JP2981828B2 - Control Method of Oxidation Reduction Potential and Dissolved Gas of Combined Acoustic Generated Jet Water - Google Patents

Control Method of Oxidation Reduction Potential and Dissolved Gas of Combined Acoustic Generated Jet Water

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Publication number
JP2981828B2
JP2981828B2 JP6307052A JP30705294A JP2981828B2 JP 2981828 B2 JP2981828 B2 JP 2981828B2 JP 6307052 A JP6307052 A JP 6307052A JP 30705294 A JP30705294 A JP 30705294A JP 2981828 B2 JP2981828 B2 JP 2981828B2
Authority
JP
Japan
Prior art keywords
water
gas
tank
reduction potential
oxidation
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 - Lifetime
Application number
JP6307052A
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Japanese (ja)
Other versions
JPH08141561A (en
Inventor
真之 大槻
喜久 大槻
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.)
Mikasa KK
Original Assignee
Mikasa KK
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Filing date
Publication date
Application filed by Mikasa KK filed Critical Mikasa KK
Priority to JP6307052A priority Critical patent/JP2981828B2/en
Publication of JPH08141561A publication Critical patent/JPH08141561A/en
Application granted granted Critical
Publication of JP2981828B2 publication Critical patent/JP2981828B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、水の酸化還元電位及び
溶存ガス量を変化させる方法に関する。
The present invention relates to the oxidation-reduction potential of water and
The present invention relates to a method for changing a dissolved gas amount .

【0002】[0002]

【従来の技術】水の酸化還元を行ってその電位を変化さ
せ、その水を種々の産業等に利用することは知られてお
り、そのための装置も実用化されている。
2. Description of the Related Art It is known that oxidation and reduction of water is performed to change its potential, and the water is used in various industries and the like, and apparatuses for this purpose have been put to practical use.

【0003】そして、この装置により得られた水は、農
業においては、作物の鮮度保持、無農薬栽培、栽培効率
の向上に役立ち、水産業においては魚貝類の鮮度保持、
無薬品栽培、漁業に効果的に利用することができる。
[0003] The water obtained by this apparatus is useful for maintaining freshness of crops, cultivation without pesticides and improving cultivation efficiency in agriculture, and maintaining freshness of fish and shellfish in the fishing industry.
It can be effectively used for chemical-free cultivation and fishing.

【0004】また、畜産業においても、家畜の無薬品飼
育、畜産公害を防ぐ環境改善、畜産品の鮮度保持に有効
であり、食品工業においても、無酸素水の使用による鮮
度保持に役立つ。
[0004] In the livestock industry, it is also effective in raising livestock without chemicals, improving the environment to prevent livestock pollution, and maintaining the freshness of livestock products. In the food industry, it is also useful for maintaining the freshness by using oxygen-free water.

【0005】さらに、浄水産業においては、飲料水、汚
水の処理性能を向上させる。また、酒類等の醸造産業に
おいては、品質、生産性を向上させ、医学、薬学の分野
においても薬品効果の向上、予防医学の向上に役立ち、
工業においては、工業用水を無酸素水とすることによる
酸化防止に有効である。その他、種々の環境改善にも役
立つものとして利用範囲が広い。
[0005] Further, in the water purification industry, the treatment performance of drinking water and sewage is improved. In the brewing industry, such as alcoholic beverages, improve quality and productivity, and in the fields of medicine and pharmacy, improve drug efficacy and preventive medicine.
In industry, it is effective in preventing oxidation by converting industrial water to oxygen-free water. In addition, it is widely used for various environmental improvements.

【0006】そして前記の酸化還元電位は、水に空気を
送り込んだり、水に音波を照射したりすることで変化す
ることも公知である。
It is also known that the above-mentioned oxidation-reduction potential changes by blowing air into water or irradiating water with sound waves.

【0007】また、 ガスをエアレーション方式で注
入することによっても前記の酸化還元電位の変化が起こ
ることも公知である。図4はその場合の溶存酸素(D
O)量の変化を示す。横軸は時間(単位は1時間)、縦
軸は溶存酸素(DO)量で、単位はppmである。さら
に図5はその場合の酸化還元電位の変化であって、横軸
は時間(単位は1時間)、縦軸は酸化還元電位(単位は
×100mV)である。両図ともに、A点において
ガスの注入を開始してB点で注入を停止し、その後その
まま容器を開放状態で放置したものである。両図で理解
されるように、水へ ガスを開放状態でエアレーショ
ン方式で注入した場合の溶存酸素量の変化や酸化還元電
位の変化は発生するが、その変化量は非常に微々たるも
のである。
It is also known that the above-mentioned change in the oxidation-reduction potential is caused by injecting N 2 gas by an aeration method. FIG. 4 shows the dissolved oxygen (D
O) shows the change in the amount. The horizontal axis is time (unit is 1 hour), and the vertical axis is dissolved oxygen (DO) amount, and the unit is ppm. FIG. 5 shows the change in the oxidation-reduction potential in that case, where the horizontal axis represents time (unit is 1 hour), and the vertical axis represents the oxidation-reduction potential (unit is × 100 mV). In both figures, N 2 at point A
The injection of gas is started, the injection is stopped at point B, and then the container is left in an open state. As seen in both figures, a change in the change and the redox potential in the dissolved oxygen amount when injected with aeration method with N 2 gas into the water in the open state occurs, but the variation is very insignificant It is.

