JPH04277088A - Aeration device for waste liquid treatment - Google Patents
Aeration device for waste liquid treatmentInfo
- Publication number
- JPH04277088A JPH04277088A JP3064068A JP6406891A JPH04277088A JP H04277088 A JPH04277088 A JP H04277088A JP 3064068 A JP3064068 A JP 3064068A JP 6406891 A JP6406891 A JP 6406891A JP H04277088 A JPH04277088 A JP H04277088A
- Authority
- JP
- Japan
- Prior art keywords
- screw
- hollow shaft
- ventilation pipe
- wastewater
- air
- 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
- 238000005273 aeration Methods 0.000 title claims description 11
- 239000007788 liquid Substances 0.000 title abstract 2
- 239000002699 waste material Substances 0.000 title abstract 2
- 239000010865 sewage Substances 0.000 claims description 4
- 238000009423 ventilation Methods 0.000 abstract description 27
- 238000005276 aerator Methods 0.000 abstract description 9
- 238000003756 stirring Methods 0.000 abstract description 9
- 230000001105 regulatory effect Effects 0.000 abstract 1
- 239000002351 wastewater Substances 0.000 description 21
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 13
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 9
- 229910052757 nitrogen Inorganic materials 0.000 description 4
- 241000894006 Bacteria Species 0.000 description 2
- 241000192700 Cyanobacteria Species 0.000 description 2
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000008239 natural water Substances 0.000 description 2
- 230000000149 penetrating effect Effects 0.000 description 2
- 229910052698 phosphorus Inorganic materials 0.000 description 2
- 239000011574 phosphorus Substances 0.000 description 2
- JVMRPSJZNHXORP-UHFFFAOYSA-N ON=O.ON=O.ON=O.N Chemical compound ON=O.ON=O.ON=O.N JVMRPSJZNHXORP-UHFFFAOYSA-N 0.000 description 1
- MMDJDBSEMBIJBB-UHFFFAOYSA-N [O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O.[NH6+3] Chemical compound [O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O.[NH6+3] MMDJDBSEMBIJBB-UHFFFAOYSA-N 0.000 description 1
- 238000010564 aerobic fermentation Methods 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 229910001873 dinitrogen Inorganic materials 0.000 description 1
- 239000010840 domestic wastewater Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000012851 eutrophication Methods 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 238000011017 operating method Methods 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 239000000126 substance Substances 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
- 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
- Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
Description
【0001】0001
【産業上の利用分野】本発明は汚水の撹拌を行う嫌気運
転と、給気と撹拌を同時に行う好気運転とを一台の曝気
機を用い、簡易に切り換えて運転するようになした汚水
処理用曝気装置に関するものである。[Industrial Application Field] The present invention uses a single aerator to easily switch between anaerobic operation for stirring sewage and aerobic operation for simultaneously supplying air and stirring. This invention relates to a treatment aeration device.
