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JP4128890B2 - Gas-liquid mixing reaction method and gas-liquid mixing reaction apparatus - Google Patents
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JP4128890B2 - Gas-liquid mixing reaction method and gas-liquid mixing reaction apparatus - Google Patents

Gas-liquid mixing reaction method and gas-liquid mixing reaction apparatus Download PDF

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JP4128890B2
JP4128890B2 JP2003063927A JP2003063927A JP4128890B2 JP 4128890 B2 JP4128890 B2 JP 4128890B2 JP 2003063927 A JP2003063927 A JP 2003063927A JP 2003063927 A JP2003063927 A JP 2003063927A JP 4128890 B2 JP4128890 B2 JP 4128890B2
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liquid mixing
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JP2004267940A (en
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聡 中野
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株式会社日本環境科学
廣前 孝明
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Description

【0001】
【発明の属する技術分野】
本発明は、気液混合反応装置に関するものである。
【0002】
【従来の技術】
従来、気液混合反応装置の一例として、処理水を加圧タンクに入れ、同加圧タンク内に加圧した酸素を供給することにより、この酸素を加圧状態で処理水に溶解させ、その後、この処理水を大気開放することにより溶存した酸素を微細気泡となして水中に浮遊させることによって、この微細気泡の酸素を再び処理水中に溶解させる気液混合反応装置があった(例えば、特許文献1参照。)。
【0003】
上記気液混合反応装置は、図6に示すように、加圧タンク100を立直した筒状に形成し、エアーコンプレッサー200によって圧縮した空気に酸素を混合した混合気体を、前記加圧タンク100の上部から供給するようにしている。一方、この加圧タンク100内側上部に、先端を斜め下方向で、かつこの加圧タンク100の接線方向に向けて配設したノズル300から被処理水を加圧状態にて噴出し、加圧タンク100内の上部の酸素を巻き込みながら、この加圧タンク100内に酸素を含む渦流を発生させて回転させることによって、酸素を被処理水に溶解させるものである。そして、その後に前記加圧タンク100の下流に設けたバルブ400を開いて加圧タンク100中の被処理水を大気圧中に放出することによって、溶解されなかった酸素を微細気泡とし、同微細気泡が被処理水中に長時間浮遊することによって2次的な酸素移動が起こり、高い効率の酸素溶解が行われるようにしている。
【0004】
なお、上記加圧タンク100には、実際には図示しない水面検知センサや圧力計が設けられており、加圧タンク100に供給される被処理水の量や圧力を調整できるようになっている。図中、500は加圧用ポンプである。
【0005】
【特許文献1】
特開平11−207162号公報
【0006】
【発明が解決しようとする課題】
しかし、上記従来の気液混合反応装置は、酸素を混合した気体を加圧タンク100内に上方から供給するとともに、同加圧タンク100内の外周部上部に配設したノズル300から被処理水を噴射するようにしていたために、未溶解分の気体は加圧タンク100の上部に留まることになる。
【0007】
したがって、水面管理、流入気体量管理、流入被処理水量及び加圧タンク100の圧力管理が必要となり、これらの管理を充分に行うことは困難であるとともに、被処理水の水質によっては管理不能又は頻繁なメンテナンスを必要とする等の不具合があった。さらに、上記気液混合反応装置は、ノズルから吐出される被処理水によって酸素が混合された気体を巻き込むようにしているだけなので、酸素と被処理水とが充分に混合されず、酸素溶解の効率が低下するおそれがあった。
【0008】
また、気体を溶解した被処理水を大気開放する際には、加圧タンク100の下流に設けたバルブ400を開いて加圧タンク100の被処理水を大気圧下に放出するだけなので、一旦処理液に溶解した気体が気泡化した微細気泡は、被処理液中において充分かつ満遍なく浮遊することがないために、気液混合反応を効率良く行えないおそれがあった。
【0009】
本発明は、上記課題を解決することのできる気液混合反応方法、及び気液混合反応装置を提供することを目的としている。
【0010】
【課題を解決するための手段】
そこで、請求項1記載の本発明に係る気液混合反応方法では、被処理水中にエジェクタ効果により気体を混合するとともに、円筒状の加圧タンク内へ、同タンクの下部の周方向に所定間隔をあけて複数個配設した吐出ノズルからタンク底面の接線方向に吐出させ、この加圧タンクの下部から上方へ旋回させながら移動させる間に前記気体を前記被処理水中に溶解させる気液混合反応方法において、前記吐出ノズルは、略円筒形状のパイプ体の先端に複数の切り込みを入れて複数の切り込み片を形成し、各切り込み片のそれぞれの先端をパイプの中心に向けてすぼめるとともに、各切り込み片のそれぞれを前記パイプ体の軸線方向に対して所定角度をつけながらねじり、しかも、それぞれ隣接する切り込み片同士が所定間隔をあけて一定方向に重なり合うように構成している。
【0011】
また、請求項2記載の本発明では、前記加圧タンクの後段に、大気圧とした円筒状の大気解放タンクを配設し、前記加圧タンクの上部から排出させた被処理水を、前記大気解放タンクの下部からタンク底面の接線方向に吐出させ、被処理水に溶解した前記気体成分を微細気泡化してこの大気解放タンク内を下部から上方へと浮遊させることにより前記被処理水と前記気体とを気液混合反応させることとした。
【0012】
また、請求項3記載の本発明では、前記気体は、少なくともオゾンを含む気体とした。
【0013】
請求項4記載の本発明に係る気液混合反応装置では、円筒状の加圧タンクの下部に、同タンクの周方向に所定間隔をあけて複数個配設され、タンク底面に対して接線方向に吐出可能とした吐出ノズルを配設し、この吐出ノズルと被処理水を吸引する吸引手段とを被処理水供給路を介して連通連結するとともに、この被処理水供給路の中途に、エジェクタ効果により気体を前記被処理水中に混合する混合手段を設けた気液混合反応装置において、前記吐出ノズルは、略円筒形状のパイプ体の先端に複数の切り込みを入れて複数の切り込み片を形成し、各切り込み片のそれぞれの先端をパイプの中心に向けてすぼめるとともに、各切り込み片のそれぞれを前記パイプ体の軸線方向に対して所定角度をつけながらねじり、しかも、それぞれ隣接する切り込み片同士が所定間隔をあけて一定方向に重なり合うように構成した
【0014】
また、請求項5記載の本発明では、前記加圧タンクの後段に、大気圧とした円筒状の大気解放タンクを配設するとともに、同大気解放タンクの下部に、タンク底面に対して接線方向に吐出可能とした吐出ノズルを配設し、前記加圧タンクの上部から排出させた被処理水を、この大気解放タンクの下部からタンク底面の接線方向に吐出させ、被処理水中に溶解した前記気体成分を微細気泡化してこの大気解放タンク内を下部から上方へと浮遊させるように構成した。
