Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JP5721587B2 - Dissolution separation tank and gas-liquid mixing dissolution apparatus - Google Patents
[go: Go Back, main page]

JP5721587B2 - Dissolution separation tank and gas-liquid mixing dissolution apparatus - Google Patents

Dissolution separation tank and gas-liquid mixing dissolution apparatus Download PDF

Info

Publication number
JP5721587B2
JP5721587B2 JP2011181810A JP2011181810A JP5721587B2 JP 5721587 B2 JP5721587 B2 JP 5721587B2 JP 2011181810 A JP2011181810 A JP 2011181810A JP 2011181810 A JP2011181810 A JP 2011181810A JP 5721587 B2 JP5721587 B2 JP 5721587B2
Authority
JP
Japan
Prior art keywords
gas
liquid
tank body
tank
longitudinal direction
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
JP2011181810A
Other languages
Japanese (ja)
Other versions
JP2013043113A (en
Inventor
荘一郎 大崎
荘一郎 大崎
佳浩 照屋
佳浩 照屋
橋本 幸雄
幸雄 橋本
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nikuni KK
Original Assignee
Nikuni KK
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Nikuni KK filed Critical Nikuni KK
Priority to JP2011181810A priority Critical patent/JP5721587B2/en
Publication of JP2013043113A publication Critical patent/JP2013043113A/en
Application granted granted Critical
Publication of JP5721587B2 publication Critical patent/JP5721587B2/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • Degasification And Air Bubble Elimination (AREA)

Description

本発明は、液中に気体を溶解させ、さらに溶解しきれなかった気体を分離する溶解分離タンクおよびその溶解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 dissolution / separation tank that dissolves a gas in a liquid and further separates a gas that has not been dissolved, and a gas-liquid mixing and dissolution apparatus using the dissolution / 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は、液中に気体を混合する渦流ポンプから供給された気液混合流体を溶解タンク1の上部に設けられた入口2からタンク内に噴出させて液中に気体を溶解させ、この溶解タンク1の下部に設けられた出口3から取り出された気液混合流体を、溶解タンク1の側部に配置された気液分離タンク4に導き、液中に溶解されなかった気体をこの気液分離タンク4で分離して、気体が高濃度に溶解された液のみを液出口5から必要な施設に供給し、気体は抜気口6より排出するようにした気液混合溶解装置がある。   As shown in FIG. 4, a gas-liquid mixing and dissolving device used as a microbubble generating device that generates microbubbles such as microbubbles is a gas-liquid mixed fluid supplied from a vortex pump that mixes gas in the liquid. The gas-liquid mixed fluid taken out from the outlet 3 provided at the lower part of the dissolution tank 1 is dissolved in the liquid by being jetted into the tank from the inlet 2 provided at the upper part of the dissolution tank 1, and the dissolution tank 1 1 is led to a gas-liquid separation tank 4 arranged on the side of 1, and the gas not dissolved in the liquid is separated by this gas-liquid separation tank 4, and only the liquid in which the gas is dissolved at a high concentration is separated from the liquid outlet 5. There is a gas-liquid mixing and dissolving device in which the gas is supplied to necessary facilities and the gas is discharged from the vent 6.

また、複数の溶解タンクを横方向に順次配置した気液混合溶解装置(例えば、特許文献1参照)、1つのタンクの上部内に溶解タンク機能を持たせるとともに下部内に分離タンク機能を持たせた気液混合溶解装置(例えば、特許文献2参照)もある。   In addition, a gas-liquid mixing and dissolving apparatus in which a plurality of dissolution tanks are sequentially arranged in the horizontal direction (see, for example, Patent Document 1), a dissolution tank function is provided in the upper part of one tank and a separation tank function is provided in the lower part. There is also a gas-liquid mixing and dissolving apparatus (see, for example, Patent Document 2).

特開2001−129377号公報JP 2001-129377 A 特開2002−273183号公報JP 2002-273183 A

上記のような気液混合溶解装置は、いずれも縦長の溶解タンクを用いるため高さ方向に大型化するとともに、渦流ポンプなどを溶解タンクの横方向に配置せざるを得ないため、平面設置スペースも大きくなる問題がある。   Since the gas-liquid mixing and dissolving apparatus as described above uses a vertically long dissolution tank, the size is increased in the height direction, and a vortex pump or the like must be disposed in the lateral direction of the dissolution tank. There is also a problem that becomes larger.

本発明は、このような点に鑑みなされたもので、コンパクトな溶解分離タンクおよび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 | formed in view of such a point, and it aims at providing a compact melt | dissolution separation tank and a gas-liquid mixing melt | dissolution apparatus.

