JPH02119991A - Device for producing ozone water - Google Patents
Device for producing ozone waterInfo
- Publication number
- JPH02119991A JPH02119991A JP27095588A JP27095588A JPH02119991A JP H02119991 A JPH02119991 A JP H02119991A JP 27095588 A JP27095588 A JP 27095588A JP 27095588 A JP27095588 A JP 27095588A JP H02119991 A JPH02119991 A JP H02119991A
- Authority
- JP
- Japan
- Prior art keywords
- gas
- water
- ozone
- ejector
- stage pump
- 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.)
- Pending
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 59
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 title claims abstract description 51
- 239000000203 mixture Substances 0.000 claims abstract description 12
- 239000007788 liquid Substances 0.000 claims description 33
- 239000007789 gas Substances 0.000 claims description 28
- 238000000926 separation method Methods 0.000 claims description 13
- 238000004519 manufacturing process Methods 0.000 claims description 12
- 238000004090 dissolution Methods 0.000 claims description 7
- 238000005406 washing Methods 0.000 claims description 5
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 claims description 3
- 229910001882 dioxygen Inorganic materials 0.000 claims description 3
- 239000008399 tap water Substances 0.000 claims description 3
- 235000020679 tap water Nutrition 0.000 claims description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 2
- 239000001301 oxygen Substances 0.000 claims description 2
- 229910052760 oxygen Inorganic materials 0.000 claims description 2
- 238000011144 upstream manufacturing Methods 0.000 claims 2
- 230000002035 prolonged effect Effects 0.000 abstract 1
- 238000004140 cleaning Methods 0.000 description 6
- 238000000034 method Methods 0.000 description 5
- 238000000354 decomposition reaction Methods 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- 230000001954 sterilising effect Effects 0.000 description 4
- 238000004659 sterilization and disinfection Methods 0.000 description 4
- 238000013019 agitation Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 229920001131 Pulp (paper) Polymers 0.000 description 1
- 230000005587 bubbling Effects 0.000 description 1
- 238000004042 decolorization Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000004332 deodorization Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000010800 human waste Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 239000004065 semiconductor Substances 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
Landscapes
- Treatment Of Water By Oxidation Or Reduction (AREA)
- Oxygen, Ozone, And Oxides In General (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、オシ／水製造装置に関するもので、詳しくは
、原材料や加工品などの食品、上下水道、し尿処理、医
療機器１紙パルプ、半導体の各分野における殺菌、除菌
、脱色、脱臭の手段として有効であるオゾン水を製造す
る装置に関するものである。[Detailed Description of the Invention] [Field of Industrial Application] The present invention relates to a sludge/water production device, and more specifically, it is used for food such as raw materials and processed products, water supply and sewage, human waste treatment, medical equipment, paper pulp, The present invention relates to an apparatus for producing ozonated water, which is effective as a means for sterilization, sterilization, decolorization, and deodorization in various semiconductor fields.
従来のオゾン水製造には、大別して２ つのエジェクタ方式がある。 Conventional ozonated water production can be roughly divided into two types. There are two ejector methods.
その第１のエジェクタ方式は、たとえば、第３図に示す
ようなものからなる。第３図において、５１はオゾナイ
ザで、空気または酸素が併給される。５２はエジェクタ
。The first ejector system is, for example, as shown in FIG. In FIG. 3, 51 is an ozonizer, to which air or oxygen is co-supplied. 52 is an ejector.
５５は水を加圧するポンプで、該ポンプ５３で加圧され
た水がエジェクタ５２に供給されてオゾナイザ５１から
のオゾンガスを吸引する。５４は気液分離槽である。55 is a pump that pressurizes water, and the water pressurized by the pump 53 is supplied to the ejector 52, which sucks ozone gas from the ozonizer 51. 54 is a gas-liquid separation tank.
すなわち、エジェクタ５２内にポンプ
５３で加圧した水を流し、ノズルから噴射させることに
より、側面から大気圧下のオゾンガスを吸引し、乱流攪
拌状態で気液混合させたのち、気液分離槽５４内で排オ
ゾンガスを分離し、オゾン水を製造する。That is, by flowing water pressurized by a pump 53 into the ejector 52 and injecting it from the nozzle, ozone gas under atmospheric pressure is sucked from the side, and after gas-liquid mixing in a turbulent agitation state, the gas-liquid separation tank is Exhaust ozone gas is separated in 54 to produce ozone water.
また第２のエジェクタ方式は、第４図に示すように、ち
ょうど、第３図に示した装置に、パルプ５５を追加して
いる。In the second ejector system, as shown in FIG. 4, pulp 55 is added to the apparatus shown in FIG. 3.
