JP2000308892A - Oxidation of metal in water - Google Patents

Oxidation of metal in water

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Publication number
JP2000308892A
JP2000308892A JP11118386A JP11838699A JP2000308892A JP 2000308892 A JP2000308892 A JP 2000308892A JP 11118386 A JP11118386 A JP 11118386A JP 11838699 A JP11838699 A JP 11838699A JP 2000308892 A JP2000308892 A JP 2000308892A
Authority
JP
Japan
Prior art keywords
air
impeller
liquid
water
metal
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
JP11118386A
Other languages
Japanese (ja)
Inventor
Akihito Umeda
明史 梅田
Takanori Kamiyama
隆徳 上山
Kazuhiko Isaka
和彦 伊坂
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.)
Nippon Steel Corp
Air Water Inc
Original Assignee
Air Water Inc
Sumitomo Metal Industries Ltd
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 Air Water Inc, Sumitomo Metal Industries Ltd filed Critical Air Water Inc
Priority to JP11118386A priority Critical patent/JP2000308892A/en
Publication of JP2000308892A publication Critical patent/JP2000308892A/en
Pending legal-status Critical Current

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  • Treatment Of Water By Oxidation Or Reduction (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a method for oxidizing metallic ions and metallic compounds at a low running cost with good maintainability for treating waste water containing them. SOLUTION: Air and a bottom liquid are introduced to a pressure-reduced area generated at the rear side in the rotation direction of an impeller fixed to a drive shaft which rotates in water. Fine bubbles 37 of the air are generated by vortex caused by the rotation of the impeller and shearing force of the impeller to efficiently oxidize the metallic ions and metallic compounds in the waste water. As a result, a supply pressure of air can be made equivalent to only the liquid height (liquid pressure) so that the running cost can be reduced, and the maintenance and inspection can easily be performed.

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、金属イオンおよび
金属化合物を含有する廃水中の金属イオンおよび金属化
合物を効率よく酸化する方法に関する。
The present invention relates to a method for efficiently oxidizing metal ions and metal compounds in wastewater containing metal ions and metal compounds.

【0002】[0002]

【従来の技術】鉄鋼材料の酸洗においては、第1鉄イオ
ン(Fe2+)および第1鉄化合物(FeCl2、FeSO4)を含有する
酸洗廃液が発生する。第1鉄イオンおよび第1鉄化合物を
含有する酸洗廃液の処理方法としては、廃塩酸処理には
焙焼方式(噴霧焙焼、流動焙焼)と加熱蒸発方式(硫酸置
換)、中和処理法が、廃硫酸処理には硫酸鉄結晶法、中
和処理法などが知られている。
2. Description of the Related Art In pickling of steel materials, pickling waste liquid containing ferrous ions (Fe 2+ ) and ferrous compounds (FeCl 2 , FeSO 4 ) is generated. As a method for treating the pickling waste liquid containing ferrous ions and a ferrous compound, waste hydrochloric acid treatment includes a roasting method (spray roasting, fluidized roasting), a heat evaporation method (substitution with sulfuric acid), and a neutralization treatment. Known methods of treating waste sulfuric acid include an iron sulfate crystal method and a neutralization treatment method.

【0003】上記のうち中和処理法は、アルカリ剤により廃
水を中和処理して塩化鉄あるいは硫酸鉄を第1鉄イオ
ン、水酸化第1鉄としたのち、第1鉄イオンおよび水酸化
第1鉄を酸化剤により強制酸化して水酸化第2鉄として回
収している。この場合の酸化剤としては、空気、純酸
素、オゾンがあるが、空気を用いるのが最も一般的であ
る。
[0003] Among the above, in the neutralization treatment method, wastewater is neutralized with an alkali agent to convert iron chloride or iron sulfate into ferrous ions and ferrous hydroxide, and then ferrous ions and ferrous hydroxide. Iron is forcibly oxidized with an oxidizing agent and recovered as ferric hydroxide. As the oxidizing agent in this case, there are air, pure oxygen, and ozone, and air is most commonly used.