求項に記載された発明は、水平方向を長手方向とする横置き筒形のタンク本体と、上記タンク本体の長手方向一側部上に長手方向に沿って設けられ、加圧供給された気液混合流体を上記タンク本体の長手方向一側部内に導入する気液混合流体圧入口部と、上記タンク本体の長手方向一側部内から長手方向他側部内に向かって設けられ、液中に気体を溶解させる溶解槽部と、上記タンク本体の長手方向他側部内にタンク本体の底部から立設され、途中部から上記溶解槽部とは反対側に向かって上昇傾斜状に形成された斜面部を有し、かつ上端の上方に開口部を形成する気液分離用の気液分離板と、上記タンク本体の長手方向他側部の下部に設けられ、上記気液分離板の上端を経て上記タンク本体の下方に分離された液を取り出す液取出口と、上記タンク本体の長手方向他側部の上部に設けられ、上記気液分離板を経て上記タンク本体の上方に分離された気体を外部へ排出する気体抜き口とを具備し、上記気液分離板と上記タンク本体の長手方向他側部の端面板との間には、上記液取出口の上側に位置する液流制御板が水平に設けられ、上記液流制御板には、上記気液分離板に最も接近し上記液取出口から最も離れた位置に通液穴が開口された溶解分離タンクである。 Invention described in Motomeko 1 includes a horizontal cylindrical tank body to the horizontal direction is the longitudinal direction, is provided along the longitudinal direction on one longitudinal side of the tank body, it is supplied under pressure A gas-liquid mixed fluid pressure inlet for introducing the gas-liquid mixed fluid into one side of the tank body in the longitudinal direction, and from the inside of the tank body to the other side in the longitudinal direction. The dissolution tank part for dissolving the gas in the tank body, and the tank body from the bottom of the tank body in the other side in the longitudinal direction, and formed in a rising slope from the middle part toward the opposite side of the dissolution tank part A gas-liquid separation plate for gas-liquid separation having an inclined surface and forming an opening above the upper end; and a lower portion on the other side in the longitudinal direction of the tank body, the upper end of the gas-liquid separation plate being A liquid outlet for taking out the liquid separated below the tank body Provided above the other longitudinal side of the tank body, through the gas-liquid separator plate comprising a gas release port for discharging the gas separated above the tank body to the outside, the gas-liquid separator plate And a liquid flow control plate located above the liquid outlet is horizontally provided between the tank body and the end face plate on the other side in the longitudinal direction of the tank body. The liquid flow control plate includes the gas-liquid separation plate. This is a dissolution / separation tank in which a liquid passage hole is opened at a position closest to the plate and farthest from the liquid outlet.

請求項に記載された発明は、請求項1記載の溶解分離タンクと、上記溶解分離タンクの下側に配置され、上記溶解分離タンクの上記気液混合流体圧入口部に気液混合流体を加圧供給する渦流ポンプとを具備した気液混合溶解装置である。 The invention described in claim 2, the dissolution separation tank according to claim 1 Symbol mounting, disposed below the dissolution separation tank, the gas-liquid mixture fluid into the gas-liquid mixed fluid pressure inlet portion of the dissolved separating tank Is a gas-liquid mixing and dissolving device equipped with a vortex pump for supplying pressure under pressure.

求項記載の発明によれば、水平方向を長手方向とする横置き筒形のタンク本体内に溶解槽部および気液分離板が設けられたので、コンパクトで気体溶解効率および気液分離効率の良い溶解分離タンクを提供できる。すなわち、加圧供給された気液混合流体を気液混合流体圧入口部からタンク本体の長手方向一側部内に導入する際に、タンク本体の長手方向一側部内から長手方向他側部内にわたって形成される気層部を巻き込むようにして気液混合流体をタンク本体内の液中に噴射させるので、高い気体溶解効率が得られるとともに、液中に溶解しない気泡状態の気体は、気液分離板に沿って上昇する液とともに上昇し、タンク本体の長手方向他側部の下部に設けられた液取出口に向かって下降する液から効率良く分離され、タンク本体の上部内に形成される気層部となって、タンク本体の長手方向他側部の上部に設けられた気体抜き口から外部へ排出されるので、高い気液分離効率が得られる。特に、横置き筒形のタンク本体の長手方向に沿って広範囲に気液混合流体圧入口部を設けることで、タンク本体内の長手方向の広範囲で気体と液体の衝突による接触面積を増やし、タンク全体で気体と液体とを攪拌して溶解を促すことができ、また、未溶解の気泡を分離するために気液分離板の途中部から上記溶解槽部とは反対側に向かって上昇傾斜状に形成された斜面部により、気液混合流体を開口部内の気層部付近まで案内することで上昇流をつくり、気泡を気層部に巻き上げることによって、小さなタンク内でも効率よく気泡を分離できる。さらに、気液分離板とタンク本体の長手方向他側部の端面板との間に水平に設けられた液流制御板に、気液分離板に最も接近し液取出口から最も離れた位置に通液穴を開口したので、気液分離板を経て液取出口に向かう液の流れに効率良く抵抗を与えることができ、より高い気液分離効率が得られる。 According to the invention Motomeko 1, since the horizontal longitudinal direction and the dissolution tank portion horizontal cylindrical tank body to and gas-liquid separation plate is provided, the gas dissolution efficiency and the gas-liquid separation in Compact An efficient dissolution separation tank can be provided. That is, when the gas-liquid mixed fluid supplied under pressure is introduced from the gas-liquid mixed fluid pressure inlet portion into one side in the longitudinal direction of the tank body, it is formed from one side in the longitudinal direction of the tank body to the other side in the longitudinal direction. The gas-liquid mixed fluid is injected into the liquid in the tank body so as to entrain the gas layer portion to be produced, so that high gas dissolution efficiency is obtained and the gas in a bubble state that does not dissolve in the liquid is a gas-liquid separation plate A gas layer formed in the upper part of the tank body that is efficiently separated from the liquid that rises with the liquid rising along the tank and descends toward the liquid outlet provided at the lower part of the other side of the tank body Since it becomes a part and is discharged | emitted outside from the gas vent provided in the upper part of the longitudinal direction other side part of a tank main body, high gas-liquid separation efficiency is obtained. In particular, by providing a gas-liquid mixed fluid pressure inlet in a wide range along the longitudinal direction of the horizontal tank body, the contact area due to collision of gas and liquid in the longitudinal direction in the tank body is increased. The gas and liquid can be stirred as a whole to promote dissolution, and in order to separate undissolved bubbles, the gas-liquid separation plate is inclined upward from the middle to the opposite side of the dissolution tank. By creating the upward flow by guiding the gas-liquid mixed fluid to the vicinity of the gas layer in the opening by the inclined surface formed in the upper part, the bubbles can be efficiently separated even in a small tank by winding the bubbles around the gas layer. . Furthermore, the liquid flow control plate provided horizontally between the gas-liquid separation plate and the end face plate on the other side in the longitudinal direction of the tank body is positioned closest to the gas-liquid separation plate and farthest from the liquid outlet. Since the liquid passage hole is opened, it is possible to efficiently provide resistance to the flow of liquid toward the liquid outlet through the gas-liquid separation plate, and higher gas-liquid separation efficiency can be obtained.

