CN1134730A - Upgrading titaniferous materials - Google Patents
Upgrading titaniferous materials Download PDFInfo
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- CN1134730A CN1134730A CN94194061A CN94194061A CN1134730A CN 1134730 A CN1134730 A CN 1134730A CN 94194061 A CN94194061 A CN 94194061A CN 94194061 A CN94194061 A CN 94194061A CN 1134730 A CN1134730 A CN 1134730A
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- Prior art keywords
- alkali
- smecta
- leaching
- alkali leaching
- leaches
- Prior art date
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- 239000000463 material Substances 0.000 title claims abstract description 58
- 238000002386 leaching Methods 0.000 claims abstract description 53
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims abstract description 37
- 238000000034 method Methods 0.000 claims abstract description 35
- 239000012535 impurity Substances 0.000 claims abstract description 25
- 230000008569 process Effects 0.000 claims abstract description 10
- 239000003513 alkali Substances 0.000 claims description 63
- GUJOJGAPFQRJSV-UHFFFAOYSA-N dialuminum;dioxosilane;oxygen(2-);hydrate Chemical compound O.[O-2].[O-2].[O-2].[Al+3].[Al+3].O=[Si]=O.O=[Si]=O.O=[Si]=O.O=[Si]=O GUJOJGAPFQRJSV-UHFFFAOYSA-N 0.000 claims description 19
- YDZQQRWRVYGNER-UHFFFAOYSA-N iron;titanium;trihydrate Chemical compound O.O.O.[Ti].[Fe] YDZQQRWRVYGNER-UHFFFAOYSA-N 0.000 claims description 18
- 239000002893 slag Substances 0.000 claims description 17
- 239000011435 rock Substances 0.000 claims description 11
- 230000008929 regeneration Effects 0.000 claims description 8
- 238000011069 regeneration method Methods 0.000 claims description 8
- 238000001556 precipitation Methods 0.000 claims description 6
- 230000001172 regenerating effect Effects 0.000 claims description 5
- 230000001376 precipitating effect Effects 0.000 claims 1
- 239000003518 caustics Substances 0.000 abstract description 2
- 235000011149 sulphuric acid Nutrition 0.000 abstract 1
- 239000001117 sulphuric acid Substances 0.000 abstract 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 38
- 238000005516 engineering process Methods 0.000 description 34
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 25
- HEMHJVSKTPXQMS-UHFFFAOYSA-M sodium hydroxide Inorganic materials [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 25
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 24
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 23
- 239000000047 product Substances 0.000 description 21
- 239000000377 silicon dioxide Substances 0.000 description 19
- 235000012239 silicon dioxide Nutrition 0.000 description 18
- 229960001866 silicon dioxide Drugs 0.000 description 18
- 239000002994 raw material Substances 0.000 description 13
- 229910052742 iron Inorganic materials 0.000 description 12
- 239000000203 mixture Substances 0.000 description 12
- 229910010413 TiO 2 Inorganic materials 0.000 description 11
- 239000007788 liquid Substances 0.000 description 11
- 235000011121 sodium hydroxide Nutrition 0.000 description 11
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 10
- 239000000049 pigment Substances 0.000 description 10
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 9
- 239000004408 titanium dioxide Substances 0.000 description 9
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 7
- 235000011941 Tilia x europaea Nutrition 0.000 description 7
- 239000004411 aluminium Substances 0.000 description 7
- 229910052782 aluminium Inorganic materials 0.000 description 7
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 7
- 239000004571 lime Substances 0.000 description 7
- 239000007787 solid Substances 0.000 description 7
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 6
- 239000000571 coke Substances 0.000 description 6
- 239000007789 gas Substances 0.000 description 6
- 229910052748 manganese Inorganic materials 0.000 description 6
- 239000011572 manganese Substances 0.000 description 6
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 description 6
- 239000010936 titanium Substances 0.000 description 6
- 229910052719 titanium Inorganic materials 0.000 description 6
- 238000011282 treatment Methods 0.000 description 6
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 5
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 description 5
- 238000005660 chlorination reaction Methods 0.000 description 5
- 239000012467 final product Substances 0.000 description 5
- 229910052749 magnesium Inorganic materials 0.000 description 5
- 239000011777 magnesium Substances 0.000 description 5
- 239000000395 magnesium oxide Substances 0.000 description 5
- 230000009467 reduction Effects 0.000 description 5
- 239000000126 substance Substances 0.000 description 5
- 229910052720 vanadium Inorganic materials 0.000 description 5
- LEONUFNNVUYDNQ-UHFFFAOYSA-N vanadium atom Chemical compound [V] LEONUFNNVUYDNQ-UHFFFAOYSA-N 0.000 description 5
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- 229910004298 SiO 2 Inorganic materials 0.000 description 4
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 4
- 239000000654 additive Substances 0.000 description 4
- 230000000996 additive effect Effects 0.000 description 4
- 239000000460 chlorine Substances 0.000 description 4
- 239000011651 chromium Substances 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 229910052500 inorganic mineral Inorganic materials 0.000 description 4
- 235000010755 mineral Nutrition 0.000 description 4
- 239000011707 mineral Substances 0.000 description 4
- 238000012545 processing Methods 0.000 description 4
- 229910052710 silicon Inorganic materials 0.000 description 4
- 239000010703 silicon Substances 0.000 description 4
- 238000005406 washing Methods 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 3
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 3
- 229910052776 Thorium Inorganic materials 0.000 description 3
- 239000002253 acid Substances 0.000 description 3
- 238000005054 agglomeration Methods 0.000 description 3
- 230000002776 aggregation Effects 0.000 description 3
- 229910052784 alkaline earth metal Inorganic materials 0.000 description 3
- 150000001342 alkaline earth metals Chemical class 0.000 description 3
- 229910052801 chlorine Inorganic materials 0.000 description 3
- 238000009833 condensation Methods 0.000 description 3
- 230000005494 condensation Effects 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 238000001914 filtration Methods 0.000 description 3
- 229910052739 hydrogen Inorganic materials 0.000 description 3
- 239000001257 hydrogen Substances 0.000 description 3
