JP4371323B2 - Niobium powder, niobium sintered body, and capacitor using niobium sintered body - Google Patents
Niobium powder, niobium sintered body, and capacitor using niobium sintered body Download PDFInfo
- Publication number
- JP4371323B2 JP4371323B2 JP2006336468A JP2006336468A JP4371323B2 JP 4371323 B2 JP4371323 B2 JP 4371323B2 JP 2006336468 A JP2006336468 A JP 2006336468A JP 2006336468 A JP2006336468 A JP 2006336468A JP 4371323 B2 JP4371323 B2 JP 4371323B2
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- Prior art keywords
- niobium
- sintered body
- capacitor
- powder
- group
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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- GUCVJGMIXFAOAE-UHFFFAOYSA-N niobium atom Chemical compound [Nb] GUCVJGMIXFAOAE-UHFFFAOYSA-N 0.000 title claims description 243
- 239000003990 capacitor Substances 0.000 title claims description 158
- 239000010955 niobium Substances 0.000 title claims description 120
- 229910052758 niobium Inorganic materials 0.000 title claims description 120
- 239000011148 porous material Substances 0.000 claims description 108
- 238000000034 method Methods 0.000 claims description 58
- -1 sulfonate anion Chemical class 0.000 claims description 51
- 238000009826 distribution Methods 0.000 claims description 30
- 229920001940 conductive polymer Polymers 0.000 claims description 28
- 239000004065 semiconductor Substances 0.000 claims description 26
- 238000004519 manufacturing process Methods 0.000 claims description 22
- 239000000463 material Substances 0.000 claims description 19
- 229910052757 nitrogen Inorganic materials 0.000 claims description 19
- 229910052799 carbon Inorganic materials 0.000 claims description 17
- 239000002019 doping agent Substances 0.000 claims description 15
- 229910052760 oxygen Inorganic materials 0.000 claims description 15
- 239000001301 oxygen Substances 0.000 claims description 15
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical group [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 14
- 125000004432 carbon atom Chemical group C* 0.000 claims description 13
- 229920006395 saturated elastomer Polymers 0.000 claims description 12
- 125000004122 cyclic group Chemical group 0.000 claims description 9
- 125000004435 hydrogen atom Chemical group [H]* 0.000 claims description 9
- 125000000217 alkyl group Chemical group 0.000 claims description 8
- URLJKFSTXLNXLG-UHFFFAOYSA-N niobium(5+);oxygen(2-) Chemical compound [O-2].[O-2].[O-2].[O-2].[O-2].[Nb+5].[Nb+5] URLJKFSTXLNXLG-UHFFFAOYSA-N 0.000 claims description 7
- 125000004417 unsaturated alkyl group Chemical group 0.000 claims description 7
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical group [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims description 6
- 150000002148 esters Chemical class 0.000 claims description 6
- 125000004433 nitrogen atom Chemical group N* 0.000 claims description 6
- 125000001997 phenyl group Chemical group [H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 claims description 6
- 229920000128 polypyrrole Polymers 0.000 claims description 6
- 229930195734 saturated hydrocarbon Natural products 0.000 claims description 6
- 229910052717 sulfur Inorganic materials 0.000 claims description 6
- 239000011593 sulfur Chemical group 0.000 claims description 6
- 239000008151 electrolyte solution Substances 0.000 claims description 5
- 229910000484 niobium oxide Inorganic materials 0.000 claims description 5
- 229920000642 polymer Polymers 0.000 claims description 5
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 claims description 4
- 125000003545 alkoxy group Chemical group 0.000 claims description 4
- 229920000123 polythiophene Polymers 0.000 claims description 4
- SIKJAQJRHWYJAI-UHFFFAOYSA-N Indole Chemical compound C1=CC=C2NC=CC2=C1 SIKJAQJRHWYJAI-UHFFFAOYSA-N 0.000 claims description 3
- 229920001609 Poly(3,4-ethylenedioxythiophene) Polymers 0.000 claims description 3
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 claims description 3
- 125000005907 alkyl ester group Chemical group 0.000 claims description 3
- 150000001408 amides Chemical class 0.000 claims description 3
- 125000002915 carbonyl group Chemical group [*:2]C([*:1])=O 0.000 claims description 3
- 125000004093 cyano group Chemical group *C#N 0.000 claims description 3
- 125000005843 halogen group Chemical group 0.000 claims description 3
- 125000001841 imino group Chemical group [H]N=* 0.000 claims description 3
- 125000000449 nitro group Chemical group [O-][N+](*)=O 0.000 claims description 3
- 229920000767 polyaniline Polymers 0.000 claims description 3
- 125000002924 primary amino group Chemical group [H]N([H])* 0.000 claims description 3
- 125000000467 secondary amino group Chemical group [H]N([*:1])[*:2] 0.000 claims description 3
- 125000001424 substituent group Chemical group 0.000 claims description 3
- 125000000475 sulfinyl group Chemical group [*:2]S([*:1])=O 0.000 claims description 3
- 125000000472 sulfonyl group Chemical group *S(*)(=O)=O 0.000 claims description 3
- 125000001302 tertiary amino group Chemical group 0.000 claims description 3
- UGNWTBMOAKPKBL-UHFFFAOYSA-N tetrachloro-1,4-benzoquinone Chemical compound ClC1=C(Cl)C(=O)C(Cl)=C(Cl)C1=O UGNWTBMOAKPKBL-UHFFFAOYSA-N 0.000 claims description 3
- PCCVSPMFGIFTHU-UHFFFAOYSA-N tetracyanoquinodimethane Chemical compound N#CC(C#N)=C1C=CC(=C(C#N)C#N)C=C1 PCCVSPMFGIFTHU-UHFFFAOYSA-N 0.000 claims description 3
- 239000011800 void material Substances 0.000 claims description 3
- 229930195735 unsaturated hydrocarbon Natural products 0.000 claims description 2
- 125000001183 hydrocarbyl group Chemical group 0.000 claims 1
- 239000012190 activator Substances 0.000 description 61
- 239000000843 powder Substances 0.000 description 53
- 239000002245 particle Substances 0.000 description 52
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 33
- 229910001868 water Inorganic materials 0.000 description 33
- 238000005245 sintering Methods 0.000 description 31
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 30
- QVQLCTNNEUAWMS-UHFFFAOYSA-N barium oxide Chemical compound [Ba]=O QVQLCTNNEUAWMS-UHFFFAOYSA-N 0.000 description 30
- 239000010410 layer Substances 0.000 description 30
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 28
- 239000007864 aqueous solution Substances 0.000 description 26
- 238000000465 moulding Methods 0.000 description 24
- 238000010079 rubber tapping Methods 0.000 description 24
- 239000000243 solution Substances 0.000 description 23
- 239000000203 mixture Substances 0.000 description 22
- GUVRBAGPIYLISA-UHFFFAOYSA-N tantalum atom Chemical compound [Ta] GUVRBAGPIYLISA-UHFFFAOYSA-N 0.000 description 22
- 239000002994 raw material Substances 0.000 description 20
- 239000002904 solvent Substances 0.000 description 20
- 239000000126 substance Substances 0.000 description 19
- 230000000704 physical effect Effects 0.000 description 18
- 239000000047 product Substances 0.000 description 18
- 239000007789 gas Substances 0.000 description 17
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 16
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 description 16
- 239000003795 chemical substances by application Substances 0.000 description 16
- 229910052715 tantalum Inorganic materials 0.000 description 16
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 description 15
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 15
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 15
- 238000005121 nitriding Methods 0.000 description 15
- 229910052709 silver Inorganic materials 0.000 description 15
- 239000004332 silver Substances 0.000 description 15
- 150000001450 anions Chemical class 0.000 description 13
- 238000006243 chemical reaction Methods 0.000 description 13
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 12
- 239000002253 acid Substances 0.000 description 12
- 150000001875 compounds Chemical class 0.000 description 12
- 239000007800 oxidant agent Substances 0.000 description 12
- 229910045601 alloy Inorganic materials 0.000 description 10
- 239000000956 alloy Substances 0.000 description 10
- 239000003822 epoxy resin Substances 0.000 description 10
- 229920000647 polyepoxide Polymers 0.000 description 10
- 238000010298 pulverizing process Methods 0.000 description 10
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 9
- 239000012298 atmosphere Substances 0.000 description 9
- 230000000052 comparative effect Effects 0.000 description 9
- 229910052751 metal Inorganic materials 0.000 description 9
- 239000002184 metal Substances 0.000 description 9
- 239000002002 slurry Substances 0.000 description 9
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 8
- 238000002156 mixing Methods 0.000 description 8
- 230000001590 oxidative effect Effects 0.000 description 8
- LSNNMFCWUKXFEE-UHFFFAOYSA-M Bisulfite Chemical compound OS([O-])=O LSNNMFCWUKXFEE-UHFFFAOYSA-M 0.000 description 7
- 229910001257 Nb alloy Inorganic materials 0.000 description 7
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 7
- 238000005470 impregnation Methods 0.000 description 7
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 6
- MUBZPKHOEPUJKR-UHFFFAOYSA-N Oxalic acid Chemical compound OC(=O)C(O)=O MUBZPKHOEPUJKR-UHFFFAOYSA-N 0.000 description 6
- KAESVJOAVNADME-UHFFFAOYSA-N Pyrrole Chemical compound C=1C=CNC=1 KAESVJOAVNADME-UHFFFAOYSA-N 0.000 description 6
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 6
- 229910052782 aluminium Inorganic materials 0.000 description 6
- ROOXNKNUYICQNP-UHFFFAOYSA-N ammonium persulfate Chemical compound [NH4+].[NH4+].[O-]S(=O)(=O)OOS([O-])(=O)=O ROOXNKNUYICQNP-UHFFFAOYSA-N 0.000 description 6
- 239000007772 electrode material Substances 0.000 description 6
- WABPQHHGFIMREM-UHFFFAOYSA-N lead(0) Chemical compound [Pb] WABPQHHGFIMREM-UHFFFAOYSA-N 0.000 description 6
- NUJOXMJBOLGQSY-UHFFFAOYSA-N manganese dioxide Chemical compound O=[Mn]=O NUJOXMJBOLGQSY-UHFFFAOYSA-N 0.000 description 6
- 238000005259 measurement Methods 0.000 description 6
- 229910052759 nickel Inorganic materials 0.000 description 6
- 238000007254 oxidation reaction Methods 0.000 description 6
- 238000007747 plating Methods 0.000 description 6
- 239000007787 solid Substances 0.000 description 6
- 238000003756 stirring Methods 0.000 description 6
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 5
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 5
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 5
- 229910052796 boron Inorganic materials 0.000 description 5
- 239000003792 electrolyte Substances 0.000 description 5
- 239000001257 hydrogen Substances 0.000 description 5
- 229910052739 hydrogen Inorganic materials 0.000 description 5
- 239000007788 liquid Substances 0.000 description 5
- 229910017604 nitric acid Inorganic materials 0.000 description 5
- 239000003960 organic solvent Substances 0.000 description 5
- 230000003647 oxidation Effects 0.000 description 5
- 238000006116 polymerization reaction Methods 0.000 description 5
- 238000012545 processing Methods 0.000 description 5
- 229920005989 resin Polymers 0.000 description 5
- 239000011347 resin Substances 0.000 description 5
- 239000011734 sodium Substances 0.000 description 5
- 238000005406 washing Methods 0.000 description 5
- AZQWKYJCGOJGHM-UHFFFAOYSA-N 1,4-benzoquinone Chemical compound O=C1C=CC(=O)C=C1 AZQWKYJCGOJGHM-UHFFFAOYSA-N 0.000 description 4
- HZNVUJQVZSTENZ-UHFFFAOYSA-N 2,3-dichloro-5,6-dicyano-1,4-benzoquinone Chemical compound ClC1=C(Cl)C(=O)C(C#N)=C(C#N)C1=O HZNVUJQVZSTENZ-UHFFFAOYSA-N 0.000 description 4
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 4
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 4
- ZOXJGFHDIHLPTG-UHFFFAOYSA-N Boron Chemical compound [B] ZOXJGFHDIHLPTG-UHFFFAOYSA-N 0.000 description 4
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 4
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 4
- 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 4
- 229920002845 Poly(methacrylic acid) Polymers 0.000 description 4
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 4
- 229920002125 Sokalan® Polymers 0.000 description 4
- WNLRTRBMVRJNCN-UHFFFAOYSA-N adipic acid Chemical compound OC(=O)CCCCC(O)=O WNLRTRBMVRJNCN-UHFFFAOYSA-N 0.000 description 4
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 4
- 229910052786 argon Inorganic materials 0.000 description 4
- 239000011230 binding agent Substances 0.000 description 4
- 238000003763 carbonization Methods 0.000 description 4
- YADSGOSSYOOKMP-UHFFFAOYSA-N dioxolead Chemical compound O=[Pb]=O YADSGOSSYOOKMP-UHFFFAOYSA-N 0.000 description 4
- 239000000178 monomer Substances 0.000 description 4
- 239000008188 pellet Substances 0.000 description 4
- 239000004584 polyacrylic acid Substances 0.000 description 4
- 229920000137 polyphosphoric acid Polymers 0.000 description 4
- NROKBHXJSPEDAR-UHFFFAOYSA-M potassium fluoride Chemical compound [F-].[K+] NROKBHXJSPEDAR-UHFFFAOYSA-M 0.000 description 4
- 239000011164 primary particle Substances 0.000 description 4
- 238000009751 slip forming Methods 0.000 description 4
- 229910052708 sodium Inorganic materials 0.000 description 4
- JOXIMZWYDAKGHI-UHFFFAOYSA-N toluene-4-sulfonic acid Chemical compound CC1=CC=C(S(O)(=O)=O)C=C1 JOXIMZWYDAKGHI-UHFFFAOYSA-N 0.000 description 4
- 229920002554 vinyl polymer Polymers 0.000 description 4
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 3
- KCXVZYZYPLLWCC-UHFFFAOYSA-N EDTA Chemical compound OC(=O)CN(CC(O)=O)CCN(CC(O)=O)CC(O)=O KCXVZYZYPLLWCC-UHFFFAOYSA-N 0.000 description 3
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 235000011054 acetic acid Nutrition 0.000 description 3
- 239000003513 alkali Substances 0.000 description 3
- 229910001870 ammonium persulfate Inorganic materials 0.000 description 3
- KGBXLFKZBHKPEV-UHFFFAOYSA-N boric acid Chemical compound OB(O)O KGBXLFKZBHKPEV-UHFFFAOYSA-N 0.000 description 3
- 239000004327 boric acid Substances 0.000 description 3
- 150000001732 carboxylic acid derivatives Chemical class 0.000 description 3
- 239000000460 chlorine Substances 0.000 description 3
- 239000011247 coating layer Substances 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 229910052802 copper Inorganic materials 0.000 description 3
- 239000010949 copper Substances 0.000 description 3
- 238000001035 drying Methods 0.000 description 3
- 229910052736 halogen Inorganic materials 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 150000004678 hydrides Chemical class 0.000 description 3
- 150000002431 hydrogen Chemical class 0.000 description 3
- 238000005342 ion exchange Methods 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 3
- 229910052749 magnesium Inorganic materials 0.000 description 3
- 239000011777 magnesium Substances 0.000 description 3
- MIVBAHRSNUNMPP-UHFFFAOYSA-N manganese(2+);dinitrate Chemical compound [Mn+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O MIVBAHRSNUNMPP-UHFFFAOYSA-N 0.000 description 3
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 3
- 229910052753 mercury Inorganic materials 0.000 description 3
- 239000011259 mixed solution Substances 0.000 description 3
- PSZYNBSKGUBXEH-UHFFFAOYSA-N naphthalene-1-sulfonic acid Chemical compound C1=CC=C2C(S(=O)(=O)O)=CC=CC2=C1 PSZYNBSKGUBXEH-UHFFFAOYSA-N 0.000 description 3
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 3
- 239000004810 polytetrafluoroethylene Substances 0.000 description 3
- 239000012266 salt solution Substances 0.000 description 3
- 150000003839 salts Chemical class 0.000 description 3
- 239000007790 solid phase Substances 0.000 description 3
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 description 2
- FRASJONUBLZVQX-UHFFFAOYSA-N 1,4-naphthoquinone Chemical compound C1=CC=C2C(=O)C=CC(=O)C2=C1 FRASJONUBLZVQX-UHFFFAOYSA-N 0.000 description 2
- HIXDQWDOVZUNNA-UHFFFAOYSA-N 2-(3,4-dimethoxyphenyl)-5-hydroxy-7-methoxychromen-4-one Chemical compound C=1C(OC)=CC(O)=C(C(C=2)=O)C=1OC=2C1=CC=C(OC)C(OC)=C1 HIXDQWDOVZUNNA-UHFFFAOYSA-N 0.000 description 2
- PAWQVTBBRAZDMG-UHFFFAOYSA-N 2-(3-bromo-2-fluorophenyl)acetic acid Chemical compound OC(=O)CC1=CC=CC(Br)=C1F PAWQVTBBRAZDMG-UHFFFAOYSA-N 0.000 description 2
- JAJIPIAHCFBEPI-UHFFFAOYSA-N 9,10-dioxoanthracene-1-sulfonic acid Chemical compound O=C1C2=CC=CC=C2C(=O)C2=C1C=CC=C2S(=O)(=O)O JAJIPIAHCFBEPI-UHFFFAOYSA-N 0.000 description 2
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonia chloride Chemical compound [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 description 2
- PAYRUJLWNCNPSJ-UHFFFAOYSA-N Aniline Chemical compound NC1=CC=CC=C1 PAYRUJLWNCNPSJ-UHFFFAOYSA-N 0.000 description 2
- WKBOTKDWSSQWDR-UHFFFAOYSA-N Bromine atom Chemical compound [Br] WKBOTKDWSSQWDR-UHFFFAOYSA-N 0.000 description 2
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- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 2
