JP2007313464A - Gas dissolving apparatus - Google Patents

Gas dissolving apparatus Download PDF

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JP2007313464A
JP2007313464A JP2006147396A JP2006147396A JP2007313464A JP 2007313464 A JP2007313464 A JP 2007313464A JP 2006147396 A JP2006147396 A JP 2006147396A JP 2006147396 A JP2006147396 A JP 2006147396A JP 2007313464 A JP2007313464 A JP 2007313464A
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gas
liquid
cylindrical body
interface
side wall
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JP2006147396A
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JP4872459B2 (en
Inventor
Yasunari Maeda
康成 前田
Shigeyuki Yamaguchi
重行 山口
Kazumasa Rokushima
一雅 六嶋
Hisanori Shibata
尚紀 柴田
Hitoshi Kitamura
仁史 北村
Noriyuki Kitachi
範行 北地
Yoshiyasu Ito
良泰 伊藤
Takaya Nibu
貴也 丹生
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Panasonic Electric Works Co Ltd
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Matsushita Electric Works Ltd
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Priority to JP2006147396A priority Critical patent/JP4872459B2/en
Application filed by Matsushita Electric Works Ltd filed Critical Matsushita Electric Works Ltd
Priority to EP07744621A priority patent/EP2032240B1/en
Priority to US12/300,678 priority patent/US8128741B2/en
Priority to PCT/JP2007/061234 priority patent/WO2007142164A1/en
Priority to CN200780019327.1A priority patent/CN101454070B/en
Priority to AT07744621T priority patent/ATE530246T1/en
Priority to KR1020087030516A priority patent/KR101166606B1/en
Publication of JP2007313464A publication Critical patent/JP2007313464A/en
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a gas dissolving apparatus in which an area of an interface of liquid and gas stored in a roughly cylindrical body is increased and flow out of liquid with large bubbles mixed therein from the cylindrical body is prevented by deepening the depth of the stored liquid. <P>SOLUTION: This gas dissolving apparatus 1 stores gas and liquid in the cylindrical body 2, and dissolves gas into liquid by jetting the gas-liquid mixed fluid in which gas and liquid are mixed in the cylindrical body 2. The cylindrical body 2 is disposed with its central axis a tilted state in relation to the horizontal direction b, the interface 40 of the gas and liquid stored in the cylindrical body 2 is located at the intermediate part of a roughly cylindrical side wall part 21 of the cylindrical body 2, and an upper side above the interface 40 in the cylindrical body 2 and a lower side are used as a gas storing part 41 and a liquid storing part 42, respectively. A jetting port 31 is provided at the same level as the interface 40, or at a slightly lower level in the cylindrical body 2, for jetting the gas-liquid mixed fluid into the gas storing part 41 in the cylindrical body 2, and a flow out port 32 is provided near a lower end part of the cylindrical body 2 for running out the liquid in the cylindrical body 2. <P>COPYRIGHT: (C)2008,JPO&INPIT

Description

本発明は、気液溶解装置に関し、詳しくは例えば微細気泡を発生させる浴槽装置や、養殖での酸素補給・池や沼の水浄化(汚泥浮上)に利用される気液溶解タンクの構造に関するものである。   TECHNICAL FIELD The present invention relates to a gas-liquid dissolution apparatus, and more particularly to a bathtub apparatus that generates fine bubbles, and a structure of a gas-liquid dissolution tank used for oxygen supplementation in aquaculture and water purification of ponds and swamps (sludge floating). It is.

従来、気体溶解タンクを備え、この気体溶解タンク内に気体と液体とが混合した気液混合流体を噴射して攪拌させることで気体を液体に溶解させる気体溶解装置が知られているが(例えば特許文献1参照)、このような気体溶解タンクは設置スペースをとるため、小型の気体溶解装置が考案されている。   2. Description of the Related Art Conventionally, there is known a gas dissolution apparatus that includes a gas dissolution tank and that dissolves gas in a liquid by jetting and stirring a gas-liquid mixed fluid in which gas and liquid are mixed in the gas dissolution tank (for example, Such a gas dissolution tank takes up installation space, and thus a small gas dissolution apparatus has been devised.

これは、略円筒状の筒状体を流路の途中に備えたもので、筒状体内に気体と液体とを貯留すると共に、筒状体内に気体と液体とが混合した気液混合流体を噴射して攪拌させることで気体を液体に溶解させることができ、上記気体溶解タンクのような大掛かりなタンクを必要とせず省スペース化が図られるものであった。   This has a substantially cylindrical cylindrical body in the middle of the flow path, and stores gas and liquid in the cylindrical body, and a gas-liquid mixed fluid in which the gas and liquid are mixed in the cylindrical body. By jetting and stirring, the gas can be dissolved in the liquid, and a large tank such as the above-described gas dissolution tank is not required, and space saving can be achieved.

ところで、このような筒状体を備えた気体溶解装置にあっては、筒状体をその長手方向が水平となるように配置すると、気体と液体との界面が長手方向の全域に亘って形成されて界面の面積が大きくなるものの、貯留している液体の深さは筒状体の半径程度と浅くなり、液体に大きな気泡が多数存在する状態で流出されてしまい、また、筒状体をその長手方向が鉛直となるように配置する場合は、貯留している液体の深さが深くなるものの、気体と液体との界面が筒状体の断面積程度にしかならず、混合攪拌の効率が低い、という問題があった。
特開2004−290803号公報
By the way, in the gas dissolving apparatus provided with such a cylindrical body, when the cylindrical body is arranged so that its longitudinal direction is horizontal, an interface between the gas and the liquid is formed over the entire area in the longitudinal direction. Although the area of the interface is increased, the depth of the stored liquid is as shallow as the radius of the cylindrical body, and the liquid flows out in the state where there are many large bubbles in the liquid. When arranged so that the longitudinal direction is vertical, the depth of the stored liquid becomes deep, but the interface between the gas and the liquid is only about the cross-sectional area of the cylindrical body, and the efficiency of mixing and stirring is low. There was a problem.
JP 2004-290803 A

本発明は上記の点に鑑みてなされたものであり、その目的とするところは、略円筒状をした筒状体の内部に貯留される液体と気体との界面の面積を大きくすると共に、貯留される液体の深さを深くして大きな気泡が混合された状態で筒状体から流出することのない気体溶解装置を提供することを課題とするものである。   The present invention has been made in view of the above points, and the object of the present invention is to increase the area of the interface between the liquid and the gas stored inside the substantially cylindrical cylindrical body and An object of the present invention is to provide a gas dissolving device that does not flow out of a cylindrical body in a state in which large bubbles are mixed by increasing the depth of the liquid to be produced.

