JPH0352696A - Method for controlling operation of blower for aeration - Google Patents

Method for controlling operation of blower for aeration

Info

Publication number
JPH0352696A
JPH0352696A JP1187035A JP18703589A JPH0352696A JP H0352696 A JPH0352696 A JP H0352696A JP 1187035 A JP1187035 A JP 1187035A JP 18703589 A JP18703589 A JP 18703589A JP H0352696 A JPH0352696 A JP H0352696A
Authority
JP
Japan
Prior art keywords
value
lower limit
blower
blowers
sensor
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
Application number
JP1187035A
Other languages
Japanese (ja)
Inventor
Atsushi Hibino
淳 日比野
Kozo Ashizawa
公三 芦沢
Masaru Yamamoto
勝 山本
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Resonac Corp
Original Assignee
Hitachi Chemical Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Hitachi Chemical Co Ltd filed Critical Hitachi Chemical Co Ltd
Priority to JP1187035A priority Critical patent/JPH0352696A/en
Publication of JPH0352696A publication Critical patent/JPH0352696A/en
Pending legal-status Critical Current

Links

Classifications

    • 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

Landscapes

  • Activated Sludge Processes (AREA)

Abstract

PURPOSE:To save the energy of a blower operation by controlling blowers to 3 stages; low, middle and high speed revolutions in order to maintain a DO(dissolved oxygen) value within upper and lower limit values by utilizing a DO sensor with upper and lower limit alarms mounted in an aeration tank. CONSTITUTION:The DO value in the aeration tank 1 is measured by the DO sensor 2 with the upper and lower limit alarms and is sent to a DO sensor body 3. The blowers 5 are controlled in revolution at a certain specified revolving speed (middle speed) by an inverter 4 while the DO value exists between the upper and lower limit values preset in the DO sensor body 3. An upper limit alarm signal is outputted from the DO sensor body 3 when the DO value exceeds the upper limit value. The inverter 4 lowers the revolving speed of the blowers 5 by this signal. The blowers 5 are similarly revolved at the high speed when the DO value falls below the lower limit value. The revolving speeds of the blowers are thus controlled in three stages by load fluctuations and, therefore, the rate of saving the energy is improved.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、ばっ気式浄化槽に使用するばっ気用ブロワの
運転制御方法に関する。
DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a method for controlling the operation of an aeration blower used in an aeration type septic tank.

(従来の技術) 従来、ばっ気槽の過ばっ気によるpH低下によって水質
の悪化するのを防止するため、あるいは省エネルギーの
観点から、ばっ気槽にDOセンサを取付け、その検出D
O値に比例してインバータによりブロワの回転数を制御
する方法があった。
(Prior art) Conventionally, in order to prevent the water quality from deteriorating due to a drop in pH due to overaeration in the aeration tank, or from the viewpoint of energy conservation, a DO sensor was attached to the aeration tank, and its detection D
There is a method of controlling the rotation speed of the blower using an inverter in proportion to the O value.

《発明が解決しようとする課題} ところで、ばっ気槽内のDO(溶存酸素)値は、第2図
に示すように、流入負荷の変動によって細かくふらつい
ている。このため、従来のようなDO値に比例した制御
では、このふらつきによってインバータやブロワに「う
なり」等の現象が発生し、機械的な寿命を短くする原因
となっていた。
<<Problems to be Solved by the Invention>> Incidentally, as shown in FIG. 2, the DO (dissolved oxygen) value in the aeration tank fluctuates finely due to fluctuations in the inflow load. For this reason, in conventional control proportional to the DO value, this fluctuation causes phenomena such as "beating" in the inverter or blower, which shortens the mechanical life of the inverter or blower.

また、インバータとDOセンサを繋ぐ演算器は高価であ
り、取扱いも困難であるため、専任の管理者が特別に必
要とされていた。
Furthermore, the computing unit that connects the inverter and the DO sensor is expensive and difficult to handle, so a special administrator is required.

上記問題に鑑み、本発明は、ばっ気槽内のDO値のふら
つきによるインバータ等のうなり現象をなくし、かつ専
任の管理者を不要にするばっ気用ブロワの運転制御方法
を提供しようとするものである。
In view of the above problems, the present invention aims to provide a method for controlling the operation of an aeration blower, which eliminates the humming phenomenon of the inverter, etc. due to fluctuations in the DO value in the aeration tank, and eliminates the need for a dedicated manager. It is.

《課題を解決するための手段〉 これらの問題点を解決するために、本発明において採用
された手段を、第1図に示す実施例の符号を用いて説明
する。
<<Means for Solving the Problems>> Means adopted in the present invention to solve these problems will be explained using the reference numerals of the embodiment shown in FIG.

