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JPH04346895A - Ozone dissolving equipment - Google Patents

Ozone dissolving equipment

Info

Publication number
JPH04346895A
JPH04346895A JP22250391A JP22250391A JPH04346895A JP H04346895 A JPH04346895 A JP H04346895A JP 22250391 A JP22250391 A JP 22250391A JP 22250391 A JP22250391 A JP 22250391A JP H04346895 A JPH04346895 A JP H04346895A
Authority
JP
Japan
Prior art keywords
ozone
water
water tank
stage
aeration means
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.)
Granted
Application number
JP22250391A
Other languages
Japanese (ja)
Other versions
JP2785082B2 (en
Inventor
Masateru Niimura
新村 正照
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP3222503A priority Critical patent/JP2785082B2/en
Publication of JPH04346895A publication Critical patent/JPH04346895A/en
Application granted granted Critical
Publication of JP2785082B2 publication Critical patent/JP2785082B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

PURPOSE:To obtain water dissolving ozone with high solubility at a low cost without necessitating the arrangement space and motive power by communicating and connecting the water supply pipe of water mixed with ozone with the lower end of a water tank main body, communicating and connecting a discharge pipe with the upper end thereof and providing the aeration means of gaseous ozone in multistages to the inside of the water tank main body. CONSTITUTION:When water mixed with ozone is supplied into a water tank main body 1 via a water supply pipe 11 communicated and connected with the lower end of the water tank main body 1 from a supply device 13 of the water mixed with ozone, ozone is discharged and bubbled from the water mixed with ozone and gaseous ozone 0 is gradually stored to the rear surface side of an aeration means 2 thereof provided to the lowermost stage, namely to the rear surface side of a meshy body 22. When the bubbles become size of some degrees, these are aerated therein and permeate the aeration means 2 by aerating action. Gaseous ozone 0 is dissolved into water stored in the upper stage. This aerating action is repeated by the number of the stages of the aeration means 2. The water dissolved with ozone being in a state wherein gaseous ozone 0 is almost dissolved is obtained in the uppermost stage.

Description

【発明の詳細な説明】[Detailed description of the invention]

【0001】0001

【産業上の利用分野】この発明は、オゾン溶融装置に係
り、特に、動力を用いることなく高溶融度のオゾン溶融
水を得ることができるオゾン溶融装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an ozone melting apparatus, and more particularly to an ozone melting apparatus capable of obtaining ozone melt water with a high melting degree without using power.

【0002】0002

【従来の技術】周知のように、生活水の汚れや悪臭の発
生などを防止するためにオゾン溶融水が利用されること
が多く、そのため、これまでに種々のオゾン溶融装置が
提案されている。
[Prior Art] As is well known, ozone melt water is often used to prevent pollution and bad odors from occurring in household water, and for this purpose, various ozone melting devices have been proposed. .

【0003】例えば、紫外線ランプによって出現される
オゾン雰囲気中に水をジェット噴流させ、該水にオゾン
を混合させてこれを回収する提案があり、この場合には
、比較的簡単にオゾン溶融水を入手できる利点がある。
For example, there has been a proposal to jet water into an ozone atmosphere produced by an ultraviolet lamp, mix ozone with the water, and recover it. In this case, it is relatively easy to collect ozone molten water. It has the advantage of being available.

【0004】しかしながら、上記従来の提案にあっては
、オゾンの殆どが水に混合しているのみで溶融されてお
らず、従って、生成されたオゾン溶融水から簡単にオゾ
ンが放出される不都合がある。
However, in the above-mentioned conventional proposal, most of the ozone is only mixed with water and not melted, and therefore, ozone is easily released from the ozone melt water produced. be.

【0005】そこで、従来では、大型の撹拌羽根を備え
たは装置でオゾン溶融水を得るか、或は、一旦生成され
たオゾン溶融水を再度ジェット噴流で混合する等の手段
が採用されているのが現状である。
[0005] Conventionally, therefore, methods have been adopted such as obtaining ozone molten water using a device equipped with a large stirring blade, or mixing ozone molten water once produced again with a jet stream. is the current situation.

