JP2785082B2 - Ozone melting method and its device - Google Patents
Ozone melting method and its deviceInfo
- Publication number
- JP2785082B2 JP2785082B2 JP3222503A JP22250391A JP2785082B2 JP 2785082 B2 JP2785082 B2 JP 2785082B2 JP 3222503 A JP3222503 A JP 3222503A JP 22250391 A JP22250391 A JP 22250391A JP 2785082 B2 JP2785082 B2 JP 2785082B2
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- JP
- Japan
- Prior art keywords
- ozone
- water
- stage
- melting
- bubbles
- 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.)
- Expired - Lifetime
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- Treatment Of Water By Oxidation Or Reduction (AREA)
Description
【0001】[0001]
【産業上の利用分野】この発明は、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
融方法およびその装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an ozone melting method and an apparatus for obtaining ozone melt water having a high degree of melting 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。2. Description of the Related Art As is well known, ozone-melted water is often used to prevent contamination of living water and the generation of offensive odors. For this reason, 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。[0003] For example, there is a proposal to jet water into an ozone atmosphere generated by an ultraviolet lamp, mix ozone with the water, and recover the ozone. There are advantages 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 mixed only with water and is not melted. Therefore, there is a disadvantage that ozone is easily released from the generated ozone molten water. is there.
【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。Therefore, conventionally, means for obtaining molten ozone by means of a device equipped with large stirring blades, or means for mixing once generated ozone molten water again with a jet jet have been adopted. 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。However, in the above-mentioned conventional proposals, large power is required to operate the apparatus by any means, and as a result, the installation space must be widened. In addition, there was a problem that the running cost increased and the cost increased.
【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] Further, generally, the rate at which ozone can be dissolved in water without using power is about 10%, and it is said that if the melting rate is 15% or more, breakthrough is achieved. 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、動力を特に必
要とすることなく15%以上の高溶融度のオゾン溶融水
を簡便な設備で廉価に得ることができるオゾン溶融方法
およびその装置を提供しようとするものである。The present invention has been made in view of the above situation, and an object of the present invention is to provide a simple facility for dissolving ozone-melted water having a high melting degree of 15% or more without particularly requiring power. An object of the present invention is to provide an ozone melting method and an apparatus which can be obtained at 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、この発明に係るオゾン溶融方法は、内部に多段のメ
ッシュ体を配設してなる水槽本体の下方からオゾン混合
水を供給し、下段で水と混合しなかったオゾン気泡を、
該段目の上部に配設されたメッシュ体の下方で溜めて徐
々に大きな気泡に成長させた後、一定の大きさまで成長
した気泡を曝気させてオゾンを上段へと圧送すること
で、該上段のオゾン水に曝気したオゾンを溶融させる工
程を多段階繰り返すように構成したことを特徴とするも
のである。また、この発明にあっては、上記方法を実現
させるため、オゾン溶融装置を、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と、該水槽本体内に多段に展設され
たメッシュ体と、から構成し、下段で水と混合しなかっ
たオゾン気泡を、該段目の上部に配設されたメッシュ体
の下方で溜めて徐々に大きな気泡に成長させて一定の大
きさまで成長させた気泡を、該段のメッシュ体下方で曝
気させてオゾンを上段へと圧送することで、該上段のオ
ゾン水に曝気したオゾンを溶融させ、これを多段階繰り
返すように構成したことを特徴とするものである。In order to achieve the above object, an ozone melting method according to the present invention comprises: supplying ozone mixed water from below a water tank body having a multi-stage mesh body disposed therein; Ozone bubbles not mixed with water in
After accumulating under the mesh body arranged at the upper part of the stage and gradually growing it into large bubbles, the bubbles grown to a certain size are aerated, and ozone is pumped to the upper stage to thereby feed the upper stage. The step of melting the ozone aerated in the ozone water is repeated in multiple stages. Further, in the present invention, in order to realize the above method, an ozone melting device, a water tank main body having a lower end connected to an ozone mixed water supply pipe, and an upper end connected to a discharge pipe, And a mesh body extended in multiple stages in the water tank main body, and ozone bubbles not mixed with water in the lower stage are gradually collected under the mesh body arranged at the upper part of the stage. The bubbles grown to a certain size by growing into large bubbles are aerated under the mesh body of the stage and ozone is pumped to the upper stage to melt the ozone aerated in the ozone water of the upper stage. Is repeated in multiple stages.