【0004】この空気を使用した廃水中の第1鉄イオンおよ
び水酸化第1鉄の酸化は、その殆んどが散気管を用いた
ものであり、圧縮空気またはブロワーによる昇圧空気を
酸洗廃液槽の底部から散気管を通じて散気ノズルより散
気し、廃水中の第1鉄イオンおよび水酸化第1鉄を酸化し
ている。
[0004] Most of the oxidation of ferrous ions and ferrous hydroxide in wastewater using air is performed using a diffuser, and pressurized air generated by compressed air or a blower is used to remove pickling wastewater. Air is diffused from the bottom of the tank through the air diffuser through the air diffuser, oxidizing ferrous ions and ferrous hydroxide in the wastewater.

【0005】散気管による酸化方法は、散気ノズルの孔径を
小さくすると、散気ノズルの目詰まりの問題が生じるこ
とから、散気ノズルから吹き出す気泡サイズに限界があ
り、効率の悪い気液接触となっている。このため、この
方法では、散気空気中の酸素利用効率が低くて多量の空
気を必要とし、圧縮空気、ブロワー等にかかる動力が大
きいという欠点がある。また、散気ノズルの補修時に
は、酸洗廃液槽を空にする必要があり、メンテナンス性
が悪いという欠点もある。
[0005] In the oxidation method using a diffuser tube, when the hole diameter of the diffuser nozzle is reduced, the problem of clogging of the diffuser nozzle occurs. Therefore, the size of bubbles blown out from the diffuser nozzle is limited, and inefficient gas-liquid contact occurs. It has become. For this reason, this method has a drawback that the efficiency of using oxygen in diffused air is low, a large amount of air is required, and the power applied to the compressed air, the blower and the like is large. Further, at the time of repairing the air diffuser nozzle, it is necessary to empty the pickling waste liquid tank, and there is a disadvantage that the maintenance property is poor.

【0006】また、他の散気装置としては、上方に気体取入
口を有し且つ下方側部に複数の気体噴出孔を穿設した通
気パイプと、前記通気パイプに沿うよう通気パイプの下
方側部に固定したインペラーと、通気パイプの下端開口
部を閉塞する仕切板とを有する気液混合装置(特公昭62-
34436号公報)等が提案されている。
[0006] Further, as another air diffusing device, a ventilation pipe having a gas inlet above and a plurality of gas ejection holes formed in a lower side portion, and a lower side of the ventilation pipe along the ventilation pipe. Gas-liquid mixing device having an impeller fixed to the section and a partition plate closing the lower opening of the ventilation pipe
No. 34436) has been proposed.

【0007】[0007]

【発明が解決しようとする課題】上記特公昭62-34436号
公報に開示の気液混合装置は、回転軸を兼用した通気パ
イプを液中から液外まで延出し、液外に設けた回転駆動
機により回転させるため、槽の深さに対応して装置が大
型化すると共に、保守点検等が容易に行えない難点があ
った。
The gas-liquid mixing device disclosed in Japanese Patent Publication No. 62-34436 discloses a rotary drive provided with a ventilation pipe, which also serves as a rotating shaft, extending from inside the liquid to outside the liquid. Since the apparatus is rotated by the machine, the size of the apparatus is increased according to the depth of the tank, and there is a problem that maintenance and inspection cannot be easily performed.

【0008】本発明の目的は、上記従来技術の欠点を解消
し、金属イオンおよび金属化合物を含有する廃水処理に
おいて、ランニングコストが低く、かつメンテナンス性
の良好な酸化方法を提供することにある。
[0008] An object of the present invention is to solve the above-mentioned drawbacks of the prior art, and to provide an oxidizing method with low running cost and good maintainability in treating wastewater containing metal ions and metal compounds.

【0009】[0009]

【課題を解決するための手段】本発明の水中金属の酸化
方法は、液中回転駆動機の回転軸に固定した羽根車の回
転方向の背側に生じる負圧中に空気と下方の液体を導入
し、羽根車の回転により発生する渦流と羽根車の剪断力
とにより空気の微細気泡を発生させ、廃水中の金属イオ
ンおよび金属化合物を効率的に酸化することを特徴とす
る。
SUMMARY OF THE INVENTION According to the present invention, there is provided a method for oxidizing a metal in water, comprising the steps of separating air and a liquid underneath into a negative pressure generated behind a rotating direction of an impeller fixed to a rotating shaft of a submerged rotary drive. The method is characterized in that vortices generated by the rotation of the impeller and the shear force of the impeller generate fine air bubbles to efficiently oxidize metal ions and metal compounds in wastewater.