- WPBNNNQJVZRUHP-UHFFFAOYSA-L manganese(2+);methyl n-[[2-(methoxycarbonylcarbamothioylamino)phenyl]carbamothioyl]carbamate;n-[2-(sulfidocarbothioylamino)ethyl]carbamodithioate Chemical compound [Mn+2].[S-]C(=S)NCCNC([S-])=S.COC(=O)NC(=S)NC1=CC=CC=C1NC(=S)NC(=O)OC WPBNNNQJVZRUHP-UHFFFAOYSA-L 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000000941 radioactive substance Substances 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- 238000007669 thermal treatment Methods 0.000 description 3
- XJDNKRIXUMDJCW-UHFFFAOYSA-J titanium tetrachloride Chemical compound Cl[Ti](Cl)(Cl)Cl XJDNKRIXUMDJCW-UHFFFAOYSA-J 0.000 description 3
- ZSLUVFAKFWKJRC-IGMARMGPSA-N 232Th Chemical compound [232Th] ZSLUVFAKFWKJRC-IGMARMGPSA-N 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 2
- 238000002441 X-ray diffraction Methods 0.000 description 2
- 230000009471 action Effects 0.000 description 2
- 150000001339 alkali metal compounds Chemical class 0.000 description 2
- 229910000272 alkali metal oxide Inorganic materials 0.000 description 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 2
- 238000004458 analytical method Methods 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 2
- 229910052728 basic metal Inorganic materials 0.000 description 2
- 150000003818 basic metals Chemical class 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 235000011089 carbon dioxide Nutrition 0.000 description 2
- 239000003610 charcoal Substances 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 239000002131 composite material Substances 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 238000004821 distillation Methods 0.000 description 2
- 238000000227 grinding Methods 0.000 description 2
- IXCSERBJSXMMFS-UHFFFAOYSA-N hydrogen chloride Substances Cl.Cl IXCSERBJSXMMFS-UHFFFAOYSA-N 0.000 description 2
- 229910000041 hydrogen chloride Inorganic materials 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 238000001465 metallisation Methods 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- NDLPOXTZKUMGOV-UHFFFAOYSA-N oxo(oxoferriooxy)iron hydrate Chemical compound O.O=[Fe]O[Fe]=O NDLPOXTZKUMGOV-UHFFFAOYSA-N 0.000 description 2
- 230000004044 response Effects 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 239000007921 spray Substances 0.000 description 2
- 238000005728 strengthening Methods 0.000 description 2
- AKEJUJNQAAGONA-UHFFFAOYSA-N sulfur trioxide Chemical compound O=S(=O)=O AKEJUJNQAAGONA-UHFFFAOYSA-N 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 1
- VTLYFUHAOXGGBS-UHFFFAOYSA-N Fe3+ Chemical compound [Fe+3] VTLYFUHAOXGGBS-UHFFFAOYSA-N 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 229910000805 Pig iron Inorganic materials 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 1
- 229910052770 Uranium Inorganic materials 0.000 description 1
- QGQNBUCELYWKKL-UHFFFAOYSA-I [Cl+].[Cl-].[Ti+4].[Cl-].[Cl-].[Cl-].[Cl-] Chemical compound [Cl+].[Cl-].[Ti+4].[Cl-].[Cl-].[Cl-].[Cl-] QGQNBUCELYWKKL-UHFFFAOYSA-I 0.000 description 1
- HGWOWDFNMKCVLG-UHFFFAOYSA-N [O--].[O--].[Ti+4].[Ti+4] Chemical compound [O--].[O--].[Ti+4].[Ti+4] HGWOWDFNMKCVLG-UHFFFAOYSA-N 0.000 description 1
- 238000005273 aeration Methods 0.000 description 1
- 229910052783 alkali metal Inorganic materials 0.000 description 1
- 150000001340 alkali metals Chemical class 0.000 description 1
- 239000012670 alkaline solution Substances 0.000 description 1
- 229910000323 aluminium silicate Inorganic materials 0.000 description 1
- 239000012752 auxiliary agent Substances 0.000 description 1
- 239000002585 base Substances 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229910021538 borax Inorganic materials 0.000 description 1
- 239000011449 brick Substances 0.000 description 1
- 238000001354 calcination Methods 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 238000005266 casting Methods 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 229910052804 chromium Inorganic materials 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 239000004567 concrete Substances 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000001627 detrimental effect Effects 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000005189 flocculation Methods 0.000 description 1
- 230000016615 flocculation Effects 0.000 description 1
- 238000005243 fluidization Methods 0.000 description 1
- 230000004927 fusion Effects 0.000 description 1
- 238000005469 granulation Methods 0.000 description 1
- 230000003179 granulation Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 238000011835 investigation Methods 0.000 description 1
- -1 iron titanate compound Chemical class 0.000 description 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
- 238000009533 lab test Methods 0.000 description 1
- AXZKOIWUVFPNLO-UHFFFAOYSA-N magnesium;oxygen(2-) Chemical compound [O-2].[Mg+2] AXZKOIWUVFPNLO-UHFFFAOYSA-N 0.000 description 1
- 238000007885 magnetic separation Methods 0.000 description 1
- 150000007522 mineralic acids Chemical class 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000011085 pressure filtration Methods 0.000 description 1
- 238000002203 pretreatment Methods 0.000 description 1
- 229910052705 radium Inorganic materials 0.000 description 1
- 230000002829 reductive effect Effects 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 210000002966 serum Anatomy 0.000 description 1
- 229910052665 sodalite Inorganic materials 0.000 description 1
- 239000004328 sodium tetraborate Substances 0.000 description 1
- 235000010339 sodium tetraborate Nutrition 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 229910052721 tungsten Inorganic materials 0.000 description 1
- JFALSRSLKYAFGM-UHFFFAOYSA-N uranium(0) Chemical compound [U] JFALSRSLKYAFGM-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B34/00—Obtaining refractory metals
- C22B34/10—Obtaining titanium, zirconium or hafnium
- C22B34/12—Obtaining titanium or titanium compounds from ores or scrap by metallurgical processing; preparation of titanium compounds from other titanium compounds see C01G23/00 - C01G23/08
- C22B34/1236—Obtaining titanium or titanium compounds from ores or scrap by metallurgical processing; preparation of titanium compounds from other titanium compounds see C01G23/00 - C01G23/08 obtaining titanium or titanium compounds from ores or scrap by wet processes, e.g. by leaching
- C22B34/1254—Obtaining titanium or titanium compounds from ores or scrap by metallurgical processing; preparation of titanium compounds from other titanium compounds see C01G23/00 - C01G23/08 obtaining titanium or titanium compounds from ores or scrap by wet processes, e.g. by leaching using basic solutions or liquors
