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JP7442846B2 - Gas solution generation device - Google Patents
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JP7442846B2 - Gas solution generation device - Google Patents

Gas solution generation device Download PDF

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JP7442846B2
JP7442846B2 JP2022011469A JP2022011469A JP7442846B2 JP 7442846 B2 JP7442846 B2 JP 7442846B2 JP 2022011469 A JP2022011469 A JP 2022011469A JP 2022011469 A JP2022011469 A JP 2022011469A JP 7442846 B2 JP7442846 B2 JP 7442846B2
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JP2023110186A (en
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一郎 手柴
康矢 田仲
雅文 宮田
圭史 中村
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穂栄株式会社
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    • 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
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Description

本発明は、水やその他の液体に酸素や空気などの気体を溶解させて気体溶解液を生成する気体溶解液生成装置に関する。 The present invention relates to a gas solution generating device that generates a gas solution by dissolving a gas such as oxygen or air in water or other liquid.

本発明に係る気体溶解液生成装置と同様、酸素や空気などの気体を水に溶解させて気体溶解水を生成する機能を有する装置として、例えば、特許文献1に記載された「微細気泡発生装置」が知られている。 Similar to the gas-dissolved liquid generating device according to the present invention, an example of a device having a function of generating gas-dissolved water by dissolving a gas such as oxygen or air in water is the “fine bubble generating device” described in Patent Document 1. "It has been known.

特許文献1に記載された「微細気泡発生装置」は、気液が旋回可能な筒状空間を有する気液旋回室と、前記気液旋回室内へ液体を導入して前記気液旋回室内に液体旋回流を発生させるため前記気液旋回室の基端側に配置された液体導入手段と、前記気液旋回室へ気体を供給するため前記気液旋回室に連通して設けられた気体導入手段と、前記気液旋回室内の気液を吐出するため前記気液旋回室の先端側に配置された気液吐出口と、前記気液吐出口から吐出される気液を導入する気液接触室と、前記気液接触室内の気液を排出する気液排出口と、を備えたことを特徴とする。 The "fine bubble generator" described in Patent Document 1 includes a gas-liquid swirling chamber having a cylindrical space in which gas and liquid can swirl, and a liquid being introduced into the gas-liquid swirling chamber to generate liquid in the gas-liquid swirling chamber. a liquid introducing means arranged on the base end side of the gas-liquid swirling chamber to generate a swirling flow; and a gas introducing means provided in communication with the gas-liquid swirling chamber to supply gas to the gas-liquid swirling chamber. a gas-liquid discharge port disposed on the tip side of the gas-liquid swirling chamber for discharging the gas-liquid in the gas-liquid swirling chamber; and a gas-liquid contact chamber into which the gas-liquid discharged from the gas-liquid discharge port is introduced. and a gas-liquid outlet for discharging the gas-liquid in the gas-liquid contact chamber.

特許文献1に記載された「微細気泡発生装置」を使用することにより、空気や酸素などの気体が溶解した気体溶解水を生成することができ、この気体溶解水は植物栽培用水や魚介類養殖用水などの用途に広く利用することができ、植物の成長や魚介類の生育に良い影響を与えている。 By using the "fine bubble generator" described in Patent Document 1, it is possible to generate gas-dissolved water in which gases such as air and oxygen are dissolved, and this gas-dissolved water can be used as water for plant cultivation or for fish and shellfish aquaculture. It can be widely used for purposes such as irrigation water, and has a positive impact on the growth of plants and seafood.

特許第3765759号公報Patent No. 3765759

特許文献1に記載された「微細気泡発生装置」は、微細気泡が溶解した液体(気体溶解液)を効率良く生成することができ、設置に要するスペースや配管資材を大幅に削減することができるなどの長所を有しているが、気体溶解液の生成効率の向上は、今後も引き続き重要な課題である。 The "micro bubble generator" described in Patent Document 1 can efficiently generate a liquid in which micro bubbles are dissolved (gas solution), and can significantly reduce the space and piping materials required for installation. However, improving the production efficiency of gaseous solution will continue to be an important issue in the future.

そこで、本発明が解決しようとする課題は、大量の気体が溶解した液体を効率良く、安定的に生成することができる気体溶解液生成装置を提供することにある。 Therefore, an object of the present invention is to provide a gas-dissolved liquid generating device that can efficiently and stably generate a liquid in which a large amount of gas is dissolved.

