JPH07196B2 - How to operate an endless waterway - Google Patents
How to operate an endless waterwayInfo
- Publication number
- JPH07196B2 JPH07196B2 JP3035431A JP3543191A JPH07196B2 JP H07196 B2 JPH07196 B2 JP H07196B2 JP 3035431 A JP3035431 A JP 3035431A JP 3543191 A JP3543191 A JP 3543191A JP H07196 B2 JPH07196 B2 JP H07196B2
- Authority
- JP
- Japan
- Prior art keywords
- endless
- water channel
- flow velocity
- installation angle
- peripheral side
- 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 - Fee Related
Links
- 238000005273 aeration Methods 0.000 claims description 36
- 238000009434 installation Methods 0.000 claims description 23
- 230000002093 peripheral effect Effects 0.000 claims description 23
- 238000000034 method Methods 0.000 claims description 12
- 238000005276 aerator Methods 0.000 claims description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 10
- 239000010802 sludge Substances 0.000 description 19
- 238000003756 stirring Methods 0.000 description 10
- 238000002156 mixing Methods 0.000 description 9
- 239000010865 sewage Substances 0.000 description 9
- 238000001514 detection method Methods 0.000 description 6
- 238000010586 diagram Methods 0.000 description 6
- 239000002351 wastewater Substances 0.000 description 4
- 238000004065 wastewater treatment Methods 0.000 description 4
- 238000011017 operating method Methods 0.000 description 3
- 230000003647 oxidation Effects 0.000 description 3
- 238000007254 oxidation reaction Methods 0.000 description 3
- 238000005259 measurement Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 101000927062 Haematobia irritans exigua Aquaporin Proteins 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 238000010564 aerobic fermentation Methods 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 238000000265 homogenisation Methods 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen 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)
Description
【0001】[0001]
【産業上の利用分野】本発明は無終端水路に設置した曝
気装置の設置角度を調節して水路内の汚水を均一に混合
する運転方法に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an operating method for uniformly mixing sewage in a waterway by adjusting the installation angle of an aeration device installed in an endless waterway.
【0002】[0002]
【従来の技術】下水汚水、産業廃棄汚水等の有機物を含
有する汚水の処理に際しては長円形の循環水路、二重円
形水路の如く、いわゆる無終端水路を形成した曝気槽に
曝気装置を設置し、この槽内の汚水中に空気中の酸素を
連続的に供給しつつ汚水を混合撹拌して曝気、すなわち
好気性発酵処理を行う方法が提案されている。2. Description of the Related Art In the treatment of sewage sewage, industrial waste sewage, and other sewage containing organic matter, an aeration device is installed in an aeration tank that forms a so-called endless channel such as an oval circulation channel or a double circular channel. A method has been proposed in which sewage is mixed with agitation while continuously supplying oxygen in the air to the sewage in the tank to aerate, that is, aerobically fermenting treatment is performed.
【0003】従来、下水処理は大都市において標準活性
汚泥法が中心となって普及してきたが、今日、地方の中
小都市に移行しつつある。地方においては技術者が少な
いため、簡便で、安定した処理水質が得られ、かつ観光
シーズン等で影響される流入汚水量の変動に対応できる
処理方式が望まれている。このような状況の中で円形、
又は長円形の無終端水路を有するオキシデーションディ
ッチは上記ニーズにマッチするものであり、着実に地方
へ普及している。一般に、オキシデーションディッチ法
に限らず、活性汚泥法は好気性発酵処理を行うため、曝
気装置による空気の供給と活性汚泥を汚水と接触させる
ための撹拌流速が必要である。この撹拌流速は通常、底
部流速が10cm/sec以上必要とされており、これ
以下の流速になると活性汚泥が堆積してしまう。また、
水路内外周に流速差を生じた場合、流速の遅い側へ活性
汚泥が集中して活性汚泥勾配が形成され、完全混合系と
はならないし、極端な場合にはその粘性により、活性汚
泥は堆積してしまい、十分な水処理が期待できない。Conventionally, sewage treatment has been popularized mainly in the standard activated sludge method in big cities, but nowadays it is shifting to local small and medium cities. Since there are few engineers in rural areas, there is a need for a treatment method that is simple, that provides stable treated water quality, and that can cope with fluctuations in the amount of inflowing wastewater that is affected by the tourist season. Circular in this situation,
Or, an oxidation ditch having an oval endless water channel meets the above needs and is steadily spreading to rural areas. In general, not only the oxidation ditch method but also the activated sludge method performs aerobic fermentation processing, and thus it is necessary to supply air by an aeration device and a stirring flow rate for contacting the activated sludge with waste water. This stirring flow rate is usually required to have a bottom flow rate of 10 cm / sec or higher, and if the flow rate is lower than this, activated sludge will be deposited. Also,
If there is a flow velocity difference between the inside and outside of the water channel, the activated sludge concentrates on the slower flow velocity side to form an activated sludge gradient, which does not form a complete mixing system. As a result, sufficient water treatment cannot be expected.
