JPH0239956B2 - - Google Patents
Info
- Publication number
- JPH0239956B2 JPH0239956B2 JP61312509A JP31250986A JPH0239956B2 JP H0239956 B2 JPH0239956 B2 JP H0239956B2 JP 61312509 A JP61312509 A JP 61312509A JP 31250986 A JP31250986 A JP 31250986A JP H0239956 B2 JPH0239956 B2 JP H0239956B2
- Authority
- JP
- Japan
- Prior art keywords
- water
- ozone
- dissolved
- water tank
- water supply
- 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
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 170
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims description 33
- 238000004519 manufacturing process Methods 0.000 claims description 22
- 238000010586 diagram Methods 0.000 description 7
- 239000000498 cooling water Substances 0.000 description 5
- 238000010257 thawing Methods 0.000 description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 4
- 230000001580 bacterial effect Effects 0.000 description 4
- 235000013305 food Nutrition 0.000 description 4
- 238000012545 processing Methods 0.000 description 4
- 230000001954 sterilising effect Effects 0.000 description 4
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 3
- 238000004378 air conditioning Methods 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 230000035622 drinking Effects 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 3
- 238000005086 pumping Methods 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- 238000004090 dissolution Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000003595 mist Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 241000195493 Cryptophyta Species 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 210000004666 bacterial spore Anatomy 0.000 description 1
- 235000013361 beverage Nutrition 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000003111 delayed effect Effects 0.000 description 1
- 230000001877 deodorizing effect Effects 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 235000013611 frozen food Nutrition 0.000 description 1
- 230000001678 irradiating effect Effects 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000008213 purified water Substances 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 230000001988 toxicity Effects 0.000 description 1
- 231100000419 toxicity Toxicity 0.000 description 1
Landscapes
- Treatment Of Water By Oxidation Or Reduction (AREA)
Description
【発明の詳細な説明】
［産業上の利用分野］
この発明は、飲料用、食品加工用、解凍処理用
あるいは空調用等の水の殺菌、脱臭、滅菌を目的
に、オゾン溶解水を自動的・継続的に供給する装
置に関する。より具体的には、オゾン溶解水を水
槽中の原水に継続的に循環混入することによりオ
ゾン溶解率を一定に維持すると共に、この浄化さ
れた水を随時取り出すことができる装置に関す
る。[Detailed Description of the Invention] [Field of Industrial Application] This invention automatically generates ozone-dissolved water for the purpose of sterilizing, deodorizing, and sterilizing water for drinking, food processing, thawing, air conditioning, etc. - Concerning continuous supply equipment. More specifically, the present invention relates to a device that maintains a constant ozone dissolution rate by continuously circulating and mixing ozone-dissolved water into raw water in an aquarium, and can take out the purified water at any time.
［従来技術］
従来、オゾン溶解水供給装置としては、オゾン
溶解水の貯溜槽と、これに付属した蛇口等の取出
部とから成るものが知られている。[Prior Art] Conventionally, as an ozone-dissolved water supply device, one is known which consists of an ozone-dissolved water storage tank and an attached outlet such as a faucet.
［発明が解決しようとする問題点］
しかるに、オゾンは空気中にあつて自己分解作
用が急速で、一旦放出されたオゾン溶解水は20〜
30分程で元の水に戻つてしまうため、従来の供給
装置においては、オゾン溶解水の使用に際してオ
ゾン溶解水を製造し、その場でこれを利用すると
いう方式が一般で、利用範囲は限られていた。ま
た、一旦放出されたオゾン溶解水を再度利用する
ということは考えられておらず、不経済であつ
た。[Problems to be solved by the invention] However, ozone is present in the air and self-decomposes rapidly, and the ozone-dissolved water once released is
Because it returns to its original state in about 30 minutes, conventional supply equipment generally produces ozone-dissolved water and uses it on the spot, which limits its scope of use. It was getting worse. Furthermore, no consideration has been given to reusing the ozone-dissolved water once released, which is uneconomical.
