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JP2005000880A - Gas dissolution and separation apparatus - Google Patents

Gas dissolution and separation apparatus Download PDF

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Publication number
JP2005000880A
JP2005000880A JP2003169944A JP2003169944A JP2005000880A JP 2005000880 A JP2005000880 A JP 2005000880A JP 2003169944 A JP2003169944 A JP 2003169944A JP 2003169944 A JP2003169944 A JP 2003169944A JP 2005000880 A JP2005000880 A JP 2005000880A
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Japan
Prior art keywords
gas
liquid
chamber
concentration solution
dissolution
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JP2003169944A
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Japanese (ja)
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JP3814262B2 (en
Inventor
Soichiro Osaki
荘一郎 大崎
Tatsuo Mori
龍生 森
Masashi Hamada
昌史 濱田
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Nikuni KK
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Nikuni KK
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a gas dissolution and separation apparatus which does not require a pressure-resistant structure as a pressure container, can efficiently separate an excess gas undissolved in a liquid, and is small-sized and low in cost. <P>SOLUTION: In the upper part of a tank body 42, a gas/liquid mixture injection pipe 43 for injecting downward a gas/liquid mixture A prepared by mixing a gas with a liquid is installed. In the tank body 42, a reflection plate 45 facing the injection port 44 of the gas/liquid mixture injection pipe 43 is installed so as to partition a gas dissolution chamber 46 above the reflection plate 45. A turbulent flow caused by reflecting the jet stream of the gas/liquid mixture A by the reflection plate 45 is made to stir the gas and the liquid to dissolve the gas in the liquid, thus producing a high-concentration solution C. At the upper end of the tank body 42, positioned at the upper side of the gas dissolution chamber 46, a gas-extraction-amount adjustment valve 47 for discharging the excess gas B is installed. Below the reflection plate 45, a high-concentration solution chamber 49 is partitioned and a liquid take-out part 50 is also installed. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

【0001】
【発明の属する技術分野】
本発明は、気体を液体中に溶解させて高濃度溶解液を分離生成する気体溶解分離装置に関するものである。
【0002】
【従来の技術】
従来の気体溶解分離装置は、複数のタンクを直列に接続し、前段のタンク内で、気液混合体を攪拌して、液体中への気体の溶解量を増大させるようにし、後段のタンク内で、液中に溶解しなかった余剰気体を高濃度溶解液から分離し、高濃度溶解液のみを取出すようにしている(例えば、特許文献1参照)。
【0003】
【特許文献1】
特開2001−129377号公報(第6−8頁、図1)
【0004】
【発明が解決しようとする課題】
このように、従来の気体溶解分離装置は、液体中へ気体を溶解させるための前段のタンクと、液体中に溶解しなかった余剰気体を高濃度溶解液から分離するための後段のタンクとをそれぞれ設け、前段のタンクの下部から吐出された液を後段のタンクの上部に順次供給するので、タンクを圧力容器として耐圧構造にしなければならないとともに、その認定を受ける必要があり、装置が大型化するとともに、安価に提供することが困難である。
【0005】
本発明は、このような点に鑑みなされたもので、圧力容器としての耐圧構造を要求されないとともに、液体中に溶解されなかった余剰気体を効率良く分離できる小型で安価な気体溶解分離装置を提供することを目的とするものである。
【0006】
【課題を解決するための手段】
請求項1に記載された発明は、タンク本体と、このタンク本体の上部内に気体と液体とが混合された気液混合体を下向きに噴入する気液混合体噴入管と、この気液混合体噴入管の噴入口に対向して上記タンク本体内に設けられた反射板と、この反射板の上側に仕切形成され反射板により気液混合体の噴入流を反射して発生した乱流により気体と液体とを攪拌することで気体を液体中に溶解させて高濃度溶解液を作る気体溶解室と、この気体溶解室の上側に位置する上記タンク本体の上端に設けられ液体中に溶解されなかった余剰気体を外部へ排出する余剰気体排出手段と、上記反射板の下側に上記気体溶解室と連通可能に仕切形成され上記気体溶解室から上記反射板を経て下側へ透過させた高濃度溶解液を収容する高濃度溶解液室と、この高濃度溶解液室から高濃度溶解液を外部へ取出す液取出口部とを具備した気体溶解分離装置であり、タンク本体の上部内に気液混合体を下向きに噴入する気液混合体噴入管の噴入口と対向する反射板の上側に気体溶解室を仕切形成し、この気体溶解室のさらに上側に位置するタンク本体の上端に余剰気体排出手段を設け、気体溶解室内の液体中に溶解されなかった余剰気体をこの余剰気体排出手段により外部へ排出するので、タンク本体に圧力容器としての耐圧構造が要求されないとともに、気体溶解室内の余剰気体を効率良く分離できるので、溶解用のタンクのほかに分離用のタンクを設置する必要がなく、小型で安価な気体溶解分離装置を提供できる。また、1つのタンク本体内に反射板により上側の気体溶解室と下側の高濃度溶解液室とをコンパクトに分離形成でき、気体溶解室にて、気液混合体噴入管から噴入された気液混合体の噴入流を反射板により反射させることで発生した乱流により気体と液体とを攪拌することで、気体を液体中に効率良く溶解させて高濃度溶解液を作ることができるとともに、この高濃度溶解液のみを高濃度溶解液室から液取出口部を経て取出すことができる。
【0007】