【0004】[0004]
【発明が解決しようとする課題】無終端水路における曝
気装置の設置角度は曝気装置の流速特性、動力特性等よ
り総合的見地から決定している。しかし横軸曝気装置は
大型で、かつ両軸端を水路の両端に固定するため、一度
設置するとその設置角度の変更は難しい。しかしなが
ら、実運転において、無終端水路に供給される汚水の流
量、水質、曝気槽内の活性汚泥量が刻々と変化すること
により、その流速特性が変化しても、その撹拌、曝気特
性はその流速特性に対応して変化することなく一定であ
るため、汚泥が水路底部に堆積、圧密して良好な汚水処
理が行われない欠点がある。The installation angle of the aeration device in the endless water channel is determined from a comprehensive point of view based on the flow velocity characteristics and power characteristics of the aeration device. However, since the horizontal axis aerator is large and both shaft ends are fixed to both ends of the water channel, it is difficult to change the installation angle once installed. However, in actual operation, even if the flow velocity characteristic changes due to the flow rate of sewage supplied to the endless water channel, the water quality, and the amount of activated sludge in the aeration tank changing momentarily, the stirring and aeration characteristics are Since it does not change according to the flow velocity characteristic and is constant, sludge is accumulated and compacted at the bottom of the water channel, and there is a drawback that good wastewater treatment cannot be performed.
【0005】本発明は、水路内の混合撹拌状況を常に検
知し、その検知情報に対応して曝気装置の設置角度を調
節し、常に水路内を均一に混合撹拌し、最適な汚水処理
を行うことを可能にする無終端水路の運転方法を提供す
ることを目的とする。The present invention constantly detects the mixing and stirring condition in the water channel, adjusts the installation angle of the aeration device in accordance with the detection information, always uniformly mixes and stirs the water channel, and performs the optimum wastewater treatment. It is an object of the present invention to provide a method for operating an endless water channel that enables the above.
【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、無終端水路内に曝気装置を設
置して水処理を行う無終端水路の運転方法において、無
終端水路内の内周側と外周側に設置した流速センサーに
より無終端水路の内周側と外周側の流速を検出し、検出
した無終端水路の内周側と外周側の流速の比が所定の範
囲から外れた場合、前記曝気装置の設置角度を調節し
て、無終端水路の内周側と外周側の流速の比が所定の範
囲内になるように自動制御することを要旨とする。SUMMARY OF THE INVENTION The present invention has been made to achieve the above object, and is an endless water channel operating method for treating water by installing an aerator in the endless water channel. The flow velocity sensors installed on the inner and outer circumferences of the inside detect the flow velocity on the inner and outer sides of the endless water channel, and the ratio of the detected flow velocity on the inner and outer sides of the endless water channel is within the specified range. If it is out of the range, the installation angle of the aeration device is adjusted to automatically control so that the ratio of the flow velocities on the inner peripheral side and the outer peripheral side of the endless water channel is within a predetermined range.