すなわち、この第２のエジェクタ方式は、パルプ５５を
半開にして、エジェクタ５２内にポンプ５３で加圧した
水を流し、ノズルから噴射させることにより、側面から
大気圧下のオゾンガスを吸引し、乱流攪拌状態で気液混
合させ、再度、ポンプ５３の１次側に戻し、再加圧後、
気液分離槽５４に送給し、気液分離槽５４で排オゾンガ
スを分離し、オゾン水を製造する。That is, in this second ejector method, the pulp 55 is half-opened, water pressurized by the pump 53 is flowed into the ejector 52, and the water is injected from the nozzle, thereby sucking ozone gas under atmospheric pressure from the side surface and causing turbulence. Gas-liquid is mixed in a flowing agitation state, returned to the primary side of the pump 53 again, and after repressurization,
The ozone gas is fed to the gas-liquid separation tank 54, and the exhausted ozone gas is separated therein to produce ozone water.
前述した第１のエジェクタ方式では、エジェクタ５２内
に流し込む水量に対し、吸引するオゾンガス量が少ない
ため、高偵度のオシ／水ができなく、またエジェクタ５
２の２次側圧力が低いため、オゾンガスの溶解量が少な
く、さらに、ワンスルーのため、オゾン濃度のコントロ
ールが困難であるという問題点があった。In the first ejector method described above, the amount of ozone gas sucked is small compared to the amount of water flowing into the ejector 52, so it is not possible to eject/water with high accuracy.
Since the pressure on the secondary side of No. 2 is low, the amount of ozone gas dissolved is small, and furthermore, since it is a one-through method, it is difficult to control the ozone concentration.
また第２のエジェクタ方式では、ポンプ５３の１次Ｉ１
１に負圧が生じ、ポンプ５３にキャビテーションを起こ
しやすいという問題点があった。In addition, in the second ejector method, the primary I1 of the pump 53
There was a problem in that negative pressure was generated in the pump 53, and cavitation was likely to occur in the pump 53.
本発明は、上記の問題点を解決しようとするものである
。すなわち、本発明は、ポンプにキャビテーショ／を発
生させることなく、加圧下で気液溶解させることが可能
となって、高濃度のオゾン水が得られるとともに、装置
全体の大きさをコンパクト圧することができて、設備費
および運転費を低減することが可能なオゾン水製造装置
を提供することを目的とするものである。The present invention attempts to solve the above problems. That is, the present invention makes it possible to dissolve gas and liquid under pressure without causing cavitation in the pump, thereby obtaining highly concentrated ozone water, and reducing the overall size of the device. It is an object of the present invention to provide an ozone water production device that can reduce equipment costs and operating costs.
上記目的を達成するために１本発明は。 One aspect of the present invention is to achieve the above objects.
エジェクタと、このエジェクタにオゾンガスを供給する
オゾナイザと、水を加圧する１段目ポンプと、この１段
目ポンプで加圧された加圧水および前記エジェクタから
の気液混合体を再加圧してその一部を前記エジェクタに
圧送する２段目ポンプと、この２段目ポンプで加圧され
た該気液混合体の前記一部以外の気′ＦＩＬ’＋％合体
を流入させてオゾン水と排オゾンガスとに気液分離する
気液分離槽とを備えているものとした。An ejector, an ozonizer that supplies ozone gas to the ejector, a first-stage pump that pressurizes water, and a repressurized water and gas-liquid mixture from the ejector. a second-stage pump that pumps a part of the gas to the ejector, and a combination of air 'FIL'+% other than the part of the gas-liquid mixture pressurized by the second-stage pump to flow into ozone water and exhaust ozone gas. and a gas-liquid separation tank for separating gas and liquid.
本発明によれば、エジェクタを用い、オゾナイザで発生
させたオゾンガスを気液接触させたのち、水を加圧する
１段目ポンプと２段目ポンプの間に戻して再加圧するの
で、該２段目ポンプにキャビテーションを発生させるこ
となく、加圧下で気液溶解させることが可能となり、高
７ｓ度のオゾン水が得られるとともに、排オゾンガス濃
度を低くおさえ、装置全体の大きさをコンパクトにする
ことが可能となる。According to the present invention, the ejector is used to bring the ozone gas generated by the ozonizer into gas-liquid contact, and then the water is returned between the first stage pump and the second stage pump to repressurize the water. It is possible to dissolve gas and liquid under pressure without causing cavitation in the pump, and it is possible to obtain ozonated water with a high temperature of 7 seconds, to keep the exhaust ozone gas concentration low, and to make the overall size of the device compact. becomes possible.
