JP2013043112A - Gas-liquid separation tank and gas-liquid mixture dissolving apparatus - Google Patents

Gas-liquid separation tank and gas-liquid mixture dissolving apparatus Download PDF

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JP2013043112A
JP2013043112A JP2011181809A JP2011181809A JP2013043112A JP 2013043112 A JP2013043112 A JP 2013043112A JP 2011181809 A JP2011181809 A JP 2011181809A JP 2011181809 A JP2011181809 A JP 2011181809A JP 2013043112 A JP2013043112 A JP 2013043112A
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JP5570074B2 (en
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Soichiro Osaki
荘一郎 大崎
Yoshihiro Teruya
佳浩 照屋
Yukio Hashimoto
幸雄 橋本
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Nikuni KK
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Abstract

PROBLEM TO BE SOLVED: To provide a gas-liquid separation tank which can suppress labor and cost required for its manufacture by devising elimination of the necessity of boring a hole on a main member which is cylindrical and is made of a resin or welding a pipe to the main member.SOLUTION: An upper side cylindrical part 34 is continuously attached to the upper side opening of a body cylindrical vessel 31 which is cylindrical and is made of the resin. The upper side cylindrical part 34 has, at its flank, a gas-liquid mixed fluid inlet 32 for introducing gas-liquid mixed fluid into the body cylindrical vessel 31 from a tangential direction and further has, at its upper end surface, a gas outlet 33 for discharging gas separated from the fluid. At its lower side opening of the body cylindrical vessel 31, a bottom plate part 36 having a liquid taking-out port 35 is provided. A buffer plate 38 is provided above the liquid taking-out port 35 of the bottom plate part 36 via a liquid passage gap 37.

Description

本発明は、気液混合溶解工程で液中に溶解されなかった気体を分離する気液分離タンクおよびその気液分離タンクを用いた気液混合溶解装置に関する。   The present invention relates to a gas-liquid separation tank that separates a gas that has not been dissolved in a liquid in a gas-liquid mixing and dissolving step, and a gas-liquid mixing and dissolving apparatus that uses the gas-liquid separation tank.

図4に示されるように、マイクロバブルなどの微細気泡を発生させる微細気泡発生装置などとして用いられる気液混合溶解装置1は、液中に気体を混合する渦流ポンプ2と、さらに液中に気体を溶解させる溶解タンク3と、さらに液中に溶解されなかった気体を分離する気液分離タンク4とを、配管により順次接続したものである(例えば、特許文献1参照)。   As shown in FIG. 4, a gas-liquid mixing and dissolving apparatus 1 used as a microbubble generator for generating microbubbles such as microbubbles, etc. includes a vortex pump 2 that mixes gas in liquid, and further gas in liquid A dissolution tank 3 that dissolves the gas and a gas-liquid separation tank 4 that separates a gas that has not been dissolved in the liquid are sequentially connected by piping (see, for example, Patent Document 1).

また、上記気液分離タンクとしては、本体容器の天井部に気体出口、中央付近に気液混合流体入口、下方に液体出口、および、液体出口の直前に隔壁をそれぞれ有し、本体容器下部は底板により密閉された気液分離器がある(例えば、特許文献2参照)。   The gas-liquid separation tank has a gas outlet at the ceiling of the main body container, a gas-liquid mixed fluid inlet near the center, a liquid outlet at the lower side, and a partition wall just before the liquid outlet. There is a gas-liquid separator sealed with a bottom plate (see, for example, Patent Document 2).

この特許文献2に記載された気液分離器の気液混合流体入口は、本体容器の円筒接線方向に接続されているため、該入口から流入した気液混合流体は円筒の内壁に沿って渦巻き状に流れ、気液混合流体の流入速度が速いと、生じる渦の勢いが強く、液と気体の混合体よりなるロート状の渦は本体容器の下方まで消えることが無いが、液流排出口の直前に隔壁を設けると、渦は隔壁に邪魔されて、隔壁より下方では渦は弱くなるか消えてしまうので、渦の存在しない場所では気体は液の深部まで到達することはできず、比重の差により気体は浮上する。さらに、液が液体出口に到達する前に一度隔壁の下部を通過するように構成してあるので、気体はなおのことその部分を通過することはできず、気液分離が効率良くなされる。   Since the gas-liquid mixed fluid inlet of the gas-liquid separator described in Patent Document 2 is connected in the cylinder tangential direction of the main body container, the gas-liquid mixed fluid flowing from the inlet swirls along the inner wall of the cylinder. If the flow velocity of the gas-liquid mixed fluid is high, the vortex generated is strong, and the funnel-shaped vortex consisting of a mixture of liquid and gas does not disappear to the bottom of the main body container. If a partition is provided immediately before the vortex, the vortex is obstructed by the partition, and the vortex is weakened or disappears below the partition, so that the gas cannot reach the deep part of the liquid in the place where the vortex does not exist, and the specific gravity The gas rises due to the difference. Further, since the liquid once passes through the lower part of the partition wall before reaching the liquid outlet, the gas cannot pass through the part yet, and the gas-liquid separation is efficiently performed.

