JPS625032B2 - - Google Patents
Info
- Publication number
- JPS625032B2 JPS625032B2 JP3175482A JP3175482A JPS625032B2 JP S625032 B2 JPS625032 B2 JP S625032B2 JP 3175482 A JP3175482 A JP 3175482A JP 3175482 A JP3175482 A JP 3175482A JP S625032 B2 JPS625032 B2 JP S625032B2
- Authority
- JP
- Japan
- Prior art keywords
- tank
- sludge
- wastewater
- treatment
- present
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- 239000010802 sludge Substances 0.000 claims description 32
- 239000002351 wastewater Substances 0.000 claims description 13
- 239000007788 liquid Substances 0.000 claims description 6
- 238000007664 blowing Methods 0.000 claims description 3
- 238000000034 method Methods 0.000 description 7
- 238000013019 agitation Methods 0.000 description 4
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 4
- 238000002156 mixing Methods 0.000 description 4
- 238000003756 stirring Methods 0.000 description 3
- 238000000354 decomposition reaction Methods 0.000 description 2
- 230000029087 digestion Effects 0.000 description 2
- 238000000855 fermentation Methods 0.000 description 2
- 230000004151 fermentation Effects 0.000 description 2
- 239000005416 organic matter Substances 0.000 description 2
- 239000013049 sediment Substances 0.000 description 2
- 238000005273 aeration Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000000265 homogenisation Methods 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000008400 supply water Substances 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
-
- 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
- Activated Sludge Processes (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
- Treatment Of Sludge (AREA)
Description
【発明の詳細な説明】 本発明は、廃水及び汚泥の処理槽に関する。[Detailed description of the invention] The present invention relates to a wastewater and sludge treatment tank.
活性汚泥法や嫌気性汚泥消化法(メタン発酵
法)等のように、微生物を利用し廃水中の有機物
を分解し生成する汚泥を分離して廃水を処理する
方法が広く行われている。 BACKGROUND ART Methods such as activated sludge method and anaerobic sludge digestion method (methane fermentation method) are widely used to treat wastewater by using microorganisms to decompose organic matter in wastewater and separate the generated sludge.
これらの方法では、いかに有機物の分解率や分
解速度及び処理効率を向上させるかが問題点であ
り、これに係る廃水及び汚泥の処理槽、つまり汚
泥消化槽、曝気槽及びメタン発酵槽等の開発改良
が行われてきた。特に、処理槽内の滞留液を混合
撹拌し十分な均一化をはかることによつて前述し
たような問題点が満足し得るものとなる。 The problem with these methods is how to improve the decomposition rate, decomposition rate, and treatment efficiency of organic matter, and the development of wastewater and sludge treatment tanks, such as sludge digestion tanks, aeration tanks, and methane fermentation tanks, is a problem in these methods. Improvements have been made. In particular, the above-mentioned problems can be solved by mixing and stirring the liquid remaining in the treatment tank to achieve sufficient homogenization.
従来より知られている撹拌機構を具備した処理
槽としては、例えばエアリフトポンプの原理を応
用したガスリフト方式がある。この方式は、槽の
中央に設けた垂直管の中央部又は底部にガスを圧
入するものであるが、撹拌力不足で槽の底部にか
なりの沈砂や汚泥が堆積し汚泥の希釈等を招きや
すい欠点がある。 As a conventionally known processing tank equipped with a stirring mechanism, there is, for example, a gas lift system that applies the principle of an air lift pump. This method involves pressurizing gas into the center or bottom of a vertical pipe installed in the center of the tank, but due to insufficient stirring power, a considerable amount of sediment and sludge accumulates at the bottom of the tank, which tends to lead to dilution of the sludge. There are drawbacks.
又、掻寄機やスクリユー等の撹拌機を内装した
処理槽は、騒動装置の極性の切替えにより回転方
向を逆転できる利点はあるが、槽上部のシール方
法が困難で繊維物質がスクリユー等に付着して電
動機及び処理能力の低下を招きやすい欠点があ
る。 In addition, processing tanks equipped with agitators such as scrapers or screws have the advantage of being able to reverse the rotation direction by switching the polarity of the agitator, but it is difficult to seal the top of the tank and fibers may adhere to the screws. However, there is a drawback that the electric motor and processing capacity tend to deteriorate.
そして、従来のいずれのタイプの処理槽も、堆
積汚泥によるデツドスペース(死空間)を生じや
すく、堆積汚泥の取出し作業をしなければならな
いものであつた。 In addition, all types of conventional treatment tanks tend to produce dead spaces due to accumulated sludge, and the accumulated sludge must be removed.