【0016】
また、請求項6記載の本発明では、前記加圧タンク及び大気解放タンクの上部に、それぞれ前記吐出ノズルと同形の排出ノズルを垂設し、しかも、タンク上面からノズル先端までを、所定距離だけ離隔させた。
【0018】
【発明の実施の形態】
本発明に係る気液混合反応方法は、被処理水中にエジェクタ効果により気体を混合するとともに、円筒状の加圧タンク内へ、同タンクの下部からタンク底面の接線方向に吐出させ、この加圧タンクの下部から上方へ旋回させながら移動させる間に前記気体を前記被処理水中に溶解させるようにしたものである。
【0019】
上記方法により、湖沼や河川、その他各種排水などの浄化処理を行う際に、被処理水中に浄化に必要な気体を効率良く混合させることができる。
【0020】
特に、前記加圧タンクの後段に、大気圧とした円筒状の大気解放タンクを配設し、前記加圧タンクの上部から排出させた被処理水を、前記大気解放タンクの下部からタンク底面の接線方向に吐出させ、被処理水に溶解した前記気体成分を微細気泡化してこの大気解放タンク内を下部から上方へと浮遊させることにより前記被処理水と前記気体とを気液混合反応させるとよい。
【0021】
このように、被処理水を旋回させながら、下方から上方へと移動させることで、水圧により気体を溶解・混合しやすく、また、大気解放タンク内の狭い領域で微細気泡を混合させることになるので反応性が向上する。したがって、十分に気液を溶解させて気液混合反応をより効率良く行うことができるのである。
【0022】
使用する気体としては特に限定するものではなく、例えば水中の溶存酸素を補って微生物の活動を促進させて汚水処理するために酸素などを好適に使用することができる。
【0023】
本実施の形態では、水処理に使用する気体として少なくともオゾンを含む気体を用いるようにしており、これによって湖沼の場合であればアオコなどの分解が可能となる他、家畜糞尿を含む被処理水であれば懸濁物の分解、さらに工業排水でれば懸濁物の分解、脱色が可能となる。なお、そのほかにも、例えば二酸化炭素を用いてpH調整をしたりすることも可能である。
【0024】
上記方法を実現するための装置としては、円筒状の加圧タンクの下部に、タンク底面に対して接線方向に吐出可能とした吐出手段を配設し、この吐出手段と被処理水を吸引する吸引手段とを被処理水供給路を介して連通連結するとともに、この被処理水供給路の中途に、エジェクタ効果により気体を前記被処理水中に混合する混合手段を設ける構成の気液混合反応装置とすることができる。
【0025】
この場合も、前記加圧タンクの後段に、大気圧とした円筒状の大気解放タンクを配設するとともに、同大気解放タンクの下部に、タンク底面に対して接線方向に吐出可能とした吐出手段を配設し、前記加圧タンクの上部から排出させた被処理水を、この大気解放タンクの下部からタンク底面の接線方向に吐出させ、被処理水中に溶解した前記気体成分を微細気泡化してこの大気解放タンク内を下部から上方へと浮遊させるように構成するとよい。
【0026】
また、前記吐出手段を吐出ノズルとし、同吐出ノズルはタンク周方向に所定間隔をあけて複数個配設することが望ましい。すなわち、吐出のノズルを複数個用いることで、前記加圧タンク内では、気体を含んだ被処理水にタンク内での旋回を確実に行わせることができ、広範囲で大容量の被処理水に気体を溶解させることができ、前記大気解放タンク内においては、微細気泡を長時間浮遊させながら気体と被処理水との気液混合反応を効率良く行える。
【0027】
以上説明してきたように、本実施形態に係る気液混合反応装置は、加圧タンク、大気解放タンク、両タンク内に配設した吐出ノズルを主たる構成とするもので、きわめて簡単な構造で、コンパクトなシステムでありながら、効率のよい水処理が可能となる。
【0028】
また、気体をコンプレッサなどを用いて強制的に送給するのではなく、エジェクタ効果を用いた自吸式としているのでメンテナンスや電気代が不要で大きなコストダウンとなる
また、タンク内において水面が下がることがないので、液面管理のためのレベルセンサなどが不要であり、やはりメンテナンスの容易化、及びコストダウンが図れる。なお、前記レベルセンサは、粘度や懸濁物の多い液体を対象とした場合センサ機能がはたらかないことが分かっているので、この点からも液面管理を不要とした本装置は、汚濁程度が激しい家畜糞尿を含む被処理水、あるいは工業排水などを主とする被処理水への適用も可能となる。
【0029】
このように、本実施形態に係る気液混合反応装置は、タンク内の水面管理や、流入させる気体量の管理、さらには被処理水量の管理などが不要であり、いかなる水質の被処理水にも対応が可能となる。しかも、煩雑な設備や操作が不要な装置なので、設備の小型化、作業効率の向上、管理の簡素化を図ることができる。
【0030】
ところで、前記加圧タンク及び大気解放タンクの上部に、それぞれ前記吐出ノズルと同形の排出ノズルを垂設し、しかも、タンク上面からノズル先端までを、所定距離だけ離隔させるとよい。
【0031】
かかる構成とすることで、前記両タンク内で被処理水が旋回しながら下方から上方へと上昇移動したときに、共に上昇した気体がタンク上部に滞留しても、被処理水に巻き込まれながら排出されるので、気液混合反応を効率的に行える。
【0032】
上述した排出ノズルの構成としては、略円筒形状のパイプ体の先端に複数の切り込みを入れて複数の切り込み片を形成し、各切り込み片のそれぞれの先端をパイプの中心に向けてすぼめるとともに、各切り込み片のそれぞれを前記パイプ体の軸線方向に対して所定角度をつけながらねじり、しかも、それぞれ隣接する切り込み片同士が所定間隔をあけて一定方向に重なり合うようにするとよい。
【0033】
すなわち、排出する場合であれば、ノズル内においても被処理水を旋回させながら排出可能であり、ノズル内において気体と被処理水との混合を促進させることが可能となり、さらにタンク内における旋回によって、加圧タンク内であれば気体の溶解を、大気解放タンク内であれば微細気泡と被処理水との接触を増大することができ、気体の溶解、混合を促進することができ、その結果気液混合反応効率をより向上させることができる。
【0034】
以下、本発明の実施の形態について、図面を参照しながらより具体的に説明する。
【0035】
図1は本実施形態に係る気液混合反応装置の模式的説明図、図2は同気液混合反応装置の横断面視による説明図、図3は同気液混合反応装置に用いられるノズルの斜視図、図4は同ノズルの正面図である。
【0036】
図1に示すように、本実施形態に係る気液混合反応装置は、円筒状の加圧タンク1の下部に、先端をタンク底面10に対して接線方向に向けて吐出手段として吐出ノズル2を配設し、同吐出ノズル2と被処理水を加圧状態で送給する吸引手段としての加圧ポンプ3とを、被処理水供給路としての給水管4を介して連通連結した気体溶解部Aと、前記加圧タンク1と連通管5を介して連通連結し、下部には前記加圧タンク1と同様に、先端をタンク底面60に対して接線方向に向けて吐出ノズル2を配設した円筒状の大気解放タンク6を具備する気液混合部Bとを具備している。7は前記大気解放タンクの上面より伸延させた排出管、50は前記連通管5の中途に設けた流量調整バルブであり、同流量調整バルブ50によって加圧タンク1内の圧力も調整することができる。
【0037】
また、前記気体溶解部Aの給水管4の中途には、混合手段としてエジェクタ8を配設しており、前記加圧ポンプ3により吸引した被処理水中に例えばオゾンを含む気体をエジェクタ効果により混合可能としている。
【0038】
また、前記加圧タンク1及び大気解放タンク6の上面には、それぞれ前記吐出ノズル2と同形の排出ノズル9を垂設し、しかも、各タンク上面から前記排出ノズル9の先端までを、所定距離だけ離隔させている。
【0039】
かかる構成により、溶解部Aにおいて、被処理水には前記エジェクタ8により気体が混合され、気体が混合された被処理水は、前記加圧タンク1の下部からタンク内接線方向へ加圧された状態で吐出され、この加圧タンク1内を旋回しながら上昇するうちに混合された気体が被処理水中に溶解する。
【0040】