請求項2に記載された発明は、請求項1記載の気体溶解分離装置において、余剰気体排出手段は、余剰気体の抜気量を調整できる抜気量調整弁を備え、この抜気量調整弁は、最も閉じ操作された状態でも開弁状態を保つ通気穴を有するものであり、抜気量調整弁の開度を調整することで、余剰気体の浮上速度を調整できるので、この浮上速度が、高濃度溶解液の高濃度溶解液室への下降速度より大きくなるように、抜気量調整弁の開度を調整することにより、余剰気体が反射板を透過して高濃度溶解液室へ入り込むことを防止できる。また、抜気量調整弁を最も閉じ操作しても、通気穴により開弁状態が保たれるので、抜気量調整弁を誤操作により閉じても、余剰気体を外部へ排出する機能を維持できる。
【0008】
請求項3に記載された発明は、請求項1または2記載の気体溶解分離装置における反射板が、上面が凹状に彎曲形成された円板の中央部に形成され気液混合体の噴入流を反射する凹状反射面部と、上記円板の周縁部に沿って設けられ気体溶解室の高濃度溶解液を高濃度溶解液室に透過させる液透過部とを具備したものであり、気液混合体噴入管から噴入された気液混合体の噴入流を反射板の円板の中央部の凹状反射面部に衝突させることで、気体溶解室内に激しい攪拌作用を伴なう乱流を発生させるので、この気体溶解室内で高濃度溶解液を効率良く生成できるとともに、この気体溶解室で生成された高濃度溶解液のみを、反射板の円板の周縁部に沿って設けられた液透過部を経て下側の高濃度溶解液室に透過させ、液取出口部から外部へ取出すことができる。
【0009】
請求項4に記載された発明は、請求項1乃至3のいずれか記載の気体溶解分離装置において、タンク本体の上端に設けられ設定圧力で余剰気体および液体の少なくとも一方を外部へ排出する安全弁を具備したものであり、タンク本体内からの流出量に対しタンク本体内への流入量が増大してタンク本体内の圧力が上昇しようとする場合でも、安全弁により自動的に余剰気体または液体を外部へ排出することで、タンク本体内の異常な圧力上昇を防止でき、タンク本体が圧力容器となることを確実に回避できるとともに、余剰気体を確実に抜気できる。
【0010】
【発明の実施の形態】
以下、本発明を、図1乃至図5に示された一実施の形態、図6および図7に示された他の実施の形態を参照しながら詳細に説明する。
【0011】
先ず、図1乃至図5に示された一実施の形態を説明すると、図4に示されるように、気液混合手段としての渦流ポンプ11における液体吸込口12に、吸込側圧力計13および吸込圧力調整弁14を経て液体を供給する管路15が接続されるとともに、空気などの気体を吸込むための気体吸込手段16も、この渦流ポンプ11における液体吸込口12に接続されている。
【0012】
気体吸込手段16は、渦流ポンプ11の液体吸込口12に挿入された吸込ノズル16aに、気体吸引管16bが接続され連通されている。この気体吸引管16bは、例えば気体として空気を吸引する場合は、垂直に設けられた上端開放の管である。
【0013】
さらに、渦流ポンプ11にて液体中に気体が混合された気液混合体を吐出する気液吐出口17より管路18が引出され、この管路18は、気体溶解分離装置19に接続されている。
【0014】
図5に示されるように、渦流ポンプ11は、ポンプ本体32内に環状の昇圧通路33が形成され、この昇圧通路33の入口部34に液体吸込口12が連通形成されているとともに、昇圧通路33の出口部35に気液吐出口17が連通形成され、昇圧通路33の入口部34と出口部35との間には隔離部36が形成されている。
【0015】
ポンプ本体32内に羽根車37が回転可能に嵌合されており、この羽根車37の外周部には、所定ピッチで形成された径方向の小羽根38と、これらの小羽根38間の羽根溝39が設けられており、羽根車37の中心に嵌着された回転軸40を外部のモータなどで回動することにより、これらの小羽根38および羽根溝39は、羽根車37と同心円の昇圧通路33内を回転する。
【0016】
渦流ポンプ11の液体吸込口12を形成する部分には、吸込ノズル16aが螺入されて固定されており、この吸込ノズル16aの先端部分は昇圧通路33の入口部34まで挿入され、この吸込ノズル16aから昇圧通路33の入口部34に気体が吸込まれる。
【0017】
図1に示されるように、この気体溶解分離装置19は、脚部41によって立形に設置された縦長状のタンク本体42を中心に設けられている。
【0018】
このタンク本体42の上部内には、上記管路18に接続される気液混合体噴入管43が側方から挿入して固定され、この気液混合体噴入管43の先端には、気体と液体とが混合された気液混合体Aをタンク本体42の上部内に下向きに噴入する噴入口44が開口されている。
【0019】
この気液混合体噴入管43の噴入口44に対向して、上記タンク本体42内に、上面凹状に彎曲形成された反射板45が設けられ、この反射板45の上側に気体溶解室46が仕切形成されている。
【0020】
この気体溶解室46は、反射板45により気液混合体Aの噴入流を反射して発生した乱流により気体と液体とを攪拌することで気体を液体中に溶解させて高濃度溶解液を作る室である。
【0021】
この気体溶解室46の上側に位置するタンク本体42の上端には、液体中に溶解されなかった微細な気泡状の余剰気体Bを外部へ排出する余剰気体排出手段としての抜気量調整弁47および安全弁48が、それぞれ設けられている。
【0022】
抜気量調整弁47は、手動調整された所定の弁開度で、外部へ排出される余剰気体Bの抜気量を調整できるとともに、抜気に伴なう微量の液を外部へ排出する弁であり、一方、安全弁48は、タンク本体42の上部内の圧力が設定圧力を超えたときに自動的に開弁動作して、余剰気体Bおよび液体の少なくとも一方を外部へ排出する弁である。
【0023】
上記反射板45の下側には、上記気体溶解室46と連通可能な高濃度溶解液室49が仕切形成され、この高濃度溶解液室49に、上記気体溶解室46から上記反射板45を経て下側へ透過させた高濃度溶解液Cが収容される。タンク本体42の下部の側面には、この高濃度溶解液室49から高濃度溶解液Cを外部へ取出す液取出口部50が突設されている。
【0024】
図2に示されるように、抜気量調整弁47は、弁本体51の内部にハンドル52の回動により開閉操作される可動弁体53が設けられ、この可動弁体53には、図示されるように最も閉じ操作された状態でも開弁状態を保つ通気穴54が穿設されている。
【0025】
図3に示されるように、上記反射板45は、上面が凹状に彎曲形成された円板55の中央部に、気液混合体Aの噴入流を反射する凹状反射面部56が形成され、また、上記円板55の周縁部に沿って、気体溶解室46から高濃度溶解液室49に高濃度溶解液Cを透過させる多数の透孔状の液透過部57が設けられている。
【0026】
次に、図示された渦流ポンプ11および気体溶解分離装置19の作用を説明する。
【0027】
管路15より液体を渦流ポンプ11の液体吸込口12に吸引する。渦流ポンプ11の液体吸込口12に吸込まれた液体は、羽根車37と共に昇圧通路33をほぼ一周し、その間、液体は、羽根車37の各羽根溝39内と昇圧通路33との間で渦流となり、これが各羽根溝39で同時に行なわれながら昇圧通路33内を進み、昇圧通路33を進むにつれて昇圧されて、気液吐出口17から吐出される。
【0028】
このとき同時に、吸込側圧力計13を見ながら吸込圧力調整弁14を絞り、渦流ポンプ11の液体吸込口12を負圧にして、気体吸引管16bから吸込ノズル16aを経て空気などの気体を吸引する。
【0029】
よって、液体吸込口12から昇圧通路33内に液体が吸込まれる際に、吸込ノズル16aから昇圧通路33の入口部34に気体も吸込まれ、液体と気体とが一緒に羽根車37と昇圧通路33との間で生じる渦流によって攪拌され、液体中に微細な気泡を混合された気液混合体が作られる。
【0030】
この渦流ポンプ11で昇圧された気液混合体は、気液吐出口17から管路18に吐出され、この管路18を経て気体溶解分離装置19に供給される。
【0031】
この気体溶解分離装置19では、気液混合体噴入管43の噴入口44より気体溶解室46内に気液混合体Aが噴入され、この気体溶解室46内で気液混合体Aが乱流攪拌され、液体中への気体の溶解量を増大させることができる。
【0032】
すなわち、気液混合体噴入管43の噴入口44から気体溶解室46内に噴入された気液混合体Aの噴入流を反射板45の凹状反射面部56により反射させることで発生した乱流により気体と液体とを激しく攪拌することで、気体を液体中に効率良く高濃度に溶解させて高濃度溶解液を作ることができる。
【0033】
このとき、液体中に溶解されなかった余剰気体Bと液体との間には比重差があり、微細な気泡状の余剰気体Bには浮力が作用するので、余剰気体Bは、タンク本体42の上部に向かって浮上し、少なくとも抜気量調整弁47より、また場合によっては安全弁48より外部へ排出される。
【0034】
一方、気体溶解室46内の高濃度溶解液は、より低圧の高濃度溶解液室49に向って移動し、反射板45の周縁部の液透過部57を透過して高濃度溶解液室49に入り、この高濃度溶解液室49内の高濃度溶解液Cは、液取出口部50より外部へ流出する。