【0006】[0006]

【発明が解決しようとする課題】しかしながら、上記従
来の提案にあっては、いずれの手段によっても、装置を
稼動させるためには大動力を必要とし、その結果、設置
スペースを広くしなければならない他、ランニングコス
トが嵩みコスト高となる、という問題を有していた。
[Problem to be Solved by the Invention] However, in any of the above conventional proposals, a large amount of power is required to operate the device, and as a result, the installation space must be expanded. Another problem was that the running costs were bulky, resulting in high costs.

【0007】また、一般に、動力を用いることなくオゾ
ンを水に溶融させることができる割合は10%程度とさ
れており、溶融率が15%以上あれば画期的である、と
言われているのも現状である。
[0007] Additionally, it is generally said that the rate at which ozone can be melted into water without using power is about 10%, and it is said that a melting rate of 15% or more is revolutionary. This is also the current situation.

【0008】この発明は、かかる現状に鑑み創案された
ものであって、その目的とするところは、設置スペース
をとらず、しかも、動力を必要とすることなく15%以
上の高溶融度のオゾン溶融水を廉価に得ることができる
オゾン溶融装置を提供しようとするものである。
The present invention was devised in view of the current situation, and its purpose is to provide ozone with a high melting rate of 15% or more without taking up much installation space and without requiring power. The object of the present invention is to provide an ozone melting device that can obtain melt water at a low cost.

【0009】[0009]

【課題を解決するための手段】上記目的を達成するため
に、この発明にかかるオゾン溶融装置にあっては、下端
にオゾン混合水の給水管が連通接続され、かつ、上端に
排出管が連通接続されてなる水槽本体内に、オゾンガス
曝気手段を多段に配設したことを特徴とするものである
[Means for Solving the Problems] In order to achieve the above object, in the ozone melting device according to the present invention, an ozone mixed water supply pipe is connected to the lower end, and a discharge pipe is connected to the upper end. This system is characterized in that ozone gas aeration means are arranged in multiple stages within the connected aquarium bodies.

【0010】0010

【作用】それ故、この発明に係るオゾン溶融装置にあっ
ては、外部からのオゾン混合水が水槽本体の下端に連通
接続された給水管を介して水槽本体内に供給されると、
該水槽本体の最下段に配設されたオゾンガス曝気手段の
下面側にオゾン混合水から放出されるオゾンガスの気泡
が一時的に貯留される。
[Operation] Therefore, in the ozone melting apparatus according to the present invention, when ozone-mixed water from the outside is supplied into the water tank main body through the water supply pipe connected to the lower end of the water tank main body,
Bubbles of ozone gas released from the ozone-mixed water are temporarily stored on the lower surface side of the ozone gas aeration means disposed at the lowest stage of the water tank body.

【0011】そして、該気泡の貯溜状態が継続されると
、オゾンガス曝気手段の下面側に徐々に貯留されたオゾ
ンガスが曝気し、該曝気作用でオゾンガスがオゾンガス
曝気手段を透過して上段に貯溜されている水と溶融する
。そして、かかる曝気作用が水槽本体の最上段に至まで
の間に複数回繰り返されることによって、オゾンガスが
徐々に水に溶蝕し、最終的にオゾンガスの殆どが溶融さ
れた状態のオゾン溶融水が得られる。
[0011] When the bubbles continue to be stored, the ozone gas stored on the lower side of the ozone gas aeration means is gradually aerated, and due to the aeration, the ozone gas passes through the ozone gas aeration means and is stored in the upper stage. It melts with water. By repeating this aeration several times until reaching the top of the tank body, the ozone gas gradually erodes into the water, and finally ozone molten water in which most of the ozone gas has been melted is obtained. It will be done.

【0012】0012

【実施例】以下、添付図面に示す実施例に基き、この発
明を詳細に説明する。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described in detail below based on embodiments shown in the accompanying drawings.