第１図は本発明の一実施例を示し、第２図は第１図のラ
インの矢印の説明図である。FIG. 1 shows an embodiment of the present invention, and FIG. 2 is an explanatory diagram of line arrows in FIG. 1.
第１図において、１はオゾナイザ、２は水道水を加圧す
る１段目ポンプ、３と４は水道水と気液混合体を加圧す
る２段目ポンプ、５は加圧溶解槽、６は気液混合体をオ
ゾン水と排オシ／ガスに分離する気液分離槽、７は洗浄
水槽、８はエジェクタ、９は排オゾン分解装置、１０は
酸素ガスボンベ、１１．１２，１３．１４はフローメー
タ、１５．１６．１７は気相オゾン濃度計、１８．１？
、２０．２１は圧力計、２２は減圧弁、２３，２４，２
５，２６，２７゜２８．２９は流量調整弁、６０はチャ
ツキ弁、３１，３２，５５，５４，３５，５６゜５７．
３８，３９，４０．４１はストップ弁、４２はチャツキ
弁である。In Figure 1, 1 is an ozonizer, 2 is a first-stage pump that pressurizes tap water, 3 and 4 are second-stage pumps that pressurize tap water and a gas-liquid mixture, 5 is a pressurized dissolution tank, and 6 is a gas-liquid mixture. A gas-liquid separation tank that separates the liquid mixture into ozone water and exhaust gas/gas; 7 is a cleaning water tank; 8 is an ejector; 9 is an exhaust ozone decomposition device; 10 is an oxygen gas cylinder; 11.12 and 13.14 are flow meters. , 15.16.17 is a gas phase ozone concentration meter, 18.1?
, 20.21 is a pressure gauge, 22 is a pressure reducing valve, 23, 24, 2
5, 26, 27° 28. 29 is a flow rate adjustment valve, 60 is a check valve, 31, 32, 55, 54, 35, 56° 57.
38, 39, 40, and 41 are stop valves, and 42 is a check valve.
第１図に示すように構成されたオゾン製造装置において
は、１段目ポンプ２で加圧した水道水を２段目ポンプ３
と４でさらに加圧し、その一部をエジェクタ８に供給す
る。一方、オゾナイザ１で発生させたオゾンガスを該エ
ジェクタ８の側面へ供給することにより、加圧水によっ
て、オシ／ガスはエジェクタ８内に吸引され、加圧下で
水中に混合されて気液混合体となる。In the ozone production apparatus configured as shown in FIG.
Further pressure is applied in steps 4 and 4, and a portion of the pressure is supplied to the ejector 8. On the other hand, by supplying the ozone gas generated by the ozonizer 1 to the side surface of the ejector 8, the ozone/gas is sucked into the ejector 8 by pressurized water and mixed into water under pressure to form a gas-liquid mixture.
この気液混合体は、１段目ポンプ２の２次側に至り、２
段目ポンプ３と４でさらに加圧溶解されたのち、加圧溶
解槽５へ入れられる。This gas-liquid mixture reaches the secondary side of the first stage pump 2, and
After being further pressurized and dissolved by the stage pumps 3 and 4, it is put into the pressurized dissolution tank 5.
この加圧溶解槽５は、気体溶解に最適な接触時間（１〜
５分）を保てるように設計されているため、オゾンガス
は、加圧下で飽和状態に近いレベルまで水中に溶解され
たのち、通常は流量調整弁２６を通り、気液分離槽６へ
入る。気液分離槽６内は常圧（大気圧）であるので、オ
ゾン水は常圧での飽和状態となり、ここの過飽和分が排
オゾンガスとして分離され、排オゾン分解装置９内でオ
ゾンが分解されたのち、大気中に放出される。オゾン水
はストップ弁３２を通り、洗浄水槽７へ入る。このとき
、流量調整弁２７の開度を調節することにより、オゾナ
イザ１のオゾン発生量を可変することなく、洗浄水槽７
内のオゾン水濃度をコントロールすることが可能となる
。This pressurized dissolution tank 5 has an optimum contact time (1 to
5 minutes), the ozone gas is dissolved in water under pressure to a level close to saturation, and then normally passes through the flow rate regulating valve 26 and enters the gas-liquid separation tank 6. Since the inside of the gas-liquid separation tank 6 is at normal pressure (atmospheric pressure), the ozonated water becomes saturated at normal pressure, and the supersaturated portion is separated as exhaust ozone gas, and the ozone is decomposed in the exhaust ozone decomposition device 9. It is then released into the atmosphere. The ozonated water passes through the stop valve 32 and enters the washing water tank 7. At this time, by adjusting the opening degree of the flow rate adjustment valve 27, the cleaning water tank 7 can be
It becomes possible to control the ozone water concentration inside the tank.