また、気液分離タンクとしては、次のような気泡除去装置もある。この気泡除去装置は、本体に、円筒状の流入空間と逆円錐形状の円錐空間と小円筒状の流出空間を形成し、上記流入空間に開口する入口と流出空間に開口する流出口は、それぞれ各空間の接線方向に設けられている。上記流入空間の上方には、気泡を排出する排出口があり、排出口と流入空間の間には弁室があり、この弁室内には、通孔を有するシリンダが設けられている。このシリンダにはプレ−トを有するキャップ状のフロ−トが嵌められ、このフロ−トは、上記流入空間に気泡が一定量溜まったとき、内部圧で上昇され、通孔を開き、気泡のみを排出口から排出するので、流体中に含まれている気泡を効率よく除去できる(例えば、特許文献3参照)。   Further, as the gas-liquid separation tank, there is the following bubble removing device. This bubble removing device forms a cylindrical inflow space, an inverted conical conical space, and a small cylindrical outflow space in the main body, and an inlet opening to the inflow space and an outlet opening to the outflow space are respectively It is provided in the tangential direction of each space. Above the inflow space, there is a discharge port for discharging bubbles, and there is a valve chamber between the discharge port and the inflow space, and a cylinder having a through hole is provided in the valve chamber. This cylinder is fitted with a cap-like float having a plate. When a certain amount of bubbles accumulates in the inflow space, the float is raised by internal pressure, opens a through hole, and only the bubbles. Is discharged from the discharge port, so that bubbles contained in the fluid can be efficiently removed (see, for example, Patent Document 3).

特開2001−129377号公報JP 2001-129377 A 特開2003−265984号公報JP 2003-265984 A 特開2001−137615号公報JP 2001-137615 A

特許文献2に記載された気液分離器は、本体容器に気体出口、気液混合流体入口、液体出口および隔壁などを直接取り付けているので、構造が単純であるように見えるが、このような構造とするには、本体容器を金属製にして、本体容器に配管や隔壁などを溶接付けする必要があり、製造に手間がかかるとともにコストがかかる問題がある。   Since the gas-liquid separator described in Patent Document 2 has a gas outlet, a gas-liquid mixed fluid inlet, a liquid outlet, a partition wall, and the like directly attached to the main body container, it seems that the structure is simple. In order to obtain a structure, it is necessary to make the main body container made of metal and weld pipes and partition walls to the main body container.

また、特許文献3に記載された気泡除去装置は、本体上部の気泡を排出する排出口と流入空間の間に弁室を設け、この弁室内にシリンダおよびフロ−トなどの複雑な気泡排出機構を設置する必要があり、製造に手間がかかるとともにコストがかかる問題がある。   In addition, the bubble removing device described in Patent Document 3 has a valve chamber provided between a discharge port for discharging bubbles in the upper part of the main body and an inflow space, and a complicated bubble discharging mechanism such as a cylinder and a float in the valve chamber. There is a problem that it takes time to manufacture and costs.

本発明は、このような点に鑑みなされたもので、円筒形樹脂製の主要な部材に穴を開けたり配管を溶接する必要をなくす工夫をすることで製造にかかる手間やコストを抑えることができる気液分離タンクを提供するとともに、この気液分離タンクを用いた気液混合溶解装置を提供することを目的とする。   This invention is made in view of such a point, and can suppress the effort and cost concerning manufacture by devising which eliminates the need to make a hole in a cylindrical resin-made main member or to weld piping. An object of the present invention is to provide a gas-liquid separation tank that can be used, and to provide a gas-liquid mixing and dissolving apparatus using the gas-liquid separation tank.

請求項1に記載された発明は、開口部が上下方向に設置された円筒形樹脂製の本体円筒容器と、上記本体円筒容器の上側の開口部に連続的に取り付けられ、気液混合流体を接線方向から上記本体円筒容器内に導入する気液混合流体入口を側面に有するとともに、液中から分離された気体を排出する気体出口を上端面に有する上側円筒部と、上記本体円筒容器の下側の開口部に設けられた液取出口を有する底板部と、上記底板部の液取出口上に通液間隙を介して設けられたバッファプレートとを具備した気液分離タンクである。   The invention described in claim 1 is continuously attached to a cylindrical resin-made main body cylindrical container in which an opening is installed in the vertical direction, and an upper opening of the main body cylindrical container. An upper cylindrical portion having a gas outlet for introducing a gas-liquid mixed fluid to be introduced into the main body cylindrical container from the tangential direction on the side surface and a gas outlet for discharging gas separated from the liquid on the upper end surface; and a lower part of the main body cylindrical container A gas-liquid separation tank comprising a bottom plate portion having a liquid outlet provided in a side opening, and a buffer plate provided on the liquid outlet of the bottom plate portion via a liquid passage.

請求項2に記載された発明は、請求項1記載の気液分離タンクにおける液取出口が、底板部の中央部に穿設され、バッファプレートは、上記底板部と平行にかつ上記液取出口と同心状に配置された上記液取出口よりも大きな平板であり、上記底板部と上記バッファプレートとの間の通液間隙は、本体円筒容器内の4方に向かって開口された気液分離タンクである。   According to a second aspect of the present invention, the liquid outlet in the gas-liquid separation tank according to the first aspect is drilled in the center of the bottom plate, and the buffer plate is parallel to the bottom plate and the liquid outlet. The liquid-liquid separation between the bottom plate and the buffer plate is a gas-liquid separation that is open toward the four sides in the main body cylindrical container. It is a tank.

請求項3に記載された発明は、請求項1または2記載の気液分離タンクにおいて、上側円筒部内に気液混合流体入口の上側部から気体出口にわたって漸次径小に設けられた円錐形状の抜気案内板を具備した気液分離タンクである。   According to a third aspect of the present invention, there is provided a gas-liquid separation tank according to the first or second aspect, wherein a conical shape is provided in the upper cylindrical portion that is gradually reduced in diameter from the upper side of the gas-liquid mixed fluid inlet to the gas outlet. It is a gas-liquid separation tank equipped with an air guide plate.