請求項記載の発明によれば、コンパクトな溶解分離タンクに加えて、この溶解分離タンクの下側に気液混合流体を加圧供給する渦流ポンプを配置したので、平面設置スペースがコンパクトな気液混合溶解装置を提供できる。 According to the second aspect of the present invention, in addition to the compact dissolution / separation tank, the vortex pump for pressurizing and supplying the gas-liquid mixed fluid is disposed below the dissolution / separation tank, so that the plane installation space is compact. A liquid mixing and dissolving apparatus can be provided.

本発明に係る溶解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 melt | dissolution separation tank which concerns on this invention. 図1のII線断面図である。It is the II sectional view taken on the line of FIG. 同上溶解分離タンクを備えた気液混合溶解装置の一実施の形態を示す回路図である。It is a circuit diagram which shows one Embodiment of the gas-liquid mixing dissolution apparatus provided with the dissolution separation tank same as the above. 従来の溶解分離タンクを示す断面図である。It is sectional drawing which shows the conventional melt | dissolution separation tank.

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1および図2に示されるように、溶解分離タンク11は、水平方向を長手方向とする横置き筒形のタンク本体12を備えている。このタンク本体12の長手方向一端部(図1右端部)には端面板13が溶接付けされており、この端面板13にはドレン口14が設けられ、このドレン口14は通常は弁により閉じられている。一方、タンク本体12の長手方向他端部(図1左端部)のフランジ部12fには、端面板15がパッキング16を介してボルト17およびナット18により取り付けられている。   As shown in FIGS. 1 and 2, the dissolution / separation tank 11 includes a horizontally-placed cylindrical tank body 12 whose longitudinal direction is the horizontal direction. An end plate 13 is welded to one end of the tank body 12 in the longitudinal direction (the right end in FIG. 1). The end plate 13 is provided with a drain port 14, which is normally closed by a valve. It has been. On the other hand, an end face plate 15 is attached to a flange portion 12f at the other longitudinal end portion (left end portion in FIG. 1) of the tank body 12 with a bolt 17 and a nut 18 via a packing 16.

タンク本体12の長手方向一側部(図1右側部)上には、加圧供給された気液混合流体Aをタンク本体12の長手方向一側部内に導入する気液混合流体圧入口部21が、タンク本体12の長手方向に沿ってタンク本体12の長手方向の全長に対しほぼ半分もの広範囲にわたって設けられている。この気液混合流体圧入口部21は、タンク本体12の上面部にタンク本体12の長手方向に沿って複数の気液混合流体圧入孔22が直線的に配置された状態で穿設され、これらの気液混合流体圧入孔22を囲むようにタンク本体12の上面部に入口枠23が溶接付けされ、この入口枠23の周縁に沿って設けられたフランジ部23fにシール部材23sを介して蓋板24が、図示しないボルトにより取り付けられ、この蓋板24に計器取付口25と、気液混合流体供給口26とが設けられたものである。   On the one side in the longitudinal direction of the tank body 12 (right side in FIG. 1), the gas-liquid mixed fluid pressure inlet 21 for introducing the pressurized gas-liquid mixed fluid A into the one side in the longitudinal direction of the tank body 12. However, it is provided along a longitudinal direction of the tank body 12 over a wide range of almost half of the entire length of the tank body 12 in the longitudinal direction. The gas-liquid mixed fluid pressure inlet 21 is formed in the upper surface of the tank body 12 with a plurality of gas-liquid mixed fluid injection holes 22 arranged linearly along the longitudinal direction of the tank body 12. An inlet frame 23 is welded to the upper surface of the tank body 12 so as to surround the gas-liquid mixed fluid press-fitting hole 22, and a flange 23f provided along the periphery of the inlet frame 23 is covered via a seal member 23s. The plate 24 is attached by bolts (not shown), and the instrument plate installation port 25 and the gas-liquid mixed fluid supply port 26 are provided on the lid plate 24.

