濃度が向
上するという効果がある。Therefore, according to the present invention, since the formation of dead zones in the reaction tank is prevented, all the immobilized biocatalysts filled in the reaction tank are effectively activated, and the biocatalyst concentration is substantially increased. effective.
また、原水が処理水と共に、下降流の下端に流入させる
ことにより、原水が十分に混合攪拌されるので、原水の
濃度が高い場合特に処理効率が向上するという効果もあ
る。Furthermore, by causing the raw water to flow into the lower end of the downward flow together with the treated water, the raw water is sufficiently mixed and agitated, which has the effect of improving the treatment efficiency especially when the concentration of the raw water is high.
第1図乃・至第3図はそれぞれこの発明の実施装置の例
を示す概略図である。
1.1・・・反応槽、2・・・上昇管、3・・・処理水
、5・・・被処理水、6・・・原水
特許出願人 久保田鉄工株式会社
同代理人 鎌 1)文 二FIGS. 1 to 3 are schematic diagrams each showing an example of an apparatus for implementing the present invention. 1.1...Reaction tank, 2...Rising pipe, 3...Treated water, 5...Water to be treated, 6...Raw water Patent applicant Kubota Iron Works Co., Ltd. Same agent Kama 1) Sentence two
Claims (1)
上昇流によつて上昇管内を上昇せしめ、反応槽内の上部
に上昇せしめた被処理水を下降流によつて上昇管の外壁
と反応槽の内壁との間を下降せしめて生体触媒と被処理
水とを接触させる生物学的廃水処理方法において、上記
下降流の下端へ原水と共に処理水の一部を下降流と同方
向に流入させることを特徴とする生物学的廃水処理方法
。A riser pipe is installed in the reaction tank, and the water to be treated at the bottom of the reaction tank is made to rise in the riser pipe by an upward flow, and the water to be treated that has risen to the top of the reaction tank is caused to rise by a downward flow. In a biological wastewater treatment method in which the biocatalyst and the water to be treated are brought into contact by descending between the outer wall of a pipe and the inner wall of a reaction tank, a portion of the treated water along with the raw water is made to flow downward to the lower end of the downward flow. A biological wastewater treatment method characterized by flowing in the same direction.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60174666A JPS6233594A (en) | 1985-08-06 | 1985-08-06 | Biological wastewater treatment method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60174666A JPS6233594A (en) | 1985-08-06 | 1985-08-06 | Biological wastewater treatment method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS6233594A true JPS6233594A (en) | 1987-02-13 |
Family
ID=15982571
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP60174666A Pending JPS6233594A (en) | 1985-08-06 | 1985-08-06 | Biological wastewater treatment method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6233594A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2017176957A (en) * | 2016-03-29 | 2017-10-05 | 株式会社クラレ | Method of treating waste water using carrier |
-
1985
- 1985-08-06 JP JP60174666A patent/JPS6233594A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2017176957A (en) * | 2016-03-29 | 2017-10-05 | 株式会社クラレ | Method of treating waste water using carrier |
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