本発明の目的は、前記従来の欠点を解決した廃
水及び汚泥の処理槽、特に槽内の混合撹拌を十分
に、かつ均一に行える廃水及び汚泥の処理槽を提
供することにあり、本発明者らは本発明の目的を
達成すべく鋭意検討を重ねた結果、本発明を完成
した。 An object of the present invention is to provide a wastewater and sludge treatment tank that solves the above-mentioned conventional drawbacks, and in particular, to provide a wastewater and sludge treatment tank that can perform sufficient and uniform mixing and agitation in the tank. They completed the present invention as a result of repeated studies to achieve the object of the present invention.
即ち、本発明は、槽内の滞留液中で少なくとも
堆積汚泥の上方に、槽横断の同一円周方向に廃水
及び又は汚泥の吹き出し可能な吹出し管を槽内壁
に設けたことを特徴とする廃水及び又は汚泥の処
理槽である。 That is, the present invention provides a wastewater treatment system characterized in that a blowout pipe capable of blowing out wastewater and/or sludge in the same circumferential direction across the tank is provided on the inner wall of the tank, at least above the accumulated sludge in the stagnant liquid in the tank. and/or a sludge treatment tank.
以下に、本発明を添付の図面に基づいて詳細に
説明を行う。 The present invention will be explained in detail below based on the accompanying drawings.
第1図は本発明の実施の態様の一例を示し、第
2図は本発明の処理槽の平面概略図を示す。 FIG. 1 shows an example of an embodiment of the present invention, and FIG. 2 shows a schematic plan view of a processing tank of the present invention.
従来では、廃水や汚泥等は槽上部よりただ送液
されるのみであつたが、本発明においては第1,
2図に示したように処理槽1内の滞留液中で少な
くとも堆積汚泥2の上方に、槽横断の同一円周方
向に流体の吹出し可能な吹出し管3を槽内壁に設
けて廃水及び汚泥の槽内への供給をはかつてい
る。 In the past, wastewater, sludge, etc. were simply pumped from the top of the tank, but in the present invention, the first,
As shown in Fig. 2, a blowout pipe 3 capable of blowing out fluid in the same circumferential direction across the tank is provided on the tank inner wall at least above the accumulated sludge 2 in the stagnant liquid in the treatment tank 1. It is used to supply water into the tank.
これによつて、掻寄機やスクリユー等の撹拌機
を必要とせず十分で均一な混合撹拌が行えるだけ
の渦巻流を発生させることができる。そして、槽
内に堆積物によるデツドスペースはなくなり容積
あたりの処理量が上昇し、ポンプの動力を有効に
使用でき槽内部の簡略化がはかれ経済的にも有利
である。 Thereby, it is possible to generate a swirling flow sufficient for sufficient and uniform mixing and agitation without requiring a stirrer such as a scraper or screw. Further, there is no dead space due to deposits in the tank, the throughput per volume increases, the power of the pump can be used effectively, the inside of the tank can be simplified, and it is economically advantageous.
吹出し管の形状は、例えば第3図に示したよう
に、廃水や汚泥が同一円周方向に吹出し可能であ
れば良く、吹出し管の数や吹出し流速等は処理槽
の大きさや形状等によつて適宜決定すれば良い。
又、廃水や汚泥をあらかじめ同一配管内に送液し
たうえで処理槽内部の数ケ所から吹き出させるこ
とも可能である。 As shown in Figure 3, the shape of the blow-off pipes may be such that wastewater and sludge can be blown out in the same circumferential direction, and the number of blow-off pipes, the blow-off flow rate, etc. will depend on the size and shape of the treatment tank. You can decide accordingly.
It is also possible to send wastewater or sludge into the same pipe in advance and then blow it out from several locations inside the treatment tank.
槽内の外周部では、沈砂、汚泥等を浮遊させる
だけの流速(0.2m/sec〜0.4m/sec程度)を持
たせるが、中心部に向うに従つて流速は減じられ
ていくので一定流速以下になると沈砂、汚泥が沈
降し、槽底部の主として中央部に集められ堆積し
ていく、この堆積汚泥は前記効果によつて少量で
槽外部の汚泥引抜経路の循環汚泥ポンプ4によつ
て定常的又は断続的に引抜かれ一部は循環使用さ
れる。又、処理槽1より得られる処理液を第1図
に示したように沈殿槽5によつて沈殿分離された
汚泥を、前記廃水や循環汚泥と同様にして返送供
給しても良い。 The outer periphery of the tank has a flow velocity (approximately 0.2 m/sec to 0.4 m/sec) that is sufficient to suspend sediment, sludge, etc., but the flow velocity decreases toward the center, so a constant flow velocity is maintained. When the amount is below, the sand and sludge settle, and are collected and deposited mainly in the center of the bottom of the tank. Due to the above effect, this accumulated sludge is kept in a small amount by the circulating sludge pump 4 in the sludge extraction route outside the tank. It is extracted periodically or intermittently, and some are recycled. Further, as shown in FIG. 1, the treatment liquid obtained from the treatment tank 1 may be separated by sedimentation in the settling tank 5, and the sludge may be returned and supplied in the same manner as the waste water or circulating sludge.