- 229910021591 Copper(I) chloride Inorganic materials 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- KRHYYFGTRYWZRS-UHFFFAOYSA-N Fluorane Chemical compound F KRHYYFGTRYWZRS-UHFFFAOYSA-N 0.000 description 2
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- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 2
- AFVFQIVMOAPDHO-UHFFFAOYSA-N Methanesulfonic acid Chemical compound CS(O)(=O)=O AFVFQIVMOAPDHO-UHFFFAOYSA-N 0.000 description 2
- NTIZESTWPVYFNL-UHFFFAOYSA-N Methyl isobutyl ketone Chemical compound CC(C)CC(C)=O NTIZESTWPVYFNL-UHFFFAOYSA-N 0.000 description 2
- UIHCLUNTQKBZGK-UHFFFAOYSA-N Methyl isobutyl ketone Natural products CCC(C)C(C)=O UIHCLUNTQKBZGK-UHFFFAOYSA-N 0.000 description 2
- UFWIBTONFRDIAS-UHFFFAOYSA-N Naphthalene Chemical compound C1=CC=CC2=CC=CC=C21 UFWIBTONFRDIAS-UHFFFAOYSA-N 0.000 description 2
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 2
- 239000004698 Polyethylene Substances 0.000 description 2
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 2
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 2
- YTPLMLYBLZKORZ-UHFFFAOYSA-N Thiophene Chemical compound C=1C=CSC=1 YTPLMLYBLZKORZ-UHFFFAOYSA-N 0.000 description 2
- ROSDCCJGGBNDNL-UHFFFAOYSA-N [Ta].[Pb] Chemical compound [Ta].[Pb] ROSDCCJGGBNDNL-UHFFFAOYSA-N 0.000 description 2
- AFPRJLBZLPBTPZ-UHFFFAOYSA-N acenaphthoquinone Chemical compound C1=CC(C(C2=O)=O)=C3C2=CC=CC3=C1 AFPRJLBZLPBTPZ-UHFFFAOYSA-N 0.000 description 2
- 239000001361 adipic acid Substances 0.000 description 2
- 235000011037 adipic acid Nutrition 0.000 description 2
- VSCWAEJMTAWNJL-UHFFFAOYSA-K aluminium trichloride Chemical compound Cl[Al](Cl)Cl VSCWAEJMTAWNJL-UHFFFAOYSA-K 0.000 description 2
- 229910021529 ammonia Inorganic materials 0.000 description 2
- 150000003863 ammonium salts Chemical class 0.000 description 2
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- DNNSSWSSYDEUBZ-UHFFFAOYSA-N krypton atom Chemical compound [Kr] DNNSSWSSYDEUBZ-UHFFFAOYSA-N 0.000 description 1
- 239000005001 laminate film Substances 0.000 description 1
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- 239000003446 ligand Substances 0.000 description 1
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- 239000001095 magnesium carbonate Substances 0.000 description 1
- 229910000021 magnesium carbonate Inorganic materials 0.000 description 1
- 229910012375 magnesium hydride Inorganic materials 0.000 description 1
- 239000000395 magnesium oxide Substances 0.000 description 1
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Inorganic materials [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 1
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- 229910052748 manganese Inorganic materials 0.000 description 1
- 239000011572 manganese Substances 0.000 description 1
- 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 1
- 238000001465 metallisation Methods 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 229940098779 methanesulfonic acid Drugs 0.000 description 1
- UNASZPQZIFZUSI-UHFFFAOYSA-N methylidyneniobium Chemical compound [Nb]#C UNASZPQZIFZUSI-UHFFFAOYSA-N 0.000 description 1
- 229910052750 molybdenum Inorganic materials 0.000 description 1
- 239000011733 molybdenum Substances 0.000 description 1
- YZMHQCWXYHARLS-UHFFFAOYSA-N naphthalene-1,2-disulfonic acid Chemical compound C1=CC=CC2=C(S(O)(=O)=O)C(S(=O)(=O)O)=CC=C21 YZMHQCWXYHARLS-UHFFFAOYSA-N 0.000 description 1
- SLBHRPOLVUEFSG-UHFFFAOYSA-N naphthalene-2,6-dione Chemical compound O=C1C=CC2=CC(=O)C=CC2=C1 SLBHRPOLVUEFSG-UHFFFAOYSA-N 0.000 description 1
- KVBGVZZKJNLNJU-UHFFFAOYSA-N naphthalene-2-sulfonic acid Chemical compound C1=CC=CC2=CC(S(=O)(=O)O)=CC=C21 KVBGVZZKJNLNJU-UHFFFAOYSA-N 0.000 description 1
- QEFYFXOXNSNQGX-UHFFFAOYSA-N neodymium atom Chemical compound [Nd] QEFYFXOXNSNQGX-UHFFFAOYSA-N 0.000 description 1
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- GKAOGPIIYCISHV-UHFFFAOYSA-N neon atom Chemical compound [Ne] GKAOGPIIYCISHV-UHFFFAOYSA-N 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 150000002821 niobium Chemical class 0.000 description 1
- 150000002822 niobium compounds Chemical class 0.000 description 1
- RHDUVDHGVHBHCL-UHFFFAOYSA-N niobium tantalum Chemical compound [Nb].[Ta] RHDUVDHGVHBHCL-UHFFFAOYSA-N 0.000 description 1
- 239000012299 nitrogen atmosphere Substances 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 229910052762 osmium Inorganic materials 0.000 description 1
- SYQBFIAQOQZEGI-UHFFFAOYSA-N osmium atom Chemical compound [Os] SYQBFIAQOQZEGI-UHFFFAOYSA-N 0.000 description 1
- 229910052763 palladium Inorganic materials 0.000 description 1
- YHBDIEWMOMLKOO-UHFFFAOYSA-I pentachloroniobium Chemical compound Cl[Nb](Cl)(Cl)(Cl)Cl YHBDIEWMOMLKOO-UHFFFAOYSA-I 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 150000002978 peroxides Chemical class 0.000 description 1
- 150000004965 peroxy acids Chemical class 0.000 description 1
- JRKICGRDRMAZLK-UHFFFAOYSA-L persulfate group Chemical group S(=O)(=O)([O-])OOS(=O)(=O)[O-] JRKICGRDRMAZLK-UHFFFAOYSA-L 0.000 description 1
- 125000000843 phenylene group Chemical group C1(=C(C=CC=C1)*)* 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 229910052699 polonium Inorganic materials 0.000 description 1
- HZEBHPIOVYHPMT-UHFFFAOYSA-N polonium atom Chemical compound [Po] HZEBHPIOVYHPMT-UHFFFAOYSA-N 0.000 description 1
- 229920003229 poly(methyl methacrylate) Polymers 0.000 description 1
- 229920002401 polyacrylamide Polymers 0.000 description 1
- 229920000867 polyelectrolyte Polymers 0.000 description 1
- 229920000414 polyfuran Polymers 0.000 description 1
- 239000005518 polymer electrolyte Substances 0.000 description 1
- 239000004926 polymethyl methacrylate Substances 0.000 description 1
- 229920000069 polyphenylene sulfide Polymers 0.000 description 1
- 229920002451 polyvinyl alcohol Polymers 0.000 description 1
- 239000012286 potassium permanganate Substances 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 235000019260 propionic acid Nutrition 0.000 description 1
- RUOJZAUFBMNUDX-UHFFFAOYSA-N propylene carbonate Chemical compound CC1COC(=O)O1 RUOJZAUFBMNUDX-UHFFFAOYSA-N 0.000 description 1
- IUVKMZGDUIUOCP-BTNSXGMBSA-N quinbolone Chemical compound O([C@H]1CC[C@H]2[C@H]3[C@@H]([C@]4(C=CC(=O)C=C4CC3)C)CC[C@@]21C)C1=CCCC1 IUVKMZGDUIUOCP-BTNSXGMBSA-N 0.000 description 1
- 150000004053 quinones Chemical class 0.000 description 1
- 125000004151 quinonyl group Chemical group 0.000 description 1
- 229910052705 radium Inorganic materials 0.000 description 1
- HCWPIIXVSYCSAN-UHFFFAOYSA-N radium atom Chemical compound [Ra] HCWPIIXVSYCSAN-UHFFFAOYSA-N 0.000 description 1
- 229910052704 radon Inorganic materials 0.000 description 1
- SYUHGPGVQRZVTB-UHFFFAOYSA-N radon atom Chemical compound [Rn] SYUHGPGVQRZVTB-UHFFFAOYSA-N 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 229910052702 rhenium Inorganic materials 0.000 description 1
- WUAPFZMCVAUBPE-UHFFFAOYSA-N rhenium atom Chemical compound [Re] WUAPFZMCVAUBPE-UHFFFAOYSA-N 0.000 description 1
- 229910052703 rhodium Inorganic materials 0.000 description 1
- 239000010948 rhodium Substances 0.000 description 1
- MHOVAHRLVXNVSD-UHFFFAOYSA-N rhodium atom Chemical compound [Rh] MHOVAHRLVXNVSD-UHFFFAOYSA-N 0.000 description 1
- 229910052701 rubidium Inorganic materials 0.000 description 1
- IGLNJRXAVVLDKE-UHFFFAOYSA-N rubidium atom Chemical compound [Rb] IGLNJRXAVVLDKE-UHFFFAOYSA-N 0.000 description 1
- 229910052707 ruthenium Inorganic materials 0.000 description 1
- 229910052706 scandium Inorganic materials 0.000 description 1
- SIXSYDAISGFNSX-UHFFFAOYSA-N scandium atom Chemical compound [Sc] SIXSYDAISGFNSX-UHFFFAOYSA-N 0.000 description 1
- 238000000790 scattering method Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 229910052711 selenium Inorganic materials 0.000 description 1
- 239000011669 selenium Substances 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 229910000029 sodium carbonate Inorganic materials 0.000 description 1
- 229940080264 sodium dodecylbenzenesulfonate Drugs 0.000 description 1
- 239000011775 sodium fluoride Substances 0.000 description 1
- 235000013024 sodium fluoride Nutrition 0.000 description 1
- AKHNMLFCWUSKQB-UHFFFAOYSA-L sodium thiosulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=S AKHNMLFCWUSKQB-UHFFFAOYSA-L 0.000 description 1
- 235000019345 sodium thiosulphate Nutrition 0.000 description 1
- 235000019832 sodium triphosphate Nutrition 0.000 description 1
- HIEHAIZHJZLEPQ-UHFFFAOYSA-M sodium;naphthalene-1-sulfonate Chemical compound [Na+].C1=CC=C2C(S(=O)(=O)[O-])=CC=CC2=C1 HIEHAIZHJZLEPQ-UHFFFAOYSA-M 0.000 description 1
- 238000005476 soldering Methods 0.000 description 1
- 239000007784 solid electrolyte Substances 0.000 description 1
- 239000006104 solid solution Substances 0.000 description 1
- 229910052712 strontium Inorganic materials 0.000 description 1
- CIOAGBVUUVVLOB-UHFFFAOYSA-N strontium atom Chemical compound [Sr] CIOAGBVUUVVLOB-UHFFFAOYSA-N 0.000 description 1
- 238000000859 sublimation Methods 0.000 description 1
- 230000008022 sublimation Effects 0.000 description 1
- IIACRCGMVDHOTQ-UHFFFAOYSA-N sulfamic acid Chemical compound NS(O)(=O)=O IIACRCGMVDHOTQ-UHFFFAOYSA-N 0.000 description 1
- NYPFJVOIAWPAAV-UHFFFAOYSA-N sulfanylideneniobium Chemical compound [Nb]=S NYPFJVOIAWPAAV-UHFFFAOYSA-N 0.000 description 1
- 238000005486 sulfidation Methods 0.000 description 1
- 150000003467 sulfuric acid derivatives Chemical class 0.000 description 1
- HIFJUMGIHIZEPX-UHFFFAOYSA-N sulfuric acid;sulfur trioxide Chemical compound O=S(=O)=O.OS(O)(=O)=O HIFJUMGIHIZEPX-UHFFFAOYSA-N 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 229910052714 tellurium Inorganic materials 0.000 description 1
- PORWMNRCUJJQNO-UHFFFAOYSA-N tellurium atom Chemical compound [Te] PORWMNRCUJJQNO-UHFFFAOYSA-N 0.000 description 1
- CBXCPBUEXACCNR-UHFFFAOYSA-N tetraethylammonium Chemical compound CC[N+](CC)(CC)CC CBXCPBUEXACCNR-UHFFFAOYSA-N 0.000 description 1
- 125000003698 tetramethyl group Chemical group [H]C([H])([H])* 0.000 description 1
- UEUXEKPTXMALOB-UHFFFAOYSA-J tetrasodium;2-[2-[bis(carboxylatomethyl)amino]ethyl-(carboxylatomethyl)amino]acetate Chemical compound [Na+].[Na+].[Na+].[Na+].[O-]C(=O)CN(CC([O-])=O)CCN(CC([O-])=O)CC([O-])=O UEUXEKPTXMALOB-UHFFFAOYSA-J 0.000 description 1
- 229910052716 thallium Inorganic materials 0.000 description 1
- BKVIYDNLLOSFOA-UHFFFAOYSA-N thallium Chemical compound [Tl] BKVIYDNLLOSFOA-UHFFFAOYSA-N 0.000 description 1
- 229930192474 thiophene Natural products 0.000 description 1
- DHCDFWKWKRSZHF-UHFFFAOYSA-L thiosulfate(2-) Chemical compound [O-]S([S-])(=O)=O DHCDFWKWKRSZHF-UHFFFAOYSA-L 0.000 description 1
- 229910052718 tin Inorganic materials 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
- 239000010936 titanium Substances 0.000 description 1
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 description 1
- 229910052721 tungsten Inorganic materials 0.000 description 1
- 239000010937 tungsten Substances 0.000 description 1
- 229910052720 vanadium Inorganic materials 0.000 description 1
- GPPXJZIENCGNKB-UHFFFAOYSA-N vanadium Chemical compound [V]#[V] GPPXJZIENCGNKB-UHFFFAOYSA-N 0.000 description 1
- 239000012808 vapor phase Substances 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
- 229910052724 xenon Inorganic materials 0.000 description 1
- FHNFHKCVQCLJFQ-UHFFFAOYSA-N xenon atom Chemical compound [Xe] FHNFHKCVQCLJFQ-UHFFFAOYSA-N 0.000 description 1
- 229910052727 yttrium Inorganic materials 0.000 description 1
- VWQVUPCCIRVNHF-UHFFFAOYSA-N yttrium atom Chemical compound [Y] VWQVUPCCIRVNHF-UHFFFAOYSA-N 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
- 229910052726 zirconium Inorganic materials 0.000 description 1
Images
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01G—CAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES, LIGHT-SENSITIVE OR TEMPERATURE-SENSITIVE DEVICES OF THE ELECTROLYTIC TYPE
- H01G9/00—Electrolytic capacitors, rectifiers, detectors, switching devices, light-sensitive or temperature-sensitive devices; Processes of their manufacture
- H01G9/004—Details
- H01G9/04—Electrodes or formation of dielectric layers thereon
- H01G9/048—Electrodes or formation of dielectric layers thereon characterised by their structure
- H01G9/052—Sintered electrodes
- H01G9/0525—Powder therefor
Landscapes
- Engineering & Computer Science (AREA)
- Power Engineering (AREA)
- Microelectronics & Electronic Packaging (AREA)
- Manufacture Of Metal Powder And Suspensions Thereof (AREA)
- Powder Metallurgy (AREA)
Description
本発明は、単位質量当たりの容量が大きく、漏れ電流特性、耐湿性の良好なコンデンサを安定に製造することができるニオブ粉及び焼結体、これらを用いたコンデンサ、及びそれらの製造方法に関する。 The present invention relates to niobium powder and a sintered body that can stably produce a capacitor having a large capacity per unit mass and good leakage current characteristics and moisture resistance, a capacitor using these, and a method for producing the same.
携帯電話やパーソナルコンピュータ等の電子機器に使用されるコンデンサは、小型で大容量のものが望まれている。このようなコンデンサの中でもタンタルコンデンサは大きさの割には容量が大きく、しかも性能が良好なため、好んで使用されている。さらに、最近の電子デバイスは、低電圧での作動、高周波での作動、低ノイズ化が求められており、個体電解コンデンサにおいても、より低ESR(等価直列抵抗)が求められている。 Capacitors used in electronic devices such as mobile phones and personal computers are desired to be small and have a large capacity. Among such capacitors, a tantalum capacitor is preferred because it has a large capacity for its size and good performance. Furthermore, recent electronic devices are required to operate at a low voltage, operate at a high frequency, and reduce noise, and a solid electrolytic capacitor is also required to have a lower ESR (equivalent series resistance).
タンタルコンデンサの陽極体として、一般的にタンタル粉の焼結体が使用されている。この粉体を成形後焼結することにより一体化され焼結体と言われる電極になる。この焼結体内部は、前記粉体が電気的・機械的に連結した三次元の複雑な形状をとる。この焼結体の内部空隙の表面も含めた表面に誘電体皮膜層を形成した後、対電極となる材料を含浸してコンデンサが構成される。作製されたコンデンサの容量は、誘電体皮膜層が焼結体内外部の表面に均一に付着している限り、ミクロ的には、対電極材料と誘電体皮膜層との接触状況に大きく依存する。 Generally, a tantalum powder sintered body is used as an anode body of a tantalum capacitor. By sintering this powder after molding, it is integrated into an electrode called a sintered body. The inside of the sintered body has a three-dimensional complicated shape in which the powder is electrically and mechanically connected. A dielectric film layer is formed on the surface including the surface of the internal void of the sintered body, and then a capacitor is formed by impregnating a material to be a counter electrode. The capacitance of the produced capacitor greatly depends on the contact state between the counter electrode material and the dielectric coating layer as long as the dielectric coating layer is uniformly attached to the surface outside the sintered body.
これらタンタルコンデンサの容量を上げるためには、焼結体質量を増大させるか、または、タンタル粉を微粉化して表面積を増加させた焼結体を用いる必要がある。焼結体質量を増加させる方法では、コンデンサの形状が必然的に増大して小型化の要求を満たさない。一方、タンタル粉を微粉化して比表面積を増加させる方法では、タンタル焼結体の細孔直径が小さくなり、また焼結段階で閉鎖孔が多くなり、後工程における陰極剤の含浸が困難になる。例えば、対電極材料として、燐酸水溶液を用いたとき、誘電体皮膜層層との接触状況が完全として、その時の容量出現率(陰極剤含浸率とも言う)を100%とすると、粘性の大きな電極材料、とくに固体の電極材料を使用した場合、該容量出現率を100%とすることは、困難であった。とりわけ、タンタル粉の平均粒径が小さい場合や、タンタル粉から作製した焼結体の形状が大きな場合、困難さが増加し、極端な場合には、容量出現率は、50%にも満たないこともあった。また、このような低容量出現率の場合、作製したコンデンサの耐湿性を十分得ることが出来なかった。また、タンタル焼結体を作成するためのタンタル粉が持つ細孔径が小さい場合、焼結体の持つ細孔径も必然的に小さくなり容量出現率が低くなる。その結果、ESRを低くできないという問題が生じる。 In order to increase the capacity of these tantalum capacitors, it is necessary to increase the mass of the sintered body or use a sintered body having a surface area increased by pulverizing tantalum powder. In the method of increasing the mass of the sintered body, the shape of the capacitor inevitably increases and does not satisfy the demand for downsizing. On the other hand, in the method of increasing the specific surface area by pulverizing the tantalum powder, the pore diameter of the tantalum sintered body is reduced, and the number of closed pores is increased in the sintering stage, making it difficult to impregnate the cathode agent in the subsequent process . For example, when a phosphoric acid aqueous solution is used as the counter electrode material, the contact state with the dielectric coating layer is perfect, and the capacity appearance rate (also referred to as the cathode agent impregnation rate) at that time is 100%. When using a material, particularly a solid electrode material, it was difficult to set the capacity appearance rate to 100%. In particular, when the average particle size of the tantalum powder is small or the shape of the sintered body made from the tantalum powder is large, the difficulty increases, and in an extreme case, the capacity appearance rate is less than 50%. There was also. In addition, in the case of such a low capacity appearance rate, the moisture resistance of the produced capacitor could not be obtained sufficiently. In addition, when the pore diameter of the tantalum powder for producing the tantalum sintered body is small, the pore diameter of the sintered body is inevitably small and the capacity appearance rate is low. As a result, there arises a problem that ESR cannot be lowered.