本発明に係る気体溶解液生成装置は、液体を収容可能な気密構造の気液接触槽と、前記気液接触槽内に配置され前記気液接触槽の外部から供給される液体と気体とを混合して前記気液接触槽内に微細気泡混じりの液体を吐出する微細気泡発生器と、前記気液接触槽外から前記微細気泡発生器に液体を供給する液体導入経路と、前記気液接触槽外に露出した前記液体導入経路に配置した逆止弁と、前記気液接触槽外から前記微細気泡発生器に気体を供給する気体導入経路と、前記微細気泡発生器から前記気液接触槽内に吐出された微細気泡混じりの液体から形成された気体溶解液を前記気液接触槽外へ排出する排液経路と、を備え、
前記微細気泡発生器が、気液が旋回可能な筒状空間を有する気液旋回室と、前記液体導入経路を経由して供給される液体を前記気液旋回室内に噴出する複数の液体噴出口と、前記気体導入経路を経由して供給される気体を前記気液旋回室内に噴出する気体噴出口と、前記気液旋回室内の微細気泡混じりの液体を前記気液接触槽内に吐出する気液吐出口と、を備えたことを特徴とする。
A gas-dissolved liquid generating device according to the present invention includes a gas-liquid contact tank having an airtight structure capable of containing a liquid, and a gas-liquid contact tank arranged in the gas-liquid contact tank and containing a liquid and a gas supplied from outside of the gas-liquid contact tank. a fine bubble generator that mixes and discharges a liquid containing fine bubbles into the gas-liquid contact tank; a liquid introduction path that supplies the liquid from outside the gas-liquid contact tank to the fine bubble generator; and the gas-liquid contactor. a check valve disposed in the liquid introduction path exposed to the outside of the tank; a gas introduction path that supplies gas from outside the gas-liquid contact tank to the fine bubble generator; and a gas introduction path from the fine bubble generator to the gas-liquid contact tank. a drainage path for discharging the gas solution formed from the liquid mixed with fine bubbles discharged into the gas-liquid contact tank to the outside of the gas-liquid contact tank;
The fine bubble generator includes a gas-liquid swirling chamber having a cylindrical space in which gas and liquid can swirl, and a plurality of liquid spouting ports that spout liquid supplied via the liquid introduction path into the gas-liquid swirling chamber. a gas jetting port for spouting the gas supplied via the gas introduction path into the gas-liquid swirling chamber; and a gas jetting port for spouting the liquid mixed with fine bubbles from the gas-liquid swirling chamber into the gas-liquid contact tank. A liquid discharge port is provided.

前記気体溶解液生成装置の前記液体噴出口は、前記気液旋回室の中心軸に対し捻じれの位置をなす方向へ液体を噴出する位置に設けて、前記気液旋回室内に、その中心軸の周りを回転する旋回流を形成している。
The liquid spout of the gas-dissolved liquid generating device is provided at a position for spouting the liquid in a direction that is twisted with respect to the central axis of the gas-liquid swirling chamber, and the liquid spout is provided in a position in which the liquid is spouted in a direction that is twisted with respect to the central axis of the gas-liquid swirling chamber. It forms a swirling flow that rotates around the

また、前記気体噴出口は、前記旋回流の中心付近に前記気体を噴出することで、前記液体と前記気体とを前記気液旋回室内を旋回させながら下方へ移動させて、前記気液旋回室の下部隔壁に設けた前記気液吐出口を通過させることで微細気泡を発生させ、前記微細気泡混じりの液体として前記気液接触槽内へ流入させている。Further, the gas jetting port blows out the gas near the center of the swirling flow, thereby moving the liquid and the gas downward while swirling in the gas-liquid swirling chamber. Fine bubbles are generated by passing through the gas-liquid discharge port provided on the lower partition wall, and the liquid is caused to flow into the gas-liquid contact tank as a liquid mixed with the fine bubbles.

さらに、前記気液接触槽内には、垂直起立状に前記排液経路の上流側を配置するとともに、前記排液経路の開口部を反重力方向に向けた状態で前記気液接触槽内に配置することで、前記微細気泡発生器から前記気液接触槽内へ流入させた前記微細気泡混じりの液体を、前記気液接触槽内で上昇させ、この上昇の際に前記微細気泡中の前記気体を前記液体に溶解させるとともに、余剰な前記気体の分離を生じさせて、前記気液接触槽内の水面よりも下に位置する前記開口部から前記気体溶解液を前記排液経路内に流入させて、前記排液経路内を下降させている。 Further, in the gas-liquid contact tank, the upstream side of the drainage path is arranged vertically, and the opening of the drainage path is oriented in the anti-gravity direction. By arranging the fine bubble generator, the liquid containing fine bubbles flowing into the gas-liquid contact tank is caused to rise in the gas-liquid contact tank, and during this rise, the liquid in the fine bubbles is While dissolving the gas in the liquid, separating the excess gas and causing the gas-dissolved liquid to flow into the drainage path from the opening located below the water surface in the gas-liquid contact tank. and lowering the inside of the drainage path.

さらには、前記排液経路の途中に設けた流量調整バルブで当該排液経路内の流量を調整することで、前記気液接触槽内の水圧を一定値に保持し、前記気体溶解液の気体溶解率を一定に維持している。Furthermore, by adjusting the flow rate in the drainage path with a flow rate adjustment valve provided in the middle of the drainage path, the water pressure in the gas-liquid contact tank is maintained at a constant value, and the gas of the gas solution is The dissolution rate is maintained constant.