【0008】つぎに、前記のように水に ガスをエア
レーション方式で注入するのに加えて、本出願と同一の
出願人によって先に出願されたタンク内滞留水に対し
て噴射する空気または酸素、N ガスの噴射量及び照射
する音波の量とを制御可能な制御装置を備え、上記空気
または酸素、N ガスの噴射と上記音波の照射との両者
の量を前記制御装置により制御調整し、かつ、両者を同
時に行う水の酸化還元電位制御装置を用いて、水の溶存
ガス及び酸化還元電位を変化させるようにした場合の結
果を図6、7に示してある。
Next, in addition to injecting N 2 gas into water as described above, in addition to injecting N 2 gas into the water, the air injected to the retained water in the tank previously filed by the same applicant as the present application has been filed. Or the injection amount and irradiation of oxygen and N 2 gas
Comprising a controllable control device and the amount of sound waves, controlled adjustment by pre SL control device the amount of both the illumination of the air or oxygen, N 2 gas injection and the waves, and, both at the same time Water dissolution using a redox potential control device
6 and 7 show the results when the gas and the oxidation-reduction potential were changed.

【0009】両図ともに、A点において ガスの注入
を開始してB点で注入を停止し、その後そのまま容器を
開放状態で放置したものである。図6において横軸は時
間(単位は1時間)、縦軸は溶存酸素(DO)量で、単
位はppmである。図6で示されるように、溶存酸素
(DO)量の変化はゼロ近くまで減少する。図7はこの
場合の水の酸化還元電位であって、横軸は時間(単位は
1時間)、縦軸は酸化還元電位(単位は×100mV)
である。この図で理解されるように、酸化還元電位は処
理直後は低下するが、放置しておくとまた元に戻り、さ
らに上昇してしまい、安定しない状態である。
In both figures, injection of N 2 gas is started at point A, injection is stopped at point B, and the container is left as it is in an open state. In FIG. 6, the horizontal axis represents time (unit is 1 hour), and the vertical axis represents dissolved oxygen (DO) amount, and the unit is ppm. As shown in FIG. 6, the change in the amount of dissolved oxygen (DO) decreases to near zero. FIG. 7 shows the oxidation-reduction potential of water in this case. The horizontal axis represents time (unit is 1 hour), and the vertical axis represents oxidation-reduction potential (unit is 100 mV).
It is. As can be understood from this figure, the oxidation-reduction potential decreases immediately after the treatment, but returns to the original state if left untreated, and further increases, and is in an unstable state.

【0010】[0010]

【発明が解決しようとする課題】上記のように、従来の
装置では溶存酸素(DO)量、あるいは、酸化還元電位
の一方については所望の値の水を得る装置も提供されて
いるが、両者ともに望ましい値とする装置は得られてい
ないものであった。本発明は、このような点に着目し、
溶存酸素量、酸化還元電位の双方について望ましい値を
持つ処理水が得られる装置を提供するものである。
As described above, in the conventional apparatus, there is also provided an apparatus for obtaining water having a desired value with respect to one of a dissolved oxygen (DO) amount and an oxidation-reduction potential. An apparatus having both desirable values has not been obtained. The present invention focuses on such points,
It is an object of the present invention to provide an apparatus capable of obtaining treated water having desirable values for both a dissolved oxygen amount and an oxidation-reduction potential.

【0011】[0011]

【課題を解決するための手段】上記の課題は本発明によ
れば、密閉型タンク13の水滞留室15に、自動給水装
置7にて原水を供給して所定量の滞留水を得る工程と、
密閉型タンク13内の滞留水の水面上方に形成したガス
滞留室14に、N ガスを圧力調整装置2を介して供給
する工程と、密閉型タンク13内の滞留水を循環させる
水ガス循環ポンプP からの噴流水に、密閉型タンク1
3の外部において空気又は酸素を混合して気液混合水と
して複合音波発生噴流式水ガス混合装置8に供給すると
共に、密閉型タンク13の内部においてN ガスを該装
置8に供給して上記気液混合水に混合して、音波を照射
しつつ上記滞留水中に噴射する工程と、密閉型タンク1
内に設けた酸化還元電位検出センサ12の検出値で指
示値を出力する酸化還元電位指示調整器10によって上
記噴流水の量及び照射する音波の強度を制御する工程
と、密閉型タンク13内の処理された処理水を密閉型タ
ンク13の処理水取り出し口Eより取り出す工程と、
備える複合音波発生噴流式水の酸化還元電位および溶存
ガス制御方法とすることで解決することができる。
According to the present invention , an automatic water supply system is provided in a water retention chamber 15 of a closed tank 13 according to the present invention.
A step of supplying raw water at a location 7 to obtain a predetermined amount of retained water;
Gas formed above the level of the stagnant water in the closed tank 13
N 2 gas is supplied to the retention chamber 14 via the pressure adjusting device 2
And circulating the retained water in the closed type tank 13
The water jet from the water gas circulation pump P 1, sealed tank 1
3. Air or oxygen is mixed outside with gas-liquid mixed water
And supplied to the composite sound wave generating jet water gas mixing device 8
In both cases , the N 2 gas is charged inside the closed tank 13.
And then mixed with the gas-liquid mixture and radiated with sound waves
Injecting water into the stagnant water while the closed tank 1
The finger detects the detection value of the oxidation-reduction potential detection sensor 12 provided in
The value is adjusted by the redox potential indicating regulator 10 which outputs the reading.
The step of controlling the amount of the jet water and the intensity of the sound wave to be irradiated
And the treated water in the closed tank 13 is closed.
This can be solved by a method for controlling the oxidation-reduction potential and dissolved gas of the composite sound wave-producing jet water , which comprises the step of taking out from the treated water take-out port E of the ink 13 .

