Separation of Niobium and Tantalum in Liquid Extraction Ernest Lee Koerner Jr
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Iowa State University Capstones, Theses and Retrospective Theses and Dissertations Dissertations 1956 Separation of niobium and tantalum in liquid extraction Ernest Lee Koerner Jr. Iowa State College Follow this and additional works at: https://lib.dr.iastate.edu/rtd Part of the Chemical Engineering Commons Recommended Citation Koerner, Ernest Lee Jr., "Separation of niobium and tantalum in liquid extraction " (1956). Retrospective Theses and Dissertations. 13320. https://lib.dr.iastate.edu/rtd/13320 This Dissertation is brought to you for free and open access by the Iowa State University Capstones, Theses and Dissertations at Iowa State University Digital Repository. It has been accepted for inclusion in Retrospective Theses and Dissertations by an authorized administrator of Iowa State University Digital Repository. For more information, please contact [email protected]. INFORMATION TO USERS This manuscript has been reproduced from the microfilm master. 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Ann Arbor, Ml 48106-1346 USA 800-521-0600 NOTE TO USERS This reproduction is tlie best copy available. UMI* UNCLASSMED Title: Separation of Niobium and Tantalum by Liquid Extraction Author; Ernest Lee Koerner, Jr» (official certification of the classification shown is filed in the Ames Laboratory Document Library) Signature was redacted for privacy. Secretary to Declassification Committee UNCLASSlflEL SEPARATION OF NIOBIUM AND TAUTAIITM BY XigJID EXTRACTION Ernest lee Ebemer, Jr A BlsBertatlon Submitted to the Graduate Faculty in Partial Fulfillment of The Se(|uireinenta for the Degree of DOCTOR OF PHILOSOPHT Major. fi«niJjatst: M'.t}&e]Bieal.Engineering • •• •• • Approved: Signature was redacted for privacy. Signature was redacted for privacy. lartment Signature was redacted for privacy. Dean of toaduat'e College lova State College 1956 UMI Number: DP12438 ® UMI UMI Microform DP12438 Copyright 2005 by ProQuest Information and Learning Company. All rights reserved. This microform edition is protected against unauthorized copying under Title 17, United States Code. ProQuest Information and Learning Company 300 North Zeeb Road P.O. Box 1346 Ann Arbor, Ml 48106-1346 Tr^-fS./v'? !EABLB OF COHUBNOIS Pagt SOMMAHT 1 JNTHODUCTION 3 PBEVIOUS WOBK 2 IHVESTIGATIOII 19 Opening of the Ore 19 Preparation of the Extractor Feed Solution 29 Separation of Niobium and Tantalum 3^ Solvent Treatment and Recovery 69 final Conversion of Products JZ COST MAL7SIS 7^ Chemical Costs 77 Equipment Costs and Investment 77 Operating Costs 79 DlSCUSSIOir OF EBStJIiTS 85 LITERATUHE CITEa) 92 ACKROWLEaJOMEJHTS 95 APPENDICES 96 APESHDIX A 97 Analytical Methods 97 jffPEHDIX 100 T/Zi^O iU LIST OF fABLQS Page Talkie 1. Kio'bltutt-baaring mlDarals 9 Table 2. Looatlon and eetioated reserves of nlo'bltua d^oalts 10 Table 3> Ledotuc analysis of Nigerian eoltmblte ore 20 Table U. Seventy per cent hydrofluoric aold regulrementa of Nigerian coltunblte ore 22 Table 5* ^0 effect of diethyl ketone on the hydrofltiorlo aold-ooltunblte ore reaction 23 Table 6. Effect of sulfuric acid on the hydrofluoric acid treatswnt of colunblte ore 2^ Table J. BeaetiAb of Nigerian colunblte ore vlth anhydrous hydrofluoric aold 26 Table 8. Beactlons of fO per cent hydrofluoric aold and columblte ore at 100^ 0...... 28 Table 9. Sq[alllbrlun contacts with varying oxide concentration In diethyl ketone and one molar eulfarlo acid Uo Table 10. Stagevlse analyses for the first nloblun- tantalum slinulated column run using diethyl ketone Table 11. Stagevlse analyses for the second nloblun- tantalum simulated column run uAlng diethyl ketone ^7 Table 12. Stagevlse analyses for the fifth niobium- tantalum simulated column run using diethyl ketone ^9 Table 13. Stagevlse excess hydrofluoric acid determination for the eq|ulllbrlum phases of the fifth simulated column run using diethyl ketone 5^ IT Table lU. Sta^wlse analyse* for the second niobium- tantalum sinulated eoluan run using bsxon* ^6 Table l^. Stagevise analyses for the third niobiua- tantalum siimilated column run using hexone 60 Ta'ble l6. Stagswise analyses for the fourth niobium- tantalum simulated column run using hexone 63 Table I7. Stagewise analyses for niobium-tantalum continuous extraction run 68 Table 18. Preliminary rav material cost estimate for the proposed niobium and tantalum purification process . 