【0002】0002
【従来の技術】近年、湖沼、河川等、自然水域の富栄養
化が進み、赤潮、アオコが頻繁に発生し、各地で環境問
題がクローズアップしている。富栄養化の大きな要因は
、赤潮、アオコの栄養塩となる窒素、燐を高濃度に含ん
だ下水処理水の自然水域への放流及び家庭排水の直接放
流である。この問題を解決するためには、排水中の窒素
、燐を高効率で除去する水処理技術の開発と、下水道の
完備が不可欠である。このうち、窒素の除去については
次のようなメカニズムが明らかになっている。すなわち
、窒素は下水中にアンモニア態窒素として存在し、曝気
により硝化が進行し、硝酸態窒素、亜硝酸態窒素に変化
する。さらにこれらの窒素は嫌気条件下で脱窒菌に酸素
を奪われ、窒素ガスとして水中より大気中へ拡散し、脱
窒が行われる。汚水の脱窒を行うには汚水を嫌気状態に
すればよい。しかし汚水は生物処理を行うため、汚水中
に空気を吹き込むものとして曝気機が汎用されている。
この曝気を効率的に、かつ撹拌もともに行うため、自吸
式曝気機が用いられることがしばしばある。BACKGROUND OF THE INVENTION In recent years, natural water bodies such as lakes and rivers have become increasingly eutrophic, red tides and blue-green algae occur frequently, and environmental problems have become a focus of attention in various places. Major causes of eutrophication are red tide, the discharge of treated sewage water containing high concentrations of nitrogen and phosphorus, which are nutrients for blue-green algae, into natural water bodies, and the direct discharge of domestic wastewater. To solve this problem, it is essential to develop water treatment technology that removes nitrogen and phosphorus from wastewater with high efficiency and to install a complete sewer system. Among these, the following mechanism for nitrogen removal has been clarified. That is, nitrogen exists in sewage as ammonia nitrogen, and aeration progresses nitrification and changes to nitrate nitrogen and nitrite nitrogen. Further, under anaerobic conditions, these nitrogens are deprived of oxygen by denitrifying bacteria and diffused from the water into the atmosphere as nitrogen gas, resulting in denitrification. To denitrify wastewater, it is sufficient to bring the wastewater into an anaerobic state. However, since wastewater undergoes biological treatment, aerators are commonly used to blow air into the wastewater. A self-priming aerator is often used to efficiently perform this aeration and also to perform stirring.
【0003】0003
【発明が解決しようとする課題】従って自吸式曝気機を
備えた処理池または槽においては脱窒を行うための嫌気
状態は曝気機を停止することにより得られる。しかしこ
のような場合、脱窒菌が汚泥と共に沈降して汚水との接
触効率が低下し、十分な処理が行えない。従って効率的
に脱窒を行うためには嫌気状態においても汚水を撹拌混
合を行う必要がある。この曝気と嫌気撹拌を一台の自吸
式の曝気機にて行う方法が提案されている。これは曝気
運転時、吸気用バルブを開くことによりスクリュー先端
水域に発生する負圧を利用して吸気され、汚水中へ空気
を微細気泡として供給し、また嫌気運転時は前記吸気用
バルブを閉塞して運転すれば汚水中には吸気されず、撹
拌のみ行われる。このため曝気機に吸気用バルブを要す
るものとなる。Therefore, in a treatment pond or tank equipped with a self-priming aerator, an anaerobic state for denitrification can be obtained by stopping the aerator. However, in such cases, the denitrifying bacteria settle together with the sludge, reducing the efficiency of contact with the wastewater, making it impossible to perform sufficient treatment. Therefore, in order to perform denitrification efficiently, it is necessary to stir and mix wastewater even in an anaerobic state. A method has been proposed in which this aeration and anaerobic stirring are performed using a single self-priming aerator. During aeration operation, air is taken in using the negative pressure generated in the water area at the tip of the screw by opening the intake valve, and air is supplied into the wastewater as fine bubbles, and during anaerobic operation, the intake valve is closed. If the system is operated in this way, air will not be sucked into the wastewater and only agitation will occur. For this reason, the aerator requires an intake valve.
【0004】一台の自吸式曝気機を用い、吸気バルブを
開閉しつつ好気・嫌気運転を交互に切り換えて行う場合
、運転方法は単なるタイマーにより好気・嫌気運転時間
を予め定め、ON−OFF運転にて行っている。このた
め十分な脱窒が進行しなかったり、負荷変動にともなっ
て硝化・脱窒性能が変化する等の欠点がある。[0004] When using one self-priming aerator and switching between aerobic and anaerobic operation alternately while opening and closing the intake valve, the operating method is simply to preset the aerobic and anaerobic operation times using a timer, and then turn the -This is done in OFF operation. For this reason, there are drawbacks such as insufficient denitrification and changes in nitrification and denitrification performance due to load fluctuations.
【0005】本発明では好気・嫌気運転の切替をバルブ
を用いることなく、中空軸内に貫通した通気管の出没に
て行い、簡易に通気量を調整して運転切替を行うことを
目的とする。[0005] The purpose of the present invention is to switch between aerobic and anaerobic operation by using a ventilation pipe penetrating the hollow shaft, without using a valve, and to easily adjust the amount of ventilation and switch the operation. do.
