GB866716A - Process for separating and purifying niobium and tantalum - Google Patents

Process for separating and purifying niobium and tantalum

Info

Publication number
GB866716A
GB866716A GB13314/57A GB1331457A GB866716A GB 866716 A GB866716 A GB 866716A GB 13314/57 A GB13314/57 A GB 13314/57A GB 1331457 A GB1331457 A GB 1331457A GB 866716 A GB866716 A GB 866716A
Authority
GB
United Kingdom
Prior art keywords
tantalum
niobium
complexes
oxalic acid
addition
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
GB13314/57A
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Publication of GB866716A publication Critical patent/GB866716A/en
Expired legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B34/00Obtaining refractory metals
    • C22B34/20Obtaining niobium, tantalum or vanadium
    • C22B34/24Obtaining niobium or tantalum

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Compounds Of Heavy Metals (AREA)
  • Manufacture And Refinement Of Metals (AREA)

Abstract

Niobium and tantalum are separated by selective decomposition of their oxalato complexes of the formula H5[Nb(C2O4)5], H7 [Nb(C2O4)6], H5[Ta(C2O4)5] or H7[Ta(C2O4)6] or complexes formed with complex formulers which are themselves complexes with oxalic acid, such as aluminium, chromium, molybdenum or tungsten oxalic acid, all of which are described and claimed in Specification 866,718. The decomposition of the oxalato complexes is effected according to the procedure of Specification 866,714, that is one or more of the parameters of the liquid system containing the oxalato complexes is altered up to but not beyond the point where crystal nuclei of a niobium or tantalum compound form as determined by the Tyndall effect, the parameter then being maintained unchanged until the separation of the niobium or tantalum fraction is complete. The decomposition is preferably effected at a temperature of at least 40 DEG C. and in order to stabilize the niobium oxalato complexes whilst the tantalum is being precipitated as hydroxide or basic oxalate, complexes of a di- or tri-basic organic acid described in Specification 566,718 may be added. Decomposition of the oxalato complexes, if they are prepared in an acid solution, may be effected by ammonium oxalate, the precipitation pH value for tantalum being pH 8 and for niobium pH 6. Such pHs may be maintained by ammonia or hydrochloric acid addition. If the niobium and tantalum oxalato complexes are prepared from alkaline solution using a metal-oxalic acid as complex former, the addition of such metal oxalic acid itself produces the pH change up to the threshold value at which it is maintained by the addition of ammonia. According to Examples (1) an iron alloy containing tantalum and niobium was dissolved in a nitric/hydrofluoric acid mixture and the niobium and tantalum precipitated by the addition of ammonium hydroxide. After washing with acetic acid to remove iron, the precipitate was converted to oxides by roasting and then melted with potassium bisulphate; the melt was dissolved in aluminium oxalic acid solution at 40-50 DEG C. Precipitation of the tantalum was then effected by adding ammonium oxalate together with hydrochloric acid at a slow rate with vigorous stirring until the onset of the Tyndall effect. 98% of the tantalum comes down as a first fraction. (2) Niobium and tantalic acids are dissolved in caustic potash at 60 DEG C. and the solution diluted and the pH adjusted to 9. Aluminium oxalic acid was gradually added with vigorous stirring until a pH of 8 was reached and thereafter maintained by the addition of ammonia. The tantalum precipitate was filtered off and washed with ammonium oxalate solution and the filtrate then adjusted to pH 6 with hydrochloric acid and ammonium oxalate thereby precipitating the niobium.ALSO:Niobium and tantalum are separated by selective decomposition of their oxalato complexes of the formula H5[Nb(C2O4)5], H7[Nb(C2O4)6], H5[Ta(C2O4)5] or H7[Ta(C2O4)6] or complexes formed with complex formers which are themselves complexes with oxalic acid, such aluminium, chromium, molybdenum or tungsten oxalic acid, all of which are described and claimed in Specification 866,718. The decomposition of the oxalato complexes is effected according to the procedure of Specification 866,714, that is one or more of the parameters of the liquid system containing the oxalato complexes is altered up to, but not beyond, the point where crystal nuclei of a niobium or tantalum compound form as determined by the Tyndall effect, the parameter then being maintained unchanged until the separation of the niobium or tantalum fraction is complete. The decomposition is preferably effected at a temperature of at least 40 DEG C. and in order to stabilize the niobium oxalato complexes whilst the tantalum is being precipitated as hydroxide or basic oxalate, complexes of di- or tri-basic organic acids described in Specification 866,718 may be added. Decomposition of the oxalato complexes, if they are prepared in an acid solution, may be effected by ammonium oxalate, the precipitation pH value for tantalum being pH 8 and for niobium pH 6. Such pHs may be maintained by ammonia or hydrochloric acid addition. If the niobium and tantalum oxalato complexes are prepared from alkaline solution using a metal-oxalic acid as complex former, the addition of such metal oxalic acid itself produces the pH change up to the threshold value at which it is maintained by the addition of ammonia. According to Examples (1) an iron alloy containing tantalum and niobium was dissolved in a nitric/hydrofluoric acid mixture and the niobium and tantalum precipitated by the addition of ammonium hydroxide. After washing with acetic acid to remove iron, the precipitate was converted to oxides by roasting and then melted with potassium bisulphate; the melt was then dissolved in aluminium oxalic acid solution at 40-50 DEG C. Precipitation of the tantalum was then effected by adding ammonium oxalate together with hydrochloric acid at a slow rate with vigorous stirring until the onset of the Tyndall effect. 98% of the tantalum comes down as a first fraction. (2) Niobium and tantalic acids are dissolved in caustic potash at 60 DEG C. and the solution diluted and the pH adjusted to 9. Aluminium oxalic acid was gradually added with vigorous stirring until a pH of 8 was reached and thereafter maintained by the addition of ammonia, The tantalum precipitate was filtered off and washed with ammonium oxalate solution and the filtrate then adjusted to pH 6 with hydrochloric acid and ammonium oxalate thereby precipitating the niobium.
GB13314/57A 1956-04-26 1957-04-26 Process for separating and purifying niobium and tantalum Expired GB866716A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
AT866716X 1956-04-26