【0013】図1に示すように、この実施例に係るオゾ
ン溶融装置は、水槽本体1と、該水槽本体1内に多段に
配設されたオゾンガス曝気手段2と、を有してなる。
As shown in FIG. 1, the ozone melting apparatus according to this embodiment includes a water tank body 1 and ozone gas aeration means 2 arranged in multiple stages within the water tank body 1.

【0014】水槽本体1は、耐圧及び耐水構造に形成さ
れて地上E等に立設されるもので、下端に給水管11が
連通接続され、上端に排出管12が連通接続されている
The water tank main body 1 is formed to have a pressure-resistant and water-resistant structure and is installed upright on the ground E, etc., and has a water supply pipe 11 connected to the lower end and a discharge pipe 12 connected to the upper end.

【0015】給水管11は、ブラケット11aを介して
水槽本体1の下端に連通接続されており、外部に設置さ
れたオゾン混合水供給装置13からオゾン混合水を水槽
本体1の最下段に給水する。尚、給水管11の先端開口
は、図2中に仮想線で示すように、水槽本体1の中央部
まで延長し、開口が上方を向くように設定することもで
きる。
The water supply pipe 11 is connected to the lower end of the aquarium body 1 via a bracket 11a, and supplies ozone-mixed water to the lowest stage of the aquarium body 1 from an externally installed ozone-mixed water supply device 13. . Note that the opening at the tip of the water supply pipe 11 can be set to extend to the center of the water tank body 1 and face upward, as shown by the imaginary line in FIG. 2.

【0016】一方、排出管12は、ブラケット12aを
介して水槽本体1の上端に連通接続されており、水槽本
体1内で生成されたオゾン溶融水を水槽本体1の外部に
排出する。
On the other hand, the discharge pipe 12 is connected to the upper end of the aquarium body 1 via a bracket 12a, and discharges ozone melt water generated within the aquarium body 1 to the outside of the aquarium body 1.

【0017】オゾンガス曝気手段2は、水槽本体1の内
周壁1aの縦方向に沿って、例えば、10段程度水平に
配設されるもので、図2に示すように、これらは夫々、
上記内周壁1aに取り付けられる上下一対の枠状ブラケ
ット21,21と、該枠状ブラケット21,21に保持
されるメッシュ体22と、から構成されている。
The ozone gas aeration means 2 are arranged horizontally in, for example, about 10 stages along the vertical direction of the inner circumferential wall 1a of the water tank body 1, and as shown in FIG.
It is composed of a pair of upper and lower frame-shaped brackets 21, 21 attached to the inner circumferential wall 1a, and a mesh body 22 held by the frame-shaped brackets 21, 21.

【0018】枠状ブラケット21は、アングル状に形成
されており、一方のフランジ部21aが水槽本体1の内
周壁1aに固定され、他方のフランジ部21bにはメッ
シュ体22が挾持され、オゾン水の水流を横切るように
状態に展張されて配設されている。勿論、フランジ部2
1aと水槽本体1の内周壁1aとの間に適宜のシール部
材を介装してもよい。
The frame-shaped bracket 21 is formed into an angle shape, one flange portion 21a is fixed to the inner circumferential wall 1a of the aquarium main body 1, and the other flange portion 21b has a mesh body 22 held between them, and the ozone water is It is spread out and arranged so as to cross the water flow. Of course, flange part 2
An appropriate sealing member may be interposed between 1a and the inner circumferential wall 1a of the water tank body 1.

【0019】そして、該メッシュ体22は、即ち、その
網目の大きさが、気泡となったオゾンOが通過しない大
きさに形成されている。
The mesh body 22 is formed to have a mesh size that does not allow ozone O in the form of bubbles to pass through.

【0020】次に、以上のように構成されてなるオゾン
溶融装置によって高溶融度のオゾン溶融水を生成する場
合について説明する。
Next, a case will be described in which ozone melt water having a high melting degree is produced by the ozone melting apparatus constructed as described above.

