CN113981491B - Method for preparing metallic beryllium by low-temperature molten salt electrolysis - Google Patents
Method for preparing metallic beryllium by low-temperature molten salt electrolysis Download PDFInfo
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- CN113981491B CN113981491B CN202111562341.4A CN202111562341A CN113981491B CN 113981491 B CN113981491 B CN 113981491B CN 202111562341 A CN202111562341 A CN 202111562341A CN 113981491 B CN113981491 B CN 113981491B
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- beryllium
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- cathode
- chloride
- anode
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- ATBAMAFKBVZNFJ-UHFFFAOYSA-N beryllium atom Chemical compound [Be] ATBAMAFKBVZNFJ-UHFFFAOYSA-N 0.000 title claims abstract description 144
- 229910052790 beryllium Inorganic materials 0.000 title claims abstract description 141
- 238000005868 electrolysis reaction Methods 0.000 title claims abstract description 56
- 238000000034 method Methods 0.000 title claims abstract description 51
- 150000003839 salts Chemical class 0.000 title claims abstract description 33
- 229910052751 metal Inorganic materials 0.000 claims abstract description 74
- 239000002184 metal Substances 0.000 claims abstract description 74
- 239000003792 electrolyte Substances 0.000 claims abstract description 52
- 229910045601 alloy Inorganic materials 0.000 claims abstract description 49
- 239000000956 alloy Substances 0.000 claims abstract description 49
- 239000002994 raw material Substances 0.000 claims abstract description 39
- 239000007788 liquid Substances 0.000 claims abstract description 36
- 239000007787 solid Substances 0.000 claims abstract description 23
- 229910052710 silicon Inorganic materials 0.000 claims abstract description 15
- 239000010703 silicon Substances 0.000 claims abstract description 15
- 239000012752 auxiliary agent Substances 0.000 claims abstract description 9
- 229910001423 beryllium ion Inorganic materials 0.000 claims abstract description 7
- 230000005684 electric field Effects 0.000 claims abstract description 3
- LWBPNIJBHRISSS-UHFFFAOYSA-L beryllium dichloride Chemical compound Cl[Be]Cl LWBPNIJBHRISSS-UHFFFAOYSA-L 0.000 claims description 46
- FRWYFWZENXDZMU-UHFFFAOYSA-N 2-iodoquinoline Chemical compound C1=CC=CC2=NC(I)=CC=C21 FRWYFWZENXDZMU-UHFFFAOYSA-N 0.000 claims description 37
- LTPBRCUWZOMYOC-UHFFFAOYSA-N beryllium oxide Inorganic materials O=[Be] LTPBRCUWZOMYOC-UHFFFAOYSA-N 0.000 claims description 37
- 229910001627 beryllium chloride Inorganic materials 0.000 claims description 23
- JZKFIPKXQBZXMW-UHFFFAOYSA-L beryllium difluoride Chemical compound F[Be]F JZKFIPKXQBZXMW-UHFFFAOYSA-L 0.000 claims description 20
- 229910001633 beryllium fluoride Inorganic materials 0.000 claims description 20
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 18
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 claims description 18
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 claims description 15
- 229910052737 gold Inorganic materials 0.000 claims description 15
- 239000010931 gold Substances 0.000 claims description 15
- 229910002804 graphite Inorganic materials 0.000 claims description 14
- 239000010439 graphite Substances 0.000 claims description 14
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims description 10
- WCUXLLCKKVVCTQ-UHFFFAOYSA-M Potassium chloride Chemical compound [Cl-].[K+] WCUXLLCKKVVCTQ-UHFFFAOYSA-M 0.000 claims description 10
- HSZCZNFXUDYRKD-UHFFFAOYSA-M lithium iodide Chemical compound [Li+].[I-] HSZCZNFXUDYRKD-UHFFFAOYSA-M 0.000 claims description 10
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 9
- 229910052802 copper Inorganic materials 0.000 claims description 9
- 239000010949 copper Substances 0.000 claims description 9
- NLKNQRATVPKPDG-UHFFFAOYSA-M potassium iodide Chemical compound [K+].[I-] NLKNQRATVPKPDG-UHFFFAOYSA-M 0.000 claims description 9
- 239000011780 sodium chloride Substances 0.000 claims description 9
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 claims description 8
- PQXKHYXIUOZZFA-UHFFFAOYSA-M lithium fluoride Chemical group [Li+].[F-] PQXKHYXIUOZZFA-UHFFFAOYSA-M 0.000 claims description 8
- FUJCRWPEOMXPAD-UHFFFAOYSA-N lithium oxide Chemical compound [Li+].[Li+].[O-2] FUJCRWPEOMXPAD-UHFFFAOYSA-N 0.000 claims description 8
- 229910001947 lithium oxide Inorganic materials 0.000 claims description 8
- FGDZQCVHDSGLHJ-UHFFFAOYSA-M rubidium chloride Chemical compound [Cl-].[Rb+] FGDZQCVHDSGLHJ-UHFFFAOYSA-M 0.000 claims description 8
- 229910052709 silver Inorganic materials 0.000 claims description 8
- 239000004332 silver Substances 0.000 claims description 8
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 6
- QVQLCTNNEUAWMS-UHFFFAOYSA-N barium oxide Chemical compound [Ba]=O QVQLCTNNEUAWMS-UHFFFAOYSA-N 0.000 claims description 6
- AMXOYNBUYSYVKV-UHFFFAOYSA-M lithium bromide Chemical compound [Li+].[Br-] AMXOYNBUYSYVKV-UHFFFAOYSA-M 0.000 claims description 6
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical group [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 claims description 6
- IOLCXVTUBQKXJR-UHFFFAOYSA-M potassium bromide Chemical compound [K+].[Br-] IOLCXVTUBQKXJR-UHFFFAOYSA-M 0.000 claims description 6
- FVAUCKIRQBBSSJ-UHFFFAOYSA-M sodium iodide Chemical compound [Na+].[I-] FVAUCKIRQBBSSJ-UHFFFAOYSA-M 0.000 claims description 6
- BRPQOXSCLDDYGP-UHFFFAOYSA-N calcium oxide Chemical compound [O-2].[Ca+2] BRPQOXSCLDDYGP-UHFFFAOYSA-N 0.000 claims description 5
- 239000000292 calcium oxide Substances 0.000 claims description 5
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium oxide Inorganic materials [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 claims description 5
- 229910052759 nickel Inorganic materials 0.000 claims description 5
- 239000001103 potassium chloride Substances 0.000 claims description 5
- 235000011164 potassium chloride Nutrition 0.000 claims description 5
- TWRXJAOTZQYOKJ-UHFFFAOYSA-L Magnesium chloride Chemical compound [Mg+2].[Cl-].[Cl-] TWRXJAOTZQYOKJ-UHFFFAOYSA-L 0.000 claims description 4
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 claims description 4
- 239000010405 anode material Substances 0.000 claims description 4
- XJHCXCQVJFPJIK-UHFFFAOYSA-M caesium fluoride Chemical compound [F-].[Cs+] XJHCXCQVJFPJIK-UHFFFAOYSA-M 0.000 claims description 4
- 229910052748 manganese Inorganic materials 0.000 claims description 4
- 239000011572 manganese Substances 0.000 claims description 4
- NROKBHXJSPEDAR-UHFFFAOYSA-M potassium fluoride Chemical compound [F-].[K+] NROKBHXJSPEDAR-UHFFFAOYSA-M 0.000 claims description 4
- JAAGVIUFBAHDMA-UHFFFAOYSA-M rubidium bromide Chemical compound [Br-].[Rb+] JAAGVIUFBAHDMA-UHFFFAOYSA-M 0.000 claims description 4
- 229940102127 rubidium chloride Drugs 0.000 claims description 4