［発明の目的］
この発明は、上記問題点を解決し、主として工
業用に大量に使用されるオゾン溶解水を一定濃度
で供給でき、かつ、無駄なく、常時供給できる装
置を供給することを目的とする。[Objective of the Invention] The purpose of the present invention is to solve the above-mentioned problems and to provide a device that can supply ozone-dissolved water, which is mainly used in large quantities for industrial purposes, at a constant concentration and can be supplied constantly without waste. shall be.
［問題点を解決するための手段］
上記目的を達成するための手段として、この発
明のオゾン溶解水供給装置は、オゾン溶解水製造
装置と、水槽と、オゾン溶解水供給部と、これら
オゾン溶解水製造装置と水槽、および水槽とオゾ
ン溶解水供給部とを夫々接続する循環系とから成
る構成としている。[Means for Solving the Problems] As a means for achieving the above object, the ozone-dissolved water supply device of the present invention includes an ozone-dissolved water production device, a water tank, an ozone-dissolved water supply section, and an ozone-dissolved water supply unit. The structure includes a water production device, a water tank, and a circulation system that connects the water tank and an ozone-dissolved water supply section, respectively.
［実施例］
以下、本発明の実施例を、図面に従つて詳細に
説明する。[Examples] Examples of the present invention will be described in detail below with reference to the drawings.
第１図は食品加工用または飲料用として利用さ
れるオゾン溶解水の給水装置の概念図で、原水な
らびにオゾン溶解水が流れる経路を示す概念図で
ある。第１図において、１はオゾン溶解水製造装
置、１０は水槽、２０は給水栓である。 FIG. 1 is a conceptual diagram of a water supply device for ozone-dissolved water used for food processing or drinking, and is a conceptual diagram showing the paths through which raw water and ozone-dissolved water flow. In FIG. 1, 1 is an ozone-dissolved water production apparatus, 10 is a water tank, and 20 is a water tap.
オゾン溶解水製造装置１は、圧送手段４によつ
て水槽１０から吸引した水を流量計５を介して混
合室７へと送り込む一方、オゾン源２（具体的に
は圧縮酸素）から圧送手段３およびオゾナイザ６
を介して同オゾナイザ６で生成されたオゾンを混
合室７へと送り込む。ここで圧送手段３とはオゾ
ン源２が圧縮酸素であることから、具体的にはボ
ンベの圧縮力である。混合室７内には粉砕手段８
が設置されている。 The ozone-dissolved water production apparatus 1 is configured to feed water sucked from a water tank 10 by a pressure feeding means 4 into a mixing chamber 7 via a flow meter 5, and from an ozone source 2 (specifically, compressed oxygen) to a pressure feeding means 3. and ozonizer 6
The ozone generated by the ozonizer 6 is sent into the mixing chamber 7 through the ozonizer 6. Since the ozone source 2 is compressed oxygen, the pressure feeding means 3 specifically refers to the compression force of the cylinder. A crushing means 8 is provided in the mixing chamber 7.
is installed.
第２図は上記粉砕手段８の具体的状態を示す。
粉砕手段８は多数のノズルを混合室７内の全壁面
に配設させて成るもので、第２図および第１図に
おいて、水は圧送手段４によつて混合室７内に圧
送されてくると混合室７内の全壁面に配設された
多数のノズルから噴出して微粒子化され霧状にな
つて混合室７内に充満する。一方オゾンは、混合
室７内にあつて、同室７内に圧送され来り飛散し
衝突し合う水の微粒子に激しく衝突して、極めて
高密度、多面的に霧状の水と接触し合う。その結
果微粒子状の水はオゾンを多量に溶解した水滴と
なつて混合室７の底部に溜まり、アウトレツト９
から高濃度のオゾン溶解水として供給される。こ
の場合、水の圧送手段４、オゾンの圧送手段３、
オゾイナイザ６、あるいは粉砕手段８の力率を調
節することにより、水中のオゾン溶解率を調整す
ることが可能である。なお、上記オゾン源２とし
て圧縮酸素を使用すれば次のような効果がある。
すなわちボンベ中に詰め込まれた純度の高い酸素
を利用でき、空気からオゾンを製造する手間やコ
ストを省けオゾンが容易に入手でき、圧送手段１
１を特別に設ける手間やコストも省け、さらにま
た、空気からオゾンを製造する場合の酸化窒素物
の発生を防止でき、毒性を排除できる。 FIG. 2 shows a concrete state of the crushing means 8. As shown in FIG.
