JPS5823073B2 - How to adjust dissolved oxygen - Google Patents
How to adjust dissolved oxygenInfo
- Publication number
- JPS5823073B2 JPS5823073B2 JP54039604A JP3960479A JPS5823073B2 JP S5823073 B2 JPS5823073 B2 JP S5823073B2 JP 54039604 A JP54039604 A JP 54039604A JP 3960479 A JP3960479 A JP 3960479A JP S5823073 B2 JPS5823073 B2 JP S5823073B2
- Authority
- JP
- Japan
- Prior art keywords
- dissolved oxygen
- amount
- measured value
- deviation
- stirring motor
- 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
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 title claims description 20
- 229910052760 oxygen Inorganic materials 0.000 title claims description 20
- 239000001301 oxygen Substances 0.000 title claims description 20
- 238000003756 stirring Methods 0.000 claims description 16
- 238000000034 method Methods 0.000 claims description 9
- 244000005700 microbiome Species 0.000 description 11
- 238000005273 aeration Methods 0.000 description 3
- 239000007858 starting material Substances 0.000 description 3
- 238000012258 culturing Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- 240000004808 Saccharomyces cerevisiae Species 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 230000036284 oxygen consumption Effects 0.000 description 1
- 238000003908 quality control method Methods 0.000 description 1
- 230000002441 reversible effect Effects 0.000 description 1
- 239000010802 sludge 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
- Micro-Organisms Or Cultivation Processes Thereof (AREA)
- Activated Sludge Processes (AREA)
Description
【発明の詳細な説明】
この発明は微生物培養液や汚泥中の溶存酸素を要求量に
収束せしめることにより、微生物の培養を容易ならしめ
る方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for facilitating the cultivation of microorganisms by converging the dissolved oxygen in a microorganism culture solution or sludge to the required amount.
溶液中の溶存酸素量を調整することは酵母細菌等の微生
物の収率を増大させる上で必須不可欠の要素とされてい
るが、従来、この調整は人手により勘と熟練に頼って行
なわれていたため非常なバラツキが生じていたばかりで
なく、培養には通常24〜72時間の連続運転を行なう
ものであるため作業的にもかなりの重労働であって、こ
れを自動化することが要望されていた。Adjusting the amount of dissolved oxygen in a solution is considered to be an essential element in increasing the yield of microorganisms such as yeast bacteria, but this adjustment has traditionally been done manually, relying on intuition and skill. Therefore, not only was there a great deal of variation, but also the cultivation required continuous operation for 24 to 72 hours, which required considerable labor, and there was a desire to automate this process.
これに対して、近年自動化された微生物の培養に特公昭
45−18273号公報の技術が公表されているが、こ
れは培養液中の溶存酸素量をある設定された上限、下限
の範囲内に設定し、溶存酸素量の測定値が上限、下限を
逸脱した場合に適正な酸素量を供給するごとく攪拌又は
通気を増減し、測定値が上記範囲(許容範囲)内にある
場合には攪拌又は通気を増減しないようにしたものであ
り、これにより培養の自動運転が可能となったものであ
る。On the other hand, in recent years, the technology disclosed in Japanese Patent Publication No. 45-18273 has been published for automated culture of microorganisms, but this technology limits the amount of dissolved oxygen in the culture solution to within a set upper and lower limit. If the measured amount of dissolved oxygen exceeds the upper or lower limits, increase or decrease stirring or aeration to supply the appropriate amount of oxygen, and if the measured value is within the above range (tolerable range), stir or aerate. This design prevents the amount of aeration from increasing or decreasing, which makes it possible to automatically operate the culture.
しかしながら、上記技術は上限、下限の2位置を設定し
て、溶存酸素量が許容範囲内にある場合には攪拌、通気
のいづれの場合も前の状態を保持している。However, in the above technique, two positions, an upper limit and a lower limit, are set, and when the amount of dissolved oxygen is within an allowable range, the previous state is maintained in both stirring and aeration.
しかし、測定値が許容範囲を逸脱した場合は、酸素消費
量は短時間に数倍以上に変化するため、一旦逸脱した後
に許容範囲内に戻すには、かなりの長時間を要して培養
される微生物に悪影響を及ぼし、特に酸素量に鋭敏な微
生物の場合には培養が不可能となる可能性があった。However, if the measured value deviates from the permissible range, the oxygen consumption will change several times or more in a short period of time, so it will take a considerable amount of time to bring the value back within the permissible range. This has a negative effect on the microorganisms that are exposed to the microorganisms, and there is a possibility that culturing of microorganisms that are particularly sensitive to oxygen levels may become impossible.