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B3/00—Extraction of metal compounds from ores or concentrates by wet processes
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B34/00—Obtaining refractory metals
- C22B34/10—Obtaining titanium, zirconium or hafnium
- C22B34/12—Obtaining titanium or titanium compounds from ores or scrap by metallurgical processing; preparation of titanium compounds from other titanium compounds see C01G23/00 - C01G23/08
- C22B34/1236—Obtaining titanium or titanium compounds from ores or scrap by metallurgical processing; preparation of titanium compounds from other titanium compounds see C01G23/00 - C01G23/08 obtaining titanium or titanium compounds from ores or scrap by wet processes, e.g. by leaching
- C22B34/124—Obtaining titanium or titanium compounds from ores or scrap by metallurgical processing; preparation of titanium compounds from other titanium compounds see C01G23/00 - C01G23/08 obtaining titanium or titanium compounds from ores or scrap by wet processes, e.g. by leaching using acidic solutions or liquors
- C22B34/125—Obtaining titanium or titanium compounds from ores or scrap by metallurgical processing; preparation of titanium compounds from other titanium compounds see C01G23/00 - C01G23/08 obtaining titanium or titanium compounds from ores or scrap by wet processes, e.g. by leaching using acidic solutions or liquors containing a sulfur ion as active agent
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Geology (AREA)
- Life Sciences & Earth Sciences (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Geochemistry & Mineralogy (AREA)
- Inorganic Compounds Of Heavy Metals (AREA)
- Manufacture And Refinement Of Metals (AREA)
Abstract
A process for upgrading a titaniferous material by removal of impurities from the titaniferous material is disclosed. The process comprises alternate leaching of the titaniferous material in a caustic leach and a pressure sulphuric acid leach.
Description
The present invention relates to remove from naturally occurring and synthetic titaniferous material the method for impurity, the present invention is particularly suited for improving the grade (grade) that is used for prepare the titaniferous material of metal titanium and TiO 2 pigment by industrial chlorination system.
The essential characteristic of embodiment of the present invention is to leach the grade that improves titaniferous material with alkali leaching and pressurization sulfuric acid, and this titaniferous material for example comes from the titanium-contained slag of hard rock ilmenite.As what hereinafter will introduce, also can adopt other additional step.
In industrial chloridization process, will contain titanium dioxide raw material and coke and together add in the dissimilar chlorinator (fluidized-bed, shaft furnace, molten salt bath), and reach 700-1200 ℃ of operation down in top temperature.The most general industrial chlorinator of a class is a fluidized bed type.Cl gas flow is converted into titanium tetrachloride gas through containing the charging of titanium dioxide and carbon with titanium dioxide, and this gas is discharged with exit flow and is condensed into liquid titanium tetrachloride then, is used for further purifying and handling.
The chlorination operation of carrying out in industrial chlorinator very is suitable for carrying out the pure titinium dioxide raw material and transforms to titanium tetrachloride.Yet the trouble that other charging things of great majority (being impurities in raw materials) cause can make chloridization process itself or make that the latter stage operation of condensation, purifying and waste treatment is complicated widely.In the subordinate list problem types that is run into is described.And every kind of charging thing that does not enter product has become the waste material that needs processing or dispose basically.The refuse that some charging thing (as: special metal, radioactive substance) causes belongs to the thing class that need carry out special disposal in the warehouse of monitoring is arranged.
Therefore preferred chlorination charging thing is high-grade material, and what suit the most in the raw material at present is that rutile ore (contains 95-96%TiO
2).Because of the rutile ore shortage has caused the exploitation of other raw material, these raw materials are by improving naturally occurring ilmenite (40-60%TiO
2), as titanium-contained slag (about 86%TiO
2) and artificial rutile (contain TiO
292-95% does not wait) grade form.Originally these methods that upgrade are the center to remove iron, remove magnesium, manganese and alkaline earth metal impurity but now expanded to, and remove some aluminium.Charging element chlorination condensation purifying Fe, Mn consumes chlorine, coke solid-liquid muriate
Increase the fluidization that gas volume blocks pipeline, slagging basic metal and liquid chloride retardance alkaline-earth metal fluidized-bed
Consumption chlorine, coke Al consume chlorine, coke causes that corrosion causes that burn into slagging Si accumulates in chlorinator, and can aggravate the pipeline resistance may require from product
Reduce furnace life, consume plug, with part four in distillation
Coke, chlorine titanium chloride condensation V together must be through chemical treatments
Or distillation removal Th, Ra accumulates on the chlorinator brick
On the body, radioactivity,
Bring the difficulty in the disposal
Utilize various technology from titaniferous material in the prior art,, made artificial rutile as ilmenite.According to as the most general technology extensively carried out in the western australia, be in rotary kiln with coal or charcoal reduction titaniferous material, used temperature is higher than 1100 ℃.Under this technology, the iron content part in the mineral is metallized substantially.Additive sulfur also is used for impurity manganese partly is converted into sulfide.After the reduction, this metallization product is cooled, and separates with the charcoal of association, and carries out water liquid inflation (aqueous aeration) subsequently contained whole metallic state iron are removed substantially with separable thin form of iron oxide.This isolating titanium products that contains is handled with the aqueous sulfuric acid of 2-5%, with dissolving manganese and some residual iron.The substantial chemistry that does not have to disclose or carry out basic metal or alkaline-earth metal, aluminium, silicon, vanadium or radionuclide in this method is removed.And the removal of iron and manganese is also incomplete.