The crushing means 8 consists of a large number of nozzles arranged on the entire wall surface of the mixing chamber 7, and in FIGS. 2 and 1, water is forced into the mixing chamber 7 by the pumping means 4. The mixture is ejected from a large number of nozzles arranged on the entire wall surface of the mixing chamber 7 and is atomized into a mist, which fills the mixing chamber 7. On the other hand, ozone, which is present in the mixing chamber 7, violently collides with fine water particles that are pumped into the chamber 7, scatters and collides with each other, and comes into contact with extremely dense and multifaceted mist water. As a result, the particulate water becomes water droplets with a large amount of ozone dissolved in them and accumulates at the bottom of the mixing chamber 7, and the outlet 9
It is supplied as highly concentrated ozone-dissolved water. In this case, water pumping means 4, ozone pumping means 3,
By adjusting the power factor of the ozoizer 6 or the crushing means 8, it is possible to adjust the ozone dissolution rate in water. Note that if compressed oxygen is used as the ozone source 2, the following effects can be obtained.
In other words, high purity oxygen packed in a cylinder can be used, the effort and cost of producing ozone from air can be saved, ozone can be easily obtained, and the pressure feeding means 1
The trouble and cost of specially providing 1 can be saved, and furthermore, the generation of nitrogen oxides when producing ozone from air can be prevented, and toxicity can be eliminated.
次に、水槽１０は原水を取り込む取込口１１
と、この取込口１１に接続され原水の水位に応動
して開閉する給水弁１２と、原水を前記オゾン溶
解水製造装置１へ送り込む送出口１３と、オゾン
溶解水をオゾン溶解水製造装置１から取り込み給
水のための給水口１４へとオゾン溶解水を導く導
管１５と、前記給水口１４に端を発し水槽１０の
外部に伸びる循環管２１を介してオゾン溶解水を
受け入れる戻入口１６とから構成されている。１
７は水槽１０の上端を密封する蓋である。戻管１
８の１端が、この蓋１７を貫通して蓋１７下面に
開口部を広げ、他端がオゾン溶解水製造装置１内
の混合室７に接続されている。水槽１０中にあつ
て自己分解したオゾンはこの戻管１８を通つて混
合室７へ戻り、無駄なく利用される。１９はエア
フイルタで、蓋１７により密封された水槽１０か
ら戻管１８を通つてオゾンが逃げるに応じ、空気
が濾過侵入できるようにされている。 Next, the water tank 10 has an intake port 11 that takes in raw water.
, a water supply valve 12 connected to this intake port 11 and opened and closed in response to the water level of the raw water, a delivery port 13 that sends the raw water to the ozone-dissolved water production device 1 , and a water supply valve 12 that is connected to the intake port 11 and opens and closes in response to the water level of the raw water; a conduit 15 that leads ozone-dissolved water to a water supply port 14 for water supply; and a return port 16 that receives ozone-dissolved water via a circulation pipe 21 that originates from the water supply port 14 and extends to the outside of the water tank 10. It is configured. 1
7 is a lid that seals the upper end of the water tank 10. Return pipe 1
One end of 8 passes through this lid 17 to form an opening on the lower surface of the lid 17, and the other end is connected to the mixing chamber 7 in the ozone-dissolved water production apparatus 1. The self-decomposed ozone in the water tank 10 returns to the mixing chamber 7 through the return pipe 18 and is utilized without waste. Reference numeral 19 denotes an air filter, which allows air to filter and enter as ozone escapes from the water tank 10 sealed by the lid 17 through the return pipe 18.