【0035】
次に、図1乃至図3に示された実施形態の効果を説明する。
【0036】
タンク本体42の上部内に気液混合体Aを下向きに噴入する気液混合体噴入管43の噴入口44と対向する反射板45の上側に気体溶解室46を仕切形成し、この気体溶解室46のさらに上側に位置するタンク本体42の上端に抜気量調整弁47を設け、気体溶解室46内の液体中に溶解されなかった余剰気体Bをこの抜気量調整弁47により外部へ排出するので、タンク本体42に圧力容器としての耐圧構造が要求されないとともに、気体溶解室46内の余剰気体Bを効率良く分離できるので、溶解用のタンクのほかに分離用のタンクを設置する必要がなく、小型で安価な気体溶解分離装置19を提供できる。
【0037】
また、1つのタンク本体42内に、反射板45により、上側の気体溶解室46と下側の高濃度溶解液室49とをコンパクトに分離形成でき、気体溶解室46では、気液混合体噴入管43から噴入された気液混合体Aの噴入流を反射板45の中央部の凹状反射面部56に衝突させ反射させることで、気体溶解室46内に激しい攪拌作用を伴なう乱流を発生させるので、この乱流中で気体を液体中に効率良く溶解させて高濃度溶解液Cを効率良く生成できるとともに、この気体溶解室46で生成された高濃度溶解液Cのみを、反射板45の周縁部に沿って設けられた液透過部57を経て下側の高濃度溶解液室49に透過させ、この高濃度溶解液室49から液取出口部50を経て外部へ取出すことができる。
【0038】
さらに、抜気量調整弁47の開度を調整することで、余剰気体Bの浮上速度を調整できるので、この浮上速度が、高濃度溶解液Cの高濃度溶解液室49への下降速度より大きくなるように、抜気量調整弁47の開度を調整することにより、余剰気体Bが反射板45の液透過部57に吸込まれて高濃度溶解液室49へ入り込むことを防止できる。
【0039】
このとき、抜気量調整弁47を誤って最も閉じ操作しても、その通気穴54により開弁状態が保たれるので、余剰気体Bを外部へ排出する機能を維持できる。
【0040】
その上、タンク本体42内からの流出量に対しタンク本体42内への流入量が増大してタンク本体42内の圧力が上昇しようとする場合でも、安全弁48により自動的に余剰気体Bまたは液体を外部へ排出することで、タンク本体42内の異常な圧力上昇を防止でき、タンク本体42が圧力容器となることを確実に回避できるとともに、余剰気体Bを確実に抜気できる。
【0041】
次に、図6および図7に示された他の実施の形態を説明する。なお、図1乃至図3に示された実施の形態と同様の部分には同一符号を付して、その説明を省略する。
【0042】
図6に示されるように、タンク本体42の上部内には、図4に示された管路18に接続される気液混合体噴入管43aがタンク上面部から挿入して固定され、この気液混合体噴入管43aの下端には、気体と液体とが混合された気液混合体Aをタンク本体42の上部内に下向きに噴入する噴入口44aが開口されている。
【0043】
また、タンク本体42内の高濃度溶解液室49から高濃度溶解液Cを外部へ取出す液取出口部50aは、タンク本体42の最下部からいったん真下に引出された後、側方へ折曲されている。
【0044】
さらに、気液混合体噴入管43aの噴入口44aに対向して、上記タンク本体42内に、上面凹状に彎曲形成された反射板45aが設けられ、この反射板45aは、図7に示されるように、上面が凹状に彎曲形成された円板55の中央部に、気液混合体Aの噴入流を反射する凹状反射面部56が形成され、また、円板55の外周部に複数の凸部57aが等ピッチで突設され、これらの各凸部57aをタンク本体42の内壁面に当接させることで、各凸部57a,57a間に隙間状の液透過部57bが上記円板55の周縁部に沿って設けられ、これらの液透過部57bを経て気体溶解室46から高濃度溶解液室49に高濃度溶解液Cが透過される。
【0045】
なお、この気体溶解分離装置19は、液体に空気、酸素またはオゾンなどの各種気体を混合溶解させるもので、本装置には、微細気泡発生装置、酸素富化装置またはオゾン溶解装置などが含まれる。
【0046】
【発明の効果】
請求項1記載の発明によれば、タンク本体の上部内に気液混合体を下向きに噴入する気液混合体噴入管の噴入口と対向する反射板の上側に気体溶解室を仕切形成し、この気体溶解室のさらに上側に位置するタンク本体の上端に余剰気体排出手段を設け、気体溶解室内の液体中に溶解されなかった余剰気体をこの余剰気体排出手段により外部へ排出するので、タンク本体に圧力容器としての耐圧構造が要求されないとともに、気体溶解室内の余剰気体を効率良く分離できるので、溶解用のタンクのほかに分離用のタンクを設置する必要がなく、小型で安価な気体溶解分離装置を提供できる。また、1つのタンク本体内に反射板により上側の気体溶解室と下側の高濃度溶解液室とをコンパクトに分離形成でき、気体溶解室にて、気液混合体噴入管から噴入された気液混合体の噴入流を反射板により反射させることで発生した乱流により気体と液体とを攪拌することで、気体を液体中に効率良く溶解させて高濃度溶解液を作ることができるとともに、この高濃度溶解液のみを高濃度溶解液室から液取出口部を経て外部へ取出すことができる。
【0047】
請求項2記載の発明によれば、抜気量調整弁の開度を調整することで、余剰気体の浮上速度を調整できるので、この浮上速度が、高濃度溶解液の高濃度溶解液室への下降速度より大きくなるように、抜気量調整弁の開度を調整することにより、余剰気体が反射板を透過して高濃度溶解液室へ入り込むことを防止できる。また、抜気量調整弁を最も閉じ操作しても、その通気穴により開弁状態が保たれるので、抜気量調整弁を誤って閉じ操作しても、余剰気体を外部へ排出する機能を維持できる。
【0048】
請求項3記載の発明によれば、気液混合体噴入管から噴入された気液混合体の噴入流を反射板の円板の中央部の凹状反射面部に衝突させることで、気体溶解室内に激しい攪拌作用を伴なう乱流を発生させるので、この気体溶解室内で高濃度溶解液を効率良く生成できるとともに、この気体溶解室で生成された高濃度溶解液のみを、反射板の円板の周縁部に沿って設けられた液透過部を経て下側の高濃度溶解液室に透過させ、液取出口部から外部へ取出すことができる。
【0049】
請求項4記載の発明によれば、タンク本体内からの流出量に対しタンク本体内への流入量が増大してタンク本体内の圧力が上昇しようとする場合でも、安全弁により自動的に余剰気体または液体を外部へ排出することで、タンク本体内の異常な圧力上昇を防止でき、タンク本体が圧力容器となることを確実に回避できるとともに、余剰気体を確実に抜気できる。
【図面の簡単な説明】
【図1】本発明に係る気体溶解分離装置の一実施の形態を示す断面図である。
【図2】同上気体溶解分離装置に用いられている抜気量調整弁の平面図である。
【図3】同上気体溶解分離装置に用いられている反射板の平面図である。
【図4】同上気体溶解分離装置に気液混合用の渦流ポンプを接続した回路の概要図である。
【図5】同上渦流ポンプの断面図である。
【図6】本発明に係る気体溶解分離装置の他の実施の形態を示す断面図である。
【図7】同上気体溶解分離装置に用いられている反射板の平面図である。
【符号の説明】
42 タンク本体
43 気液混合体噴入管
44 噴入口
45 反射板
46 気体溶解室
47 余剰気体排出手段としての抜気量調整弁
48 余剰気体排出手段としての安全弁
49 高濃度溶解液室
50 液取出口部
54 通気穴
55 円板
56 凹状反射面部
57 液透過部
A 気液混合体
B 余剰気体
C 高濃度溶解液
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a gas dissolution / separation apparatus for dissolving a gas in a liquid to separate and produce a high concentration solution.
[0002]
[Prior art]
In the conventional gas dissolution and separation apparatus, a plurality of tanks are connected in series, and the gas-liquid mixture is stirred in the preceding tank so as to increase the amount of gas dissolved in the liquid. Then, the excess gas which did not melt | dissolve in a liquid is isolate | separated from a high concentration solution, and only a high concentration solution is taken out (for example, refer patent document 1).