Recently the someone has proposed a kind of technology, and it is reducing under lower temperature and is carrying out hydrochloric acid and leach after inflation of water liquid and ferric oxide separating step.According to described content, this technology can be removed aluminium charging thing and some vanadium and the thorium of iron, manganese, alkalies and alkaline earth impurity, significant proportion effectively.This technology can be used as a kind of innovation scheme and moves in existing stove class device.But this technology can not be removed vanadium fully effectively and silicon almost not had chemical action.
In the invention of another prior art, realized the removal of the higher degree of magnesium, manganese, iron and aluminium.In such technology, ilmenite at first usually in rotary kiln by thermal reduction, make its ferric oxide that contains reduce (promptly not having sizable metallization) substantially fully.Then with the refrigerative reduzate at 35psi (pound/inch
2) hydrochloric acid with excessive 20% under pressure and 140-150 ℃ leaches, to remove iron, magnesium, aluminium and manganese.Leach liquor is through the spray roasting hydrogenchloride of regenerating, and this hydrogenchloride is recycled to the leaching step.
In other technology, ilmenite carries out granularity refinement and adopts thermooxidizing, subsequent thermal reduction (in fluidized-bed or in rotary kiln).Then, the refrigerative reduzate is carried out normal pressure with 20% excessive hydrochloric acid leach, to remove detrimental impurity.In this technology, also realize the regeneration of acid by spray roasting.
In above-mentioned all these class technologies that leach with hydrochloric acid, the removal of impurity is similar.Can not remove vanadium, aluminium and silicon fully effectively.
Other has a technology, and ilmenite reduction with carbon in rotary kiln (not metallizing) is then in nonoxidizing atmosphere cooling down., under 20-30psi gauge pressure and 130 ℃, and promote the hydrolysis of dissolved titanium dioxide and promote then in the presence of the seed material that impurity leaches, having through the refrigerative reduzate with the sulfuric acid leaching of 10-60% (general 18-25%).In this technology, indicate acceptable salts acid substitution sulfuric acid.In this case, the removal of impurity is estimated with the effect of other hydrochloric acid leaching type system of employing similar.When adopting sulfuric acid, the removal of radioactive substance can be incomplete.
A kind of blanket method that makes ilmenite be upgraded to high-grade product is: add coke under 1500 ℃ of temperature ilmenite is melted in electric furnace surpassing, generate fusion titanium-contained slag (being used for casting or broken) and pig iron product.Problem is that this mode only can be with the removal of the iron in the impurity thereby very not comprehensive, and the result is the limitation that this technology has composition.
In another kind of technology, make to contain titanium ore in company with alkali metal compound roasting together, the strong acid with non-sulfuric acid leaches (Australian Patent AU-B-70976/87) subsequently.According to wherein said, can realize the substantial removal of various impurity, " substance " speech means greater than 10%.Under implication of the present invention, so few Impurity removal particularly for thorium and uranium impurity, can not become an effective means.This technology is not pointed out the concrete phase structure after the roasting, but the analytical results that provides (analyze differently with charging, product analysis is not summed up to 100%, and does not provide the alkali-metal analysis to being added) shows, and is remarkable in the amount retained of final product inner additive.Under this specified criteria, we can say that expectation can form the alkaline iron titanate compound that is unfavorable for that acidleach subsequently goes out.The final delay of alkali can make final product be unsuitable for the raw material as the muriate pigment production.
Also having a kind of technology is to replace to leach by a kind of inorganic acid aqueous solution with the aqueous solution of alkali metal compound and non-sulfuric acid to handle titanium ore (United States Patent (USP) 5085837).This technology is confined to especially at mineral and concentrate, and does not have to consider to be intended to people's pre-treatment of phase structure for a change.Thereby this technology even, and can not produce the raw material that is used to prepare muriate pigment economically for the effect that obtains part also needs to use excess reagent and harsh operational condition.
There is multiple available material to upgrade and becomes the material that is suitable for the high content of titanium dioxide of chlorating.Adopt and produce the example that the existing technology that is suitable for the chlorating material can't improve the primary titanium dioxide resource of its grade satisfactorily, comprise hard rock (non-landwaste) ilmenite, siliceous leucoxene, multiple primary (not weathering) ilmenite and a large amount of anatase octahedrite resources.Also have many these class available renewable sources (as: containing the titanium dioxide titanium slag).
Particularly for the high titaniferous material of silicon-dioxide, aluminum oxide and content of magnesia, titanium-contained slag such as being generated by hard rock ferrotianium mineral resources had not proposed a kind of effective ways that improve its grade in the past and had prepared the raw material that is used for industrial muriate pigment production flow process.Can not remove silicon-dioxide economically with above-mentioned technology; Aluminum oxide during heating treatment impels pseudobrookite-anosovite type ore deposit to form mutually with magnesium oxide jointly, and the leaching of the hydrochloric acid under the relative actual industrial condition in this ore deposit is disadvantageous; Silicon-dioxide, aluminum oxide and magnesian and deposit the raw material that the use that makes this class material is confined to sulfate pigment technology.Owing to wish that the pigment technology of the satisfied pigment demand that increases is chloride process, so this limitation is serious restriction comprehensively.