【0007】[0007]
【作用】長円形、あるいは円形の無終端水路は流線が外
周部に集まるため内周部の流速が遅く外周部が速い。こ
の内外周の均一化を省エネ運転で実現するため、無終端
水路内の内周側と外周側に設置した流速センサーにより
無終端水路の内周側と外周側の流速を検出し、無終端水
路の内周側と外周側の流速の比が所定の範囲から外れた
場合、前記曝気装置の設置角度を調節して、無終端水路
の内周側と外周側の流速の比が所定の範囲内になるよう
に制御し、常に無終端水路内を均一に混合撹拌して、最
適な条件で汚水処理が行われるようにする。In the oval or circular endless water channel, streamlines gather at the outer peripheral portion, so the flow velocity at the inner peripheral portion is slow and the outer peripheral portion is fast. In order to realize this homogenization of the inner and outer circumferences in energy-saving operation, the flow velocity sensors installed on the inner and outer circumferences of the endless water channel detect the flow velocity on the inner and outer circumferences of the endless water channel. If the ratio of the flow velocities on the inner circumference side and the outer circumference side is out of the predetermined range, the installation angle of the aeration device is adjusted so that the ratio of the flow velocities on the inner circumference side and the outer circumference side of the endless water channel falls within the predetermined range. Therefore, the endless water channel is always mixed and stirred uniformly so that the wastewater treatment is performed under the optimum conditions.
【0008】[0008]
【実施例】以下本発明を図示の実施例に基づいて説明す
る。図1に示すものは無終端水路が円形をなした二重円
形曝気槽を用いた実施例である。図において1は二重円
形曝気槽で、これは小径の円周壁11と大径の外周12
を同心上にして配設し、この内外両周壁11,12間に
所要幅と深さを有する循環式無終端水路13を形成す
る。2は自吸式スクリュー形の曝気装置で、図2に詳示
するようにモータ22に直結される中空シャフト23と
このシャフト23の先端に設けるスクリュー24とによ
り構成され、スクリューの回転により水流を起こすとと
もに、それに伴って発生するスクリュー先端部の負圧を
利用して空気を中空シャフトを介して吸引し、汚水中に
微細気泡として供給させ、気泡を水中に効率的に溶け込
むようになしたものである。曝気装置2は無終端水路1
3の上部を横切るように配設された取付フレーム21に
設けるが、前記モータ及び中空シャフトをカバーにて覆
い、このカバーを介してモータ等をフレームに取付角度
調整器25を介して取り付ける。DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described below based on the illustrated embodiments. FIG. 1 shows an embodiment using a double circular aeration tank having a circular endless water channel. In the figure, 1 is a double circular aeration tank, which has a small diameter circumferential wall 11 and a large diameter outer circumference 12.
Are arranged concentrically, and a circulating type endless water channel 13 having a required width and depth is formed between the inner and outer peripheral walls 11, 12. Reference numeral 2 denotes a self-priming screw type aerator, which is composed of a hollow shaft 23 directly connected to the motor 22 and a screw 24 provided at the tip of the shaft 23, as shown in FIG. Along with raising it, air is sucked through the hollow shaft by using the negative pressure of the screw tip that is generated along with it, and it is supplied as fine bubbles into the dirty water, and the bubbles are efficiently dissolved in the water. Is. Aeration device 2 is endless water channel 1
The motor and the hollow shaft are covered with a cover, and the motor and the like are mounted on the frame via the mounting angle adjuster 25 through the cover.
【0009】また、無終端水路13内には少なくともそ
の内周側と外周側に混合撹拌検知センサー3,3を取り
付ける。この混合撹拌検知センサー3としては流速計に
加えて、汚泥濃度計、DO計等を使用することができ
る。Further, in the endless water channel 13, the mixing and stirring detecting sensors 3, 3 are attached at least on the inner peripheral side and the outer peripheral side thereof. As the mixing and stirring detection sensor 3, a sludge concentration meter, a DO meter, or the like can be used in addition to the velocity meter.