7^ Table I9. Installed process eo(aipinent cost for the proposed niobium and tantalum purification plant 80 Table 20. Capital inrestment for the proposed niobium and tantalum purification plant 82 Table 21. Preliminaiy process cost estimate for niohium- tantalum purification plant 83 Tahle 22. Sq|uilibrium data for pure niobium and tantalum fltioridss with hexons 100 T LIST OF 7IGUBSS FlgoM 1. Proposed process for the separation of niobium and tantalum 6 Figure 2. distribution curves for pure niobium and tantalum fluorides with hexone 3^ Figure 3* Effect of initial feed concentration in diethgrl ketone on tajitalua-niobiua separation factors ... 39 Figure U. Equilibrium diagram for the fifth diethyl ketone simulated column ^1 Figure Sq[ulllbrlum diagram for the second hexone simulated column run I . , 33 Figure 6. Sqjuilibrium diagram for the third hexone simulated column run 3S Figure 7. Eqiuilibrium diagram for the fourth hexone simulated column run 63 Figure g. Photograph of the polyethylene mixer-settler extractor 66 Figure 9* Qpantitatiye flov diagram for the proposed process 76 1 SUMHAWr irio1)lttm, also knowx as eoluiniblum. Is one of the new Indiuitrial metals likely to play an is^ortant role in industrial processing In the near future. Its high melting point (U376^ S*.) and low cross section for neutron alisozption (l.l barne) makes it of special interest to the Atomic Snergy Commission. Since tantalum, which invariably acconqpanies niobium in its ores, has a somewhat hi^er cross section for neutron absorption (21 bams) there is considerable interest in developing an industrial process for producing tantalum^free niobium. Tantalum itself is a valuable metal because of its hi^ melting point ) and its resistance to most corrosive chemicals. !I!he purpose of this research was to find an economical method of producing a niobium oxide product containing ais little tantalum and other impurities as possible starting with a typical niobiumorich ore or concen trate. The process selected as a result of the research consisted of the following processing steps: 1. Digestion of the ore or concentrate with hydrofluoric acid. 2. Sxtractibn of niobium and tantalum from the digested mass with an organic solvent suoth as methyl isobutyl ketone. 3. Separation of tantalum and niobium by continuous countercxirrent multistage extraction using an organic solvent and an aqueous scrubbing solvent. 2 Separation of nloljiam from other ixi^tiritles "by a second solvent extraction step using an organic solvent. Stripping of the niohitun and tantaltui from their solvents and regeneration of solvents. IThe process as outlined above was studied on a small scale and demonstrated on a somewhat larger scale so that a more accurate cost estimate could he made. Several pounds of nlohium oxide containing less than 700 parts per million of tantalum oxide tKere produced. Several pounds of tantalum oxide containing less than 100 parts per million of niobium oxide mre produced. Both purity values v^ere the limit of detection for the i^ectrogre{)hio methods en^loyed. Preliminary cost estimates veve made for production of purified niohiun and tantalum oxides from an ore concentrate assaying 63 paz* cent niohium oxide and 7 cent tantalum oxide. The basis chosen was a plant producing 300,000 pounds of total oxides per year or 270,000 pounds niohium oxide and 30,000 pounds tantalum oxide. Estimated chemical and total operating costs for oxie poxuid of either tantalum or niohium oxide vere ^1.89 and 3 imOBUOTlOH moblvfii and tantaliua have had an Interesting histoxy. In 1801 Hatehett discovered niohitm in a Connecticut mineral. Since niohium-i hearing minerals without tantalum are virtually unknown, the first investi gators irfere dealing with mixtures of these tvo chemically similar elements* IThe presence of titanium in some cases caused additional con^lications. Before their final identification, seven names had heen ascribed to new elements that were thoTight to he present in these minerals. Marignac finally identified the two elements in 1866 hy separating them as complex potassiuB fluorides hy fractional crystallization. He found that the con^lex niobium fluoride was isomoxphous with the known salts EgTlFg* 1^0 and vAiich indicated that the valence of niohium was and the formula of