本発明により、大量の気体が溶解した液体を効率良く、安定的に生成することができる気体溶解液生成装置を提供することができる。 According to the present invention, it is possible to provide a gas-dissolved liquid generating device that can efficiently and stably generate a liquid in which a large amount of gas is dissolved.

本発明の実施形態である酸素溶解水生成装置を示す一部省略垂直断面図である。1 is a partially omitted vertical cross-sectional view showing an oxygen-dissolved water generating device according to an embodiment of the present invention. 図1中のA-A線における一部省略水平断面図である。2 is a partially omitted horizontal sectional view taken along line AA in FIG. 1. FIG. 図1に示す酸素溶解水生成装置の使用状態を示す一部省略概要図である。FIG. 2 is a partially omitted schematic diagram showing how the oxygen-dissolved water generating device shown in FIG. 1 is used.

以下、図1~図3に基づいて、本発明に係る気体溶解液生成装置の実施形態の一つである酸素溶解水生成装置100について説明する。 Hereinafter, an oxygen-dissolved water generating apparatus 100, which is one embodiment of a gas-dissolved liquid generating apparatus according to the present invention, will be described based on FIGS. 1 to 3.

図1に示すように、酸素溶解水生成装置100は、酸素溶解水OWを収容可能な気液接触槽1と、気液接触槽1内に配置され気液接触槽1外から供給される水Wと酸素O2とを混合して気液接触槽1内に微細気泡MB混じりの水MBWを吐出する微細気泡発生器2と、気液接触槽1外から微細気泡発生器2に水Wを供給する液体導入経路3と、気液接触槽1外から微細気泡発生器2に酸素O2を供給する気体導入経路4と、微細気泡発生器2から気液接触槽1内に吐出された微細気泡MB混じりの水MBWから形成された酸素溶解水OWを気液接触槽1外へ排出する排液経路5と、を備えている。気液接触槽1外に露出する液体導入経路3の途中には逆止弁7が配置され、気液接触槽1外に露出する排液経路5の途中には流量調整バルブ8が配置されている。 As shown in FIG. 1, the oxygen-dissolved water generating device 100 includes a gas-liquid contact tank 1 capable of accommodating oxygen-dissolved water OW, and water disposed inside the gas-liquid contact tank 1 and supplied from outside the gas-liquid contact tank 1. A fine bubble generator 2 mixes W and oxygen O 2 and discharges water MBW mixed with fine bubbles MB into the gas-liquid contact tank 1, and a fine bubble generator 2 supplies water W from outside the gas-liquid contact tank 1 to the fine bubble generator 2. A gas introduction path 4 supplies oxygen O 2 from outside the gas-liquid contact tank 1 to the fine bubble generator 2, and a gas introduction path 4 supplies oxygen O 2 from the outside of the gas-liquid contact tank 1 to the gas-liquid contact tank 1. A drain path 5 is provided for discharging oxygen-dissolved water OW formed from water MBW mixed with air bubbles MB to the outside of the gas-liquid contact tank 1. A check valve 7 is arranged in the middle of the liquid introduction path 3 exposed to the outside of the gas-liquid contact tank 1, and a flow rate adjustment valve 8 is arranged in the middle of the liquid drainage path 5 exposed to the outside of the gas-liquid contact tank 1. There is.

気液接触槽1は、円筒状の周壁部1aと、周壁部1aの下面を閉塞する底板部1bと、周壁部1aの上面を閉塞する天板部1cと、を備え、気密構造をなしている。気液接触槽1の周壁部1aの天板部1c寄りの部分には、エルボー形状の排気管6aが接続され、排気管6aの起立部の上方に排気手段6が設けられている。排気手段6は排気管6aを介して、気液接触槽1の内部と連通している。後述するように、排気手段6は、気液接触槽1内の上部(天板部1c寄りの部分)に滞留する未溶解気体を気液接触槽1外に排出する機能を有している。 The gas-liquid contact tank 1 includes a cylindrical peripheral wall portion 1a, a bottom plate portion 1b that closes the lower surface of the peripheral wall portion 1a, and a top plate portion 1c that closes the upper surface of the peripheral wall portion 1a, and has an airtight structure. There is. An elbow-shaped exhaust pipe 6a is connected to a portion of the peripheral wall 1a of the gas-liquid contact tank 1 near the top plate 1c, and an exhaust means 6 is provided above the upright portion of the exhaust pipe 6a. The exhaust means 6 communicates with the inside of the gas-liquid contact tank 1 via an exhaust pipe 6a. As will be described later, the exhaust means 6 has a function of discharging undissolved gas remaining in the upper part of the gas-liquid contact tank 1 (the part near the top plate 1c) to the outside of the gas-liquid contact tank 1.