他に、本発明の処理槽に、第1図に示したよう
にエアリフトポンプ等を併用するとガス撹拌によ
り槽内滞留液の上部と下部の混合撹拌を促進する
ことができる。 In addition, when an air lift pump or the like is used in combination with the treatment tank of the present invention as shown in FIG. 1, mixing and agitation of the upper and lower parts of the liquid staying in the tank can be promoted by gas agitation.
なお、図中、4′は返送汚泥ポンプ、6はブロ
ワーを示す。 In addition, in the figure, 4' is a return sludge pump, and 6 is a blower.
第1図は、本発明の実施の態様の一例を示し、
第2図は本発明の処理槽の平面概略図であり、第
3図は吹出し管の具体例を示す。
1……処理槽、2……堆積汚泥、3,3′……
吹出し管、4……環循汚泥ポンプ。
FIG. 1 shows an example of an embodiment of the present invention,
FIG. 2 is a schematic plan view of the processing tank of the present invention, and FIG. 3 shows a specific example of the blow-off pipe. 1... Treatment tank, 2... Accumulated sludge, 3, 3'...
Blowout pipe, 4... Circulating sludge pump.
Claims (1)
に、槽横断の同一円周方向に廃水及び又は汚泥の
吹き出し可能な吹出し管を槽内壁に設けたことを
特徴とする廃水及び汚泥の処理槽。1. A treatment tank for wastewater and sludge, characterized in that a blowout pipe capable of blowing out wastewater and/or sludge in the same circumferential direction across the tank is provided on the inner wall of the tank, at least above the accumulated sludge in the accumulated liquid in the tank. .
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57031754A JPS58150493A (en) | 1982-03-02 | 1982-03-02 | Tank for treating waste water and sludge |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57031754A JPS58150493A (en) | 1982-03-02 | 1982-03-02 | Tank for treating waste water and sludge |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS58150493A JPS58150493A (en) | 1983-09-07 |
| JPS625032B2 true JPS625032B2 (en) | 1987-02-03 |
Family
ID=12339803
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP57031754A Granted JPS58150493A (en) | 1982-03-02 | 1982-03-02 | Tank for treating waste water and sludge |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS58150493A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2020204013A1 (en) * | 2019-03-29 | 2020-10-08 | 古河電気工業株式会社 | Insulating tape for coating connection part of power cable, method for forming insulating coating on exterior surface of connection part of power cable, and power cable |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS61178016A (en) * | 1985-02-01 | 1986-08-09 | Takuma Sogo Kenkyusho:Kk | Recovery of methane gas in digestion tank |
| DE10358400A1 (en) * | 2003-12-11 | 2005-07-07 | Linde-Kca-Dresden Gmbh | Biological treatment of suspension of, e.g. waste water, sewage sludge, in bioreactor by feeding horizontal jet(s) of fluid superimposing on vertical flow in bottom part of bioreactor |
| JP5872521B2 (en) * | 2013-03-27 | 2016-03-01 | 株式会社神鋼環境ソリューション | Methane fermentation tank and method for removing deposits in methane fermentation tank |
| JP5412598B1 (en) * | 2013-08-21 | 2014-02-12 | 株式会社神鋼環境ソリューション | Operation method of methane fermentation tank |
| CN108867270B (en) * | 2018-08-01 | 2020-10-02 | 四川启创建设工程有限公司 | Highway and urban road cement stabilization rubble basic unit mud intelligence are spilled cloth car |
-
1982
- 1982-03-02 JP JP57031754A patent/JPS58150493A/en active Granted
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2020204013A1 (en) * | 2019-03-29 | 2020-10-08 | 古河電気工業株式会社 | Insulating tape for coating connection part of power cable, method for forming insulating coating on exterior surface of connection part of power cable, and power cable |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS58150493A (en) | 1983-09-07 |
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