JP2008119690A5 - - Google Patents

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JP2008119690A5
JP2008119690A5 JP2007318184A JP2007318184A JP2008119690A5 JP 2008119690 A5 JP2008119690 A5 JP 2008119690A5 JP 2007318184 A JP2007318184 A JP 2007318184A JP 2007318184 A JP2007318184 A JP 2007318184A JP 2008119690 A5 JP2008119690 A5 JP 2008119690A5
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arsenic
solution
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JP4615561B2 (en
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本発明者らは、上記課題を解決するために鋭意研究した結果、5価の砒素を含む溶液に2価の鉄イオンを加えて、溶液中の砒素に対する鉄のモル比(Fe/As)を1以上にし、酸化剤を加えて大気圧下で撹拌しながら温度70℃以上で反応させた後、固液分離して固形分を回収することにより、砒素の溶出濃度が非常に小さい鉄と砒素の化合物として回収することができることを見出し、本発明を完成するに至った。 The present inventors have made intensive studies to solve the above problems, the addition of bivalent iron ions in a solution containing pentavalent arsenic, the molar ratio of iron to arsenic in the solution to (Fe / As) Iron and arsenic with a very low elution concentration of arsenic by adding an oxidizing agent and reacting at a temperature of 70 ° C. or higher while stirring at atmospheric pressure and then separating the solid and liquid to recover the solid content. As a result, the present invention was completed.

すなわち、本発明による砒素含有溶液の処理方法は、5価の砒素を含む溶液に2価の鉄イオンを加えて、溶液中の砒素に対する鉄のモル比を1以上にし、酸化剤を加えて大気圧下で撹拌しながら温度70℃以上で反応させた後、固液分離して固形分を回収することを特徴とする。 That is, the processing method of the arsenic containing solution according to the present invention, in addition to bivalent iron ions in a solution containing pentavalent arsenic, the molar ratio of iron to arsenic in the solution to 1 or more, the addition of oxidant large After reacting at a temperature of 70 ° C. or higher while stirring under atmospheric pressure, the solid content is separated and solid content is recovered.

この砒素含有溶液の処理方法において、砒素に対する鉄のモル比が1〜1.5であるのが好ましく、反応温度が95℃以下であるのが好ましい。また、溶液中の砒素の濃度が10g/L以上であるのが好ましく、20g/L以上であるのがさらに好ましい。また、5価の砒素を含む溶液に2価の鉄イオンを加えて、溶液のpHを2以下にするのが好ましい。また、2価の鉄イオンとして硫酸鉄(II)七水塩を溶液に加えるのが好ましい。さらに、酸化剤として酸素ガスを使用することができる。
In this method for treating an arsenic-containing solution, the molar ratio of iron to arsenic is preferably 1 to 1.5, and the reaction temperature is preferably 95 ° C. or lower. Further, the concentration of arsenic in the solution is preferably 10 g / L or more, and more preferably 20 g / L or more. Further, it is preferable to add divalent iron ions to a solution containing pentavalent arsenic so that the pH of the solution is 2 or less. Further, it is preferable to add iron (II) sulfate heptahydrate as divalent iron ions to the solution. Furthermore, oxygen gas can be used as an oxidizing agent.

Claims (10)