これらの欠点を解決する手段の一つとして、タンタルより大きい誘電率の誘電体の得られる電極材料を用い、高い容量出現率の得られる焼結体を作製し、これを電極としたコンデンサが考えられる。 As one of the means to solve these drawbacks, a capacitor using an electrode material capable of obtaining a dielectric having a dielectric constant larger than that of tantalum and producing a sintered body having a high capacity appearance rate can be considered. It is done.
工業的に供給可能なこのような電極材料としては、タンタルより誘電率が大きく埋蔵量も多いニオブが知られている。 As such an electrode material that can be supplied industrially, niobium having a larger dielectric constant and a larger reserve than tantalum is known.
特開昭55−157226号公報(特許文献1)には、凝集粉から粒径2.0μm、あるいはそれ以下のニオブ微粉末を加圧成形して焼結し、その成形焼結体を細かく裁断して、これにリード部を接合した後再び焼結するコンデンサ用焼結素子の製造方法が開示されている。しかしながら、該公報にはコンデンサの特性についての詳細は示されてない。 Japanese Patent Application Laid-Open No. 55-157226 (Patent Document 1) discloses that niobium fine powder having a particle size of 2.0 μm or less is pressed from an agglomerated powder and sintered, and the molded sintered body is finely cut. And the manufacturing method of the sintered element for capacitors which joins a lead part to this and sinters again is indicated. However, the publication does not give details on the characteristics of the capacitor.
米国特許4,084,965号公報には、ニオブインゴットを水素化して粉砕し、平均粒子径5.1μmのニオブ粉末を得、これを焼結して用いたコンデンサが開示されている。しかしながら、開示されているコンデンサは、漏れ電流(以下LCと略記することがある)値が大きく実用性に乏しい。 US Pat. No. 4,084,965 discloses a capacitor in which a niobium ingot is hydrogenated and pulverized to obtain niobium powder having an average particle diameter of 5.1 μm, which is sintered. However, the disclosed capacitor has a large leakage current (hereinafter sometimes abbreviated as LC) value, and is not practical.
特開平10−242004号公報(特許文献2)には、ニオブ粉の一部を窒化すること等により、LC値を改善することが開示されている。 Japanese Patent Laid-Open No. 10-224004 (Patent Document 2) discloses that the LC value is improved by nitriding a part of niobium powder.
コンデンサ用ニオブ粉のタッピング密度は、ニオブ粉を成形作業する上で重要な因子であり、これまでのものについては、タッピング密度が2.5g/mlより大きく、4g/ml程度であり、成形するためには十分ではなかった。 The tapping density of the niobium powder for capacitors is an important factor in forming the niobium powder. For the conventional ones, the tapping density is larger than 2.5 g / ml and about 4 g / ml. It wasn't enough for that.
すなわち、このようなニオブ粉を成形、焼結して焼結体を作成する場合、ニオブ粉の成形機ホッパーから金型への流れが悪く、常に一定量のニオブ粉を計量し金型に入れることが困難であった。このため、成形体の形状が常に十分に安定化せず、成形体、焼結体の強度が不足し、結果としてLCが悪いコンデンサが高頻度で生産されてしまう欠点があった。また、流れ性の悪い粉体も扱える特別な成形装置を用いたのでは、成形コストが高くなりすぎ、実用的でない。 That is, when forming a sintered body by forming and sintering such niobium powder, the flow of niobium powder from the molding machine hopper to the mold is poor, and a certain amount of niobium powder is always measured and put into the mold. It was difficult. For this reason, there is a drawback that the shape of the molded body is not always sufficiently stabilized, the strength of the molded body and the sintered body is insufficient, and as a result, a capacitor having a poor LC is frequently produced. In addition, if a special molding apparatus that can handle powder with poor flowability is used, the molding cost becomes too high and it is not practical.
このようなことから、従来既知のコンデンサ用ニオブ粉は、連続成形に十分適応できるものではなく、コンデンサの生産性が低いという問題があった。 For these reasons, the conventionally known niobium powder for capacitors is not sufficiently adaptable to continuous molding, and there is a problem that the productivity of capacitors is low.
本発明の目的は、単位質量当たりの容量が大きく、漏れ電流値が小さいコンデンサ及び耐湿性の高いコンデンサ、この電極材料となり高い容量出現率の得られる焼結体、この焼結体材料として好ましく、成形時の作業上流れ性が良好で、連続成形が容易であり、コンデンサの安定した生産が可能なニオブ粉、及びそれらの製造方法を提供することにある。 The object of the present invention is preferably a capacitor having a large capacity per unit mass and a small leakage current value and a capacitor having high moisture resistance, a sintered body that can be obtained as an electrode material and has a high capacity appearance rate, and this sintered body material. An object of the present invention is to provide a niobium powder that has good flowability in operation during molding, is easy to be continuously formed, and that enables stable production of capacitors, and a method for manufacturing the same.
本発明者らは、前述の課題を鋭意検討した。その結果、特定の細孔分布を持つニオブ焼結体、好ましくは、複数の細孔直径ピークトップを有する細孔分布を持つニオブ焼結体をコンデンサ電極に用いると、高い容量出現率が得られ、漏れ電流が低く、耐湿性の良好なコンデンサが生産できることを見出した。さらに、好ましくはタッピング密度が0.5〜2.5g/ml、さらに好ましくは平均粒子径が10〜1000μmのニオブ粉は、流れ性が良好で、連続成形が可能であり、前記焼結体材料として好ましく、このニオブ粉を用いると漏れ電流値が低いコンデンサを安定に生産できることを見出した。これらを見出し本発明を完成した。更に好ましくは、空孔分布が広く、細孔直径のピークトップが複数あり、その細孔直径ピークトップのすべてが0.5μm以上のニオブ粉を用いて作成したニオブ焼結体をコンデンサ電極に用いると高い容量出現率とともに低ESRが達成できることを見いだした。 The present inventors diligently studied the aforementioned problems. As a result, when a niobium sintered body having a specific pore distribution, preferably a niobium sintered body having a pore distribution having a plurality of pore diameter peak tops, is used for a capacitor electrode, a high capacity appearance rate can be obtained. They found that capacitors with low leakage current and good moisture resistance can be produced. Furthermore, niobium powder having a tapping density of 0.5 to 2.5 g / ml, more preferably an average particle size of 10 to 1000 μm, has good flowability and can be continuously formed. It has been found that a capacitor having a low leakage current value can be stably produced by using this niobium powder. These were found and the present invention was completed. More preferably, a niobium sintered body prepared by using niobium powder having a wide pore distribution and a plurality of peak diameter peak tops, all of which have a pore diameter peak top of 0.5 μm or more, is used as a capacitor electrode. We found that low ESR can be achieved with a high capacity appearance rate.
すなわち、本発明は、以下のニオブ粉、ニオブ焼結体、それを用いたコンデンサ、及びそれらの製造方法に関する。
1.コンデンサ電極用ニオブ焼結体において、ニオブ焼結体の細孔分布が、複数の細孔直径ピークトップを有することを特徴とするニオブ焼結体。
2.細孔分布が、2つの細孔直径ピークトップよりなる前記1に記載のニオブ焼結体。
3.複数の細孔直径ピークトップの内、相対強度が最も大きい2つのピークのピークトップが、それぞれ0.2〜0.7μm及び0.7〜3μmの範囲にある前記1または2に記載のニオブ焼結体。
4.複数の細孔直径ピークトップの内、相対強度が最も大きいピークのピークトップが、相対強度が次に大きいピークのピークトップより大径側にある前記1乃至3のいずれか1項に記載のニオブ焼結体。
5.焼結体が、細孔空隙容積を含めて10mm3以上の体積を持つ前記1乃至4に記載のニオブ焼結体。
6.焼結体が、0.2〜7m2/gの比表面積を持つ前記1乃至5に記載のニオブ焼結体。
7.焼結体の一部が、窒化している前記1乃至6に記載のニオブ焼結体。
8.焼結体が、1300℃で焼結した場合40000〜200000μFV/gのCV値を持つ焼結体を与えるニオブ成形体より得られた焼結体である前記2乃至7のいずれか1項に記載のニオブ焼結体。
9.前記1乃至8のいずれか1項に記載のニオブ焼結体を一方の電極とし、対電極との間に介在した誘電体とから構成されたコンデンサ。
10.誘電体の主成分が酸化ニオブである前記9に記載のコンデンサ。
11.対電極が、電解液、有機半導体及び無機半導体からなる群より選ばれる少なくとも1種の材料である前記9に記載のコンデンサ。
12.対電極が、有機半導体であって、該有機半導体が、ベンゾピロリン4量体とクロラニルからなる有機半導体、テトラチオテトラセンを主成分とする有機半導体、テトラシアノキノジメタンを主成分とする有機半導体及び導電性高分子からなる群より選ばれる少なくとも1種の材料である前記11に記載のコンデンサ。
13.導電性高分子が、ポリピロール、ポリチオフェン、ポリアニリン及びこれらの置換誘導体から選ばれる少なくとも1種である前記12に記載のコンデンサ。
14.導電性高分子が、下記一般式(1)又は一般式(2)
15.導電性高分子が、下記一般式(3)
16.導電性高分子が、ポリ(3,4−エチレンジオキシチオフェン)にドーパントをドープした導電性高分子である前記12に記載のコンデンサ。
17.対電極が、層状構造を少なくとも一部に有する材料からなる前記9に記載のコンデンサ。
18.対電極が、有機スルホン酸アニオンをドーパントとして含んだ材料である前記9に記載のコンデンサ。
19.ニオブ焼結体を一方の電極とし、その焼結体表面上に形成された誘電体と、前記誘電体上に設けられた対電極を含むコンデンサの製造方法であって、ニオブ焼結体が、前記1乃至8のいずれか1項に記載のニオブ焼結体であることを特徴とするコンデンサの製造方法。
20.前記9乃至18のいずれか1項に記載のコンデンサを使用した電子回路。
21.前記9乃至18のいずれか1項に記載のコンデンサを使用した電子機器。
That is, the present invention relates to the following niobium powder, a niobium sintered body, a capacitor using the niobium powder, and a manufacturing method thereof.
1. A niobium sintered body for a capacitor electrode, wherein the pore distribution of the niobium sintered body has a plurality of pore diameter peak tops.
2. 2. The niobium sintered body according to 1 above, wherein the pore distribution comprises two pore diameter peak tops.
3. 2. The niobium firing according to 1 or 2 above, wherein the peak tops of the two peaks having the highest relative intensity among the plurality of pore diameter peak tops are in the ranges of 0.2 to 0.7 μm and 0.7 to 3 μm, respectively. Union.
4). 4. The niobium according to any one of 1 to 3, wherein a peak top of a peak having the highest relative intensity among a plurality of pore diameter peak tops is located on a larger diameter side than a peak top of a peak having the next highest relative intensity. Sintered body.
5. 5. The niobium sintered body according to 1 to 4, wherein the sintered body has a volume of 10 mm 3 or more including a pore void volume.
6). 6. The niobium sintered body according to 1 to 5, wherein the sintered body has a specific surface area of 0.2 to 7 m 2 / g.
7). 7. The niobium sintered body according to 1 to 6, wherein a part of the sintered body is nitrided.
8). 8. The sintered body according to any one of 2 to 7, which is a sintered body obtained from a niobium molded body that gives a sintered body having a CV value of 40000 to 200000 μFV / g when sintered at 1300 ° C. Niobium sintered body.
9. 9. A capacitor comprising the niobium sintered body according to any one of 1 to 8 as one electrode and a dielectric interposed between the counter electrode.
10. 10. The capacitor as described in 9 above, wherein the main component of the dielectric is niobium oxide.
11. 10. The capacitor according to 9, wherein the counter electrode is at least one material selected from the group consisting of an electrolytic solution, an organic semiconductor, and an inorganic semiconductor.
12 The counter electrode is an organic semiconductor, and the organic semiconductor is an organic semiconductor composed of benzopyrroline tetramer and chloranil, an organic semiconductor composed mainly of tetrathiotetracene, and an organic semiconductor composed mainly of tetracyanoquinodimethane. 12. The capacitor as described in 11 above, which is at least one material selected from the group consisting of conductive polymers.
13. 13. The capacitor according to 12 above, wherein the conductive polymer is at least one selected from polypyrrole, polythiophene, polyaniline, and substituted derivatives thereof.
14 The conductive polymer is represented by the following general formula (1) or general formula (2).
15. The conductive polymer is represented by the following general formula (3)
16. 13. The capacitor as described in 12 above, wherein the conductive polymer is a conductive polymer obtained by doping poly (3,4-ethylenedioxythiophene) with a dopant.
17. 10. The capacitor according to 9 above, wherein the counter electrode is made of a material having at least a part of a layered structure.
18. 10. The capacitor according to 9 above, wherein the counter electrode is a material containing an organic sulfonate anion as a dopant.
19. A niobium sintered body as one electrode, a dielectric formed on the surface of the sintered body, and a capacitor manufacturing method including a counter electrode provided on the dielectric, the niobium sintered body, A method for manufacturing a capacitor, which is the niobium sintered body according to any one of 1 to 8 above.
20. 19. An electronic circuit using the capacitor according to any one of 9 to 18 above.
21. 19. An electronic device using the capacitor according to any one of 9 to 18.
タッピング密度が0.5〜2.5g/ml、平均粒子径が10〜1000μm、安息角が10〜60度、BET比表面積が0.5〜40m2/gである本発明のコンデンサ用ニオブ粉は、流れ性が良好で、連続成形が可能であり、そのニオブ粉を焼結して得られる0.01μm〜500μmの範囲内に細孔直径ピークトップを有し、好ましくは、複数の細孔直径ピークトップを有する細孔分布を持つ本発明のニオブ焼結体をコンデンサ電極に用いることにより、高い容量出現率が得られ、漏れ電流が低く、耐湿性の良好なコンデンサが生産できる。 Niobium powder for capacitors of the present invention having a tapping density of 0.5 to 2.5 g / ml, an average particle size of 10 to 1000 μm, an angle of repose of 10 to 60 degrees, and a BET specific surface area of 0.5 to 40 m 2 / g Has good flowability, can be continuously formed, has a pore diameter peak top in the range of 0.01 μm to 500 μm obtained by sintering the niobium powder, and preferably has a plurality of pores. By using the niobium sintered body of the present invention having a pore distribution with a diameter peak top as a capacitor electrode, a high capacity appearance rate is obtained, a leakage current is low, and a capacitor with good moisture resistance can be produced.
以下、漏れ電流特性や耐湿性の良好なコンデンサ、その特性を引き出し高い容量出現率の得られるニオブ焼結体、この焼結体材料として好ましい流れ性が良好で連続成形が可能なニオブ粉、及びそれらの製造方法に関し説明する。 Hereinafter, a capacitor having good leakage current characteristics and moisture resistance, a niobium sintered body that draws out the characteristics and obtains a high capacity appearance rate, niobium powder that has good flowability and can be continuously formed as a sintered body material, and These manufacturing methods will be described.
本発明では、前記コンデンサの特性を満足し、コンデンサ製造の生産性を向上させるニオブ粉として、タッピング密度が0.5〜2.5g/mlであるようなコンデンサ用ニオブ粉(単にニオブ粉と略記することもある)を使用する。ここで、コンデンサ用ニオブとは、ニオブを主成分とし、コンデンサを製造するための素材となりうるものをいう。これには、例えば、ニオブと合金となりうる成分、窒素、及び/または酸素等のニオブ以外の成分が含まれてもよい。 In the present invention, as niobium powder that satisfies the characteristics of the capacitor and improves the productivity of capacitor production, niobium powder for capacitors having a tapping density of 0.5 to 2.5 g / ml (simply abbreviated as niobium powder). May be used). Here, the niobium for a capacitor means niobium as a main component and can be a material for producing a capacitor. This may include components other than niobium such as, for example, components that can be alloyed with niobium, nitrogen, and / or oxygen.
コンデンサ用にオブ粉を次のような方法により成形、焼結してコンデンサ用焼結体(単にニオブ焼結体と略記することもある)を得、これに誘電体層、対電極を形成し、コンデンサを得ることができる。 The ob powder is formed and sintered for the capacitor by the following method to obtain a sintered body for the capacitor (sometimes abbreviated simply as a niobium sintered body), and a dielectric layer and a counter electrode are formed thereon. , You can get a capacitor.
バインダー(後述する)をトルエンやメタノールなどの有機溶剤に溶解させた溶液に、コンデンサ用ニオブ粉を入れ、これを振とう混合機、V型混合機などを用いて十分に混合する。その後、コニカルドライヤーなどの乾燥機を用い、減圧下、有機溶媒を留去して、バインダーを含んだニオブ調合粉を作製する。この調合粉を自動成形機ホッパーに入れる。ニオブ調合粉を、ホッパーから成形機金型への導入管を流して自動的に金型に自然落下しながら計量し、リード線と共に成形する。この成形体を減圧下、バインダーを除去した後、500℃〜2000℃で焼結してニオブ焼結体を作製する。そして、例えばニオブ焼結体を温度30〜90℃、濃度0.1質量%程度のリン酸、アジピン酸等の電解溶液中で、20〜60Vまで昇圧して1〜30時間化成処理し、酸化ニオブを主体とする誘電層を作成する。この誘電層上に、二酸化マンガン、二酸化鉛、導電性高分子などの固体電解質層を形成し、ついでグラファイト層、銀ペースト層を形成する。ついで、その上に陰極端子をハンダ付けなどで接続した後、樹脂で封止し固体電解コンデンサを作成する。 Niobium powder for a capacitor is put into a solution in which a binder (described later) is dissolved in an organic solvent such as toluene or methanol, and this is sufficiently mixed using a shaker, a V-type mixer or the like. Then, using a dryer such as a conical dryer, the organic solvent is distilled off under reduced pressure to produce a niobium blended powder containing a binder. This mixed powder is put into an automatic molding machine hopper. Niobium blended powder is weighed while flowing naturally through the introduction pipe from the hopper to the molding machine mold, and molded together with the lead wire. After the binder is removed under reduced pressure, the compact is sintered at 500 ° C. to 2000 ° C. to produce a niobium sintered body. For example, the niobium sintered body is subjected to chemical conversion treatment for 1 to 30 hours by raising the pressure to 20 to 60 V in an electrolytic solution such as phosphoric acid and adipic acid having a temperature of 30 to 90 ° C. and a concentration of about 0.1% by mass. Create a dielectric layer mainly composed of niobium. A solid electrolyte layer such as manganese dioxide, lead dioxide, or conductive polymer is formed on the dielectric layer, and then a graphite layer and a silver paste layer are formed. Next, a cathode terminal is connected thereto by soldering or the like, and then sealed with resin to produce a solid electrolytic capacitor.