また加圧溶解槽５を出たのち、ストップ弁３３を通るこ
とにより（このとき、前記弁２６．２７，３２．５６は
全開とする。）、加圧状態の飽和オゾン水が洗浄水槽７
内で大気圧下に戻るため、過飽和分のオゾンガスが微細
な気泡として洗浄水槽中で発生し、バブリング効果によ
り、洗浄力を高めることが可能となる。Further, after leaving the pressurized dissolution tank 5, the pressurized saturated ozone water passes through the stop valve 33 (at this time, the valves 26, 27 and 32, 56 are fully opened), and the pressurized saturated ozone water flows into the washing water tank 7.
As the pressure inside the tank returns to atmospheric pressure, supersaturated ozone gas is generated as fine bubbles in the cleaning tank, and the bubbling effect makes it possible to increase the cleaning power.
なお上記実施例では、２段目ポンプ３と４が２台からな
る場合を示したが、この２段目ポンプは１台でもよいが
、あるいは直列状に３台またはそれ以上を接続したもの
としてもよい。また加圧溶解槽５は、配管が長い場合な
どのように、気液接触時間を保てる手段がある場合には
省略することができる。さらに、洗浄水槽７を設けない
で、被洗浄物体へ直接オゾンの加圧水を吹き付けること
により、洗浄、殺菌、除菌をしてもよい。In the above embodiment, the second stage pumps 3 and 4 are composed of two units, but the second stage pump may be one unit, or three or more units may be connected in series. Good too. Further, the pressurized dissolution tank 5 can be omitted when there is a means to maintain the gas-liquid contact time, such as when the piping is long. Furthermore, cleaning, sterilization, and sterilization may be performed by directly spraying pressurized ozone water onto the object to be cleaned without providing the cleaning water tank 7.
以上説明したように、本発明によれば、エジェクタを用
い、オゾナイザで発生させたオゾンガスを気液接触させ
たのち、水を加圧する１段目ポンプと２段目ポンプの間
に戻して再加圧するので、該２段目ポンプにキャビテー
ションを発生させることがなく、該２段目ポンプの寿命
が伸び、また加圧下でオゾンガスを水中に溶解させるた
め。As explained above, according to the present invention, the ejector is used to bring the ozone gas generated by the ozonizer into gas-liquid contact, and then the water is returned between the first-stage pump and the second-stage pump that pressurize the water to be re-pressurized. Because the pressure is applied, cavitation does not occur in the second stage pump, extending the life of the second stage pump, and ozone gas is dissolved in water under pressure.
エジェクタの性能にだ右されずに高濃度のオゾン水を製
造することが可能となる。しかも、加圧下で運転するの
で、オゾンの蒸気分圧が下がり、気液接触時間を短かく
することができ、同時に加圧運転のため、実際の取扱い
ガス容量が減少するので、オゾナイザ、溶解槽、排オゾ
ン分解装置等の容量を小さくすることができ、したがっ
て。It becomes possible to produce highly concentrated ozonated water without depending on the performance of the ejector. Moreover, since it operates under pressure, the partial pressure of ozone vapor decreases, making it possible to shorten the gas-liquid contact time. Therefore, the capacity of exhaust ozone decomposition equipment etc. can be reduced.
装置全体をコンパクトにすることができて、設備費およ
び運転費を低減することが可能となる。The entire device can be made compact, and equipment costs and operating costs can be reduced.
第１図は本発明の一実施例をフローシートで示した説明
図、第２図は第１図の矢印の説明図、第３図は従来の技
術の１つの例を示した説明図、第４図は同じくもう１つ
の例を示した説明図である。
１ ・オン゛ナイザ、２・ １段目ポンフ゛、
３．４・ ・２段目ポンフ゛、５・・加圧溶解槽、６・
・気液分離槽、７・・洗浄水槽、８・ パエジエクタ
、９・・排オゾン分解装置、１０・ ・酸素ガスポンベ
。
第
ス
策
図FIG. 1 is an explanatory diagram showing an embodiment of the present invention in the form of a flow sheet, FIG. 2 is an explanatory diagram of the arrows in FIG. FIG. 4 is an explanatory diagram showing another example. 1. Onizer, 2. 1st stage pump,
3.4. 2nd stage pump, 5. Pressure dissolving tank, 6.