上記気液混合流体圧入口部21には、複数の気液混合流体圧入孔22に替えて、タンク本体12の長手方向に沿って細長く穿設されたスリット状の気液混合流体圧入孔を設けるようにしてもよい。   The gas-liquid mixed fluid pressure inlet 21 is provided with slit-like gas-liquid mixed fluid injection holes elongated in the longitudinal direction of the tank body 12 in place of the plurality of gas-liquid mixed fluid injection holes 22. You may do it.

タンク本体12の長手方向一側部内から長手方向他側部(図1左側部)内に向かって、液中に気体を溶解させる溶解槽部27が設けられている。   A dissolution tank 27 for dissolving a gas in the liquid is provided from one longitudinal side of the tank body 12 toward the other longitudinal side (left side in FIG. 1).

タンク本体12の長手方向他側部内にタンク本体12の底部から中位まで立ち上げるように気液分離用の気液分離板28が立設されている。この気液分離板28において、タンク本体12のほぼ中心の高さにあたる途中部から溶解槽部27とは反対側に向かって上昇傾斜状に形成された斜面部28sが、下部に対し折曲形成されている。この気液分離板28の斜面部28sの上端より上方には、開口部29が設けられている。   A gas-liquid separation plate 28 for gas-liquid separation is erected in the other side portion in the longitudinal direction of the tank body 12 so as to rise from the bottom of the tank body 12 to the middle. In this gas-liquid separation plate 28, a slope portion 28s formed in an upward inclined shape from the middle portion corresponding to the height of the center of the tank body 12 toward the side opposite to the dissolution tank portion 27 is bent with respect to the lower portion. Has been. An opening 29 is provided above the upper end of the slope portion 28s of the gas-liquid separation plate 28.

タンク本体12の長手方向他側部の端面板15の下部には、気液分離板28を経てタンク本体12の下方に分離された液を取り出す液取出口31が設けられている。   A liquid outlet 31 is provided below the end face plate 15 on the other side in the longitudinal direction of the tank body 12 to take out the liquid separated below the tank body 12 via the gas-liquid separator 28.

タンク本体12の長手方向他側部の端面板15の上部には、気液分離板28を経てタンク本体12の上方に分離された気体を外部へ排出する気体抜き口32が設けられている。   A gas vent 32 for discharging the gas separated above the tank body 12 via the gas-liquid separation plate 28 to the outside is provided at the upper part of the end face plate 15 on the other side in the longitudinal direction of the tank body 12.

気液分離板28とタンク本体12の長手方向他側部の端面板15との間には、液取出口31の上側に位置する液流制御板33が水平に設けられ、この液流制御板33には、気液分離板28に最も接近し液取出口31から最も離れた位置に通液穴34が開口されている。   A liquid flow control plate 33 located above the liquid outlet 31 is horizontally provided between the gas-liquid separation plate 28 and the end face plate 15 on the other side in the longitudinal direction of the tank body 12, and this liquid flow control plate In 33, a liquid passage hole 34 is opened at a position closest to the gas-liquid separation plate 28 and farthest from the liquid outlet 31.

気液分離板28と端面板15との間には、気液分離板28の上端を経た液を通液穴34を通して液取出口31に導く液取出通路35が形成されている。気液分離板28は、この液取出通路35と上記溶解槽部27との間に設置されている。   Between the gas-liquid separation plate 28 and the end face plate 15, a liquid extraction passage 35 is formed that guides the liquid passing through the upper end of the gas-liquid separation plate 28 to the liquid outlet 31 through the liquid hole 34. The gas-liquid separation plate 28 is installed between the liquid extraction passage 35 and the dissolution tank 27.

図3は、気液混合溶解装置41を示し、溶解分離タンク11と、この溶解分離タンク11の気液混合流体圧入口部21に気液混合流体Aを加圧供給する渦流ポンプ42とを具備している。この渦流ポンプ42は、溶解分離タンク11の下側に配置され、図示しないフレームにより一体的に構成されている。   FIG. 3 shows a gas / liquid mixing / dissolving device 41, which includes a dissolution / separation tank 11 and a vortex pump 42 that pressurizes and supplies the gas / liquid mixed fluid A to the gas / liquid mixed fluid pressure inlet 21 of the dissolution / separation tank 11. doing. The vortex pump 42 is disposed below the dissolution / separation tank 11 and is integrally configured by a frame (not shown).

渦流ポンプ42は、流量調整弁43を有する液吸込配管44に接続された液吸込口45から液Lを吸い込むとともに、気体吸込口46から空気などの気体Gを吸い込み、ポンプ本体47内で回転される羽根車により移送しながら気液を羽根車内で発生する多数の渦流により混合攪拌し、気液混合流体Aを吐出口48より吐出する。この吐出口48は配管49により溶解分離タンク11の気液混合流体圧入口部21に接続されている。   The vortex pump 42 sucks the liquid L from the liquid suction port 45 connected to the liquid suction pipe 44 having the flow rate adjusting valve 43 and sucks the gas G such as air from the gas suction port 46 and is rotated in the pump body 47. The gas and liquid are mixed and stirred by a large number of vortex flows generated in the impeller while being transferred by the impeller, and the gas-liquid mixed fluid A is discharged from the discharge port 48. The discharge port 48 is connected to the gas-liquid mixed fluid pressure inlet 21 of the dissolution / separation tank 11 by a pipe 49.