そして、後段の気液混合部Bでは、前記溶解部Aにおいて気体が混合された被処理水が、大気解放タンク6の下部から、やはりタンク接線方向に吐出されて大気圧下において被処理水中に溶解した気体が微細気泡化し、この微細気泡化した気体が被処理水と一緒に旋回しながら大気解放タンク6内を上昇していく。
【0041】
したがって、微細気泡化した気体と被処理水との接触が増大し、気体、特にこの場合はオゾンを含んだ気体なので被処理水を効果的に殺菌、浄化することができる。
【0042】
しかも、加圧タンク1内では、溶解した気体が、また、大気解放タンク6内では微細気泡化した気体が、それぞれタンク上部に滞留しても、水に巻き込まれながら排出ノズル9から排出されるので、気体がタンク内に無駄に止まることがなく、気液混合反応の効率を高めることができる。
【0043】
ところで、前述の吐出ノズル2は、前記タンク1(6)の周方向に複数個配設しており、本実施の形態においては、図2で示すように、4個の排出ノズル2を等間隔で配置するとともに、それぞれをタンク底面10(60)に対して同じ向きの接線方向に被処理水を吐出可能としている。したがって、より強力な旋回流を発生させることができる。
【0044】
ここで、本実施形態で用いる吐出ノズル2及び排出ノズル9について、さらに詳述する。
【0045】
本実施の形態においては、前記吐出ノズル2及び排出ノズル9は同一ノズルを用いており、図3及び図4に示すように、略円筒形状のパイプ体20の先端に複数の切り込み21を入れて複数の切り込み片22を形成し、各切り込み片22のそれぞれの先端をパイプ中心に向けてすぼめるとともに、各切り込み片22のそれぞれを前記パイプ体20の軸線方向に対して所定角度をつけながらねじり、しかも、それぞれ隣接する切り込み片22同士が所定間隔をあけて一定方向に重なり合うように構成されている。
【0046】
切り込み21の長さとしては、特に限定するものではないが、パイプ体20の全長に対して1/4〜1/3の長さとしている。また、切り込み片22(切り込み21)の数についても特に限定するものではないが、本実施の形態では6枚の切り込み片22を備えるようにしている。
【0047】
上記構成の吐出ノズル2及び排出ノズル9を用いることにより、吐出時においては、吐出ノズル2内において被処理水に旋回力を与え、前記エジェクタ8により混合された気体を被処理水中に溶解しやすくし、しかも先端を絞ることで吐出圧を上げて加圧タンク1内を旋回しやすくし、旋回させることによって気体の溶解を促進させることができる。一方、排出時においては、前述したように、両タンク1,6の上部に気体が滞留しても、被処理水がこれを巻き込み、上記構成の排出ノズル9中に進入する際に、切り込み片22によって細かくされ、かつ旋回しながら排出ノズル9中を進行するので、加圧タンク1から排出されるときに気体の溶解量が損なわれることがなく、また、大気解放タンク9から排出される場合についても、同様に排出ノズル9の中でも旋回が発生して微細気泡化した気体と被処理水とが十分に接触することにより、水処理効果が向上する。
【0048】
なお、本実施の形態では被処理水に対して用いる気体は少なくともオゾンを含むものとしたが、例えば二酸化炭素を用いて被処理水のpH調整などを実行することも可能であり、気体としては処理目的に応じて適宜選択して使用することができる。
【0049】
ところで、上記排出ノズル9については、これを備えなくとも気液混合反応による水処理は可能である。
【0050】
例えば、図5に示すように、加圧タンク1及び大気解放タンク2の上面に、連通管4、排出管7の一端を直接連結してもよい。なお、この例においては、供給管4と連通管5と排出管7の径に差をつけており、連通管5よりも供給管4の径を大きくして供給される被処理水量と連通管4を介して排出される被処理水量とに差をもたせ、加圧タンク1内が高圧力下の雰囲気になるようにしている。かかる構成により、高圧の下で被処理水中に溶解した気体が、大気解放タンク6に至って大気圧となったときの微細気泡化が促進される。
【0051】
【発明の効果】
本発明により、以下の効果を生起する。
【0052】
(1)請求項1記載の本発明では、被処理水中にエジェクタ効果により気体を混合するとともに、円筒状の加圧タンク内へ、同タンクの下部の周方向に所定間隔をあけて複数個配設した吐出ノズルからタンク底面の接線方向に吐出させ、この加圧タンクの下部から上方へ旋回させながら移動させる間に前記気体を前記被処理水中に溶解させる気液混合反応方法において、前記吐出ノズルは、略円筒形状のパイプ体の先端に複数の切り込みを入れて複数の切り込み片を形成し、各切り込み片のそれぞれの先端をパイプの中心に向けてすぼめるとともに、各切り込み片のそれぞれを前記パイプ体の軸線方向に対して所定角度をつけながらねじり、しかも、それぞれ隣接する切り込み片同士が所定間隔をあけて一定方向に重なり合うように構成している。したがって、被処理水や気体は限定されることなく両者を混合することができ、汎用性が高まるとともに、簡単な操作で、かつ低コストでの水処理が可能となる。
【0053】
(2)請求項2記載の本発明では、前記加圧タンクの後段に、大気圧とした円筒状の大気解放タンクを配設し、前記加圧タンクの上部から排出させた被処理水を、前記大気解放タンクの下部からタンク底面の接線方向に吐出させ、被処理水に溶解した前記気体成分を微細気泡化してこの大気解放タンク内を下部から上方へと浮遊させることにより前記被処理水と前記気体とを気液混合反応させることとした。したがって、簡単な操作で、かつ低コストでの気液混合反応による水処理が行え、処理の効率化を図ることができる。
【0054】
(3)請求項3記載の本発明では、前記気体は、少なくともオゾンを含む気体とした。したがって、殺菌効果が高く、懸濁の激しい被処理水であってもこれの清浄化が可能となる。
【0055】
(4)請求項4記載の本発明に係る気液混合反応装置では、円筒状の加圧タンクの下部に、同タンクの周方向に所定間隔をあけて複数個配設され、タンク底面に対して接線方向に吐出可能とした吐出ノズルを配設し、この吐出ノズルと被処理水を吸引する吸引手段とを被処理水供給路を介して連通連結するとともに、この被処理水供給路の中途に、エジェクタ効果により気体を前記被処理水中に混合する混合手段を設けた気液混合反応装置において、前記吐出ノズルは、略円筒形状のパイプ体の先端に複数の切り込みを入れて複数の切り込み片を形成し、各切り込み片のそれぞれの先端をパイプの中心に向けてすぼめるとともに、各切り込み片のそれぞれを前記パイプ体の軸線方向に対して所定角度をつけながらねじり、しかも、それぞれ隣接する切り込み片同士が所定間隔をあけて一定方向に重なり合うように構成した。したがって、コンパクトで簡単な装置となるので、低コストでの水処理が容易に効率良く行える。
【0056】
(5)請求項5記載の本発明では、前記加圧タンクの後段に、大気圧とした円筒状の大気解放タンクを配設するとともに、同大気解放タンクの下部に、タンク底面に対して接線方向に吐出可能とした吐出ノズルを配設し、前記加圧タンクの上部から排出させた被処理水を、この大気解放タンクの下部からタンク底面の接線方向に吐出させ、被処理水中に溶解した前記気体成分を微細気泡化してこの大気解放タンク内を下部から上方へと浮遊させるように構成した。したがって、コンパクトで簡単な構成の気液混合反応装置を提供することが可能となり、気液混合反応による水処理を低コストで効率良く行え、しかも煩わしい操作なども必要としない。
【0058】
(6)請求項6記載の本発明では、前記加圧タンク及び大気解放タンクの上部に、それぞれ前記吐出ノズルと同形の排出ノズルを垂設し、しかも、タンク上面からノズル先端までを、所定距離だけ離隔させた。したがって、気体がタンク上部に滞留しても、被処理水に巻き込まれながら排出されるので、気液混合反応を効率的に行える。
【図面の簡単な説明】
【図1】本実施形態に係る気液混合反応装置の模式的説明図である。
【図2】同気液混合反応装置の横断面視による説明図である。
【図3】図3は同気液混合反応装置に用いられるノズルの斜視図である。
【図4】同ノズルの正面図である。
【図5】気液混合反応装置の変容例を示す説明図である。