微細気泡発生器2は、気液が旋回可能な筒状空間を有する気液旋回室21と、液体導入経路3を経由して供給される水Wを気液旋回室21内に噴出する複数の液体噴出口22と、気体導入経路4を経由して供給される酸素O2を気液旋回室21内に噴出する気体噴出口4aと、気液旋回室21内に形成された微細気泡混じりの水MBWを気液接触槽1内に吐出する気液吐出口23と、を備えている。 The fine bubble generator 2 includes a gas-liquid swirling chamber 21 having a cylindrical space in which gas and liquid can swirl, and a plurality of gas-liquid swirling chambers 21 that eject water W supplied via the liquid introduction path 3 into the gas-liquid swirling chamber 21. A liquid spout 22 , a gas spout 4 a that spouts oxygen O 2 supplied via the gas introduction path 4 into the gas-liquid swirling chamber 21 , and a gas spout 4 a that spouts oxygen O 2 supplied via the gas introduction path 4 into the gas-liquid swirling chamber 21 . A gas-liquid discharge port 23 for discharging water MBW into the gas-liquid contact tank 1 is provided.

微細気泡発生器2は、円筒状のケーシング20と、ケーシング20の上面を閉塞する上部隔壁20aを貫通して気液旋回室21内に垂下するように配置された円筒状の液体導入部24と、を備えている。ケーシング20の下面は下部隔壁20bで閉塞され、下部隔壁20bの中心に気液吐出口23が開設されている。ケーシング20の内径は液体導入部24の外径より大であり、液体導入部24の中心軸(図示せず)は気液旋回室21の中心軸21cと同一であり、液体導入部24はケーシング20と同軸をなすように配置されている。 The micro bubble generator 2 includes a cylindrical casing 20 and a cylindrical liquid introduction part 24 that is disposed so as to pass through an upper partition wall 20a that closes the upper surface of the casing 20 and hang down into a gas-liquid swirling chamber 21. , is equipped with. The lower surface of the casing 20 is closed by a lower partition wall 20b, and a gas-liquid discharge port 23 is opened at the center of the lower partition wall 20b. The inner diameter of the casing 20 is larger than the outer diameter of the liquid introduction part 24, the central axis (not shown) of the liquid introduction part 24 is the same as the central axis 21c of the gas-liquid swirling chamber 21, and the liquid introduction part 24 is larger than the outer diameter of the liquid introduction part 24. It is arranged coaxially with 20.

液体導入部24の下面は下部隔壁24bで閉塞され、液体導入部24の上方は、気液接触槽1の周壁部1aを貫通して気液接触槽1内に配設された液体導入経路3のエルボー部3aに接続されている。円筒状をなす液体導入部24の周壁部24aの下部隔壁24b寄りの部分には複数の液体噴出口22が開設されている。図2に示すように、複数の液体噴出口22は、微細気泡発生器2の気液旋回室21の中心軸21cに対し捻じれの位置をなす方向に沿って液体を噴出する位置に開設されている。 The lower surface of the liquid introduction part 24 is closed by a lower partition wall 24b, and the upper part of the liquid introduction part 24 is connected to a liquid introduction path 3 that penetrates the peripheral wall 1a of the gas-liquid contact tank 1 and is arranged in the gas-liquid contact tank 1. It is connected to the elbow part 3a of. A plurality of liquid jet ports 22 are provided in a portion of the peripheral wall portion 24a of the cylindrical liquid introducing portion 24 near the lower partition wall 24b. As shown in FIG. 2, the plurality of liquid ejection ports 22 are opened at positions for ejecting liquid along a direction that is twisted with respect to the central axis 21c of the gas-liquid swirling chamber 21 of the micro bubble generator 2. ing.

気体導入経路4は、気液接触槽1の天板部1cを貫通して気液接触室1内に垂下し、液体導入経路3の周壁部3bを貫通して液体導入部24内に入り、気液旋回室21の中心軸21cと同軸をなすように配置され、気体導入経路4の下端部側(気体噴出口4a側)は液体導入部24の下部隔壁24bを貫通して気液旋回室21内に突出し、気体噴出口4aは気液旋回室21内の中心軸21c上に位置している。 The gas introduction path 4 penetrates the top plate 1c of the gas-liquid contact tank 1 and hangs down into the gas-liquid contact chamber 1, penetrates the peripheral wall 3b of the liquid introduction path 3 and enters the liquid introduction part 24, It is arranged coaxially with the central axis 21c of the gas-liquid swirling chamber 21, and the lower end side of the gas introduction path 4 (the side of the gas jet port 4a) penetrates the lower partition wall 24b of the liquid introduction part 24 to form the gas-liquid swirling chamber. The gas jet port 4 a protrudes into the gas-liquid swirling chamber 21 and is located on the central axis 21 c within the gas-liquid swirling chamber 21 .