循環系の１部を成す循環管２１は、水槽１０の
給水口１４と水槽１０の戻入口１６とを接続し、
この循環管２１の途上には、オゾン溶解水供給部
を成す給水栓２０が設けられている。さらに循環
管２１の途上には圧送手段２２が設けられ、オゾ
ン溶解水を水槽１０の給水口１４から取り出し循
環管２１を経由して１部を給水栓２０を経て排出
し、他部を戻入口１６から水槽１０内へ戻して循
環させている。さらに、循環管２１の途上には、
給水口１４と給水栓２０との間、すなわち水槽１
０から導かれた水が給水栓２０に至る手前の箇所
に殺菌器２３が設置されている。この殺菌器２３
は例えば紫外線を照射して水を殺菌する紫外線殺
菌器である。さらに、この殺菌器２３に隣接させ
て活性炭フイルタ２４を設置すれば、食飲に当た
つてのオゾン溶解水からオゾン及び有機物等を吸
着し、水をおいしくする。なお、食品加工用に給
水する場合には、活性炭フイルタ２４に代えてフ
イルタ２５を設置することもよい。 The circulation pipe 21, which forms part of the circulation system, connects the water supply port 14 of the water tank 10 and the return port 16 of the water tank 10,
A water tap 20 serving as an ozone-dissolved water supply section is provided in the middle of the circulation pipe 21. Further, a pressure feeding means 22 is provided in the middle of the circulation pipe 21, which takes out the ozone-dissolved water from the water supply port 14 of the water tank 10 and discharges one part through the water supply faucet 20 via the circulation pipe 21, and the other part from the return port. 16 and returned to the water tank 10 for circulation. Furthermore, in the middle of the circulation pipe 21,
Between the water supply port 14 and the water supply faucet 20, that is, the water tank 1
A sterilizer 23 is installed at a location before the water led from 0 reaches the water tap 20. This sterilizer 23
For example, it is an ultraviolet sterilizer that sterilizes water by irradiating it with ultraviolet light. Furthermore, if an activated carbon filter 24 is installed adjacent to the sterilizer 23, ozone and organic matter will be adsorbed from the ozone-dissolved water used for eating and drinking, making the water more delicious. Note that when water is supplied for food processing, a filter 25 may be installed in place of the activated carbon filter 24.
次に第３図は、第２実施例である解凍処理用の
オゾン溶解水供給装置を示す概念図である。第３
図において水槽１０は解凍を目的とした水槽であ
つて、冷凍物が投げ入れられるように上縁は解放
されている。この水槽１０は原水を取り込む取込
口１１と、水槽１０内の水をオゾン溶解水製造装
置１へ送り出す送出口１３と、オゾン溶解水製造
装置１で製造されたオゾン溶解水を取り込みオゾ
ン溶解水供給部である給水端３０までオゾン溶解
水を導く導管１５とから成り、その解放された上
縁の上方にフード３１を懸架させて被覆されてい
る。そしてフード３１の壁面に穿設された開口部
に端を発する戻管１８がオゾン溶解水製造装置１
と接続されている。水槽１０内で自己分解したオ
ゾンを収集して再びオゾン溶解水製造装置１へと
戻し無駄のないようにしたものである。循環系の
１部を成す給水管３２は、前記送出口１３に端を
発し水槽１０をオゾン溶解水製造装置１と結んで
いる。この給水管３２の途上には圧送手段２２、
フイルタ２５を介して第２水槽３３が設置されて
いる。この第２水槽３３は、底部に加熱手段３４
を有し、水量を適量に維持するリミツトスイツチ
３５が取り付けられ、送出口１３から圧送手段２
２で送られてくる水を取り込む取込口３６とオゾ
ン溶解水製造装置１へ給水する給水口３７とが設
けられている。冷凍物は解凍されるにしたがい塵
芥を水槽１０中に浮遊させるので、水槽１０内で
解凍処理された水は送出口１３を出るとフイルタ
２５で一旦濾過されて第２水槽３３に入り加熱手
段３４で加熱殺菌された後、オゾン溶解水製造装
置１でオゾンを溶解され導管１５を通つて給水端
３０へと循環され再び水槽１０へと給水される。 Next, FIG. 3 is a conceptual diagram showing an ozone-dissolved water supply apparatus for thawing treatment, which is a second embodiment. Third
In the figure, a water tank 10 is a water tank for the purpose of thawing, and its upper edge is open so that frozen items can be thrown into it. This water tank 10 has an intake port 11 that takes in raw water, a delivery port 13 that sends the water in the water tank 10 to the ozone-dissolved water production device 1, and an ozone-dissolved water that takes in the ozone-dissolved water produced by the ozone-dissolved water production device 1. It consists of a conduit 15 that guides ozone-dissolved water to a water supply end 30, which is a supply section, and is covered with a hood 31 suspended above the open upper edge of the conduit 15. The return pipe 18 originating from the opening formed in the wall of the hood 31 is connected to the ozone-dissolved water production apparatus 1.
