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
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Description
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)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2007318184A JP4615561B2 (en) | 2006-04-28 | 2007-12-10 | Arsenic-containing solution processing method |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
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JP2006126896 | 2006-04-28 | ||
JP2007318184A JP4615561B2 (en) | 2006-04-28 | 2007-12-10 | Arsenic-containing solution processing method |
Related Parent Applications (1)
Application Number | Title | Priority Date | Filing Date |
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JP2007153621A Division JP4087433B2 (en) | 2006-04-28 | 2007-06-11 | Arsenic-containing solution processing method |
Publications (3)
Publication Number | Publication Date |
---|---|
JP2008119690A JP2008119690A (en) | 2008-05-29 |
JP2008119690A5 true JP2008119690A5 (en) | 2009-08-13 |
JP4615561B2 JP4615561B2 (en) | 2011-01-19 |
Family
ID=39505016
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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JP2007318184A Active JP4615561B2 (en) | 2006-04-28 | 2007-12-10 | Arsenic-containing solution processing method |
Country Status (1)
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JP (1) | JP4615561B2 (en) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
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 |
Family Cites Families (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
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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2007
- 2007-12-10 JP JP2007318184A patent/JP4615561B2/en active Active
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