[go: up one dir, main page]

JP2002177947A - Dissolved ozone removal equipment - Google Patents

Dissolved ozone removal equipment

Info

Publication number
JP2002177947A
JP2002177947A JP2000373971A JP2000373971A JP2002177947A JP 2002177947 A JP2002177947 A JP 2002177947A JP 2000373971 A JP2000373971 A JP 2000373971A JP 2000373971 A JP2000373971 A JP 2000373971A JP 2002177947 A JP2002177947 A JP 2002177947A
Authority
JP
Japan
Prior art keywords
gas
ozone
water
dissolved ozone
liquid separation
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
Application number
JP2000373971A
Other languages
Japanese (ja)
Inventor
Kiyonori Oguma
清典 小熊
Hideaki Ike
池  英昭
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.)
Yaskawa Electric Corp
Original Assignee
Yaskawa Electric Corp
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 Yaskawa Electric Corp filed Critical Yaskawa Electric Corp
Priority to JP2000373971A priority Critical patent/JP2002177947A/en
Publication of JP2002177947A publication Critical patent/JP2002177947A/en
Pending legal-status Critical Current

Links

Landscapes

  • Physical Water Treatments (AREA)

Abstract

(57)【要約】 【課題】メンテナンスが不要であり、イニシャルコス
ト、ランニングコストが小さく、かつ、小型の溶存オゾ
ンを除去する装置を得る。 【解決手段】本発明の溶存オゾン除去装置は、溶存オゾ
ン水を送水する配管に接続される給水口2と排水口3とを
有し、給水口と排水口の途中に収縮部3を設け、その収
縮部にオゾンを含まないガスを注入するガス注入部4を
設けたガス混合管1と、ガス混合管の後段にガス抜き弁7
を有する気液分離槽6とからなり、ガス注入部からオゾ
ンを含まないガスをオゾン水に注入し、気液分離槽によ
り、オゾンを含んだガスと水とを分離し、溶存オゾンを
除去する構成にしている。また、ガス混合管と気液分離
槽の間に気液混合装置を設けてもよい。
(57) [Problem] To provide a small-sized apparatus for removing dissolved ozone, which requires no maintenance, has low initial cost and running cost, and has a small size. The dissolved ozone removing apparatus of the present invention has a water supply port 2 and a drain port 3 connected to a pipe for sending dissolved ozone water, and a contraction section 3 is provided in the middle of the water supply port and the drain port. A gas mixing pipe 1 provided with a gas injection section 4 for injecting a gas not containing ozone into the contraction section, and a gas release valve 7 at a stage subsequent to the gas mixing pipe.
And a gas-liquid separation tank 6 having a gas-liquid separation tank. The ozone-free gas is injected into the ozone water from a gas injection unit, and the gas-liquid separation tank separates the ozone-containing gas and water to remove dissolved ozone. It has a configuration. Further, a gas-liquid mixing device may be provided between the gas mixing pipe and the gas-liquid separation tank.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、オゾンを利用した
水処理において、オゾン水中の溶存オゾンを除去する装
置に関するものである。
The present invention relates to an apparatus for removing dissolved ozone from ozone water in water treatment using ozone.

【0002】[0002]