【0010】それ故、この発明にあっては、外部からオ
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
に配設されたメッシュ体の下方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。Therefore, according to the present invention, when the ozone-mixed water is supplied from the outside into the water tank main body through a water supply pipe connected to the lower end of the water tank main body, the ozone-mixed water is disposed at the lowest stage of the water tank main body. Ozone gas bubbles released from the ozone mixed water are temporarily stored below the provided mesh 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。When the stored state of the air bubbles is continued, the ozone gas gradually stored on the lower surface side of the ozone gas aerator is aerated, and the ozone gas is transmitted through the ozone gas aerator and stored in the upper stage by the aeration. Melts with water. The aeration is repeated a plurality of times before reaching the top of the water tank body, whereby the ozone gas is gradually eroded into the water, and finally, ozone molten water in which most of the ozone gas is melted is obtained. Can be
【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。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described below in detail 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 has a water tank body 1 and ozone gas aeration means 2 provided in the water tank body 1 in multiple stages.
【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 erected on the ground E or the like. A water supply pipe 11 is connected to a lower end thereof, and a discharge pipe 12 is connected to an upper end thereof.
【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 water tank main body 1 via a bracket 11a, and supplies ozone mixed water to the lowermost stage of the water tank main body 1 from an ozone mixed water supply device 13 installed outside. . In addition, the opening of the distal end of the water supply pipe 11 may be extended to the center of the water tank main body 1 as shown by a virtual line in FIG. 2 so that the opening faces upward.
【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 water tank main body 1 through a bracket 12a, and discharges the ozone molten water generated in the water tank main body 1 to the outside of the water tank main 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 is arranged horizontally, for example, about 10 steps along the longitudinal direction of the inner peripheral wall 1a of the water tank main body 1. As shown in FIG.
It comprises a pair of upper and lower frame-shaped brackets 21 and 21 attached to the inner peripheral wall 1a, and a mesh body 22 held by the frame-shaped brackets 21 and 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 in an angle shape. One of the flange portions 21a is fixed to the inner peripheral wall 1a of the water tank main body 1, and the other flange portion 21b has a mesh body 22 sandwiched therebetween. It is arranged in a state of being stretched across the water flow. Of course, the flange part 2
An appropriate sealing member may be interposed between the inner peripheral wall 1a of the tank body 1 and the inner peripheral wall 1a.
【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 so that the size of its mesh does not allow the ozone O which has become 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 description will be given of a case where ozone molten water having a high degree of melting is generated by the ozone melting apparatus having the above-described structure.
【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 water tank main body 1 through the water supply pipe 11 connected to the lower end of the water tank main body 1, as shown in FIG. On the lower surface side of the ozone gas aeration means 2 arranged at the lowermost stage of the water tank main body 1, that is, on the lower surface side of the mesh body 22, the ozone gas O bubbled from the ozone mixed water is gradually stored.
【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。The ozone gas O is supplied to the mesh 2
When the bubble gas reaches a certain size and is stored on the lower surface side of the ozone gas 2, the ozone gas O is aerated there (indicated by a broken line in FIG. 3), and the ozone gas aeration means 2
And the ozone gas O is dissolved in 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。The aeration is performed by the ozone gas aerator 2
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. Then, the ozone melt water thus generated is discharged from the discharge pipe 12 to the outside of the water tank main 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。When the ozone melting rate in the first stage of the ozone melting apparatus according to the above embodiment is set to 10%,
In the experiment, the second-stage ozone melting rate was 9%, the third-stage ozone melting rate was 8.1%, and the fourth-stage ozone melting rate was 7.29.
%, The ozone melting rate of the fifth stage is 6.561%, the ozone melting ratio of the sixth stage is 5.9047%, the ozone melting ratio of the seventh stage is 5.3144%, and the ozone melting ratio of the eighth stage is 4 .7829
%, The ozone melting rate at the ninth stage was 4.3046%, and the ozone melting ratio at the tenth stage was 3.8742%.
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3.455
0%となり、合計では、80.1325%のオゾン溶融
率が得られた。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 second stage ozone melting rate was 12.75%, the third stage ozone melting ratio was 10.8375%, the fourth stage ozone melting ratio was 9.2118%, and the fifth stage ozone melting ratio was 7.
7869%, the sixth stage ozone melting rate is 6.6189%,
The seventh stage has an ozone melting ratio of 5.6260%, the eighth stage has an ozone melting ratio of 4.7821%, the ninth stage has an ozone melting ratio of 4.0643%, and the tenth stage has an ozone melting ratio of 3.455.
The ozone melting rate was 80.1325% in total.
【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, in the ozone melting apparatus according to this embodiment, no power is required except for the tap water pressure when the ozone mixed water is supplied into the water tank main body 1, so that the running cost is greatly reduced. In addition to the reduction, the size of the apparatus itself can be reduced. As a result, the installation space can be reduced, and ozone molten water having a high melting degree of 15% or more can be obtained at low cost as a whole.