第1図は本発明を表わすシステムの概略図である。ばっ
気槽1内のDO値は、上・下限警報装置付DOセンサ2
により測定され、DOセンサ本体3に送られる。ここで
、DO値がDOセンサ本体3に予め設定された上限値お
よび下限値の間にある場合は、インバータ4はブロワ(
ブロワモータ)5をある一定の回転数で制御する。しか
し、DO値が上限値を越えている場合は、DOセンサ本
体3より上限警報信号が出力されるため、インバータ4
はこの信号を感知してブロワ5の回転数を低下させる。
FIG. 1 is a schematic diagram of a system representing the invention. The DO value in the aeration tank 1 is determined by a DO sensor 2 with an upper/lower limit alarm device.
is measured and sent to the DO sensor main body 3. Here, if the DO value is between the upper limit and lower limit set in advance in the DO sensor main body 3, the inverter 4 operates as a blower (
The blower motor) 5 is controlled at a certain rotation speed. However, if the DO value exceeds the upper limit, an upper limit alarm signal is output from the DO sensor body 3, so the inverter 4
detects this signal and reduces the rotation speed of the blower 5.

これによって、ばっ気量は減少し、DO値は上限値を下
回るようになる。
As a result, the amount of aeration decreases and the DO value falls below the upper limit.

これとは逆に、DO値が下限値を下回った場合は、下限
警報か出力され、インバータ4はブロワ5の回転数を上
昇させるため、ばっ気量が増加し、下限値を上回る。
On the contrary, if the DO value falls below the lower limit, a lower limit alarm is output and the inverter 4 increases the rotation speed of the blower 5, so that the aeration amount increases and exceeds the lower limit.

このように、本発明におけるブロワの運転制御方法にあ
っては、上・下限警報装置付DOセンサによる上限値と
下限値の間にDO値を調整するために、インバータ4が
ブロワの回転数を低・中・高速の3段階に制御すること
を特徴とする。
As described above, in the blower operation control method of the present invention, in order to adjust the DO value between the upper limit value and the lower limit value determined by the DO sensor with upper/lower limit alarm device, the inverter 4 controls the rotation speed of the blower. It is characterized by three levels of control: low, medium, and high speed.

したがって、ブロワ5が3段階に制御され、上・下限値
の所定範囲内にばっ気槽のDO値が収まるので、流入負
荷が変動してもDO値が細かくふらつくようなことがな
い。その結果、インバータ4やブロワ5に「うなり」等
の現象が発生することがなくなる。
Therefore, the blower 5 is controlled in three stages, and the DO value of the aeration tank is kept within a predetermined range of upper and lower limit values, so that the DO value does not fluctuate minutely even if the inflow load fluctuates. As a result, phenomena such as "beating" will not occur in the inverter 4 or the blower 5.

(実施例) 以下、本発門の一実施例を第1図を参照しながら詳しく
説明する。
(Example) Hereinafter, an example of the present invention will be described in detail with reference to FIG.

昭和55年建設省告示第1292号では、「ばっ気槽内
のDO値は、おおむねlppmに保持すること」となっ
ている。このため、本実施例では余裕をみて、上・下限
警報装置付DOセンサ本体3の上限値を4ppm,下限
値を2ppmと設定した。また、これに対応するインバ
ータ4の出力周波数の設定値を、ブロワ5のモータ回転
数を低・中・高速回転の3段階に運転できるようにした
According to the Ministry of Construction Notification No. 1292 of 1981, ``the DO value in the aeration tank must be maintained at approximately lppm.'' Therefore, in this embodiment, the upper limit value of the DO sensor main body 3 with upper/lower limit warning device was set to 4 ppm and the lower limit value was set to 2 ppm, taking into consideration a margin. In addition, the setting value of the output frequency of the inverter 4 corresponding to this allows the motor rotation speed of the blower 5 to be operated in three stages: low, medium, and high speed rotation.

すなわち、この出力周波数は、ばっ気槽1内のDO値が
」二限値を越えている場合は30Hz,上限値と下限値
の間にある場合は40Hz,下限値を下回っている場合
は50Hzとした。
That is, this output frequency is 30Hz when the DO value in the aeration tank 1 exceeds the second limit, 40Hz when it is between the upper and lower limits, and 50Hz when it is below the lower limit. And so.

ここにばっ気槽1の有効容量は48.57m3である。Here, the effective capacity of the aeration tank 1 is 48.57 m3.