図1に示すように、酸素溶解水生成装置100においては、微細気泡発生器2は気液接触槽1内の底板部1b寄りの部分に、気液吐出口23を重力方向(底板部1b方向)に向けた状態で配置されている。また、酸素溶解水生成装置100においては、排液経路5の上流側を気液接触槽1内に垂直起立状に配置するとともに、排液経路5の開口部5aを気液接触槽1内の天板部1c寄りの部分に反重力方向(天板部1c方向)に向いた状態で配置することにより下向流気泡分離経路を形成している。 As shown in FIG. 1, in the oxygen-dissolved water generation device 100, the fine bubble generator 2 has a gas-liquid discharge port 23 in a portion of the gas-liquid contact tank 1 near the bottom plate 1b in the direction of gravity (in the direction of the bottom plate 1b). ). In addition, in the oxygen-dissolved water generating device 100, the upstream side of the liquid drainage path 5 is arranged vertically in the gas-liquid contact tank 1, and the opening 5a of the liquid drainage path 5 is arranged in the gas-liquid contact tank 1. A downward flow bubble separation path is formed by arranging it in the anti-gravity direction (towards the top plate 1c) in a portion near the top plate 1c.

次に、図3に基づいて、図1に示す酸素溶解水生成装置100の使用事例について説明する。図3に示すように、酸素溶解水生成装置100の液体導入経路3の上流側は送水ポンプ9を介して灌漑用水や井戸などの水源(図示せず)に接続され、排液経路5の下流側は所定の灌漑設備(図示せず)に延設されている。また、気体導入経路4の上流側は酸素ガス調整器11を経由して酸素ボンベ10に接続されている。 Next, an example of use of the oxygen-dissolved water generating apparatus 100 shown in FIG. 1 will be described based on FIG. 3. As shown in FIG. 3, the upstream side of the liquid introduction path 3 of the oxygen-dissolved water generation device 100 is connected to a water source (not shown) such as irrigation water or a well via a water pump 9, and the downstream side of the liquid drainage path 5 The sides are extended to designated irrigation facilities (not shown). Further, the upstream side of the gas introduction path 4 is connected to an oxygen cylinder 10 via an oxygen gas regulator 11.

図3中に示す酸素溶解水生成装置100に対し、送水ポンプ9を稼働させて液体導入経路3を経由して水Wを供給するとともに、酸素ガス調整器11を調整して酸素ボンベ10から気体導入経路4を経由して酸素O2を供給すると、図1,図2に示すように、水Wは微細気泡発生器2の液体導入部24内に流入した後、複数の液体噴出口22を通過して気液旋回室21内に噴出し、酸素O2は気体導入経路4の下端部分の気体噴出口4aから気液旋回室21内に噴出する。 The water supply pump 9 is operated to supply water W via the liquid introduction path 3 to the oxygen-dissolved water generation device 100 shown in FIG. When oxygen O 2 is supplied via the introduction path 4, water W flows into the liquid introduction part 24 of the micro bubble generator 2, and then flows through the plurality of liquid jet ports 22, as shown in FIGS. 1 and 2. The oxygen O 2 passes through and is ejected into the gas-liquid swirling chamber 21 , and oxygen O 2 is ejected into the gas-liquid swirling chamber 21 from the gas ejection port 4 a at the lower end portion of the gas introduction path 4 .

このとき、複数の液体噴出口22から噴出する水Wは気液旋回室21の中心軸21cに対し捻じれの位置をなす方向に沿って噴出するので、気液旋回室21内にはその中心軸21cの周りを回転する旋回流Sが形成され、気体噴出口4aから噴出する酸素O2は旋回流Sの中心付近に供給される。 At this time, the water W ejected from the plurality of liquid ejection ports 22 is ejected along the direction of the twisting position with respect to the central axis 21c of the gas-liquid swirling chamber 21. A swirling flow S rotating around the axis 21c is formed, and oxygen O 2 ejected from the gas jet port 4a is supplied near the center of the swirling flow S.

このように、気液旋回室21内に形成された旋回流Sに対して気体噴出口4aから酸素O2が供給されると、気液旋回室21内を旋回しながら下方へ移動した水W及び酸素O2が、気液旋回室21の下部隔壁20bの気液吐出口23を通過するときに水W中に酸素O2を含む大量の微細気泡MBが発生し、これによって形成された微細気泡MB混じりの水MBWが気液接触槽1内へ流入する。 In this way, when oxygen O 2 is supplied from the gas jet port 4a to the swirling flow S formed in the gas-liquid swirling chamber 21, the water W that moves downward while swirling in the gas-liquid swirling chamber 21 When oxygen O 2 and oxygen O 2 pass through the gas-liquid discharge port 23 of the lower partition wall 20b of the gas-liquid swirling chamber 21, a large amount of microbubbles MB containing oxygen O 2 are generated in the water W, and the microbubbles MB formed thereby Water MBW mixed with air bubbles MB flows into the gas-liquid contact tank 1.