【0010】このように、液中回転駆動機の回転軸に固定し
た羽根車の回転方向の背側に生じる負圧中に空気と下方
の液体を導入し、羽根車の回転により発生する渦流と羽
根車の剪断力とにより空気の微細気泡を発生させる水中
散気装置を使用することによって、廃液と空気との気液
接触が高められて酸素利用効率が向上し、廃水中の金属
イオンおよび金属化合物を効率的に酸化することができ
る。この結果、空気の供給圧力を廃水処理槽の液深圧
(液圧)のみとすることができ、ランニングコストを低減
できる。また、液中回転駆動機と羽根車で主要部を構成
したので、保守点検を容易に行うことができる。
As described above, the air and the lower liquid are introduced into the negative pressure generated on the rear side in the rotation direction of the impeller fixed to the rotation shaft of the submerged rotary drive, and the vortex generated by the rotation of the impeller is generated. By using an underwater air diffuser that generates fine air bubbles by the shearing force of the impeller, gas-liquid contact between the waste liquid and the air is enhanced, oxygen utilization efficiency is improved, and metal ions and metals in the waste water are improved. The compound can be oxidized efficiently. As a result, the air supply pressure is reduced to the liquid depth pressure of the wastewater treatment tank.
(Hydraulic pressure) only, and running costs can be reduced. In addition, since the main part is constituted by the submerged rotary drive and the impeller, maintenance and inspection can be easily performed.

【0011】[0011]

【発明の実施の形態】本発明の水中金属の酸化方法の一
実施例の系統図である図3に基づいて説明する。図3に示
した装置は、主として金属イオンおよび金属化合物を含
有する廃水を酸化する酸化槽31、酸化槽31中の廃水32、
空気を昇圧するブロワー33、ブロワー33で昇圧した空気
を水中散気装置34に導く空気供給管35からなる。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the method for oxidizing a metal in water according to the present invention will be described with reference to FIG. The apparatus shown in FIG. 3 is an oxidation tank 31 for oxidizing wastewater mainly containing metal ions and metal compounds, a wastewater 32 in the oxidation tank 31,
It comprises a blower 33 for pressurizing air, and an air supply pipe 35 for guiding the air pressurized by the blower 33 to an underwater air diffuser 34.

【0012】例えば、鉄鋼材料を酸洗した酸洗廃液には、通
常、数百ppmないし数千ppmのレベルで第1鉄イオンと第1
鉄化合物が混入している。このような酸洗廃液は、アル
カリ剤による中和処理後、原水36として酸化槽31に連続
的に流入する。一方、ブロワー33により昇圧した空気
は、空気供給管35を介して水中散気装置34の空気導入管
に連続的に導入される。この時の空気の導入圧力は、酸
化槽31の水深に相当する圧力より低い圧力とする。空気
の導入圧力を水深に相当する圧力より高い圧力にする
と、水中散気装置34の回転する羽根車の回転方向の背側
の液体中に発生する負圧の作用を利用できないからであ
る。
For example, a pickling waste liquid obtained by pickling a steel material usually contains ferrous ions and ferrous ions at a level of several hundred ppm to several thousand ppm.
Iron compound is mixed. Such pickling waste liquid continuously flows into the oxidation tank 31 as raw water 36 after neutralization treatment with an alkali agent. On the other hand, the air pressurized by the blower 33 is continuously introduced into the air introduction pipe of the underwater air diffuser 34 via the air supply pipe 35. The pressure at which the air is introduced at this time is lower than the pressure corresponding to the water depth of the oxidation tank 31. If the pressure for introducing the air is higher than the pressure corresponding to the water depth, the action of the negative pressure generated in the liquid on the back side in the rotation direction of the impeller that rotates the underwater air diffuser 34 cannot be used.