- AHLATJUETSFVIM-UHFFFAOYSA-M rubidium fluoride Chemical compound [F-].[Rb+] AHLATJUETSFVIM-UHFFFAOYSA-M 0.000 claims description 4
- WFUBYPSJBBQSOU-UHFFFAOYSA-M rubidium iodide Chemical compound [Rb+].[I-] WFUBYPSJBBQSOU-UHFFFAOYSA-M 0.000 claims description 4
- DVMZCYSFPFUKKE-UHFFFAOYSA-K scandium chloride Chemical compound Cl[Sc](Cl)Cl DVMZCYSFPFUKKE-UHFFFAOYSA-K 0.000 claims description 4
- JHJLBTNAGRQEKS-UHFFFAOYSA-M sodium bromide Chemical compound [Na+].[Br-] JHJLBTNAGRQEKS-UHFFFAOYSA-M 0.000 claims description 4
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 claims description 3
- 229920000049 Carbon (fiber) Polymers 0.000 claims description 3
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 claims description 3
- 229910052782 aluminium Inorganic materials 0.000 claims description 3
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 3
- 239000001110 calcium chloride Substances 0.000 claims description 3
- 229910001628 calcium chloride Inorganic materials 0.000 claims description 3
- 239000004917 carbon fiber Substances 0.000 claims description 3
- 229910021389 graphene Inorganic materials 0.000 claims description 3
- 229910052742 iron Inorganic materials 0.000 claims description 3
- 229910052750 molybdenum Inorganic materials 0.000 claims description 3
- 239000011733 molybdenum Substances 0.000 claims description 3
- 229910052697 platinum Inorganic materials 0.000 claims description 3
- CHWRSCGUEQEHOH-UHFFFAOYSA-N potassium oxide Chemical compound [O-2].[K+].[K+] CHWRSCGUEQEHOH-UHFFFAOYSA-N 0.000 claims description 3
- 229910001950 potassium oxide Inorganic materials 0.000 claims description 3
- BHXBZLPMVFUQBQ-UHFFFAOYSA-K samarium(iii) chloride Chemical compound Cl[Sm](Cl)Cl BHXBZLPMVFUQBQ-UHFFFAOYSA-K 0.000 claims description 3
- KKCBUQHMOMHUOY-UHFFFAOYSA-N sodium oxide Chemical compound [O-2].[Na+].[Na+] KKCBUQHMOMHUOY-UHFFFAOYSA-N 0.000 claims description 3
- 229910001948 sodium oxide Inorganic materials 0.000 claims description 3
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 claims description 2
- 229910052788 barium Inorganic materials 0.000 claims description 2
- DSAJWYNOEDNPEQ-UHFFFAOYSA-N barium atom Chemical compound [Ba] DSAJWYNOEDNPEQ-UHFFFAOYSA-N 0.000 claims description 2
- WDIHJSXYQDMJHN-UHFFFAOYSA-L barium chloride Chemical compound [Cl-].[Cl-].[Ba+2] WDIHJSXYQDMJHN-UHFFFAOYSA-L 0.000 claims description 2
- 229910001626 barium chloride Inorganic materials 0.000 claims description 2
- LYQFWZFBNBDLEO-UHFFFAOYSA-M caesium bromide Chemical compound [Br-].[Cs+] LYQFWZFBNBDLEO-UHFFFAOYSA-M 0.000 claims description 2
- AIYUHDOJVYHVIT-UHFFFAOYSA-M caesium chloride Chemical compound [Cl-].[Cs+] AIYUHDOJVYHVIT-UHFFFAOYSA-M 0.000 claims description 2
- XQPRBTXUXXVTKB-UHFFFAOYSA-M caesium iodide Chemical compound [I-].[Cs+] XQPRBTXUXXVTKB-UHFFFAOYSA-M 0.000 claims description 2
- 229910021393 carbon nanotube Inorganic materials 0.000 claims description 2
- 239000002041 carbon nanotube Substances 0.000 claims description 2
- 229910052804 chromium Inorganic materials 0.000 claims description 2
- 239000011651 chromium Substances 0.000 claims description 2
- 229910017052 cobalt Inorganic materials 0.000 claims description 2
- 239000010941 cobalt Substances 0.000 claims description 2
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 claims description 2
- ICAKDTKJOYSXGC-UHFFFAOYSA-K lanthanum(iii) chloride Chemical compound Cl[La](Cl)Cl ICAKDTKJOYSXGC-UHFFFAOYSA-K 0.000 claims description 2
- 229910001629 magnesium chloride Inorganic materials 0.000 claims description 2
- 239000000395 magnesium oxide Substances 0.000 claims description 2
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Inorganic materials [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 claims description 2
- AXZKOIWUVFPNLO-UHFFFAOYSA-N magnesium;oxygen(2-) Chemical compound [O-2].[Mg+2] AXZKOIWUVFPNLO-UHFFFAOYSA-N 0.000 claims description 2
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 claims description 2
- 229910052753 mercury Inorganic materials 0.000 claims description 2
- 239000011698 potassium fluoride Substances 0.000 claims description 2
- 235000003270 potassium fluoride Nutrition 0.000 claims description 2
- LHBNLZDGIPPZLL-UHFFFAOYSA-K praseodymium(iii) chloride Chemical compound Cl[Pr](Cl)Cl LHBNLZDGIPPZLL-UHFFFAOYSA-K 0.000 claims description 2
- 235000009518 sodium iodide Nutrition 0.000 claims description 2
- 229910001631 strontium chloride Inorganic materials 0.000 claims description 2
- AHBGXTDRMVNFER-UHFFFAOYSA-L strontium dichloride Chemical compound [Cl-].[Cl-].[Sr+2] AHBGXTDRMVNFER-UHFFFAOYSA-L 0.000 claims description 2
- WEQHQGJDZLDFID-UHFFFAOYSA-J thorium(iv) chloride Chemical compound Cl[Th](Cl)(Cl)Cl WEQHQGJDZLDFID-UHFFFAOYSA-J 0.000 claims description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 claims 1
- 229910052779 Neodymium Inorganic materials 0.000 claims 1
- ADVAFVCNOHMBDT-UHFFFAOYSA-L [Cl+].[Li+].[Cl-].[Cl-] Chemical compound [Cl+].[Li+].[Cl-].[Cl-] ADVAFVCNOHMBDT-UHFFFAOYSA-L 0.000 claims 1
- QEFYFXOXNSNQGX-UHFFFAOYSA-N neodymium atom Chemical compound [Nd] QEFYFXOXNSNQGX-UHFFFAOYSA-N 0.000 claims 1
- 238000004886 process control Methods 0.000 claims 1
- 238000002844 melting Methods 0.000 abstract description 8
- 230000008018 melting Effects 0.000 abstract description 8
- 229910052760 oxygen Inorganic materials 0.000 abstract description 6
- 239000001301 oxygen Substances 0.000 abstract description 6
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 5
- 238000005265 energy consumption Methods 0.000 abstract description 3
- 239000000463 material Substances 0.000 abstract description 2
- 238000005272 metallurgy Methods 0.000 abstract description 2
- 239000000203 mixture Substances 0.000 description 18
- KWGKDLIKAYFUFQ-UHFFFAOYSA-M lithium chloride Chemical compound [Li+].[Cl-] KWGKDLIKAYFUFQ-UHFFFAOYSA-M 0.000 description 14
- 238000004458 analytical method Methods 0.000 description 9
- 150000002500 ions Chemical class 0.000 description 7
- 229910052749 magnesium Inorganic materials 0.000 description 5
- 239000011777 magnesium Substances 0.000 description 5
- 230000005611 electricity Effects 0.000 description 4
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 3
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 3
- 229910052791 calcium Inorganic materials 0.000 description 3
- 239000011575 calcium Substances 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 238000002360 preparation method Methods 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 2
- 239000011195 cermet Substances 0.000 description 2
- 238000009792 diffusion process Methods 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 229910001234 light alloy Inorganic materials 0.000 description 2
- 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 2