Publications (1)

Publication Number Publication Date
GB866716A true GB866716A (en) 1961-04-26

Family

ID=3682441

Family Applications (1)

Application Number Title Priority Date Filing Date
GB13314/57A Expired GB866716A (en) 1956-04-26 1957-04-26 Process for separating and purifying niobium and tantalum

Country Status (1)

Country Link
GB (1) GB866716A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4490340A (en) * 1984-02-29 1984-12-25 Gte Products Corporation Process for the recovery of high purity tantalum oxide
US4495158A (en) * 1984-02-29 1985-01-22 Gte Products Corporation Process for the recovery of tantalum values
US4537750A (en) * 1984-02-29 1985-08-27 Gte Products Corporation Process for producing high purity tantalum oxide
FR3043696A1 (en) * 2015-11-17 2017-05-19 Eramet HYDROMETALLURGICAL METHOD FOR THE SEPARATION AND PURIFICATION OF TANTALIUM AND NIOBIUM

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4490340A (en) * 1984-02-29 1984-12-25 Gte Products Corporation Process for the recovery of high purity tantalum oxide
US4495158A (en) * 1984-02-29 1985-01-22 Gte Products Corporation Process for the recovery of tantalum values
US4537750A (en) * 1984-02-29 1985-08-27 Gte Products Corporation Process for producing high purity tantalum oxide
FR3043696A1 (en) * 2015-11-17 2017-05-19 Eramet HYDROMETALLURGICAL METHOD FOR THE SEPARATION AND PURIFICATION OF TANTALIUM AND NIOBIUM
WO2017085404A1 (en) * 2015-11-17 2017-05-26 Eramet Hydrometallurgical method for separating and purifying tantalum and niobium

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