【0013】[0013]

【作用】タンク中の滞留水を循環させる水ガス循環ポン
プから出力される噴流水には、前記密閉型タンクの外部
において空気または酸素とを効率よく混合させると共
に、前記密閉型タンク内部においてN ガスを混合させ
音波とともに前記滞留水に噴射して、その溶存ガス量
酸化還元電位を変化させる。密閉型とした前記タン
クは、その上部空間に加圧供給されるガスを効率的に水
に溶解させて、水の溶存ガス量を変化させる。また、密
閉型であることは変化させた酸化還元電位値を経時変化
のない安定なものとする。
[Action] The water jets that will be output from the water gas circulation Pont <br/> flop circulating the accumulated water in the tank, outside the sealed tank
When the Ru is mixed efficiently with air or oxygen co
Then, N 2 gas was mixed inside the closed type tank.
And injected into the accumulated water in the waves together with Te, the dissolved gas amount
Changing the redox potential. The closed-type tank efficiently dissolves the gas supplied under pressure to the upper space in water, and changes the dissolved gas amount of water. In addition, the hermetic type makes the changed oxidation-reduction potential value stable without change over time.

【0014】タンク中に設けた酸化還元電位センサの検
出値によって指示値を出力する酸化還元電位指示調整器
は、水ガス循環ポンプから出力される水の量、および照
射される音波の強度を制御して水の溶存ガス量と酸化還
元電位を所望の値とする。
An oxidation-reduction potential indicator adjuster for outputting an indication value according to a detection value of an oxidation-reduction potential sensor provided in the tank controls the amount of water output from the water gas circulation pump and the intensity of sound waves emitted. Then, the dissolved gas amount of water and the oxidation-reduction potential are set to desired values.

【0015】[0015]

【実施例】図1に本発明の一実施例をブロック構成図に
よって示す。同図において、13は密閉型タンクであっ
て、処理水を滞留させる水滞留室15とその上方の
ガスを充填する ガス滞留室14とからなる。1は前
記のガス滞留室14に対し ガスを供給する ガス
供給装置であり、該装置から圧力調整装置2を介してガ
ス滞留室14に対し前記ガスが供給される。3は前記ガ
ス滞留室14内のガス圧を検出する圧力計、4はガス滞
留室14内のガス圧が危険な状態になった場合に作動す
る安全装置である。
FIG. 1 is a block diagram showing an embodiment of the present invention. In the figure, reference numeral 13 denotes a closed tank, which is a water retention chamber 15 for retaining treated water and N 2 above the water retention chamber 15.
And a N 2 gas retention chamber 14 for filling gas. 1 is a N 2 gas supply unit for supplying a N 2 gas to the gas retention chamber 14, the gas is supplied to the gas retaining chamber 14 through the pressure regulator 2 from the device. Reference numeral 3 denotes a pressure gauge for detecting the gas pressure in the gas storage chamber 14, and reference numeral 4 denotes a safety device which operates when the gas pressure in the gas storage chamber 14 becomes dangerous.

【0016】5はガス滞留室14内のガス圧を調整する
圧力調整装置であり、該圧力調整装置を経て過剰ガスは
過剰ガス噴出口Bから外部へ逃がされるようになってい
る。6はガス精製装置で、これに接続されているガス循
環ポンプP とともにガス滞留室14内のガスを循環さ
せ精製して常にガス滞留室14内のガスを清浄なものと
する。7は自動給水装置であり、符号Aの原水導入口か
ら導入され原水バルブVを経て供給される原水の量を
調整し、水滞留室15内の滞留水の量を適量なものとす
る。
Reference numeral 5 denotes a pressure adjusting device for adjusting the gas pressure in the gas storage chamber 14, through which excess gas is released from the excess gas outlet B to the outside. 6 is a gas purification unit, always shall clean the gas in the gas residence chamber 14 with a gas circulation pump P 2 which is connected purified by circulating gas in the gas residence chamber 14 to this. 7 is an automatic watering system, to adjust the amount of water supplied through the introduced raw water valve V 1 from the raw water inlet of the code A, and an appropriate amount things the amount of accumulated water in the water holding chamber 15..