【0021】先ず、オゾン混合水供給装置13からオゾ
ン混合水が、水槽本体1の下端に連通接続された給水管
11を介して水槽本体1内に供給されると、図3に示す
ように、水槽本体1の最下段に配設されたオゾンガス曝
気手段2の下面側、即ち、メッシュ体22の下面側にオ
ゾン混合水から放出される気泡化されたオゾンガスOが
徐々に貯留される。
First, when ozone mixed water is supplied from the ozone mixed water supply device 13 into the aquarium main body 1 through the water supply pipe 11 connected to the lower end of the aquarium main body 1, as shown in FIG. Bubbled ozone gas O released from the ozone mixed water is gradually stored on the lower surface side of the ozone gas aeration means 2 disposed at the lowest stage of the water tank body 1, that is, on the lower surface side of the mesh body 22.

【0022】そして、このオゾンガスOがメッシュ体2
2の下面側に貯留され、気泡ガスがある程度の大きさに
なると、オゾンガスOがそこで曝気(図3中に破線で示
す)し、該曝気作用によって上記オゾンガス曝気手段2
を透過し、オゾンガスOが上段に貯溜されている水に溶
融する。
[0022] Then, this ozone gas O
2, and when the bubble gas reaches a certain size, ozone gas O is aerated there (indicated by the broken line in FIG. 3), and due to the aeration action, the ozone gas aeration means 2
The ozone gas O melts into the water stored in the upper stage.

【0023】かかる曝気作用は、オゾンガス曝気手段2
が設けられた段数の数だけ繰り返して行なわれ、最上段
では、オゾンガスOの殆どが溶融された状態のオゾン溶
融水が得られる。そして、このようにして生成されたオ
ゾン溶融水は排出管12から水槽本体1の外部へと排出
される。
[0023] Such aeration effect is achieved by the ozone gas aeration means 2.
This is repeated as many times as the number of stages provided, and at the top stage, ozone molten water in which most of the ozone gas O is melted is obtained. The ozone melt water thus generated is discharged from the discharge pipe 12 to the outside of the water tank body 1.

【0024】因に、上記実施例に係るオゾン溶融装置の
1段目におけるオゾン溶融率を10%とした場合には、
実験では、2段目のオゾン溶融率が9%、3段目のオゾ
ン溶融率が8.1%、4段目のオゾン溶融率が7.29
%、5段目のオゾン溶融率が6.561%、6段目のオ
ゾン溶融率が5.9047%、7段目のオゾン溶融率が
5.3144%、8段目のオゾン溶融率が4.7829
%、9段目のオゾン溶融率が4.3046%、10段目
のオゾン溶融率が3.8742%となり、合計では、6
5.132%のオゾン溶融率が得られた。
Incidentally, when the ozone melting rate in the first stage of the ozone melting apparatus according to the above embodiment is 10%,
In the experiment, the ozone melting rate in the second stage was 9%, the ozone melting rate in the third stage was 8.1%, and the ozone melting rate in the fourth stage was 7.29.
%, the ozone melting rate of the 5th stage is 6.561%, the ozone melting rate of the 6th stage is 5.9047%, the ozone melting rate of the 7th stage is 5.3144%, the ozone melting rate of the 8th stage is 4 .7829
%, the ozone melting rate at the 9th stage was 4.3046%, the ozone melting rate at the 10th stage was 3.8742%, and the total was 6.
An ozone melting rate of 5.132% was obtained.

【0025】また、上記実施例に係るオゾン溶融装置の
1段目におけるオゾン溶融率を15%とした場合には、
実験では、2段目のオゾン溶融率が12.75%、3段
目のオゾン溶融率が10.8375%、4段目のオゾン
溶融率が9.2118%、5段目のオゾン溶融率が7.
7869%、6段目のオゾン溶融率が6.6189%、
7段目のオゾン溶融率が5.6260%、8段目のオゾ
ン溶融率が4.7821%、9段目のオゾン溶融率が4
.0643%、10段目のオゾン溶融率が3.4550
%となり、合計では、80.1325%のオゾン溶融率
が得られた。
Further, when the ozone melting rate in the first stage of the ozone melting apparatus according to the above embodiment is 15%,
In the experiment, the ozone melting rate in the second stage was 12.75%, the ozone melting rate in the third stage was 10.8375%, the ozone melting rate in the fourth stage was 9.2118%, and the ozone melting rate in the fifth stage was 7.
7869%, 6th stage ozone melting rate is 6.6189%,
The ozone melting rate in the 7th stage is 5.6260%, the ozone melting rate in the 8th stage is 4.7821%, and the ozone melting rate in the 9th stage is 4.
.. 0643%, 10th stage ozone melting rate is 3.4550
%, and in total, an ozone melting rate of 80.1325% was obtained.