【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 the 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 continuously performed a plurality of times, so that it is possible to easily obtain ozone molten water having a higher degree of melting. it 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。According to the present invention, as described above, the ozone-mixed water is supplied into the water tank body via the water supply pipe, so that no installation space is required and power is required. This provides an excellent effect that a low-cost ozone molten water with a high degree of melting can be obtained without performing.
【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 showing the entire ozone melting apparatus according to one embodiment of the present invention, partially cut away.
【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 an enlarged partial longitudinal sectional view showing a 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 an enlarged partial longitudinal sectional view showing an operation state of an ozone aerator.
【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 configuration example of the ozone melting device.
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 DESCRIPTION OF SYMBOLS 1 Water tank main body 2 Ozone aeration means 11 Water supply pipe 12 Drain pipe 21 Frame bracket 22 Mesh body
Claims (2)
水槽本体の下方からオゾン混合水を供給し、下段で水と
混合しなかったオゾン気泡を、該段目の上部に配設され
たメッシュ体の下方で溜めて徐々に大きな気泡に成長さ
せた後、一定の大きさまで成長した気泡を曝気させてオ
ゾンを上段へと圧送することで、該上段のオゾン水に曝
気したオゾンを溶融させる工程を多段階繰り返すことを
特徴とするオゾン溶融方法。1. A multi-stage mesh body is provided inside.
Ozone mixed water is supplied from below the water tank body, and water is
The unmixed ozone bubbles are placed above the stage.
Accumulated under the mesh body, and gradually grows into large bubbles.
Air bubbles that have grown to a certain size and aerated.
By pumping the zon to the upper stage, it is exposed to the ozone water in the upper stage.
To repeat the process of melting the ozone
A characteristic ozone melting method .
され、かつ、上端に排出管が連通接続されてなる水槽本
体と、該水槽本体内に多段に展設されたメッシュ体と、
から構成し、下段で水と混合しなかったオゾン気泡を、
該段目の上部に配設されたメッシュ体の下方で溜めて徐
々に大きな気泡に成長させて一定の大きさまで成長させ
た気泡を、該段のメッシュ体下方で曝気させてオゾンを
上段へと圧送することで、該上段のオゾン水に曝気した
オゾンを溶融させ、これを多段階繰り返すように構成し
たことを特徴とするオゾン溶融装置。2. An ozone mixed water supply pipe is connected to a lower end thereof.
Tank with a discharge pipe connected to the upper end
A body, and a mesh body extended in multiple stages in the aquarium body;
And ozone bubbles not mixed with water in the lower stage,
It is collected below the mesh body arranged at the top of the step and gradually
Grow into large bubbles and grow to a certain size
The air bubbles are aerated under the mesh body of the step to remove ozone.
By pumping to the upper stage, the ozone water in the upper stage was aerated.
Ozone is melted, and this is configured to be repeated in multiple stages.
An ozone melting apparatus , characterized in that:
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 |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3222503A JP2785082B2 (en) | 1991-05-24 | 1991-05-24 | Ozone melting method and its device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH04346895A JPH04346895A (en) | 1992-12-02 |
| JP2785082B2 true JP2785082B2 (en) | 1998-08-13 |
Family
ID=16783451
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP3222503A Expired - Lifetime JP2785082B2 (en) | 1991-05-24 | 1991-05-24 | Ozone melting method and its device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2785082B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101549935B1 (en) * | 2015-02-27 | 2015-09-03 | (주)그린아이엔지 | Washing device having ozonizer |
Families Citing this family (5)
| 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 |
| US6406551B1 (en) | 1999-05-14 | 2002-06-18 | Fsi International, Inc. | Method for treating a substrate with heat sensitive agents |
| US6274506B1 (en) | 1999-05-14 | 2001-08-14 | Fsi International, Inc. | Apparatus and method for dispensing processing fluid toward a substrate surface |
| JP7677652B2 (en) * | 2021-01-22 | 2025-05-15 | 学校法人 工学院大学 | Gas-liquid mixing device |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5613001Y2 (en) * | 1976-09-18 | 1981-03-26 | ||
| JPH0716394B2 (en) * | 1988-08-03 | 1995-03-01 | 日揮株式会社 | Bubble tower with draft tube |
-
1991
- 1991-05-24 JP JP3222503A patent/JP2785082B2/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101549935B1 (en) * | 2015-02-27 | 2015-09-03 | (주)그린아이엔지 | Washing device having ozonizer |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH04346895A (en) | 1992-12-02 |
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