- DDFHBQSCUXNBSA-UHFFFAOYSA-N 5-(5-carboxythiophen-2-yl)thiophene-2-carboxylic acid Chemical compound S1C(C(=O)O)=CC=C1C1=CC=C(C(O)=O)S1 DDFHBQSCUXNBSA-UHFFFAOYSA-N 0.000 description 1
- MIMUSZHMZBJBPO-UHFFFAOYSA-N 6-methoxy-8-nitroquinoline Chemical compound N1=CC=CC2=CC(OC)=CC([N+]([O-])=O)=C21 MIMUSZHMZBJBPO-UHFFFAOYSA-N 0.000 description 1
- KZBUYRJDOAKODT-UHFFFAOYSA-N Chlorine Chemical compound ClCl KZBUYRJDOAKODT-UHFFFAOYSA-N 0.000 description 1
- KRHYYFGTRYWZRS-UHFFFAOYSA-M Fluoride anion Chemical compound [F-] KRHYYFGTRYWZRS-UHFFFAOYSA-M 0.000 description 1
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- 229910001361 White metal Inorganic materials 0.000 description 1
- 229910001508 alkali metal halide Inorganic materials 0.000 description 1
- 150000001340 alkali metals Chemical class 0.000 description 1
- 229910001615 alkaline earth metal halide Inorganic materials 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- WPJWIROQQFWMMK-UHFFFAOYSA-L beryllium dihydroxide Chemical compound [Be+2].[OH-].[OH-] WPJWIROQQFWMMK-UHFFFAOYSA-L 0.000 description 1
- 229910001865 beryllium hydroxide Inorganic materials 0.000 description 1
- 238000009395 breeding Methods 0.000 description 1
- 230000001488 breeding effect Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000005660 chlorination reaction Methods 0.000 description 1
- 239000006258 conductive agent Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 238000003487 electrochemical reaction Methods 0.000 description 1
- 230000005672 electromagnetic field Effects 0.000 description 1
- 150000004673 fluoride salts Chemical class 0.000 description 1
- 229910052731 fluorine Inorganic materials 0.000 description 1
- 239000011737 fluorine Substances 0.000 description 1
- 238000004508 fractional distillation Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 229910052736 halogen Inorganic materials 0.000 description 1
- 150000002367 halogens Chemical class 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 150000008040 ionic compounds Chemical class 0.000 description 1
- RYZCLUQMCYZBJQ-UHFFFAOYSA-H lead(2+);dicarbonate;dihydroxide Chemical compound [OH-].[OH-].[Pb+2].[Pb+2].[Pb+2].[O-]C([O-])=O.[O-]C([O-])=O RYZCLUQMCYZBJQ-UHFFFAOYSA-H 0.000 description 1
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 1
- ATINCSYRHURBSP-UHFFFAOYSA-K neodymium(iii) chloride Chemical compound Cl[Nd](Cl)Cl ATINCSYRHURBSP-UHFFFAOYSA-K 0.000 description 1
- 238000001956 neutron scattering Methods 0.000 description 1
- -1 oxygen ions Chemical class 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 239000000523 sample Substances 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 239000010969 white metal Substances 0.000 description 1
Images
Classifications
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25C—PROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
- C25C3/00—Electrolytic production, recovery or refining of metals by electrolysis of melts
- C25C3/02—Electrolytic production, recovery or refining of metals by electrolysis of melts of alkali or alkaline earth metals
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25C—PROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
- C25C7/00—Constructional parts, or assemblies thereof, of cells; Servicing or operating of cells
- C25C7/005—Constructional parts, or assemblies thereof, of cells; Servicing or operating of cells of cells for the electrolysis of melts
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25C—PROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
- C25C7/00—Constructional parts, or assemblies thereof, of cells; Servicing or operating of cells
- C25C7/02—Electrodes; Connections thereof
- C25C7/025—Electrodes; Connections thereof used in cells for the electrolysis of melts
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25C—PROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
- C25C7/00—Constructional parts, or assemblies thereof, of cells; Servicing or operating of cells
- C25C7/06—Operating or servicing
-
- 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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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Electrolytic Production Of Metals (AREA)
Abstract
本发明公开了一种低温熔盐电解制备金属铍的方法,采用低温液态合金连接隔离状态的阳极工作区和阴极工作区,含铍原料进入阳极工作区,在低温下经电场电解作用,含铍原料被还原成金属铍并溶解进入低温液态合金,同时低温液态合金中的铍在阴极工作区被氧化成铍离子,后于阴极得电子还原沉积出固态金属铍。本发明在电解质中加入含氧类辅助剂,增加含铍原料的溶解性,可扩大含铍原料的适用范围,也可降低原料纯度要求低。本发明在液态合金中加入硅,增加了液态合金的流动性、降低其热膨胀性,极大地降低合金的熔点,使电解温度更低,能够降低电解能耗,减少铍的挥发损失。本发明工艺简单,且制得的金属铍纯度高,是铍冶金领域的一大创新。
The invention discloses a method for preparing metal beryllium by electrolysis of low-temperature molten salt. A low-temperature liquid alloy is used to connect an anode working area and a cathode working area in an isolated state, raw materials containing beryllium enter the anode working area, and are electrolyzed by an electric field at a low temperature to produce beryllium-containing materials. The raw material is reduced to metal beryllium and dissolved into the low-temperature liquid alloy. At the same time, the beryllium in the low-temperature liquid alloy is oxidized into beryllium ions in the cathode working area, and then the solid metal beryllium is deposited by electron reduction at the cathode. The present invention adds an oxygen-containing auxiliary agent into the electrolyte to increase the solubility of the beryllium-containing raw material, expand the application range of the beryllium-containing raw material, and reduce the requirement for low purity of the raw material. The invention adds silicon to the liquid alloy, which increases the fluidity of the liquid alloy, reduces its thermal expansion, greatly reduces the melting point of the alloy, lowers the electrolysis temperature, reduces electrolysis energy consumption, and reduces volatilization loss of beryllium. The process of the invention is simple, and the obtained metal beryllium has high purity, which is a great innovation in the field of beryllium metallurgy.
Description
技术领域technical field
本发明涉及一种低温熔盐电解制备金属铍的方法,属于铍冶金领域。The invention relates to a method for preparing metal beryllium by low-temperature molten salt electrolysis, which belongs to the field of beryllium metallurgy.
背景技术Background technique
铍是一种银白色金属,其对X-射线的可透性是铝的17倍,是制造X-光管窗口和放射性检测探头的唯一材料。金属铍中子俘获面很小,而中子散射截面很大,常用于制造中子增殖装置,反应堆的反射层、减速剂及核武器部件等。此外,铍可制成铍陀螺,广泛应用于航空航天领域。因此,铍是一种极具战略意义的金属。Beryllium is a silver-white metal that is 17 times more transparent to X-rays than aluminum, and is the only material used to make X-ray tube windows and radiation detection probes. Metal beryllium has a small neutron capture surface and a large neutron scattering cross section, and is often used in the manufacture of neutron breeding devices, reactor reflectors, moderators and nuclear weapon components. In addition, beryllium can be made into beryllium gyroscope, which is widely used in aerospace field. Therefore, beryllium is a metal of great strategic importance.