【0017】8は、前記密閉型タンク13中の滞留水に
対して噴射する空気または酸素、N ガスの噴射量及び
照射される音波の量を制御可能な制御装置とを備え、上
記空気または酸素、N ガスの噴射と上記音波の照射と
の両者の量を前記制御装置により制御調整し、かつ、両
者を同時に行う水の酸化還元電位制御装置であって、以
下、複合音波発生噴流式水ガス混合装置と呼称すること
にする。
[0017] 8, air or oxygen is injected to the front SL accumulated water in the sealed tank 13, the injection amount of N 2 gas and
And a controllable control the amount of sound waves to be irradiated, the control adjusts the upper <br/> Symbol air or oxygen, the amount of both the illumination of the injection and the waves of the N 2 gas by the front Symbol CONTROLLER In addition, it is a water oxidation-reduction potential control device that performs both of them simultaneously, and is hereinafter referred to as a composite sound wave generating jet water gas mixing device.

【0018】密閉型タンク13内の滞留水を循環させる
水ガス循環ポンプP からの噴流水に、密閉型タンク1
3の外部において空気又は酸素を混合して気液混合水と
して複合音波発生噴流式水ガス混合装置8に供給すると
共に、密閉型タンク13の内部においてN ガスを該装
置8に供給して上記気液混合水に混合して、音波を照射
しつつ上記滞留水中に噴射する。 図中、16は水ガス循
環ポンプP の出力側、即ち、密閉型タンク13の外部
に設けた空気又は酸素供給装置を示し、A’はその出力
側を示し、Cは密閉型タンク13内のガス滞留室14に
配置したN ガスを複合音波発生噴流式水ガス混合装置
8に導入する為のN ガス導入口を示す。
Circulating the accumulated water in the closed type tank 13
The water jet from the water gas circulation pump P 1, sealed tank 1
3. Air or oxygen is mixed outside with gas-liquid mixed water
And supplied to the composite sound wave generating jet water gas mixing device 8
In both cases , the N 2 gas is charged inside the closed tank 13.
And then mixed with the gas-liquid mixture and radiated with sound waves
While spraying into the stagnant water. In the figure, reference numeral 16 denotes water gas circulation.
The output side of the ring pump P 1, i.e., outside of the sealed tank 13
A 'indicates the air or oxygen supply device provided at
And C indicates the gas retention chamber 14 in the closed type tank 13.
Combined sound wave generating jet-type water-gas mixing device for N 2 gas arranged
8 shows an N 2 gas inlet for introduction.

【0019】9はポンプモータ回転数制御装置で、前記
水ガス循環ポンプP のモータの回転数制御を行う。1
2は前記水滞留室15部付近に配置される酸化還
元電位センサで、水滞留室15内の滞留水の酸化還元電
位を測定検出し、そのデータを出力する。10は前記酸
化還元電位センサ12が出力する酸化還元電位データを
入力されて、そのデータにより、前記ポンプモータ回転
数制御装置9に対し制御に必要な指示信号を出力する酸
化還元電位指示調整器、11は前記データを記録する酸
化還元電位記録器である。
Reference numeral 9 denotes a pump motor speed control device,
The rotation speed control of the motor Water gas circulation pump P 1. 1
2 is a redox potential sensor disposed near the bottom of the said water holding chamber 15, measured detected oxidation-reduction potential of the accumulated water in the water retention chamber 15 and outputs the data. 10 is inputted to the redox potential data output from the redox potential sensor 12, by the data, the redox potential indication regulator for outputting an instruction signal required to against control the pump motor speed control device 9, An oxidation-reduction potential recorder 11 records the data.

【0020】Eは処理の終了した滞留水を取り出す処理
水取り出し口、Vは該取り出し口に連なる処理水取り
出しバルブである。
[0020] E is treated water outlet to take out the finished accumulated water processing, V 2 is a process water outlet valve connected to the outlet.

【0021】本発明の装置の動作を以下に説明する。密
閉型タンク13内に原水導入口Aから原水バルブ
介して供給される原水は自動給水装置7によって適量が
導入され、水滞留室15に滞留水として滞留する。この
滞留水ガス循環ポンプP により、空気又は酸素供
給装置16に送り込まれ、該装置16で空気又は酸素が
混合されて気液混合水となって複合音波発生噴流式水ガ
ス混合装置8に噴流され、該装置8でN ガスが混合さ
れた気液混合水が滞留水に音波の照射と共に噴射循環さ
せられる。
The operation of the apparatus according to the present invention will be described below. Raw water supplied through the raw water valve V 1 from the raw water inlet A into the sealed tank 13 an appropriate amount is introduced by automatic water supply device 7, it retained as retained water in the water holding chamber 15. The retained water by the water gas circulation pump P 1, air or oxygen supply
Is fed into a supply device 16 where air or oxygen is
The water is mixed into gas-liquid mixed water and jetted into a composite sound wave jet water gas mixing device 8 where N 2 gas is mixed.
The gas-liquid mixing water Ru is jetted circulated together with irradiation of sound waves to standing water.