【0013】また、この時の空気の導入量は、水中散気装置
34の羽根車寸法、羽根車回転数により調整することがで
きる。酸化槽31の底部に配置した水中散気装置34を作動
させると、回転する羽根車の回転方向の背面に液体中に
発生する負圧の作用によって空気が連続的に廃液中に吸
入され、羽根車の回転により発生する渦流と羽根車の剪
断力とにより空気の微細気泡37が発生し、微細気泡37は
廃液32に噴出される。酸化槽31内では、廃液32と微細気
泡37となった空気の気液接触が生じ、廃液32中の第1鉄
イオンと第1鉄化合物を空気中の酸素によって効率よく
酸化する。酸化処理された処理水38は、酸化槽31よりオ
ーバーフローして後工程に搬送される。
[0013] The amount of air introduced at this time is determined by an underwater air diffuser.
It can be adjusted by 34 impeller dimensions and impeller rotation speed. When the underwater air diffuser 34 disposed at the bottom of the oxidation tank 31 is operated, air is continuously sucked into the waste liquid by the action of the negative pressure generated in the liquid on the back side in the rotation direction of the rotating impeller, and the blades Due to the vortex generated by the rotation of the car and the shearing force of the impeller, fine air bubbles 37 are generated, and the fine air bubbles 37 are ejected to the waste liquid 32. In the oxidation tank 31, gas-liquid contact between the waste liquid 32 and the air that has become the fine bubbles 37 occurs, and ferrous ions and ferrous compounds in the waste liquid 32 are efficiently oxidized by oxygen in the air. The oxidized treatment water 38 overflows from the oxidation tank 31 and is transported to a subsequent process.

【0014】この発明で使用する水中散気装置34としては、
水中ポンプ用モータ、羽根車、空気噴出路、整流板、吸
い込み穴、空気供給管とで主要部を構成する。羽根車
は、水中ポンプ用モータにより回転されて液体を下方か
ら側方へ送流させる。空気噴出路は、例えば、羽根車に
設けられて羽根車の回転方向の背面に生じる負圧中に空
気を噴出させる。整流板は、羽根車の下側に位置し、羽
根車からの液体を側方へ案内する。吸い込み穴は、整流
板に設けられて下側の液体を羽根車へ導く。空気供給管
は、整流板に設けられて液外からの空気を空気噴出路に
供給する。
The underwater air diffuser 34 used in the present invention includes:
The main part is composed of a submersible pump motor, an impeller, an air ejection path, a straightening plate, a suction hole, and an air supply pipe. The impeller is rotated by a motor for a submersible pump to cause the liquid to flow laterally from below. The air ejection path is provided, for example, in the impeller, and ejects air during negative pressure generated on the back surface in the rotation direction of the impeller. The current plate is located below the impeller, and guides liquid from the impeller to the side. The suction hole is provided in the current plate and guides the lower liquid to the impeller. The air supply pipe is provided on the current plate and supplies air from outside the liquid to the air ejection path.

【0015】[0015]

【実施例】実施例1 表1に示す仕様の酸化槽の底部に、表1に示す散気管また
は表1に示す仕様の水中散気装置を設置し、原水として
アルカリ剤により中和処理後の第1鉄イオンと水酸化第1
鉄を含む酸洗廃液を供給し、空気はブロワーから供給
し、水中の第1鉄イオンと水酸化第1鉄を低減する従来例
の散気管方式と、本発明例の水中散気装置方式の酸化比
較試験を行った。酸化試験の条件と結果を表2に示す。
なお、水中の第1鉄濃度は、前処理後、原子吸光分析装
置を用いて測定した。
Example 1 An air diffusion tube shown in Table 1 or an underwater air diffuser shown in Table 1 was installed at the bottom of an oxidation tank having the specifications shown in Table 1, and neutralized with an alkaline agent as raw water. Ferrous ion and hydroxide
The pickling waste liquid containing iron is supplied, the air is supplied from the blower, and the air diffuser system of the conventional example that reduces ferrous ions and ferrous hydroxide in water, and the underwater air diffuser system of the present invention example An oxidation comparison test was performed. Table 2 shows the conditions and results of the oxidation test.
In addition, the ferrous iron concentration in water was measured using an atomic absorption spectrometer after the pretreatment.

【0016】比較例の散気管方式は、図1に示すように、酸
化槽1の底部に孔径3mmの散気ノズル2を配置し、槽外よ
り供給管3を介して圧縮空気を散気ノズル2に供給し、酸
洗廃液中に空気をバブリングした。
As shown in FIG. 1, the air diffuser system of the comparative example has an air diffuser nozzle 2 having a hole diameter of 3 mm at the bottom of an oxidation tank 1, and supplies compressed air from outside the tank via a supply pipe 3 to the air diffuser nozzle. 2 and air was bubbled into the pickling waste liquid.