上記課題を解決するために請求項1に係る発明にあっては、両端が閉塞された略円筒状の筒状体2を備え、筒状体2内に気体と液体とを貯留すると共に、筒状体2内に気体と液体とが混合した気液混合流体を噴射して攪拌させることで気体を液体に溶解させる気体溶解装置1であって、筒状体2をその中心軸イが水平方向ロに対して傾斜するように配置し、筒状体2の略円筒状をした側壁部21の中間部に内部に貯留される気体と液体の界面40を位置させ、筒状体2内の界面40より上側の部分を気体貯留部41とすると共に界面40より下側の部分を液体貯留部42とし、筒状体2の側壁部21の界面40と同レベル又は界面40より若干下のレベルに気液混合流体を筒状体2内の気体貯留部42に噴射するための噴射口31を設け、筒状体2の液体貯留部42の下端部近傍に筒状体2内の液体を流出させる流出口32を設けて成ることを特徴とするものである。   In order to solve the above-mentioned problem, the invention according to claim 1 includes a substantially cylindrical tubular body 2 whose both ends are closed, stores gas and liquid in the tubular body 2, and A gas-dissolving device 1 for dissolving a gas in a liquid by injecting and stirring a gas-liquid mixed fluid in which a gas and a liquid are mixed in a cylindrical body 2, and the cylindrical body 2 has a central axis A in the horizontal direction. The interface 40 in the cylindrical body 2 is positioned so as to be inclined with respect to the gas and the liquid 40 stored in the middle portion of the substantially cylindrical side wall 21 of the cylindrical body 2. The part above 40 is a gas storage part 41 and the part below the interface 40 is a liquid storage part 42, at the same level as the interface 40 of the side wall part 21 of the cylindrical body 2 or slightly below the interface 40. The injection port 31 for injecting the gas-liquid mixed fluid to the gas storage part 42 in the cylindrical body 2 is provided, and the cylinder It is characterized in that comprising a lower end outlet 32 to the vicinity of the outflow of the liquid of the cylindrical body 2 in the liquid storage part 42 of the body 2 is provided.

このような構成とすることで、筒状体の内部に貯留される液体と気体との界面の面積を大きくすると共に、貯留される液体の深さを深くして大きな気泡が混合された状態で筒状体から流出するのを防止することができる。   By adopting such a configuration, the area of the interface between the liquid and gas stored inside the cylindrical body is increased, and the depth of the stored liquid is increased so that large bubbles are mixed. Outflow from the cylindrical body can be prevented.

また、請求項2に係る発明にあっては、請求項1に係る発明において、筒状体2の略円筒状をした側壁部21の長手方向に垂直な断面における下端底部に噴射口31を設けて成ることを特徴とするものである。   In the invention according to claim 2, in the invention according to claim 1, the injection port 31 is provided at the bottom of the lower end of the cross-section perpendicular to the longitudinal direction of the substantially cylindrical side wall portion 21 of the cylindrical body 2. It is characterized by comprising.

このような構成とすることで、気液混合流体の側壁部21の内壁面との衝突や界面40での衝突による攪拌、噴射される際の噴流による貯留している液体の攪拌により、気体の液体への溶解が促進される。   By adopting such a configuration, the gas mixture is stirred by collision with the inner wall surface of the side wall portion 21 of the gas-liquid mixed fluid, collision at the interface 40, and stirring of the stored liquid by the jet flow at the time of jetting. Dissolution in the liquid is promoted.

また、請求項3に係る発明にあっては、請求項2に係る発明において、噴射口31に接続される気液混合流体を筒状体2に搬送するための流入管51の接続端部を気体貯留部41の上流側Aに向けて傾斜させて成ることを特徴とするものである。   Moreover, in the invention which concerns on Claim 3, in the invention which concerns on Claim 2, the connection edge part of the inflow pipe 51 for conveying the gas-liquid mixed fluid connected to the injection nozzle 31 to the cylindrical body 2 is provided. It is made to incline toward the upstream side A of the gas storage part 41, It is characterized by the above-mentioned.

このような構成とすることで、気体貯留部41の内面の広範囲にわたって気液混合流体が衝突することとなり、気体の溶解がより一層促進される。   By setting it as such a structure, a gas-liquid mixed fluid will collide over the wide range of the inner surface of the gas storage part 41, and melt | dissolution of gas will be accelerated | stimulated further.

また、請求項4に係る発明にあっては、請求項1に係る発明において、筒状体2の略円筒状をした側壁部21の長手方向に垂直な断面における下端底部から左右にずれた位置に噴射口31を設けて成ることを特徴とするものである。   Moreover, in the invention which concerns on Claim 4, in the invention which concerns on Claim 1, the position which shifted | deviated right and left from the lower end bottom part in the cross section perpendicular | vertical to the longitudinal direction of the substantially cylindrical side wall part 21 of the cylindrical body 2. This is characterized in that an injection port 31 is provided.

このような構成とすることで、噴射口31から噴射された気液混合流体が筒状体2の左右一方側の内壁面に沿って旋回する旋回流となり、液体貯留部42に貯留されている液体の界面40で勢い良く衝突して激しく混合攪拌され、気体の溶解がより一層促進される。   With such a configuration, the gas-liquid mixed fluid ejected from the ejection port 31 becomes a swirl flow that swirls along the inner wall surface on the left and right sides of the cylindrical body 2, and is stored in the liquid storage unit 42. It collides vigorously at the liquid interface 40 and vigorously mixes and stirs, thereby further promoting the dissolution of the gas.