【図6】従来の気液混合反応装置のを示す説明図である。
【符号の説明】
A 溶解部
B 気液混合部
1 加圧タンク
2 排出ノズル
6 大気解放タンク
8 エジェクタ
9 排出ノズル
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a gas-liquid mixing reaction apparatus.
[0002]
[Prior art]
Conventionally, as an example of a gas-liquid mixing reactor, treated water is put into a pressurized tank, and oxygen is supplied into the pressurized tank to dissolve the oxygen in the treated water. In addition, there is a gas-liquid mixing reaction apparatus in which oxygen dissolved in fine water is dissolved again in the treated water by making dissolved oxygen into fine bubbles and floating in the water by releasing the treated water into the atmosphere (for example, patents) Reference 1).
[0003]
As shown in FIG. 6, the gas-liquid mixing reaction apparatus forms a pressurized tank 100 in an upright cylindrical shape, and mixes oxygen mixed with air compressed by an air compressor 200. Supply from the top. On the other hand, to-be-treated water is ejected in a pressurized state from a nozzle 300 disposed on the inside upper part of the pressurized tank 100 with the tip inclined downward and tangential to the pressurized tank 100. Oxygen is dissolved in the water to be treated by generating and rotating an eddy current containing oxygen in the pressurized tank 100 while entraining oxygen in the upper part of the tank 100. Then, the valve 400 provided downstream of the pressurized tank 100 is opened to discharge the water to be treated in the pressurized tank 100 into the atmospheric pressure, whereby the undissolved oxygen is turned into fine bubbles, and the same minute When the bubbles float in the water to be treated for a long time, secondary oxygen movement occurs, and highly efficient oxygen dissolution is performed.
[0004]
The pressurized tank 100 is actually provided with a water level detection sensor and a pressure gauge (not shown) so that the amount and pressure of water to be treated supplied to the pressurized tank 100 can be adjusted. . In the figure, 500 is a pressurizing pump.
[0005]
[Patent Document 1]
JP-A-11-207162 [0006]
[Problems to be solved by the invention]
However, the conventional gas-liquid mixing reaction apparatus supplies a gas mixed with oxygen into the pressurized tank 100 from above and from the nozzle 300 disposed at the upper part of the outer periphery of the pressurized tank 100 to be treated water. Therefore, the undissolved gas stays in the upper portion of the pressurized tank 100.
[0007]
Therefore, water surface management, inflow gas amount management, inflow to-be-treated water amount and pressure management of the pressurized tank 100 are necessary, and it is difficult to sufficiently manage these, and depending on the quality of the to-be-treated water, There were problems such as requiring frequent maintenance. Furthermore, since the gas-liquid mixing reaction apparatus only involves a gas mixed with oxygen by the water to be treated discharged from the nozzle, the oxygen and the water to be treated are not sufficiently mixed, so There was a risk that efficiency would decrease.
[0008]
Further, when the treated water in which the gas is dissolved is opened to the atmosphere, the valve 400 provided downstream of the pressurized tank 100 is opened to release the treated water in the pressurized tank 100 to atmospheric pressure. Since the fine bubbles in which the gas dissolved in the treatment liquid is bubbled do not float sufficiently and evenly in the treatment liquid, there is a possibility that the gas-liquid mixing reaction cannot be performed efficiently.