気液接触槽1内へ流入した微細気泡MB混じりの水MBWは気液接触槽1内を上昇していくが、この過程において微細気泡MB中の酸素O2が水Wに溶解していくことにより酸素溶解水OWとなり、排液経路5の上端の開口部5aから排液経路5内に流入し、排液経路5内を下降して気液接触槽1外の排液経路5内を流動していき、所定の灌漑設備(図示せず)などに送給される。 The water MBW mixed with microbubbles MB that has flowed into the gas-liquid contact tank 1 rises in the gas-liquid contact tank 1, but in this process, the oxygen O 2 in the microbubbles MB dissolves into the water W. The water becomes oxygen-dissolved water OW, flows into the drainage path 5 from the opening 5a at the upper end of the drainage path 5, descends inside the drainage path 5, and flows inside the drainage path 5 outside the gas-liquid contact tank 1. The water is then fed to a predetermined irrigation facility (not shown).

酸素溶解水生成装置100で生成された酸素溶解水OWの用途は限定されないので、植物栽培用水や魚介類養殖用水などの用途に広く利用することができ、植物の成長を促進させたり、魚介類の生育状態を向上させたりすることができる。 The use of the oxygen-dissolved water OW generated by the oxygen-dissolved water generation device 100 is not limited, so it can be widely used as water for plant cultivation, water for fish and shellfish cultivation, etc. It is possible to improve the growth condition of.

微細気泡MB混じりの水MBWが気液接触槽1内を流動するとき、余剰な酸素O2ガスは浮力を有する大型気泡12となり、排液経路5内を下降する酸素溶解水OWから分離して上昇していき、気液接触槽1の天板部1cの下面の気体溜り1dに貯留される。気体溜り1dに貯留されていく未溶解の酸素O2ガスの体積が増加して気液接触槽1内の水面13が、排気管6aと周壁部1aとの接続部分より低くなると、気体溜り1dに存在する未溶解の酸素O2ガスは排気管6aを通過して排気手段6から大気中に排出される。 When water MBW mixed with fine bubbles MB flows in the gas-liquid contact tank 1, excess oxygen O 2 gas becomes large bubbles 12 with buoyancy and is separated from the oxygen-dissolved water OW descending in the drainage path 5. The gas rises and is stored in a gas reservoir 1d on the lower surface of the top plate portion 1c of the gas-liquid contact tank 1. When the volume of undissolved oxygen O 2 gas stored in the gas reservoir 1d increases and the water level 13 in the gas-liquid contact tank 1 becomes lower than the connecting portion between the exhaust pipe 6a and the peripheral wall portion 1a, the gas reservoir 1d The undissolved oxygen O 2 gas present in the exhaust gas passes through the exhaust pipe 6a and is discharged from the exhaust means 6 into the atmosphere.

このように、気体溜り1dに存在する未溶解の酸素O2ガスが一定量を超えると排気管6aを通過して排気手段6から大気中に排出されるので、気体溜り1dに貯留された未溶解の酸素O2ガスが気体塊となって排液経路5の開口部5aから排出されるのを防止することができる。 In this way, when the undissolved oxygen O 2 gas present in the gas reservoir 1d exceeds a certain amount, it passes through the exhaust pipe 6a and is discharged from the exhaust means 6 into the atmosphere. Dissolved oxygen O 2 gas can be prevented from becoming a gas mass and being discharged from the opening 5 a of the drain path 5 .

酸素溶解水生成装置100においては、液体導入経路3の途中に逆止弁7を配置しているので、酸素ボンベ10から気体導入経路4を経由して加圧状態で微細気泡発生器2に供給される酸素O2ガスが液体導入経路3の上流側へ逆流するのを防止することができる。 In the oxygen-dissolved water generation device 100, the check valve 7 is disposed in the middle of the liquid introduction path 3, so that the oxygen cylinder 10 is supplied to the fine bubble generator 2 in a pressurized state via the gas introduction path 4. It is possible to prevent the oxygen O 2 gas from flowing back to the upstream side of the liquid introduction path 3.

酸素溶解水生成装置100においては、排液経路5の途中に流量調整バルブ8を配置しているので、流量調整バルブ8で排液経路5内の流量を調整することにより、気液接触槽1内の水圧を一定値に保持することができ、これにより酸素溶解水OWの酸素溶解率を一定に維持することができる。このように、酸素溶解水生成装置100を使用することにより、大量の酸素が溶解した酸素溶解水OWを効率良く、安定的に生成することができる。 In the oxygen-dissolved water generation device 100, the flow rate adjustment valve 8 is disposed in the middle of the drain path 5, so by adjusting the flow rate in the drain path 5 with the flow rate adjustment valve 8, the gas-liquid contact tank 1 The water pressure inside can be maintained at a constant value, and thereby the oxygen dissolution rate of the oxygen-dissolved water OW can be maintained constant. In this way, by using the oxygen-dissolved water generating device 100, oxygen-dissolved water OW in which a large amount of oxygen is dissolved can be efficiently and stably generated.