【0017】本発明例の水中散気装置方式は、図2に示すよ
うに、水中ポンプ用モータ21、羽根車22、空気噴出路2
3、整流板24、吸い込み穴25、空気供給管26とで主要部
を構成した水中散気装置27を酸化槽の底部に設置し、水
中ポンプ用モータ21を駆動して羽根車22を回転させると
共に、槽外より空気供給管26を介して空気噴出路23に空
気を導入し、回転する羽根車22の回転方向の背面に液体
中に発生する負圧の作用によって空気が連続的に廃液中
に吸入され、羽根車の回転により発生する渦流と羽根車
の剪断力とにより空気の微細気泡を発生させ、微細気泡
を廃液中に噴出させた。
As shown in FIG. 2, the underwater air diffuser system according to the present invention employs a submersible pump motor 21, an impeller 22, an air
3, an underwater air diffuser 27, which is composed mainly of a current plate 24, a suction hole 25, and an air supply pipe 26, is installed at the bottom of the oxidation tank, and the submersible pump motor 21 is driven to rotate the impeller 22. At the same time, air is introduced into the air ejection passage 23 from outside the tank via the air supply pipe 26, and the air is continuously discharged into the waste liquid by the action of the negative pressure generated in the liquid on the back side in the rotation direction of the rotating impeller 22. The air was sucked into the nozzle, and the vortex generated by the rotation of the impeller and the shearing force of the impeller generated fine air bubbles, which were ejected into the waste liquid.

【0018】[0018]

【表1】 【table 1】

【0019】[0019]

【表2】 [Table 2]

【0020】表2に示すように、ケース2の本発明例の水中散
気装置方式による酸化では、ケース1の比較例の散気管
方式の酸化に比較し、空気流量1/3以下で水中の第1鉄が
十分に酸化されている。なお、比較例の散気管方式の酸
化では、酸素利用率が15%であったのに対し、本発明例
の水中散気装置方式の酸化では、酸素利用率が47%であ
った。また、ケース2の本発明例の水中散気装置方式に
よる酸化時の水中散気装置の消費電力は、0.8KWと非常
に低い動力であった。
[0020] As shown in Table 2, in the oxidation of the case 2 by the underwater aeration device system of the present invention, compared to the oxidation of the diffuser system of the comparative example of the case 1, the air flow rate was 1/3 or less. Ferrous iron is fully oxidized. The oxygen utilization rate was 15% in the diffusion tube type oxidation of the comparative example, whereas the oxygen utilization rate was 47% in the underwater diffusion apparatus type oxidation of the present invention example. In addition, the power consumption of the underwater air diffuser at the time of oxidation by the underwater air diffuser system of Case 2 of the present invention was very low power of 0.8 KW.

【0021】本発明による水中金属の酸化方法は、必要空気
量、酸素利用率および水中散気装置の消費電力から判断
すると、低ランニングコスト性から、非常に高性能であ
ると判断できる。
The method for oxidizing underwater metal according to the present invention can be judged to be extremely high in performance from the viewpoint of low running cost, when judged from the required air amount, oxygen utilization rate and power consumption of the underwater air diffuser.

【0022】[0022]

【発明の効果】本発明の水中金属の酸化方法は、水中散
気装置を酸化槽底部に配置し、水中散気装置の空気導入
管に空気を供給し、酸化槽の廃液中で水中散気装置を作
動し、回転する羽根車の回転方向の背面の液体中に発生
する負圧の作用によって、空気を連続的に廃液中に吸入
させ、羽根車の回転により発生する渦流と、羽根車の剪
断力とにより空気の微細気泡を発生させ、廃液と空気の
気液接触を高め、廃液中の金属イオンおよび金属化合物
を空気中の酸素によって効率よく酸化することができ
る。したがって、従来方式に比較し、ランニングコスト
等のコストダウンを図ることができると共に、メンテナ
ンス性を改善することができる。
According to the method for oxidizing underwater metals of the present invention, an underwater air diffuser is disposed at the bottom of an oxidation tank, air is supplied to an air introduction pipe of the underwater air diffusion apparatus, and the underwater air diffusion is performed in the waste liquid of the oxidation tank. By operating the device, the air is continuously sucked into the waste liquid by the action of the negative pressure generated in the liquid behind the rotating impeller in the direction of rotation, and the vortex generated by the rotation of the impeller and the vortex Due to the shearing force, fine bubbles of air are generated, the gas-liquid contact between the waste liquid and the air is increased, and metal ions and metal compounds in the waste liquid can be efficiently oxidized by oxygen in the air. Therefore, as compared with the conventional method, it is possible to reduce the running cost and the like, and it is possible to improve the maintainability.