このため、適度な流れ性や安息角を持たない調合粉では、ホッパーから金型に流れにくく安定に成形できない。特に振動などの方法を用いてホッパーから輸送するため、調合粉のタッピング密度や平均粒子径が大きすぎても小さすぎても、成形体の質量、焼結体強度や形状のバラツキが大きくなり、欠け、割れが発生することもあり、結果として漏れ電流値が悪くなる。この様に調合粉のタッピング密度、平粒子径、流れ性及び安息角は、良好な焼結体及びコンデンサを作製する上での重要な要素となる。 For this reason, in the mixed powder which does not have moderate flowability and angle of repose, it cannot flow stably from a hopper to a metal mold, and cannot be formed stably. Especially because it is transported from the hopper using a method such as vibration, even if the tapping density and average particle size of the blended powder are too large or too small, the mass of the molded body, the strength of the sintered body and the variation in shape will increase. Chipping and cracking may occur, resulting in a poor leakage current value. As described above, the tapping density, the flat particle diameter, the flowability and the angle of repose of the blended powder are important factors in producing a good sintered body and capacitor.
調合粉のこのような物性はバインダーとの調合前後でほとんど変化せず、調合粉の物性は使用したコンデンサ用ニオブ粉の物性で決定される。そのため使用するニオブ粉のタッピング密度、平均粒子径、流れ性、安息角などが重要となる。ニオブ粉の流れ性や安息角は、タッピング密度、や平均粒子径の影響を大きく受けるため、タッピング密度、や平均粒子径が重要な要素となる。 Such physical properties of the blended powder hardly change before and after blending with the binder, and the physical properties of the blended powder are determined by the physical properties of the used capacitor niobium powder. Therefore, the tapping density, average particle diameter, flowability, angle of repose, etc. of the niobium powder used are important. Since the flowability and angle of repose of niobium powder are greatly affected by the tapping density and the average particle diameter, the tapping density and the average particle diameter are important factors.
流れ性や安息角の改善に伴う生産性及び焼結体強度の向上、及びそれに伴う漏れ電流値の低減の効果を得るために、本発明においてはタッピング密度は、0.5〜2.5g/mlが好ましく、0.8〜1.9g/mlが特に好ましい。また、本発明のニオブ粉の平均粒子径は、10〜1000μmが好ましく、50〜200μmが特に好ましい。 In order to obtain the effect of improving the productivity and the strength of the sintered body accompanying the improvement of the flowability and the angle of repose, and the accompanying reduction of the leakage current value, in the present invention, the tapping density is 0.5 to 2.5 g / ml is preferred, and 0.8 to 1.9 g / ml is particularly preferred. Moreover, 10-1000 micrometers is preferable and, as for the average particle diameter of the niobium powder of this invention, 50-200 micrometers is especially preferable.
成形機ホッパーから金型へニオブ粉を自然落下させるためには、本発明のニオブ粉の安息角は、10〜60度が好ましく、さらには10〜50度が特に好ましい。 In order for the niobium powder to fall naturally from the molding machine hopper to the mold, the repose angle of the niobium powder of the present invention is preferably 10 to 60 degrees, more preferably 10 to 50 degrees.
上記の様な物性を持つニオブ粉は、ニオブ粉またはニオブ化合物粉(以下、これらを「原料ニオブ粉」と記載する)と、賦活剤(「細孔形成剤」とも言う。以下、「添加物」と記載することもある)とを含む混合物(以下、「原料混合物」と記載する)を原料とし、少なくとも焼結工程、解砕工程を順次経て製造することができる。賦活剤は、原料混合物から本発明のニオブ粉を製造する焼結工程または解砕工程のいずれかの工程で除去される。賦活剤の除去は、前記焼結工程や解砕工程とは独立して行なってもよい。 Niobium powder having the above physical properties is also referred to as niobium powder or niobium compound powder (hereinafter referred to as “raw niobium powder”) and an activator (“pore forming agent”. And the like (hereinafter referred to as “raw material mixture”) as a raw material, and can be produced through at least a sintering step and a pulverizing step. The activator is removed in any step of the sintering step or the crushing step for producing the niobium powder of the present invention from the raw material mixture. The removal of the activator may be performed independently of the sintering step and the crushing step.
賦活剤を除去する方法は、賦活剤の化学的性質により、任意に種々の方法を採用することができ、賦活剤を除去しやすい方法をいずれか1つまたは複数を組み合わせて用いればよい。賦活剤を除去する方法としては、例えば、賦活剤を蒸発、昇華または熱分解し気体にすることにより除去する方法、溶媒で賦活剤を溶解することにより除去する方法が挙げられる。 As a method for removing the activator, various methods can be arbitrarily adopted depending on the chemical properties of the activator, and any one or more methods that can easily remove the activator may be used in combination. Examples of the method for removing the activator include a method for removing the activator by evaporating, sublimating or thermally decomposing it into a gas, and a method for removing the activator by dissolving it in a solvent.
賦活剤を気体にして除去する場合、焼結工程で行なうか、または焼結前に加熱及び/または減圧により賦活剤を除去する工程を設けてもよい。賦活剤を溶媒に溶解し除去する場合、原料混合物を焼結後、または解砕中、または解砕後に後述する溶媒と焼結物またはその解砕物とを接触させることにより賦活剤を溶解除去する。 When removing the activator as a gas, it may be performed in a sintering step, or a step of removing the activator by heating and / or decompression before sintering may be provided. When the activator is dissolved and removed in a solvent, the activator is dissolved and removed by bringing the solvent, which will be described later, into contact with the sintered product or its crushed material after sintering, during or after crushing the raw material mixture. .
また、原料混合物から本発明のニオブ粉を製造する工程中のいずれかにおいて、ニオブ粉の一部を窒化、ホウ化、炭化、または硫化する工程を設けてもよい。 Further, in any of the steps of producing the niobium powder of the present invention from the raw material mixture, a step of nitriding, boriding, carbonizing, or sulfiding a part of the niobium powder may be provided.
以下、本発明のニオブ粉の製造方法について詳しく説明する。原料ニオブ粉としては、ニオブ、水素化ニオブ、ニオブ合金、及び水素化ニオブ合金より選ばれる少なくとも1種の粉体を用いることができる。また、これらの一部が、窒化、硫化、炭化、またはホウ化しているものであってもよい。なお、本発明で用いる合金とは、他方の合金成分との固溶体を含むものである。原料ニオブ粉の平均粒子径は0.01〜10μmが好ましく、0.02〜5μmが更に好ましく、0.05〜2μmが特に好ましくい。 Hereinafter, the manufacturing method of the niobium powder of the present invention will be described in detail. As the raw material niobium powder, at least one kind of powder selected from niobium, niobium hydride, niobium alloy, and niobium hydride alloy can be used. Some of these may be nitrided, sulfided, carbonized, or borated. The alloy used in the present invention includes a solid solution with the other alloy component. The average particle diameter of the raw material niobium powder is preferably 0.01 to 10 μm, more preferably 0.02 to 5 μm, and particularly preferably 0.05 to 2 μm.
原料ニオブ粉となるニオブを得る方法は、例えば、ニオブインゴット、ニオブペレット、ニオブ粉などを水素化し、粉砕し、脱水素する方法、フッ化ニオブ酸カリウムをナトリウムなどで還元物し粉砕する方法、酸化ニオブを、水素、炭素、マグネシウム、アルミニウム等の少なくとも1種を使用して還元し、該還元物を粉砕する方法、あるいはハロゲン化ニオブを水素還元する方法、等が挙げれられる。 The method of obtaining niobium as raw material niobium powder is, for example, a method of hydrogenating niobium ingot, niobium pellets, niobium powder, etc., pulverizing and dehydrogenating, a method of reducing potassium fluorinated niobate with sodium etc. Examples thereof include a method of reducing niobium oxide using at least one of hydrogen, carbon, magnesium, aluminum and the like, pulverizing the reduced product, or a method of reducing niobium halide with hydrogen.
原料ニオブ粉となる水素化ニオブを得る方法は、例えば、ニオブインゴット、ニオブペレット、ニオブ粉等を水素化し、粉砕する方法が挙げれられる。 Examples of the method for obtaining niobium hydride to be a raw material niobium powder include a method in which niobium ingot, niobium pellets, niobium powder and the like are hydrogenated and pulverized.
また、原料ニオブ粉となる水素化ニオブ合金を得る方法は、例えば、ニオブ合金インゴット、ニオブ合金ペレット、またはニオブ合金粉など、これらの水素化物を粉砕する方法により得ることができる。原料ニオブ粉となるニオブ合金を得る方法は、この水素化ニオブ合金を脱水素する方法がある。 Moreover, the method of obtaining the niobium hydride alloy used as raw material niobium powder can be obtained by a method of pulverizing these hydrides such as niobium alloy ingot, niobium alloy pellets, or niobium alloy powder. As a method for obtaining a niobium alloy as raw material niobium powder, there is a method of dehydrogenating this niobium hydride alloy.
前記ニオブ合金、水素化ニオブ合金は、ニオブ以外の他の合金成分として、原子番号88以下の元素からなる群から、水素、窒素、酸素、フッ素、塩素、臭素、沃素、ニオブ、ヘリウム、ネオン、クリプトン、アルゴン、キセノン、及びラドンを除いた群から選ばれた少なくとも1種の元素を含む。 The niobium alloy, the niobium hydride alloy, as an alloy component other than niobium, from the group consisting of elements having an atomic number of 88 or less, hydrogen, nitrogen, oxygen, fluorine, chlorine, bromine, iodine, niobium, helium, neon, It contains at least one element selected from the group excluding krypton, argon, xenon, and radon.
賦活剤は、原料混合物から本発明のニオブ粉を製造するいずれかの工程中で除去可能な物質である。通常、本発明のニオブ粉中で、賦活剤が除去された部分は細孔を形成する。 An activator is a substance that can be removed in any step of producing the niobium powder of the present invention from a raw material mixture. Usually, in the niobium powder of the present invention, the portion from which the activator is removed forms pores.
賦活剤の粒径は、本発明のニオブ粉の細孔直径に影響し、ニオブ粉の細孔直径はニオブ焼結体の細孔直径に影響し、焼結体の細孔直径はコンデンサの容量及びコンデンサ製造工程における陰極剤の含浸性に影響する。 The particle size of the activator affects the pore diameter of the niobium powder of the present invention, the pore diameter of the niobium powder affects the pore diameter of the niobium sintered body, and the pore diameter of the sintered body indicates the capacitance of the capacitor. And the impregnation property of the cathode agent in the capacitor manufacturing process.
陰極剤の含浸性は、高い容量をもち、かつ低いESRのコンデンサの作成に大きく影響を与える。ニオブ焼結体は、ニオブ粉を加圧成形して作成するため、焼結体の持つ細孔直径は、必然的にニオブ粉の持つ細孔直径より小さくなる。小さな細孔直径ピークを持つ粉体から作成した焼結体に対する陰極剤の含浸性の困難さから考えると、ニオブ粉の持つ細孔直径は、平均径として0.5μm以上、とりわけ1μm以上であることが望ましい。 The impregnation property of the cathodic agent has a great influence on the production of a capacitor having a high capacity and a low ESR. Since the niobium sintered body is prepared by press-molding niobium powder, the pore diameter of the sintered body is necessarily smaller than the pore diameter of niobium powder. Considering the difficulty of impregnation of the cathode material into the sintered body prepared from the powder having a small pore diameter peak, the niobium powder has an average pore diameter of 0.5 μm or more, particularly 1 μm or more. It is desirable.
これら細孔直径は、平均径として、0.01〜500μmが好ましく、0.03〜300μmがさらに好ましく、0.1〜200μmが特に好ましい。そのため、賦活剤の平均粒子径は、0.01〜500μmが好ましく、0.03〜300μmがさらに好ましく、0.1〜200μmが特に好ましい。 The average diameter of these pores is preferably 0.01 to 500 μm, more preferably 0.03 to 300 μm, and particularly preferably 0.1 to 200 μm. Therefore, the average particle diameter of the activator is preferably 0.01 to 500 μm, more preferably 0.03 to 300 μm, and particularly preferably 0.1 to 200 μm.
最も好ましいニオブ粉の細孔直径は、平均径として0.5μm〜100μmであり、この細孔直径を作り出す最も好ましい賦活剤の平均粒子径は、0.5μm〜100μmである。これらの細孔直径を小さくするには、粒径の小さな賦活剤を用いればよく、大きくするには、粒径の大きな賦活剤を用いればよい。 The most preferable niobium powder has a pore diameter of 0.5 μm to 100 μm as an average diameter, and the most preferable average particle diameter of the activator for producing the pore diameter is 0.5 μm to 100 μm. In order to reduce these pore diameters, an activator having a small particle size may be used, and in order to increase the pore diameter, an activator having a large particle size may be used.
また、賦活剤の粒度分布を調整することにより細孔直径分布を調整できる。陰極剤の含浸性の問題が無く、十分な容量を持つコンデンサを得るには、ニオブ焼結体中に、所望の容量が得られる程度に小さい細孔と、陰極剤が十分含浸する程度に大きい細孔とを、陰極剤の物性に合わせ適度に設けることが好ましい。 Further, the pore diameter distribution can be adjusted by adjusting the particle size distribution of the activator. In order to obtain a capacitor having a sufficient capacity without the problem of impregnation of the cathodic agent, the niobium sintered body is small enough to obtain a desired capacity, and large enough to be sufficiently impregnated with the cathodic agent. It is preferable that the pores are appropriately provided in accordance with the physical properties of the cathode agent.
ニオブ粉またはニオブ焼結体の細孔直径分布を調整するには、例えば、ピークトップを2つ以上有する粒度分布を持つ賦活剤(粉体)を用い、ニオブ粉にピークトップが2つ以上ある細孔直径分布を持たせることができる。このニオブ粉を焼結することにより、同等な細孔直径のピークトップが2つ以上ある細孔径分布を持つニオブ焼結体を得ることができる。この場合、細孔直径ピークトップは、0.01〜500μmの範囲内にあることが好ましく、0.03〜300μmがより好ましく、0.1〜200μmがさらに好ましく、0.1〜30μmが特に好ましく、0.2〜3μmが最も好ましい。 In order to adjust the pore diameter distribution of the niobium powder or the niobium sintered body, for example, an activator (powder) having a particle size distribution having two or more peak tops is used, and the niobium powder has two or more peak tops. A pore diameter distribution can be provided. By sintering the niobium powder, a niobium sintered body having a pore size distribution having two or more peak tops having the same pore diameter can be obtained. In this case, the pore diameter peak top is preferably in the range of 0.01 to 500 μm, more preferably 0.03 to 300 μm, further preferably 0.1 to 200 μm, and particularly preferably 0.1 to 30 μm. 0.2 to 3 μm is most preferable.
このようなニオブ焼結体を与えるニオブ粉は、2つ以上の細孔直径ピークトップをもつ。このニオブ粉の2つ以上の細孔直径ピークトップは、いずれも0.5μm以上であることが望ましい。例えば、0.7μmと3μmに2つの細孔直径ピークトップを持つニオブ焼結体を作成する場合、ニオブ粉の持つ2つの細孔直径ピークトップを、例えば、約1.5μmと約25μmに調整してやればよい。 The niobium powder that gives such a niobium sintered body has two or more pore diameter peak tops. The niobium powder preferably has two or more pore diameter peak tops of 0.5 μm or more. For example, when creating a niobium sintered body having two pore diameter peak tops at 0.7 μm and 3 μm, the two pore diameter peak tops of niobium powder are adjusted to, for example, about 1.5 μm and about 25 μm. Just do it.
このような約1.5μmの小さいな細孔直径を与える賦活剤の平均粒径は約1.5μmであり、約25μmの大きな細孔直径を与える賦活剤の平均粒径は約25μmである。通常、小さな細孔直径と大きな細孔直径がニオブ粉に存在する場合、加圧成形時に大きな細孔直径はつぶされて小さくなる。したがって、大きな細孔直径ピークトップは、20μm以上にあることが望ましい。細孔直径ピークトップが3つの場合でも大きな細孔直径ピークトップは、20μm以上であることが望ましい。また、全空孔容積の30体積%以上が20μm以上の細孔直径を有することが望ましく、40体積%以上であることが特に好ましい。 The average particle size of the activator that gives such a small pore diameter of about 1.5 μm is about 1.5 μm, and the average particle size of the activator that gives a large pore diameter of about 25 μm is about 25 μm. Usually, when a small pore diameter and a large pore diameter are present in niobium powder, the large pore diameter is crushed and becomes smaller during pressure molding. Therefore, it is desirable that the large pore diameter peak top be 20 μm or more. Even when there are three pore diameter peak tops, the large pore diameter peak top is desirably 20 μm or more. Further, it is desirable that 30% by volume or more of the total pore volume has a pore diameter of 20 μm or more, and particularly preferably 40% by volume or more.
さらに上記の例について、図を用いて詳しく説明する。図1は、本発明のニオブ粉の様子を模式的に示す断面図である。本発明のニオブ粉は、1次粉が賦活剤によって形成された特定の細孔を持った造粒粉である。細孔Aは平均粒径が約1.5μmの賦活剤によって形成された細孔であり、細孔Bは平均粒径が約25μmの賦活剤によって形成された細孔である。このように、1次粉同士を効率的に凝集させることが可能である。図2は、本発明のニオブ粉の細孔分布を水銀圧入法で測定した場合の概略図である。ピークAは、約1.5μmの賦活剤が形成した細孔Aのピークであり、ピークBは約25μmの賦活剤が形成した細孔Bのピークである。また、ピークBの高さはピークAより高く、全空孔容積44%が20μm以上の細孔直径である。 Further, the above example will be described in detail with reference to the drawings. FIG. 1 is a cross-sectional view schematically showing the state of the niobium powder of the present invention. The niobium powder of the present invention is a granulated powder having specific pores in which the primary powder is formed by an activator. The pore A is a pore formed by an activator having an average particle size of about 1.5 μm, and the pore B is a pore formed by an activator having an average particle size of about 25 μm. Thus, it is possible to agglomerate primary powders efficiently. FIG. 2 is a schematic view when the pore distribution of the niobium powder of the present invention is measured by a mercury intrusion method. Peak A is the peak of pore A formed by an activator of about 1.5 μm, and peak B is the peak of pore B formed by an activator of about 25 μm. The height of the peak B is higher than that of the peak A, and the total pore volume 44% is a pore diameter of 20 μm or more.
粒度分布のピークトップを2つ以上持つ賦活剤は、例えば、粒度分布のピークトップの異なる賦活剤を2種類以上混合することにより得ることができる。 An activator having two or more peak tops in the particle size distribution can be obtained, for example, by mixing two or more activators having different peak tops in the particle size distribution.