なお、酸素溶解水生成装置100は、酸素O2ガスを水Wに溶解させて酸素溶解水OWを生成する機能を有しているが、これに限定するものではなく、酸素O2ガス以外の気体を水W以外の液体に溶解して気体溶解水を生成することもできる。また、図1~図3に基づいて説明した酸素溶解水生成装置100は、本発明に係る気体溶解水生成装置の一例を示すものであり、本発明に係る気体溶解水生成装置は、前述した酸素溶解水生成装置100に限定されない。 Note that the oxygen-dissolved water generating device 100 has a function of dissolving oxygen O 2 gas in water W to generate oxygen-dissolved water OW, but is not limited to this, and can be used with other than oxygen O 2 gas. It is also possible to generate gas-dissolved water by dissolving gas in a liquid other than water W. Further, the oxygen-dissolved water generating device 100 described based on FIGS. 1 to 3 is an example of the gas-dissolved water generating device according to the present invention, and the gas-dissolved water generating device according to the present invention is similar to the one described above. The present invention is not limited to the oxygen-dissolved water generating device 100.

本発明に係る気体溶解水生成装置は、農林業、畜産業、水産業などの産業分野において、広く利用することができる。 The gas-dissolved water generating device according to the present invention can be widely used in industrial fields such as agriculture and forestry, livestock farming, and fisheries.

1 気液接触槽
1a,3b,24a 周壁部
1b 底板部
1c 天板部
1d 気体溜り
2 微細気泡発生器
3 液体導入経路
3a エルボー部
4 気体導入経路
4a 気体噴出口
5 排液経路
5a 開口部
6 排気手段
6a 排気管
7 逆止弁
8 流量調整バルブ
9 送水ポンプ
10 酸素ボンベ
11 酸素ガス調整器
12 大型気泡
13 水面
20 ケーシング
20a 上部隔壁
20b,24b 下部隔壁
21 気液旋回室
21c 中心軸
22 液体噴出口
23 気液吐出口
24 液体導入部
100 酸素溶解水生成装置
MB 微細気泡
MBW 微細気泡混じりの水
OW 酸素溶解水
S 旋回流
W 水
1 Gas-liquid contact tank 1a, 3b, 24a Peripheral wall portion 1b Bottom plate portion 1c Top plate portion 1d Gas reservoir 2 Fine bubble generator 3 Liquid introduction path 3a Elbow portion 4 Gas introduction path 4a Gas spout 5 Drainage path 5a Opening 6 Exhaust means 6a Exhaust pipe 7 Check valve 8 Flow rate adjustment valve 9 Water pump 10 Oxygen cylinder 11 Oxygen gas regulator 12 Large bubble 13 Water surface 20 Casing 20a Upper partition 20b, 24b Lower partition 21 Gas-liquid swirling chamber 21c Central axis 22 Liquid jet Outlet 23 Gas-liquid discharge port 24 Liquid introduction part 100 Oxygen-dissolved water generator MB Microbubbles MBW Water mixed with microbubbles OW Oxygen-dissolved water S Swirling flow W Water

Claims (1)