The titanium dioxide reserves major part of Que Rening is hard rock ilmenite form in the world.
Obviously, finding a kind of method that improves this class titaniferous material grade, is very valuable with its high-grade product of producing the raw material that is suitable for use as muriate pigment technology economically.
The present invention proposes the plant combination of step of a kind of multiplex (MUX), it can be combined with the more general technology that improves the titaniferous material grade, make these technologies can than its original processing more wide region raw material and generate higher-quality product.
For this reason, the present invention proposes a kind ofly to remove impurity and improve the method for titaniferous material grade, and this method comprises that the mode that leaches (caustic leach) and the leaching of pressurization sulfuric acid with alkali replaces leaching to material.
In a specific embodiments of the present invention, take the recycle base leach liquor by the alkali regeneration step of adding the lime precipitation Smecta (complex aluminosilicates) and the alkali lye of regenerating after the solid/liquid separation, even need be with excessive alkali when leaching, the present invention can guarantee that also the alkali leaching carries out cost-effectively.This Smecta subsequently with desire to loop back the regeneration alkali lye that leaches step and separate.
Handle in this way not only salic but also silica containing titaniferous material also not the someone propose, this paper will point out, only implement such technology under the specific operation condition, Smecta did not precipitate when alkali was leached.
Find unexpectedly, the concentration of silicon-dioxide, aluminum oxide, titanium dioxide and other impurity in the restriction alkali leaching liquor, promptly under low serum density, leach and, usually can avoid being formed on the Smecta that can generate when alkali lye leaches through the alkali leach liquor that circulates of regenerating.
Another unexpected discovery is that the Smecta that the alkali leaching stage forms can go out the stage in acidleach subsequently and other impurity is together effectively removed.Because in most of the cases, the silicon-dioxide in the titaniferous material can not be gone out to remove by acidleach, and this result is just particularly unexpected.
Like this, can carry out a kind of operation that comprises the simple process of two stage processing in another embodiment, Smecta formed and consumes when the subordinate phase acidleach goes out in the fs in this processing, and wherein acidleach goes out the stage and realizes the removal of silicon-dioxide and also be combined with other advantage that acidleach in the general technology that upgrades goes out step.
Specifically, formation and the difficulty or ease of acidleach removal when the going out ratio (it determine this silico-aluminate be sodalite type or other form) that depend in leach liquor alkali and silicon-dioxide of Smecta when alkali leaches, alkali is then removed easily with the ratio height of silicon-dioxide.Therefore, leach and add the alkali leaching liquor circulation of the follow-up pressurization sulfuric acid leaching of alkali liquid regeneration (lime keeps the ratio of high-alkali and silicon-dioxide) of lime through alkali, all be a kind of titaniferous material that improves very effectively in many cases, the method for the titaniferous material grade that generates by the hard rock ilmenite particularly.
Have been found that the inventive method can remove iron, magnesium, aluminium, silicon, calcium, magnesium, manganese, phosphorus, chromium and vanadium, these impurity have constituted the impurity of nearly all type in the hard rock ilmenite mineral resources of titanium dioxide.
This technology when needed also can be in conjunction with some additional steps, for example:
(1) titaniferous material is before leaching, can be in the equipment of any suitable and under oxidation or reductive condition roasting to any temperature.For strengthening this material to the response of leaching step or reduce the generation of sulfurous gas when leaching, this roasting can be carried out with any titanous oxide compound in the oxidation titaniferous material.
(2) for strengthening this material to the response of leaching step or be other purpose, can in titaniferous material, add additive before in such roasting.
(3) pre-grinding to be improving speed of reaction before this titaniferous material can or leach in roasting, or can pre-grinding when preparing to carry out some agglomeration step, and this agglomeration step is improved by caused the size-grade distribution of broad in material to be reunited.
(4) can carry out an agglomeration step and make before the roasting blast blending in titaniferous material.
(5) for the physical sepn of the material of further upgrading (magnetic separation as final product separates, be used for selective removal and reclaim rich iron substance).
(6) the final titanium products that contains can be reunited with the technology of any suitable, make its size composition be suitable for the market requirement of artificial rutile.Product after the reunion is fired being enough to generate under the temperature of sinter bonded (sintered bonds), thereby has exempted the dust loss in the fluidized bed chlorination device.
(7) no matter whether final product reunites all can be calcined, to remove volatile matter (as water, sulfurous gas and sulphur trioxide).
(8) can carry out that alkaline solution discharges or the step of spent liquor evaporation (to remove washing water).
(9) sulfuric acid can be leached the liquid effluent neutralization, generate solid-state vitriol and oxyhydroxide so that dispose.
(10) this sulfuric acid leaching liquid effluent can be treated, is regenerated as sulfuric acid by the sulfate solution that forms in this technology.
(11) other leaching step, filtration step and washing step can be incorporated into this technology as required.For example, carry out hydrochloric acid and leach the radioactive substance that may assist in removing trace.Sedimentary Smecta when alkali lye reclaims is carried out pressure filtration help solid/liquid separation.
(12) available flocculation agent or other auxiliary agent promote solid/liquid separation.
Embodiment
Following embodiment has recorded and narrated some laboratory tests, is used for illustrating the techniques described herein.Embodiment 1
This embodiment is used for proof: the treatment process that is considered to effectively to improve other titaniferous material grade is invalid for the material such as the titanium-contained slag that generates from the hard rock ilmenite.