【0022】上記複合音波発生噴流式ガス水混合装置の
要部の断面図を図2に示す。同図において、21は円筒
状の固定パイプで、その内径部に、先端が細径となった
水噴射ノズル22を嵌入させる。固定パイプ21の中間
部側壁にはガス導入パイプ23が取り付けられ、水噴射
ノズル22の先端部付近に導入開口している。24は固
定パイプ21の先端に嵌合させたガス水混合ノズルであ
り、処理された水を出力する。
[0022] illustrates a cross-sectional view of an essential part of the composite wave generation injection Nagareshiki gas water mixing device in FIG. In the figure, reference numeral 21 denotes a cylindrical fixed pipe into which a water jet nozzle 22 having a small diameter is fitted. A gas introduction pipe 23 is attached to an intermediate side wall of the fixed pipe 21, and an introduction opening is provided near a tip of the water injection nozzle 22. Reference numeral 24 denotes a gas / water mixing nozzle fitted to the tip of the fixed pipe 21, and outputs treated water.

【0023】固定パイプ21及び水噴射ノズル22の入
力側A’から導入された気液混合水は、水噴射ノズル2
2の先端から噴出するとともに、ガス導入パイプ23の
入力側から導入されたN ガスが混合された気液混合水
となって、その噴出口Dから滞留水中に音波の照射と共
に噴射されるものである。
The gas-liquid mixed water introduced from the fixed pipe 21 and the input side A ′ of the water injection nozzle 22
With ejected from the second tip, the gas-liquid mixing water N 2 gas introduced from the input side of the gas introduction pipe 23 is mixed
From the ejection port D,
Is a shall injected into.

【0024】水滞留室15の滞留水は、この噴射と照射
とにより酸化還元電位と溶存ガス量とが変化する。滞留
の酸化還元電位は、密閉型タンク13の底部付近に配
置された酸化還元電位検出センサ12により測定検出さ
れ、そのデータは酸化還元電位指示調整器10へ送られ
る。
The retained water in the water holding chamber 15, an oxidation-reduction potential and the dissolved gas amount is changed by the irradiation with the injection. Stay
The oxidation-reduction potential of water is measured and detected by an oxidation-reduction potential detection sensor 12 arranged near the bottom of the closed type tank 13, and the data is sent to the oxidation-reduction potential instruction controller 10.

【0025】データを送られた酸化還元電位指示調整器
10は、そのデータを監視するとともに、予め設定され
た、酸化還元電位値と、水ガス循環ポンプP の出力
量、空気または酸素、N ガスの噴射量及び音波の照射
量との関係に従って、ポンプモータ回転数制御装置9お
よび図示しない空気制御装置に対し制御に必要な指示信
号を出力する。
The oxidation sent data reduction potential indication regulator 10 is configured to monitor the data, previously set, and the redox potential value, the output amount of the water gas circulation pump P 1, air or oxygen, N according to the relationship between the injection quantity of 2 gas and sonic irradiation amount, and outputs an instruction signal necessary for control against the pneumatic control equipment for the pump motor speed control system 9 and it is not shown.

【0026】指示信号を入力されたポンプモータ回転数
制御装置9および図示しない空気制御装置は、前記指示
信号に従い、水ガス循環ポンプP の出力量、空気又は
酸素の量及びガス導入パイプ23から導入される
スの噴射量を調整し、所定の量とすると共に照射される
音波の照射量を調整され、所定の量とする。
The instruction signal air control device is a pump motor speed control device 9 and an unillustrated enter, in accordance with the instruction signal, the output of the water gas circulation pump P 1, air or
Amount of oxygen and N 2 gas introduced from gas introduction pipe 23
Adjust the injection amount of the scan, also adjusting the irradiation amount of acoustic waves irradiation Isa with the amount of Jo Tokoro, a predetermined amount.

【0027】このような動作の前に、密閉型タンク13
の上部のガス滞留室14に対し、 ガス供給装置1に
よって圧力調整装置2を介し、Nガスが送り込まれ
る。送り込まれたガスは圧力計3、安全装置4、圧力
調整装置5により所要の圧力に制御管理され、余剰なガ
スは過剰ガス噴出口Bがら排出される。また、ガス滞留
室14のガスはガス精製装置6およびガス循環ポンプP
によって常時清浄な状態に保たれる。このようにして
溶存ガスの制御が行われる。
Before such an operation, the closed tank 13
The relative top of the gas residence chamber 14, via a pressure regulator 2 by N 2 gas supply unit 1, and N 2 gas is fed
There Ru. The supplied gas is controlled and controlled to a required pressure by a pressure gauge 3, a safety device 4, and a pressure adjusting device 5, and excess gas is discharged from an excess gas jet port B. The gas in the gas storage chamber 14 is supplied to the gas purifier 6 and the gas circulation pump P
2 keeps it clean at all times. Thus, the control of the dissolved gas is performed.