・Gas-liquid separation tank, 7. Washing water tank, 8. Passenger tank, 9. Exhaust ozone decomposition device, 10. Oxygen gas pump. First plan
Claims (1)
するオゾナイザと、水を加圧する１段目ポンプと、この
１段目ポンプで加圧された加圧水および前記エジエクタ
からの気液混合体を再加圧してその一部を前記エジエク
タに圧送する２段目ポンプと、 この２段目ポンプで加圧された該気液混合体の前記一部
以外の気液混合体を流入させてオゾン水と排オゾンガス
とに気液分離する気液分離槽とを備えていることを特徴
とする、オゾン水製造装置。 ２、２段目ポンプが、直列状に接続された複数台からな
る請求項１記載のオゾン水製造装置。 ３、気液分離槽の上流側に加圧溶解槽を有する請求項１
または２記載のオゾン水製造装置。 ４、気液分離槽の下流側に洗浄水槽を有する請求項１ま
たは２記載のオゾン水製造装置。５、気液分離槽の上流
側に加圧溶解槽を有し、かつ、該気液分離槽の下流側に
洗浄水槽を有する請求項１または２記載のオゾン水製造
装置。 ６、気体の酸素をオゾナイザに供給する酸素ガスボンベ
を備えている請求項１、２、３、４または５記載のオゾ
ン水製造装置。 ７、１段目ポンプに水道水を供給するようにした請求項
１、２、３、４、５または６記載のオゾン水製造装置。[Claims] 1. An ejector, an ozonizer that supplies ozone gas to the ejector, a first stage pump that pressurizes water, pressurized water pressurized by the first stage pump, and gas-liquid mixture from the ejector. a second-stage pump that repressurizes the body and pumps a part of it to the ejector; and a second-stage pump that allows a gas-liquid mixture other than the part of the gas-liquid mixture pressurized by the second-stage pump to flow in. An ozonated water production device comprising a gas-liquid separation tank that separates ozonated water and exhaust ozone gas into gas-liquid. 2. The ozone water production apparatus according to claim 1, wherein the second stage pump comprises a plurality of units connected in series. 3. Claim 1 comprising a pressurized dissolution tank on the upstream side of the gas-liquid separation tank.
Or the ozone water manufacturing device according to 2. 4. The ozone water production apparatus according to claim 1 or 2, further comprising a washing tank on the downstream side of the gas-liquid separation tank. 5. The ozonated water production apparatus according to claim 1 or 2, further comprising a pressurized dissolution tank upstream of the gas-liquid separation tank, and a washing water tank downstream of the gas-liquid separation tank. 6. The ozonated water production apparatus according to claim 1, 2, 3, 4 or 5, further comprising an oxygen gas cylinder for supplying gaseous oxygen to the ozonizer. 7. The ozone water production apparatus according to claim 1, 2, 3, 4, 5 or 6, wherein tap water is supplied to the first stage pump.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP27095588A JPH02119991A (en) | 1988-10-28 | 1988-10-28 | Device for producing ozone water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP27095588A JPH02119991A (en) | 1988-10-28 | 1988-10-28 | Device for producing ozone water |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH02119991A true JPH02119991A (en) | 1990-05-08 |
Family
ID=17493349
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP27095588A Pending JPH02119991A (en) | 1988-10-28 | 1988-10-28 | Device for producing ozone water |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH02119991A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0648825U (en) * | 1992-06-01 | 1994-07-05 | 昇 阪野 | Low-pressure decomposable gas absorption method |
| CN103435146A (en) * | 2013-09-16 | 2013-12-11 | 南京盟博环保科技有限公司 | Culture water treatment device |
| CN105439098A (en) * | 2015-12-09 | 2016-03-30 | 广州创环臭氧电器设备有限公司 | Ozone water machine using raw material water for cooling |
-
1988
- 1988-10-28 JP JP27095588A patent/JPH02119991A/en active Pending
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0648825U (en) * | 1992-06-01 | 1994-07-05 | 昇 阪野 | Low-pressure decomposable gas absorption method |
| CN103435146A (en) * | 2013-09-16 | 2013-12-11 | 南京盟博环保科技有限公司 | Culture water treatment device |
| CN103435146B (en) * | 2013-09-16 | 2015-01-21 | 南京盟博环保科技有限公司 | Culture water treatment device |
| CN105439098A (en) * | 2015-12-09 | 2016-03-30 | 广州创环臭氧电器设备有限公司 | Ozone water machine using raw material water for cooling |
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