[0009]
An object of this invention is to provide the gas-liquid mixing reaction method and gas-liquid mixing reaction apparatus which can solve the said subject.
[0010]
[Means for Solving the Problems]
Therefore, in the gas-liquid mixing reaction method according to the first aspect of the present invention, the gas is mixed into the water to be treated by the ejector effect, and the gas is mixed into the cylindrical pressurized tank at a predetermined interval in the circumferential direction of the lower portion of the tank. open the discharged tangentially of the tank bottom from the discharge nozzle in which a plurality arranged, said gas-liquid mixing Ru dissolved in the water to be treated with the gas while moving while turning upward from the bottom of the pressurized tank In the reaction method, the discharge nozzle is formed with a plurality of cuts at the end of a substantially cylindrical pipe body to form a plurality of cut pieces, and each tip of each cut piece is narrowed toward the center of the pipe, Each notch piece is twisted while making a predetermined angle with respect to the axial direction of the pipe body, and the adjacent notch pieces are spaced apart from each other in a certain direction. It is configured so as each other now.
[0011]
Moreover, in this invention of Claim 2, the cylindrical air release tank made into atmospheric pressure is arrange | positioned in the back | latter stage of the said pressurization tank, The to-be-processed water discharged | emitted from the upper part of the said pressurization tank, By discharging in the tangential direction of the tank bottom from the lower part of the air release tank, the gas component dissolved in the water to be treated is made into fine bubbles and suspended in the air release tank upward from the lower part to the water to be treated and the A gas-liquid mixed reaction was performed with gas.
[0012]
In the present invention according to claim 3, the gas is a gas containing at least ozone.
[0013]
In the gas-liquid mixing reactor according to the fourth aspect of the present invention, a plurality of tanks are disposed at a predetermined interval in the circumferential direction of the tank at a lower portion of the cylindrical pressurized tank, and are tangential to the tank bottom surface. A discharge nozzle that can discharge the liquid is disposed, and the discharge nozzle and a suction unit that sucks the water to be treated are connected to each other through the water supply path to be treated, and an ejector is disposed in the middle of the water supply path to be treated. In the gas-liquid mixing reaction apparatus provided with mixing means for mixing gas into the water to be treated by effect , the discharge nozzle forms a plurality of cut pieces by making a plurality of cuts at the tip of a substantially cylindrical pipe body. The notches are squeezed toward the center of the pipe, and the notches are twisted at a predetermined angle with respect to the axial direction of the pipe body, and are adjacent to each other. Interrupt pieces would configured to overlap in a predetermined direction at predetermined intervals.
[0014]
Further, in the present invention according to claim 5, a cylindrical atmospheric release tank having an atmospheric pressure is disposed downstream of the pressurized tank, and a tangential direction with respect to the tank bottom surface is provided at a lower portion of the atmospheric release tank. Discharge nozzles that can be discharged are disposed, and the treated water discharged from the upper part of the pressurized tank is discharged from the lower part of the atmospheric release tank in the tangential direction of the tank bottom, and dissolved in the treated water. The gas component was made into fine bubbles and configured to float in the atmosphere release tank from the bottom upward.
[0016]
Further, in the present invention according to claim 6 , a discharge nozzle having the same shape as the discharge nozzle is provided above each of the pressurization tank and the atmospheric release tank, and further, a predetermined distance is provided from the tank upper surface to the nozzle tip. Separated.
[0018]
DETAILED DESCRIPTION OF THE INVENTION
In the gas-liquid mixing reaction method according to the present invention, gas is mixed into the water to be treated by the ejector effect, and discharged into the cylindrical pressurized tank from the bottom of the tank in the tangential direction of the tank bottom. The gas is dissolved in the water to be treated while moving while turning upward from the lower part of the tank.
[0019]
By the above method, when purification treatment of lakes, rivers, and other various wastewater is performed, the gas necessary for purification can be efficiently mixed into the water to be treated.
[0020]
In particular, a cylindrical atmospheric release tank having an atmospheric pressure is disposed downstream of the pressurized tank, and the water to be treated discharged from the upper part of the pressurized tank is disposed on the bottom surface of the tank from the lower part of the atmospheric release tank. When the gas component is discharged in a tangential direction and the gas component dissolved in the water to be treated is made into fine bubbles and suspended in the atmosphere release tank from the lower part to the upper part, the water to be treated and the gas are subjected to a gas-liquid mixed reaction. Good.
[0021]
In this way, by moving the water to be treated from the lower side to the upper side while swirling, it is easy to dissolve and mix the gas by the water pressure, and the fine bubbles are mixed in a narrow area in the air release tank. So the reactivity is improved. Therefore, the gas-liquid mixing reaction can be performed more efficiently by sufficiently dissolving the gas-liquid.
[0022]
The gas to be used is not particularly limited. For example, oxygen or the like can be preferably used to treat dissolved water by supplementing dissolved oxygen in water to promote the activity of microorganisms.
[0023]
In the present embodiment, a gas containing at least ozone is used as a gas used for water treatment, so that in the case of a lake, water can be decomposed and water to be treated containing livestock manure If so, the suspension can be decomposed, and if it is industrial wastewater, the suspension can be decomposed and decolored. In addition, it is also possible to adjust pH using, for example, carbon dioxide.
[0024]
As an apparatus for realizing the above method, a discharge means capable of discharging in a tangential direction with respect to the bottom surface of the tank is disposed at the lower part of a cylindrical pressurized tank, and the discharge means and the water to be treated are sucked. A gas-liquid mixing reaction apparatus having a structure in which a suction means is connected to and communicated via a to-be-treated water supply path, and a mixing means for mixing gas into the to-be-treated water by an ejector effect is provided in the middle of the to-be-treated water supply path. It can be.
[0025]
In this case as well, a cylindrical atmospheric release tank having an atmospheric pressure is disposed downstream of the pressurized tank, and a discharge means capable of discharging in a tangential direction with respect to the bottom of the tank at the lower part of the atmospheric release tank. The treated water discharged from the upper part of the pressurized tank is discharged from the lower part of the atmospheric release tank in the tangential direction of the tank bottom, and the gas component dissolved in the treated water is made into fine bubbles. The atmosphere release tank may be configured to float upward from the lower part.
[0026]
Further, it is desirable that the discharge means is a discharge nozzle, and a plurality of the discharge nozzles are arranged at predetermined intervals in the circumferential direction of the tank. That is, by using a plurality of discharge nozzles, the water to be treated containing gas can be reliably swirled in the tank in the pressurized tank, and the water to be treated can be treated in a wide range and with a large capacity. The gas can be dissolved, and in the atmosphere release tank, the gas-liquid mixing reaction between the gas and the water to be treated can be performed efficiently while the fine bubbles are suspended for a long time.