賦活剤となる物質としては、例えば、焼結温度以下で気体となる物質、または少なくとも焼結後に溶媒に可溶である物質が挙げられる。 Examples of the substance serving as the activator include a substance that becomes a gas at a sintering temperature or lower, or a substance that is at least soluble in a solvent after sintering.
焼結温度以下で気体となる物質としては、例えば、蒸発、昇華または熱分解して気体となる物質等が挙げられ、低温においても残留物を残さず容易に気体になる安価な物質が好ましい。このような物質として、例えば、ナフタレン、アントラセン、キノンなどの芳香族化合物、樟脳、NH4Cl、ZnO、WO2、SnO2、MnO3、有機物ポリマーが挙げられる。 Examples of the substance that becomes a gas below the sintering temperature include a substance that becomes a gas by evaporation, sublimation, or thermal decomposition, and an inexpensive substance that easily becomes a gas without leaving a residue even at a low temperature is preferable. Examples of such substances include aromatic compounds such as naphthalene, anthracene, and quinone, camphor, NH 4 Cl, ZnO, WO 2 , SnO 2 , MnO 3 , and organic polymers.
有機物ポリマーとしては、例えば、ポリアクリル酸、ポリアクリル酸エステル、ポリアクリルアミド、ポリメタクリル酸、ポリメタクリル酸エステル、ポリメタクリルアミド、ポリビニルアルコールが挙げられる。 Examples of the organic polymer include polyacrylic acid, polyacrylic acid ester, polyacrylamide, polymethacrylic acid, polymethacrylic acid ester, polymethacrylamide, and polyvinyl alcohol.
少なくとも焼結後に可溶性である物質としては、賦活剤またはその熱分解物の残留物が溶媒に可溶である物質であり、焼結の後、解砕中、または解砕の後に、後述する溶媒に容易に溶解する物質が特に好ましいが、溶媒との組み合わせにより多くの物質から選ぶことができる。 The substance that is soluble at least after sintering is a substance in which the activator or the residue of its thermal decomposition product is soluble in the solvent, and the solvent described later after sintering, during crushing, or after crushing Substances that readily dissolve in water are particularly preferred, but can be selected from many substances in combination with solvents.
このような物質としては、例えば、金属と炭酸、硫酸、亜硫酸、ハロゲン、過ハロゲン酸、次亜ハロゲン酸、硝酸、亜硝酸、燐酸、酢酸、蓚酸、または硼酸との化合物、金属酸化物、金属水酸化物、及び金属が挙げられる。好ましくは、酸、アルカリ、アンモニウム塩溶液などの溶媒への溶解度が大きい化合物であり、例えば、リチウム、ナトリウム、カリウム、ルビジウム、セシウム、及びフランシウム、ベリリウム、マグネシウム、カルシウム、ストロンチウム、バリウム、ラジウム、スカンジウム、イットリウム、セリウム、ネオジム、エルビウム、チタン、ジルコニウム、ハフニウム、バナジウム、ニオブ、タンタル、モリブデン、タングステン、マンガン、レニウム、ルテニウム、オスミウム、コバルト、ロジウム、イリジウム、ニッケル、パラジウム、白金、銀、金、亜鉛、カドミウム、アルミニウム、ガリウム、インジウム、タリウム、ゲルマニウム、錫、鉛、アンチモン、ビスマス、セレン、テルル、ポロニウム、硼素、珪素、及び砒素よりなる群から選ばれた少なくとも1種を含む化合物が挙げられる。これらの中で好ましくは金属塩であり、さらに好ましくは、例えば、酸化バリウム、硝酸マンガン(II)、炭酸カルシウム等が挙げられる。これら前記賦活剤は、単独で用いても良いし、2種類以上を組み合わせて用いても何ら問題はない。 Examples of such materials include compounds of metal and carbonic acid, sulfuric acid, sulfurous acid, halogen, perhalogenic acid, hypohalous acid, nitric acid, nitrous acid, phosphoric acid, acetic acid, oxalic acid, or boric acid, metal oxides, metals A hydroxide and a metal are mentioned. Preferably, it is a compound having high solubility in a solvent such as acid, alkali, ammonium salt solution, for example, lithium, sodium, potassium, rubidium, cesium, and francium, beryllium, magnesium, calcium, strontium, barium, radium, scandium. Yttrium, cerium, neodymium, erbium, titanium, zirconium, hafnium, vanadium, niobium, tantalum, molybdenum, tungsten, manganese, rhenium, ruthenium, osmium, cobalt, rhodium, iridium, nickel, palladium, platinum, silver, gold, zinc , Cadmium, aluminum, gallium, indium, thallium, germanium, tin, lead, antimony, bismuth, selenium, tellurium, polonium, boron, silicon, and arsenic Compounds containing at least one selected from the like. Of these, metal salts are preferable, and barium oxide, manganese (II) nitrate, calcium carbonate, and the like are more preferable. These activators may be used alone or in combination of two or more without any problem.
特定の細孔を効率よく形成することを考えると、焼結温度で固体として存在する物質が好ましい。このことは、焼結温度において、賦活剤が固体で存在することによりニオブ1次粉の必要以上な凝集をブロックして、ニオブ同士の接点でのみニオブ同士の融着を起こさせるためである。焼結温度において、液体または気体で存在する場合は、ブロックする効果が小さく、望む細孔より小さな細孔を形成する場合がある。したがって、低融点な物質、例えば、アルミニウム金属、マグネシウム金属、水素化マグネシウム、カルシウム金属などを賦活剤として用いた場合よりも、高い融点、例えば酸化バリウム、炭酸カルシウム、酸化アルミニウム、酸化マグネシウム、などを賦活剤として用いた方が細孔径は安定する。 Considering efficient formation of specific pores, a substance that exists as a solid at the sintering temperature is preferred. This is because, at the sintering temperature, the activator is present as a solid, thereby blocking the aggregation of the niobium primary powder more than necessary and causing the fusion of niobium only at the contact points of niobium. When present in a liquid or gas at the sintering temperature, the blocking effect is small, and pores smaller than the desired pores may be formed. Therefore, a higher melting point, for example, barium oxide, calcium carbonate, aluminum oxide, magnesium oxide, etc., than when a low melting point material such as aluminum metal, magnesium metal, magnesium hydride, calcium metal or the like is used as an activator. The pore diameter is more stable when used as an activator.
賦活剤の添加量は、少なければ、タッピング密度及び安息角が大きくなり、多ければタッピング密度は小さくなり焼結段階での閉鎖孔が多くなる。焼結段階での閉鎖孔の問題が無く、安息角60度以下で、タッピング密度0.5〜2.5g/mlを得るには、賦活剤の平均粒子径によっても変わるが、一般的には、原料ニオブに対して1質量%以上40質量%以下(以下、特に断りの無い限り質量%を単に%と略記する)、好ましくは5%以上25%以下、さらに好ましくは10%以上20%以下である。 If the addition amount of the activator is small, the tapping density and the angle of repose become large, and if it is large, the tapping density becomes small and the number of closed holes in the sintering stage increases. In order to obtain a tapping density of 0.5 to 2.5 g / ml at an angle of repose of 60 degrees or less without the problem of closed pores in the sintering stage, it varies depending on the average particle diameter of the activator. 1% by mass to 40% by mass with respect to the raw material niobium (hereinafter, unless otherwise specified, mass% is simply abbreviated as%), preferably 5% or more and 25% or less, more preferably 10% or more and 20% or less. It is.
原料混合物は、前述の賦活剤と前述のニオブ原料とを、粉体同士で無溶媒で混合したものでもよいし、適当な溶媒を用いて両者を混合し乾燥したものでもよい。 The raw material mixture may be a mixture of the above-described activator and the above-mentioned niobium raw material without solvent, or a mixture obtained by mixing both using a suitable solvent and drying.
使用できる溶媒としては、水、アルコール類、エーテル類、セルソルブ類、ケトン類、脂肪族炭化水素類、芳香族炭化水素類、ハロゲン化炭化水素類などが挙げられる。混合には混合機を用いることも出来る。混合機としては、振とう混合機、V型混合機、ナウターミキサーなど、通常の装置が問題なく使用できる。混合における温度は、溶媒の沸点、凝固点により制限されるが、一般的には、−50℃〜120℃、好ましくは−50℃〜50℃、さらに好ましくは、−10℃〜30℃である。混合にかかる時間は、10分以上であれば特に制限はないが、通常1〜6時間であり、窒素、アルゴンなどの不活性ガスを用いて無酸素雰囲気下で行うことが望ましい。 Examples of the solvent that can be used include water, alcohols, ethers, cellosolves, ketones, aliphatic hydrocarbons, aromatic hydrocarbons, halogenated hydrocarbons, and the like. A mixer can also be used for mixing. As the mixer, ordinary apparatuses such as a shake mixer, a V-type mixer, and a Nauta mixer can be used without any problem. Although the temperature in mixing is limited by the boiling point and freezing point of the solvent, it is generally -50 ° C to 120 ° C, preferably -50 ° C to 50 ° C, more preferably -10 ° C to 30 ° C. The time required for mixing is not particularly limited as long as it is 10 minutes or longer, but it is usually 1 to 6 hours, and it is desirable to carry out in an oxygen-free atmosphere using an inert gas such as nitrogen or argon.
溶媒を用いた場合、得られた混合物をコニカルドライヤー、棚段式乾燥機などを用いて、80℃未満、好ましくは50℃未満で乾燥する。80℃以上の温度で乾燥すると、ニオブまたは水素化ニオブ微粉の酸素量が増加するため好ましくない。 When a solvent is used, the obtained mixture is dried at a temperature of less than 80 ° C., preferably less than 50 ° C., using a conical dryer or a shelf dryer. Drying at a temperature of 80 ° C. or higher is not preferable because the amount of oxygen in niobium or niobium hydride fine powder increases.
賦活剤が焼結温度以下でガスとなる場合、焼結時に賦活剤を除去することも可能だが、賦活剤の化学的性質に合わせ除去しやすい温度、圧力、時間等の条件下で、焼結前に賦活剤を気体にして除去する工程を独立に設けてもよい。この場合、例えば、100℃〜800℃、減圧下、数時間で賦活剤を留去する。 When the activator becomes a gas below the sintering temperature, it is possible to remove the activator during sintering, but sintering under conditions such as temperature, pressure, time, etc. that are easy to remove in accordance with the chemical properties of the activator. A step of removing the activator in the form of gas may be independently provided. In this case, for example, the activator is distilled off at 100 ° C. to 800 ° C. under reduced pressure for several hours.
また、原料ニオブとして水素化ニオブまたは水素化ニオブ合金を用いた場合、賦活剤の種類にかかわらず、本工程を行うことで脱水素することができる。 When niobium hydride or a niobium hydride alloy is used as the raw material niobium, dehydrogenation can be performed by performing this step regardless of the type of the activator.
焼結工程は、減圧下またはアルゴンなどの還元雰囲気下で、500℃〜2000℃、好ましくは800℃〜1500℃、さらに好ましくは1000℃〜1300℃、で行なう。好ましくは、焼結終了後、ニオブの温度(品温とも略する)が30℃以下になるまで冷却し、0.01体積%〜10体積%、好ましくは、0.1体積%〜1体積%の酸素を含む窒素やアルゴンなどの不活性ガスを品温が30℃を越えないように徐々に加え、8時間以上放置後取り出し、焼結塊を得る。解砕工程では、焼結塊をロールグラニュレーターなどの解砕機を用いて、適当な粒径に解砕する。 The sintering step is performed at 500 ° C. to 2000 ° C., preferably 800 ° C. to 1500 ° C., more preferably 1000 ° C. to 1300 ° C. under reduced pressure or a reducing atmosphere such as argon. Preferably, after the sintering is completed, the niobium is cooled until the temperature of the niobium (also abbreviated as the product temperature) is 30 ° C. or less, and is 0.01 vol% to 10 vol%, preferably 0.1 vol% to 1 vol% An inert gas such as nitrogen or argon containing oxygen is gradually added so that the product temperature does not exceed 30 ° C., and is left for 8 hours or longer to obtain a sintered ingot. In the crushing step, the sintered ingot is crushed to an appropriate particle size using a crusher such as a roll granulator.
賦活剤が、少なくとも焼結工程後に溶媒に可溶である場合、焼結後で解砕前、解砕中、解砕後、またはこれら複数の工程で適当な溶媒を焼結塊または解砕粉に接触させ、賦活剤成分を溶解し除去する。除去し易さから、解砕後の解砕粉から溶解除去するのが好ましい。 If the activator is soluble in the solvent at least after the sintering step, an appropriate solvent is sintered or crushed powder after sintering, before crushing, during crushing, after crushing, or in these multiple steps The activator component is dissolved and removed. From the viewpoint of easy removal, it is preferable to dissolve and remove from the crushed powder after pulverization.
ここで用いる溶媒としては、溶解すべき賦活剤の溶解度が十分に得られる溶媒であり、好ましくは、安価で残留しにくいものがよい。例えば、賦活剤が、水溶性ならば水を用い、有機溶剤可溶性ならば、メチルイソブチルケトン、エタノール、ジメチルスルホキルシド(DMSO)等の有機溶媒を用い、酸可溶性ならば、硝酸、硫酸、リン酸、硼酸、炭酸、フッ化水素酸、塩酸、臭化水素酸、沃化水素酸、有機酸等の酸溶液を用い、アルカリ可溶性ならば、アルカリ金属の水酸化物、アルカリ土類金属の水酸化物、アンモニア等のアルカリ溶液を用い、可溶性錯体を形成するならば、その配位子となるアンモニア、エチレンジアミン等のアミン類、グリシン等のアミノ酸類、トリポリ燐酸ナトリウム等のポリリン酸類、クラウンエーテル類、チオ硫酸ナトリウム等のチオ硫酸塩、エチレンジアミン四酢酸等のキレート剤等の溶液を用いればよい。 As a solvent used here, it is a solvent from which the solubility of the activator which should be melt | dissolved is obtained sufficiently, Preferably, what is cheap and cannot remain easily is good. For example, if the activator is water-soluble, use water. If the activator is soluble in organic solvents, use an organic solvent such as methyl isobutyl ketone, ethanol, or dimethylsulfoalkylside (DMSO). If it is acid-soluble, use nitric acid, sulfuric acid, phosphorus. If an acid solution such as acid, boric acid, carbonic acid, hydrofluoric acid, hydrochloric acid, hydrobromic acid, hydroiodic acid, or organic acid is used and is alkali-soluble, alkali metal hydroxide, alkaline earth metal water If an alkaline solution such as oxide or ammonia is used to form a soluble complex, the ligand is ammonia, amines such as ethylenediamine, amino acids such as glycine, polyphosphoric acids such as sodium tripolyphosphate, crown ethers A solution of a thiosulfate such as sodium thiosulfate or a chelating agent such as ethylenediaminetetraacetic acid may be used.
また、塩化アンモニウム、硝酸アンモニウム、硫酸アンモニウムなどのアンモニウム塩の溶液や陽イオン交換樹脂、陰イオン交換樹脂なども好適に使用できる。賦活剤の溶解除去する温度は、低いことが望ましい。ニオブは酸素との親和性が高いため、溶解除去する温度が高いとニオブ表面が酸化される。したがって、50℃以下が好ましい。−10℃〜40℃で溶解除去することが好ましく、0℃〜30℃で行うことが特に好ましい。また、前記理由により、溶解除去する際に発熱が少ない方法を選択することが好ましい。例えば、賦活剤に金属酸化物や金属を用いた場合、酸で溶解除去する方法は、中和熱などが発生する。したがって、たとえば、水や有機溶剤に溶解させる方法、硝酸アンモニウム塩水溶液やエチレンジアミン4酢酸などを用いて可溶性錯体を形成する方法、イオン交換樹脂を含む溶液に溶解する方法などの発熱しにくい方法を選択することもできる。 Also, ammonium salt solutions such as ammonium chloride, ammonium nitrate, and ammonium sulfate, cation exchange resins, and anion exchange resins can be suitably used. It is desirable that the temperature at which the activator is removed by dissolution is low. Since niobium has a high affinity with oxygen, the surface of niobium is oxidized when the temperature for dissolution and removal is high. Therefore, 50 degrees C or less is preferable. It is preferable to dissolve and remove at −10 ° C. to 40 ° C., particularly preferably at 0 ° C. to 30 ° C. For the above reasons, it is preferable to select a method that generates less heat when dissolved and removed. For example, when a metal oxide or metal is used as the activator, the method of dissolving and removing with an acid generates heat of neutralization. Therefore, for example, select a method that hardly generates heat, such as a method of dissolving in water or an organic solvent, a method of forming a soluble complex using an aqueous ammonium nitrate salt solution or ethylenediaminetetraacetic acid, or a method of dissolving in a solution containing an ion exchange resin. You can also
より具体的に賦活剤と溶媒との組み合わせは、例えば、酸化バリウムと水、蓚酸カルシウムと塩酸、酸化アルミニウムと水酸化ナトリウム水溶液、酸化ハフニウムとメチルイソブチルケトン、炭酸マグネシウムとエチレンジアミン四酢酸4ナトリウム塩水溶液等が挙げられる。 More specifically, the combination of the activator and the solvent is, for example, barium oxide and water, calcium oxalate and hydrochloric acid, aluminum oxide and sodium hydroxide aqueous solution, hafnium oxide and methyl isobutyl ketone, magnesium carbonate and ethylenediaminetetraacetic acid tetrasodium salt aqueous solution Etc.
賦活剤を溶解除去した後、十分洗浄し、乾燥する。例えば、酸化バリウムを水で除去した場合、イオン交換水を用いて洗浄水の電気伝導度が、5μS/cm以下になるまで充分に洗浄する。次に減圧下、品温50℃以下で乾燥する。ここで残留する賦活剤や溶媒成分の量は、洗浄の条件にもよるが、通常100ppm以下である。 After dissolving and removing the activator, it is thoroughly washed and dried. For example, when barium oxide is removed with water, it is sufficiently washed with ion exchange water until the electric conductivity of the washing water becomes 5 μS / cm or less. Next, it is dried at a product temperature of 50 ° C. or lower under reduced pressure. The amount of the activator and solvent component remaining here is usually 100 ppm or less, although it depends on the washing conditions.
このようにして得られたニオブ粉、前記焼結塊、またはニオブ原料粉に、LC値を更に改善するために、ニオブ粉の一部を窒化、ホウ化、炭化、硫化、または複数のこれらの処理をしてもよい。 In order to further improve the LC value in the niobium powder thus obtained, the sintered ingot, or the niobium raw material powder, a part of the niobium powder is nitrided, borated, carbonized, sulfided, or a plurality of these Processing may be performed.