目前,大多数企业采用氟化铍镁热还原法生产金属铍,但也有少部分企业采用氯化铍电解法生产金属铍。氟化铍镁热还原法首先将氧化铍或氢氧化铍溶于氟化氢铵制取氟铍化铵,然后加热氟铍化铵使其分解,得到氟化铵和氟化铍,最后,用金属镁还原氟化铍得到金属铍,该方法在工业上应用普遍,但该方法为间歇操作,无法连续生产,同时,氟化铍制备工序繁琐,生产成本较高。氯化铍电解法则首先对氧化铍进行氯化得到氯化铍,然后对氯化铍进行电解制取金属铍。不同于氟化铍镁热还原法,该方法可以连续生产金属铍,但氯化铍的制取十分困难,因为氧化铍难以被氯化,需要引入碳,同时,氯化铍电解过程会产生氯气,污染环境。At present, most enterprises use beryllium fluoride magnesium thermal reduction method to produce metal beryllium, but there are also a small number of enterprises that use beryllium chloride electrolysis method to produce metal beryllium. Beryllium fluoride magnesium thermal reduction method first dissolves beryllium oxide or beryllium hydroxide in ammonium bifluoride to produce ammonium fluoroberyllium, then heats ammonium fluoroberyllium to decompose it to obtain ammonium fluoride and beryllium fluoride, and finally, use metal magnesium The method of reducing beryllium fluoride to obtain metal beryllium is widely used in industry, but the method is a batch operation and cannot be produced continuously. At the same time, the preparation process of beryllium fluoride is cumbersome and the production cost is relatively high. The beryllium chloride electrolysis method first chlorinates beryllium oxide to obtain beryllium chloride, and then electrolyzes beryllium chloride to obtain metal beryllium. Different from the magnesium thermal reduction method of beryllium fluoride, this method can continuously produce metal beryllium, but the preparation of beryllium chloride is very difficult, because beryllium oxide is difficult to be chlorinated, and carbon needs to be introduced. At the same time, chlorine gas will be generated during the electrolysis of beryllium chloride ,polluted environment.
美国专利US 1980378A公开了一种熔盐电解制取金属铍及其轻合金的方法,该方法以氟化物作为熔盐,将氟化铍或氧化铍溶解于氟化物熔盐中,电解制备铍或铍的轻合金。以氧化铍为原料时进行电解时,为保证氧化铍溶解,需严格控制氧化铍的添加速率,以氟化铍为原料进行电解时,阳极会析出氟气,对环境危害很大。U.S. Patent US 1980378A discloses a method for producing metal beryllium and its light alloys by electrolysis of molten salts. The method uses fluoride as a molten salt, dissolves beryllium fluoride or beryllium oxide in molten fluoride salts, and prepares beryllium or beryllium by electrolysis. Light alloys of beryllium. When using beryllium oxide as raw material for electrolysis, in order to ensure the dissolution of beryllium oxide, the addition rate of beryllium oxide must be strictly controlled. When using beryllium fluoride as raw material for electrolysis, fluorine gas will be precipitated at the anode, which is very harmful to the environment.
中国专利CN 109295309 B公开了一种氯化铍还原制备金属铍的方法,该方法利用钠或钾还原氯化铍制备金属铍,通过还原、分馏提纯两个步骤即可实现高纯金属铍的制备,但该法无法连续生产,同时,该方法需以氯化铍为原料,但如前文所述,氧化铍的氯化十分困难。Chinese patent CN 109295309 B discloses a method for preparing metal beryllium by reducing beryllium chloride. The method utilizes sodium or potassium to reduce beryllium chloride to prepare metal beryllium. The preparation of high-purity metal beryllium can be realized through two steps of reduction and fractional distillation. , but this method cannot be produced continuously. At the same time, this method needs to use beryllium chloride as a raw material, but as mentioned above, the chlorination of beryllium oxide is very difficult.
氯化铍、氟化铍之外,氧化铍也可用来制备金属铍。美国专利US 6811678 B2公开了一种电化学还原氧化铍制备金属铍的方法,该方法通过电解还原的方式首先在氧化铍阴极得到金属钙,金属钙紧接着与氧化铍发生反应,将氧化铍还原为金属铍,该法可连续生产,但金属钙会溶解在熔盐中,使得熔盐的电子导电性增加,导致电流效率下降,同时,还原得到的金属铍容易含有CaBe13杂质。中国专利CN 111235603 A公开了一种熔盐电脱氧制备金属铍的方法,该方法将氧化铍与造孔剂和导电剂混合均匀后制成阴极片,通电脱氧即可制得金属铍,但还原得到的金属铍会包裹在电极表面,对电极内部氧离子的扩散造成阻碍,导致电极内部的氧难以扩散出来,同时,该方法要求氧化铍的纯度在99%以上,对原料适应性较差。Besides beryllium chloride and beryllium fluoride, beryllium oxide can also be used to prepare metal beryllium. U.S. Patent No. 6,811,678 B2 discloses a method for preparing metal beryllium by electrochemical reduction of beryllium oxide. In this method, metallic calcium is first obtained at the cathode of beryllium oxide through electrolytic reduction, and then the metallic calcium reacts with beryllium oxide to reduce beryllium oxide. For metal beryllium, this method can be continuously produced, but metal calcium will dissolve in molten salt, which will increase the electronic conductivity of molten salt and cause a decrease in current efficiency. At the same time, the metal beryllium obtained by reduction will easily contain CaBe 13 impurities. Chinese patent CN 111235603 A discloses a method for preparing metal beryllium by electrodeoxidation of molten salt. In this method, beryllium oxide is uniformly mixed with a pore-forming agent and a conductive agent to make a cathode sheet. The obtained metal beryllium will be wrapped on the surface of the electrode, hindering the diffusion of oxygen ions inside the electrode, making it difficult for the oxygen inside the electrode to diffuse out. At the same time, this method requires the purity of beryllium oxide to be above 99%, which is poor in adaptability to raw materials.
发明内容Contents of the invention
针对现有技术的不足,本发明的目的是提供一种低温下高效制备金属铍的方法,该方法工艺简单,且制得的金属铍纯度高。Aiming at the deficiencies of the prior art, the purpose of the present invention is to provide a method for efficiently preparing metal beryllium at low temperature, the method has a simple process, and the obtained metal beryllium has high purity.
为了实现上述目的,本发明的技术方案是:In order to achieve the above object, technical scheme of the present invention is:
一种低温熔盐电解制备金属铍的方法,采用低温液态合金连接隔离状态的阳极工作区和阴极工作区,含铍原料进入阳极工作区,在低温下经电场电解作用,含铍原料被还原成金属铍并溶解进入低温液态合金,同时低温液态合金中的铍在阴极工作区被氧化成铍离子,后于阴极得电子还原沉积出固态金属铍。A method for preparing metal beryllium by low-temperature molten salt electrolysis, using a low-temperature liquid alloy to connect an isolated anode working area and a cathode working area, the beryllium-containing raw material enters the anode working area, and is electrolyzed by an electric field at a low temperature, and the beryllium-containing raw material is reduced to The metal beryllium is dissolved into the low-temperature liquid alloy, and at the same time, the beryllium in the low-temperature liquid alloy is oxidized into beryllium ions in the cathode working area, and then the solid metal beryllium is deposited by electron reduction at the cathode.
具体的,包括以下步骤:Specifically, the following steps are included:
(1)将电解槽分为阳极工作区和阴极工作区,阳极工作区和阴极工作区内均盛有电解质,电解槽底部还盛有低温液态合金;所述阳极工作区和阴极工作区的电解质互不接触而通过电解槽底部的低温液态合金相连接;(1) The electrolytic cell is divided into an anode work area and a cathode work area, the anode work area and the cathode work area are filled with electrolyte, and the bottom of the electrolytic cell is also filled with a low-temperature liquid alloy; the electrolyte in the anode work area and the cathode work area They are not in contact with each other but connected by the low-temperature liquid alloy at the bottom of the electrolytic cell;
(2)向阳极工作区中加入含铍原料,然后在阳极工作区和阴极工作区分别插入阳极和阴极,低温下通电,含铍原料在阳极工作区电解质与低温液态合金界面处被还原成金属铍并溶解进入低温液态合金,同时,低温液态合金中的铍在低温液态合金与阴极工作区电解质界面处被氧化成铍离子进入阴极电解质,并在阴极表面被还原成金属铍。(2) Add beryllium-containing raw materials into the anode working area, then insert the anode and cathode respectively in the anode working area and the cathode working area, and electrify at low temperature, and the beryllium-containing raw materials are reduced to metal at the interface between the electrolyte and the low-temperature liquid alloy in the anode working area The beryllium is dissolved into the cryogenic liquid alloy, and at the same time, the beryllium in the cryogenic liquid alloy is oxidized into beryllium ions at the interface between the cryogenic liquid alloy and the cathode working area electrolyte, enters the cathode electrolyte, and is reduced to metal beryllium on the surface of the cathode.