【0026】それ故、この実施例に係るオゾン溶融装置
にあっては、オゾン混合水を水槽本体1内に供給すると
きの水道圧以外は、動力を全く必要としないので、ラン
ニングコストを大幅に低減することができると共に、装
置自体も小型化することができ、その結果、設置スペー
スが狭くてすみ、総じて低コストで15%以上の高溶融
度のオゾン溶融水を得ることができる。
Therefore, the ozone melting apparatus according to this embodiment does not require any power other than the water pressure for supplying ozone-mixed water into the water tank body 1, so running costs can be significantly reduced. In addition, the device itself can be made smaller, and as a result, only a small installation space is required, and ozone molten water with a high melting degree of 15% or more can be obtained at a generally low cost.

【0027】尚、オゾンガスの溶融度をより高める場合
には、例えば、図4に示すように、前記構成からなる水
槽本体1を多数本が並設し、隣接する一方の水槽本体1
の排出管12の終端を他の水槽本体1の下端に連通接続
することで、曝気作用を連続して複数回行なうことがで
きるので、より超高溶融度のオゾン溶融水を簡単に得る
ことができる。
In order to further increase the degree of melting of ozone gas, for example, as shown in FIG.
By connecting the end of the discharge pipe 12 to the lower end of the other water tank main body 1, the aeration action can be performed several times in succession, so it is possible to easily obtain ozone melt water with an ultra-high melting degree. can.

【0028】[0028]

【発明の効果】この発明によれば、以上説明したように
、オゾン混合水を給水管を介して水槽本体内に給水する
ように構成したので、設置スペースをとらず、しかも、
動力を必要とすることなく高溶融度で低コストのオゾン
溶融水を得ることができる、という優れた効果を奏する
[Effects of the Invention] According to the present invention, as explained above, the ozone mixed water is supplied into the aquarium body through the water supply pipe, so it does not take up much installation space.
It has the excellent effect of being able to obtain low-cost ozone melt water with a high melting degree without requiring power.

【図面の簡単な説明】[Brief explanation of the drawing]

【図1】この発明の一実施例に係るオゾン溶融装置の全
体を一部破断して示す縦断面図である。
FIG. 1 is a longitudinal sectional view, partially cut away, showing the entirety of an ozone melting apparatus according to an embodiment of the present invention.

【図2】オゾン溶融装置の下端部分を拡大して示す部分
縦断面図である。
FIG. 2 is a partial vertical sectional view showing an enlarged lower end portion of the ozone melting device.

【図3】オゾン曝気手段の作動状態を拡大して示す部分
縦断面図である。
FIG. 3 is a partial vertical sectional view showing an enlarged operating state of the ozone aeration means.

【図4】オゾン溶融装置の他の構成例を示す縦断面図で
ある。
FIG. 4 is a longitudinal sectional view showing another example of the configuration of the ozone melting device.