【0028】滞留水の酸化還元電位は酸化還元電位記録
器11により、時間経過に従い記録される。前記酸化還
元電位値と、水ガス循環ポンプP の出力量、空気また
は酸素、N ガスの噴射量及び音波の照射量との関係の
設定は、この記録値を元に修正して微調整することがで
きる。
The oxidation-reduction potential of the retained water is recorded by the oxidation-reduction potential recorder 11 over time. It said redox potential value, the output quantity of water gas circulation pump P 1, setting the relationship between the air or oxygen, the injection amount of N 2 gas and sonic irradiation amount is finely modify this recorded value based on Can be adjusted.

【0029】図3に、本発明を実施した装置による水処
理の結果を示してある。同図は酸化還元電位の変化であ
り、横軸は時間(単位は1時間)、縦軸は酸化還元電位
(単位は×100mV)である。図おいて、A点で
ガスを注入開始してB点で ガスの注入を中止し、密
閉型タンク13はその密閉状態を維持したまま、その上
部にガス滞留室14としてNガスが滞留したまま所定
時間放置する。このように、B点で低下した酸化還元電
位は、時間の経過とともに、ごく僅かの上昇はあるが、
ほとんど安定状態であるということができる。溶存酸素
(DO)量については、前記の図6で示したように安定
状態が得られているので、増加することはない。
FIG. 3 shows the results of water treatment by the apparatus embodying the present invention. The figure shows changes in oxidation-reduction potential, where the horizontal axis represents time (unit is 1 hour), and the vertical axis represents oxidation-reduction potential (unit: x100 mV). In the figure, at point A, N 2
The injection of the gas is started, and the injection of the N 2 gas is stopped at the point B, and the sealed tank 13 is left as it is for a predetermined period of time while the N 2 gas is retained as a gas retaining chamber 14 above the sealed tank while maintaining the sealed state. . As described above, the oxidation-reduction potential lowered at the point B slightly increases with time,
It can be said that it is almost in a stable state. The amount of dissolved oxygen (DO) does not increase because a stable state is obtained as shown in FIG.

【0030】ガス滞留室に供給するガスの種類は本実施
例ではNガスとしたが、ガスの種類を選択することに
よって、高酸化性の水から、高還元性の水まで、所望の
ものを得ることが可能である。
In this embodiment, the type of gas supplied to the gas retaining chamber is N 2 gas. However, by selecting the type of gas, a desired gas from highly oxidizing water to highly reducing water can be obtained. It is possible to obtain

【0031】また、本実施例では酸化還元電位指示調整
器10により、水ガス循環ポンプP の出力量、噴射さ
れる空気または酸素、N ガスの噴射量、照射される音
波の照射量を制御するように構成したが、この組み合わ
せは目的等により任意であり、どのように変更すること
も可能である。
Further, the oxidation-reduction potential indication regulator 10 in the present embodiment, the output of the water gas circulation pump P 1, air is injected or oxygen injection amount of N 2 gas, the dose of sound waves emitted Is controlled, but this combination is arbitrary according to the purpose and the like, and can be changed in any manner.

【0032】[0032]

【発明の効果】以上のように本発明によれば、密閉型タ
ンクを用いた水の酸化還元電位制御装置において、複合
音波発生噴流式水ガス混合装置を用い、空気又は酸素
ガスの噴射と、音波の照射とを同時に行って酸化還
元電位と溶存ガス量と変化させ、さらに、上記タンク
内のガス滞留室においてNガスを滞留させ水に溶解さ
せるようにしたので、所望の酸化還元電位を有し、しか
も溶存酸素量の少ない処理水を得ることができる。
According to the present invention as described above, according to the present invention, the redox potential control device of water using a closed-type tank, a composite wave generation nozzle-type water gas mixing device, air or oxygen,
The N 2 gas injection and the sound wave irradiation were simultaneously performed to change the oxidation-reduction potential and the amount of dissolved gas , and further, the N 2 gas was retained in the gas retaining chamber in the tank and dissolved in water. Therefore, treated water having a desired oxidation-reduction potential and a small amount of dissolved oxygen can be obtained.

【0033】また、密閉型のタンク内で複合音波発生噴
流式水ガス混合装置を使用するため、安全性も高い。
Further, since the composite sound wave generating jet-type water-gas mixing device is used in a closed tank, the safety is high.

【0034】さらに、密閉型のタンク内でNガスを滞
留させるため、ガス圧を高めることが可能となり、従っ
て水へのガス溶解度を高めることができる。
Further, since the N 2 gas is retained in the closed tank, the gas pressure can be increased, and therefore, the solubility of the gas in water can be increased.