この発明は、上記の欠点を解消するためになされたもの
で、溶存酸素量を自動的に調整することは勿論、溶存酸
素量を常に所定の設定値の近傍に調節することができる
方法を提供するものであり、以下に詳細に説明する。This invention was made to eliminate the above-mentioned drawbacks, and provides a method that not only automatically adjusts the amount of dissolved oxygen but also allows the amount of dissolved oxygen to be constantly adjusted to be close to a predetermined set value. This will be explained in detail below.
第1図はこの発明方法を示す概略図であり1は微生物ヲ
培養するためのジャーで、槽1a内に攪拌子2と溶液中
の溶存酸素量を測定するための電極3が具備しており、
スターテ1bには攪拌用モータ4と、この攪拌用モータ
4に連結する攪拌子2の回転数を後述するシーケンスに
伝達するジェネレータ5が内蔵される。FIG. 1 is a schematic diagram showing the method of this invention. Reference numeral 1 is a jar for culturing microorganisms, and a tank 1a is equipped with a stirrer 2 and an electrode 3 for measuring the amount of dissolved oxygen in the solution. ,
The starter 1b includes a stirring motor 4 and a generator 5 that transmits the rotational speed of the stirrer 2 connected to the stirring motor 4 in a sequence to be described later.
上記攪拌子2は攪拌用モータ4の回転駆動力がマグネッ
ト等の適宜の手段で伝達されて槽1a内の溶液を攪拌す
るためのもので、このスターテ1bの攪拌により空気中
の酸素を溶液内に溶解するようになっている。The stirring bar 2 is used to stir the solution in the tank 1a by transmitting the rotational driving force of the stirring motor 4 by an appropriate means such as a magnet, and the stirring of the starter 1b removes oxygen from the air into the solution. It is designed to dissolve in
上記測定用の電極3は記録計6と時間比例式調節計7に
連結しており、電極3の測定値がこれらの記録計6と時
間比例式調節計7に共に伝達され、記録計6で前記測定
値をスターテ1bの回転数と相関せしめてグラフに記録
し、時間比例式調節計7で測定値を感知すると同時に該
測定値とあらかじめ設定しておいた設定値との偏差を計
算し、この偏差に応じて攪拌用モータ4の増速または減
速作動時間比率を決定し、これを電気的信号に変換して
シーケンス8を介して、モータ4に伝達し、該モータ4
を駆動するものである。The measurement electrode 3 is connected to a recorder 6 and a time proportional controller 7, and the measured value of the electrode 3 is transmitted to both the recorder 6 and the time proportional controller 7, and the recorder 6 transmits the measured value to the recorder 6 and the time proportional controller 7. Correlating the measured value with the rotation speed of the starter 1b and recording it on a graph, sensing the measured value with the time proportional controller 7 and simultaneously calculating the deviation between the measured value and a preset setting value, The speed increase or deceleration operation time ratio of the stirring motor 4 is determined according to this deviation, and this is converted into an electrical signal and transmitted to the motor 4 via the sequence 8.
It is what drives the.
上記のシーケンス8は上記時間比例式調節計7からの電
気信号を内蔵するポテンショメータとこのポテンショメ
ータを駆動する可逆転モータとにより増速または減速量
に変換し、これを攪拌用モータ4に伝達すると共に、ジ
ェネレータ5からの信号を受け、これを記録計6に伝達
する記録用信号とするものである。The above sequence 8 converts the electric signal from the time proportional controller 7 into an amount of speed increase or deceleration using a built-in potentiometer and a reversible motor that drives this potentiometer, and transmits this to the stirring motor 4. , receives a signal from the generator 5 and uses it as a recording signal to be transmitted to the recorder 6.
このように構成されたこの発明は、まず、培養する微生
物の種類、培養量に応じてあらかじめ必要な溶存酸素量
を設定し、時間比例式調節計7に記憶させておく。In the present invention configured as described above, first, a required amount of dissolved oxygen is set in advance according to the type of microorganism to be cultured and the amount of culture, and is stored in the time proportional controller 7.
次に槽1a内に設置した電極3により溶液内の溶存酸素
量を測定し、これを記録計6に伝達して記録すると共に
、時間比例式調節計7に伝達する。Next, the amount of dissolved oxygen in the solution is measured by the electrode 3 installed in the tank 1a, and this is transmitted to the recorder 6 for recording, and is also transmitted to the time proportional controller 7.
時間比例式調節計7では前述のように測定値と設定値と
の偏差を算出して攪拌用モータ4の増速または減速の作
動時間比率を決定し、これをシーケンス8を介して攪拌
用モータ4に伝達して偏差をゼロにするように攪拌子2
を増速または減速しつつ回転し、渦巻流を生起して、空
気中の酸素を必要量だけ溶解せしめる。The time proportional controller 7 calculates the deviation between the measured value and the set value as described above, determines the operating time ratio for speeding up or decelerating the stirring motor 4, and transmits this to the stirring motor 4 through the sequence 8. 4 to make the deviation zero.