【0010】次に図3に示す実験設備及び測定位置に基
づいて説明する。この実験設備は1日約600立方メー
トルの処理能力を有する二重円形式オキシデーションデ
ィッチで、曝気装置の設置を半径方向に垂直に交わる設
置角度を0゜とし、以後、設置角度を順次内周側に角度
変更した。混合撹拌状態(流速及び活性汚泥濃度)の測
定は、A〜Dの断面において、内周側から外周側に設け
たa〜dのポイント、合計16ヶ所で行った。Next, description will be made on the basis of the experimental equipment and measurement positions shown in FIG. This experimental equipment is a double circular oxidation ditch with a processing capacity of about 600 cubic meters per day, and the installation angle of the aerator is perpendicular to the radial direction is 0 °. I changed the angle. The measurement of the mixed stirring state (flow velocity and activated sludge concentration) was carried out at a total of 16 points a to d provided from the inner peripheral side to the outer peripheral side in the cross sections A to D.
【0011】〈結果〉 (1)底部平均流速は曝気装置の設置角度θを大きくし
て内周側に向けるほど速くなりθ=31゜の時、最大で
ありθ=45゜に至って頭打ち状態となった(図4)。 (2)曝気槽内の底部流速分布は内周側が遅く外周側が
速い(図5)。 (3)底部平均流速の内周側バランスはθが大きくなる
に従って均一化され、θ=45゜の時、内外比(a:
d)は1:1.4となり、最も完全混合に近い状態とな
った(図5)。 (4)曝気槽内の活性汚泥濃度はθ=31゜の時、ほぼ
均一となっているが、θ=6゜の時、槽内平均値810
mg/リットルに対して内周側は8000mg/リット
ル以上と高くなり、内周側に汚泥が堆積し、外周側は平
均値以下となって完全混合がなされていない。 (5)動力はθが大きくなるに従って増加した。θ=4
5゜の時、軸動力は3.73KWとなりモータの定格値
3.7KW以上となった(図7)。<Results> (1) The average flow velocity at the bottom becomes faster as the installation angle θ of the aerator is increased and it is directed toward the inner circumference side. When θ = 31 °, the average flow velocity reaches its maximum, reaching θ = 45 ° and reaching a peak condition. (Fig. 4). (2) The bottom flow velocity distribution in the aeration tank is slower on the inner side and faster on the outer side (Fig. 5). (3) The inner peripheral side balance of the bottom average flow velocity becomes uniform as θ increases, and when θ = 45 °, the internal / external ratio (a:
The ratio d) was 1: 1.4, which was the closest to perfect mixing (Fig. 5). (4) The concentration of activated sludge in the aeration tank is almost uniform when θ = 31 °, but when θ = 6 °, the average value in the tank is 810.
The inner peripheral side is as high as 8,000 mg / liter or higher with respect to mg / liter, sludge is accumulated on the inner peripheral side, and the outer peripheral side is below the average value and is not completely mixed. (5) The power increased as θ increased. θ = 4
At 5 °, the shaft power was 3.73 KW, which was above the motor rated value of 3.7 KW (Fig. 7).
【0012】以上の特性を持つ無終端水路の曝気装置の
運転方法順位は、 (1)曝気装置の動力はモータの定格値内になるように
設置角度を調整する。 (2)安定した水処理を行うために曝気槽内を完全混合
する。 (3)ランニングコストが安価となるような運転条件と
すべきである。 となるが、実運転においては、供用開始の低濃度活性汚
泥時には全般的に底部流速が速く、汚泥が堆積しにくい
こと、及び汚水の滞留時間が長く水処理が安定している
ことから、ただ単に内外周の流速比が等しい完全混合系
を作るために最適な曝気装置の設置角度に取り付けるの
ではなくて、ランニングコスト面をも十分重視した設置
角度とすることがより望ましい。一方、供用開始から時
間とともに発生汚水量、及び活性汚泥濃度が増加した場
合、曝気槽内ではやがて底部流速が低下して汚泥が堆積
してしまうため、この時点で再度、設置角度を変更して
汚泥を巻き上げ、完全混合系を作る必要がある。本実施
例では、図5に示す如く曝気槽内の内周側と外周側に混
合撹拌検知用センサー(具体的には、流速センサー)を
取り付け、角度調節可能な曝気装置と組み合わせて、常
に完全混合が行え、かつ安価なランニングコストとなる
ように曝気装置の設置角度を調節するものである。すな
わち、曝気槽の規模によって曝気装置の設置角度は多少
差異があるが、おおむね、0゜≦θ≦45゜の範囲であ
り、好ましくは内外周の底部流速比が1:2に近似した
設置角度で完全混合系を得ることができる。The order of operating method of the aerator of the endless water channel having the above characteristics is as follows: (1) The installation angle is adjusted so that the power of the aerator is within the rated value of the motor. (2) Completely mix the inside of the aeration tank for stable water treatment. (3) The operating conditions should be such that the running cost is low. However, in actual operation, when the low-concentration activated sludge at the start of service is used, the bottom flow velocity is generally high, sludge is hard to accumulate, and the retention time of