請求項4に記載された発明は、液中に気体を混合する渦流ポンプと、上記渦流ポンプに配管により接続され、液中に気体を溶解させる溶解タンクと、上記溶解タンクに配管により接続され、液中に溶解されなかった気体を分離する請求項1乃至3のいずれか記載の気液分離タンクとを具備した気液混合溶解装置である。   The invention described in claim 4 is connected to the vortex pump that mixes the gas in the liquid, the vortex pump to the vortex pump by a pipe, and dissolves the gas in the liquid, and is connected to the lysis tank by the pipe. A gas-liquid mixing and dissolving apparatus comprising the gas-liquid separation tank according to any one of claims 1 to 3, which separates a gas that has not been dissolved in the liquid.

請求項1記載の発明によれば、開口部が上下方向に設置された本体円筒容器を、気液混合流体入口および気体出口を有する上側円筒部や、液取出口およびバッファプレートを有する底板部とは別個に設けたので、本体円筒容器に気液混合流体入口、気体出口および液取出口の穴加工をしたり配管やバッファプレートを溶接する必要性をなくして、主要な本体円筒容器を安価な配管部材などとして用いられる円筒形樹脂製とすることができるので、製造にかかる手間やコストを抑えることができる気液分離タンクを提供できる。   According to the invention described in claim 1, the main body cylindrical container in which the opening is installed in the vertical direction, the upper cylindrical portion having the gas-liquid mixed fluid inlet and the gas outlet, the bottom plate portion having the liquid outlet and the buffer plate, Are provided separately, eliminating the need for drilling the gas-liquid mixed fluid inlet, gas outlet and liquid outlet in the main body cylindrical container and welding pipes and buffer plates, making the main main body cylindrical container inexpensive. Since it can be made of a cylindrical resin used as a piping member or the like, it is possible to provide a gas-liquid separation tank that can reduce labor and cost for manufacturing.

また、気液混合流体入口を接線方向に設けることによって、本体円筒容器内で液と気体を旋回させ、液中に溶解しなかった気体を本体円筒容器内の中心軸部に気泡として集め、気体出口から外部へ排出するが、一方では、液取出口上に通液間隙を介してバッファプレートを設けることによって、本体円筒容器の中心軸部に形成されようとする気泡柱をバッファプレートにより中心軸部の周囲に拡散させて、きれいな気泡柱が本体円筒容器の中心軸部に形成されることを防止することで、本体円筒容器の中心軸部に集まった気泡がそのまま液とともに液取出口から流出することを防止でき、また、本体円筒容器の中心軸部と内壁面との差圧が大きくならないように旋回渦流を乱して、本体円筒容器の中心軸部で負圧が立つことを防止することで、上部の気体出口から気体を効率よく排出できるとともに、液中に溶解している気体までも目に見える大きさの気泡に成長して液から分離する気泡化を防止できる。   Further, by providing the gas-liquid mixed fluid inlet in the tangential direction, the liquid and the gas are swirled in the main body cylindrical container, and the gas that has not been dissolved in the liquid is collected as bubbles in the central shaft portion in the main body cylindrical container, While discharging from the outlet to the outside, on the other hand, by providing a buffer plate on the liquid outlet via a liquid passage gap, the bubble column to be formed in the central axis portion of the main body cylindrical container is removed by the buffer plate from the central axis. The air bubbles gathered around the central shaft of the main body cylindrical container flow out of the liquid outlet with the liquid as it is. In addition, the swirl vortex is disturbed so that the differential pressure between the central shaft portion of the main body cylindrical container and the inner wall surface does not increase, and negative pressure is prevented from standing at the central shaft portion of the main body cylindrical container. By With a gas can be efficiently discharged from the top of the gas outlet, thereby preventing bubbling to separate from the liquid to grow to a size of bubbles visible to the gas dissolved in the liquid.

請求項2記載の発明によれば、バッファプレートは、本体円筒容器の底板部と平行にかつ底板部の中央部に穿設された液取出口と同心状に配置された液取出口よりも大きな平板であり、底板部とバッファプレートとの間の通液間隙は、本体円筒容器内の4方に向かって開口されたので、接線方向から本体円筒容器内に流入して本体円筒容器内で旋回しながら底板部の中央部から流出しようとしていた本体円筒容器中心軸部回りの高速の渦が、バッファプレートによってバランスを崩され、上記中心軸部の周囲に分散して複数の小さな渦となり、その分、上記中心軸部回りの渦は緩やかに旋回することにより、上記中心軸部回りの高速の渦による強力な遠心力が減少し、本体円筒容器の中心軸部に発生する強い負圧部がなくなることで、液中に溶解している気体の負圧部への分離(微細な気泡の成長を含む)を抑えつつ、液中に比較的大きな気泡状態で混在する気体の塊だけを集めることができ、かつ微細な気泡はバッファプレートにより反射する上昇流に載せて本体円筒容器内で旋回させることによって本体円筒容器内に長時間滞留させ、微細な気泡の液中への溶解を促進させることができる。   According to the invention described in claim 2, the buffer plate is larger than the liquid outlet arranged parallel to the bottom plate portion of the main body cylindrical container and concentrically with the liquid outlet formed in the center portion of the bottom plate portion. Since it is a flat plate and the liquid passage gap between the bottom plate and the buffer plate is opened in four directions in the main body cylindrical container, it flows into the main body cylindrical container from the tangential direction and swivels in the main body cylindrical container. However, the high-speed vortex around the central axis of the main body cylindrical container that was about to flow out from the center of the bottom plate was unbalanced by the buffer plate and dispersed around the central axis to form a plurality of small vortices. The vortex around the central shaft portion is gently swirled to reduce the strong centrifugal force due to the high-speed vortex around the central shaft portion, and the strong negative pressure portion generated at the central shaft portion of the main body cylindrical container is reduced. By disappearing, in the liquid It is possible to collect only gas lumps mixed in a relatively large bubble state in the liquid while suppressing the separation of the dissolved gas into the negative pressure part (including the growth of fine bubbles), and the fine bubbles Can be retained in the main body cylindrical container for a long time by being swung in the main body cylindrical container on the upward flow reflected by the buffer plate, and can promote dissolution of fine bubbles in the liquid.