この溶解分離タンク11の気液混合流体圧入口部21には、圧力計51が設置され、この圧力計51により溶解分離タンク11の上部内に形成される気層部の圧力が計測される。   A pressure gauge 51 is installed at the gas-liquid mixed fluid pressure inlet 21 of the dissolution / separation tank 11, and the pressure of the gas layer formed in the upper part of the dissolution / separation tank 11 is measured by the pressure gauge 51.

溶解分離タンク11の気体抜き口32に接続された配管52中には気体抜き流量を調整する気体抜き量調整弁53が設けられ、また、溶解分離タンク11の液取出口31に接続された配管54には液取出流量を調整する液取出量調整弁55が設けられているので、圧力計51を見ながら、気体抜き量調整弁53を開度調整するとともに、液取出量調整弁55を開度調整することで、気液の各流量と共に気層部56と液層部57の厚み(高さ)が適切なバランスを保つように調整する。   In the pipe 52 connected to the gas vent 32 of the dissolution / separation tank 11, a gas vent amount adjusting valve 53 for adjusting the gas vent flow rate is provided, and the pipe connected to the liquid outlet 31 of the dissolution / separation tank 11 54 is provided with a liquid discharge amount adjustment valve 55 for adjusting the liquid discharge flow rate, so that while looking at the pressure gauge 51, the opening degree of the gas discharge amount adjustment valve 53 is adjusted and the liquid discharge amount adjustment valve 55 is opened. By adjusting the degree, the thickness (height) of the gas layer part 56 and the liquid layer part 57 is adjusted so as to maintain an appropriate balance together with each flow rate of the gas and liquid.

気体抜き量調整弁53を経た配管58は、余剰気体分離器61に接続され、この余剰気体分離器61の下部すなわち液溜り部62は、電磁弁63を経て渦流ポンプ42への液吸込配管44に接続され、余剰気体分離器61に設けられた液位検知スイッチ64により、余剰気体分離器61内の液位が所定位置まで上昇すると感知され、電磁弁63が開いて余剰気体分離器61内の液が渦流ポンプ42へ吸収される。   The pipe 58 that has passed through the gas venting amount adjustment valve 53 is connected to the surplus gas separator 61. Is detected by the liquid level detection switch 64 provided in the surplus gas separator 61 when the liquid level in the surplus gas separator 61 rises to a predetermined position, and the electromagnetic valve 63 is opened and the surplus gas separator 61 is opened. Is absorbed into the vortex pump 42.

余剰気体分離器61の上部すなわち気体溜り部65は、配管66を経てドレン配管67に接続されている。   The upper part of the surplus gas separator 61, that is, the gas reservoir 65 is connected to the drain pipe 67 via the pipe 66.

次に、図1乃至図3に示された実施の形態の作用効果を説明する。   Next, functions and effects of the embodiment shown in FIGS. 1 to 3 will be described.

渦流ポンプ42は、液吸込口45から液Lを吸い込むとともに気体吸込口46から空気などの気体を吸い込み、これらの気液をポンプ本体47内で回転される羽根車により移送しながら多数の渦流により混合攪拌し、気液混合流体Aを吐出口48より吐出する。   The vortex pump 42 sucks in the liquid L from the liquid suction port 45 and sucks in gas such as air from the gas suction port 46, and transfers these gas and liquid by the impeller rotated in the pump body 47 by a large number of vortex flows. After mixing and stirring, the gas-liquid mixed fluid A is discharged from the discharge port 48.

この気液混合流体Aは、配管49によって溶解分離タンク11の気液混合流体圧入口部21に加圧供給され、入口枠23内を経て複数の気液混合流体圧入孔22から溶解分離タンク11のタンク本体12内に噴射され、このタンク本体12内で激しく混合攪拌されつつ横方向(図1左方)へ移動し、溶解槽部27内での液中への気体の溶解が促進される。   The gas-liquid mixed fluid A is pressurized and supplied to the gas-liquid mixed fluid pressure inlet 21 of the dissolution / separation tank 11 through the pipe 49, passes through the inlet frame 23, and is dissolved from the plurality of gas-liquid mixed fluid injection holes 22. The liquid is injected into the tank main body 12 and moved in the lateral direction (left side in FIG. 1) while being vigorously mixed and stirred in the tank main body 12, and the dissolution of the gas into the liquid in the dissolution tank 27 is promoted. .

このとき、横型のタンク本体12の長手方向の全長に対しほぼ半分にわたる広範囲に気液混合流体圧入孔22もしくはスリット状の気液混合流体圧入孔を設けることで、これらの圧入孔がタンク本体12の長手方向に広がるようにすることによって、タンク本体12内の長手方向の広範囲で気体と液体の衝突による接触面積を増やし、タンク全体で気体と液体とを攪拌して溶解を促すようにする。   At this time, by providing the gas-liquid mixed fluid press-fitting hole 22 or the slit-like gas-liquid mixed fluid press-fitting hole in a wide range almost half the total length in the longitudinal direction of the horizontal tank main body 12, these press-fitting holes are formed in the tank main body 12. In this way, the contact area due to the collision of the gas and the liquid is increased over a wide range in the longitudinal direction in the tank body 12, and the gas and the liquid are stirred in the entire tank to promote dissolution.