また、請求項5に係る発明にあっては、両端が閉塞された略円筒状の筒状体2を備え、筒状体2内に気体と液体とを貯留すると共に、筒状体2内に気体と液体とが混合した気液混合流体を噴射して攪拌させることで気体を液体に溶解させる気体溶解装置1であって、筒状体2をその中心軸イが水平方向ロに対して傾斜するように配置し、筒状体2の略円筒状をした側壁部21の中間部に内部に貯留される気体と液体の界面40を位置させ、筒状体2内の界面40より上側の部分を気体貯留部41とすると共に界面40より下側の部分を液体貯留部42とし、筒状体2の略円筒状をした側壁部21の長手方向に垂直な断面における上端部に噴射口31を設け、筒状体2の液体貯留部42の下端部近傍に筒状体2内の液体を流出させる流出口32を設けて成ることを特徴とするものである。   The invention according to claim 5 includes the substantially cylindrical tubular body 2 whose both ends are closed, stores gas and liquid in the tubular body 2, and stores in the tubular body 2. A gas dissolving device 1 for dissolving a gas in a liquid by injecting and stirring a gas-liquid mixed fluid in which a gas and a liquid are mixed, and the cylindrical body 2 is inclined with respect to the horizontal direction B. The gas / liquid interface 40 stored inside is located in the middle part of the substantially cylindrical side wall part 21 of the cylindrical body 2, and the part above the interface 40 in the cylindrical body 2. The gas storage part 41 and the part below the interface 40 are the liquid storage part 42, and the injection port 31 is provided at the upper end in the cross section perpendicular to the longitudinal direction of the substantially cylindrical side wall part 21 of the cylindrical body 2. An outlet 32 for allowing the liquid in the cylindrical body 2 to flow out in the vicinity of the lower end of the liquid storage section 42 of the cylindrical body 2. Is characterized in that made provided.

このような構成とすることで、噴射口31から噴射された気液混合流体が噴射口31の下方の界面40に勢い良く衝突して激しく混合攪拌され、これにより気体の溶解がより一層促進される。   With such a configuration, the gas-liquid mixed fluid ejected from the ejection port 31 vigorously collides with the interface 40 below the ejection port 31 and vigorously mixes and stirs, thereby further promoting gas dissolution. The

本発明にあっては、略円筒状をした筒状体の内部に貯留される液体と気体との界面の面積を大きくすると共に、貯留される液体の深さを深くして大きな気泡が混合された状態で筒状体から流出するのを防止することができ、略円筒状という簡単な構成の筒状体を利用して攪拌効率が高くて大きな気泡が流出しない気体溶解装置を構成することができる。   In the present invention, the area of the interface between the liquid and gas stored in the cylindrical body having a substantially cylindrical shape is increased, and the depth of the stored liquid is increased to mix large bubbles. Can be prevented from flowing out of the cylindrical body in a state where the gas is dissolved, and a gas dissolving device that has high stirring efficiency and does not flow out large bubbles can be configured by using a cylindrical body having a simple configuration of a substantially cylindrical shape. it can.

以下、本発明の一実施形態について図1乃至図3に基いて説明する。本発明の気体溶解装置は、例えば浴槽水中に微細気泡を発生させる微細気泡発生装置に用いられたりするもので、以下に微細気泡発生装置を設けた浴槽装置の例について説明する。   Hereinafter, an embodiment of the present invention will be described with reference to FIGS. 1 to 3. The gas dissolving apparatus of the present invention is used, for example, in a microbubble generator that generates microbubbles in bath water, and an example of a bathtub apparatus provided with a microbubble generator will be described below.

図2に微細気泡発生装置を設けた浴槽装置の全体構成を示す。これは、浴槽61の内側面に吸込口62と吐出口63とが設けてあり、浴槽11のフランジ部に空気吸込口64が設けてある。吸込口62は接続管65を介してポンプ66の吸い込み側に接続され、ポンプ66の吐出側は流入管51を介して気体溶解装置1の吸込側の噴射口31に接続されている。ポンプ66は遠心ポンプを利用したもの等が用いられるが特に限定されない。気体溶解装置1の吐出側の流出口32は流出管52を介して圧力開放部となるベンチュリ70の一端に接続され、ベンチュリ70の他端は接続管71を介して浴槽61の側面に設置された上記吐出口63に接続されている。気体が溶解した湯水が吐出口63より浴槽61の浴水中に吐出されると、浴水中で溶解気体が析出して微細気泡が発生するものである。なお、図中67は流入管51の途中と逆止弁68との間に接続される空気流路となる接続管、69は空気吸込口64と逆止弁68との間に接続される空気流路となる接続管である。   The whole structure of the bathtub apparatus which provided the fine bubble generator in FIG. 2 is shown. The suction port 62 and the discharge port 63 are provided on the inner surface of the bathtub 61, and the air suction port 64 is provided on the flange portion of the bathtub 11. The suction port 62 is connected to the suction side of the pump 66 through a connection pipe 65, and the discharge side of the pump 66 is connected to the injection port 31 on the suction side of the gas dissolving apparatus 1 through an inflow pipe 51. The pump 66 may be a centrifugal pump or the like, but is not particularly limited. The outlet 32 on the discharge side of the gas dissolving device 1 is connected to one end of a venturi 70 serving as a pressure release portion via an outflow pipe 52, and the other end of the venturi 70 is installed on the side surface of the bathtub 61 via a connection pipe 71. The discharge port 63 is connected. When hot water in which the gas is dissolved is discharged from the discharge port 63 into the bath water of the bathtub 61, the dissolved gas is precipitated in the bath water and fine bubbles are generated. In the figure, 67 is a connecting pipe serving as an air flow path connected between the midway of the inflow pipe 51 and the check valve 68, and 69 is air connected between the air suction port 64 and the check valve 68. It is a connecting pipe that becomes a flow path.