is connected to. Ozone self-decomposed in the water tank 10 is collected and returned to the ozone-dissolved water production device 1 to avoid waste. A water supply pipe 32, which forms part of the circulation system, originates from the outlet 13 and connects the water tank 10 to the ozone-dissolved water production apparatus 1. On the way of this water supply pipe 32, a pressure feeding means 22,
A second water tank 33 is installed with a filter 25 in between. This second water tank 33 has a heating means 34 at the bottom.
A limit switch 35 is installed to maintain the amount of water at an appropriate level, and a limit switch 35 is installed to maintain the amount of water at an appropriate level.
An intake port 36 for taking in the water sent in the ozone solution water production apparatus 1 and a water supply port 37 for supplying water to the ozone-dissolved water production apparatus 1 are provided. As the frozen food is thawed, it causes dust to float in the water tank 10, so when the water that has been thawed in the water tank 10 exits the outlet 13, it is filtered by the filter 25, and then enters the second water tank 33 and is heated by the heating means 34. After being heated and sterilized, ozone is dissolved in the ozone-dissolved water production device 1, and the ozone is circulated through the conduit 15 to the water supply end 30, and then the water is supplied to the water tank 10 again.
この解凍処理用のオゾン溶解水供給装置によれ
ば、処理水を大量に廃棄する無駄を省くと共に、
水槽内のオゾン濃度を一定に保つので、安定した
確実な殺菌効果が得られる。 According to this ozone-dissolved water supply device for thawing treatment, it is possible to avoid wasteful disposal of large amounts of treated water, and
Since the ozone concentration in the aquarium is kept constant, a stable and reliable sterilization effect can be obtained.
次に第４図は、第３実施例である空調その他冷
却水の浄化を目的としたオゾン溶解水供給装置を
示す概念図である。第４図において水槽１０は冷
却塔であつて、補給水を取り込む取込口１１と、
この取込口１１に接続され水槽１０内の水位に応
動して開閉する給水弁１２と、水槽１０内の水を
オゾン溶解水製造装置１へ送り出す送出口１３
と、この送出口１３から出てオゾン溶解水製造装
置１でオゾンを溶解され再び水槽１０へと戻る水
を受け入れるオゾン溶解水供給部である給水端３
０と、水槽１０内の水を排出し熱交換器４０を経
て再び水槽１０へと戻す循環管２１に接続される
給水口１４と、この給水口１４から出て戻つてく
る水を受け入れる戻入口１６とから成つている。
循環系の１部を成す循環管２１の途上には圧送手
段２２が設置されている。また水槽１０内の給水
端３０とオゾン溶解水製造装置１とを導管１５が
結んでいる。 Next, FIG. 4 is a conceptual diagram showing a third embodiment of an ozone-dissolved water supply apparatus for purifying air conditioning and other cooling water. In FIG. 4, the water tank 10 is a cooling tower, and has an intake port 11 for taking in makeup water;
A water supply valve 12 that is connected to this intake port 11 and opens and closes in response to the water level in the water tank 10 , and an outlet port 13 that sends out the water in the water tank 10 to the ozone-dissolved water production device 1
and a water supply end 3 which is an ozone-dissolved water supply section that receives water that comes out from this outlet 13, has ozone dissolved in the ozone-dissolved water production device 1, and returns to the water tank 10.