[0003]
[Patent Document 1]
JP 2001-129377 A (page 6-8, FIG. 1)
[0004]
[Problems to be solved by the invention]
As described above, the conventional gas dissolution / separation apparatus includes a front-stage tank for dissolving the gas in the liquid and a rear-stage tank for separating the excess gas not dissolved in the liquid from the high-concentration solution. Since each is provided and the liquid discharged from the lower part of the preceding tank is sequentially supplied to the upper part of the subsequent tank, the tank must be made a pressure-resistant structure as a pressure vessel, and it must be certified, and the equipment is enlarged In addition, it is difficult to provide at a low cost.
[0005]
The present invention has been made in view of these points, and provides a compact and inexpensive gas dissolution and separation apparatus that does not require a pressure-resistant structure as a pressure vessel and can efficiently separate excess gas that has not been dissolved in a liquid. It is intended to do.
[0006]
[Means for Solving the Problems]
The invention described in claim 1 includes a tank body, a gas-liquid mixture injection pipe for injecting a gas-liquid mixture in which gas and liquid are mixed into an upper portion of the tank body, and the gas-liquid mixture. A turbulent flow generated by reflecting the jet flow of the gas-liquid mixture by the reflector formed on the upper side of the reflector and the reflector provided in the tank body facing the jet port of the mixture jet pipe The gas dissolution chamber that dissolves the gas in the liquid by agitating the gas and the liquid to create a high-concentration solution, and is dissolved in the liquid provided at the upper end of the tank body located above the gas dissolution chamber A surplus gas discharging means for discharging the surplus gas that has not been discharged to the outside, and a partition formed on the lower side of the reflecting plate so as to be able to communicate with the gas dissolving chamber, and transmitted from the gas dissolving chamber to the lower side through the reflecting plate. A high-concentration dissolution chamber containing the high-concentration dissolution solution, A gas dissolution / separation device having a liquid outlet for taking out a high concentration solution from a high temperature solution chamber and injecting the gas / liquid mixture downward into the upper part of the tank body A gas dissolution chamber is formed on the upper side of the reflecting plate facing the nozzle inlet, and an excess gas discharge means is provided at the upper end of the tank body located further above the gas dissolution chamber so as to be dissolved in the liquid in the gas dissolution chamber. Since the surplus gas that has not been discharged is discharged to the outside by this surplus gas discharge means, the tank body is not required to have a pressure-resistant structure as a pressure vessel, and the surplus gas in the gas dissolution chamber can be separated efficiently. Therefore, it is not necessary to install a separation tank, and it is possible to provide a small and inexpensive gas dissolution separation apparatus. In addition, the upper gas dissolution chamber and the lower high-concentration solution chamber can be compactly separated and formed in one tank body by a reflector, and injected from the gas-liquid mixture injection pipe in the gas dissolution chamber. While stirring the gas and liquid by the turbulent flow generated by reflecting the jet flow of the gas-liquid mixture with the reflector, the gas can be efficiently dissolved in the liquid and a high concentration solution can be made. Only this high concentration solution can be taken out from the high concentration solution chamber through the liquid outlet.