【従来の技術】従来、オゾン水中の溶存オゾンを除去す
る方法として、主に次の三つがある。第1は、活性炭を
用いた吸着による方法である。図3は従来の活性炭を用
いた溶存オゾン除去装置示す構成図である。オゾン水は
活性炭を充填した溶存オゾン除去槽10へ導入され、活性
炭充填部11を通過した後に排出される。溶存オゾンは活
性炭充填部11を通過するときに活性炭表面に吸着され、
水中から除去される。第2は、紫外線照射による方法で
ある。図4は従来の紫外線照射による溶存オゾンの分解
除去を示す構成図である。溶存オゾン除去槽10には、電
源13に接続された紫外線ランプ12が備えられている。オ
ゾン水は溶存オゾン除去槽10内で紫外線を照射され、酸
素に分解される。第3は、散気管からガスを散気する方
法である。図5は従来のガス散気により溶存オゾンを除
去する方法を示す構成図である(特開平6−71273)。溶
存オゾン除去槽10には散気管14が備えられており、散気
管14には送風用ブロワ15が接続されている。送風用ブロ
ワ15によって、散気管14へオゾンを含まないガスが送ら
れ、水中へ散気される。水中へ散気されたガスにはオゾ
ンが含まれていないので、水中の溶存オゾンが気相へ除
去される。
2. Description of the Related Art Conventionally, there are mainly three methods for removing dissolved ozone in ozone water. The first is an adsorption method using activated carbon. FIG. 3 is a configuration diagram showing a conventional dissolved ozone removing apparatus using activated carbon. The ozone water is introduced into the dissolved ozone removal tank 10 filled with activated carbon, and is discharged after passing through the activated carbon filling section 11. Dissolved ozone is adsorbed on the activated carbon surface when passing through the activated carbon filling unit 11,
Removed from water. The second is a method using ultraviolet irradiation. FIG. 4 is a configuration diagram showing a conventional method of decomposing and removing dissolved ozone by ultraviolet irradiation. The dissolved ozone removal tank 10 is provided with an ultraviolet lamp 12 connected to a power supply 13. The ozone water is irradiated with ultraviolet rays in the dissolved ozone removal tank 10 and decomposed into oxygen. Third is a method of diffusing gas from a diffuser tube. FIG. 5 is a configuration diagram showing a conventional method for removing dissolved ozone by gas aeration (Japanese Patent Laid-Open No. 6-71273). The dissolved ozone removal tank 10 is provided with an air diffuser 14, and the blower 15 is connected to the air diffuser 14. A gas that does not contain ozone is sent to the air diffuser 14 by the blower 15 and is diffused into water. Since the gas diffused into the water does not contain ozone, dissolved ozone in the water is removed to the gas phase.

【0003】[0003]

【発明が解決しようとする課題】ところが、従来の技術
では以下のような問題点がある。 1)活性炭による吸着除去の場合、時間の経過とともに
活性炭の吸着能力が低下するので、定期的な点検や交換
などのメンテナンスが必要である。 2)紫外線による分解除去の場合、紫外線ランプに寿命
があるために、定期的な点検や交換などのメンテナンス
が必要である。また、紫外線ランプは高価であるため
に、イニシャルコストが大きい。さらに、紫外線を常に
照射していなければならないので、ランニングコストが
大きくなる。 3)散気管からガスを散気することによって溶存オゾン
を除去する場合、送風用ブロワを常に運転していなけれ
ばならないので、ランニングコストが大きくなる。ま
た、送風用ブロワを設置するためのスペースが溶存オゾ
ン除去槽とは別に必要になるので設備の小型化が困難で
ある。 そこで、本発明はメンテナンスが不要であり、イニシャ
ルコスト、ランニングコストが小さく、かつ、小型の設
備で溶存オゾンを除去する装置を提供することを目的と
する。
However, the prior art has the following problems. 1) In the case of adsorption removal by activated carbon, the adsorption ability of activated carbon decreases with the passage of time, so that maintenance such as periodic inspection and replacement is required. 2) In the case of decomposition and removal by ultraviolet rays, maintenance such as periodic inspection and replacement is necessary because the ultraviolet lamp has a service life. Further, since the ultraviolet lamp is expensive, the initial cost is large. In addition, since ultraviolet rays must be constantly emitted, running costs increase. 3) When dissolving ozone is removed by diffusing gas from the air diffuser, the blower for blowing must be constantly operated, which increases running costs. In addition, a space for installing a blower for blowing air is required separately from the dissolved ozone removal tank, so that it is difficult to reduce the size of the equipment. Therefore, an object of the present invention is to provide an apparatus that does not require maintenance, has low initial cost and running cost, and removes dissolved ozone with a small facility.