0, a water supply port 14 that is connected to a circulation pipe 21 that discharges the water in the water tank 10 and returns it to the water tank 10 via the heat exchanger 40, and a return port that receives water that comes out from the water supply port 14 and returns. It consists of 16.
A pressure feeding means 22 is installed in the middle of a circulation pipe 21 that forms a part of the circulation system. Further, a conduit 15 connects the water supply end 30 in the water tank 10 and the ozone-dissolved water production apparatus 1.
元来、空調その他冷却水は水の有効利用のため
循環使用されているが、冷却塔は大容量であり冷
却部は大気解放式なため、水の１部は蒸発し大量
の細菌胞子が混入する。したがつて冷却水は濃縮
され、かつ、細菌汚染および細菌増殖によつて急
速に悪化し、配管や使用機器の腐食、スケール付
着、微生物障害等を起こしている。これに対して
は通常、化学薬品が使用されているが、水温暖か
く細菌増殖に好環境なため十分な効果を上げてい
ない。しかるにオゾンには確実な殺菌効果があ
る。そしてこの第３の実施例のオゾン溶解水供給
装置によれば、冷却水を循環系途上で繰り返しオ
ゾン溶解させるため、細菌増殖を著しく抑制して
藻、スケール等を防止し、濃縮を遅らせて補結水
を節約し、また、化学薬品を不要にし、配管や機
器の寿命を延ばす。 Originally, cooling water for air conditioners and other equipment is circulated to make effective use of water, but since cooling towers have a large capacity and the cooling section is open to the atmosphere, a portion of the water evaporates and a large amount of bacterial spores are mixed in. do. Therefore, the cooling water becomes concentrated and rapidly degrades due to bacterial contamination and bacterial growth, causing corrosion of piping and equipment, scale adhesion, microbial damage, and the like. Chemicals are usually used to combat this, but they are not sufficiently effective because the water is warm and the environment is favorable for bacterial growth. However, ozone has a certain sterilizing effect. According to the ozone-dissolved water supply device of the third embodiment, since ozone is repeatedly dissolved in the cooling water during the circulation system, bacterial growth is significantly suppressed, algae, scale, etc. are prevented, and concentration is delayed and supplemented. It saves water, eliminates the need for chemicals, and extends the life of pipes and equipment.
［発明の効果］
上記の構成から概に明らかなように、本発明に
係るオゾン溶解水供給装置によれば、オゾン溶解
水供給部を閉じている不使用時でもオゾン溶解水
は循環系中を循環する結果、常にオゾン溶解が繰
り返されオゾン濃度は一定を維持される。また、
使用されたオゾン溶解水でも再び水槽に戻りここ
で継続的にオゾン溶解水製造装置から供給されて
くるオゾン溶解水と自然混合させられるから、水
の無駄がなく、オゾン濃度はますます安定維持さ
れる。[Effects of the Invention] As is generally clear from the above configuration, according to the ozone-dissolved water supply device according to the present invention, ozone-dissolved water continues to flow through the circulation system even when the ozone-dissolved water supply section is closed and is not in use. As a result of the circulation, ozone is constantly dissolved and the ozone concentration remains constant. Also,
Even the used ozone-dissolved water returns to the water tank, where it is naturally mixed with the ozone-dissolved water continuously supplied from the ozone-dissolved water production equipment, so there is no wastage of water and the ozone concentration is maintained more and more stably. Ru.