It rotates while speeding up or slowing down, creating a swirling flow that dissolves the required amount of oxygen in the air.
同時にこのスターク1bの回転数を記録計6で記録する
ことにより、第2図のような測定値、設定値及び回転数
の相関グラフを得る。At the same time, by recording the rotational speed of the stark 1b with a recorder 6, a correlation graph of measured values, set values, and rotational speed as shown in FIG. 2 is obtained.
従って、例えば駆動直後における測定値の偏差が大きい
としても、偏差がプラス、マイナスを繰返して序々に設
定値に近づき、一定時間経過後にはほとんど設定値に収
束して測定値の変動がなくなり、微生物培養の良好な環
境が得られるものである。Therefore, for example, even if the deviation of the measured value immediately after driving is large, the deviation repeats plus and minus and gradually approaches the set value, and after a certain period of time, it almost converges to the set value and the fluctuation of the measured value disappears, and the microorganism A good environment for culture can be obtained.
この場合、培養する微生物の種類、量により必要とする
酸素量は異なるが、それに応じて攪拌用モータの能力は
適宜選択すればよい。In this case, the amount of oxygen required varies depending on the type and amount of microorganisms to be cultured, and the capacity of the stirring motor may be selected accordingly.
以上、詳述したように、この発明の方法による場合は、
溶存酸素量調整を全く自動化して行なうことが可能で従
事する人員の削減ができ、熟練も要さず、作業性も良好
であるばかりでな(、溶存酸素量を設定値に序々に収束
せしめることができるため、一定時間後には測定値の変
動がほとんどなくなり、非常に良好な培養環境が得られ
る等、優れた効果を奏することができると共にこの発明
によるとPID制御方式よりも安価にかつ単純なon
−off制御方式よりも質の高い制御が可能である。As detailed above, in the case of the method of this invention,
It is possible to completely automate the adjustment of the amount of dissolved oxygen, which reduces the number of personnel involved, does not require any skill, and is not only easy to work with, but also allows the amount of dissolved oxygen to gradually converge to the set value. As a result, fluctuations in measured values are almost eliminated after a certain period of time, and a very good culture environment can be obtained, resulting in excellent effects, and according to the present invention, it is cheaper and simpler than the PID control method. On
-Higher quality control than the off control method is possible.
第1図はこの発明による回路図、第2図はこの発明によ
り得られる相関グラフである。
1・・・・・・ジャー、1b・・・・・・スターク、2
・・・・・・攪拌子、3・・・・・・電極、4・・・・
・・攪拌用モータ、5・・・・・・ジェネレータ、6・
・・・・・記録計、7・・・・・・時間比例式調節計、
8・・・・・・シーケンス。FIG. 1 is a circuit diagram according to the present invention, and FIG. 2 is a correlation graph obtained according to the present invention. 1...Jar, 1b...Stark, 2
... Stirrer, 3... Electrode, 4...
... Stirring motor, 5... Generator, 6.
...Recorder, 7...Time proportional controller,
8...Sequence.
Claims (1)
と設定値との偏差に応じて、該偏差をゼロとするように
攪拌用モータの増速または減速作動時間比率を調節する
ことを特徴とする溶存酸素の調整方法。1 By measuring the amount of dissolved oxygen in the solution, it is possible to adjust the speed-up or deceleration operating time ratio of the stirring motor according to the deviation between the measured value and the set value so as to reduce the deviation to zero. Characteristic method for adjusting dissolved oxygen.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP54039604A JPS5823073B2 (en) | 1979-04-02 | 1979-04-02 | How to adjust dissolved oxygen |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP54039604A JPS5823073B2 (en) | 1979-04-02 | 1979-04-02 | How to adjust dissolved oxygen |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS55131384A JPS55131384A (en) | 1980-10-13 |
| JPS5823073B2 true JPS5823073B2 (en) | 1983-05-12 |
Family
ID=12557711
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP54039604A Expired JPS5823073B2 (en) | 1979-04-02 | 1979-04-02 | How to adjust dissolved oxygen |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5823073B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS59160594A (en) * | 1983-03-03 | 1984-09-11 | Hitachi Kiden Kogyo Ltd | Aerator |
| JPS59162996A (en) * | 1983-03-08 | 1984-09-13 | Toyota Motor Corp | Controlling method for aeration in mechanical aeration tank |
-
1979
- 1979-04-02 JP JP54039604A patent/JPS5823073B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS55131384A (en) | 1980-10-13 |
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