【0004】[0004]

【課題を解決するための手段】上記の課題を解決するた
めに、本発明は、溶存オゾン水を送水する配管に接続さ
れる給水口と排水口とを有し、前記給水口と排水口の途
中に収縮部を設け、その収縮部にオゾンを含まないガス
を注入するガス注入部を設けたガス混合管と、前記ガス
混合管の後段にガス抜き弁を有する気液分離槽とからな
り、前記ガス注入部から前記オゾンを含まないガスを前
記オゾン水に注入し、前記気液分離槽により、オゾンを
含んだガスと水とを分離し、前記溶存オゾンを除去する
構成にしている。また、前記ガス混合管と前記気液分離
槽の間に気液混合装置を設けてもよい。
In order to solve the above-mentioned problems, the present invention has a water supply port and a water discharge port connected to a pipe for supplying dissolved ozone water, and the water supply port and the water discharge port are connected to each other. A gas mixing pipe provided with a gas injection section for injecting a gas containing no ozone into the contraction section, and a gas-liquid separation tank having a gas release valve at a stage subsequent to the gas mixing pipe, The gas containing no ozone is injected into the ozone water from the gas injection unit, the ozone-containing gas and water are separated by the gas-liquid separation tank, and the dissolved ozone is removed. Further, a gas-liquid mixing device may be provided between the gas mixing pipe and the gas-liquid separation tank.

【0005】[0005]

【発明の実施の形態】以下、本発明の実施の形態を図に
基づいて説明する。 (第1の実施形態)本発明の溶存オゾン除去装置の第一
の実施形態を図1に示す。図において、1はガス混合
管、2は給水口、3は収縮部、4はガス注入部、5は排水
口、6は気液分離槽、7はガス抜き弁、8はオゾンガス分
解槽である。ガス混合管1は、オゾン水を導入する給水
口2と内径を狭めた収納部3と、オゾンを含まないガス
を注入するガス注入部4と、オゾンを含まないガスを混
合したオゾン水を排出する排水口5からなる。オゾンを
含まないガスとして、空気を用いた。つぎに、動作につ
いて述べる。いま、オゾン水が送水管1の給水口2から収
縮部3へ圧送される。そうするとオゾン水は収縮部2で流
速を増し、ガス注入部4の静圧が大気圧以下になる。こ
の減圧によって、ガス注入部4からガスを吸引する。オ
ゾン水とオゾンを含まないガスが混合されると、溶存オ
ゾン濃度と気相中のオゾン濃度が非平衡であるために、
溶存オゾンは気相中へ移動し、水中から除去される。溶
存オゾンが除去された水とオゾンを含むガスの混合流体
は送水管1の排水口5から排出され、気液分離槽6へ導入
される。気液分離槽6ではガスと水がそれぞれ上下に分
離され、水は気液分離槽6の下部から排出される。一
方、オゾンを含むガスは気液分離槽6の頂点に設けられ
たガス抜き弁7を通ってオゾンガス分解槽8へ導入され、
周知の熱分解、触媒を用いた分解によって、無害な酸素
に分解されて大気に排出される。なお、本実施例では、
注入するガスとして空気を用いたが、これに限らず、オ
ゾンを含んでいなければ、N2ガス、Arガスなどの不
活性ガスを用いてもよい。また、気液分離槽6から排出
されるオゾンを含むガスは、分解せずに他のオゾン処理
設備に導入し、再使用してもよい。 (第2の実施形態)図2は、本発明の第二の実施形態示
す溶存オゾン除去装置の構成図である。図において、9
は気液混合装置であり、配管中に混合エレメントを内蔵
している。送水管1の後段に気液混合装置9を設けること
により、ガスとオゾン水の混合効率が向上し、溶存オゾ
ンの除去率を向上させることができる。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Embodiments of the present invention will be described below with reference to the drawings. (First Embodiment) FIG. 1 shows a first embodiment of a dissolved ozone removing apparatus according to the present invention. In the figure, 1 is a gas mixing pipe, 2 is a water supply port, 3 is a contraction section, 4 is a gas injection section, 5 is a drain port, 6 is a gas-liquid separation tank, 7 is a gas release valve, and 8 is an ozone gas decomposition tank. . The gas mixing pipe 1 includes a water supply port 2 for introducing ozone water, a storage section 3 having a reduced inner diameter, a gas injection section 4 for injecting a gas containing no ozone, and discharging ozone water containing a gas containing no ozone. Drain 5 Air was used as the ozone-free gas. Next, the operation will be described. Now, the ozone water is pumped from the water supply port 2 of the water pipe 1 to the contraction section 3. Then, the flow rate of the ozone water increases in the contraction section 2, and the static pressure of the gas injection section 4 becomes lower than the atmospheric pressure. By this reduced pressure, gas is sucked from the gas injection unit 4. When ozone water and a gas that does not contain ozone are mixed, the dissolved ozone concentration and the ozone concentration in the gas phase are not equilibrium.
Dissolved ozone moves into the gas phase and is removed from the water. A mixed fluid of water and gas containing ozone from which dissolved ozone has been removed is discharged from the drain port 5 of the water supply pipe 1 and introduced into the gas-liquid separation tank 6. In the gas-liquid separation tank 6, gas and water are separated vertically, and the water is discharged from the lower part of the gas-liquid separation tank 6. On the other hand, the gas containing ozone is introduced into the ozone gas decomposition tank 8 through the gas release valve 7 provided at the top of the gas-liquid separation tank 6,
It is decomposed into harmless oxygen by well-known thermal decomposition and decomposition using a catalyst and is discharged to the atmosphere. In this embodiment,
Although air is used as the gas to be injected, the present invention is not limited to this, and an inert gas such as N 2 gas or Ar gas may be used as long as it does not contain ozone. Further, the gas containing ozone discharged from the gas-liquid separation tank 6 may be introduced into another ozone treatment facility without being decomposed and reused. (Second Embodiment) FIG. 2 is a configuration diagram of a dissolved ozone removing apparatus according to a second embodiment of the present invention. In the figure, 9
Is a gas-liquid mixing device, which has a mixing element built in the piping. By providing the gas-liquid mixing device 9 after the water pipe 1, the mixing efficiency of gas and ozone water is improved, and the removal rate of dissolved ozone can be improved.