液体を収容可能な気密構造の気液接触槽と、
前記気液接触槽内に配置され前記気液接触槽の外部から供給される液体と気体とを混合して前記気液接触槽内に微細気泡混じりの液体を吐出する微細気泡発生器と、
前記気液接触槽外から前記微細気泡発生器に液体を供給する液体導入経路と、
前記気液接触槽外に露出した前記液体導入経路に配置した逆止弁と、
前記気液接触槽外から前記微細気泡発生器に気体を供給する気体導入経路と、
前記微細気泡発生器から前記気液接触槽内に吐出された微細気泡混じりの液体から形成された気体溶解液を前記気液接触槽外へ排出する排液経路と、
を備え、
前記微細気泡発生器が、
気液が旋回可能な筒状空間を有する気液旋回室と、
前記液体導入経路を経由して供給される液体を前記気液旋回室内に噴出する複数の液体噴出口と、
前記気体導入経路を経由して供給される気体を前記気液旋回室内に噴出する気体噴出口と、
前記気液旋回室内の微細気泡混じりの液体を前記気液接触槽内に吐出する気液吐出口と、を備え、
前記液体噴出口は、前記気液旋回室の中心軸に対し捻じれの位置をなす方向へ液体を噴出する位置に設けて、前記気液旋回室内に、その中心軸の周りを回転する旋回流を形成し、
前記気体噴出口は、前記旋回流の中心付近に前記気体を噴出することで、前記液体と前記気体とを前記気液旋回室内を旋回させながら下方へ移動させて、前記気液旋回室の下部隔壁に設けた前記気液吐出口を通過させることで微細気泡を発生させ、前記微細気泡混じりの液体として前記気液接触槽内へ流入させ、
前記気液接触槽内には、垂直起立状に前記排液経路の上流側を配置するとともに、前記排液経路の開口部を反重力方向に向けた状態で前記気液接触槽内に配置することで、前記微細気泡発生器から前記気液接触槽内へ流入させた前記微細気泡混じりの液体を、前記気液接触槽内で上昇させ、この上昇の際に前記微細気泡中の前記気体を前記液体に溶解させるとともに、余剰な前記気体の分離を生じさせて、前記気液接触槽内の水面よりも下に位置する前記開口部から前記気体溶解液を前記排液経路内に流入させて、前記排液経路内を下降させ、
前記排液経路の途中に設けた流量調整バルブで当該排液経路内の流量を調整することで、前記気液接触槽内の水圧を一定値に保持し、前記気体溶解液の気体溶解率を一定に維持している
気体溶解液生成装置。
A gas-liquid contact tank with an airtight structure capable of containing liquid;
a fine bubble generator disposed in the gas-liquid contact tank that mixes a liquid and gas supplied from outside the gas-liquid contact tank and discharges a liquid containing fine bubbles into the gas-liquid contact tank;
a liquid introduction path for supplying liquid to the microbubble generator from outside the gas-liquid contact tank;
a check valve disposed in the liquid introduction path exposed outside the gas-liquid contact tank;
a gas introduction path for supplying gas to the fine bubble generator from outside the gas-liquid contact tank;
a drainage path for discharging a gas solution formed from a liquid mixed with fine bubbles discharged from the fine bubble generator into the gas-liquid contact tank to the outside of the gas-liquid contact tank;
Equipped with
The fine bubble generator is
a gas-liquid swirling chamber having a cylindrical space in which gas and liquid can swirl;
a plurality of liquid ejection ports that eject the liquid supplied via the liquid introduction path into the gas-liquid swirling chamber;
a gas ejection port that ejects the gas supplied via the gas introduction path into the gas-liquid swirling chamber;
a gas-liquid discharge port for discharging the liquid containing fine bubbles in the gas-liquid swirling chamber into the gas-liquid contact tank;
The liquid spout is provided at a position that spouts liquid in a direction that is twisted with respect to the central axis of the gas-liquid swirling chamber, and creates a swirling flow that rotates around the central axis within the gas-liquid swirling chamber. form,
The gas spout is configured to eject the gas near the center of the swirling flow, thereby moving the liquid and the gas downward while swirling within the gas-liquid swirling chamber, thereby creating a lower part of the gas-liquid swirling chamber. Generating fine bubbles by passing through the gas-liquid discharge port provided in the partition wall, and causing the fine bubbles to flow into the gas-liquid contact tank as a liquid mixed with the fine bubbles,
In the gas-liquid contact tank, the upstream side of the drainage path is arranged in a vertically standing manner, and the opening of the drainage path is arranged in the gas-liquid contact tank with the opening facing in the anti-gravity direction. By doing so, the liquid containing fine bubbles that has flowed into the gas-liquid contact tank from the fine bubble generator is raised in the gas-liquid contact tank, and during this rise, the gas in the fine bubbles is removed. Dissolving the gas in the liquid and causing separation of the excess gas, causing the gas-dissolved liquid to flow into the drainage path from the opening located below the water surface in the gas-liquid contact tank. , lowering the liquid in the drainage path;
By adjusting the flow rate in the drainage path with a flow rate adjustment valve provided in the middle of the drainage path, the water pressure in the gas-liquid contact tank is maintained at a constant value, and the gas dissolution rate of the gas-dissolved liquid is adjusted. A gas solution generating device that maintains a constant state.
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Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003225546A (en) 2002-02-04 2003-08-12 Tashizen Techno Works:Kk Fine foam generation apparatus
JP2005000882A (en) 2003-06-13 2005-01-06 Aura Tec:Kk Micro bubble generator
JP2007185594A (en) 2006-01-12 2007-07-26 Tashizen Techno Works:Kk Waste liquid treatment apparatus and method
JP2010115586A (en) 2008-11-12 2010-05-27 Kawamoto Pump Mfg Co Ltd Microbubble generator
JP2018202375A (en) 2017-06-09 2018-12-27 穂栄株式会社 Gas-liquid mixing nozzle

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003225546A (en) 2002-02-04 2003-08-12 Tashizen Techno Works:Kk Fine foam generation apparatus
JP2005000882A (en) 2003-06-13 2005-01-06 Aura Tec:Kk Micro bubble generator
JP2007185594A (en) 2006-01-12 2007-07-26 Tashizen Techno Works:Kk Waste liquid treatment apparatus and method
JP2010115586A (en) 2008-11-12 2010-05-27 Kawamoto Pump Mfg Co Ltd Microbubble generator
JP2018202375A (en) 2017-06-09 2018-12-27 穂栄株式会社 Gas-liquid mixing nozzle

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