[0027]
As described above, the gas-liquid mixing reaction apparatus according to the present embodiment mainly has a pressurized tank, an air release tank, and a discharge nozzle disposed in both tanks, and has a very simple structure. Although it is a compact system, it enables efficient water treatment.
[0028]
In addition, gas is not forcibly fed using a compressor, but is self-priming using the ejector effect, so maintenance and electricity costs are not required, resulting in a large cost reduction. Also, the water level is lowered in the tank. Therefore, there is no need for a level sensor for liquid level management, and maintenance can be facilitated and costs can be reduced. In addition, since it is known that the sensor function does not work if the level sensor is used for liquids with high viscosity or suspended matter, this device, which does not require liquid level management from this point, Therefore, it can be applied to water to be treated containing livestock manure, or water to be treated mainly including industrial wastewater.
[0029]
As described above, the gas-liquid mixing reaction apparatus according to this embodiment does not require management of the water level in the tank, management of the amount of gas to be introduced, and management of the amount of water to be treated. Can also be supported. In addition, since it is a device that does not require complicated facilities and operations, it is possible to reduce the size of the facilities, improve work efficiency, and simplify management.
[0030]
By the way, it is preferable that a discharge nozzle having the same shape as the discharge nozzle is provided above the pressurization tank and the atmosphere release tank, respectively, and further, the tank upper surface and the nozzle tip are separated by a predetermined distance.
[0031]
By adopting such a configuration, when the water to be treated moves upward from below while turning in both tanks, even if the gas that has risen together stays in the upper part of the tank, the water is caught in the water to be treated. Since it is discharged, the gas-liquid mixing reaction can be performed efficiently.
[0032]
As the configuration of the discharge nozzle described above, a plurality of cuts are formed at the tip of a substantially cylindrical pipe body to form a plurality of cut pieces, and each tip of each cut piece is narrowed toward the center of the pipe, Each of the cut pieces may be twisted while making a predetermined angle with respect to the axial direction of the pipe body, and adjacent cut pieces may be overlapped in a predetermined direction with a predetermined interval.
[0033]
That is, in the case of discharging, the water to be treated can be discharged while swirling in the nozzle, and the mixing of the gas and the water to be treated can be promoted in the nozzle, and further by swirling in the tank. In the pressurized tank, the dissolution of gas can be increased, and in the atmospheric release tank, the contact between the fine bubbles and the water to be treated can be increased, and the dissolution and mixing of the gas can be promoted. The gas-liquid mixing reaction efficiency can be further improved.
[0034]
Hereinafter, embodiments of the present invention will be described more specifically with reference to the drawings.
[0035]
FIG. 1 is a schematic explanatory view of a gas-liquid mixed reaction apparatus according to the present embodiment, FIG. 2 is an explanatory view in a cross-sectional view of the same gas-liquid mixed reaction apparatus, and FIG. 3 is a diagram of a nozzle used in the same gas-liquid mixed reaction apparatus. A perspective view and FIG. 4 are front views of the nozzle.
[0036]
As shown in FIG. 1, the gas-liquid mixing reaction apparatus according to the present embodiment has a discharge nozzle 2 as a discharge means at a lower portion of a cylindrical pressurized tank 1 with a tip tangential to a tank bottom surface 10. A gas dissolving part which is disposed and communicated with a discharge pump 2 and a pressure pump 3 as a suction means for supplying the water to be treated in a pressurized state via a water supply pipe 4 as a water supply path for water to be treated. A is connected in communication with the pressurized tank 1 via the communication pipe 5, and the discharge nozzle 2 is disposed at the lower portion with the tip tangential to the tank bottom surface 60 in the same manner as the pressurized tank 1. And a gas-liquid mixing part B having a cylindrical atmospheric release tank 6. 7 is a discharge pipe extended from the upper surface of the atmosphere release tank, and 50 is a flow rate adjusting valve provided in the middle of the communication pipe 5. The flow rate adjusting valve 50 can also adjust the pressure in the pressurized tank 1. it can.
[0037]
Further, an ejector 8 is provided as a mixing means in the middle of the water supply pipe 4 of the gas dissolving part A, and a gas containing, for example, ozone is mixed in the water to be treated sucked by the pressure pump 3 by the ejector effect. It is possible.
[0038]
Discharge nozzles 9 having the same shape as the discharge nozzles 2 are provided on the upper surfaces of the pressurized tank 1 and the air release tank 6, respectively, and a predetermined distance from each tank upper surface to the tip of the discharge nozzle 9. Just separated.
[0039]
With this configuration, in the dissolving portion A, the treated water is mixed with gas by the ejector 8, and the treated water mixed with gas is pressurized from the lower part of the pressurized tank 1 in the tank tangential direction. The mixed gas dissolves in the water to be treated as it is discharged in a state and ascends while rotating in the pressurized tank 1.
[0040]
Then, in the gas-liquid mixing part B at the subsequent stage, the water to be treated in which the gas is mixed in the dissolving part A is discharged from the lower part of the atmosphere release tank 6 in the tank tangential direction and into the water to be treated under atmospheric pressure. The dissolved gas is made into fine bubbles, and the fine bubbles are raised in the atmosphere release tank 6 while swirling together with the water to be treated.
[0041]
Therefore, the contact between the microbubbled gas and the water to be treated is increased, and since the gas, particularly the gas containing ozone in this case, the water to be treated can be effectively sterilized and purified.
[0042]
Moreover, the dissolved gas in the pressurized tank 1 and the fine gas bubbles in the atmospheric release tank 6 are discharged from the discharge nozzle 9 while being caught in water even if they stay in the upper part of the tank. Therefore, the gas does not stop in the tank and the efficiency of the gas-liquid mixing reaction can be increased.
[0043]
By the way, a plurality of the above-described discharge nozzles 2 are arranged in the circumferential direction of the tank 1 (6). In the present embodiment, as shown in FIG. In addition, the water to be treated can be discharged in a tangential direction in the same direction with respect to the tank bottom surface 10 (60). Therefore, a stronger swirl flow can be generated.
[0044]
Here, the discharge nozzle 2 and the discharge nozzle 9 used in this embodiment will be described in more detail.
[0045]
In the present embodiment, the discharge nozzle 2 and the discharge nozzle 9 are the same nozzle, and as shown in FIGS. 3 and 4, a plurality of cuts 21 are made at the tip of a substantially cylindrical pipe body 20. A plurality of cut pieces 22 are formed, the respective leading ends of the cut pieces 22 are squeezed toward the center of the pipe, and the cut pieces 22 are twisted while making a predetermined angle with respect to the axial direction of the pipe body 20. Moreover, the adjacent cut pieces 22 are configured to overlap each other at a predetermined interval in a certain direction.