[0007]
According to a second aspect of the present invention, in the gas dissolution / separation apparatus according to the first aspect, the surplus gas discharging means includes a venting amount adjusting valve capable of adjusting a venting amount of the surplus gas, and this venting amount adjusting valve Has a vent hole that keeps the valve open even in the most closed state, and by adjusting the opening of the air extraction amount adjusting valve, the surging gas surfacing speed can be adjusted. By adjusting the opening of the air extraction amount adjustment valve so that the descending speed of the high concentration solution into the high concentration solution chamber becomes larger, excess gas permeates the reflector and enters the high concentration solution chamber. It can be prevented from entering. In addition, even if the exhaust air amount adjustment valve is most closed, the vent is kept open, so that the function of exhausting excess gas to the outside can be maintained even if the exhaust air amount adjustment valve is closed by mistake. .
[0008]
According to a third aspect of the present invention, the reflector in the gas dissolution / separation device according to the first or second aspect is formed at the center of a disk having a concavely curved upper surface, and the injection flow of the gas-liquid mixture is A gas-liquid mixture comprising: a reflecting concave reflecting surface portion; and a liquid permeable portion that is provided along the peripheral edge portion of the disk and allows a high-concentration solution in the gas dissolution chamber to pass through the high-concentration solution chamber. Since the jet flow of the gas-liquid mixture injected from the injection pipe collides with the concave reflecting surface at the center of the reflector plate, a turbulent flow with intense stirring action is generated in the gas dissolution chamber. The high-concentration dissolution liquid can be efficiently generated in the gas dissolution chamber, and only the high-concentration dissolution liquid generated in the gas dissolution chamber is provided with a liquid transmission portion provided along the peripheral edge of the reflector plate. Then, it passes through the lower high-concentration solution chamber and is taken out from the liquid outlet. Succoth can.
[0009]
According to a fourth aspect of the present invention, there is provided the gas dissolution / separation device according to any one of the first to third aspects, wherein a safety valve is provided at the upper end of the tank body and discharges at least one of surplus gas and liquid to the outside at a set pressure. Even if the amount of inflow into the tank body increases relative to the amount of outflow from the tank body and the pressure in the tank body increases, the safety valve automatically removes excess gas or liquid from the outside. As a result, the abnormal pressure rise in the tank body can be prevented, the tank body can be surely avoided from becoming a pressure vessel, and excess gas can be vented reliably.
[0010]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, the present invention will be described in detail with reference to one embodiment shown in FIGS. 1 to 5 and another embodiment shown in FIGS.
[0011]
First, an embodiment shown in FIGS. 1 to 5 will be described. As shown in FIG. 4, a suction side pressure gauge 13 and a suction side are provided in a liquid suction port 12 of a vortex pump 11 as a gas-liquid mixing means. A pipe 15 for supplying liquid via the pressure regulating valve 14 is connected, and a gas suction means 16 for sucking a gas such as air is also connected to the liquid suction port 12 in the vortex pump 11.
[0012]
The gas suction means 16 is connected to a suction nozzle 16 a inserted into the liquid suction port 12 of the vortex pump 11 with a gas suction pipe 16 b connected thereto. The gas suction tube 16b is a vertically open upper end tube, for example, when sucking air as a gas.
[0013]
Further, a pipe 18 is drawn out from a gas-liquid discharge port 17 that discharges a gas-liquid mixture in which gas is mixed in the liquid by the vortex pump 11, and this pipe 18 is connected to a gas dissolution and separation device 19. Yes.
[0014]
As shown in FIG. 5, in the vortex pump 11, an annular pressure increasing passage 33 is formed in the pump main body 32, and the liquid suction port 12 is formed in communication with the inlet 34 of the pressure increasing passage 33. A gas-liquid discharge port 17 is formed in communication with the outlet portion 35 of 33, and an isolation portion 36 is formed between the inlet portion 34 and the outlet portion 35 of the pressure increasing passage 33.
[0015]
An impeller 37 is rotatably fitted in the pump body 32, and a radial small blade 38 formed at a predetermined pitch and a blade between these small blades 38 are formed on the outer peripheral portion of the impeller 37. A groove 39 is provided, and the small blade 38 and the blade groove 39 are concentric with the impeller 37 by rotating a rotating shaft 40 fitted in the center of the impeller 37 by an external motor or the like. The inside of the pressure increasing passage 33 is rotated.
[0016]
A suction nozzle 16a is screwed into and fixed to a portion of the vortex pump 11 forming the liquid suction port 12, and a tip portion of the suction nozzle 16a is inserted up to the inlet 34 of the pressure increasing passage 33, and this suction nozzle The gas is sucked into the inlet 34 of the pressure increasing passage 33 from 16a.
[0017]
As shown in FIG. 1, the gas dissolving / separating apparatus 19 is provided around a vertically long tank body 42 installed in a vertical shape by legs 41.
[0018]
In the upper part of the tank body 42, a gas-liquid mixture injection pipe 43 connected to the pipe line 18 is inserted and fixed from the side, and at the tip of the gas-liquid mixture injection pipe 43, gas and An injection port 44 through which the gas-liquid mixture A mixed with the liquid is injected downward into the upper portion of the tank body 42 is opened.
[0019]
Opposite the injection port 44 of the gas-liquid mixture injection pipe 43, a reflection plate 45 is formed in the tank main body 42 so as to be bent in a concave shape on the upper surface, and a gas dissolution chamber 46 is provided above the reflection plate 45. A partition is formed.