wastewater is long and the water treatment is stable. It is more preferable not to simply install the aerator at an optimal installation angle in order to create a complete mixing system in which the flow rate ratios of the inner and outer circumferences are equal, but to set the installation angle with due consideration given to the running cost. On the other hand, if the amount of generated wastewater and the concentration of activated sludge increase with time from the start of service, the bottom flow velocity will eventually decrease in the aeration tank and sludge will accumulate, so at this point the installation angle must be changed again. It is necessary to roll up the sludge to make a completely mixed system. In the present embodiment, as shown in FIG. 5, sensors for mixing and stirring (specifically, flow velocity sensors) are attached to the inner and outer peripheral sides in the aeration tank, and combined with an aerator capable of adjusting the angle, it is always perfect. The installation angle of the aeration device is adjusted so that the mixing can be performed and the running cost is low. That is, although the installation angle of the aeration device is somewhat different depending on the scale of the aeration tank, it is generally in the range of 0 ° ≦ θ ≦ 45 °, and preferably the installation angle at which the bottom flow velocity ratio of the inner and outer circumferences approximates 1: 2. A completely mixed system can be obtained with.
【0013】このように曝気槽内の流速をリアルタイム
で測定し、曝気装置の設置角度としてフィードバックす
ることにより良好な水処理を行うことができるととも
に、ランニングコストを低廉にでき、また、曝気装置の
運転を自動化することができる。また、応用分野として
は長円形の無終端水路においてもコーナー部では底部流
速が内周で遅く、外周で速く、同様の傾向となることか
ら、本発明を適用することが可能である。図8のフロ−
チャ−トは、曝気装置の運転方法を示し、無終端水路内
の内周側に設置した流速センサーAと外周側に設置した
流速センサーBにより無終端水路の内周側と外周側の流
速を検出し、検出した無終端水路の内周側と外周側の流
速の比が所定の範囲(具体的には、1:2以内)から外
れた場合、2台の曝気装置の設置角度を調節して、無終
端水路の内周側と外周側の流速の比が所定の範囲内にな
るように自動制御するものである。また、図9の電気ブ
ロック図は、2つの検知センサー3,3により、流速分
布と汚泥堆積を演算し、これに基づいて曝気装置の設置
角度を調節する方法を示す説明図である。As described above, by measuring the flow velocity in the aeration tank in real time and feeding it back as the installation angle of the aeration device, it is possible to perform good water treatment, reduce the running cost, and reduce the aeration device. Driving can be automated. Further, as an application field, even in an oval endless water channel, the bottom flow velocity at the corner portion is slow at the inner circumference and fast at the outer circumference, and the same tendency is exhibited, so that the present invention can be applied. The flow of FIG.
The chart shows the operation method of the aerator, and the flow velocity sensor A installed on the inner peripheral side of the endless water channel and the flow velocity sensor B installed on the outer peripheral side show the flow velocity on the inner peripheral side and the outer peripheral side of the endless water channel. If the ratio of the flow velocities on the inner circumference side and the outer circumference side of the detected endless water channel deviates from the predetermined range (specifically, within 1: 2), the installation angles of the two aeration devices are adjusted. Then, it is automatically controlled so that the ratio of the flow velocities on the inner circumference side and the outer circumference side of the endless water channel is within a predetermined range. Further, the electric block diagram of FIG. 9 is an explanatory diagram showing a method of calculating the flow velocity distribution and sludge accumulation by the two detection sensors 3 and 3 and adjusting the installation angle of the aeration device based on the calculation.