[0046]
The length of the notch 21 is not particularly limited, but is set to a length of ¼ to 3 with respect to the entire length of the pipe body 20. Further, the number of the cut pieces 22 (cuts 21) is not particularly limited, but in the present embodiment, six cut pieces 22 are provided.
[0047]
By using the discharge nozzle 2 and the discharge nozzle 9 configured as described above, during discharge, a swirl force is applied to the water to be treated in the discharge nozzle 2, and the gas mixed by the ejector 8 is easily dissolved in the water to be treated. In addition, it is possible to increase the discharge pressure by narrowing the tip to facilitate turning in the pressurized tank 1 and to promote gas dissolution by turning. On the other hand, at the time of discharge, as described above, even if gas stays in the upper part of both tanks 1 and 6, when the water to be treated is entrained and enters the discharge nozzle 9 having the above-described configuration, When the gas is discharged from the pressurized tank 1, the amount of dissolved gas is not impaired and the gas is discharged from the air release tank 9 Similarly, the water treatment effect is improved by sufficiently bringing the gas to be treated into fine bubbles into contact with the water to be treated in the discharge nozzle 9.
[0048]
In this embodiment, the gas used for the water to be treated includes at least ozone. However, the pH of the water to be treated can be adjusted using carbon dioxide, for example. It can be appropriately selected and used depending on the processing purpose.
[0049]
By the way, even if the discharge nozzle 9 is not provided, water treatment by gas-liquid mixing reaction is possible.
[0050]
For example, as shown in FIG. 5, one end of the communication pipe 4 and the discharge pipe 7 may be directly connected to the upper surfaces of the pressurized tank 1 and the atmosphere release tank 2. In this example, the diameters of the supply pipe 4, the communication pipe 5, and the discharge pipe 7 are different, and the amount of water to be treated and the communication pipe supplied with the diameter of the supply pipe 4 larger than that of the communication pipe 5. The amount of water to be treated discharged through 4 is made different so that the inside of the pressurized tank 1 becomes an atmosphere under high pressure. With this configuration, the formation of fine bubbles when the gas dissolved in the water to be treated under high pressure reaches the atmospheric pressure release tank 6 and becomes atmospheric pressure is promoted.
[0051]
【The invention's effect】
According to the present invention, the following effects occur.
[0052]
(1) In the present invention described in claim 1, gas is mixed in the water to be treated by the ejector effect, and a plurality of gas is disposed in the cylindrical pressurized tank at a predetermined interval in the circumferential direction at the bottom of the tank. discharged from the discharge nozzles set in the tangential direction of the tank bottom, the gas-liquid mixing reactions how the gas Ru is dissolved in the treatment water while moving while turning upward from the lower portion of the pressurizing tank, the discharge The nozzle is formed with a plurality of cuts at the tip of a substantially cylindrical pipe body to form a plurality of cut pieces, each tip of each cut piece is squeezed toward the center of the pipe, and each cut piece is twisting paying careful predetermined angle with respect to the axial direction of the pipe body, moreover, the cut pieces that are adjacent each configured to overlap in a predetermined direction at predetermined intervals That. Therefore, both water to be treated and gas can be mixed without limitation, and versatility is enhanced, and water treatment can be performed with a simple operation and at low cost.
[0053]
(2) In the present invention according to claim 2, a cylindrical atmospheric release tank having an atmospheric pressure is disposed downstream of the pressurization tank, and the water to be treated discharged from the upper part of the pressurization tank, Discharge from the lower part of the atmosphere release tank in the tangential direction of the tank bottom, make the gas component dissolved in the water to be treated into fine bubbles and float the inside of the atmosphere release tank upward from the lower part to The gas was subjected to a gas-liquid mixed reaction. Therefore, it is possible to perform water treatment by gas-liquid mixing reaction at a low cost with a simple operation, and the efficiency of the treatment can be improved.
[0054]
(3) In the present invention described in claim 3, the gas is a gas containing at least ozone. Therefore, even if the water to be treated has a high sterilizing effect and is severely suspended, it can be cleaned.
[0055]
(4) In the gas-liquid mixing reaction apparatus according to the present invention as set forth in claim 4, a plurality of tanks are disposed at a predetermined interval in the circumferential direction of the tank at the lower part of the cylindrical pressurized tank, the discharge nozzle is disposed which enables discharge tangentially Te, thereby communicatively connected through the treated water supply passage and a suction means for sucking the treated water and the discharge nozzle, midway of the water to be treated supply passage Further, in the gas-liquid mixing reaction apparatus provided with mixing means for mixing gas into the water to be treated by an ejector effect , the discharge nozzle is formed by making a plurality of cuts at a tip end of a substantially cylindrical pipe body. And squeeze the tip of each notch piece toward the center of the pipe, twist each notch piece with a predetermined angle with respect to the axial direction of the pipe body, and To cut pieces would configured to overlap in a predetermined direction at predetermined intervals. Therefore, since it becomes a compact and simple device, water treatment at low cost can be performed easily and efficiently.
[0056]
(5) In the present invention according to claim 5, a cylindrical atmospheric release tank having an atmospheric pressure is disposed downstream of the pressurized tank, and a tangent to the bottom of the tank is provided below the atmospheric release tank. Discharge nozzles that can be discharged in the direction are disposed, and the treated water discharged from the upper part of the pressurized tank is discharged from the lower part of the atmospheric release tank in the tangential direction of the tank bottom, and dissolved in the treated water The gas component was made into fine bubbles and configured to float in the atmosphere release tank from the bottom upward. Accordingly, it is possible to provide a gas-liquid mixing reaction apparatus having a compact and simple configuration, and water treatment by gas-liquid mixing reaction can be efficiently performed at low cost, and troublesome operations are not required.
[0058]
(6) In the present invention according to claim 6 , a discharge nozzle having the same shape as the discharge nozzle is provided above each of the pressurized tank and the atmospheric release tank, and a predetermined distance is provided from the tank upper surface to the nozzle tip. Only separated. Therefore, even if the gas stays in the upper part of the tank, the gas-liquid mixing reaction can be performed efficiently because the gas is discharged while being caught in the water to be treated.
[Brief description of the drawings]
FIG. 1 is a schematic explanatory view of a gas-liquid mixing reaction apparatus according to the present embodiment.
FIG. 2 is an explanatory view of the same gas-liquid mixing reaction apparatus in a cross-sectional view.
FIG. 3 is a perspective view of a nozzle used in the same gas-liquid mixing reaction apparatus.