得られたニオブの窒化物、ニオブのホウ化物、ニオブの炭化物、ニオブの硫化物、またはこれらの複数種を本発明のニオブ粉中に含有してもよい。その窒素、ホウ素、炭素、及び硫黄の各元素の含有量の総和は、ニオブ粉の形状にもよって変わるが、0ppm〜200,000ppm、好ましくは50ppm〜100,000ppm、さらに好ましくは、200ppm〜20,000ppmである。200,000ppmを越えると容量特性が悪化し、コンデンサとして適さない。 The obtained niobium nitride, niobium boride, niobium carbide, niobium sulfide, or a plurality of these may be contained in the niobium powder of the present invention. The total content of each element of nitrogen, boron, carbon, and sulfur varies depending on the shape of the niobium powder, but is 0 ppm to 200,000 ppm, preferably 50 ppm to 100,000 ppm, and more preferably 200 ppm to 20 ppm. 1,000 ppm. If it exceeds 200,000 ppm, the capacity characteristics deteriorate and it is not suitable as a capacitor.
ニオブ粉の窒化方法は、液体窒化、イオン窒化、ガス窒化などのうち、何れかあるいは、それらの組み合わせた方法で実施することができる。窒素ガス雰囲気によるガス窒化は、装置が簡便で操作が容易なため好ましい。例えば、窒素ガス雰囲気によるガス窒化の方法は、前記ニオブ粉を窒素雰囲気中に放置することにより達成される。窒化する雰囲気の温度は、2000℃以下、放置時間は100時間以内で目的とする窒化量のニオブ粉が得られる。また、より高温で処理することにより処理時間を短縮できる。 The niobium powder nitriding method can be performed by any one of liquid nitriding, ion nitriding, gas nitriding, or a combination thereof. Gas nitriding in a nitrogen gas atmosphere is preferable because the apparatus is simple and easy to operate. For example, the gas nitriding method using a nitrogen gas atmosphere is achieved by leaving the niobium powder in a nitrogen atmosphere. The temperature of the nitriding atmosphere is 2000 ° C. or less and the standing time is 100 hours or less, so that a niobium powder having a desired nitriding amount can be obtained. Further, the processing time can be shortened by processing at a higher temperature.
ニオブ粉のホウ化方法は、ガスホウ化、固相ホウ化いずれであってもよい。例えば、ニオブ粉をホウ素ペレットやトリフルオロホウ素などのハロゲン化ホウ素のホウ素源とともに、減圧下、2000℃以下で1分〜100時間放置しておけばよい。 The method for boring niobium powder may be either gas boriding or solid phase boriding. For example, niobium powder may be allowed to stand at 2000 ° C. or less for 1 minute to 100 hours under reduced pressure together with a boron source of boron halide such as boron pellets or trifluoroboron.
ニオブ粉の炭化は、ガス炭化、固相炭化、液体炭化いずれであってもよい。例えば、ニオブ粉を炭素材やメタンなどの炭素を有する有機物などの炭素源とともに、減圧下、2000℃以下で1分〜100時間放置しておけばよい。 Niobium powder may be carbonized by gas carbonization, solid phase carbonization, or liquid carbonization. For example, niobium powder may be allowed to stand at 2000 ° C. or lower for 1 minute to 100 hours under reduced pressure together with a carbon source such as a carbon material or an organic substance having carbon such as methane.
ニオブ粉の硫化方法は、ガス硫化、イオン硫化、固相硫化いずれであってもよい。例えば、硫黄ガス雰囲気によるガス硫化の方法は、前記ニオブ粉を硫黄雰囲気中に放置することにより達成される。硫化する雰囲気の温度は、2000℃以下、放置時間は100時間以内で目的とする硫化量のニオブ粉が得られる。また、より高温で処理することにより処理時間を短縮できる。 Niobium powder may be sulfurized by any of gas sulfiding, ionic sulfiding, and solid phase sulfiding. For example, the method of gas sulfiding in a sulfur gas atmosphere is achieved by leaving the niobium powder in a sulfur atmosphere. The temperature of the sulfiding atmosphere is 2000 ° C. or less and the standing time is 100 hours or less, so that niobium powder having the desired amount of sulfiding can be obtained. Further, the processing time can be shortened by processing at a higher temperature.
以上の様にして得られる本発明のニオブ粉のBET比表面積は、通常、0.5〜40m2/g、好ましくは0.7〜10m2/g、さらに好ましくは0.9〜2m2/gである。 The BET specific surface area of the niobium powder of the present invention obtained as described above is usually 0.5 to 40 m 2 / g, preferably 0.7 to 10 m 2 / g, more preferably 0.9 to 2 m 2 / g. g.
本発明のニオブ粉は、タッピング密度、粒径、安息角、BET比表面積、細孔径分布、窒化、ホウ化、炭化、硫化による処理のそれぞれ異なるニオブ粉同士を混合して使用してもよい。 The niobium powder of the present invention may be used by mixing niobium powders each having different tapping density, particle size, angle of repose, BET specific surface area, pore size distribution, nitriding, boriding, carbonization, and sulfidation.
コンデンサ用電極に用いることのできる本発明の焼結体は、例えば、前述した本発明のニオブ粉を焼結して製造することが好ましい。例えば、ニオブ粉を所定の形状に加圧成形した後に10-5〜102Paで1分〜10時間、500℃〜2000℃、好ましくは800℃〜1500℃、さらに好ましくは1000℃〜1300℃の範囲で加熱して焼結体を得ることができる。 The sintered body of the present invention that can be used for the capacitor electrode is preferably produced, for example, by sintering the niobium powder of the present invention described above. For example, after press-molding niobium powder into a predetermined shape, 10 -5 to 10 2 Pa for 1 minute to 10 hours, 500 ° C to 2000 ° C, preferably 800 ° C to 1500 ° C, more preferably 1000 ° C to 1300 ° C. The sintered body can be obtained by heating in the range of.
本発明のニオブ粉より得られる焼結体の細孔径分布は、通常、細孔直径ピークトップを、0.01μm〜500μmの範囲内に持つ。 The pore size distribution of the sintered body obtained from the niobium powder of the present invention usually has a pore diameter peak top in the range of 0.01 μm to 500 μm.
また、成形時の加圧を特定の加圧値に調節することにより、ニオブ粉の持つ細孔直径ピークトップの数より多くの細孔直径ピークトップを焼結体に持たせることが出来る。この加圧値は、ニオブ粉の物性、成形体の形状、あるいは成形機等の加圧成形条件により異なるが、加圧成形が可能な圧力以上、焼結体の細孔が閉鎖しない程度の圧力以下の範囲内にある。好ましい加圧値は、予備実験により、複数の細孔径ピークトップを持つように、成形するニオブ粉の物性等に合わせて決定できる。なお、加圧値は、例えば、成形機の成形体へかける加重を調節することで調整できる。 Further, by adjusting the pressure during molding to a specific pressure value, the sintered body can have more pore diameter peak tops than the number of pore diameter peak tops of the niobium powder. This pressure value varies depending on the physical properties of the niobium powder, the shape of the molded body, or the pressure molding conditions of the molding machine, etc., but a pressure that does not close the pores of the sintered body beyond the pressure at which pressure molding is possible. Within the following range. A preferable pressurization value can be determined according to the physical properties of the niobium powder to be molded so as to have a plurality of pore diameter peak tops by a preliminary experiment. In addition, a pressurization value can be adjusted by adjusting the load applied to the molded object of a molding machine, for example.
焼結体の細孔径分布は、所望の容量が得られる程度に小さい細孔と、陰極剤の物性に合わせて陰極剤が十分含浸する程度に大きい細孔とが含まれるように、少なくとも2つの細孔径ピークトップを有することが好ましい。このように、細孔直径分布が複数のピークトップを持つような焼結体からは、対電極の含浸性が良好で、容量出現率が高いコンデンサが得られる。 The pore size distribution of the sintered body includes at least two pores so that the pores are small enough to obtain a desired capacity and the pores are large enough to be sufficiently impregnated with the cathode agent in accordance with the physical properties of the cathode agent. It is preferable to have a pore diameter peak top. Thus, a sintered body having a pore diameter distribution having a plurality of peak tops can provide a capacitor with good counter electrode impregnation and a high capacity appearance rate.
また、複数の細孔直径ピークトップの内、相対強度が最も大きい2つのピークのピークトップが、それぞれ各々0.2〜0.7μmと0.7〜3μmに、好ましくは各々0.2〜0.7μmと0.9〜3μmに存在する場合、この焼結体から作製したコンデンサの耐湿性は、好ましいものになる。さらに、複数の細孔直径ピークトップの内、相対強度が最も大きいピークのピークトップが、相対強度が次に大きいピークのピークトップより大径側にある場合、より耐湿性が良好なコンデンサとなるため、特に好ましい。 The peak tops of the two peaks having the highest relative intensity among the plurality of pore diameter peak tops are 0.2 to 0.7 μm and 0.7 to 3 μm, respectively, preferably 0.2 to 0 respectively. When the thickness is 0.7 μm and 0.9 to 3 μm, the moisture resistance of the capacitor produced from this sintered body is preferable. Furthermore, if the peak top of the peak with the highest relative intensity among the plurality of pore diameter peak tops is on the larger diameter side than the peak top of the peak with the next highest relative intensity, the capacitor has better moisture resistance. Therefore, it is particularly preferable.
このように作製した焼結体の比表面積は、一般に、0.2m2/g〜7m2/gになる。通常、焼結体の形状は大きいほど対電極の含浸が困難になる。例えば、焼結体の大きさが10mm3以上である場合、本発明の複数のピークトップを有する細孔直径分布を持つ焼結体を特に有効に用いることができる。 The specific surface area of the sintered body produced in this manner will generally 0.2m 2 / g~7m 2 / g. Usually, the larger the shape of the sintered body, the more difficult the impregnation of the counter electrode. For example, when the size of the sintered body is 10 mm 3 or more, the sintered body having a pore diameter distribution having a plurality of peak tops according to the present invention can be used particularly effectively.
本発明の焼結体は、一部窒化されていても良い。窒化方法として、前述したニオブ粉に適用した方法と反応条件が採用できる。焼結体を作製するニオブ粉の一部を窒化しておき、さらにこの粉体から作製した焼結体の一部を窒化することも可能である。 The sintered body of the present invention may be partially nitrided. As the nitriding method, the method and reaction conditions applied to the niobium powder described above can be adopted. It is also possible to nitride a part of the niobium powder for producing the sintered body and further nitride a part of the sintered body produced from this powder.
尚、このような焼結体には酸素が、通常、500〜70000質量ppm含まれる。これは、焼結前からニオブ粉に含まれている自然酸化酸素と、焼結後に自然酸化したことによって加わった酸素があるためである。また、本発明の焼結体中のニオブ、合金形成元素、酸素、窒素以外の元素の含有量は、通常、400質量ppm以下である。 Such a sintered body usually contains 500 to 70000 mass ppm of oxygen. This is because there is natural oxidized oxygen contained in the niobium powder before sintering and oxygen added by natural oxidation after sintering. The content of elements other than niobium, alloy forming elements, oxygen, and nitrogen in the sintered body of the present invention is usually 400 mass ppm or less.
本発明の焼結体は、一例として、1300℃で焼結した場合、CV値(0.1質量%燐酸水溶液中で、80℃120分化成した場合の化成電圧値と120Hzでの容量との積)が、40000〜200000μFV/gとなる。 As an example, when the sintered body of the present invention is sintered at 1300 ° C., the CV value (the conversion voltage value in the case of 120 ° C. differentiation at 80 ° C. in a 0.1 mass% phosphoric acid aqueous solution and the capacity at 120 Hz) Product) is 40000-200000 μFV / g.
次に、コンデンサ素子の製造について説明する。例えば、ニオブ又はタンタルなどの弁作用金属からなる、適当な形状及び長さを有するリードワイヤーを用意し、これを前述したニオブ粉の加圧成形時にリードワイヤーの一部が成形体の内部に挿入させるように一体成形して、リードワイヤーを前記焼結体の引き出しリードとなるように組み立て設計するか、あるいは、リードワイヤーなしで成形、焼結した後に別途用意したリードワイヤーを溶接などで接続するように設計する。 Next, manufacturing of the capacitor element will be described. For example, a lead wire made of a valve metal such as niobium or tantalum and having an appropriate shape and length is prepared, and a part of the lead wire is inserted into the molded body when the niobium powder is pressure-molded as described above. The lead wire is assembled and designed so that it becomes the lead for drawing out the sintered body, or the lead wire prepared separately is formed and sintered without the lead wire and connected by welding or the like Design as follows.
前述した焼結体を一方の電極とし、対電極との間に介在した誘電体とからコンデンサを製造することができる。例えば、ニオブ焼結体を一方の電極とし、その焼結体表面(細孔内表面含む)上に誘電体を形成し、前記誘電体上に対電極を設け、コンデンサを構成する。 A capacitor can be manufactured from the above-mentioned sintered body as one electrode and a dielectric interposed between the counter electrode. For example, a niobium sintered body is used as one electrode, a dielectric is formed on the surface of the sintered body (including the surface in the pores), and a counter electrode is provided on the dielectric to constitute a capacitor.
ここでコンデンサの誘電体として、酸化ニオブを主体とする誘電体が好ましく、さらに好ましくは五酸化ニオブを主体とする誘電体が挙げられる。五酸化ニオブを主体とする誘電体は、例えば、一方の電極であるニオブ焼結体を電解酸化することによって得られる。ニオブ電極を電解液中で電解酸化するには、通常プロトン酸水溶液、例えば、0.1%リン酸水溶液、硫酸水溶液又は1%の酢酸水溶液、アジピン酸水溶液等を用いて行われる。このように、ニオブ電極を電解液中で化成して酸化ニオブ誘電体を得る場合、本発明のコンデンサは、電解コンデンサとなりニオブ電極が陽極となる。 Here, the dielectric of the capacitor is preferably a dielectric mainly composed of niobium oxide, more preferably a dielectric mainly composed of niobium pentoxide. A dielectric body mainly composed of niobium pentoxide can be obtained, for example, by electrolytic oxidation of a niobium sintered body that is one of the electrodes. Electrolytic oxidation of the niobium electrode in the electrolytic solution is usually performed using a protonic acid aqueous solution, for example, a 0.1% phosphoric acid aqueous solution, a sulfuric acid aqueous solution, a 1% acetic acid aqueous solution, an adipic acid aqueous solution, or the like. Thus, when a niobium electrode is formed in an electrolytic solution to obtain a niobium oxide dielectric, the capacitor of the present invention becomes an electrolytic capacitor and the niobium electrode becomes an anode.
本発明のコンデンサにおいて、ニオブ焼結体の対電極(対極)は格別限定されるものではなく、例えば、アルミ電解コンデンサ業界で公知である電解液、有機半導体及び無機半導体から選ばれた少なくとも1種の材料(化合物)が使用できる。 In the capacitor of the present invention, the counter electrode (counter electrode) of the niobium sintered body is not particularly limited. For example, at least one selected from an electrolyte, an organic semiconductor, and an inorganic semiconductor known in the aluminum electrolytic capacitor industry. These materials (compounds) can be used.
電解液の具体例としては、イソブチルトリプロピルアンモニウムボロテトラフルオライド電解質を5質量%溶解したジメチルホルムアミドとエチレングリコールの混合溶液、テトラエチルアンモニウムボロテトラフルオライドを7質量%溶解したプロピレンカーボネートとエチレングリコールの混合溶液などが挙げられる。 Specific examples of the electrolyte include a mixed solution of dimethylformamide and ethylene glycol in which 5% by mass of isobutyltripropylammonium borotetrafluoride electrolyte is dissolved, propylene carbonate and ethylene glycol in which 7% by mass of tetraethylammonium borotetrafluoride is dissolved. Examples thereof include mixed solutions.
有機半導体の具体例としては、ベンゾピロリン4量体とクロラニルからなる有機半導体、テトラチオテトラセンを主成分とする有機半導体、テトラシアノキノジメタンを主成分とする有機半導体、あるいは下記一般式(1)又は一般式(2)で表される繰り返し単位を含む導電性高分子が挙げられる。 Specific examples of the organic semiconductor include an organic semiconductor composed of benzopyrroline tetramer and chloranil, an organic semiconductor composed mainly of tetrathiotetracene, an organic semiconductor composed mainly of tetracyanoquinodimethane, or the following general formula (1 ) Or a conductive polymer containing a repeating unit represented by the general formula (2).
式中、R1〜R4はそれぞれ独立して水素原子、炭素数1乃至10の直鎖上もしくは分岐状の飽和もしくは不飽和のアルキル基、アルコキシ基あるいはアルキルエステル基、またはハロゲン原子、ニトロ基、シアノ基、1級、2級もしくは3級アミノ基、CF3基、フェニル基及び置換フェニル基からなる群から選ばれる一価基を表わす。R1とR2及びR3とR4の炭化水素鎖は互いに任意の位置で結合して、かかる基により置換を受けている炭素原子と共に少なくとも1つ以上の3〜7員環の飽和または不飽和炭化水素の環状構造を形成する二価鎖を形成してもよい。前記環状結合鎖には、カルボニル、エーテル、エステル、アミド、スルフィド、スルフィニル、スルホニル、イミノの結合を任意の位置に含んでもよい。Xは酸素、硫黄又は窒素原子を表し、R5はXが窒素原子の時のみ存在して、独立して水素又は炭素数1乃至10の直鎖上もしくは分岐状の飽和もしくは不飽和のアルキル基を表す。 In the formula, each of R 1 to R 4 independently represents a hydrogen atom, a linear or branched alkyl group having 1 to 10 carbon atoms, a branched or saturated alkyl group, an alkoxy group or an alkyl ester group, a halogen atom, or a nitro group. , A monovalent group selected from the group consisting of a cyano group, a primary, secondary or tertiary amino group, a CF 3 group, a phenyl group and a substituted phenyl group. The hydrocarbon chains of R 1 and R 2 and R 3 and R 4 are bonded to each other at any position, and at least one or more 3- to 7-membered saturated or unsaturated groups with carbon atoms substituted by such groups. You may form the bivalent chain | strand which forms the cyclic structure of a saturated hydrocarbon. The cyclic bond chain may contain a bond of carbonyl, ether, ester, amide, sulfide, sulfinyl, sulfonyl, or imino at any position. X represents an oxygen, sulfur or nitrogen atom, R 5 is present only when X is a nitrogen atom, and is independently hydrogen or a linear or branched saturated or unsaturated alkyl group having 1 to 10 carbon atoms. Represents.
さらに、本発明においては前記一般式(1)又は一般式(2)のR1〜R4は、好ましくは、それぞれ独立して水素原子、炭素数1乃至6の直鎖上もしくは分岐状の飽和もしくは不飽和のアルキル基又はアルコキシ基を表し、R1とR2及びR3とR4は互いに結合して環状になっていてもよい。 Furthermore, in the present invention, R 1 to R 4 in the general formula (1) or general formula (2) are preferably each independently a hydrogen atom, a linear or branched saturated group having 1 to 6 carbon atoms. Alternatively, it represents an unsaturated alkyl group or alkoxy group, and R 1 and R 2 and R 3 and R 4 may be bonded to each other to form a ring.
さらに、本発明においては、前記一般式(1)で表される繰り返し単位を含む導電性高分子は、好ましくは下記一般式(3)で示される構造単位を繰り返し単位として含む導電性高分子が挙げられる。 Furthermore, in the present invention, the conductive polymer containing a repeating unit represented by the general formula (1) is preferably a conductive polymer containing a structural unit represented by the following general formula (3) as a repeating unit. Can be mentioned.