进一步,所述的低温<600℃。Further, the low temperature is <600°C.
进一步,所述低温液态合金含53-85at.%金、0-38at.%铍、0-20at.%硅,可含有铜、银、锰中一种或以上,其在<600℃下为液态。Further, the low-temperature liquid alloy contains 53-85 at.% gold, 0-38 at.% beryllium, 0-20 at.% silicon, and may contain one or more of copper, silver, and manganese, which is liquid at <600°C .
进一步,所述含铍原料为氧化铍、氟化铍、氯化铍中至少一种,含铍原料的纯度≥50%。Further, the beryllium-containing raw material is at least one of beryllium oxide, beryllium fluoride, and beryllium chloride, and the purity of the beryllium-containing raw material is ≥50%.
优选的,所述低温液态合金中含54-81at.%金、0.1-38at.%铍、6-18at.%硅。Preferably, the low-temperature liquid alloy contains 54-81 at.% gold, 0.1-38 at.% beryllium, and 6-18 at.% silicon.
进一步,电解过程控制方式为控制电流、控制电压的一种或以上;控制电流时,电流密度为0.01-1.0A/cm2,控制电压时,阴极电压为≤-2.5V(vs NHE)。Further, the electrolysis process is controlled by one or more of current control and voltage control; when controlling current, the current density is 0.01-1.0A/cm 2 , and when controlling voltage, the cathode voltage is ≤-2.5V (vs NHE).
进一步,所述阳极工作区和阴极工作区的电解质由熔盐电解质和辅助剂组成,辅助剂添加量≤10at.%。Further, the electrolyte in the anode working area and the cathode working area is composed of molten salt electrolyte and auxiliary agent, and the amount of auxiliary agent added is ≤10 at.%.
进一步,所述熔盐电解质为氟化锂、氟化钾、氟化铷、氟化铯、氟化铍、氯化锂、氯化钠、氯化钾、氯化铷、氯化铯、氯化铍、氯化镁、氯化钙、氯化锶、氯化钡、氯化镧、氯化镨、氯化钪、氯化钕、氯化钐、氯化钍、溴化锂、溴化钠、溴化钾、溴化铷、溴化铯、碘化锂、碘化钠、碘化钾、碘化铷、碘化铯中至少一种;所述辅助剂为氧化锂、氧化钠、氧化钾、氧化铍、氧化镁、氧化钙、氧化钡中至少一种。Further, the molten salt electrolyte is lithium fluoride, potassium fluoride, rubidium fluoride, cesium fluoride, beryllium fluoride, lithium chloride, sodium chloride, potassium chloride, rubidium chloride, cesium chloride, Beryllium, magnesium chloride, calcium chloride, strontium chloride, barium chloride, lanthanum chloride, praseodymium chloride, scandium chloride, neodymium chloride, samarium chloride, thorium chloride, lithium bromide, sodium bromide, potassium bromide, At least one of rubidium bromide, cesium bromide, lithium iodide, sodium iodide, potassium iodide, rubidium iodide, cesium iodide; the auxiliary agent is lithium oxide, sodium oxide, potassium oxide, beryllium oxide, magnesium oxide, At least one of calcium oxide and barium oxide.
进一步,所述阳极为惰性阳极和活性阳极的一种;所述阴极为铂、金、铁、银、铝、铜、钡、钴、铬、汞、钼、镍、石墨中至少一种。Further, the anode is one of an inert anode and an active anode; the cathode is at least one of platinum, gold, iron, silver, aluminum, copper, barium, cobalt, chromium, mercury, molybdenum, nickel, and graphite.
进一步,所述惰性阳极材料为合金类、金属陶瓷类中至少一种;所述活性阳极材料为石墨质、半石墨质、石墨、石墨烯、碳纳米管、炭纤维中至少一种。Further, the inert anode material is at least one of alloys and cermets; the active anode material is at least one of graphite, semi-graphite, graphite, graphene, carbon nanotubes, and carbon fibers.
本发明的有益效果:Beneficial effects of the present invention:
1、原料纯度要求低,产品纯度更高。本发明低温电解制备高纯金属铍的方法,通过低温液态合金隔开两个电解工作区,并在阳极工作区中加入含铍原料,通电后含铍原料被还原得到的金属铍可直接溶解进入液态合金,其中比铍电位更负的离子不会从阳极工作区进入液态合金,比铍电位更正的离子虽然会进入液态合金,但不会从液态合金进入阴极工作区,因此,本发明能够很好的除去原料中的杂质,降低对含铍原料的纯度要求,原料的适应性好。1. The raw material purity requirement is low, and the product purity is higher. The method for preparing high-purity metal beryllium by low-temperature electrolysis of the present invention separates two electrolytic working areas by a low-temperature liquid alloy, and adds beryllium-containing raw materials into the anode working area, and the metal beryllium obtained by reducing the beryllium-containing raw materials can be directly dissolved into the Liquid alloy, wherein more negative ions than beryllium potential will not enter the liquid alloy from the anode working area, although more positive ions than the beryllium potential will enter the liquid alloy, but will not enter the cathode working area from the liquid alloy, therefore, the present invention can be very It is good for removing impurities in raw materials, reducing the purity requirements for raw materials containing beryllium, and has good adaptability of raw materials.
2、原料来源更丰富。本发明低温电解制备高纯金属铍的方法,不同于熔盐电脱盐需以氧化铍为原料,镁还原法制铍中以氟化铍为原料,或以氯化铍为原料的熔盐电解,本发明在电解质中的含氧类辅助剂,增加含铍原料的溶解性,因此本发明的含铍原料可以为氧化铍、氟化铍、氯化铍中的一种或以上。同时,含铍原料溶解性的增加,可极大地降低铍离子或络合离子对含铍原料的依赖性,进一步降低对其纯度的要求,如含铍原料铍质量分数≥50%均可满足本申请工艺要求,含铍原料来源更丰富。2. The sources of raw materials are more abundant. The method for preparing high-purity metal beryllium by low-temperature electrolysis of the present invention is different from molten salt electrolysis that requires beryllium oxide as a raw material, and magnesium reduction method that uses beryllium fluoride as a raw material or molten salt electrolysis that uses beryllium chloride as a raw material. The oxygen-containing auxiliary agent in the electrolyte is invented to increase the solubility of the beryllium-containing raw material, so the beryllium-containing raw material of the present invention can be one or more of beryllium oxide, beryllium fluoride, and beryllium chloride. At the same time, the increase in the solubility of beryllium-containing raw materials can greatly reduce the dependence of beryllium ions or complex ions on beryllium-containing raw materials, and further reduce the requirements for their purity. According to the application process requirements, the sources of beryllium-containing raw materials are more abundant.
3、操作温度低、能耗少。本发明电解温度更低(<600℃),能够降低电解能耗,减少铍的挥发损失。本发明在液态合金中加入硅,增加了液态合金的流动性,降低其热膨胀性,极大地降低合金的熔点。3. Low operating temperature and low energy consumption. The electrolysis temperature of the present invention is lower (<600 DEG C), can reduce electrolysis energy consumption, and reduce volatilization loss of beryllium. The invention adds silicon into the liquid alloy, which increases the fluidity of the liquid alloy, reduces its thermal expansion, and greatly reduces the melting point of the alloy.