第１図は本発明の第１実施例である飲料用また
は食品加工用のオゾン溶解水供給装置を示す概念
図である。第２図は上記第１実施例中のオゾン溶
解水製造装置に付属の混合室および粉砕手段を示
す断面図である。第３図は第２実施例である解凍
処理用のオゾン溶解水供給装置を示す概念図であ
る。第４図は第３実施例である空調その他冷却水
浄化用のオゾン溶解水供給装置を示す概念図であ
る。
１……オゾン溶解水製造装置、７……オゾナイ
ザ、８……粉砕手段、１０……水槽、１１……取
込口、１３……送出口、１４……給水口、１５…
…導管、１６……戻入口、１８……戻管、２０…
…給水栓、２１……循環管、２２……圧送手段、
３０……給水端、３３……第２水槽、４０……熱
交換器。
FIG. 1 is a conceptual diagram showing an ozone-dissolved water supply apparatus for beverages or food processing, which is a first embodiment of the present invention. FIG. 2 is a cross-sectional view showing the mixing chamber and crushing means attached to the ozone-dissolved water production apparatus in the first embodiment. FIG. 3 is a conceptual diagram showing a second embodiment of an ozone-dissolved water supply device for thawing treatment. FIG. 4 is a conceptual diagram showing a third embodiment of an ozone-dissolved water supply apparatus for purifying cooling water for air conditioning and other purposes. DESCRIPTION OF SYMBOLS 1... Ozone dissolved water manufacturing device, 7... Ozonizer, 8... Crushing means, 10... Water tank, 11... Intake port, 13... Outlet port, 14... Water supply port, 15...
...Conduit, 16...Return port, 18...Return pipe, 20...
... Water tap, 21 ... Circulation pipe, 22 ... Pressure feeding means,
30... Water supply end, 33... Second water tank, 40... Heat exchanger.
Claims (1)
解水供給部と、これらオゾン溶解水製造装置と水
槽、および水槽とオゾン溶解水供給部とを夫々接
続する循環系とから成るオゾン溶解水供給装置。1 Ozone dissolved water supply device consisting of an ozone dissolved water production device, a water tank, an ozone dissolved water supply section, and a circulation system that connects the ozone dissolved water production device, the water tank, and the water tank and the ozone dissolved water supply section, respectively. .
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP31250986A JPS63171694A (en) | 1986-12-29 | 1986-12-29 | Ozonized water feeder |
| JP3205573A JPH06182366A (en) | 1986-12-29 | 1991-07-22 | Thawing treatment device for frozen mater |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP31250986A JPS63171694A (en) | 1986-12-29 | 1986-12-29 | Ozonized water feeder |
Related Child Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP3205573A Division JPH06182366A (en) | 1986-12-29 | 1991-07-22 | Thawing treatment device for frozen mater |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS63171694A JPS63171694A (en) | 1988-07-15 |
| JPH0239956B2 true JPH0239956B2 (en) | 1990-09-07 |
Family
ID=18030075
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP31250986A Granted JPS63171694A (en) | 1986-12-29 | 1986-12-29 | Ozonized water feeder |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS63171694A (en) |
Families Citing this family (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH02144191A (en) * | 1988-11-21 | 1990-06-01 | Sumitomo Seika Chem Co Ltd | Method for purifying water circulating in cooling tower |
| JPH03154691A (en) * | 1989-11-10 | 1991-07-02 | Permelec Electrode Ltd | Method and apparatus for making high concentration ozone water |
| JPH03221195A (en) * | 1990-01-29 | 1991-09-30 | Japan Steel Works Ltd:The | Apparatus for making ozonized water |
| JPH03221196A (en) * | 1990-01-29 | 1991-09-30 | Japan Steel Works Ltd:The | Apparatus for making ozonized water |
| JPH03254890A (en) * | 1990-03-02 | 1991-11-13 | Japan Steel Works Ltd:The | Ozone water making apparatus |
| JP4673673B2 (en) * | 2005-06-06 | 2011-04-20 | 有限会社ガリュー | Ozone water production device, cleaning device using ozone water production device, and water quality improvement device using ozone water production device |
| JP4631561B2 (en) * | 2005-06-27 | 2011-02-16 | パナソニック電工株式会社 | Microbubble generator |
| JP5032810B2 (en) * | 2006-08-31 | 2012-09-26 | 三井造船株式会社 | Ballast water treatment system |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS607990A (en) * | 1983-06-28 | 1985-01-16 | Nippon Rosuiki Kogyo Kk | Sterilization method of feeding system of high-purity water |
-
1986
- 1986-12-29 JP JP31250986A patent/JPS63171694A/en active Granted
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS607990A (en) * | 1983-06-28 | 1985-01-16 | Nippon Rosuiki Kogyo Kk | Sterilization method of feeding system of high-purity water |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS63171694A (en) | 1988-07-15 |
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