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

【図1】実施例で用いた比較例の散気管方式の説明図で
ある。
FIG. 1 is an explanatory diagram of a diffuser system of a comparative example used in Examples.

【図2】実施例で用いた本発明例の水中散気装置の概略
説明図である。
FIG. 2 is a schematic explanatory view of an underwater air diffuser according to an example of the present invention used in an example.

【図3】本発明の水中金属の酸化方法の概略説明図であ
る。
FIG. 3 is a schematic explanatory view of a method for oxidizing a metal in water according to the present invention.

【符号の説明】[Explanation of symbols]

1、31 酸化槽 2 散気ノズル 3 供給管 21 水中ポンプ用モータ 22 羽根車 23 空気噴出路 24 整流板 25 吸い込み穴 26、35 空気供給管 27、34 水中散気装置 32 廃水 33 ブロワー 36 原水 37 微細気泡 38 処理水 1, 31 Oxidation tank 2 Aeration nozzle 3 Supply pipe 21 Submersible pump motor 22 Impeller 23 Air ejection path 24 Rectifier plate 25 Suction hole 26, 35 Air supply pipe 27, 34 Underwater air diffuser 32 Wastewater 33 Blower 36 Raw water 37 Microbubbles 38 Treated water

───────────────────────────────────────────────────── フロントページの続き (72)発明者 上山 隆徳 茨城県鹿嶋市大字光3番地 住友金属工業 株式会社鹿島製鉄所内 (72)発明者 伊坂 和彦 茨城県鹿嶋市大字光3番地 住友金属工業 株式会社鹿島製鉄所内 Fターム(参考) 4D050 AA13 AB52 AB55 BB01 BC10 BD02 BD03 BD06  ──────────────────────────────────────────────────続 き Continuing on the front page (72) Inventor Takanori Ueyama, 3rd, Oaza Hikari, Kashima City, Ibaraki Prefecture Sumitomo Metal Industries, Ltd. Kashima Works, Ltd. F-term in Kashima Works (reference) 4D050 AA13 AB52 AB55 BB01 BC10 BD02 BD03 BD06

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 金属イオンおよび金属化合物を含有する
廃水処理における水中金属の酸化方法において、液中回
転駆動機の回転軸に固定した羽根車の回転方向の背側に
生じる負圧中に空気と下方の液体を導入し、羽根車の回
転により発生する渦流と羽根車の剪断力とにより空気の
微細気泡を発生させ、廃水中の金属イオンおよび金属化
合物を効率的に酸化することを特徴とする水中金属の酸
化方法。
1. A method for oxidizing a metal in water in the treatment of wastewater containing metal ions and a metal compound, wherein air and air are mixed during a negative pressure generated on the back side in the rotation direction of an impeller fixed to a rotation shaft of a submerged rotary drive. Introduces liquid below and generates fine air bubbles by the vortex generated by the rotation of the impeller and the shearing force of the impeller, thereby efficiently oxidizing metal ions and metal compounds in wastewater. How to oxidize metals in water.
JP11118386A 1999-04-26 1999-04-26 Oxidation of metal in water Pending JP2000308892A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11118386A JP2000308892A (en) 1999-04-26 1999-04-26 Oxidation of metal in water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11118386A JP2000308892A (en) 1999-04-26 1999-04-26 Oxidation of metal in water

Publications (1)

Publication Number Publication Date
JP2000308892A true JP2000308892A (en) 2000-11-07

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
JP11118386A Pending JP2000308892A (en) 1999-04-26 1999-04-26 Oxidation of metal in water

Country Status (1)

Country Link
JP (1) JP2000308892A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007275713A (en) * 2006-04-04 2007-10-25 Sumitomo Metal Mining Co Ltd Oxidization method for removing of metal in liquid
CN103833125A (en) * 2013-12-11 2014-06-04 武汉拓泰石化环保科技有限公司 High-speed aeration oxidation treatment apparatus for industrial sewage

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007275713A (en) * 2006-04-04 2007-10-25 Sumitomo Metal Mining Co Ltd Oxidization method for removing of metal in liquid
CN103833125A (en) * 2013-12-11 2014-06-04 武汉拓泰石化环保科技有限公司 High-speed aeration oxidation treatment apparatus for industrial sewage
CN103833125B (en) * 2013-12-11 2015-06-03 武汉拓泰石化环保科技有限公司 High-speed aeration oxidation treatment apparatus for industrial sewage

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