【0006】[0006]
【課題を解決するための手段】本発明は上記目的を達成
するためになしたもので、中空状のモータ軸に、スクリ
ューを下端に設けた中空軸を連結するとともにこのモー
タ軸・中空軸内に一本の通気管を貫通して成り、この通
気管の下端の突出量を調整してスクリューの回転数に関
係なく通気量を調整可能としたことを要旨とする。[Means for Solving the Problems] The present invention has been made to achieve the above object, and includes connecting a hollow shaft having a screw at the lower end to a hollow motor shaft, and The main feature is that the vent tube is formed by penetrating a single vent pipe, and by adjusting the amount of protrusion of the lower end of the vent pipe, the amount of ventilation can be adjusted regardless of the rotational speed of the screw.
【0007】[0007]
【作用】中空状のモータ軸と中空軸内に貫通した通気管
をスクリュー先端水域に突出させ、この通気管をスライ
ドさせてその下端の突出量を調整する。これにより、通
気管下端域での負圧が変化するため通気量を設定された
最大値より0まで任意に調整できる。[Operation] A hollow motor shaft and a vent pipe passing through the hollow shaft are made to protrude into the screw tip water area, and the vent pipe is slid to adjust the amount of protrusion of its lower end. As a result, the negative pressure in the lower end region of the ventilation pipe changes, so that the ventilation amount can be arbitrarily adjusted from the set maximum value to zero.
【0008】[0008]
【実施例】以下本発明を図示の実施例にもとづいて説明
する。図において1は汚水を効率的に撹拌し、かつ先端
水域に所要の負圧を発生するようになした曝気装置のス
クリューで、このスクリュー1は所要長の中空軸2の先
端に固定されている。そしてこの中空軸2の基端側はモ
ータ3の中空状のモータ軸3aに直結または連結され、
モータ軸3aと中空軸2とを一本状にし、かつその内部
空洞を互いに導通せしめる。DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be explained below based on the illustrated embodiments. In the figure, 1 is a screw of an aeration device that efficiently stirs wastewater and generates the required negative pressure in the water area at the tip. This screw 1 is fixed to the tip of a hollow shaft 2 of a specified length. . The base end side of the hollow shaft 2 is directly connected or connected to the hollow motor shaft 3a of the motor 3.
The motor shaft 3a and the hollow shaft 2 are made into a single piece, and their internal cavities are electrically connected to each other.
【0009】モータ軸3aの上端はモータ3のモータカ
バー3bよりも外方へ突出せしめるとともにモータ軸3
a、中空軸2の内部空洞内には一本の通気管4を貫通せ
しめ、この通気管4の下端側4aを図1に示すようにス
クリュー端面近傍Aより予め定めた距離Lの最突出位置
Bまでを出没するようにして中空軸2内に嵌挿支持され
る。The upper end of the motor shaft 3a protrudes outward from the motor cover 3b of the motor 3, and
a. A single ventilation pipe 4 is passed through the internal cavity of the hollow shaft 2, and the lower end side 4a of this ventilation pipe 4 is placed at the most protruding position at a predetermined distance L from the vicinity of the screw end face A, as shown in FIG. It is inserted and supported within the hollow shaft 2 so that up to B extends and retracts.