価の砒素を含む溶液に2価の鉄イオンを加えて、溶液中の砒素に対する鉄のモル比を1以上にし、酸化剤を加えて大気圧下で撹拌しながら温度70℃以上で反応させた後、固液分離して固形分を回収することを特徴とする、砒素含有溶液の処理方法。 The solution was added divalent iron ions containing pentavalent arsenic, the molar ratio of iron to arsenic in the solution to 1 or more, at a temperature 70 ° C. or more while stirring under atmospheric pressure by adding an oxidizing agent After that, a method for treating an arsenic-containing solution, wherein solid content is separated and solid content is recovered. 前記砒素に対する鉄のモル比が1〜1.5であることを特徴とする、請求項1に記載の砒素含有溶液の処理方法。 The method for treating an arsenic-containing solution according to claim 1, wherein the molar ratio of iron to arsenic is 1 to 1.5. 前記温度が95℃以下であることを特徴とする、請求項1または2に記載の砒素含有溶液の処理方法。 The method for treating an arsenic-containing solution according to claim 1 or 2 , wherein the temperature is 95 ° C or lower. 前記溶液中の砒素の濃度が10g/L以上であることを特徴とする、請求項1乃至3のいずれかに記載の砒素含有溶液の処理方法。The method for treating an arsenic-containing solution according to any one of claims 1 to 3, wherein the concentration of arsenic in the solution is 10 g / L or more. 前記溶液中の砒素の濃度が20g/L以上であることを特徴とする、請求項1乃至のいずれかに記載の砒素含有溶液の処理方法。 The method for treating an arsenic-containing solution according to any one of claims 1 to 3 , wherein the concentration of arsenic in the solution is 20 g / L or more. 前記5価の砒素を含む溶液に前記2価の鉄イオンを加えて、前記溶液のpHを2以下にすることを特徴とする、請求項1乃至5のいずれかに記載の砒素含有溶液の処理方法。The treatment of an arsenic-containing solution according to any one of claims 1 to 5, wherein the divalent iron ions are added to the solution containing pentavalent arsenic to make the pH of the solution 2 or less. Method. 前記2価の鉄イオンとして硫酸鉄(II)七水塩を前記溶液に加えることを特徴とする、請求項1乃至のいずれかに記載の砒素含有溶液の処理方法。 The method for treating an arsenic-containing solution according to any one of claims 1 to 6 , wherein iron (II) sulfate heptahydrate is added to the solution as the divalent iron ion. 前記酸化剤が酸素ガスであることを特徴とする、請求項1乃至のいずれかに記載の砒素含有溶液の処理方法。 Characterized in that the oxidizing agent is oxygen gas, the processing method of the arsenic containing solution according to any of claims 1 to 7. 前記砒素を含む溶液が、砒素含有物質をアルカリ溶液に加えてpH10以上にして酸化しながらアルカリ浸出した後に固液分離して砒素を含む浸出液を得る工程と、この浸出液にアルカリ土類金属またはその塩を添加した後に固液分離して砒素とアルカリ土類金属の化合物を含む残渣を得る工程と、この残渣を洗浄して硫酸溶液に添加した後に固液分離して砒素含有溶液を得る工程とを備えた方法によって製造された砒素含有溶液であることを特徴とする、請求項1乃至のいずれかに記載の砒素含有溶液の処理方法。 The arsenic-containing solution is obtained by adding an arsenic-containing substance to an alkaline solution and leaching the alkali while oxidizing to obtain a leaching solution containing arsenic by solid-liquid separation and oxidizing the alkaline-earth metal or its A step of solid-liquid separation after adding a salt to obtain a residue containing an arsenic and alkaline earth metal compound, a step of washing the residue and adding it to a sulfuric acid solution, and then solid-liquid separation to obtain an arsenic-containing solution; The method for treating an arsenic-containing solution according to any one of claims 1 to 8 , wherein the arsenic-containing solution is produced by a method comprising: 前記砒素含有溶液の製造の際に、前記砒素含有物質として硫黄を含む砒素含有物質を使用するか、あるいは前記砒素含有物質が硫黄を含まない場合には前記砒素含有物質または前記浸出液に硫黄を添加し、さらに、前記浸出液に添加する前記アルカリ土類金属またはその塩の量を、前記砒素とアルカリ土類金属の化合物を生成するのに必要なアルカリ土類金属またはその塩の量以上にすることを特徴とする、請求項に記載の砒素含有溶液の処理方法。 In manufacturing the arsenic-containing solution, an arsenic-containing material containing sulfur is used as the arsenic-containing material, or when the arsenic-containing material does not contain sulfur, sulfur is added to the arsenic-containing material or the leachate In addition, the amount of the alkaline earth metal or salt thereof added to the leachate should be more than the amount of the alkaline earth metal or salt required to produce the arsenic and alkaline earth metal compound. The processing method of the arsenic containing solution of Claim 9 characterized by these.
JP2007318184A 2006-04-28 2007-12-10 Arsenic-containing solution processing method Active JP4615561B2 (en)

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JP4538481B2 (en) * 2007-09-25 2010-09-08 日鉱金属株式会社 Method for producing scorodite and method for recycling liquid after synthesis of scorodite
JP5481233B2 (en) * 2010-03-04 2014-04-23 Dowaメタルテック株式会社 Recycling method of waste liquid containing Sn ion
JP6241661B2 (en) * 2013-03-29 2017-12-06 三菱マテリアル株式会社 Arsenic separation and immobilization method
CN112891811B (en) * 2021-01-18 2022-03-25 昆明理工大学 Method for removing arsenic in contaminated acid by using silica gel reinforced zinc slag

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JPS53123368A (en) * 1977-04-02 1978-10-27 Dowa Mining Co Removal of arsenic
JPS59164639A (en) * 1983-03-08 1984-09-17 Nippon Mining Co Ltd Separation of arsenic
JP3254501B2 (en) * 1993-01-12 2002-02-12 秋田製錬株式会社 Method for removing arsenic from acidic solution containing arsenic and iron
JP4126415B2 (en) * 1998-03-31 2008-07-30 Dowaホールディングス株式会社 Method for removing and fixing arsenic present in iron sulfate solution
JP3756687B2 (en) * 1999-01-29 2006-03-15 同和鉱業株式会社 Method for removing and fixing arsenic from arsenic-containing solutions
JP4288828B2 (en) * 2000-04-07 2009-07-01 三菱マテリアル株式会社 Arsenic wastewater treatment method
JP4087433B2 (en) * 2006-04-28 2008-05-21 Dowaメタルマイン株式会社 Arsenic-containing solution processing method

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