GB1137075A - Process for removing titanium and vanadium from phosphoric acid - Google Patents

Process for removing titanium and vanadium from phosphoric acid

Info

Publication number
GB1137075A
GB1137075A GB2195566A GB2195566A GB1137075A GB 1137075 A GB1137075 A GB 1137075A GB 2195566 A GB2195566 A GB 2195566A GB 2195566 A GB2195566 A GB 2195566A GB 1137075 A GB1137075 A GB 1137075A
Authority
GB
United Kingdom
Prior art keywords
phosphoric acid
solution
aqueous
organic
vanadium
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.)
Expired
Application number
GB2195566A
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.)
Dow Chemical Co
Original Assignee
Dow Chemical Co
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 Dow Chemical Co filed Critical Dow Chemical Co
Publication of GB1137075A publication Critical patent/GB1137075A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B25/00Phosphorus; Compounds thereof
    • C01B25/16Oxyacids of phosphorus; Salts thereof
    • C01B25/18Phosphoric acid
    • C01B25/234Purification; Stabilisation; Concentration

Abstract

1,137,075. Purification of phosphoric acid. DOW CHEMICAL CO. 17 May, 1966 [21 May, 1965], No. 2195.5/66. Heading C1A. Aqueous phosphoric acid solution is treated for the removal of titanium and vanadium therefrom by extracting the solution with an organic solvent not soluble in water to more than 10 wt. per cent of the mixture, contacting the thus-obtained organic solution with an aqueous solution containing 0À2-30 wt. per cent of hydrogen peroxide to obtain an organic phase containing the phosphoric acid and an aqueous phase containing the titanium and vanadium, and separating these two phases. Aqueous phosphoric acid or sodium phosphate are recovered from the organic phase by washing it with water or sodium hydroxide solution respectively. The hydrogen peroxide is applied in a volume ratio of 1 : 10 to 1 : 50 in relation to the organic solution. The organic solvent may be a trialkyl phosphate, an aliphatic alcohol, cyclohexanol, methyloyolohexanol, methylcyclohexanone, an ester, an ether or an amide, and may optionally be admixed with a diluent such as toluene, " Varsol " (Registered Trade Mark), benzene, decane, xylene, kerosene or mesitylene. The process is especially suitable for the treatment of phosphoric acid obtained by treating phosphate rock or ore with HC1, H 2 SO 4 , or HNO 3 .
GB2195566A 1965-05-21 1966-05-17 Process for removing titanium and vanadium from phosphoric acid Expired GB1137075A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US45782365A 1965-05-21 1965-05-21

Publications (1)

Publication Number Publication Date
GB1137075A true GB1137075A (en) 1968-12-18

Family

ID=23818201

Family Applications (1)

Application Number Title Priority Date Filing Date
GB2195566A Expired GB1137075A (en) 1965-05-21 1966-05-17 Process for removing titanium and vanadium from phosphoric acid

Country Status (5)

Country Link
BE (1) BE681315A (en)
BR (1) BR6679649D0 (en)
DE (1) DE1567456A1 (en)
GB (1) GB1137075A (en)
IL (1) IL25610A (en)

Also Published As

Publication number Publication date
IL25610A (en) 1969-11-30
DE1567456A1 (en) 1970-08-06
BE681315A (en) 1966-11-21
BR6679649D0 (en) 1973-09-11

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