【0010】この通気管4と中空軸2との間にはパッキ
ン5を介在せしめ、通気管外周面と中空軸内周面間の隙
間を通して汚水が中空軸にそって水位より上方へ侵入浮
上しないようになすとともにこの通気管4の上部外周に
ねじ4cを刻設し、モータ軸3aの内周面に直接刻設し
た雌ねじまたは図示のようにモータ軸内に嵌合固定した
ナット状のねじ部材7と螺合せしめ、かつこの通気管4
を回動させることにより中空軸先端のスクリュー端より
通気管4の下端の突出量を調整できるようになす。この
場合の通気管4の出没する最大許容範囲となる距離Lは
スクリュー先端またはスクリューを固定した中空軸下端
2aより、スクリューの回動にて汚水中に発生する負圧
にて気体(空気)を汚水中に吸入可能域として適当に定
め、最大突出点のB位置では水中の負圧が0で通気管4
の上端4bより吸気停止となるようにする。なおモータ
3の駆動によりモータ軸3a、中空軸2を介してスクリ
ュー1が回動してもこの中空軸内を貫通する通気管4は
回動しないようにして支持されているが、通気管4を中
空軸とともに回動させ、かつ通気管上端に回転継手を介
してシリンダ等に接続し、このシリンダの操作にて通気
管4を長手軸心方向に移動可能とすることもできる。A packing 5 is interposed between the vent pipe 4 and the hollow shaft 2 to prevent dirty water from entering and floating above the water level along the hollow shaft through the gap between the outer circumferential surface of the vent pipe and the inner circumferential surface of the hollow shaft. At the same time, a screw 4c is carved on the upper outer periphery of this ventilation pipe 4, and a female thread is carved directly on the inner peripheral surface of the motor shaft 3a, or a nut-shaped screw member is fitted and fixed inside the motor shaft as shown in the figure. 7, and this ventilation pipe 4.
By rotating the screw, the amount of protrusion of the lower end of the vent pipe 4 from the screw end at the tip of the hollow shaft can be adjusted. In this case, the distance L that is the maximum permissible range for the vent pipe 4 to protrude and retract is the distance L from the tip of the screw or the lower end 2a of the hollow shaft to which the screw is fixed. The area where suction is possible is determined appropriately in the wastewater, and at position B, which is the maximum protrusion point, the negative pressure in the water is 0 and the ventilation pipe 4 is closed.
Intake is stopped from the upper end 4b. Note that even if the screw 1 rotates through the motor shaft 3a and the hollow shaft 2 due to the drive of the motor 3, the ventilation pipe 4 passing through the hollow shaft is supported so as not to rotate. It is also possible to rotate the vent pipe 4 together with the hollow shaft and connect the upper end of the vent pipe to a cylinder or the like via a rotary joint, so that the vent pipe 4 can be moved in the longitudinal axis direction by operating the cylinder.
【0011】従って上述の如く構成する曝気装置におい
て汚水を好気・嫌気雰囲気にて処理する場合について以
下説明する。まず汚水中に空気を吹き込み、好気性発酵
にて汚水中の有機物質を分解処理するには、通気管4を
中空軸内をその長手軸心方向にそって通気管4の下端を
中空軸下端位置A点よりB点までの間にて突設固定する
。これは負荷に応じて効率的に汚水中へ吸気できるよう
にして定める。これによりモータ3を駆動させてスクリ
ュー1の回動によってスクリュー先端水域に発生する負
圧は通気管4内に作用し、通気管上端より吸気し、通気
管内を流下し、通気管下端より水中へ微細気泡として放
出され、汚水に散気され、汚水を好気状態とし、所要の
好気運転とする。[0011] Therefore, the case where wastewater is treated in an aerobic or anaerobic atmosphere in the aeration apparatus constructed as described above will be described below. First, air is blown into the wastewater, and in order to decompose organic substances in the wastewater by aerobic fermentation, the ventilation pipe 4 is inserted into the hollow shaft along its longitudinal axis, and the lower end of the ventilation pipe 4 is connected to the lower end of the hollow shaft. Protruding and fixing between point A and point B. This is determined so that air can be efficiently sucked into the wastewater depending on the load. This drives the motor 3 and the negative pressure generated in the water area at the tip of the screw by the rotation of the screw 1 acts on the inside of the ventilation pipe 4, sucks air from the top end of the ventilation pipe, flows down inside the ventilation pipe, and enters the water from the bottom end of the ventilation pipe. It is released as fine bubbles and diffused into the wastewater to bring the wastewater into an aerobic state and achieve the required aerobic operation.