請求項3記載の発明によれば、上側円筒部内に設置された円錐形状の抜気案内板により、本体円筒容器内の液から分離されて旋回する気体を気体出口へと円滑に案内し排出することができる。   According to the third aspect of the present invention, the conical extraction guide plate installed in the upper cylindrical portion smoothly guides and discharges the swirling gas separated from the liquid in the main body cylindrical container to the gas outlet. be able to.

請求項4記載の発明によれば、気液分離タンクの本体円筒容器を、気液混合流体入口、気体出口および液取出口の穴加工をしたり配管やバッファプレートを溶接する必要性をなくして、主要な本体円筒容器を安価な配管部材などとして用いられる円筒形樹脂製とすることができるので、その本体円筒容器を主材とする気液分離タンクに対し渦流ポンプおよび溶解タンクを接続して、安価な気液混合溶解装置を提供できる。   According to the fourth aspect of the present invention, it is possible to eliminate the necessity of drilling the gas-liquid mixed fluid inlet, the gas outlet, and the liquid outlet in the main body cylindrical container of the gas-liquid separation tank or welding the pipe and the buffer plate. Since the main body cylindrical container can be made of a cylindrical resin used as an inexpensive piping member, a vortex pump and a dissolution tank are connected to a gas-liquid separation tank mainly composed of the main body cylindrical container. An inexpensive gas-liquid mixing and dissolving apparatus can be provided.

本発明に係る気液分離タンクの一実施の形態を示す断面図である。It is sectional drawing which shows one Embodiment of the gas-liquid separation tank which concerns on this invention. 同上分離タンクのバッファプレートを示す平面図である。It is a top view which shows the buffer plate of a separation tank same as the above. 同上分離タンクを有する気液混合溶解装置の一実施の形態を示す斜視図である。It is a perspective view which shows one Embodiment of the gas-liquid mixing dissolution apparatus which has a separation tank same as the above. 従来の気液混合溶解装置を示す配管図である。It is a piping diagram which shows the conventional gas-liquid mixing dissolution apparatus.

以下、本発明を、図1乃至図3に示された一実施の形態に基いて詳細に説明する。   Hereinafter, the present invention will be described in detail based on the embodiment shown in FIGS.

図3は、気液混合溶解装置11を示し、この気液混合溶解装置11は、液中に気体を混合する渦流ポンプ12と、液中に気体を溶解させる溶解タンク13とが、配管14により接続され、上記溶解タンク13と、液中に溶解されなかった気体を分離する気液分離タンク15とが、配管16により接続されている。   FIG. 3 shows a gas-liquid mixing / dissolving device 11. The gas-liquid mixing / dissolving device 11 includes a vortex pump 12 that mixes gas in the liquid and a dissolution tank 13 that dissolves gas in the liquid. The dissolution tank 13 connected and the gas-liquid separation tank 15 for separating the gas not dissolved in the liquid are connected by a pipe 16.

上記渦流ポンプ12は、ベースフレーム17上に設置され、上記溶解タンク13および上記気液分離タンク15は、ベースフレーム17上の基台18上に設置されている。   The vortex pump 12 is installed on the base frame 17, and the dissolution tank 13 and the gas-liquid separation tank 15 are installed on a base 18 on the base frame 17.

上記渦流ポンプ12は、液吸込圧力を調整するための液吸込圧力調整弁19および圧力計20を経てポンプ吸込口部12aに液を吸い込むとともに、このポンプ吸込口部12aに外部から挿入された吸気管(図に現われず)を経て空気などの気体を吸い込み、ポンプ本体12b内の環状通路を多数の回転翼間で渦流となりながらほぼ1周移送する段階で気液混合を促進し、ポンプ本体12bの上部に設けられたポンプ吐出口部12cより気液混合流体を吐出する。   The vortex pump 12 sucks liquid into the pump suction port portion 12a through the liquid suction pressure adjusting valve 19 and the pressure gauge 20 for adjusting the liquid suction pressure, and intake air inserted into the pump suction port portion 12a from the outside. Gas, such as air, is sucked in through a pipe (not shown in the figure), and gas-liquid mixing is promoted in a stage where the annular passage in the pump main body 12b is transported almost once in a vortex between many rotor blades. The gas-liquid mixed fluid is discharged from a pump discharge port portion 12c provided on the upper side of the nozzle.

上記溶解タンク13は、渦流ポンプ12から吐出された気液混合流体をタンク上部に加圧供給され、タンク下部の取出口から取り出すまでの過程で液中への気体の溶解を促進させるものであり、そのタンク本体は、上下水道などで用いられる硬質の塩化ビニル管などの合成樹脂管21の上下開口端縁部に、同様の合成樹脂製のフランジ22,23をそれぞれ接着して形成する。   The dissolution tank 13 is a gas-liquid mixed fluid discharged from the vortex pump 12 is pressurized and supplied to the upper part of the tank, and promotes dissolution of gas into the liquid in the process from taking out from the outlet at the lower part of the tank. The tank body is formed by bonding similar synthetic resin flanges 22 and 23 to upper and lower opening end edges of a synthetic resin pipe 21 such as a hard vinyl chloride pipe used in water and sewage.