【0006】[0006]

【発明の効果】以上説明したように、本発明によれば、
収縮部とガス注入部を備えたガス混合管と気液分離槽と
を設けたので、メンテナンスが不要になり、イニシャル
コストが小さく、設備が小型化ができる効果がある。ま
た、紫外線ランプや送風用ブロワを使用しないので、ラ
ンニングコストも小さくできる。
As described above, according to the present invention,
Since the gas mixing tube having the contraction section and the gas injection section and the gas-liquid separation tank are provided, maintenance is not required, the initial cost is small, and the equipment can be downsized. In addition, since no ultraviolet lamp or blower is used, running costs can be reduced.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明の第1の実施形態を示す溶存オゾン除去
装置の構成図である。
FIG. 1 is a configuration diagram of a dissolved ozone removing device according to a first embodiment of the present invention.

【図2】本発明の第2の実施形態を示す溶存オゾン除去
装置の構成図である。
FIG. 2 is a configuration diagram of a dissolved ozone removing device according to a second embodiment of the present invention.

【図3】従来の活性炭を用いた溶存オゾン除去装置の構
成図である。
FIG. 3 is a configuration diagram of a conventional dissolved ozone removing device using activated carbon.

【図4】従来の紫外線を用いた溶存オゾン除去方法の構
成図である。
FIG. 4 is a configuration diagram of a conventional method for removing dissolved ozone using ultraviolet rays.

【図5】従来の散気管を用いた溶存オゾン除去装置の構
成図である。
FIG. 5 is a configuration diagram of a conventional dissolved ozone removing device using a diffuser tube.

【符号の説明】[Explanation of symbols]

1 ガス混合管 2 給水口 3 収縮部 4 ガス注入口 5 排水口 6 気液分離槽 7 ガス抜き弁 8 オゾンガス分解槽 9 気液混合装置 10 溶存オゾン除去槽 11 活性炭充填部 12 紫外線ランプ 13 電源 14 散気管 15 送風用ブロワ DESCRIPTION OF SYMBOLS 1 Gas mixing pipe 2 Water supply port 3 Shrinkage part 4 Gas injection port 5 Drainage port 6 Gas-liquid separation tank 7 Gas release valve 8 Ozone gas decomposition tank 9 Gas-liquid mixing device 10 Dissolved ozone removal tank 11 Activated carbon filling unit 12 Ultraviolet lamp 13 Power supply 14 Air diffuser 15 Blower for blower