この段階で、液中に溶解されなかった気体は、気泡として浮上し、タンク本体12内の上部に溜るが、特に、気液分離板28に沿って上方へ移動する液中の気泡は、気液分離板28の先端で下方へ向かって移動する液から分離し易く、タンク本体12内の上部で気層部56となり、気体抜き口32からタンク本体12の外部へ排出される。   At this stage, the gas that has not been dissolved in the liquid floats up as bubbles and accumulates in the upper part of the tank body 12. In particular, the bubbles in the liquid that move upward along the gas-liquid separation plate 28 are gas bubbles. It is easy to separate from the liquid moving downward at the tip of the liquid separation plate 28, becomes the gas layer part 56 at the upper part in the tank body 12, and is discharged from the gas vent 32 to the outside of the tank body 12.

すなわち、未溶解の気泡を分離するためにタンク本体12のほぼ中心レベルに相当する気液分離板28の途中部から上記溶解槽部27とは反対側に向かって上昇傾斜状に傾けた斜面部28sを設け、この斜面部28sにより気液混合流体を開口部29内の気層部56付近まで案内することで上昇流をつくり、気泡を気層部56に巻き上げることによって、小さなタンク内でも効率よく気泡を分離できる。   That is, in order to separate undissolved bubbles, a slope portion inclined in a rising inclination from the middle portion of the gas-liquid separation plate 28 corresponding to the substantially central level of the tank body 12 toward the side opposite to the dissolution tank portion 27. Efficient even in a small tank by providing 28s and creating an upward flow by guiding the gas-liquid mixed fluid to the vicinity of the gas layer part 56 in the opening 29 by this inclined surface part 28s and winding up the bubbles to the gas layer part 56 Air bubbles can be separated well.

一方、気液分離板28の先端を回り込むようにして下降した液は、液流制御板33に衝突して、微細な気泡も振り払うように蛇行しながら、液流制御板33の通液穴34を通って液取出口31より外部の気体溶解液を利用する施設、例えば浴槽などに供給され、浴槽内などでマイクロバブルなどの微細気泡を発生させる。   On the other hand, the liquid descending so as to go around the tip of the gas-liquid separation plate 28 collides with the liquid flow control plate 33, meandering so as to shake off fine bubbles, and the liquid flow hole 34 of the liquid flow control plate 33. Through the liquid outlet 31, it is supplied to a facility that uses an external gas solution, such as a bathtub, and generates fine bubbles such as microbubbles in the bathtub.

このように、水平方向を長手方向とする横置き筒形のタンク本体12内に溶解槽部27および気液分離板28が設けられたので、コンパクトで気体溶解効率および気液分離効率の良い溶解分離タンク11を提供できる。   As described above, since the dissolution tank 27 and the gas-liquid separation plate 28 are provided in the horizontal cylindrical tank body 12 with the horizontal direction as the longitudinal direction, it is compact and dissolves with good gas dissolution efficiency and gas-liquid separation efficiency. A separation tank 11 can be provided.

すなわち、加圧供給された気液混合流体Aを気液混合流体圧入口部21からタンク本体12の長手方向一側部内に導入する際に、タンク本体12の長手方向一側部内から長手方向他側部内にわたって形成される気層部56を巻き込むようにして気液混合流体をタンク本体12内の液中に噴射させるので、高い気体溶解効率が得られるとともに、液中に溶解しない気泡状態の気体は、気液分離板28に沿って上昇する液とともに上昇し、タンク本体12の長手方向他側部の下部に設けられた液取出口31に向かって下降する液から効率良く分離され、タンク本体12の上部内に形成される気層部56となって、タンク本体12の長手方向他側部の上部に設けられた気体抜き口32から外部へ排出されるので、高い気液分離効率が得られる。   That is, when the gas-liquid mixed fluid A supplied under pressure is introduced from the gas-liquid mixed fluid pressure inlet 21 into one side in the longitudinal direction of the tank body 12, the other in the longitudinal direction from the one side in the longitudinal direction of the tank body 12. Since the gas-liquid mixed fluid is injected into the liquid in the tank body 12 so as to involve the gas layer part 56 formed in the side part, high gas dissolution efficiency is obtained and gas in a bubble state that does not dissolve in the liquid Is efficiently separated from the liquid rising along with the gas rising along the gas-liquid separation plate 28 and descending toward the liquid outlet 31 provided at the lower part of the other side in the longitudinal direction of the tank body 12. Since the gas layer part 56 formed in the upper part of 12 is discharged to the outside from the gas vent 32 provided in the upper part of the other side part of the tank body 12 in the longitudinal direction, high gas-liquid separation efficiency is obtained. It is done.