式中、R6及びR7は、各々独立して水素原子、炭素数1乃至6の直鎖状もしくは分岐状の飽和もしくは不飽和のアルキル基、または該アルキル基が互いに任意の位置で結合して、2つの酸素元素を含む少なくとも1つ以上の5〜7員環の飽和炭化水素の環状構造を形成する置換基を表わす。また、前記環状構造には置換されていてもよいビニレン結合を有するもの、置換されていてもよいフェニレン構造のものが含まれる。 In the formula, R 6 and R 7 are each independently a hydrogen atom, a linear or branched saturated or unsaturated alkyl group having 1 to 6 carbon atoms, or the alkyl group is bonded to each other at an arbitrary position. And a substituent that forms a cyclic structure of at least one 5- to 7-membered saturated hydrocarbon containing two oxygen elements. The cyclic structure includes those having a vinylene bond which may be substituted and those having a phenylene structure which may be substituted.
このような化学構造を含む導電性高分子には、ドーパントがドープされる。ドーパントには公知のドーパントが制限なく使用できる。 A conductive polymer having such a chemical structure is doped with a dopant. A well-known dopant can be used for a dopant without a restriction | limiting.
無機半導体の具体例としては、二酸化鉛又は二酸化マンガンを主成分とする無機半導体、四三酸化鉄からなる無機半導体などが挙げられる。このような半導体は単独でも、又は二種以上組み合わせて使用してもよい。 Specific examples of the inorganic semiconductor include an inorganic semiconductor mainly composed of lead dioxide or manganese dioxide, and an inorganic semiconductor composed of iron trioxide. Such semiconductors may be used alone or in combination of two or more.
一般式(1)又は一般式(2)で表される繰り返し単位を含む重合体としては、例えば、ポリアニリン、ポリオキシフェニレン、ポリフェニレンサルファイド、ポリチオフェン、ポリフラン、ポリピロール、ポリメチルピロール、及びこれらの置換誘導体や共重合体などが挙げられる。中でもポリピロール、ポリチオフェン及びこれらの置換誘導体(例えばポリ(3,4−エチレンジオキシチオフェン)等)が好ましい。 Examples of the polymer containing the repeating unit represented by the general formula (1) or (2) include polyaniline, polyoxyphenylene, polyphenylene sulfide, polythiophene, polyfuran, polypyrrole, polymethylpyrrole, and substituted derivatives thereof. And copolymers. Of these, polypyrrole, polythiophene, and substituted derivatives thereof (for example, poly (3,4-ethylenedioxythiophene)) are preferable.
上記有機半導体及び無機半導体として、電導度10-2S/cm〜103S/cmの範囲のものを使用すると、作製したコンデンサのインピーダンス値がより小さくなり高周波での容量を更に一層大きくすることができる。 When the organic semiconductor and the inorganic semiconductor having a conductivity in the range of 10 −2 S / cm to 10 3 S / cm are used, the impedance value of the manufactured capacitor is further reduced, and the capacitance at high frequency is further increased. Can do.
前記導電性高分子層を製造する方法としては、例えばアニリン、チオフェン、フラン、ピロール、メチルピロール又はこれらの置換誘導体の重合性化合物を、脱水素的2電子酸化の酸化反応を充分行わせ得る酸化剤の作用で重合する方法が採用される。重合性化合物(モノマー)からの重合反応は、例えばモノマーの気相重合、溶液重合等があり、誘電体を有するニオブ焼結体の表面に形成される。導電性高分子が溶液塗布可能な有機溶媒可溶性のポリマーの場合には、表面に塗布して形成する方法が採用される。 As the method for producing the conductive polymer layer, for example, aniline, thiophene, furan, pyrrole, methylpyrrole or a polymerizable compound of these substituted derivatives may be oxidized enough to cause an oxidation reaction of dehydrogenative two-electron oxidation. A method of polymerizing by the action of the agent is employed. The polymerization reaction from the polymerizable compound (monomer) includes, for example, vapor phase polymerization of a monomer, solution polymerization, and the like, and is formed on the surface of a niobium sintered body having a dielectric. In the case where the conductive polymer is an organic solvent-soluble polymer that can be applied by solution, a method in which the conductive polymer is formed by applying to the surface is employed.
溶液重合による好ましい製造方法の1つとして、誘電体層を形成したニオブ焼結体を、酸化剤を含む溶液(溶液1)に浸漬し、次いでモノマー及びドーパントを含む溶液(溶液2)に浸漬して重合し、該表面に導電性高分子層を形成得する方法が例示される。また、前記焼結体を、溶液2に浸漬した後で溶液1に浸漬してもよい。また、前記溶液2においては、ドーパントを含まないモノマー溶液として前記方法に使用してもい。また、ドーパントを使用する場合、酸化剤を含む溶液に共存させて使用してもよい。 As one of preferred production methods by solution polymerization, a niobium sintered body having a dielectric layer formed is immersed in a solution containing an oxidizing agent (solution 1), and then immersed in a solution containing a monomer and a dopant (solution 2). And a method of polymerizing and forming a conductive polymer layer on the surface. Further, the sintered body may be immersed in the solution 1 after being immersed in the solution 2. Moreover, in the said solution 2, you may use for the said method as a monomer solution which does not contain a dopant. Moreover, when using a dopant, you may use it making it coexist in the solution containing an oxidizing agent.
このような重合工程操作を、誘電体を有する前記ニオブ焼結体に対して1回以上、好ましくは3〜20回繰り返すことによって緻密で層状の導電性高分子層を容易に形成することができる。 A dense and layered conductive polymer layer can be easily formed by repeating such a polymerization process operation once or more, preferably 3 to 20 times, with respect to the niobium sintered body having a dielectric. .
本発明のコンデンサの製造方法においては、酸化剤はコンデンサ性能に悪影響を及ぼすことなく、その酸化剤の還元体がドーパントになって導電性高分子の電動度を向上させ得る酸化剤であれば良く、工業的に安価で製造上取り扱いの容易な化合物が好まれる。 In the method for manufacturing a capacitor of the present invention, the oxidant may be any oxidant that does not adversely affect the performance of the capacitor and can be used to improve the electric power of the conductive polymer by using the reduced form of the oxidant as a dopant. Industrially inexpensive compounds that are easy to handle in production are preferred.
このような酸化剤としては、具体的には、例えばFeCl3やFeClO4、Fe(有機酸アニオン)塩等のFe(III)系化合物類、または無水塩化アルミニウム/塩化第一銅、アルカリ金属過硫酸塩類、過硫酸アンモニウム塩類、過酸化物類、過マンガン酸カリウム等のマンガン類、2,3−ジクロロ−5,6−ジシアノ−1,4−ベンゾキノン(DDQ)、テトラクロロ−1,4−ベンゾキノン、テトラシアノ−1,4−ベンゾキノン等のキノン類、よう素、臭素等のハロゲン類、過酸、硫酸、発煙硫酸、三酸化硫黄、クロロ硫酸、フルオロ硫酸、アミド硫酸等のスルホン酸、オゾン等及びこれら複数の酸化剤の組み合わせが挙げられる。 Specific examples of such an oxidizing agent include FeCl (III) compounds such as FeCl 3 , FeClO 4 , Fe (organic acid anion) salt, anhydrous aluminum chloride / cuprous chloride, alkali metal peroxide. Sulfates, ammonium persulfates, peroxides, manganese such as potassium permanganate, 2,3-dichloro-5,6-dicyano-1,4-benzoquinone (DDQ), tetrachloro-1,4-benzoquinone Quinones such as tetracyano-1,4-benzoquinone, halogens such as iodine and bromine, sulfonic acids such as peracid, sulfuric acid, fuming sulfuric acid, sulfur trioxide, chlorosulfuric acid, fluorosulfuric acid and amidosulfuric acid, ozone and the like A combination of these plural oxidizing agents can be mentioned.
これらの中で、前記Fe(有機酸アニオン)塩を形成する有機酸アニオンの基本化合物としては、有機スルホン酸または有機カルボン酸、有機リン酸、有機ホウ酸等が挙げられる。有機スルホン酸の具体例としては、ベンゼンスルホン酸やp−トルエンスルホン酸、メタンスルホン酸、エタンスルホン酸、α−スルホ−ナフタレン、β−スルホ−ナフタレン、ナフタレンジスルホン酸、アルキルナフタレンスルホン酸(アルキル基としてはブチル、トリイソプロピル、ジ−t−ブチル等)等が使用される。 Among these, examples of the basic compound of the organic acid anion that forms the Fe (organic acid anion) salt include organic sulfonic acid or organic carboxylic acid, organic phosphoric acid, and organic boric acid. Specific examples of the organic sulfonic acid include benzenesulfonic acid, p-toluenesulfonic acid, methanesulfonic acid, ethanesulfonic acid, α-sulfo-naphthalene, β-sulfo-naphthalene, naphthalene disulfonic acid, alkylnaphthalenesulfonic acid (alkyl group). As butyl, triisopropyl, di-t-butyl, etc.).
一方、有機カルボン酸の具体例としては、酢酸、プロピオン酸、安息香酸、シュウ酸等が挙げられる。さらに本発明においては、ポリアクリル酸、ポリメタクリル酸、ポリスチレンスルホン酸、ポリビニルスルホン酸、ポリビニル硫酸ポリ−α−メチルスルホン酸、ポリエチレンスルホン酸、ポリリン酸等の高分子電解質アニオンも使用される。なお、これら有機スルホン酸または有機カルボン酸の例は単なる例示であり、これらに限定されるものではないない。また、前記アニオンの対カチオンは、H+、Na+、K+等のアルカリ金属イオン、または水素原子やテトラメチル基、テトラエチル基、テトラブチル基、テトラフェニル基等で置換されたアンモニウムイオン等が例示されるが、これらに限定されるものではない。前記の酸化剤のうち、特に好ましいのは、3価のFe系化合物類、または塩化第一銅系、過硫酸アルカリ塩類、過硫酸アンモニウム塩類酸類、キノン類を含む酸化剤である。 On the other hand, specific examples of the organic carboxylic acid include acetic acid, propionic acid, benzoic acid, oxalic acid and the like. Furthermore, in the present invention, polyelectrolyte anions such as polyacrylic acid, polymethacrylic acid, polystyrene sulfonic acid, polyvinyl sulfonic acid, polyvinyl sulfate poly-α-methyl sulfonic acid, polyethylene sulfonic acid, and polyphosphoric acid are also used. In addition, the example of these organic sulfonic acid or organic carboxylic acid is a mere illustration, and is not limited to these. Examples of the counter cation of the anion include alkali metal ions such as H + , Na + and K + , or ammonium ions substituted with a hydrogen atom, a tetramethyl group, a tetraethyl group, a tetrabutyl group, a tetraphenyl group, or the like. However, it is not limited to these. Of the above oxidizing agents, particularly preferred are oxidizing agents containing trivalent Fe compounds, or cuprous chloride, alkali persulfates, ammonium persulfates, and quinones.
導電性高分子の重合体組成物の製造方法において必要に応じて共存させるドーパント能を有するアニオン(酸化剤の還元体アニオン以外のアニオン)は、前述の酸化剤から産生される酸化剤アニオン(酸化剤の還元体)を対イオンに持つ電解質アニオンまたは他の電解質アニオンを使用することができる。具体的には例えば、PF6 -、SbF6 -、AsF6 -の如き5B族元素のハロゲン化物アニオン、BF4 -の如き3B族元素のハロゲン化物アニオン、I-(I3 -)、Br-、Cl-の如きハロゲンアニオン、ClO4 -の如き過ハロゲン酸アニオン、AlCl4 -、FeCl4 -、SnCl5 -等の如きルイス酸アニオン、あるいはNO3 -、SO4 2-の如き無機酸アニオン、またはp−トルエンスルホン酸やナフタレンスルホン酸、炭素数1乃至5(C1〜5と略する)のアルキル置換ナフタレンスルホン酸等のスルホン酸アニオン、CF3SO3 -,CH3SO3 -の如き有機スルホン酸アニオン、またはCH3COO-、C6H5COO-のごときカルボン酸アニオン等のプロトン酸アニオンを挙げることができる。 An anion (anion other than the reductant anion of the oxidant) having a dopant ability to coexist as necessary in the method for producing a polymer composition of a conductive polymer is an oxidant anion (oxidation) produced from the oxidant described above. It is possible to use an electrolyte anion having a reductant of the agent) as a counter ion or another electrolyte anion. Specifically, for example, a halide anion of a group 5B element such as PF 6 − , SbF 6 − , AsF 6 − , a halide anion of a group 3B element such as BF 4 − , I − (I 3 − ), Br − , Halogen anions such as Cl − , perhalogenate anions such as ClO 4 − , Lewis acid anions such as AlCl 4 − , FeCl 4 − and SnCl 5 − , or inorganic acid anions such as NO 3 − and SO 4 2− Or sulfonate anions such as p-toluenesulfonic acid, naphthalenesulfonic acid, alkyl-substituted naphthalenesulfonic acid having 1 to 5 carbon atoms (abbreviated as C1-5), CF 3 SO 3 − , CH 3 SO 3 − Mention may be made of organic acid sulfonate anions or protonic acid anions such as carboxylic acid anions such as CH 3 COO − and C 6 H 5 COO − .
また、同じく、ポリアクリル酸、ポリメタクリル酸、ポリスチレンスルホン酸、ポリビニルスルホン酸、ポリビニル硫酸、ポリ−α−メチルスルホン酸、ポリエチレンスルホン酸、ポリリン酸等の高分子電解質のアニオン等を挙げることができるが、これらに限定されるものではない。しかしながら、好ましくは、高分子系及び低分子系の有機スルホン酸化合物あるいはポリリン酸化合物のアニオンが挙げられ、望ましくは芳香族系のスルホン酸化合物(ドデシルベンゼンスルホン酸ナトリウム、ナフタレンスルホン酸ナトリウム等)がアニオン供出化合物として用いられる。 Similarly, anions of polymer electrolytes such as polyacrylic acid, polymethacrylic acid, polystyrene sulfonic acid, polyvinyl sulfonic acid, polyvinyl sulfuric acid, poly-α-methyl sulfonic acid, polyethylene sulfonic acid, and polyphosphoric acid can be exemplified. However, it is not limited to these. However, preferably, anions of high molecular weight and low molecular weight organic sulfonic acid compounds or polyphosphoric acid compounds are used, and desirably aromatic sulfonic acid compounds (sodium dodecylbenzene sulfonate, sodium naphthalene sulfonate, etc.) are used. Used as an anion-providing compound.
また、有機スルホン酸アニオンのうち、さらに有効なドーパントとしては、分子内に一つ以上のスルホアニオン基(−SO3 -)とキノン構造を有するスルホキノン化合物や、アントラセンスルホン酸アニオンが挙げられる。 Among organic sulfonate anions, more effective dopants include sulfoquinone compounds having one or more sulfoanion groups (—SO 3 − ) and a quinone structure in the molecule, and anthracene sulfonate anions.
前記スルホキノン化合物のスルホキノンアニオンの基本骨格として、p−ベンゾキノン、o−ベンゾキノン、1,2−ナフトキノン、1,4−ナフトキノン、2,6−ナフトキノン、9,10−アントラキノン、1,4−アントラキノン、1,2−アントラキノン、1,4−クリセンキノン、5,6−クリセンキノン、6,12−クリセンキノン、アセナフトキノン、アセナフテンキノン、カンホルキノン、2,3−ボルナンジオン、9,10−フェナントレンキノン、2,7−ピレンキノンが挙げられる。 As the basic skeleton of the sulfoquinone anion of the sulfoquinone compound, p-benzoquinone, o-benzoquinone, 1,2-naphthoquinone, 1,4-naphthoquinone, 2,6-naphthoquinone, 9,10-anthraquinone, 1,4-anthraquinone, 1,2-anthraquinone, 1,4-chrysenequinone, 5,6-chrysenequinone, 6,12-chrysenequinone, acenaphthoquinone, acenaphthenequinone, camphorquinone, 2,3-bornanedione, 9,10-phenanthrenequinone, 2,7- Examples include pyrenequinone.
対電極(対極)が固体の場合には、所望により用いられる外部引き出しリード(例えば、リードフレームなど)との電気的接触をよくするため、その上に導電体層を設けてもよい。 When the counter electrode (counter electrode) is solid, a conductor layer may be provided thereon in order to improve electrical contact with an external lead (for example, a lead frame) used as desired.
導電体層としては、例えば、導電ペーストの固化、メッキ、金属蒸着、耐熱性の導電樹脂フィルムなどにより形成することができる。導電ペーストとしては、銀ペースト、銅ペースト、アルミペースト、カーボンペースト、ニッケルペーストなどが好ましいが、これらは、1種を用いても2種以上を用いてもよい。2種以上を用いる場合、混合してもよく、又は別々の層として重ねてもよい。導電ペースト適用した後、空気中に放置するか、又は加熱して固化せしめる。メッキとしては、ニッケルメッキ、銅メッキ、銀メッキ、アルミメッキなどがあげられる。また、蒸着金属としては、アルミニウム、ニッケル、銅、銀などがあげられる。 The conductor layer can be formed by, for example, solidifying a conductive paste, plating, metal deposition, a heat-resistant conductive resin film, or the like. As the conductive paste, a silver paste, a copper paste, an aluminum paste, a carbon paste, a nickel paste, and the like are preferable, but these may be used alone or in combination of two or more. When using 2 or more types, they may be mixed or overlapped as separate layers. After applying the conductive paste, it is left in the air or heated to solidify. Examples of plating include nickel plating, copper plating, silver plating, and aluminum plating. Further, examples of the deposited metal include aluminum, nickel, copper, and silver.
具体的には、例えば第二の電極上にカーボンペースト、銀ペーストを順次積層し、エポキシ樹脂のような材料で封止してコンデンサが構成される。このコンデンサは、ニオブ焼結体と一体に焼結成形された、または、後で溶接されたニオブ又は、タンタルリードを有していてもよい。 Specifically, for example, a carbon paste and a silver paste are sequentially laminated on the second electrode and sealed with a material such as an epoxy resin to constitute a capacitor. The capacitor may have a niobium or tantalum lead that is sintered integrally with the niobium sintered body or is later welded.
以上のような構成の本発明のコンデンサは、例えば、樹脂モールド、樹脂ケース、金属性の外装ケース、樹脂のディッピング、ラミネートフィルムによる外装により各種用途のコンデンサ製品とすることができる。 The capacitor of the present invention having the above-described configuration can be made into a capacitor product for various uses by, for example, a resin mold, a resin case, a metallic outer case, resin dipping, and a laminate film.