FIG. 4 is a front view of the nozzle.
FIG. 5 is an explanatory view showing a modification example of the gas-liquid mixing reaction apparatus.
FIG. 6 is an explanatory view showing a conventional gas-liquid mixing reaction apparatus.
[Explanation of symbols]
A Dissolving part B Gas-liquid mixing part 1 Pressurized tank 2 Discharge nozzle 6 Atmospheric release tank 8 Ejector 9 Discharge nozzle

Claims (6)

被処理水中にエジェクタ効果により気体を混合するとともに、円筒状の加圧タンク内へ、同タンクの下部の周方向に所定間隔をあけて複数個配設した吐出ノズルからタンク底面の接線方向に吐出させ、この加圧タンクの下部から上方へ旋回させながら移動させる間に前記気体を前記被処理水中に溶解させる気液混合反応方法において、
前記吐出ノズルは、略円筒形状のパイプ体の先端に複数の切り込みを入れて複数の切り込み片を形成し、各切り込み片のそれぞれの先端をパイプの中心に向けてすぼめるとともに、各切り込み片のそれぞれを前記パイプ体の軸線方向に対して所定角度をつけながらねじり、しかも、それぞれ隣接する切り込み片同士が所定間隔をあけて一定方向に重なり合うように構成していることを特徴とする気液混合反応方法。
Gas is mixed into the water to be treated by the ejector effect and discharged into a cylindrical pressurized tank from a plurality of discharge nozzles arranged at predetermined intervals in the circumferential direction at the bottom of the tank in the tangential direction of the tank bottom. are allowed, in the gas-liquid mixing reactions how the gas Ru is dissolved in the treatment water while moving while turning upward from the bottom of the pressure tank,
The discharge nozzle is formed with a plurality of cuts at the tip of a substantially cylindrical pipe body to form a plurality of cut pieces, and each tip of the cut pieces is squeezed toward the center of the pipe, Gas-liquid mixing characterized in that each is twisted while making a predetermined angle with respect to the axial direction of the pipe body, and the adjacent cut pieces overlap each other at a predetermined interval in a predetermined direction Reaction method.
前記加圧タンクの後段に、大気圧とした円筒状の大気解放タンクを配設し、前記加圧タンクの上部から排出させた被処理水を、前記大気解放タンクの下部からタンク底面の接線方向に吐出させ、被処理水に溶解した前記気体成分を微細気泡化してこの大気解放タンク内を下部から上方へと浮遊させることにより前記被処理水と前記気体とを気液混合反応させることを特徴とする請求項1記載の気液混合反応方法。  A cylindrical atmospheric release tank having an atmospheric pressure is disposed at the subsequent stage of the pressurized tank, and the water to be treated discharged from the upper part of the pressurized tank is tangential to the bottom of the tank from the lower part of the atmospheric release tank. The gas component dissolved in the water to be treated is made into fine bubbles and suspended in the atmosphere release tank from the lower part to the upper part to cause the water to be treated and the gas to undergo a gas-liquid mixed reaction. The gas-liquid mixing reaction method according to claim 1. 前記気体は、少なくともオゾンを含む気体としたことを特徴とする請求項1又は請求項2記載の気液混合反応方法。  The gas-liquid mixed reaction method according to claim 1 or 2, wherein the gas is a gas containing at least ozone. 円筒状の加圧タンクの下部に、同タンクの周方向に所定間隔をあけて複数個配設され、タンク底面に対して接線方向に吐出可能とした吐出ノズルを配設し、この吐出ノズルと被処理水を吸引する吸引手段とを被処理水供給路を介して連通連結するとともに、この被処理水供給路の中途に、エジェクタ効果により気体を前記被処理水中に混合する混合手段を設けた気液混合反応装置において、
前記吐出ノズルは、略円筒形状のパイプ体の先端に複数の切り込みを入れて複数の切り込み片を形成し、各切り込み片のそれぞれの先端をパイプの中心に向けてすぼめるとともに、各切り込み片のそれぞれを前記パイプ体の軸線方向に対して所定角度をつけながらねじり、しかも、それぞれ隣接する切り込み片同士が所定間隔をあけて一定方向に重なり合うように構成したことを特徴とする気液混合反応装置。
The bottom of the cylindrical pressure tank, is plurality disposed at predetermined intervals in the circumferential direction of the tank, it is disposed an ejection nozzles can eject tangentially to the tank bottom, and the discharge nozzle A suction means for sucking water to be treated is connected in communication with the water supply path to be treated, and a mixing means for mixing gas into the water to be treated by an ejector effect is provided in the middle of the water supply path to be treated. In the gas-liquid mixing reactor,
The discharge nozzle is formed with a plurality of cuts at the tip of a substantially cylindrical pipe body to form a plurality of cut pieces, and each tip of the cut pieces is squeezed toward the center of the pipe, A gas-liquid mixing reaction apparatus characterized in that each is twisted while making a predetermined angle with respect to the axial direction of the pipe body, and the adjacent cut pieces are overlapped in a predetermined direction with a predetermined interval. .
前記加圧タンクの後段に、大気圧とした円筒状の大気解放タンクを配設するとともに、同大気解放タンクの下部に、タンク底面に対して接線方向に吐出可能とした吐出ノズルを配設し、前記加圧タンクの上部から排出させた被処理水を、この大気解放タンクの下部からタンク底面の接線方向に吐出させ、被処理水中に溶解した前記気体成分を微細気泡化してこの大気解放タンク内を下部から上方へと浮遊させるように構成したことを特徴とする請求項4記載の気液混合反応装置。A cylindrical atmospheric release tank at atmospheric pressure is disposed downstream of the pressurized tank, and a discharge nozzle capable of discharging in a tangential direction with respect to the tank bottom is disposed at the lower part of the atmospheric release tank. The treated water discharged from the upper part of the pressurized tank is discharged from the lower part of the atmosphere release tank in the tangential direction of the tank bottom, and the gas component dissolved in the treated water is made into fine bubbles to form the atmosphere released tank. 5. The gas-liquid mixing reaction apparatus according to claim 4, wherein the gas-liquid mixing reaction apparatus is configured to float inside from below to above. 前記加圧タンク及び大気解放タンクの上部に、それぞれ前記吐出ノズルと同形の排出ノズルを垂設し、しかも、タンク上面からノズル先端までを、所定距離だけ離隔させたことを特徴とする請求項5に記載の気液混合反応装置。  6. A discharge nozzle having the same shape as the discharge nozzle is provided above the pressurization tank and the atmosphere release tank, respectively, and further, the tank upper surface and the nozzle tip are separated by a predetermined distance. The gas-liquid mixing reactor described in 1.
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