[0020]
The gas dissolution chamber 46 dissolves the gas in the liquid by agitating the gas and the liquid by the turbulent flow generated by reflecting the jet flow of the gas-liquid mixture A by the reflector 45, so that the high-concentration solution is obtained. It is a room to make.
[0021]
At the upper end of the tank main body 42 located above the gas dissolution chamber 46, an air removal amount adjustment valve 47 as a surplus gas discharge means for discharging the fine bubble surplus gas B that has not been dissolved in the liquid to the outside. And a safety valve 48 is provided respectively.
[0022]
The air removal amount adjusting valve 47 can adjust the air removal amount of the surplus gas B discharged to the outside with a manually adjusted predetermined valve opening, and discharge a small amount of liquid accompanying the air removal to the outside. On the other hand, the safety valve 48 is a valve that automatically opens when the pressure in the upper part of the tank body 42 exceeds the set pressure, and discharges at least one of the excess gas B and the liquid to the outside. is there.
[0023]
A high concentration solution chamber 49 that can communicate with the gas dissolution chamber 46 is partitioned below the reflection plate 45, and the reflection plate 45 is connected to the high concentration solution chamber 49 from the gas dissolution chamber 46. The high-concentration solution C that has been permeated downward is accommodated. On the side surface of the lower part of the tank main body 42, a liquid outlet 50 for taking out the high concentration solution C from the high concentration solution chamber 49 is projected.
[0024]
As shown in FIG. 2, the air removal amount adjustment valve 47 is provided with a movable valve body 53 that is opened and closed by turning a handle 52 inside the valve body 51. Thus, a vent hole 54 is formed to keep the valve open even in the most closed state.
[0025]
As shown in FIG. 3, the reflecting plate 45 has a concave reflecting surface portion 56 that reflects the jet flow of the gas-liquid mixture A at the center of a circular plate 55 whose upper surface is bent in a concave shape. Along the peripheral portion of the disk 55, a large number of through-hole-shaped liquid permeation portions 57 are provided for allowing the high-concentration solution C to permeate from the gas dissolution chamber 46 to the high-concentration solution chamber 49.
[0026]
Next, the operation of the illustrated vortex pump 11 and gas dissolution separation device 19 will be described.
[0027]
Liquid is sucked into the liquid suction port 12 of the vortex pump 11 from the pipe line 15. The liquid sucked into the liquid suction port 12 of the vortex pump 11 substantially goes around the pressure increasing passage 33 together with the impeller 37, and the liquid is swirled between each pressure groove 33 of the impeller 37 and the pressure increasing passage 33. This is carried out simultaneously in each blade groove 39 and proceeds in the pressure-up passage 33, and the pressure is increased as the pressure-up passage 33 is advanced and discharged from the gas-liquid discharge port 17.
[0028]
At the same time, the suction pressure adjustment valve 14 is throttled while looking at the suction side pressure gauge 13, the liquid suction port 12 of the vortex pump 11 is set to a negative pressure, and a gas such as air is sucked from the gas suction pipe 16b through the suction nozzle 16a. To do.
[0029]
Therefore, when the liquid is sucked into the pressure increasing passage 33 from the liquid suction port 12, gas is also sucked into the inlet portion 34 of the pressure increasing passage 33 from the suction nozzle 16a, and the impeller 37 and the pressure increasing passage together with the liquid and the gas. A gas-liquid mixture is produced by mixing with fine bubbles in a liquid, which is agitated by the vortex generated between the liquid and the liquid.
[0030]
The gas-liquid mixture whose pressure has been increased by the vortex pump 11 is discharged from the gas-liquid discharge port 17 to the pipe 18 and is supplied to the gas dissolution / separation device 19 through the pipe 18.
[0031]
In the gas dissolution / separation apparatus 19, the gas / liquid mixture A is injected into the gas dissolution chamber 46 from the injection port 44 of the gas / liquid mixture injection pipe 43, and the gas / liquid mixture A is disturbed in the gas dissolution chamber 46. It can be flow-stirred to increase the amount of gas dissolved in the liquid.
[0032]
That is, the turbulent flow generated by reflecting the injection flow of the gas-liquid mixture A injected from the injection port 44 of the gas-liquid mixture injection pipe 43 into the gas dissolution chamber 46 by the concave reflecting surface portion 56 of the reflection plate 45. By vigorously stirring the gas and the liquid, the gas can be efficiently dissolved in the liquid at a high concentration to make a high concentration solution.
[0033]
At this time, there is a specific gravity difference between the surplus gas B that has not been dissolved in the liquid and the liquid, and buoyancy acts on the fine bubble surplus gas B. It floats toward the upper part, and is discharged to the outside at least from the air extraction amount adjusting valve 47 and in some cases from the safety valve 48.
[0034]
On the other hand, the high-concentration dissolution liquid in the gas dissolution chamber 46 moves toward the lower-pressure high-concentration dissolution liquid chamber 49 and permeates the liquid permeation portion 57 at the peripheral edge of the reflector 45 and passes through the high-concentration dissolution liquid chamber 49. The high-concentration solution C in the high-concentration solution chamber 49 flows out from the liquid outlet 50.
[0035]
Next, effects of the embodiment shown in FIGS. 1 to 3 will be described.
[0036]
A gas dissolution chamber 46 is formed on the upper side of the reflector 45 facing the injection port 44 of the gas / liquid mixture injection pipe 43 for injecting the gas / liquid mixture A downward into the upper portion of the tank body 42, and this gas dissolution An air removal amount adjustment valve 47 is provided at the upper end of the tank body 42 located further above the chamber 46, and the excess gas B that has not been dissolved in the liquid in the gas dissolution chamber 46 is discharged to the outside by the air removal amount adjustment valve 47. Since it is discharged, the tank main body 42 is not required to have a pressure-resistant structure as a pressure vessel, and the excess gas B in the gas dissolution chamber 46 can be efficiently separated, so that it is necessary to install a separation tank in addition to the dissolution tank Therefore, a gas dissolution / separation apparatus 19 that is small and inexpensive can be provided.