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 溶存オゾン水を送水する配管に接続され
る給水口と排水口とを有し、前記給水口と排水口の途中
に収縮部を設け、その収縮部にオゾンを含まないガスを
注入するガス注入部を設けたガス混合管と、前記ガス混
合管の後段にガス抜き弁を有する気液分離槽とからな
り、前記ガス注入部から前記オゾンを含まないガスを前
記オゾン水に注入し、前記気液分離槽により、オゾンを
含んだガスと水とを分離し、前記溶存オゾンを除去する
ことを特徴とする溶存オゾン除去装置。
1. A water supply port connected to a pipe for supplying dissolved ozone water and a drain port, a contraction section is provided in the middle of the water supply port and the discharge port, and a gas containing no ozone is supplied to the contraction section. A gas mixing pipe provided with a gas injection section to be injected, and a gas-liquid separation tank having a gas release valve at a stage subsequent to the gas mixing pipe, and the ozone-free gas is injected into the ozone water from the gas injection section. And a gas-liquid separation tank for separating gas and water containing ozone to remove the dissolved ozone.
【請求項2】 前記ガス混合管と前記気液分離槽の間に
気液混合装置を設けることを特徴とする請求項1記載の
溶存オゾン除去装置。
2. The dissolved ozone removing apparatus according to claim 1, wherein a gas-liquid mixing device is provided between the gas mixing pipe and the gas-liquid separation tank.
JP2000373971A 2000-12-08 2000-12-08 Dissolved ozone removal equipment Pending JP2002177947A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000373971A JP2002177947A (en) 2000-12-08 2000-12-08 Dissolved ozone removal equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000373971A JP2002177947A (en) 2000-12-08 2000-12-08 Dissolved ozone removal equipment

Publications (1)

Publication Number Publication Date
JP2002177947A true JP2002177947A (en) 2002-06-25

Family

ID=18843254

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000373971A Pending JP2002177947A (en) 2000-12-08 2000-12-08 Dissolved ozone removal equipment

Country Status (1)

Country Link
JP (1) JP2002177947A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1652823A3 (en) * 2004-10-28 2006-06-14 Owen Thomas Leonard A rainwater treatment process

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1652823A3 (en) * 2004-10-28 2006-06-14 Owen Thomas Leonard A rainwater treatment process

Similar Documents

Publication Publication Date Title
JPH05228480A (en) Device for processing hardly biodegradable substance
US20090155131A1 (en) Ethylene oxide decomposition processing method and decomposition processing device therefor
JPH05228481A (en) Treatment equipment for bio-degradable substances
JP2002177947A (en) Dissolved ozone removal equipment
JP2003047952A (en) Groundwater purification apparatus and groundwater purification method
JP2003164861A (en) Ozone water deozone system
JP2003145180A (en) Method and apparatus for purifying contaminated water
JP3997949B2 (en) Purification method of contaminated water
JP2005254136A (en) Device for treating organic material-containing water by ozone
JPH11267691A (en) Water area purifying device
JP2002336842A (en) Equipment for purifying volatile pollutants
JP2002096058A (en) Equipment for purifying volatile pollutants
JP3769093B2 (en) Advanced wastewater treatment device and advanced treatment method
CN218089196U (en) Integrated machine for adding chemicals, blowing off and repairing underground water
JPH07185539A (en) Method and apparatus for removing residual oxidant
JP3051109B2 (en) Decomposition and detoxification of nonyl and phenol in wastewater by ozone
JP7234680B2 (en) water treatment equipment
JP2004008980A (en) Method and apparatus for purifying contaminated water
JP7225894B2 (en) Water treatment device and water treatment method
JP4641131B2 (en) Water treatment apparatus and method
JP4172415B2 (en) Multistage treatment equipment for contaminated water
JPH08192176A (en) Separate injection type ozone contact method
JP2004223363A (en) De-ozone device and de-ozone system
JP2002361270A (en) Method and apparatus for purifying contaminated water
JP2004041963A (en) Ozone separation system and deozonizer