また、図中符号6は、流量調整槽,符号7は沈jB槽,
符号8は消毒槽である。これらばっ気槽1,流量調整槽
6,沈澱槽7および消毒槽8にて構成される合併処理浄
化槽は、日平均汚水量60m3/日であって、放流水質
BOD20ppm以下の処理能力をもつ浄化槽である。
Further, in the figure, numeral 6 is a flow rate adjustment tank, numeral 7 is a sinking jB tank,
Reference numeral 8 is a disinfection tank. The combined treatment septic tank consisting of the aeration tank 1, flow rate adjustment tank 6, sedimentation tank 7, and disinfection tank 8 is a septic tank with a processing capacity of 60 m3/day of average sewage volume and effluent water quality BOD of 20 ppm or less. be.

さらに、ばっ気槽1に空気を供給するためのブロワ5の
出力は3.7KWである。
Furthermore, the output of the blower 5 for supplying air to the aeration tank 1 is 3.7 KW.

表は本実施例による水質処理性能を示したものである。The table shows the water quality treatment performance of this example.

この表から明らかなように、本発明により制御を行った
場合の放流水のBODは、制御しなかった場合と比較し
て、同等以上であり、かつ省エネルギー効率も45%あ
った。
As is clear from this table, the BOD of the discharged water when controlled according to the present invention was equal to or higher than when it was not controlled, and the energy saving efficiency was also 45%.

(発明の効果) 以」二述べたように、本発明は実施例からも明らかな如
く、次の効果を有する。
(Effects of the Invention) As described above, the present invention has the following effects as is clear from the examples.

1.ばっ気用ブロワのばっ気能力は、浄化槽の最大処理
能力に見合うように設計してあり、また、流入負荷の変
動にかかわらず常に一定の運転を行っていたが、本発明
による運転方法では、DO値が所定範囲に収まるようブ
ロワ回転数が低・中・高速に制御されるので、従来方法
に比べて十分な省エネルギー効果が得られる。
1. The aeration capacity of the aeration blower was designed to match the maximum processing capacity of the septic tank, and the aeration blower was always operated at a constant level regardless of fluctuations in the inflow load, but with the operating method of the present invention, Since the blower rotation speed is controlled at low, medium, and high speeds so that the DO value falls within a predetermined range, a sufficient energy saving effect can be obtained compared to the conventional method.

2.本発明によるブロワの運転方法は3段階制御である
ため、ばっ気槽内のDOの細かいふらつきによってイン
バータやブロワの運転が影響されず、従来のようなうな
り現象は解消し、機械的寿命が長くなる。
2. Since the blower operating method according to the present invention is a three-stage control, the operation of the inverter and blower is not affected by small fluctuations in the DO in the aeration tank, eliminating the conventional whirring phenomenon and extending the mechanical life. Become.

3.上・下限警報装置付DOセンサは演算器に比べて安
価で信頼性の高いものが多いため、コスト面および性能
面でも有利になる。
3. DO sensors with upper/lower limit warning devices are often cheaper and more reliable than arithmetic units, so they are advantageous in terms of cost and performance.

4.上記DOセンサの取扱いは誰でも簡単にできるため
、専任の管理者を必要としない。つまり、本発明におい
ては、演算器等の複雑なものは一切使用していないため
、誰にでも維持管理が可能である。
4. Anyone can easily handle the above-mentioned DO sensor, so there is no need for a dedicated administrator. In other words, the present invention does not use any complicated components such as arithmetic units, so anyone can maintain and manage the system.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は本允門方法で使用されるブロワの迂転制御装置
を示す概略システム図、第2図はばつ気槽内におけるD
O値の経時変化を表わす特性図である。 1・・・ばっ気槽 2・・・DOセンサ 3・・・上・下限警報装置付DOセンサ本体4・・・イ
ンバータ 5・・・ブロワ 6・・・流量調整{曹 7・・・沈澱槽 8・・・消毒槽
Figure 1 is a schematic system diagram showing the blower detour control device used in the present Yumen method, and Figure 2 is a diagram showing the D in the aeration tank.
FIG. 3 is a characteristic diagram showing changes in O value over time. 1... Aeration tank 2... DO sensor 3... DO sensor body with upper/lower limit alarm device 4... Inverter 5... Blower 6... Flow rate adjustment {Soda 7... Sedimentation tank 8... Disinfection tank

Claims (1)