気体溶解装置1は、断面円形の直筒状をした側壁部21と、前記側壁部21の両側の端部を閉塞する端壁部22とからなる筒状体2で主体が構成される。筒状体2は、長手方向すなわち略円筒状をした側壁部21の中心軸イ(図1一点鎖線)が水平方向ロ(図1矢印)に対して10〜45°傾斜する姿勢で配置される。そして、傾斜した筒状体2は、上方側の端部が上流側Aの端部となると共に下方側の端部が下流側Bの端部となり、上流側Aに気液混合流体を筒状体2内に噴射するための噴射口31を形成すると共に下流側Bに液体を筒状体2内から流出する流出口32を形成してある。   The gas dissolving apparatus 1 is mainly composed of a cylindrical body 2 composed of a side wall portion 21 having a straight cylindrical shape with a circular cross section and end wall portions 22 that close end portions on both sides of the side wall portion 21. The cylindrical body 2 is arranged in such a posture that the central axis i (the dashed line in FIG. 1) of the side wall portion 21 having a longitudinal direction, that is, a substantially cylindrical shape, is inclined by 10 to 45 ° with respect to the horizontal direction (arrow in FIG. 1). . The inclined cylindrical body 2 has an upper end serving as the upstream A end and a lower end serving as the downstream B end, and the gas-liquid mixed fluid is tubular into the upstream A. An injection port 31 for injecting into the body 2 is formed, and an outflow port 32 through which liquid flows out from the cylindrical body 2 is formed on the downstream side B.

筒状体2内には、溶質となる例えば空気等の気体と、溶媒となる例えば水等の液体とが貯留されるもので、略円筒状をした側壁部21の上下方向の略中央付近に前記気体と液体との界面40が位置し、界面40より上部の上流側Aの部分が気体が貯留される気体貯留部41となると共に、界面40より下部の下流側Bの部分が液体が貯留される液体貯留部42となる。上記噴射口31は、気体貯留部41の内壁面(界面40より上流側Aの側壁部21または端壁部22の内壁面)か、界面40の位置か、あるいは界面40より若干下側の液体貯留部42の内壁面(界面40より下流側Bの側壁部21の内壁面)に形成され、流出口32は、液体貯留部42の端部付近の内壁面(界面40より下流側Bの側壁部21または端壁部22の内壁面)に形成される。本実施形態では、噴射口31は界面40より若干下側の液体貯留部42の上端付近の底面、すなわち側壁部21の液体貯留部42の上流側Aの端部付近の内面で、図3(b)の筒状体2の長手方向に垂直な断面図に示すように、左右中央部の下端底部に形成されている。そして、この噴射口31に流入管51の端部が接続されるもので、本実施形態では、図に示すように前記噴射口31に流入管51の端部が該噴射口31が形成されている側壁部21の内壁面に対して略垂直に接続されている。   In the cylindrical body 2, for example, a gas such as air serving as a solute and a liquid such as water serving as a solvent are stored, and approximately in the vicinity of the center of the substantially cylindrical side wall portion 21 in the vertical direction. The interface 40 between the gas and the liquid is located, and the portion on the upstream side A above the interface 40 becomes the gas storage portion 41 in which the gas is stored, and the portion on the downstream side B below the interface 40 stores the liquid. It becomes the liquid storage part 42 to be performed. The injection port 31 is a liquid located slightly below the interface 40, at the inner wall surface of the gas reservoir 41 (the inner wall surface of the side wall 21 or the end wall 22 on the upstream side A from the interface 40), at the position of the interface 40. The storage wall 42 is formed on the inner wall surface (the inner wall surface of the side wall portion 21 on the downstream side B from the interface 40), and the outlet 32 is the inner wall surface near the end of the liquid storage portion 42 (the side wall on the downstream side B from the interface 40. The inner wall surface of the portion 21 or the end wall portion 22 is formed. In the present embodiment, the injection port 31 is a bottom surface near the upper end of the liquid storage part 42 slightly below the interface 40, that is, an inner surface of the side wall part 21 near the end of the upstream side A of the liquid storage part 42 in FIG. As shown in the cross-sectional view perpendicular to the longitudinal direction of the cylindrical body 2b in FIG. The end of the inflow pipe 51 is connected to the injection port 31. In this embodiment, the end of the inflow pipe 51 is formed at the injection port 31 as shown in the figure. It is connected substantially perpendicularly to the inner wall surface of the side wall 21.

また本実施形態では、流出口32は液体貯留部42の下流側Bの端部付近の上向きとなった底面に形成され、この流出口32に流出管52の端部が接続されている。   In the present embodiment, the outflow port 32 is formed on the bottom surface that faces upward near the end on the downstream side B of the liquid reservoir 42, and the end of the outflow pipe 52 is connected to the outflow port 32.

また筒状体2の側壁部21には、弁(図示せず)を設けた空気抜き口33が形成してあり、この空気抜き口33の位置が上記気体貯留部41に貯留される気体と液体貯留部42に貯留される液体の界面40のレベルとなる。   The side wall 21 of the cylindrical body 2 is formed with an air vent 33 provided with a valve (not shown), and the position of the air vent 33 is stored in the gas reservoir 41 with the gas and liquid stored therein. It becomes the level of the interface 40 of the liquid stored in the part 42.

この気体溶解装置1の作用について説明する。   The operation of the gas dissolving apparatus 1 will be described.