【符号の説明】[Explanation of symbols]

1  水槽本体 2  オゾン曝気手段 11  給水管 12  排出管 21  枠状ブラケット 22  メッシュ体 1 Aquarium body 2 Ozone aeration means 11 Water supply pipe 12 Discharge pipe 21 Frame bracket 22 Mesh body

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】  下端にオゾン混合水の給水管が連通接
続され、かつ、上端に排出管が連通接続されてなる水槽
本体内に、オゾンガス曝気手段を多段に配設したことを
特徴とするオゾン溶融装置。
[Claim 1] Ozone gas aeration means are arranged in multiple stages in a water tank body having a water tank body connected to a water supply pipe for ozone mixed water at the lower end and a discharge pipe at the upper end. Melting equipment.
【請求項2】  前記オゾンガス曝気手段は、水槽本体
の内周壁に水平に取り付けられる枠状ブラケットと、該
枠状ブラケットに周縁が保持されて水流を横切るように
展張されるメッシュ体と、から構成されていることを特
徴とする請求項1に記載のオゾン溶融装置。
2. The ozone gas aeration means is composed of a frame-shaped bracket horizontally attached to the inner circumferential wall of the aquarium body, and a mesh body whose periphery is held by the frame-shaped bracket and stretched across the water flow. The ozone melting apparatus according to claim 1, characterized in that:
【請求項3】  前記水槽本体は、多数本が地上等に並
設され、隣接する水槽本体の排出管の終端が他の水槽本
体の下端に連通接続されていることを特徴とする請求項
1に記載のオゾン溶融装置。
3. A large number of the water tank bodies are arranged in parallel on the ground or the like, and the terminal ends of the discharge pipes of adjacent water tank bodies are connected in communication with the lower ends of other water tank bodies. The ozone melting device described in .
JP3222503A 1991-05-24 1991-05-24 Ozone melting method and its device Expired - Lifetime JP2785082B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3222503A JP2785082B2 (en) 1991-05-24 1991-05-24 Ozone melting method and its device

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5971368A (en) * 1997-10-29 1999-10-26 Fsi International, Inc. System to increase the quantity of dissolved gas in a liquid and to maintain the increased quantity of dissolved gas in the liquid until utilized
US6235641B1 (en) 1998-10-30 2001-05-22 Fsi International Inc. Method and system to control the concentration of dissolved gas in a liquid
US6274506B1 (en) 1999-05-14 2001-08-14 Fsi International, Inc. Apparatus and method for dispensing processing fluid toward a substrate surface
US6406551B1 (en) 1999-05-14 2002-06-18 Fsi International, Inc. Method for treating a substrate with heat sensitive agents
WO2022158540A1 (en) * 2021-01-22 2022-07-28 学校法人工学院大学 Gas/liquid mixing device

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101549935B1 (en) * 2015-02-27 2015-09-03 (주)그린아이엔지 Washing device having ozonizer

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Publication number Priority date Publication date Assignee Title
JPS5343571U (en) * 1976-09-18 1978-04-14
JPH0242970A (en) * 1988-08-03 1990-02-13 Jgc Corp Bubble tower provided with draft tube

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5343571U (en) * 1976-09-18 1978-04-14
JPH0242970A (en) * 1988-08-03 1990-02-13 Jgc Corp Bubble tower provided with draft tube

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5971368A (en) * 1997-10-29 1999-10-26 Fsi International, Inc. System to increase the quantity of dissolved gas in a liquid and to maintain the increased quantity of dissolved gas in the liquid until utilized
US6488271B1 (en) * 1997-10-29 2002-12-03 Fsi International, Inc. Method to increase the quantity of dissolved gas in a liquid and to maintain the increased quantity of dissolved gas in the liquid until utilized
US6648307B2 (en) 1997-10-29 2003-11-18 Fsi International, Inc. Method to increase the quantity of dissolved gas in a liquid and to maintain the increased quantity of dissolved gas in the liquid until utilized
US6235641B1 (en) 1998-10-30 2001-05-22 Fsi International Inc. Method and system to control the concentration of dissolved gas in a liquid
US6274506B1 (en) 1999-05-14 2001-08-14 Fsi International, Inc. Apparatus and method for dispensing processing fluid toward a substrate surface
US6406551B1 (en) 1999-05-14 2002-06-18 Fsi International, Inc. Method for treating a substrate with heat sensitive agents
WO2022158540A1 (en) * 2021-01-22 2022-07-28 学校法人工学院大学 Gas/liquid mixing device

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