【特許請求の範囲】[Claims] 1、ばっ気槽に空気を供給するためのばっ気用ブロワの
運転制御方法において、ばっ気槽内に取付けた上・下限
警報装置付DOセンサを利用して、DO値を前記DOセ
ンサによる上限値と下限値の間に収めるために、ブロワ
をインバータにより低・中・高速回転の3段階に制御す
ることを特徴とするばっ気用ブロワの運転制御方法。
1. In a method for controlling the operation of an aeration blower for supplying air to an aeration tank, a DO sensor with an upper/lower limit alarm device installed in the aeration tank is used to set the DO value to the upper limit determined by the DO sensor. A method for controlling the operation of an aeration blower, characterized in that the blower is controlled in three stages of low, medium, and high speed rotation using an inverter in order to keep the rotation between the above and the lower limit values.
JP1187035A 1989-07-19 1989-07-19 Method for controlling operation of blower for aeration Pending JPH0352696A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1187035A JPH0352696A (en) 1989-07-19 1989-07-19 Method for controlling operation of blower for aeration

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1187035A JPH0352696A (en) 1989-07-19 1989-07-19 Method for controlling operation of blower for aeration

Publications (1)

Publication Number Publication Date
JPH0352696A true JPH0352696A (en) 1991-03-06

Family

ID=16199039

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1187035A Pending JPH0352696A (en) 1989-07-19 1989-07-19 Method for controlling operation of blower for aeration

Country Status (1)

Country Link
JP (1) JPH0352696A (en)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH05161898A (en) * 1991-12-13 1993-06-29 Nippon Kentetsu Co Ltd Dissolved oxygen control apparatus for waste water treating apparatus
US6200469B1 (en) * 1997-06-23 2001-03-13 North American Wetland Engineering System for removing pollutants from water
JP2002320990A (en) * 2001-04-26 2002-11-05 Hitachi Kiden Kogyo Ltd Automatic operation control method for aerator
US6652743B2 (en) 1997-06-23 2003-11-25 North American Wetland Engineering, Inc. System and method for removing pollutants from water
US7455775B2 (en) 2005-11-10 2008-11-25 Fuji Clean Co., Ltd. Water treatment method and apparatus
US7874546B2 (en) * 2007-08-22 2011-01-25 Jong Hoo Park Integrated nano-bubble generating apparatus
US7879246B2 (en) 2005-02-09 2011-02-01 Fuji Clean Co., Ltd Water treatment apparatus
JP2013078732A (en) * 2011-10-04 2013-05-02 Kubota Kankyo Service Kk Operation method, operation control device, and control method for sewage plant
CN104817195A (en) * 2015-04-08 2015-08-05 浙江大学 Low-energy consumption sewage aeration system capable of supplying oxygen by phases and partition

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS50141887A (en) * 1974-05-01 1975-11-14
JPS53123830A (en) * 1977-04-05 1978-10-28 Mitsubishi Electric Corp Control system by current type inverter driver induction motors

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS50141887A (en) * 1974-05-01 1975-11-14
JPS53123830A (en) * 1977-04-05 1978-10-28 Mitsubishi Electric Corp Control system by current type inverter driver induction motors

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH05161898A (en) * 1991-12-13 1993-06-29 Nippon Kentetsu Co Ltd Dissolved oxygen control apparatus for waste water treating apparatus
US6200469B1 (en) * 1997-06-23 2001-03-13 North American Wetland Engineering System for removing pollutants from water
US6406627B1 (en) 1997-06-23 2002-06-18 North American Wetland Engineering, Inc. Method for removing pollutants from water
US6652743B2 (en) 1997-06-23 2003-11-25 North American Wetland Engineering, Inc. System and method for removing pollutants from water
JP2002320990A (en) * 2001-04-26 2002-11-05 Hitachi Kiden Kogyo Ltd Automatic operation control method for aerator
US7879246B2 (en) 2005-02-09 2011-02-01 Fuji Clean Co., Ltd Water treatment apparatus
US7455775B2 (en) 2005-11-10 2008-11-25 Fuji Clean Co., Ltd. Water treatment method and apparatus
US7622042B2 (en) 2005-11-10 2009-11-24 Fuji Clean Co., Ltd. Water treatment apparatus and method
US7874546B2 (en) * 2007-08-22 2011-01-25 Jong Hoo Park Integrated nano-bubble generating apparatus
JP2013078732A (en) * 2011-10-04 2013-05-02 Kubota Kankyo Service Kk Operation method, operation control device, and control method for sewage plant
CN104817195A (en) * 2015-04-08 2015-08-05 浙江大学 Low-energy consumption sewage aeration system capable of supplying oxygen by phases and partition
CN104817195B (en) * 2015-04-08 2019-11-22 浙江大学 The low energy consumption sewage aeration system of subregion oxygen supply stage by stage

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