4、电解体系中铍离子浓度较高。通过在电解质中加入含氧类辅助剂,使得氧和卤素及铍形成铍氧卤素络合离子,增大了含铍原料的溶解度及电解体系中含铍离子浓度。4. The concentration of beryllium ions in the electrolytic system is relatively high. By adding oxygen-containing auxiliary agents into the electrolyte, oxygen, halogen and beryllium form beryllium oxyhalide complex ions, which increases the solubility of beryllium-containing raw materials and the concentration of beryllium-containing ions in the electrolytic system.
5、电解质体系电导率较高。增加碱金属和碱土金属卤化物类离子化合物,可以增加电解质中的离子浓度,降低体系粘度,进而提高体系电导率。5. The conductivity of the electrolyte system is high. Increasing the alkali metal and alkaline earth metal halide ionic compounds can increase the ion concentration in the electrolyte, reduce the viscosity of the system, and then improve the conductivity of the system.
6、加料速度限制少。本发明低温电解制备高纯金属铍的方法,含铍原料可以溶解于电解质,发生离子扩散,也可以不溶于电解质,仅在液固界面(电解液和固态原料界面)上发生电化学反应,降低了对加料速率的要求。6. Feed speed limit less. In the method for preparing high-purity metal beryllium by low-temperature electrolysis of the present invention, the beryllium-containing raw material can be dissolved in the electrolyte to cause ion diffusion, or it can be insoluble in the electrolyte, and the electrochemical reaction only occurs at the liquid-solid interface (electrolyte and solid raw material interface), reducing Requirements for feed rate.
7、本发明低温电解制备高纯金属铍的方法,优选的电解槽结构中阳极工作区和阴极工作区呈中心对称,电磁场分布更均匀,槽子保温性更好。7. In the method for preparing high-purity beryllium metal by low-temperature electrolysis of the present invention, the anode working area and the cathode working area in the preferred electrolytic cell structure are center-symmetrical, the electromagnetic field is more evenly distributed, and the tank has better thermal insulation.
附图说明Description of drawings
图1为本发明典型电解装置示意图。其中,图1(1)-(4)为不同设置方式,阳极区和阴极区对应阳极工作区和阴极工作区。其中,1为阴极,2为阳极,3为合金区,4为阴极区,5为阳极区。Figure 1 is a schematic diagram of a typical electrolysis device of the present invention. Among them, Fig. 1(1)-(4) shows different setting modes, the anode area and the cathode area correspond to the anode working area and the cathode working area. Among them, 1 is the cathode, 2 is the anode, 3 is the alloy area, 4 is the cathode area, and 5 is the anode area.
具体实施方式Detailed ways
以下结合实施例对本发明的具体实施方式作进一步详细说明。The specific implementation of the present invention will be described in further detail below in conjunction with the examples.
实施例1Example 1
一种低温熔盐电解制备金属铍的方法,包括以下步骤:A method for preparing metal beryllium by low-temperature molten salt electrolysis, comprising the following steps:
(1)如图1所示,向电解槽底部加入含铍合金(37.7at.%铍、8.2at.%硅、54.1at.%金),确保其熔化后能将电解装置分为阳极工作区、阴极工作区,向阳极工作区内加入59at.%氯化锂、39at.%氯化钾、1at.%氧化锂、1at.%氧化铍的混合物作为阳极电解质,向阴极工作区内加入58.5at.%氯化锂、41at.%氯化钾、0.5at.%氧化铍的混合物作为阴极电解质;加热呈熔融态或悬浮态。(1) As shown in Figure 1, add a beryllium-containing alloy (37.7at.% beryllium, 8.2at.% silicon, 54.1at.% gold) to the bottom of the electrolytic cell to ensure that the electrolytic device can be divided into an anode working area after melting , cathode working area, add 59at.% lithium chloride, 39at.% potassium chloride, 1at.% lithium oxide, 1at.% beryllium oxide mixture into the anode working area as the anode electrolyte, add 58.5at The mixture of .% lithium chloride, 41at.% potassium chloride and 0.5at.% beryllium oxide is used as catholyte; when heated, it becomes molten or suspended.
(2)向阳极工作区内加入纯度为50%的氧化铍,电解槽升温至599℃,恒温0.5h以上,将石墨阳极和铁阴极分别插入阳极电解质和阴极电解质中,通电恒温电解,控制电流密度为1.0A/cm2,电解12h,在阴极得到固态金属铍,经分析所得固态金属铍的纯度为99.0%。(2) Add beryllium oxide with a purity of 50% to the anode working area, raise the temperature of the electrolytic cell to 599°C, and keep the temperature constant for more than 0.5h. Insert the graphite anode and iron cathode into the anode electrolyte and cathode electrolyte respectively, and conduct constant temperature electrolysis with electricity to control the current The density is 1.0A/cm 2 , the electrolysis is for 12 hours, and the solid metal beryllium is obtained at the cathode, and the purity of the solid metal beryllium obtained by analysis is 99.0%.
实施例2Example 2
一种低温熔盐电解制备金属铍的方法,包括以下步骤:A method for preparing metal beryllium by low-temperature molten salt electrolysis, comprising the following steps:
(1)如图1所示,向电解槽底部加入含铍合金(3.1at.%铍、16.8at.%硅、80.1at.%金),确保其熔化后能将电解装置分为阳极工作区、阴极工作区,向阳极工作区内加入61at.%氯化钙、36at.%氯化锂、2.5at.%氧化钙、0.5at.%氧化铍的混合物作为阳极电解质,向阴极工作区内加入55.5at.%氯化锂、43.4at.%氯化铷、0.1at.%氧化钾、1at.%氧化铍的混合物作为阴极电解质;加热呈熔融态或悬浮态。(1) As shown in Figure 1, add a beryllium-containing alloy (3.1at.% beryllium, 16.8at.% silicon, 80.1at.% gold) to the bottom of the electrolytic cell to ensure that the electrolytic device can be divided into an anode working area after melting , cathode working area, add a mixture of 61at.% calcium chloride, 36at.% lithium chloride, 2.5at.% calcium oxide, 0.5at.% beryllium oxide to the anode working area as the anode electrolyte, and add A mixture of 55.5at.% lithium chloride, 43.4at.% rubidium chloride, 0.1at.% potassium oxide, and 1at.% beryllium oxide is used as the catholyte; it is molten or suspended when heated.
(2)向阳极工作区内加入纯度为60%的氧化铍,电解槽升温至370℃,恒温0.5h以上,将石墨质阳极和铂阴极分别插入阳极电解质和阴极电解质中,通电恒温电解,控制电流密度为0.8A/cm2,电解3h,在阴极得到固态金属铍,经分析所得固态金属铍的纯度为99.2%。(2) Add beryllium oxide with a purity of 60% to the anode working area, raise the temperature of the electrolytic cell to 370°C, and keep the temperature at a constant temperature for more than 0.5h. Insert the graphite anode and platinum cathode into the anode electrolyte and cathode electrolyte respectively, and conduct electrolysis at a constant temperature with power on. The current density is 0.8A/cm 2 , electrolysis is performed for 3 hours, and solid metal beryllium is obtained at the cathode. The purity of the solid metal beryllium obtained by analysis is 99.2%.