特に、横置き筒形のタンク本体12の長手方向に沿って広範囲に気液混合流体圧入口部21を設けることで、タンク本体12内の長手方向の広範囲で気体と液体の衝突による接触面積を増やし、タンク全体で気体と液体とを攪拌して溶解を促すことができる。また、未溶解の気泡を分離するために気液分離板28の途中部から上記溶解槽部27とは反対側に向かって上昇傾斜状に形成された斜面部28sにより、気液混合流体を開口部29内の気層部56付近まで案内することで上昇流をつくり、気泡を気層部56に巻き上げることによって、小さなタンク内でも効率よく気泡を分離できる。   In particular, by providing the gas-liquid mixed fluid pressure inlet 21 in a wide range along the longitudinal direction of the horizontally placed cylindrical tank body 12, the contact area due to the collision of gas and liquid in the longitudinal direction in the tank body 12 is increased. Increasing and stirring the gas and liquid throughout the tank can facilitate dissolution. Further, in order to separate the undissolved bubbles, the gas-liquid mixed fluid is opened by the slope portion 28s formed in an upward slope from the middle portion of the gas-liquid separation plate 28 toward the side opposite to the dissolution tank portion 27. By creating an upward flow by guiding to the vicinity of the gas layer portion 56 in the portion 29 and winding the bubbles around the gas layer portion 56, the bubbles can be efficiently separated even in a small tank.

さらに、気液分離板28とタンク本体12の長手方向他側部の端面板15との間に水平に設けられた液流制御板33に、気液分離板28に最も接近し液取出口31から最も離れた位置に通液穴34を開口したので、気液分離板28を経て液取出口31に向かう液の流れに効率良く抵抗を与えることができ、より高い気液分離効率が得られる。   Furthermore, the liquid flow control plate 33 provided horizontally between the gas-liquid separation plate 28 and the end face plate 15 on the other side in the longitudinal direction of the tank body 12 is closest to the gas-liquid separation plate 28 and the liquid outlet 31 Since the liquid passage hole 34 is opened at the position farthest from the liquid, it is possible to efficiently provide resistance to the flow of liquid toward the liquid outlet 31 via the gas-liquid separation plate 28, and higher gas-liquid separation efficiency can be obtained. .

また、コンパクトな溶解分離タンク11に加えて、この溶解分離タンク11の下側に気液混合流体を加圧供給する渦流ポンプ42を配置したので、平面設置スペースがコンパクトな気液混合溶解装置41を提供できる。   Further, in addition to the compact dissolution / separation tank 11, the vortex pump 42 for pressurizing and supplying the gas-liquid mixed fluid is disposed below the dissolution / separation tank 11, so that the plane-installation space is compact and the gas-liquid mixture / dissolution apparatus 41 is provided. Can provide.

本発明は、溶解分離タンク11および気液混合溶解装置41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。   The present invention can be used by those who are involved in the manufacturing, sales, and industrial manufacturing of the dissolution / separation tank 11 and the gas-liquid mixing / dissolving device 41.

A 気液混合流体
G 気体
L 液
11 溶解分離タンク
12 タンク本体
15 端面板
21 気液混合流体圧入口部
27 溶解槽部
28 気液分離板
28s 斜面部
29 開口部
31 液取出口
32 気体抜き口
33 液流制御板
34 通液穴
41 気液混合溶解装置
42 渦流ポンプ
A Gas-liquid mixed fluid G Gas L Liquid
11 Dissolution separation tank
12 Tank body
15 End plate
21 Gas-liquid mixed fluid pressure inlet
27 Dissolution tank
28 Gas-liquid separator
28s Slope
29 opening
31 Liquid outlet
32 Vent
33 Liquid flow control plate
34 Fluid flow hole
41 Gas-liquid mixing and dissolving equipment
42 Eddy current pump

Claims (2)

水平方向を長手方向とする横置き筒形のタンク本体と、
上記タンク本体の長手方向一側部上に長手方向に沿って設けられ、加圧供給された気液混合流体を上記タンク本体の長手方向一側部内に導入する気液混合流体圧入口部と、
上記タンク本体の長手方向一側部内から長手方向他側部内に向かって設けられ、液中に気体を溶解させる溶解槽部と、
上記タンク本体の長手方向他側部内にタンク本体の底部から立設され、途中部から上記溶解槽部とは反対側に向かって上昇傾斜状に形成された斜面部を有し、かつ上端の上方に開口部を形成する気液分離用の気液分離板と、
上記タンク本体の長手方向他側部の下部に設けられ、上記気液分離板の上端を経て上記タンク本体の下方に分離された液を取り出す液取出口と、
上記タンク本体の長手方向他側部の上部に設けられ、上記気液分離板を経て上記タンク本体の上方に分離された気体を外部へ排出する気体抜き口とを具備し、
上記気液分離板と上記タンク本体の長手方向他側部の端面板との間には、上記液取出口の上側に位置する液流制御板が水平に設けられ、
上記液流制御板には、上記気液分離板に最も接近し上記液取出口から最も離れた位置に通液穴が開口された
ことを特徴とする溶解分離タンク。
A horizontal tank body with the horizontal direction as the longitudinal direction;
A gas-liquid mixed fluid pressure inlet portion that is provided along the longitudinal direction on one side of the tank body in the longitudinal direction and introduces the gas-liquid mixed fluid supplied under pressure into the side of the tank body in the longitudinal direction;
A tank portion that is provided from one side in the longitudinal direction of the tank body toward the other side in the longitudinal direction, and dissolves gas in the liquid;
The tank body has a slope portion that is erected from the bottom portion of the tank body in the other longitudinal direction of the tank body, and has a slope portion that is formed to rise upward from the middle portion to the side opposite to the dissolution tank portion, and above the upper end. A gas-liquid separation plate for gas-liquid separation that forms an opening in
A liquid outlet provided at the lower part of the other side in the longitudinal direction of the tank body, and for taking out the liquid separated below the tank body through the upper end of the gas-liquid separator;
Provided at the upper part of the other side in the longitudinal direction of the tank body, and a gas vent for discharging the gas separated above the tank body through the gas-liquid separation plate to the outside,
Between the gas-liquid separation plate and the end face plate on the other side in the longitudinal direction of the tank body, a liquid flow control plate located above the liquid outlet is provided horizontally,
The aforementioned liquid flow control plate, closest dissolve the separation tank you characterized in that liquid passing hole farthest from the fluid outlet is opened to the gas-liquid separation plate.
請求項1記載の溶解分離タンクと、
上記溶解分離タンクの下側に配置され、上記溶解分離タンクの上記気液混合流体圧入口部に気液混合流体を加圧供給する渦流ポンプと
を具備したことを特徴とする気液混合溶解装置。
A dissolution separation tank according to claim 1 Symbol placement,
A gas-liquid mixing and dissolving device, comprising: a vortex pump disposed under the dissolution and separation tank and supplying a gas-liquid mixed fluid under pressure to the gas-liquid mixed fluid pressure inlet of the dissolution and separation tank .
JP2011181810A 2011-08-23 2011-08-23 Dissolution separation tank and gas-liquid mixing dissolution apparatus Active JP5721587B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2011181810A JP5721587B2 (en) 2011-08-23 2011-08-23 Dissolution separation tank and gas-liquid mixing dissolution apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2011181810A JP5721587B2 (en) 2011-08-23 2011-08-23 Dissolution separation tank and gas-liquid mixing dissolution apparatus