【0012】次にスクリュー1を所定の回転数を保って
運転しつつ通気管4を中空軸下端より突出させるように
移動させ、B点に達する位置ではスクリュー先端水域で
発生する負圧は0となる。従って通気管4の下端がA点
よりB点に至るに従い水域内の発生負圧は徐々に減少し
、B点に達したとき負圧は0となるので吸気量は0とな
り汚水中への散気は停止する。この時でもスクリュー1
は所要の回転数で回動しているため汚水の撹拌は好気運
転時と同様に効率的に行われている。Next, while operating the screw 1 at a predetermined rotational speed, the vent pipe 4 is moved so as to protrude from the lower end of the hollow shaft, and at the position where it reaches point B, the negative pressure generated in the water area at the tip of the screw becomes 0. Become. Therefore, as the lower end of the ventilation pipe 4 moves from point A to point B, the negative pressure generated in the water area gradually decreases, and when it reaches point B, the negative pressure becomes 0, so the intake air amount becomes 0, and the air is dispersed into the wastewater. Qi stops. Even at this time, screw 1
Since it rotates at the required rotation speed, stirring of the wastewater is performed as efficiently as during aerobic operation.
【0013】なお通気管4をスクリュー端より出没させ
て通気量(汚水中への散気量)を調整する方法として通
気管の上部にシリンダまたはロッドを設け、これにより
行うこともできる。この場合、通気管とシリンダ間には
回転継手を用いる。これによって自動的に好気・嫌気運
転を切り換えられる。[0013] As a method of adjusting the amount of ventilation (the amount of air diffused into the waste water) by making the ventilation pipe 4 protrude and retract from the end of the screw, it is also possible to use a cylinder or a rod provided at the upper part of the ventilation pipe. In this case, a rotary joint is used between the vent pipe and the cylinder. This allows automatic switching between aerobic and anaerobic operation.
【0014】[0014]
【発明の効果】本発明によるときは中空状のモータ軸に
連結した中空軸内に通気管をスライド自在に挿通してこ
の通気管の先端を中空軸またはスクリュー下端からの突
出量を調整して汚水中への給気量を調整するようになし
ているため、スクリューの回転数を変えることなく通気
制御が行え、従来に比べ構成が簡易となる利点を有する
。[Effects of the Invention] According to the present invention, a ventilation pipe is slidably inserted into a hollow shaft connected to a hollow motor shaft, and the amount of protrusion of the tip of this ventilation pipe from the hollow shaft or the lower end of the screw is adjusted. Since the amount of air supplied to the wastewater is adjusted, ventilation control can be performed without changing the rotational speed of the screw, and has the advantage that the configuration is simpler than the conventional method.
【図1】本発明曝気装置の全体を示す実施例図である。FIG. 1 is an embodiment diagram showing the entire aeration apparatus of the present invention.
【図2】要部の拡大断面図である。FIG. 2 is an enlarged sectional view of main parts.
1 スクリュー 2 中空軸 3 モータ 3a モータ軸 4 通気管 1 Screw 2 Hollow shaft 3 Motor 3a Motor shaft 4 Ventilation pipe
Claims (1)
端に設けた中空軸を連結するとともにこのモータ軸・中
空軸内に一本の通気管を貫通して成り、この通気管の下
端の突出量を調整してスクリューの回転数に関係なく通
気量を調整可能としたことを特徴とする汚水処理用曝気
装置。Claim 1: A hollow shaft with a screw provided at the lower end is connected to a hollow motor shaft, and a vent pipe is passed through the motor shaft/hollow shaft, and the lower end of the vent pipe protrudes. An aeration device for sewage treatment, characterized in that the amount of aeration can be adjusted regardless of the rotational speed of the screw.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3064068A JPH04277088A (en) | 1991-03-05 | 1991-03-05 | Aeration device for waste liquid treatment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3064068A JPH04277088A (en) | 1991-03-05 | 1991-03-05 | Aeration device for waste liquid treatment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH04277088A true JPH04277088A (en) | 1992-10-02 |
Family
ID=13247408
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP3064068A Pending JPH04277088A (en) | 1991-03-05 | 1991-03-05 | Aeration device for waste liquid treatment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH04277088A (en) |
-
1991
- 1991-03-05 JP JP3064068A patent/JPH04277088A/en active Pending
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