図1に示されるように、上記気液分離タンク15は、開口部が上下方向に設置された円筒形樹脂製の本体円筒容器31と、上記本体円筒容器31の上側の開口部に連続的に取り付けられ、気液混合流体を接線方向から上記本体円筒容器31内に導入する気液混合流体入口32を側面に有するとともに、液中から分離された気体を排出する気体出口33を上端面に有する上側円筒部34と、上記本体円筒容器31の下側の開口部に設けられた液取出口35を有する底板部36と、上記底板部36の液取出口35上に通液間隙37を介して設けられたバッファプレート38とを具備した構造である。底板部36にはドレン口39が設けられ、このドレン口39には、通常は図示しない弁により閉じられた配管が接続されている。   As shown in FIG. 1, the gas-liquid separation tank 15 is continuously formed in a cylindrical body 31 made of a cylindrical resin whose opening is installed in the vertical direction and an opening on the upper side of the cylindrical body 31. A gas-liquid mixed fluid inlet 32 for introducing the gas-liquid mixed fluid into the main body cylindrical container 31 from the tangential direction is provided on the side surface, and a gas outlet 33 for discharging the gas separated from the liquid is provided on the upper end surface. An upper cylindrical portion 34, a bottom plate portion 36 having a liquid outlet 35 provided in an opening on the lower side of the main body cylindrical container 31, and a liquid passing gap 37 on the liquid outlet 35 of the bottom plate portion 36. And a buffer plate 38 provided. A drain port 39 is provided in the bottom plate portion 36, and a pipe normally closed by a valve (not shown) is connected to the drain port 39.

上記本体円筒容器31は、上下水道などで用いられる塩化ビニル管などの合成樹脂管31aの上下開口部に、同様の合成樹脂製のフランジ31b,31cをそれぞれ接着して形成する。   The main body cylindrical container 31 is formed by bonding similar synthetic resin flanges 31b and 31c to upper and lower openings of a synthetic resin pipe 31a such as a vinyl chloride pipe used in water and sewage.

一方、上記上側円筒部34は、気液混合流体入口32および気体出口33を設け、これらに配管16などを溶接したり、ねじ穴を形成するため、金属筒34aに金属蓋部材34bおよび金属フランジ部材34cを溶接したものであり、同様に、上記底板部36も金属板部材にネジ穴の液取出口35を形成する。   On the other hand, the upper cylindrical portion 34 is provided with a gas-liquid mixed fluid inlet 32 and a gas outlet 33, and welds a pipe 16 or the like to them or forms a screw hole, so that a metal lid member 34b and a metal flange are formed on the metal cylinder 34a. Similarly, the member 34c is welded, and similarly, the bottom plate portion 36 also forms a liquid outlet 35 having a screw hole in the metal plate member.

この上側円筒部34内には、気液混合流体入口32の上側部から気体出口33にわたって漸次径小に設けられた円錐形状の抜気案内板41が設置されている。上記気体出口33には、抜気量を調整する抜気弁42が設けられている。   In the upper cylindrical portion 34, a conical evacuation guide plate 41 having a gradually decreasing diameter is installed from the upper portion of the gas-liquid mixed fluid inlet 32 to the gas outlet 33. The gas outlet 33 is provided with an exhaust valve 42 for adjusting the amount of exhaust.

図2に示されるように、上記液取出口35は、上記底板部36の中央部に穿設され、上記バッファプレート38は、上記底板部36と平行にかつ上記液取出口35と同心状に配置された上記液取出口35よりも大きな平板であり、上記底板部36と上記バッファプレート38との間の上記通液間隙37は、上記本体円筒容器31内の4方に向かって開口されている。   As shown in FIG. 2, the liquid outlet 35 is formed in the center of the bottom plate portion 36, and the buffer plate 38 is parallel to the bottom plate portion 36 and concentrically with the liquid outlet 35. It is a flat plate larger than the liquid outlet 35 disposed, and the liquid passage gap 37 between the bottom plate portion 36 and the buffer plate 38 is opened toward the four directions in the main body cylindrical container 31. Yes.

すなわち、上記バッファプレート38は、4方に配置された支持板45,46,47,48により上記底板部36に対して平行となるように、かつ上記液取出口35に対して同心となるように取り付けられている。2つの支持板45,47は、底板部36にネジ止め固定されている。   That is, the buffer plate 38 is parallel to the bottom plate portion 36 by the support plates 45, 46, 47, 48 arranged in four directions, and is concentric with the liquid outlet 35. Is attached. The two support plates 45 and 47 are fixed to the bottom plate portion 36 with screws.

バッファプレート38の下側に設けられた液取出口35には、図3に示されるように配管49が接続され、この配管49は、マイクロバブルなどの微細気泡を必要とする例えば浴槽などに連通されている。   As shown in FIG. 3, a pipe 49 is connected to the liquid outlet 35 provided on the lower side of the buffer plate 38, and this pipe 49 communicates with, for example, a bathtub that requires fine bubbles such as microbubbles. Has been.

次に、上記実施の形態の作用効果を説明する。   Next, the function and effect of the above embodiment will be described.