【0014】[0014]
【発明の効果】本発明によれば、曝気装置の設置角度を
調節して、無終端水路の内周側と外周側の流速の比が所
定の範囲内になるように制御することができ、これによ
り、常に無終端水路内を均一に混合撹拌して、最適な条
件で汚水処理を行うことができる。According to the present invention, the installation angle of the aeration device can be adjusted so that the ratio of the flow velocities on the inner peripheral side and the outer peripheral side of the endless water channel is within a predetermined range. As a result, it is possible to always mix and stir the inside of the endless water channel uniformly and perform the wastewater treatment under optimum conditions.
【図1】本発明の無終端水路の運転方法を示す平面図で
ある。FIG. 1 is a plan view showing a method of operating an endless water channel according to the present invention.
【図2】曝気装置の説明図である。FIG. 2 is an explanatory diagram of an aeration device.
【図3】本発明の実験設備の説明図である。FIG. 3 is an explanatory diagram of experimental equipment of the present invention.
【図4】曝気装置の設置角度と全底部平均流速との関係
を示すグラフ図である。FIG. 4 is a graph showing the relationship between the installation angle of the aeration device and the average flow velocity at all bottoms.
【図5】底部流速分布図である。FIG. 5 is a bottom flow velocity distribution map.
【図6】汚泥濃度分布図である。FIG. 6 is a sludge concentration distribution map.
【図7】曝気装置設置角度と動力との関係図である。FIG. 7 is a relationship diagram between an aeration device installation angle and power.
【図8】本発明による曝気装置の運転方法のフロ−チャ
−ト図である。FIG. 8 is a flowchart showing the method of operating the aeration apparatus according to the present invention.
【図9】2つの検知センサーによる検出信号にて曝気装
置の設置角度を調節する電気ブロック図である。FIG. 9 is an electric block diagram that adjusts the installation angle of the aeration device based on detection signals from two detection sensors.
1 無終端水路を有する曝気槽 13 無終端水路 2 曝気装置 3 検知センサー 1 Aeration tank with endless water channel 13 Endless water channel 2 Aeration device 3 Detection sensor
Claims (1)
理を行う無終端水路の運転方法において、無終端水路内
の内周側と外周側に設置した流速センサーにより無終端
水路の内周側と外周側の流速を検出し、検出した無終端
水路の内周側と外周側の流速の比が所定の範囲から外れ
た場合、前記曝気装置の設置角度を調節して、無終端水
路の内周側と外周側の流速の比が所定の範囲内になるよ
うに自動制御することを特徴とする無終端水路の運転方
法。1. A method of operating an endless waterway in which an aerator is installed in the endless waterway to perform water treatment, wherein in the endless waterway, a flow velocity sensor is installed on the inner and outer circumference sides of the endless waterway. When the flow velocities on the circumference side and the outer circumference side are detected and the ratio of the flow velocities on the inner circumference side and the outer circumference side of the detected endless water channel deviates from a predetermined range, the installation angle of the aeration device is adjusted to A method for operating an endless water channel, which is characterized by automatically controlling so that the ratio of the flow velocities on the inner peripheral side and the outer peripheral side falls within a predetermined range.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3035431A JPH07196B2 (en) | 1991-02-05 | 1991-02-05 | How to operate an endless waterway |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3035431A JPH07196B2 (en) | 1991-02-05 | 1991-02-05 | How to operate an endless waterway |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH04349993A JPH04349993A (en) | 1992-12-04 |
| JPH07196B2 true JPH07196B2 (en) | 1995-01-11 |
Family
ID=12441671
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP3035431A Expired - Fee Related JPH07196B2 (en) | 1991-02-05 | 1991-02-05 | How to operate an endless waterway |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH07196B2 (en) |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6028890A (en) * | 1983-07-27 | 1985-02-14 | Hitachi Kiden Kogyo Ltd | How to operate an aeration system |
| JPS63294997A (en) * | 1987-05-27 | 1988-12-01 | Hitachi Kiden Kogyo Ltd | Method for operating aeration device |
-
1991
- 1991-02-05 JP JP3035431A patent/JPH07196B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH04349993A (en) | 1992-12-04 |
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