实施例3Example 3
一种低温熔盐电解制备金属铍的方法,包括以下步骤:A method for preparing metal beryllium by low-temperature molten salt electrolysis, comprising the following steps:
(1)如图1所示,向电解槽底部加入含铍合金(7.9at.%铍、12.3at.%硅、78.3at.%金、0.7at.%铜、0.8at.%银),确保其熔化后能将电解装置分为阳极工作区、阴极工作区,向阳极工作区内加入66at.%溴化钾、33at.%溴化锂、0.5at.%氧化钙、0.5at.%氧化铍的混合物作为阳极电解质,向阴极工作区内加入62.5at.%碘化锂、36.5at.%碘化钾、1at.%氧化铍的混合物作为阴极电解质;加热呈熔融态或悬浮态。(1) As shown in Figure 1, add beryllium-containing alloy (7.9at.% beryllium, 12.3at.% silicon, 78.3at.% gold, 0.7at.% copper, 0.8at.% silver) to the bottom of the electrolytic cell to ensure After melting, the electrolysis device can be divided into an anode working area and a cathode working area, and a mixture of 66 at.% potassium bromide, 33 at.% lithium bromide, 0.5 at.% calcium oxide and 0.5 at.% beryllium oxide is added to the anode working area As an anode electrolyte, a mixture of 62.5 at.% lithium iodide, 36.5 at.% potassium iodide and 1 at.% beryllium oxide is added to the cathode working area as the catholyte; it becomes molten or suspended when heated.
(2)向阳极工作区内加入纯度为80%的氧化铍,电解槽升温至450℃,恒温0.5h以上,将炭纤维阳极和钼阴极分别插入阳极电解质和阴极电解质中,通电恒温电解,控制电流密度为0.01A/cm2,电解15h,在阴极得到固态金属铍,经分析所得固态金属铍的纯度为99.5%。(2) Add beryllium oxide with a purity of 80% to the anode working area, raise the temperature of the electrolytic cell to 450°C, and keep the temperature at a constant temperature for more than 0.5h. Insert the carbon fiber anode and molybdenum cathode into the anode electrolyte and cathode electrolyte respectively, and electrolyze at a constant temperature with power on. The current density is 0.01A/cm 2 , electrolysis is performed for 15 hours, and solid metal beryllium is obtained at the cathode. The purity of the solid metal beryllium obtained by analysis is 99.5%.
实施例4Example 4
一种低温熔盐电解制备金属铍的方法,包括以下步骤:A method for preparing metal beryllium by low-temperature molten salt electrolysis, comprising the following steps:
(1)如图1所示,向电解槽底部加入含铍合金(0.2at.%铍、18.0at.%硅、81.0at.%金、0.5at.%铜、0.3at.%锰),确保其熔化后能将电解装置分为阳极工作区、阴极工作区,向阳极工作区内加入17.5at.%氯化钪、82at.%碘化锂、0.5at.%氧化铍的混合物作为阳极电解质,向阴极工作区内加入45at.%氯化铍、54at.%氯化钠、1at.%氧化锂的混合物作为阴极电解质;加热呈熔融态或悬浮态。(1) As shown in Figure 1, add beryllium-containing alloy (0.2at.% beryllium, 18.0at.% silicon, 81.0at.% gold, 0.5at.% copper, 0.3at.% manganese) to the bottom of the electrolytic cell to ensure After it is melted, the electrolysis device can be divided into an anode working area and a cathode working area, and a mixture of 17.5 at.% scandium chloride, 82 at.% lithium iodide, and 0.5 at.% beryllium oxide is added to the anode working area as the anode electrolyte. Add a mixture of 45at.% beryllium chloride, 54at.% sodium chloride, and 1at.% lithium oxide into the cathode working area as the catholyte; it will be molten or suspended when heated.
(2)向阳极工作区内加入纯度为50%的氟化铍,电解槽升温至400℃,恒温0.5h以上,将金属陶瓷阳极和镍阴极分别插入阳极电解质和阴极电解质中,通电恒温电解,控制电流密度为0.5A/cm2,电解3h,在阴极得到固态金属铍,经分析所得固态金属铍的纯度为99.7%。(2) Add beryllium fluoride with a purity of 50% into the anode working area, raise the temperature of the electrolytic cell to 400° C., and keep the temperature constant for more than 0.5 hours. Insert the cermet anode and nickel cathode into the anode electrolyte and the cathode electrolyte respectively, and electrolyze at a constant temperature with electricity. The current density is controlled at 0.5A/cm 2 , electrolysis is performed for 3 hours, and solid metal beryllium is obtained at the cathode. The purity of the solid metal beryllium obtained by analysis is 99.7%.
实施例5Example 5
一种低温熔盐电解制备金属铍的方法,包括以下步骤:A method for preparing metal beryllium by low-temperature molten salt electrolysis, comprising the following steps:
(1)如图1所示,向电解槽底部加入含铍合金(24.7at.%铍、6.3at.%硅、68.4at.%金、0.1at.%锰、0.2at.%铜、0.3at.%银),确保其熔化后能将电解装置分为阳极工作区、阴极工作区,向阳极工作区内加入60at.%氯化钠、36at.%氯化钪、3at.%氧化钙、1at.%氧化铍的混合物作为阳极电解质,向阴极工作区内加入10at.%氟化锂、90at.%氟化铍的混合物作为阴极电解质;加热呈熔融态或悬浮态。(1) As shown in Figure 1, add beryllium-containing alloy (24.7at.% beryllium, 6.3at.% silicon, 68.4at.% gold, 0.1at.% manganese, 0.2at.% copper, 0.3at .% silver), to ensure that the electrolytic device can be divided into an anode work area and a cathode work area after melting, add 60at.% sodium chloride, 36at.% scandium chloride, 3at.% calcium oxide, 1at A mixture of .% beryllium oxide is used as the anode electrolyte, and a mixture of 10 at.% lithium fluoride and 90 at.% beryllium fluoride is added to the cathode working area as the cathode electrolyte; it becomes molten or suspended when heated.
(2)向阳极工作区内加入纯度为70%的氟化铍,电解槽升温至580℃,恒温0.5h以上,将石墨阳极和银阴极分别插入阳极电解质和阴极电解质中,通电恒温电解,控制电流密度为0.8A/cm2,电解4h,在阴极得到固态金属铍,经分析所得固态金属铍的纯度为99.9%。(2) Add beryllium fluoride with a purity of 70% to the anode working area, raise the temperature of the electrolytic cell to 580°C, and keep the temperature constant for more than 0.5h. Insert the graphite anode and the silver cathode into the anode electrolyte and the cathode electrolyte respectively, and electrolyze at a constant temperature with power on. The current density is 0.8A/cm 2 , and the electrolysis takes 4 hours to obtain solid metal beryllium at the cathode. The purity of the solid metal beryllium obtained by analysis is 99.9%.
实施例6Example 6
一种低温熔盐电解制备金属铍的方法,包括以下步骤:A method for preparing metal beryllium by low-temperature molten salt electrolysis, comprising the following steps:
(1)如图1所示,向电解槽底部加入含铍合金(14.3at.%铍、11.2at.%硅、74.0at.%金、0.5at.%银),确保其熔化后能将电解装置分为阳极工作区、阴极工作区,向阳极工作区内加入40at.%氯化锂,55.5at.%氯化铷、4at.%氧化钡、0.5at.%氧化铍的混合物作为阳极电解质,向阴极工作区内加入23at.%氟化锂、73at.%碘化锂、3.5at.%氧化锂、0.5at.%氧化铍的混合物作为阴极电解质;加热呈熔融态或悬浮态。(1) As shown in Figure 1, add beryllium-containing alloy (14.3at.% beryllium, 11.2at.% silicon, 74.0at.% gold, 0.5at.% silver) to the bottom of the electrolytic cell to ensure that it can be electrolyzed after melting The device is divided into an anode working area and a cathode working area. A mixture of 40 at.% lithium chloride, 55.5 at.% rubidium chloride, 4 at.% barium oxide and 0.5 at.% beryllium oxide is added to the anode working area as the anode electrolyte. Add a mixture of 23at.% lithium fluoride, 73at.% lithium iodide, 3.5at.% lithium oxide, and 0.5at.% beryllium oxide into the cathode working area as the catholyte; it will be molten or suspended when heated.