【0035】また、複合音波発生噴流式水ガス混合装置
における音波の照射は、ガス滞留室のNガスの水への
溶解度をも高めることに効果がある。
The sound wave irradiation in the composite sound wave generating jet water gas mixing apparatus is effective in increasing the solubility of N 2 gas in water in the gas retaining chamber.

【0036】ガス滞留室のガスはガス精製機能により、
水中から発生した不純ガス等を取り除き常時純度の高い
ガスのみが滞留水に溶解するため、高度の品質の処理水
が得られる。
[0036] The gas in the gas retaining chamber is subjected to a gas refining function.
Impurity gas generated from the water is removed and only high-purity gas is dissolved in the stagnant water at all times, so that high-quality treated water can be obtained.

【0037】複合音波発生噴流式水ガス混合装置は水の
噴射量を制御することが可能であるので、空気または酸
、N スの水への溶解度をコントロールすることが
できる。従って酸化還元電位も容易にコントロールする
ことも可能である。
[0037] can be controlled because the composite wave generation nozzle-type water gas mixing device is capable of controlling the injection quantity of water, air or oxygen, the solubility of the N 2 gas in water. Therefore, it is also possible to easily control the oxidation-reduction potential.

【0038】複合音波発生噴流式水ガス混合装置の噴流
式混合装置は、滞留水のクラスタ(分子集団)を小さく
することができるので、水の活性化の効果がある。
The jet-type mixing apparatus of the composite sound-generating jet-type water-gas mixing apparatus has the effect of activating water because the clusters (molecular groups) of the staying water can be reduced.

【0039】酸化還元電位の数値は、酸化還元電位検出
センサと酸化還元電位指示調整器とにより任意に所望の
数値に制御することができる。
The value of the redox potential can be controlled to a desired numerical arbitrarily by an oxidation-reduction potential sensor and the oxidation-reduction potential indication regulator.

【0040】さらに、薬品を使用せずに水の酸化還元電
位を変化させているので、ガスの滞留水への溶解度が一
部を除いて比較的小さいため、酸化還元電位の変化も薬
品によるものに比較して小さい。そのため、電位の微調
整が可能である。加えて、無薬品でなければならない微
生物の増殖を自由に行うことが可能となり、有機物の酸
化分解を促進することができ、無薬品で動植物の健全育
成が可能となる。さらに、動植物の増体率、飼料効率、
肥料効率が上がり生産性が向上する。
Further, since the oxidation-reduction potential of water is changed without using a chemical, the solubility of the gas in the stagnant water is relatively small except for a part of the gas. Smaller than. Therefore, fine adjustment of the potential is possible. In addition, the proliferation of microorganisms must be a non-chemical becomes possible to perform freely, it is possible to promote the oxidation decomposition of organic matter, it is possible to sound development of plants and animals in the absence of chemicals. In addition, animal and plant weight gain, feed efficiency,
Fertilizer efficiency increases and productivity improves.

【0041】ガスの種類を選択することによって、高酸
化性の水から、高還元性の水まで、安全かつ安価に、し
かも品質の高い処理水を得ることができる。
By selecting the type of gas, it is possible to obtain safe, inexpensive and high-quality treated water from highly oxidizing water to highly reducing water.

【0042】しかも、装置は取扱いが簡単で維持管理に
も時間がかからず、健康で安全な住環境が維持できる効
果もあるものである。
In addition, the device is easy to handle, does not require much time for maintenance, and has the effect of maintaining a healthy and safe living environment.

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

【図1】本発明の一実施例のブロック構成図である。FIG. 1 is a block diagram of an embodiment of the present invention.

【図2】本発明の一実施例の噴流式水ガス混合装置の断
面図である。
FIG. 2 is a cross-sectional view of a jet water gas mixing apparatus according to one embodiment of the present invention.

【図3】本発明の装置により得られた処理水の酸化還元
電位値のグラフである。
FIG. 3 is a graph of an oxidation-reduction potential value of treated water obtained by the apparatus of the present invention.

【図4】水にエアレーション方式でNガスを注入した
場合の溶存酸素量のグラフである。
FIG. 4 is a graph of a dissolved oxygen amount when N 2 gas is injected into water by an aeration method.

【図5】水にエアレーション方式でNガスを注入した
場合の酸化還元電位値のグラフである。
FIG. 5 is a graph of an oxidation-reduction potential value when N 2 gas is injected into water by an aeration method.

【図6】従来の装置により得られた処理水の溶存酸素量
のグラフである。
FIG. 6 is a graph of dissolved oxygen amount of treated water obtained by a conventional apparatus.

【図7】従来の装置により得られた処理水の酸化還元電
位値のグラフである。
FIG. 7 is a graph of an oxidation-reduction potential value of treated water obtained by a conventional apparatus.