渦流ポンプ12により液とともに空気などの気体を吸い込み、この渦流ポンプ12内で移送しながら気液を混合攪拌し、渦流ポンプ12から吐出された気液混合流体を溶解タンク13の上部に供給し、この溶解タンク13内で気液混合流体が下降しつつ、液中への気体の溶解を進行させ、この溶解タンク13の下部から配管16により気液混合流体Aを気液分離タンク15に供給して、液中に溶解されずに気泡として混在する気体を分離し、抜気弁42から気体Bを外部へ排出するとともに、高濃度に気体が溶解された液Cを、液取出口35より配管49に取り出し、例えば浴槽などに供給することで、浴槽内などにマイクロバブルなどの微細気泡を発生させる。   A gas such as air is sucked together with the liquid by the vortex pump 12, the gas and liquid are mixed and stirred while being transferred in the vortex pump 12, and the gas-liquid mixed fluid discharged from the vortex pump 12 is supplied to the upper part of the dissolution tank 13. While the gas-liquid mixed fluid descends in the dissolution tank 13, the gas is dissolved into the liquid, and the gas-liquid mixed fluid A is supplied to the gas-liquid separation tank 15 from the lower part of the dissolution tank 13 through the pipe 16. The gas mixed as bubbles without being dissolved in the liquid is separated, and the gas B is discharged from the vent valve 42 to the outside, and the liquid C in which the gas is dissolved at a high concentration is piped from the liquid outlet 35. For example, microbubbles such as microbubbles are generated in the bathtub or the like by taking it out to 49 and supplying it to the bathtub or the like.

上記気液分離タンク15は、気液混合流体入口32を上側円筒部34の接線方向に設けることによって、上側円筒部34およびその下側に位置する本体円筒容器31内で気液混合流体を旋回させ、中心軸部に気泡を集める。   The gas-liquid separation tank 15 swirls the gas-liquid mixed fluid in the upper cylindrical portion 34 and the main body cylindrical container 31 positioned below the upper cylindrical portion 34 by providing the gas-liquid mixed fluid inlet 32 in the tangential direction of the upper cylindrical portion 34. And collect air bubbles in the central shaft.

このとき、液と気体を分離させるために本体円筒容器31の下部形状を円錐形にしたり本体円筒容器31内への流入速度を速くして、きれいな気泡柱をつくることは防止しなければならない。すなわち、このようなことをして気泡を強力に中心軸部に集める状態では、本体円筒容器31の中心軸部と内壁面部との差圧が大きくなり、上部の気体出口33から気体を排出しにくくなり、中心軸部に溜まった気泡がそのまま液とともに液取出口35から排出されやすくなるとともに、液中に溶解した気体が本体円筒容器31の中心軸部で必要以上に液中から分離しやすくなるおそれがある。   At this time, in order to separate the liquid and the gas, it is necessary to prevent the lower cylindrical shape of the main body cylindrical container 31 from being a conical shape or increasing the flow rate into the main body cylindrical container 31 to form a clean bubble column. That is, in such a state that air bubbles are strongly collected in the central shaft portion, the differential pressure between the central shaft portion and the inner wall surface portion of the main body cylindrical container 31 becomes large, and the gas is discharged from the upper gas outlet 33. Air bubbles accumulated in the central shaft part are easily discharged from the liquid outlet 35 together with the liquid, and the gas dissolved in the liquid is easily separated from the liquid more than necessary at the central shaft part of the main body cylindrical container 31. There is a risk.

このようなおそれをなくすために、本体円筒容器31の液取出口35にバッファプレート38を取付けることによって、円滑な旋回流を乱して気泡柱を中心軸部から周囲に拡散させ、きれいな気泡柱が中心軸部にできない構造にし、本体円筒容器31の中心軸部に溜まった気体がそのまま液取出口35から出ないようにするとともに、タンク中心軸部とタンク内壁面部との差圧が大きくならないようにして、液中に溶解している気体が目に見える大きさの気泡に成長して液から分離する気泡化を防止している。   In order to eliminate such a risk, by attaching a buffer plate 38 to the liquid outlet 35 of the main body cylindrical container 31, a smooth swirling flow is disturbed to diffuse the bubble column from the central shaft portion to the surroundings, and a clean bubble column The structure prevents the central axis of the main body cylindrical container 31 from leaving the gas collected from the liquid outlet 35 and does not increase the differential pressure between the tank central axis and the tank inner wall. In this way, the gas dissolved in the liquid grows into bubbles having a visible size and prevents bubbles from separating from the liquid.

そして、開口部が上下方向に設置された本体円筒容器31を、気液混合流体入口32および気体出口33を有する上側円筒部34や、液取出口35およびバッファプレート38を有する底板部36とは別個に設けたので、本体円筒容器31に気液混合流体入口32、気体出口33および液取出口35の穴加工をしたり配管やバッファプレート38を溶接する必要性をなくして、主要な本体円筒容器31を安価な配管部材などとして用いられる円筒形樹脂製とすることができるので、製造にかかる手間やコストを抑えることができる気液分離タンク15を提供できる。   And the main body cylindrical container 31 with the opening portion installed in the vertical direction is an upper cylindrical portion 34 having a gas-liquid mixed fluid inlet 32 and a gas outlet 33, and a bottom plate portion 36 having a liquid outlet 35 and a buffer plate 38. Since it is provided separately, it eliminates the need for drilling the gas-liquid mixed fluid inlet 32, gas outlet 33 and liquid outlet 35 in the main body cylindrical container 31, and welding pipes and buffer plates 38. Since the container 31 can be made of a cylindrical resin used as an inexpensive piping member or the like, it is possible to provide the gas-liquid separation tank 15 that can reduce labor and cost for manufacturing.