筒状体2内には、液体貯留部42に液体が貯留されると共に気体貯留部41に気体が貯留されており、噴射口31から前記筒状体2内に貯留されているのと同じ液体および気体が混合した気液混合流体が噴射される。噴射口31は、上述したように界面40より若干下側の液体貯留部42の上端付近の底面に形成されているため、噴射口31から噴射される気液混合流体は液体貯留部42に貯留されている液体によって勢いを大きく減殺されることなく噴射されて、噴射口31と対向する側壁部21の上側の内壁面に衝突し、この内壁面で跳ね返って界面40にて液体貯留部42に貯留されている液体に衝突して攪拌される。また液体貯留部42に貯留されている液体は、前記のように気液混合流体が界面40に衝突して攪拌される他に、噴射口31から筒状体2内に噴射される気液混合流体によって攪拌される。   In the cylindrical body 2, the liquid is stored in the liquid storage section 42 and the gas is stored in the gas storage section 41, and the same liquid stored in the cylindrical body 2 from the injection port 31. And the gas-liquid mixed fluid in which the gas is mixed is ejected. Since the ejection port 31 is formed on the bottom surface near the upper end of the liquid storage part 42 slightly below the interface 40 as described above, the gas-liquid mixed fluid ejected from the ejection port 31 is stored in the liquid storage part 42. The liquid is injected without being greatly reduced in momentum, collides with the inner wall surface on the upper side of the side wall portion 21 facing the injection port 31, rebounds on the inner wall surface, and enters the liquid storage portion 42 at the interface 40. It collides with the stored liquid and is stirred. In addition, the liquid stored in the liquid storage unit 42 is mixed with the gas-liquid mixture injected into the cylindrical body 2 from the injection port 31 in addition to the gas-liquid mixed fluid colliding with the interface 40 and being stirred as described above. Stirred by fluid.

このように、気液混合流体の側壁部21の内壁面との衝突や界面40での衝突による攪拌、噴射される際の液体の攪拌等により、筒状体2内に貯留している気体および液体、気液混合流体中の気体および液体が混合され、気体の液体への溶解が促進される。すなわち、混合攪拌によるせん断により、液体に混合している気泡(気体)が細分化されて、液体と接する総表面積が大きくなるのに加えて、液体の気体との界面付近における気体の溶解濃度が混合攪拌による均一化により低減されて、気体の液体への溶解速度が上昇するため、気体の液体への溶解が促進される。   As described above, the gas stored in the cylindrical body 2 and the like by the collision of the gas-liquid mixed fluid with the inner wall surface of the side wall portion 21 or the collision at the interface 40, the stirring of the liquid when jetted, and the like. The liquid, the gas in the gas-liquid mixed fluid, and the liquid are mixed, and dissolution of the gas into the liquid is promoted. That is, the bubbles (gas) mixed with the liquid are subdivided by shearing by mixing and stirring, and the total surface area in contact with the liquid is increased. In addition, the dissolved concentration of the gas near the interface with the liquid gas is increased. Since it is reduced by homogenization by mixing and stirring, and the dissolution rate of the gas in the liquid increases, dissolution of the gas in the liquid is promoted.

気体の溶解が進行した液体は筒状体の液体貯留部42に貯留されるが、貯留されている液体には未溶解の気泡も数多く混合し、このような気泡は上方へ行くほど密に存在しており、液体貯留部42の下端部近傍では気泡はあまり存在せず、大きな気泡は殆ど存在しない。そして、気体の溶解が進行して大きな気泡が殆ど存在しない液体貯留部42の下端部の液体を流出口32から筒状体2外に流出させる。   The liquid in which the dissolution of the gas has progressed is stored in the liquid storage part 42 of the cylindrical body, but many undissolved bubbles are mixed in the stored liquid, and such bubbles are present as they move upward. In the vicinity of the lower end of the liquid reservoir 42, there are not many bubbles, and there are almost no large bubbles. Then, the dissolution of the gas proceeds, and the liquid at the lower end of the liquid storage part 42 in which there are almost no large bubbles is caused to flow out of the cylindrical body 2 from the outlet 32.

本発明では、気体溶解装置1の筒状体2をその側壁部21の中心軸イが水平方向ロに対して傾斜する姿勢で配置してあるため、気体と液体との界面40の面積を大きく取って混合攪拌の効率を向上させることができると共に、液体貯留部42に貯留している液体の深さを深くして気泡が筒状体2外に流出するのを抑えることができる。すなわち、筒状体2をその長手方向が水平となるように配置する場合は、気体と液体との界面40が長手方向の全域に亘って形成されて界面40の面積が大きくなるものの、液体貯留部42に貯留している液体の深さは筒状体2の半径程度となるため、液体に大きな気泡が多数存在する状態で流出されてしまい、好ましくなく、また、同じ筒状体2をその長手方向が鉛直となるように配置する場合は、液体貯留部42に貯留している液体の深さが筒状体2の長手方向の半分程度と深くなるものの、気体と液体との界面40が筒状体2の断面積程度にしか形成されないため、混合攪拌の効率が低く好ましくないが、上述したように筒状体2を傾斜させることによって、前記両者の長所を保ちつつ短所を補うことができるものである。   In the present invention, since the cylindrical body 2 of the gas dissolving device 1 is arranged in such a posture that the central axis i of the side wall portion 21 is inclined with respect to the horizontal direction B, the area of the interface 40 between the gas and the liquid is increased. In addition, the mixing and stirring efficiency can be improved, and the depth of the liquid stored in the liquid storage section 42 can be increased to prevent bubbles from flowing out of the cylindrical body 2. That is, when the cylindrical body 2 is arranged so that the longitudinal direction thereof is horizontal, the interface 40 between the gas and the liquid is formed over the entire area in the longitudinal direction and the area of the interface 40 is increased, but the liquid storage Since the depth of the liquid stored in the portion 42 is about the radius of the cylindrical body 2, the liquid flows out in a state where a large number of large bubbles exist in the liquid. In the case where the longitudinal direction is arranged to be vertical, the depth of the liquid stored in the liquid storage portion 42 becomes as deep as about half of the longitudinal direction of the cylindrical body 2, but the interface 40 between the gas and the liquid is Since it is formed only about the cross-sectional area of the cylindrical body 2, the efficiency of mixing and stirring is low, which is not preferable. However, by tilting the cylindrical body 2 as described above, it is possible to compensate for the disadvantages while maintaining the advantages of both. It can be done.