【符号の説明】[Explanation of symbols]

ガス供給装置 2 圧力調整装置 3 圧力計 4 安全装置 5 圧力調整装置 6 ガス精製装置 7 自動給水装置 8 複合音波発生噴流式水ガス混合装置 9 ポンプモータ回転数制御装置 10 酸化還元電位指示調整器 11 酸化還元電位記録器 12 酸化還元電位検出センサ 13 密閉型タンク 14 ガス滞留室 15 水滞留室 A 原水導入口 B 過剰ガス噴出口 C 混合装置ガス導入口 D 気液混合水噴出口 E 処理水取り出し口 P ガス循環ポンプ P ガス循環ポンプ 原水バルブ V 処理水取り出しバルブ REFERENCE SIGNS LIST 1 N 2 gas supply device 2 pressure regulator 3 pressure gauge 4 safety device 5 pressure regulator 6 gas purification device 7 automatic water supply device 8 composite sound wave generating jet water gas mixing device 9 pump motor rotation speed control device 10 redox potential indication Regulator 11 Oxidation reduction potential recorder 12 Oxidation reduction potential detection sensor 13 Closed tank 14 Gas retention chamber 15 Water retention chamber A Raw water inlet B Excess gas outlet C Mixer gas inlet D Gas-liquid mixed water outlet E Processing Water outlet P 1 Water gas circulation pump P 2 Gas circulation pump V 1 Raw water valve V 2 Treated water extraction valve

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 密閉型タンク(13)の水滞留室(1
5)に、自動給水装置(7)にて原水を供給して所定量
の滞留水を得る工程と、 密閉型タンク(13)内の滞留水の水面上方に形成した
ガス滞留室(14)に、N ガスを圧力調整装置(2)
を介して供給する工程と、 密閉型タンク(13)内の滞留水を循環させる水ガス循
環ポンプP からの噴流水に、密閉型タンク(13)の
外部において空気又は酸素を混合して気液混合水として
複合音波発生噴流式水ガス混合装置(8)に供給すると
共に、密閉型タンク(13)の内部においてN ガスを
該装置(8)に供給して上記気液混合水に混合して、音
波を照射しつつ上記滞留水中に噴射する工程と、 密閉型タンク(13)内に設けた酸化還元電位検出セン
サ(12)の検出値で指示値を出力する酸化還元電位指
示調整器(10)によって上記噴流水の量及び照射する
音波の強度を制御する工程と、 密閉型タンク(13)内の処理された処理水を密閉型タ
ンク(13)の処理水取り出し口Eより取り出す工程
と、 よりなる複合音波発生噴流式水の酸化還元電位および溶
存ガス制御方法。
A water retention chamber (1) of a closed type tank (13).
5) Raw water is supplied by the automatic water supply device (7)
And a step of forming the accumulated water above the level of the accumulated water in the closed type tank (13).
N 2 gas is supplied to the gas retention chamber (14) with a pressure regulator (2).
And a water gas circulation for circulating water retained in the sealed tank (13).
The water jet from ring pump P 1, sealed tank (13)
Mixing air or oxygen outside to form gas-liquid mixed water
When it is supplied to the water jet mixing device (8),
In both cases, N 2 gas is supplied inside the closed tank (13).
It is supplied to the device (8) and mixed with the gas-liquid mixed water to produce a sound.
A step of injecting into the residence water while irradiating waves, redox potential detecting sensor provided in an enclosed tank (13)
An oxidation-reduction potential finger that outputs an indicated value based on the detection value of the sensor (12).
The amount and the irradiation of the jet water are indicated by the indicator controller (10).
A step of controlling the intensity of the sound wave, and treating the treated water in the closed tank (13) with the closed tank.
Step of extracting through the treated water outlet E of ink (13)
And a method for controlling the oxidation-reduction potential and the dissolved gas of the combined acoustic wave generating jet water.
JP6307052A 1994-11-17 1994-11-17 Control Method of Oxidation Reduction Potential and Dissolved Gas of Combined Acoustic Generated Jet Water Expired - Lifetime JP2981828B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6307052A JP2981828B2 (en) 1994-11-17 1994-11-17 Control Method of Oxidation Reduction Potential and Dissolved Gas of Combined Acoustic Generated Jet Water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6307052A JP2981828B2 (en) 1994-11-17 1994-11-17 Control Method of Oxidation Reduction Potential and Dissolved Gas of Combined Acoustic Generated Jet Water

Publications (2)

Publication Number Publication Date
JPH08141561A JPH08141561A (en) 1996-06-04
JP2981828B2 true JP2981828B2 (en) 1999-11-22

Family

ID=17964475

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6307052A Expired - Lifetime JP2981828B2 (en) 1994-11-17 1994-11-17 Control Method of Oxidation Reduction Potential and Dissolved Gas of Combined Acoustic Generated Jet Water

Country Status (1)

Country Link
JP (1) JP2981828B2 (en)

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KR100320603B1 (en) * 1999-04-26 2002-01-17 김정영 Water Filtering system and water filtering method thereof
JP2007105677A (en) * 2005-10-14 2007-04-26 Mikasa:Kk Active water production method, animal breeding method, and active water
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Publication number Priority date Publication date Assignee Title
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Also Published As

Publication number Publication date
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