[0037]
Further, the upper gas dissolution chamber 46 and the lower high-concentration solution chamber 49 can be compactly separated and formed in one tank body 42 by the reflector 45. In the gas dissolution chamber 46, the gas-liquid mixture is injected. Turbulent flow with intense stirring action in the gas dissolution chamber 46 by colliding the reflected flow of the gas-liquid mixture A injected from the inlet pipe 43 with the concave reflecting surface portion 56 at the center of the reflecting plate 45 and reflecting it. In this turbulent flow, the gas can be efficiently dissolved in the liquid to efficiently generate the high concentration solution C, and only the high concentration solution C generated in the gas dissolution chamber 46 is reflected. The liquid can be transmitted to the lower high-concentration dissolution liquid chamber 49 through the liquid permeation section 57 provided along the peripheral edge of the plate 45 and taken out from the high-concentration dissolution liquid chamber 49 through the liquid outlet 50. it can.
[0038]
Furthermore, since the rising speed of the surplus gas B can be adjusted by adjusting the opening degree of the venting amount adjusting valve 47, the rising speed is higher than the descending speed of the high concentration solution C to the high concentration solution chamber 49. By adjusting the opening degree of the air extraction amount adjustment valve 47 so as to increase, it is possible to prevent the surplus gas B from being sucked into the liquid permeable portion 57 of the reflector 45 and entering the high concentration solution chamber 49.
[0039]
At this time, even if the air removal amount adjustment valve 47 is mistakenly closed most, the open state is maintained by the vent hole 54, so that the function of discharging the surplus gas B to the outside can be maintained.
[0040]
In addition, even if the amount of inflow into the tank main body 42 increases with respect to the amount of outflow from the tank main body 42 and the pressure in the tank main body 42 tends to rise, the excess gas B or liquid is automatically generated by the safety valve 48. , The abnormal pressure rise in the tank main body 42 can be prevented, the tank main body 42 can be reliably prevented from becoming a pressure vessel, and the surplus gas B can be reliably vented.
[0041]
Next, another embodiment shown in FIGS. 6 and 7 will be described. The same reference numerals are given to the same parts as those in the embodiment shown in FIGS. 1 to 3, and the description thereof is omitted.
[0042]
As shown in FIG. 6, a gas-liquid mixture injection pipe 43a connected to the pipe line 18 shown in FIG. 4 is inserted and fixed in the upper part of the tank body 42 from the upper surface of the tank. At the lower end of the liquid mixture injection pipe 43a, an injection port 44a for injecting the gas-liquid mixture A, which is a mixture of gas and liquid, downward into the upper portion of the tank body 42 is opened.
[0043]
The liquid outlet 50a for taking out the high-concentration dissolution liquid C from the high-concentration dissolution chamber 49 in the tank main body 42 to the outside is once pulled out from the bottom of the tank main body 42 and then bent sideways. Has been.
[0044]
Further, a reflecting plate 45a having a curved upper surface is provided in the tank body 42 so as to face the injection port 44a of the gas-liquid mixture injection pipe 43a. This reflecting plate 45a is shown in FIG. As described above, a concave reflection surface portion 56 for reflecting the jet flow of the gas-liquid mixture A is formed in the central portion of the circular plate 55 whose upper surface is bent in a concave shape, and a plurality of protrusions are formed on the outer peripheral portion of the circular plate 55. The protrusions 57a are projected at an equal pitch, and the protrusions 57a are brought into contact with the inner wall surface of the tank body 42, whereby the liquid-permeable portion 57b having a gap between the protrusions 57a and 57a is formed on the disk 55. The high-concentration solution C is transmitted from the gas dissolution chamber 46 to the high-concentration solution chamber 49 through these liquid permeation portions 57b.
[0045]
The gas dissolution / separation device 19 is a device for mixing and dissolving various gases such as air, oxygen or ozone in a liquid, and this device includes a fine bubble generation device, an oxygen enrichment device or an ozone dissolution device. .
[0046]
【The invention's effect】
According to the first aspect of the present invention, the gas dissolution chamber is formed on the upper side of the reflecting plate facing the injection port of the gas-liquid mixture injection pipe for injecting the gas-liquid mixture downward into the upper portion of the tank body. The surplus gas discharging means is provided at the upper end of the tank body located further above the gas dissolving chamber, and the surplus gas not dissolved in the liquid in the gas dissolving chamber is discharged to the outside by the surplus gas discharging means. The main body is not required to have a pressure-resistant structure as a pressure vessel, and the excess gas in the gas dissolution chamber can be separated efficiently, so there is no need to install a separation tank in addition to the dissolution tank, and the gas dissolution is small and inexpensive. A separation device can be provided. In addition, the upper gas dissolution chamber and the lower high-concentration solution chamber can be compactly separated and formed in one tank body by a reflector, and injected from the gas-liquid mixture injection pipe in the gas dissolution chamber. While stirring the gas and liquid by the turbulent flow generated by reflecting the jet flow of the gas-liquid mixture with the reflector, the gas can be efficiently dissolved in the liquid and a high concentration solution can be made. Only this high concentration solution can be taken out from the high concentration solution chamber through the liquid outlet.
[0047]
According to the second aspect of the present invention, the rising speed of the surplus gas can be adjusted by adjusting the opening degree of the venting amount adjusting valve, so that the rising speed is transferred to the high concentration solution chamber of the high concentration solution. By adjusting the opening degree of the air extraction amount adjustment valve so as to be larger than the lowering speed of the gas, it is possible to prevent surplus gas from passing through the reflector and entering the high concentration solution chamber. In addition, even if the exhaust air amount adjustment valve is most closed, the open state is maintained by the vent hole, so even if the exhaust air amount adjustment valve is accidentally closed, the function of discharging excess gas to the outside Can be maintained.
[0048]
According to the third aspect of the present invention, the gas-liquid mixture is injected into the gas-dissolving chamber by colliding the injection flow of the gas-liquid mixture injected from the gas-liquid mixture injection pipe with the concave reflection surface portion at the center of the disk of the reflection plate. Since a turbulent flow accompanied by a vigorous stirring action is generated, a high-concentration solution can be efficiently generated in the gas dissolution chamber, and only the high-concentration solution generated in the gas dissolution chamber can be It can permeate | transmit to a lower high concentration melt | dissolution liquid chamber through the liquid permeation | transmission part provided along the peripheral part of a board, and can take out outside from a liquid extraction part.