これにより、上述した混合攪拌の効率の向上および大きな気泡の流出防止を、略円筒状をした筒状体2を傾斜させるだけで達成することが可能となって、構成が簡単で製造が容易に行なわれるため製造コストの上昇を招くことがなく、また、装置の複雑化や大型化を招くことがないため省スペース化を図ることができるものである。   As a result, it is possible to improve the efficiency of mixing and stirring described above and prevent the outflow of large bubbles simply by inclining the cylindrical body 2 having a substantially cylindrical shape, and the configuration is simple and the manufacture is easy. Therefore, the manufacturing cost is not increased, and the apparatus is not complicated or enlarged, so that the space can be saved.

またこの時、噴射口31に接続される流入管51の端部が、筒状体2の長手方向に垂直な断面において、噴射口31から筒状体2の中心軸イに向く方向からずれた方向に接続されていてもよく、これにより、噴射口31から噴射された気液混合流体は、筒状体2の左右一方側の内壁面に衝突して旋回流となり、液体貯留部42に貯留されている液体の界面40に勢い良く衝突して激しく混合攪拌され、これにより気体の溶解がより一層促進される。   At this time, the end of the inflow pipe 51 connected to the injection port 31 is shifted from the direction toward the central axis A of the cylindrical body 2 from the injection port 31 in the cross section perpendicular to the longitudinal direction of the cylindrical body 2. The gas-liquid mixed fluid ejected from the ejection port 31 collides with the inner wall surface on one of the left and right sides of the cylindrical body 2 to form a swirling flow, and is stored in the liquid storage unit 42. The liquid interface 40 is vigorously mixed and stirred by vigorously colliding with the liquid interface 40, thereby further promoting the dissolution of the gas.

次に、他の実施形態について図4に基づいて説明するが、上述した実施形態と大部分において同じであるため同じ部分については説明を省略し、異なる部分について説明する。   Next, although other embodiment is described based on FIG. 4, since it is the same as that of embodiment mentioned above in most part, since it is the same, description is abbreviate | omitted and a different part is demonstrated.

本実施形態では、噴射口31に接続される流入管51の端部が、前記噴射口31が形成されている側壁部21の内壁面に対して略垂直な方向よりも上流側Aに傾斜する方向を向くように接続されている。噴射口31の長手方向における位置は上実施形態と同じである。   In the present embodiment, the end portion of the inflow pipe 51 connected to the injection port 31 is inclined to the upstream side A from the direction substantially perpendicular to the inner wall surface of the side wall portion 21 where the injection port 31 is formed. Connected to face in the direction. The position of the injection port 31 in the longitudinal direction is the same as in the above embodiment.

噴射口31から噴射された気液混合流体は、噴射口31と対向する内壁面に衝突して、この内壁面で跳ね返って液体貯留部42に貯留されている液体の界面40で衝突して液体に合流するが、合流するまで小さな液滴として筒状体2内を浮遊する状態となり、表面積が大きくなってこの間に気体の溶解が急速に行なわれる。本実施形態の場合、気液混合流体は気体貯留部41の上流側Aに向けて噴射されるため、上実施形態と比較すると、気体貯留部41の内面の広範囲にわたって気液混合流体が衝突することとなり、気体の溶解がより一層促進される。   The gas-liquid mixed fluid ejected from the ejection port 31 collides with the inner wall surface facing the ejection port 31, bounces off the inner wall surface, and collides at the liquid interface 40 stored in the liquid storage unit 42. However, until it merges, it becomes a state of floating in the cylindrical body 2 as a small droplet, and the surface area becomes large, and the gas is rapidly dissolved during this time. In the case of the present embodiment, since the gas-liquid mixed fluid is injected toward the upstream side A of the gas storage unit 41, the gas-liquid mixed fluid collides over a wide range of the inner surface of the gas storage unit 41 as compared with the above embodiment. As a result, dissolution of the gas is further promoted.

またこれにあたり、界面40が筒状体2の略円筒状をした側壁部21の上下方向の略中央付近に位置するようにし、側壁部21の界面40より上流側の部分に大きな気体貯留部41が形成されるようにしてあるため、気体貯留部41において気体の溶解がより多く行なわれる。   Further, in this case, the interface 40 is positioned in the vicinity of the substantially center in the vertical direction of the substantially cylindrical side wall portion 21 of the cylindrical body 2, and a large gas storage portion 41 is provided at a portion upstream of the interface 40 of the side wall portion 21. Therefore, more gas is dissolved in the gas reservoir 41.

また同様の更に他の実施形態として、図5に示すように、噴射口31を、筒状体2の長手方向に垂直な断面において、左右中央部の下端から左右にオフセットした(ずれた)位置に形成し、上方に向けて気液混合流体が噴射されるようにしてもよい。このようにすることでも、噴射口31から噴射された気液混合流体が筒状体2の左右一方側の内壁面に沿って旋回する旋回流となり、液体貯留部42に貯留されている液体の界面40で勢い良く衝突して激しく混合攪拌され、気体の溶解がより一層促進される。   Further, as another similar embodiment, as shown in FIG. 5, the injection port 31 is offset (shifted) to the left and right from the lower end of the left and right central portion in the cross section perpendicular to the longitudinal direction of the cylindrical body 2. The gas-liquid mixed fluid may be jetted upward. Also in this way, the gas-liquid mixed fluid ejected from the ejection port 31 becomes a swirl flow that swirls along the inner wall surface on the left and right sides of the cylindrical body 2, and the liquid stored in the liquid storage unit 42 It collides vigorously at the interface 40 and vigorously mixes and stirs, thereby further promoting the dissolution of the gas.

次に、更に他の実施形態について図6に基づいて説明するが、図1に示す実施形態と同じ部分については説明を省略し、異なる部分について説明する。   Next, still another embodiment will be described with reference to FIG. 6. However, the description of the same part as that of the embodiment shown in FIG. 1 will be omitted, and a different part will be described.