Make and form industrial titanium-contained slag as shown in table 1 oxidizing roasting 30 minutes under 750 ℃ and air, subsequently under the mixed atmosphere of 1: 3 hydrogen and carbonic acid gas (volume ratio) in 680 ℃ of reducing roastings 1 hour.Do not contain ferric iron and titanous oxide compound after the heat treated product cooling.X-ray diffraction shows that the phase composite of this material is a pseudobrookite.
Pulp density with 10% in 10% backflow caustic soda solution leaches this heat treated material.The composition of the solid residue after filtering and washing is as shown in table 2.
Clearly, alkali leaches silicon-dioxide or the not significantly influence of alumina content for this material.
The resistates that backflow hydrochloric acid with 20% leaches this alkali with 30% pulp density carries out leaching in 6 hours.The composition of the solid residue after filtering and washing is also listed in table 2.
Obviously, adopt 10% caustic soda, as the roasting/extract technology of leaching agent the grade that improves this slag charge is almost had no effect with 30% pulp density with 20% hydrochloric acid again with 10% pulp density.Embodiment 2
Repeat the treatment step shown in the embodiment 1, different is alkali to be leached pressurize under 165 ℃ to carry out.
Be shown in table 3 through the composition that alkali leaches and acidleach goes out after product.Obviously, alkali leaches the not obviously influence of content for silicon-dioxide or aluminum oxide in this material.Yet, although going out far, acidleach can not generate the high-grade material that is suitable for muriate pigment technology effectively, it has substantial effect to silicon-dioxide and alumina content really.
Directly carry out not seeing this influence in the slag specimen that hydrochloric acid leaches.
Obviously, pressurization alkali leaches the state that has changed silicon-dioxide, makes it be able to remove when hydrochloric acid leaching subsequently, but can't reach direct removal.Investigation shows that alkali has generated the Smecta precipitation when leaching.It is silicon-dioxide is leached but carry out under the undissolved condition that alkali leaches.
The result of present embodiment combines with the result who has realized the subsequent embodiment that effective alkali leaches, and leaching condition was depended in the removal of silicon-dioxide and aluminum oxide when the alkali leaching can be described.Embodiment 3
Mix with 2% borax forming slag specimen as shown in table 1, granulation is also carried out 2 hours reducing roasting under 19: 1 hydrogen and carbonic acid gas (volume ratio) mixed atmosphere and 1000 ℃.X-ray diffraction shows that the ore deposit phase composite of this thermal treatment postcooling product is a pseudobrookite.
This thermal treatment material sample is leached with 5% pulp density with 10% backflow caustic soda solution.The composition that filters and wash the back solid residue is as shown in table 4.Obviously, this alkali leaches very effective for the removal of silicon-dioxide, although the leaching of carrying out with 10% pulp density in embodiment 1 performance is very poor, has wherein generated Smecta.
Alkali is leached resistates 150 ℃ of pressurization leachings of carrying out 6 hours down with 20% sulfuric acid with 5% pulp density.The composition that filters and wash the back solid residue also is shown in table 4.
Obviously, low pulp density alkali leaches with the comprehensive action of follow-up pressurization sulfuric acid leaching (it can decompose pseudobrookite) and substantially this slag charge is improved into the very high-grade product that has been suitable for use as muriate pigment production raw material on the component.
Keep above-mentioned alkali and leach the leach liquor that obtains and use lime treatment in small, broken bits after analyzing, this lime uses with the weight ratio of 1.3 parts of lime with every part of dissolved silicon-dioxide.Filter and remove Smecta precipitation and any excessive lime that generates, the alkali lye that keeps " regeneration " is used further to leach.
With this regenerated alkali lye with identical condition noted earlier under this heat treated another material sample is leached.There is not any concluding difference with fresh alkali lye result who leaches and the result who leaches with regeneration alkali lye.Embodiment 4
This embodiment is intended to instruction book, and to come out from titaniferous material by acidleach be invalid such as removing silicon-dioxide the titanium-contained slag that is generated by the hard rock ilmenite.
With form industrial titanium-contained slag as shown in table 1 in the hydrogen of 1: 19 (volume ratio) and carbon dioxide mix atmosphere in 1000 ℃ of roastings two hours.Under calcination atmosphere after the cooling, in 20% sulfuric acid, leaching 6 hours under 135 ℃ with the slag charge pressurization after to this roasting of the pulp density of 25%W/W (w/w).
Table 5 provides the composition of this leaching resistates.Can expect, this direct acidleach of roasting titaniferous material is not gone out to handle and can bring anything to improve to product quality, can not remove SiO
2Embodiment 5
With with embodiment 3 described identical leaching steps to not adding additive and handling without any heat treated slag specimen.
The composition of final product is listed in table 6.Also realized the substance removal of impurity without thermal treatment.