Publications (2)

Publication Number Publication Date
JP2013043113A JP2013043113A (en) 2013-03-04
JP5721587B2 true JP5721587B2 (en) 2015-05-20

Family

ID=48007459

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2011181810A Active JP5721587B2 (en) 2011-08-23 2011-08-23 Dissolution separation tank and gas-liquid mixing dissolution apparatus

Country Status (1)

Country Link
JP (1) JP5721587B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2022038610A1 (en) * 2020-08-19 2022-02-24 Aquestia Ltd. A phase-separator and an assembly and method comprising the same

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106422426B (en) * 2016-12-05 2019-01-25 绵阳天和机械制造有限公司 Degassing device suitable for liquid circulation circuit and application method
CN108036656A (en) * 2018-01-05 2018-05-15 马鞍山钢铁股份有限公司 A kind of condensing plant for reducing condensation water dissolved oxygen
CN110013708B (en) * 2019-04-26 2024-06-07 深圳市氢蓝时代动力科技有限公司 Gas-liquid separation device
CN112897619B (en) * 2021-02-24 2024-02-20 山东友信节能科技有限公司 Geothermal water associated gas separation equipment
CN113648677A (en) * 2021-07-08 2021-11-16 暨南大学 A kind of extraction device and its method and application
CN113804013A (en) * 2021-10-15 2021-12-17 西安热工研究院有限公司 A recovery system that continuously discharges fluid into a surface condenser

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5241154Y2 (en) * 1972-06-22 1977-09-17
JPS5046564A (en) * 1973-07-30 1975-04-25
JPH0334801U (en) * 1989-08-09 1991-04-05
JP4558868B2 (en) * 1999-11-05 2010-10-06 株式会社ニクニ Gas-liquid mixing and dissolving device
JP4106196B2 (en) * 2001-03-23 2008-06-25 株式会社ニクニ Gas-liquid mixing and dissolving device

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2022038610A1 (en) * 2020-08-19 2022-02-24 Aquestia Ltd. A phase-separator and an assembly and method comprising the same

Also Published As

Publication number Publication date
JP2013043113A (en) 2013-03-04

Similar Documents

Publication Publication Date Title
JP5721587B2 (en) Dissolution separation tank and gas-liquid mixing dissolution apparatus
JP4558868B2 (en) Gas-liquid mixing and dissolving device
WO2014050521A1 (en) Gas dissolving device
JP5914802B2 (en) Gas dissolving device
JP2009119338A (en) Pressure levitation device
JP5001321B2 (en) Gas dissolving device
JP2010029754A (en) Gas dissolving apparatus
JP5887555B2 (en) Gas dissolution tank
EP2881165A1 (en) Gas-dissolving device
KR200492927Y1 (en) Degassing chamber for metering pump
JP5975385B2 (en) Gas dissolving device
KR101343346B1 (en) Wastewater treatment system
JP4872459B2 (en) Gas dissolving device
KR101290554B1 (en) Magnetic type generator for air dossolved water
JP5985270B2 (en) Gas dissolver for liquid
KR101864500B1 (en) Nano-bubble generator
KR101590029B1 (en) Gas dissolving device
JP2010227781A (en) Gas dissolving device
JP5870262B2 (en) Gas dissolution tank
JP5967567B2 (en) Gas dissolving device
CN101809226B (en) Flotation apparatus
JP5386002B2 (en) Gas dissolving device
JP4360330B2 (en) Defoaming device
JP2013233524A (en) Gas dissolving tank and gas dissolving apparatus provided therewith
TWM315603U (en) Air bubble-removing device for piping of fluid monitor

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20131127

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20140811

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20140820

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20141009

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20150318

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20150324

R150 Certificate of patent or registration of utility model

Ref document number: 5721587

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250