本実施形態では、噴射口31を、筒状体2の長手方向に垂直な断面において、左右中央部の上端部の下向きとなった内面に形成してあり、下方に向けて気液混合流体が噴射されるようになっている。   In the present embodiment, the injection port 31 is formed on the inner surface of the upper end portion of the left and right central portion that faces downward in the cross section perpendicular to the longitudinal direction of the cylindrical body 2, and the gas-liquid mixed fluid is directed downward. It comes to be injected.

噴射口31から噴射された気液混合流体は、噴射口31の下方の液体との界面40に勢い良く衝突して激しく混合攪拌され、これにより気体の溶解がより一層促進される。   The gas-liquid mixed fluid ejected from the ejection port 31 violently collides with the interface 40 with the liquid below the ejection port 31 and is vigorously mixed and stirred, thereby further promoting the dissolution of the gas.

また、図7に示す更に他の実施形態のように、筒状体2の側壁部21を、断面円形の直筒状をしたものではなく、二つの直筒状の部材を繋げた形状としてもよい。この例では、液体貯留部42の途中で側壁部21の中心軸イが屈曲した状態となっており、流出口32までの距離が長くなって大きな気泡が流出し難くなっている。   Further, as in still another embodiment shown in FIG. 7, the side wall portion 21 of the cylindrical body 2 is not a straight cylindrical shape having a circular cross section, but may be a shape in which two straight cylindrical members are connected. In this example, the central axis A of the side wall portion 21 is bent in the middle of the liquid storage portion 42, and the distance to the outflow port 32 becomes long and large bubbles are difficult to flow out.

本発明の気体溶解装置の一実施形態の斜視図である。It is a perspective view of one embodiment of the gas dissolution apparatus of the present invention. 同上の気体溶解装置を備えた浴槽装置の全体構成図である。It is a whole block diagram of the bathtub apparatus provided with the gas dissolving apparatus same as the above. 同上の気体溶解装置の断面図を示し、(a)は長手方向に沿った縦断面図であり、(b)は(a)のA−A断面図である。Sectional drawing of a gas dissolving apparatus same as the above is shown, (a) is a longitudinal cross-sectional view along a longitudinal direction, (b) is AA sectional drawing of (a). 他の実施形態の気体溶解装置の長手方向に沿った縦断面図である。It is a longitudinal cross-sectional view along the longitudinal direction of the gas dissolving apparatus of other embodiment. 更に他の実施形態の気体溶解装置の断面図を示し、(a)は長手方向に沿った縦断面図であり、(b)は(a)のA−A断面図である。Furthermore, sectional drawing of the gas dissolving apparatus of other embodiment is shown, (a) is a longitudinal cross-sectional view along a longitudinal direction, (b) is AA sectional drawing of (a). 更に他の実施形態の気体溶解装置の断面図を示し、(a)は長手方向に沿った縦断面図であり、(b)は(a)のA−A断面図である。Furthermore, sectional drawing of the gas dissolving apparatus of other embodiment is shown, (a) is a longitudinal cross-sectional view along a longitudinal direction, (b) is AA sectional drawing of (a). 本発明の他の実施形態の断面図である。It is sectional drawing of other embodiment of this invention.

符号の説明Explanation of symbols

1 気体溶解装置
2 筒状体
21 側壁部
31 噴射口
32 流出口
40 界面
41 気体貯留部
イ 中心軸
ロ 水平方向
DESCRIPTION OF SYMBOLS 1 Gas dissolving apparatus 2 Cylindrical body 21 Side wall part 31 Injection port 32 Outflow port 40 Interface 41 Gas storage part A Center axis B Horizontal direction

Claims (5)