Table 1: the composition that is used for the titanium slag of embodiment 1-4
Weight %
TiO
2 78.9
FeO 8.94
MgO 4.73
MnO 0.25
Cr
2O
3 0.16
V
2O
5 0.56
Al
2O
3 3.14
SiO
2 2.71
ZrO
2 0.05
CaO 0.42
The product of table 2: embodiment 1 is formed weight % alkali leaching acidleach and is gone out TiO
278.6 80.8FeO 9.22 7.4MgO 4.71 4.69MnO 0.24 0.23Cr
2O
30.16 0.16V
2O
50.59 0.59Al
2O
33.09 3.06SiO
22.94 2.86ZrO
20.05 0.04CaO 0.37 0.16
The product of table 3: embodiment 2 is formed weight % alkali leaching acidleach and is gone out TiO
278.4 82.7FeO 9.13 7.66MgO 4.76 4.81MnO 0.25 0.23Cr
2O
30.16 0.16V
2O
50.58 0.60Al
2O
33.08 2.73SiO
23.13 0.96ZrO
20.05 0.04CaO 0.40 0.13
The product of table 4: embodiment 3 is formed weight % alkali leaching acidleach and is gone out TiO
281.3 97.9FeO 9.56 0.89MgO 4.96 0.44MnO 0.27 0.02Cr
2O
30.20 0.12V
2O
50.57 0.12Al
2O
31.75 0.23SiO
20.73 0.09ZrO
20.05 0.06CaO 0.45 0.003
The product of table 5: embodiment 4 is formed
Weight % acidleach goes out
TiO
2 84.93
FeO 6.09
MgO 2.92
MnO 0.16
Cr
2O
3 0.16
V
2O
5 0.60
Al
2O
3 1.33
SiO
2 3.15
ZrO
2 0.06
CaO 0.03
The product of table 6: embodiment 5 is formed
Weight % acidleach goes out
TiO
2 92.1
FeO 2.98
MgO 1.21
MnO 0.08
Cr
2O
3 0.16
V
2O
5 0.18
Al
2O
3 0.60
SiO
2 0.71
ZrO
2 0.06
CaO 0.003
Claims (13)
1, a kind ofly remove the impurity in the titaniferous material and improve the method for this titaniferous material grade, this method comprises and this material is hocketed alkali leaches and pressurization sulfuric acid leaches.
2, carried out before this acidleach goes out according to the process of claim 1 wherein that this alkali leaches.
3, carry out according to the process of claim 1 wherein that this acidleach went out before this alkali leaches.
4,, wherein under 100 ℃, carry out acidleach at least and go out according to the method for aforementioned arbitrary claim.
5,, wherein under 135 ℃, carry out acidleach at least and go out according to the method for claim 4.
6,,, make Smecta with controlled and need mode to precipitate comprising control alkali leaching condition according to the method for aforementioned arbitrary claim.
7,, be included in and carry out alkali under the low pulp density condition and leach, to avoid the Smecta precipitation according to each method among the claim 1-5.
8, according to the method for claim 7, wherein this pulp density is lower than 10%.
9,, also comprise the leaching resistates is separated with alkali leaching liquor and the alkali leaching liquor of regenerating with the precipitation Smecta according to the method for claim 7 or 8.
10,, also comprise the regenerated alkali leaching liquor is separated with sedimentary Smecta, and make regenerated leach liquor be circulated to alkali leaching step according to the method for claim 9.
11, according to the method for aforementioned arbitrary claim, wherein this titaniferous material comprises the titanium-contained slag that is generated by the hard rock ilmenite.
12, a kind of method that improves this titaniferous material grade by the impurity in the titaniferous material of hard rock ilmenite generation of removing, this method comprises:
(a) under the selected alkali leaching condition that is used for precipitating Smecta, leach this material;
(b) separate this alkali leaching resistates in this alkali leaching liquor certainly; And
(c) the alkali leaching resistates to step (b) pressurizes the sulfuric acid leaching to remove this Smecta and other impurity, forms high-grade material.
13, a kind of method that improves the grade of this titaniferous material by the impurity in the titaniferous material of hard rock ilmenite generation of removing, this method comprises;
(a) alkali leaches this material;
(b) isolate this alkali leaching resistates in this alkali leaching liquor certainly;
(c) the alkali leaching resistates to step (b) pressurizes the sulfuric acid leaching to remove Smecta and other impurity, forms high-grade material;
(d) make the alkali leaching liquor regeneration of step (b) gained be suitable for effectively carrying out step (a) and regeneration alkali leaching liquor (c) by the precipitation Smecta with generation; And
(e) alkali leaching liquor of should regenerating is circulated to step (a).
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| AUPM1051 | 1993-09-07 | ||
| AUPM105193 | 1993-09-07 |
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| Publication Number | Publication Date |
|---|---|
| CN1134730A true CN1134730A (en) | 1996-10-30 |
| CN1042349C CN1042349C (en) | 1999-03-03 |
Family
ID=3777178
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN94194061A Expired - Fee Related CN1042349C (en) | 1993-09-07 | 1994-09-07 | Upgrading titaniferous materials |
Country Status (7)
| Country | Link |
|---|---|
| EP (1) | EP0717783A4 (en) |
| JP (1) | JPH09504828A (en) |
| CN (1) | CN1042349C (en) |
| CA (1) | CA2171185A1 (en) |
| NO (1) | NO317932B1 (en) |
| WO (1) | WO1995007366A1 (en) |
| ZA (1) | ZA946864B (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1060817C (en) * | 1997-08-08 | 2001-01-17 | 杨道光 | Electrolytic separating process for ilmenite |
| CN103834798A (en) * | 2012-11-26 | 2014-06-04 | 贵阳铝镁设计研究院有限公司 | Method for preparing titanium-rich material from low-grade TiO2 slag |
| CN103952533A (en) * | 2014-04-23 | 2014-07-30 | 鞍钢集团矿业公司 | Method for recleaning vanadium-titanium magnetite concentrate by calcining, alkaline leaching and desliming |