また、気液混合流体入口32を接線方向に設けることによって、本体円筒容器31内で液と気体を旋回させ、液中に溶解しなかった気体を本体円筒容器31内の中心軸部に気泡として集め、気体出口33から外部へ排出するが、一方では、液取出口35上に通液間隙37を介してバッファプレート38を設けることによって、本体円筒容器31の中心軸部に形成されようとする気泡柱をバッファプレート38により中心軸部の周囲に拡散させて、きれいな気泡柱が本体円筒容器31の中心軸部に形成されることを防止することで、本体円筒容器31の中心軸部に集まった気泡がそのまま液とともに液取出口35から流出することを防止でき、また、本体円筒容器31の中心軸部と内壁面との差圧が大きくならないように旋回渦流を乱して、本体円筒容器31の中心軸部で強い負圧が立つことを防止することで、上部の気体出口33から気体を効率よく排出できるとともに、液中に溶解している気体までも目に見える気泡に成長して液から分離する気泡化を防止できる。   Further, by providing the gas-liquid mixed fluid inlet 32 in the tangential direction, the liquid and the gas are swirled in the main body cylindrical container 31, and the gas that has not been dissolved in the liquid is formed as a bubble in the central shaft portion in the main body cylindrical container 31. Collected and discharged from the gas outlet 33 to the outside. On the other hand, by providing the buffer plate 38 on the liquid outlet 35 via the liquid passage gap 37, it is about to be formed in the central shaft portion of the main body cylindrical container 31. The bubble column is diffused around the central axis portion by the buffer plate 38 to prevent the formation of a clean bubble column at the central axis portion of the main body cylindrical container 31, thereby gathering at the central axis portion of the main body cylindrical container 31. The air bubbles can be prevented from flowing out from the liquid outlet 35 together with the liquid, and the swirl vortex can be disturbed so that the differential pressure between the central shaft portion and the inner wall surface of the main body cylindrical container 31 does not increase. Strong negative pressure is generated at the center shaft of 31 By preventing this, the gas can be efficiently discharged from the upper gas outlet 33, and even the gas dissolved in the liquid can be prevented from growing into a visible bubble and separated from the liquid.

すなわち、バッファプレート38は、本体円筒容器31の底板部36と平行にかつ底板部36の中央部に穿設された液取出口35と同心状に配置された液取出口35よりも大きな平板であり、底板部36とバッファプレート38との間の通液間隙37は、本体円筒容器31内の4方に向かって開口されたので、接線方向から本体円筒容器31内に流入して本体円筒容器31内で旋回しながら底板部36の中央部から流出しようとしていた本体円筒容器中心軸部回りの高速の渦が、バッファプレート38によってバランスを崩され、上記中心軸部の周囲に分散して複数の小さな渦dとなり、その分、上記中心軸部回りの渦は緩やかに旋回し、複数の小さな渦dが本体円筒容器31内を大きな渦Dとともに緩やかに旋回する。   That is, the buffer plate 38 is a flat plate larger than the liquid outlet 35 disposed in a concentric manner with the liquid outlet 35 provided in the center of the bottom plate 36 in parallel with the bottom plate 36 of the main body cylindrical container 31. And the liquid passage gap 37 between the bottom plate portion 36 and the buffer plate 38 is opened toward the four directions inside the main body cylindrical container 31, so that it flows into the main body cylindrical container 31 from the tangential direction and flows into the main body cylindrical container. The high-speed vortex around the central axis portion of the main body cylindrical container that was about to flow out from the center portion of the bottom plate portion 36 while swirling in 31 is unbalanced by the buffer plate 38 and dispersed around the central axis portion. Accordingly, the vortex around the central axis portion is gently swirled, and a plurality of small vortices d are gently swirled along with the large vortex D in the main body cylindrical container 31.

このような現象がもたらす効果は、上記中心軸部回りの高速の渦による強力な遠心力が減少し、本体円筒容器31の中心軸部に発生する強い負圧部がなくなることで、液中に溶解している気体の負圧部への分離(微細な気泡の成長を含む)を抑えつつ、液中に比較的大きな気泡状態で混在する気体の塊だけを集めることができ、かつ微細な気泡はバッファプレート38により反射する上昇流に載せて本体円筒容器31内で旋回させることによって本体円筒容器31内に長時間滞留させ、微細な気泡の液中への溶解を促進させることができる。   The effect brought about by such a phenomenon is that the strong centrifugal force due to the high-speed vortex around the central shaft portion is reduced and the strong negative pressure portion generated in the central shaft portion of the main body cylindrical container 31 is eliminated, so that While suppressing the separation of dissolved gas into the negative pressure part (including the growth of fine bubbles), it is possible to collect only gas masses mixed in a relatively large bubble state in the liquid, and fine bubbles Can be retained in the main body cylindrical container 31 for a long time by being swung in the main body cylindrical container 31 on the upward flow reflected by the buffer plate 38, thereby promoting the dissolution of fine bubbles in the liquid.

さらに、上側円筒部34内に設置された円錐形状の抜気案内板41により、本体円筒容器31内の液から分離されて旋回する気体を気体出口33へと円滑に案内し排出することができる。   Further, the conical air guide plate 41 installed in the upper cylindrical portion 34 can smoothly guide and discharge the swirling gas separated from the liquid in the main body cylindrical container 31 to the gas outlet 33. .

また、気液分離タンク15の本体円筒容器31を、気液混合流体入口32、気体出口33および液取出口35の穴加工をしたり配管やバッファプレート38を溶接する必要性をなくして、主要な本体円筒容器31を安価な配管部材などとして用いられる円筒形樹脂製とすることができるので、その本体円筒容器31を主材とする気液分離タンク15に対し渦流ポンプ12および溶解タンク13を接続して、安価な気液混合溶解装置を提供できる。   In addition, the main body cylindrical container 31 of the gas-liquid separation tank 15 is made free of the need to drill holes in the gas-liquid mixed fluid inlet 32, gas outlet 33 and liquid outlet 35, or weld pipes and buffer plates 38. Since the main body cylindrical container 31 can be made of a cylindrical resin used as an inexpensive piping member or the like, the vortex pump 12 and the dissolution tank 13 are provided for the gas-liquid separation tank 15 whose main material is the main body cylindrical container 31. By connecting, an inexpensive gas-liquid mixing and dissolving apparatus can be provided.