両端が閉塞された略円筒状の筒状体を備え、筒状体内に気体と液体とを貯留すると共に、筒状体内に気体と液体とが混合した気液混合流体を噴射して攪拌させることで気体を液体に溶解させる気体溶解装置であって、筒状体をその中心軸が水平方向に対して傾斜するように配置し、筒状体の略円筒状をした側壁部の中間部に内部に貯留される気体と液体の界面を位置させ、筒状体内の界面より上側の部分を気体貯留部とすると共に界面より下側の部分を液体貯留部とし、筒状体の側壁部の界面と同レベル又は界面より若干下のレベルに気液混合流体を筒状体内の気体貯留部に噴射するための噴射口を設け、筒状体の液体貯留部の下端部近傍に筒状体内の液体を流出させる流出口を設けて成ることを特徴とする気体溶解装置。   Provided with a substantially cylindrical cylindrical body closed at both ends, storing gas and liquid in the cylindrical body, and injecting and stirring a gas-liquid mixed fluid in which the gas and liquid are mixed into the cylindrical body A gas dissolving device for dissolving a gas in a liquid, wherein the cylindrical body is disposed such that its central axis is inclined with respect to the horizontal direction, and is disposed in an intermediate portion of the substantially cylindrical side wall portion of the cylindrical body. The gas-liquid interface stored in the cylindrical body is positioned, and the part above the interface in the cylindrical body is the gas storage part and the part below the interface is the liquid storage part. An injection port for injecting the gas-liquid mixed fluid into the gas storage part in the cylindrical body is provided at the same level or a level slightly below the interface, and the liquid in the cylindrical body is placed near the lower end of the liquid storage part of the cylindrical body. A gas dissolving apparatus comprising an outlet for discharging. 筒状体の略円筒状をした側壁部の長手方向に垂直な断面における下端底部に噴射口を設けて成ることを特徴とする請求項1記載の気体溶解装置。   2. The gas dissolving apparatus according to claim 1, wherein an injection port is provided at the bottom of the lower end in a cross section perpendicular to the longitudinal direction of the substantially cylindrical side wall of the cylindrical body. 噴射口に接続される気液混合流体を筒状体に搬送するための流入管の接続端部を気体貯留部の上流側に向けて傾斜させて成ることを特徴とする請求項2記載の気体溶解装置。   3. The gas according to claim 2, wherein the connection end of the inflow pipe for conveying the gas-liquid mixed fluid connected to the injection port to the cylindrical body is inclined toward the upstream side of the gas storage section. Melting device. 筒状体の略円筒状をした側壁部の長手方向に垂直な断面における下端底部から左右にずれた位置に噴射口を設けて成ることを特徴とする請求項1記載の気体溶解装置。   2. The gas dissolving apparatus according to claim 1, wherein an injection port is provided at a position shifted to the left and right from the bottom of the lower end in a cross section perpendicular to the longitudinal direction of the substantially cylindrical side wall of the cylindrical body. 両端が閉塞された略円筒状の筒状体を備え、筒状体内に気体と液体とを貯留すると共に、筒状体内に気体と液体とが混合した気液混合流体を噴射して攪拌させることで気体を液体に溶解させる気体溶解装置であって、筒状体をその中心軸が水平方向に対して傾斜するように配置し、筒状体の略円筒状をした側壁部の中間部に内部に貯留される気体と液体の界面を位置させ、筒状体内の界面より上側の部分を気体貯留部とすると共に界面より下側の部分を液体貯留部とし、筒状体の略円筒状をした側壁部の長手方向に垂直な断面における上端部に噴射口を設け、筒状体の液体貯留部の下端部近傍に筒状体内の液体を流出させる流出口を設けて成ることを特徴とする気体溶解装置。
Provided with a substantially cylindrical cylindrical body closed at both ends, storing gas and liquid in the cylindrical body, and injecting and stirring a gas-liquid mixed fluid in which the gas and liquid are mixed into the cylindrical body A gas dissolving device for dissolving a gas in a liquid, wherein the cylindrical body is disposed such that its central axis is inclined with respect to the horizontal direction, and is disposed in an intermediate portion of the substantially cylindrical side wall portion of the cylindrical body. The interface between the gas and liquid stored in the cylinder is positioned, the portion above the interface inside the cylindrical body is used as the gas storage portion, and the portion below the interface is used as the liquid storage portion, so that the cylindrical body is substantially cylindrical. A gas characterized in that an injection port is provided at the upper end in a cross section perpendicular to the longitudinal direction of the side wall, and an outlet for allowing the liquid in the cylindrical body to flow out is provided in the vicinity of the lower end of the liquid storage portion of the cylindrical body. Melting device.
JP2006147396A 2006-05-26 2006-05-26 Gas dissolving device Expired - Fee Related JP4872459B2 (en)

Priority Applications (7)

Application Number Priority Date Filing Date Title
JP2006147396A JP4872459B2 (en) 2006-05-26 2006-05-26 Gas dissolving device
US12/300,678 US8128741B2 (en) 2006-05-26 2007-05-28 Gas dissolving apparatus
PCT/JP2007/061234 WO2007142164A1 (en) 2006-05-26 2007-05-28 Gas dissolving apparatus
CN200780019327.1A CN101454070B (en) 2006-05-26 2007-05-28 Gas dissolving apparatus
EP07744621A EP2032240B1 (en) 2006-05-26 2007-05-28 Gas dissolving apparatus
AT07744621T ATE530246T1 (en) 2006-05-26 2007-05-28 GAS DISSOLVING DEVICE
KR1020087030516A KR101166606B1 (en) 2006-05-26 2007-05-28 Gas dissolving apparatus

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010029754A (en) * 2008-07-25 2010-02-12 Panasonic Electric Works Co Ltd Gas dissolving apparatus
JP2010104870A (en) * 2008-10-28 2010-05-13 Panasonic Electric Works Co Ltd Gas dissolving apparatus
JP2011092812A (en) * 2009-10-27 2011-05-12 Panasonic Electric Works Co Ltd Gas dissolving apparatus
JP2018192465A (en) * 2017-05-18 2018-12-06 株式会社カリタス&ベリタス Device and method for producing microscopic bubbles

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2854002A (en) * 1957-04-22 1958-09-30 Univ Minnesota Oxygenator
JPH09173804A (en) * 1995-10-26 1997-07-08 Idec Izumi Corp Method for dissolving and mixing gas and liquid and device therefor
JPH10244138A (en) * 1997-02-28 1998-09-14 Idec Izumi Corp Method and device for mixing and dissolving gas and liquid
JP2002239537A (en) * 2001-02-14 2002-08-27 Araco Corp Excess gas separation tank
JP2004313847A (en) * 2003-04-11 2004-11-11 Nippon Kankyo Kagaku:Kk Gas-liquid dissolving device, water treatment system using the device and water treatment method
JP2005329100A (en) * 2004-05-21 2005-12-02 Matsushita Electric Works Ltd Microbubble forming device

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2854002A (en) * 1957-04-22 1958-09-30 Univ Minnesota Oxygenator
JPH09173804A (en) * 1995-10-26 1997-07-08 Idec Izumi Corp Method for dissolving and mixing gas and liquid and device therefor
JPH10244138A (en) * 1997-02-28 1998-09-14 Idec Izumi Corp Method and device for mixing and dissolving gas and liquid
JP2002239537A (en) * 2001-02-14 2002-08-27 Araco Corp Excess gas separation tank
JP2004313847A (en) * 2003-04-11 2004-11-11 Nippon Kankyo Kagaku:Kk Gas-liquid dissolving device, water treatment system using the device and water treatment method
JP2005329100A (en) * 2004-05-21 2005-12-02 Matsushita Electric Works Ltd Microbubble forming device

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010029754A (en) * 2008-07-25 2010-02-12 Panasonic Electric Works Co Ltd Gas dissolving apparatus
JP2010104870A (en) * 2008-10-28 2010-05-13 Panasonic Electric Works Co Ltd Gas dissolving apparatus
JP2011092812A (en) * 2009-10-27 2011-05-12 Panasonic Electric Works Co Ltd Gas dissolving apparatus
JP2018192465A (en) * 2017-05-18 2018-12-06 株式会社カリタス&ベリタス Device and method for producing microscopic bubbles

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