(2)向阳极工作区内加入纯度为80%的氯化铍,电解槽升温至595℃,恒温0.5h以上,将石墨烯阳极和石墨阴极分别插入阳极电解质和阴极电解质中,通电恒温电解,控制电流密度为0.3A/cm2,电解6h,在阴极得到固态金属铍,经分析所得固态金属铍的纯度为99.5%。(2) Adding beryllium chloride with a purity of 80% to the anode working area, the electrolytic cell is heated to 595° C., and kept at a constant temperature for more than 0.5 hours. The graphene anode and the graphite cathode are respectively inserted into the anode electrolyte and the cathode electrolyte, and electrolyzed at a constant temperature with electricity. The current density is controlled at 0.3A/cm 2 , electrolysis is performed for 6 hours, and solid metal beryllium is obtained at the cathode. The purity of the solid metal beryllium obtained by analysis is 99.5%.
实施例7Example 7
一种低温熔盐电解制备金属铍的方法,包括以下步骤:A method for preparing metal beryllium by low-temperature molten salt electrolysis, comprising the following steps:
(1)如图1所示,向电解槽底部加入含铍合金(11.3at.%铍、9.1at.%硅、79.6at.%金),确保其熔化后能将电解装置分为阳极工作区、阴极工作区,向阳极工作区内加入48at.%氯化钠、48at.%氯化钐、3at.%氧化钠、1at.%氧化铍的混合物作为阳极电解质,向阴极工作区内加入41at.%氯化钾、56at.%氯化锂、2.5at.%氧化锂、0.5at.%氧化铍的混合物作为阴极电解质;加热呈熔融态或悬浮态。(1) As shown in Figure 1, add a beryllium-containing alloy (11.3at.% beryllium, 9.1at.% silicon, 79.6at.% gold) to the bottom of the electrolytic cell to ensure that the electrolytic device can be divided into an anode working area after melting , Cathode working area, add the mixture of 48at.% sodium chloride, 48at.% samarium chloride, 3at.% sodium oxide, 1at.% beryllium oxide to the anode working area as the anode electrolyte, add 41at.% to the cathode working area A mixture of % potassium chloride, 56 at.% lithium chloride, 2.5 at.% lithium oxide, and 0.5 at.% beryllium oxide is used as the catholyte; it is molten or suspended when heated.
(2)向阳极工作区内加入纯度为99%的氧化铍和99%的氯化铍(氯化铍占80at%),电解槽升温至440℃,恒温0.5h以上,将半石墨质阳极和镍阴极分别插入阳极电解质和阴极电解质中,通电恒温电解,控制电流密度为0.5A/cm2,电解6h,在阴极得到固态金属铍,经分析所得固态金属铍的纯度为99.9%。(2) Adding beryllium oxide and 99% beryllium chloride (80at% beryllium chloride) with a purity of 99% to the anode working area, the electrolytic cell is heated up to 440°C, and the temperature is maintained for more than 0.5h, and the semi-graphite anode and The nickel cathode was inserted into the anode electrolyte and the cathode electrolyte respectively, energized and electrolyzed at a constant temperature, and the current density was controlled to be 0.5A/cm 2 , electrolyzed for 6 hours, and solid metal beryllium was obtained at the cathode, and the purity of the solid metal beryllium obtained by analysis was 99.9%.
实施例8Example 8
一种低温熔盐电解制备金属铍的方法,包括以下步骤:A method for preparing metal beryllium by low-temperature molten salt electrolysis, comprising the following steps:
(1)如图1所示,向电解槽底部加入含铍合金(3.3at.%铍、17.2at.%硅、79.0at.%金、0.3at.%铜、0.2at.%锰),确保其熔化后能将电解装置分为阳极工作区、阴极工作区,向阳极工作区内加入47at.%氯化铍、53at.%氯化钠的混合物作为阳极电解质,向阴极工作区内加入41at.%氯化铍、55at.%氯化钠、4at.%氧化锂的混合物作为阴极电解质;加热呈熔融态或悬浮态。(1) As shown in Figure 1, add beryllium-containing alloy (3.3at.% beryllium, 17.2at.% silicon, 79.0at.% gold, 0.3at.% copper, 0.2at.% manganese) to the bottom of the electrolytic cell to ensure After it is melted, the electrolysis device can be divided into an anode working area and a cathode working area, and a mixture of 47at.% beryllium chloride and 53at.% sodium chloride is added to the anode working area as the anode electrolyte, and 41at.% is added to the cathode working area. % beryllium chloride, 55 at. % sodium chloride, 4 at. % lithium oxide mixture as the catholyte; heated in molten state or suspended state.
(2)向阳极工作区内加入纯度为85%的氟化铍,电解槽升温至380℃,恒温0.5h以上,将合金类阳极和石墨阴极分别插入阳极电解质和阴极电解质中,通电恒温电解,控制电流密度为0.7A/cm2,电解2h,在阴极得到固态金属铍,经分析所得固态金属铍的纯度为99.3%。(2) Add beryllium fluoride with a purity of 85% to the anode working area, raise the temperature of the electrolytic cell to 380°C, and keep the temperature at a constant temperature for more than 0.5h, insert the alloy anode and graphite cathode into the anode electrolyte and cathode electrolyte respectively, and electrolyze at a constant temperature with electricity, The current density is controlled at 0.7A/cm 2 , electrolysis is performed for 2 hours, and solid metal beryllium is obtained at the cathode. The purity of the solid metal beryllium obtained by analysis is 99.3%.
实施例9Example 9
一种低温熔盐电解制备金属铍的方法,包括以下步骤:A method for preparing metal beryllium by low-temperature molten salt electrolysis, comprising the following steps:
(1)如图1所示,向电解槽底部加入含铍合金(3.3at.%铍、17.2at.%硅、79.0at.%金、0.3at.%铜、0.2at.%锰),确保其熔化后能将电解装置分为阳极工作区、阴极工作区,向阳极工作区内加入47at.%氯化铍、53at.%氯化钠的混合物作为阳极电解质,向阴极工作区内加入41at.%氯化铍、55at.%氯化钠、4at.%氧化锂的混合物作为阴极电解质;(1) As shown in Figure 1, add beryllium-containing alloy (3.3at.% beryllium, 17.2at.% silicon, 79.0at.% gold, 0.3at.% copper, 0.2at.% manganese) to the bottom of the electrolytic cell to ensure After it is melted, the electrolysis device can be divided into an anode working area and a cathode working area, and a mixture of 47at.% beryllium chloride and 53at.% sodium chloride is added to the anode working area as the anode electrolyte, and 41at.% is added to the cathode working area. % beryllium chloride, 55at.% sodium chloride, 4at.% lithium oxide mixture as catholyte;
(2)向阳极工作区内加入纯度为90%的氟化铍,电解槽升温至380℃,将金属陶瓷类阳极和镍阴极分别插入阳极电解质和阴极电解质中,通电电解,控制阴极电压为-1.95V(vs NHE),电解8h,在阴极得到固态金属铍,经分析所得固态金属铍的纯度为99.8%。(2) Add beryllium fluoride with a purity of 90% to the anode working area, raise the temperature of the electrolytic cell to 380° C., insert the cermet anode and nickel cathode into the anode electrolyte and the cathode electrolyte respectively, power on and electrolyze, and control the cathode voltage to - 1.95V (vs NHE), electrolysis for 8 hours, solid metal beryllium was obtained at the cathode, and the purity of the solid metal beryllium obtained by analysis was 99.8%.
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CN112981461B (en) * | 2021-02-05 | 2022-05-27 | 西藏智材新材料有限公司 | High-purity metal beryllium and preparation process thereof |
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