本発明は、気液分離タンクおよび気液混合溶解装置の製造業、販売業、施工業などに携わる者にとって利用可能性がある。   INDUSTRIAL APPLICABILITY The present invention can be used by those who are involved in the manufacturing industry, the sales industry, the industrial industry, etc. of the gas-liquid separation tank and the gas-liquid mixing and dissolving apparatus.

A 気液混合流体
B 気体
C 液
11 気液混合溶解装置
12 渦流ポンプ
13 溶解タンク
14 配管
15 気液分離タンク
16 配管
31 本体円筒容器
32 気液混合流体入口
33 気体出口
34 上側円筒部
35 液取出口
36 底板部
37 通液間隙
38 バッファプレート
41 抜気案内板
A Gas-liquid mixed fluid B Gas C liquid
11 Gas-liquid mixing and dissolving equipment
12 Eddy current pump
13 Dissolution tank
14 Piping
15 Gas-liquid separation tank
16 Piping
31 Main body cylindrical container
32 Gas-liquid mixed fluid inlet
33 Gas outlet
34 Upper cylindrical part
35 Liquid outlet
36 Bottom plate
37 Fluid gap
38 Buffer plate
41 Bleeding guide plate

Claims (4)

開口部が上下方向に設置された円筒形樹脂製の本体円筒容器と、
上記本体円筒容器の上側の開口部に連続的に取り付けられ、気液混合流体を接線方向から上記本体円筒容器内に導入する気液混合流体入口を側面に有するとともに、液中から分離された気体を排出する気体出口を上端面に有する上側円筒部と、
上記本体円筒容器の下側の開口部に設けられた液取出口を有する底板部と、
上記底板部の液取出口上に通液間隙を介して設けられたバッファプレートと
を具備したことを特徴とする気液分離タンク。
A cylindrical body made of a cylindrical resin with an opening installed in the vertical direction;
A gas that is continuously attached to the upper opening of the main body cylindrical container, has a gas-liquid mixed fluid inlet for introducing the gas-liquid mixed fluid into the main body cylindrical container from the tangential direction, and is separated from the liquid. An upper cylindrical portion having a gas outlet at the upper end surface for discharging
A bottom plate having a liquid outlet provided in the lower opening of the main body cylindrical container;
A gas-liquid separation tank comprising: a buffer plate provided on a liquid outlet of the bottom plate portion via a liquid passage gap.
液取出口は、底板部の中央部に穿設され、
バッファプレートは、上記底板部と平行にかつ上記液取出口と同心状に配置された上記液取出口よりも大きな平板であり、
上記底板部と上記バッファプレートとの間の通液間隙は、本体円筒容器内の4方に向かって開口された
ことを特徴とする請求項1記載の気液分離タンク。
The liquid outlet is drilled in the center of the bottom plate,
The buffer plate is a flat plate larger than the liquid outlet arranged in parallel with the bottom plate and concentrically with the liquid outlet.
The gas-liquid separation tank according to claim 1, wherein the liquid passage gap between the bottom plate portion and the buffer plate is opened toward four directions in the main body cylindrical container.
上側円筒部内に気液混合流体入口の上側部から気体出口にわたって漸次径小に設けられた円錐形状の抜気案内板
を具備したことを特徴とする請求項1または2記載の気液分離タンク。
The gas-liquid separation tank according to claim 1 or 2, further comprising a conical vent guide plate provided in the upper cylindrical portion so as to gradually decrease in diameter from the upper portion of the gas-liquid mixed fluid inlet to the gas outlet.
液中に気体を混合する渦流ポンプと、
上記渦流ポンプに配管により接続され、液中に気体を溶解させる溶解タンクと、
上記溶解タンクに配管により接続され、液中に溶解されなかった気体を分離する請求項1乃至3のいずれか記載の気液分離タンクと
を具備したことを特徴とする気液混合溶解装置。
A vortex pump that mixes gas in the liquid;
A dissolution tank connected to the vortex pump by a pipe and dissolving a gas in the liquid;
A gas-liquid mixing and dissolving apparatus comprising the gas-liquid separation tank according to any one of claims 1 to 3, wherein the gas-liquid separation tank is connected to the dissolution tank by a pipe and separates a gas that has not been dissolved in the liquid.
JP2011181809A 2011-08-23 2011-08-23 Gas-liquid separation tank and gas-liquid mixing and dissolving device Active JP5570074B2 (en)

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CN108097191A (en) * 2017-12-28 2018-06-01 天津广顺化学科技有限公司 A kind of safety-type stirred autoclave
JP2018199116A (en) * 2017-05-30 2018-12-20 マイクロゼロ株式会社 Air separator and gas-liquid separator
WO2022158540A1 (en) * 2021-01-22 2022-07-28 学校法人工学院大学 Gas/liquid mixing device
KR20230001244A (en) * 2021-06-28 2023-01-04 농업회사법인 푸디웜 주식회사 A appratus for screening and collecting of larva

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2018199116A (en) * 2017-05-30 2018-12-20 マイクロゼロ株式会社 Air separator and gas-liquid separator
CN108097191A (en) * 2017-12-28 2018-06-01 天津广顺化学科技有限公司 A kind of safety-type stirred autoclave
WO2022158540A1 (en) * 2021-01-22 2022-07-28 学校法人工学院大学 Gas/liquid mixing device
KR20230001244A (en) * 2021-06-28 2023-01-04 농업회사법인 푸디웜 주식회사 A appratus for screening and collecting of larva
KR102528540B1 (en) 2021-06-28 2023-05-08 농업회사법인 푸디웜 주식회사 A appratus for screening and collecting of larva

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