| CN103966423A (en) * | 2014-04-23 | 2014-08-06 | 鞍钢集团矿业公司 | Method for re-concentrating vanadium-titanium magnetite concentrate through alkaline leaching, acid pickling and re-selection |
| CN104828864A (en) * | 2015-05-26 | 2015-08-12 | 昆明冶金研究院 | Process for making artificial rutile by leaching of mohsite hydrochloric acid |
Families Citing this family (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| AUPM511894A0 (en) * | 1994-04-15 | 1994-05-12 | Technological Resources Pty Limited | Treatment of leach liquors for upgrading a titaniferous material |
| US6627165B2 (en) * | 1994-04-15 | 2003-09-30 | Technological Resources Pty Ltd | Process for upgrading a titaniferous material containing silica |
| AUPM511994A0 (en) * | 1994-04-15 | 1994-05-12 | Technological Resources Pty Limited | Leaching of a titaniferous material |
| WO2005024074A1 (en) * | 2003-09-05 | 2005-03-17 | Promet Engineers Pty Ltd | Process for extracting crystalline titanium oxides |
| WO2007052801A1 (en) * | 2005-11-07 | 2007-05-10 | Tohoku University | Method for extraction of rutile |
| RU2592655C2 (en) * | 2014-12-24 | 2016-07-27 | Федеральное государственное бюджетное учреждение науки Объединенный институт высоких температур Российской академии наук (ОИВТ РАН) | Method of thermochemical processing of rare metal raw material |
| RU2623564C1 (en) * | 2016-04-25 | 2017-06-27 | Федеральное государственное бюджетное учреждение науки Институт металлургии и материаловедения им. А.А. Байкова Российской академии наук (ИМЕТ РАН) | Method of processing leukoxene concentrate |
Family Cites Families (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE276025C (en) * | ||||
| GB711833A (en) * | 1949-03-03 | 1954-07-14 | Nat Titanium Pigments Ltd | Improved manufacture of titanium compounds |
| IT1030645B (en) * | 1974-10-04 | 1979-04-10 | Sir Soc Italiana Resine Spa | PROCEDURE FOR THE PRODUCTION OF TITANIUM DIOXIDE |
| US4176159A (en) * | 1976-11-15 | 1979-11-27 | Mendonca Paulo Ayres Falcao De | Process for concentration of titanium containing anatase ore |
| ZA781126B (en) * | 1977-03-09 | 1979-01-31 | Mineracao Vale Paranaiba Sa Va | Method for obtaining high tio2 grade anatase concentrates from lower tio2 grade anatase concentrates |
| JPH01301518A (en) * | 1988-05-28 | 1989-12-05 | Sakai Chem Ind Co Ltd | Production of titanium dioxide |
| US5011666A (en) * | 1988-07-28 | 1991-04-30 | E. I. Du Pont De Nemours And Company | Method for purifying TiO2 ore |
| DE3912554C1 (en) * | 1989-04-17 | 1990-07-12 | Bayer Ag, 5090 Leverkusen, De | |
| ZA911515B (en) * | 1990-03-02 | 1991-12-24 | Wimmera Ind Minerals Pty Ltd | Production of synthetic rutile |
| US5063032A (en) * | 1990-03-27 | 1991-11-05 | Qit-Fer Et Titane, Inc. | Method of preparing a synthetic rutile from a titaniferous slag containing magnesium values |
| AU639390B2 (en) * | 1991-04-19 | 1993-07-22 | Rgc Mineral Sands Limited | Removal of radionuclides from titaniferous material |
| AU1498092A (en) * | 1991-04-19 | 1992-10-22 | Rgc Mineral Sands Limited | Removal of radionuclides from titaniferous material |
-
1994
- 1994-09-07 CN CN94194061A patent/CN1042349C/en not_active Expired - Fee Related
- 1994-09-07 ZA ZA946864A patent/ZA946864B/en unknown
- 1994-09-07 EP EP94926722A patent/EP0717783A4/en not_active Withdrawn
- 1994-09-07 JP JP7508358A patent/JPH09504828A/en active Pending
- 1994-09-07 WO PCT/AU1994/000528 patent/WO1995007366A1/en not_active Application Discontinuation
- 1994-09-07 CA CA002171185A patent/CA2171185A1/en not_active Abandoned
-
1996
- 1996-03-06 NO NO19960917A patent/NO317932B1/en unknown
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1060817C (en) * | 1997-08-08 | 2001-01-17 | 杨道光 | Electrolytic separating process for ilmenite |
| CN103834798A (en) * | 2012-11-26 | 2014-06-04 | 贵阳铝镁设计研究院有限公司 | Method for preparing titanium-rich material from low-grade TiO2 slag |
| CN103834798B (en) * | 2012-11-26 | 2015-11-18 | 贵阳铝镁设计研究院有限公司 | By low-grade TiO 2slag prepares the method for rich titanium material |
| CN103952533A (en) * | 2014-04-23 | 2014-07-30 | 鞍钢集团矿业公司 | Method for recleaning vanadium-titanium magnetite concentrate by calcining, alkaline leaching and desliming |
| CN103966423A (en) * | 2014-04-23 | 2014-08-06 | 鞍钢集团矿业公司 | Method for re-concentrating vanadium-titanium magnetite concentrate through alkaline leaching, acid pickling and re-selection |
| CN103952533B (en) * | 2014-04-23 | 2016-01-20 | 鞍钢集团矿业公司 | Calcining, alkali leaching and desliming is utilized to select the method for v-ti magnetite concentrate again |
| CN103966423B (en) * | 2014-04-23 | 2016-02-03 | 鞍钢集团矿业公司 | Alkali leaching, pickling and gravity treatment is utilized to select the method for v-ti magnetite concentrate again |
| CN104828864A (en) * | 2015-05-26 | 2015-08-12 | 昆明冶金研究院 | Process for making artificial rutile by leaching of mohsite hydrochloric acid |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH09504828A (en) | 1997-05-13 |
| NO960917D0 (en) | 1996-03-06 |
| EP0717783A4 (en) | 1997-04-23 |
| CA2171185A1 (en) | 1995-03-16 |
| NO960917L (en) | 1996-04-25 |
| WO1995007366A1 (en) | 1995-03-16 |
| CN1042349C (en) | 1999-03-03 |
| EP0717783A1 (en) | 1996-06-26 |
| NO317932B1 (en) | 2005-01-10 |
| ZA946864B (en) | 1995-09-04 |
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