JP2004074041A5 - - Google Patents

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Publication number
JP2004074041A5
JP2004074041A5 JP2002239217A JP2002239217A JP2004074041A5 JP 2004074041 A5 JP2004074041 A5 JP 2004074041A5 JP 2002239217 A JP2002239217 A JP 2002239217A JP 2002239217 A JP2002239217 A JP 2002239217A JP 2004074041 A5 JP2004074041 A5 JP 2004074041A5
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JP
Japan
Prior art keywords
fluorine
recovering
water
calcium
agglomerate
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Pending
Application number
JP2002239217A
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Japanese (ja)
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JP2004074041A (en
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Publication date
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Priority to JP2002239217A priority Critical patent/JP2004074041A/en
Priority claimed from JP2002239217A external-priority patent/JP2004074041A/en
Priority to PCT/JP2003/010450 priority patent/WO2004018369A1/en
Priority to AU2003262247A priority patent/AU2003262247A1/en
Publication of JP2004074041A publication Critical patent/JP2004074041A/en
Publication of JP2004074041A5 publication Critical patent/JP2004074041A5/ja
Pending legal-status Critical Current

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Claims (5)

フッ素が溶解した水溶液と、粒径5〜50μmの硫酸カルシウム粒子とを混合して、フッ化カルシウムを生成させることにより、フッ素を回収することを特徴とするフッ素の回収方法。A method for recovering fluorine, comprising recovering fluorine by mixing an aqueous solution in which fluorine is dissolved with calcium sulfate particles having a particle diameter of 5 to 50 μm to generate calcium fluoride. 前記水溶液は、
タンタルのフッ化カリウム塩と還元剤とを希釈塩中に投入し、還元反応して反応融液を得て、該反応融液を冷却して集塊を得て、該集塊を水で洗浄して得られた第1廃水と、
水での洗浄の後に酸で洗浄して得られた第2廃水とを含有することを特徴とする請求項1に記載のフッ素の回収方法。
The aqueous solution is
A potassium fluoride salt of tantalum and a reducing agent are put into a diluted salt, a reduction reaction is performed to obtain a reaction melt, the reaction melt is cooled to obtain an agglomerate, and the agglomerate is washed with water And the first wastewater obtained
2. The method for recovering fluorine according to claim 1, comprising: second waste water obtained by washing with water after washing with water .
前記第1廃液中のフッ素濃度は10〜300ppmで、前記第2廃水中のフッ素濃度は100〜20000ppmであることを特徴とする請求項2に記載のフッ素の回収方法。 The fluorine concentration method according to claim 2, wherein the fluorine concentration in the first waste liquid is 10 to 300 ppm, and the fluorine concentration in the second waste water is 100 to 20000 ppm . 生成した前記フッ化カルシウムを、フィルタープレスで膜処理することを特徴とする請求項1ないし3のいずれかに記載のフッ素の回収方法。 4. The method for recovering fluorine according to claim 1, wherein the produced calcium fluoride is subjected to membrane treatment with a filter press . 前記フッ素のモル数(M)と、前記硫酸カルシウムにおけるカルシウムのモル数(MCa)との比率MCa/2Mが、1.2〜2.0の範囲であることを特徴とする請求項1ないし4のいずれかに記載のフッ素の回収方法。 Claims moles of the fluorine and (M F), the ratio M Ca / 2M F of the moles of calcium in the calcium sulfate (M Ca), characterized in that in the range of 1.2 to 2.0 Item 5. The method for recovering fluorine according to any one of Items 1 to 4 .
JP2002239217A 2002-08-20 2002-08-20 Recovering method of fluorine Pending JP2004074041A (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
JP2002239217A JP2004074041A (en) 2002-08-20 2002-08-20 Recovering method of fluorine
PCT/JP2003/010450 WO2004018369A1 (en) 2002-08-20 2003-08-19 Method of recovering fluorine
AU2003262247A AU2003262247A1 (en) 2002-08-20 2003-08-19 Method of recovering fluorine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2002239217A JP2004074041A (en) 2002-08-20 2002-08-20 Recovering method of fluorine

Publications (2)

Publication Number Publication Date
JP2004074041A JP2004074041A (en) 2004-03-11
JP2004074041A5 true JP2004074041A5 (en) 2005-10-13

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JP2002239217A Pending JP2004074041A (en) 2002-08-20 2002-08-20 Recovering method of fluorine

Country Status (3)

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JP (1) JP2004074041A (en)
AU (1) AU2003262247A1 (en)
WO (1) WO2004018369A1 (en)

Families Citing this family (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4368249B2 (en) * 2004-06-01 2009-11-18 三洋電機株式会社 Treatment apparatus and treatment method of water to be treated using the same
JP4747587B2 (en) * 2005-01-27 2011-08-17 株式会社ニコン Method for producing calcium fluoride sintered body
JP4953586B2 (en) * 2005-04-14 2012-06-13 キャボットスーパーメタル株式会社 Fluorine recovery method
JP4591452B2 (en) * 2007-01-16 2010-12-01 パナソニック株式会社 Method and apparatus for treating fluorine-containing water
JP5440095B2 (en) * 2009-10-22 2014-03-12 栗田工業株式会社 Method and apparatus for treating fluorine-containing water
JP2013188673A (en) * 2012-03-13 2013-09-26 Toshiba Corp Fluorine recovery device, fluorine recovery system, and fluorine recovery method
JP5502924B2 (en) * 2012-03-30 2014-05-28 株式会社東芝 Water treatment method
JP2013220956A (en) * 2012-04-13 2013-10-28 Central Glass Co Ltd Method and apparatus for producing calcium fluoride
JP2013220955A (en) * 2012-04-13 2013-10-28 Central Glass Co Ltd Method and apparatus for producing calcium fluoride
JP2014133188A (en) * 2013-01-08 2014-07-24 Toshiba Corp Water treatment method and water treatment apparatus
CN105008357A (en) * 2013-02-21 2015-10-28 辉瑞大药厂 Solid forms of a selective CDK4/6 inhibitor
US10136709B2 (en) 2013-09-06 2018-11-27 Oliver Joen-An Ma Cantilever umbrella
JP5649749B2 (en) * 2014-01-31 2015-01-07 株式会社東芝 Water treatment method

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS49122880A (en) * 1973-03-28 1974-11-25
US5362461A (en) * 1991-10-03 1994-11-08 Kurita Water Industries, Ltd. Method for recovering calcium fluoride from fluoroetchant
JP2001137864A (en) * 1999-11-10 2001-05-22 Daikin Ind Ltd Method for treating waste water containing hydrofluoric acid

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