[0049]
According to the fourth aspect of the present invention, even when the amount of inflow into the tank main body increases with respect to the amount of outflow from the tank main body and the pressure in the tank main body tends to rise, the excess gas is automatically automatically generated by the safety valve. Alternatively, by discharging the liquid to the outside, it is possible to prevent an abnormal pressure increase in the tank main body, to reliably avoid the tank main body from becoming a pressure vessel, and to reliably vent excess gas.
[Brief description of the drawings]
FIG. 1 is a cross-sectional view showing an embodiment of a gas dissolution and separation apparatus according to the present invention.
FIG. 2 is a plan view of an evacuation amount adjusting valve used in the gas dissolution / separation apparatus.
FIG. 3 is a plan view of a reflector used in the gas dissolution / separation apparatus.
FIG. 4 is a schematic diagram of a circuit in which a gas-liquid mixing vortex pump is connected to the gas dissolution / separation apparatus.
FIG. 5 is a sectional view of the vortex pump.
FIG. 6 is a cross-sectional view showing another embodiment of the gas dissolution and separation apparatus according to the present invention.
FIG. 7 is a plan view of a reflection plate used in the gas dissolution / separation apparatus.
[Explanation of symbols]
42 Tank main body 43 Gas-liquid mixture injection pipe 44 Injection port 45 Reflector plate 46 Gas dissolution chamber 47 Exhaust amount adjustment valve 48 as surplus gas discharge means Safety valve 49 as surplus gas discharge means High-concentration solution chamber 50 Liquid outlet Part 54 vent hole 55 disk 56 concave reflection surface part 57 liquid permeation part A gas-liquid mixture B surplus gas C high concentration solution

Claims (4)

タンク本体と、
このタンク本体の上部内に気体と液体とが混合された気液混合体を下向きに噴入する気液混合体噴入管と、
この気液混合体噴入管の噴入口に対向して上記タンク本体内に設けられた反射板と、
この反射板の上側に仕切形成され反射板により気液混合体の噴入流を反射して発生した乱流により気体と液体とを攪拌することで気体を液体中に溶解させて高濃度溶解液を作る気体溶解室と、
この気体溶解室の上側に位置する上記タンク本体の上端に設けられ液体中に溶解されなかった余剰気体を外部へ排出する余剰気体排出手段と、
上記反射板の下側に上記気体溶解室と連通可能に仕切形成され上記気体溶解室から上記反射板を経て下側へ透過させた高濃度溶解液を収容する高濃度溶解液室と、
この高濃度溶解液室から高濃度溶解液を外部へ取出す液取出口部と
を具備したことを特徴とする気体溶解分離装置。
The tank body,
A gas-liquid mixture injection pipe for injecting a gas-liquid mixture in which gas and liquid are mixed into the upper part of the tank body downward;
A reflector provided in the tank body facing the injection port of the gas-liquid mixture injection pipe;
The gas is dissolved in the liquid by agitating the gas and the liquid by the turbulent flow generated by reflecting the jet flow of the gas-liquid mixture by the reflection plate formed on the upper side of the reflection plate, and the high-concentration solution is obtained. A gas dissolution chamber to make,
Surplus gas discharging means provided at the upper end of the tank body located on the upper side of the gas dissolving chamber and discharging the surplus gas that has not been dissolved in the liquid to the outside;
A high-concentration solution chamber that accommodates a high-concentration solution that is formed under the reflector so as to communicate with the gas-dissolving chamber and is transmitted from the gas-dissolving chamber to the lower side through the reflector;
A gas dissolution / separation apparatus comprising a liquid outlet portion for taking out a high concentration solution from the high concentration solution chamber.
余剰気体排出手段は、余剰気体の抜気量を調整できる抜気量調整弁を備え、
この抜気量調整弁は、最も閉じ操作された状態でも開弁状態を保つ通気穴を有する
ことを特徴とする請求項1記載の気体溶解分離装置。
The surplus gas discharge means includes an air extraction amount adjustment valve capable of adjusting the amount of exhaust of the excess gas,
2. The gas dissolution / separation apparatus according to claim 1, wherein the venting amount adjusting valve has a vent hole that keeps the valve open even when the valve is most closed.
反射板は、
上面が凹状に彎曲形成された円板の中央部に形成され気液混合体の噴入流を反射する凹状反射面部と、
上記円板の周縁部に沿って設けられ気体溶解室の高濃度溶解液を高濃度溶解液室に透過させる液透過部と
を具備したことを特徴とする請求項1または2記載の気体溶解分離装置。
The reflector is
A concave reflecting surface portion that is formed at the center of a disk whose upper surface is bent into a concave shape and reflects the jet flow of the gas-liquid mixture;
3. A gas dissolution separation according to claim 1 or 2, further comprising a liquid permeation section provided along the peripheral edge of the disc for allowing the high concentration solution in the gas dissolution chamber to pass through the high concentration solution chamber. apparatus.
タンク本体の上端に設けられ設定圧力で余剰気体および液体の少なくとも一方を外部へ排出する安全弁
を具備したことを特徴とする請求項1乃至3のいずれか記載の気体溶解分離装置。
The gas dissolution / separation device according to any one of claims 1 to 3, further comprising a safety valve provided at an upper end of the tank body and configured to discharge at least one of surplus gas and liquid to the outside at a set pressure.
JP2003169944A 2003-06-13 2003-06-13 Gas dissolution separator Expired - Fee Related JP3814262B2 (en)

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JP3814262B2 JP3814262B2 (en) 2006-08-23

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007020418A (en) * 2005-07-12 2007-02-01 Nikuni:Kk Water culture system
JP2008168293A (en) * 2007-12-14 2008-07-24 Shigen Kaihatsu Kk Microbubble generator
JP2015127052A (en) * 2015-01-30 2015-07-09 株式会社ガスター Pressure container
JP2021137717A (en) * 2020-03-04 2021-09-16 株式会社サイエンス Gas-liquid dissolution tank

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007020418A (en) * 2005-07-12 2007-02-01 Nikuni:Kk Water culture system
JP2008168293A (en) * 2007-12-14 2008-07-24 Shigen Kaihatsu Kk Microbubble generator
JP2015127052A (en) * 2015-01-30 2015-07-09 株式会社ガスター Pressure container
JP2021137717A (en) * 2020-03-04 2021-09-16 株式会社サイエンス Gas-liquid dissolution tank
JP7212949B2 (en) 2020-03-04 2023-01-26 株式会社サイエンス Gas-liquid dissolving tank

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