また、対電極が液体の場合には、前記両極と誘電体から構成されたコンデンサを、例えば、対電極と電気的に接続した缶に収納してコンデンサが形成される。この場合、ニオブ焼結体の電極側は、前記したニオブ又はタンタルリードを介して外部に導出すると同時に、絶縁性ゴムなどにより、缶との絶縁がはかられるように設計される。 Further, when the counter electrode is liquid, the capacitor composed of the two electrodes and the dielectric is housed in, for example, a can electrically connected to the counter electrode to form a capacitor. In this case, the electrode side of the niobium sintered body is designed so as to be insulated from the can by insulating rubber or the like while being led out through the niobium or tantalum lead described above.
以上、説明した本発明の実施態様にしたがって製造したニオブ粉を用いてコンデンサ用焼結体を作製し、該焼結体からコンデンサを製造することにより、漏れ電流値の小さい信頼性の良好なコンデンサを得ることができる。 As described above, by manufacturing a sintered body for a capacitor using the niobium powder manufactured according to the embodiment of the present invention described above, and manufacturing a capacitor from the sintered body, a capacitor having a small leakage current value and a good reliability. Can be obtained.
また、本発明のコンデンサは、従来のタンタルコンデンサよりも容積の割に静電容量が大きく、より小型のコンデンサ製品を得ることができる。 In addition, the capacitor of the present invention has a larger capacitance than the conventional tantalum capacitor, and a smaller capacitor product can be obtained.
このような特性を持つ本発明のコンデンサは、例えば、アナログ回路及びデジタル回路中で多用されるバイパスコンデンサ、カップリングコンデンサとしての用途や、従来のタンタルコンデンサの用途にも適用できる。 The capacitor of the present invention having such characteristics can be applied to, for example, a use as a bypass capacitor and a coupling capacitor frequently used in an analog circuit and a digital circuit, and a use of a conventional tantalum capacitor.
一般に、このようなコンデンサは電子回路中で多用されるので、本発明のコンデンサを用いれば、電子部品の配置や排熱の制約が緩和され、信頼性の高い電子回路を従来より狭い空間に収めることができる。 In general, such a capacitor is frequently used in an electronic circuit. Therefore, if the capacitor of the present invention is used, restrictions on the arrangement of electronic components and exhaust heat are alleviated, and a highly reliable electronic circuit is accommodated in a narrower space than before. be able to.
さらに、本発明のコンデンサを用いれば、従来より小型で信頼性の高い電子機器、例えば、コンピュータ、PCカード等のコンピュータ周辺機器、携帯電話などのモバイル機器、家電製品、車載機器、人工衛星、通信機器等を得ることができる。 Furthermore, if the capacitor of the present invention is used, electronic devices that are smaller and more reliable than conventional devices, for example, computer peripheral devices such as computers and PC cards, mobile devices such as mobile phones, home appliances, in-vehicle devices, artificial satellites, communication Equipment etc. can be obtained.
以下、実施例及び比較例を挙げて本発明を具体的に説明するが、本発明はこれらの例に限定されるものではない。 EXAMPLES Hereinafter, although an Example and a comparative example are given and this invention is demonstrated concretely, this invention is not limited to these examples.
なお、各例におけるニオブ粉のタッピング密度、安息角、粒子径及び細孔直径、並びにコンデンサの容量、漏れ電流値、容量出現率、耐湿値及びESR値は以下の方法により測定した。 In each example, the tapping density, repose angle, particle diameter and pore diameter of the niobium powder, capacitor capacity, leakage current value, capacity appearance rate, moisture resistance value and ESR value were measured by the following methods.
(1)タッピング密度測定タッピング密度は、JIS(日本工業規格2000年版)K1201−1に規定される工業用炭酸ナトリウムの見掛比重測定法のうちタッピング装置による方法、及び測定機器に準じて測定した。 (1) Tapping density measurement The tapping density was measured according to the method using a tapping device and the measuring instrument among the apparent specific gravity measuring methods for industrial sodium carbonate specified in JIS (Japanese Industrial Standard 2000) K1201-1. .
(2)安息角測定安息角は、JIS(日本工業規格2000年版)Z2504に規定される流れ性の測定機器と試料量を用い、水平面に対するホッパー下部の高さ6cmから、水平面にニオブ粉を落下させ、生じた円錐の頂点から水平面に対する斜面の水平面に対する角度を安息角とした。 (2) Angle of repose measurement The angle of repose uses niobium powder falling on the horizontal plane from the height of 6cm below the hopper with respect to the horizontal plane using the flowability measuring instrument and sample amount specified in JIS (Japanese Industrial Standard 2000) Z2504. The angle of repose of the slope with respect to the horizontal plane from the top of the generated cone was defined as the angle of repose.
(3)粒子径測定マイクロトラック社製(HRA 9320−X100)の装置を用い粒度分布をレーザー回折散乱法で測定した。その累積体積%が、50体積%に相当する粒径値(D50;μm)を平均粒子径とした。 (3) Particle size measurement The particle size distribution was measured by a laser diffraction scattering method using an apparatus manufactured by Microtrack (HRA 9320-X100). The average particle diameter was defined as a particle size value (D 50 ; μm) corresponding to the cumulative volume% of 50 volume%.
(4)細孔直径測定Micro Meritics社製 Poresier 9320を用い細孔分布を水銀圧入法で測定した。なお、本発明では、圧入量の変化率から極大値を求め、極大値が示す細孔直径をピークトップとし、極大値をこのピークトップの属するピークの相対強度の大きさとした。 (4) Pore diameter measurement The pore distribution was measured by a mercury intrusion method using a Poresia 9320 manufactured by Micro Merits. In the present invention, the maximum value is obtained from the rate of change of the press-fit amount, the pore diameter indicated by the maximum value is set as the peak top, and the maximum value is set as the relative intensity of the peak to which the peak top belongs.
(5)コンデンサの容量測定室温において、作製したチップの端子間にヒューレットパッカード社製LCR測定器を接続し、120Hzでの容量測定値をチップ加工したコンデンサの容量とした。 (5) Capacitor capacity measurement At room temperature, an LCR measuring instrument manufactured by Hewlett-Packard Co. was connected between the terminals of the manufactured chip, and the measured capacitance value at 120 Hz was taken as the capacity of the chip-processed capacitor.
(6)コンデンサの漏れ電流測定室温において、作製したチップの端子間に直流電圧6.3Vを1分間印加し続けた後に測定された電流値をチップに加工したコンデンサの漏れ電流値とした。 (6) Measurement of Leakage Current of Capacitor The current value measured after continuously applying a DC voltage of 6.3 V for 1 minute between the terminals of the manufactured chip at room temperature was taken as the leakage current value of the capacitor processed into the chip.
(7)コンデンサの容量出現率0.1%燐酸水溶液中で、80℃,20Vの条件で1000分間化成したときの焼結体を、30%硫酸中で測定した容量を100%として、コンデンサ形成後の容量との比で表現した。 (7) Capacitor appearance rate Capacitor formation with a sintered body formed in a 0.1% phosphoric acid aqueous solution at 80 ° C. and 20 V for 1000 minutes, with the capacity measured in 30% sulfuric acid as 100% It was expressed as a ratio to the later capacity.
(8)コンデンサの耐湿値作製したコンデンサを、60℃95%RHで500時間放置したときの容量が、初期値の110%未満および120%未満の個数で表現した。110%未満の個数が多いほど、耐湿値は良好と判断した。 (8) Moisture resistance value of the capacitor The capacity when the produced capacitor was allowed to stand at 60 ° C. and 95% RH for 500 hours was expressed as the number of less than 110% and less than 120% of the initial value. It was judged that the moisture resistance value was better as the number was less than 110%.
(9)コンデンサのESR測定室温において、作製したチップの端子間にヒューレットパッカード社製LCR測定器を接続し、100kHz、1.5VDC、0.5Vrms.でのESR測定値をチップ加工したコンデンサのESRとした。 (9) ESR measurement of capacitor At room temperature, an LCR measuring instrument manufactured by Hewlett-Packard Co. was connected between terminals of the manufactured chip, and 100 kHz, 1.5 VDC, 0.5 Vrms. The ESR measured value was taken as the ESR of the chip processed capacitor.
実施例1:ニッケル製坩堝中、80℃で充分に真空乾燥したフッ化ニオブ酸カリウム5000gに、フッ化ニオブ酸カリウムの10倍モル量のナトリウムを投入し、アルゴン雰囲気下1000℃で20時間還元反応を行った。反応後冷却させ、還元物を水洗した後に、95%硫酸、水で順次洗浄した後に真空乾燥した。さらにシリカアルミナボール入りのアルミナポットのボールミルを用いて40時間粉砕した後、粉砕物を50%硝酸と10%過酸化水素水の3:2(質量比)混合液中に浸漬撹拌した。その後、pHが7になるまで充分水洗して不純物を除去し、真空乾燥した。原料ニオブ粉の平均粒子径は1.2μmであった。
この原料ニオブ粉500gをニオブ製のポットに入れ、平均粒子径が1μmのポリメチルメタクリル酸ブチルエステル50g、およびトルエン1リットルを添加した。更にジルコニアボールを加えて、振とう混合機で1時間混合した。ジルコニアボールを除去した混合物をコニカルドライヤーに入れ、1×102Pa、80℃の条件で真空乾燥した。
続いて、このニオブ粉を1×10-2Pa、250〜400℃で12時間加熱し、ポリメチルメタクリル酸ブチルエステルを分解除去し、さらに、4×10-3Paの減圧下、1150℃で2時間焼結した。品温が30℃以下になるまで冷却した後、ニオブ焼結塊をロールグラニュレーターで解砕し、平均粒子径100μmのニオブ解砕粉を得た。
このニオブ解砕粉を、加圧下、窒素を流通させ、300℃で2時間、窒化処理を行い、約450gニオブ粉を得た。窒素含有量は、0.22%であった。
このニオブ粉のタッピング密度、平均粒子径、安息角、BET比表面積、細孔直径ピークトップなどの物理物性を表1に示す。
このようにして得られた、ニオブ粉(約0.1g)をタンタル素子自動成形機(株式会社 精研製 TAP−2R)ホッパーに入れ、0.3mmφのニオブ線と共に自動成形し、大きさがおよそ0.3cm×0.18cm×0.45cmとなるように成形体を作製した。この成形体の外観、質量のばらつきを表1に示す。
次にこれらの成形体を4×10-3Paの真空下、1250℃で30分間放置することにより焼結体を得た。この焼結体100個を用意し、20Vの電圧で、0.1%リン酸水溶液を用い、200分間電解化成して、表面に誘電体酸化皮膜を形成した。
続いて、60%硝酸マンガン水溶液に浸漬後220℃で30分間加熱することを繰り返して、誘電体酸化皮膜上に対電極層として二酸化マンガン層を形成した。引き続き、その上に、カーボン層、銀ペースト層を順次積層した。次にリードフレームを載せた後、全体をエポキシ樹脂で封止して、チップ型コンデンサを作製した。このコンデンサの容量出現率、およびこのチップ型コンデンサの容量と漏れ電流値(以下「LC」と略す)の平均(n=100個)を表1に示す。尚、LC値は室温で6.3V、1分間印加した時の値である。
Example 1: In 5000 g of potassium fluoride niobate sufficiently vacuum-dried at 80 ° C in a nickel crucible, 10 times the molar amount of sodium fluoride niobate was charged and reduced at 1000 ° C for 20 hours in an argon atmosphere. Reaction was performed. After the reaction, the reaction mixture was cooled, and the reduced product was washed with water, then washed with 95% sulfuric acid and water in that order, and then vacuum dried. Furthermore, after grind | pulverizing for 40 hours using the ball mill of the alumina pot containing a silica alumina ball | bowl, the ground material was immersed and stirred in the 3: 2 (mass ratio) liquid mixture of 50% nitric acid and 10% hydrogen peroxide solution. Thereafter, the product was sufficiently washed with water until the pH reached 7, to remove impurities, and vacuum dried. The average particle diameter of the raw material niobium powder was 1.2 μm.
500 g of this raw material niobium powder was put in a pot made of niobium, and 50 g of polymethylmethacrylic acid butyl ester having an average particle diameter of 1 μm and 1 liter of toluene were added. Further, zirconia balls were added and mixed for 1 hour with a shaking mixer. The mixture from which the zirconia balls were removed was placed in a conical dryer and vacuum dried under the conditions of 1 × 10 2 Pa and 80 ° C.
Subsequently, this niobium powder was heated at 1 × 10 −2 Pa at 250 to 400 ° C. for 12 hours to decompose and remove polymethyl methacrylate but also at 1150 ° C. under reduced pressure of 4 × 10 −3 Pa. Sintered for 2 hours. After cooling to a product temperature of 30 ° C. or lower, the niobium sintered mass was crushed with a roll granulator to obtain a niobium crushed powder having an average particle size of 100 μm.
The niobium pulverized powder was subjected to nitriding treatment at 300 ° C. for 2 hours by flowing nitrogen under pressure to obtain about 450 g of niobium powder. The nitrogen content was 0.22%.
Table 1 shows the physical properties of the niobium powder such as tapping density, average particle diameter, angle of repose, BET specific surface area, and pore diameter peak top.
The niobium powder (about 0.1 g) thus obtained is placed in a tantalum element automatic molding machine (TAP-2R manufactured by Seken Co., Ltd.) hopper and automatically molded with a 0.3 mmφ niobium wire. A molded body was prepared so as to have a size of 0.3 cm × 0.18 cm × 0.45 cm. Table 1 shows the appearance and mass variations of the molded body.
Next, these compacts were allowed to stand at 1250 ° C. for 30 minutes under a vacuum of 4 × 10 −3 Pa to obtain sintered bodies. 100 sintered bodies were prepared, and subjected to electrolytic conversion for 200 minutes using a 0.1% phosphoric acid aqueous solution at a voltage of 20 V to form a dielectric oxide film on the surface.
Subsequently, after being immersed in a 60% aqueous manganese nitrate solution, heating at 220 ° C. for 30 minutes was repeated to form a manganese dioxide layer as a counter electrode layer on the dielectric oxide film. Subsequently, a carbon layer and a silver paste layer were sequentially laminated thereon. Next, after the lead frame was mounted, the whole was sealed with an epoxy resin to produce a chip capacitor. Table 1 shows the capacitance appearance rate of this capacitor, and the average (n = 100) of the capacitance and leakage current value (hereinafter abbreviated as “LC”) of this chip capacitor. The LC value is a value when 6.3 V is applied for 1 minute at room temperature.
実施例2:ニオブインゴット1000gをSUS304製の反応容器に入れ、400℃で10時間水素を導入し続けた。冷却後、水素化されたニオブ塊を、ジルコニアボールを入れたSUS製のポットに入れ10時間粉砕した。次に、スパイクミルに、この水素化物を水で20体積%のスラリーにしたもの及びジルコニアボールを入れ、40℃以下で7時間湿式粉砕して水素化ニオブの粉砕スラリーを取得した。この原料水素化ニオブ粉の平均粒子径は、0.9μmであった。
このスラリー(スラリー濃度98%)をSUS製のポットに入れ、平均粒子径が1μmの酸化バリウム200gを添加した。更にジルコニアボールを加えて、振とう混合機で1時間混合した。ジルコニアボールを除去した混合物をニオブ製のバットに入れ、1×102Pa、50℃の条件で乾燥した。
続いて、得られた混合物を1×10-2Pa、400℃で4時間加熱し水素化ニオブを脱水素し、さらに、この混合物を4×10-3Paの減圧下、1100℃で2時間焼結した。品温が30℃以下になるまで冷却した後、酸化バリウム混合のニオブ焼結塊をロールグラニュレーターで解砕し、平均粒子径95μmの酸化バリウム混合のニオブ解砕粉を得た。
この酸化バリウム混合のニオブ解砕粉500gとイオン交換水1000gをポリテトラフルオロエチレン製の容器に入れ、15℃以下になるように冷却した。これとは別に、15℃以下に冷却した、60%硝酸600g、30%過酸化水素150g、イオン交換水750gを混合した水溶液を用意し、この水溶液500gを攪拌しながら、水温が20℃を越えないように酸化バリウム混合のニオブ解砕粉懸濁水溶液に滴下した。滴下終了後、さらに1時間攪拌を継続し、30分静置した後、デカンテーションした。イオン交換水2000gを加え、30分攪拌の後、30分静置した後、デカンテーションした。この作業を5回繰り返し、さらに、ニオブ解砕粉をポリテトラフルオロエチレン製のカラム入れ、イオン交換水を流しながら4時間水洗浄を行った。この時の洗浄水の電気伝導度は、0.9μS/cmであった。
水洗浄を終了したニオブ解砕粉を、減圧下、50℃で乾燥し、更に加圧下、窒素を流通させ、300℃で3時間、窒化処理を行い、約350gのニオブ粉を得た。 窒素含有量は、0.28%であった。
このニオブ粉のタッピング密度、平均粒子径、安息角、BET比表面積、平均細孔直径などの物理物性を表1に示す。
このようにして得られた、ニオブ粉(約0.1g)をタンタル素子自動成形機(株式会社 精研製 TAP−2R)ホッパーに入れ、0.3mmφのニオブ線と共に自動成形し、大きさがおよそ0.3cm×0.18cm×0.45cmとなるように成形体を作製した。この成形体の外観、質量のばらつきを表1に示す。
次にこれらの成形体を4×10-3Paの減圧下、1250℃で30分間放置することにより焼結体を得た。この焼結体100個を用意し、20Vの電圧で、0.1%リン酸水溶液を用い、200分間電解化成して、表面に誘電体酸化皮膜を形成した。
続いて、誘電体酸化被膜の上に、過硫酸アンモニウム10%水溶液とアントラキノンスルホン酸0.5%水溶液の等量混合液を接触させた後、ピロール蒸気を触れさせる操作を少なくとも5回行うことによりポリピロールからなる対電極(対極)を形成した。
引き続き、その上に、カーボン層、銀ペースト層を順次積層した。次にリードフレームを載せた後、全体をエポキシ樹脂で封止して、チップ型コンデンサを作製した。このコンデンサの容量出現率、およびこのチップ型コンデンサの容量とLC値の平均(n=100個)を表1に示す。尚、LC値は室温で6.3V、1分間印加した時の値である。
Example 2 1000 g of niobium ingot was placed in a reaction vessel made of SUS304, and hydrogen was continuously introduced at 400 ° C. for 10 hours. After cooling, the hydrogenated niobium lump was placed in a SUS pot containing zirconia balls and ground for 10 hours. Next, a 20% by volume slurry of this hydride with water and zirconia balls were placed in a spike mill, and wet pulverized at 40 ° C. or lower for 7 hours to obtain a pulverized niobium hydride slurry. The average particle diameter of the raw material niobium hydride powder was 0.9 μm.
This slurry (slurry concentration 98%) was put in a SUS pot, and 200 g of barium oxide having an average particle diameter of 1 μm was added. Further, zirconia balls were added and mixed for 1 hour with a shaking mixer. The mixture from which the zirconia balls were removed was placed in a niobium bat and dried under conditions of 1 × 10 2 Pa and 50 ° C.
Subsequently, the obtained mixture was heated at 1 × 10 −2 Pa at 400 ° C. for 4 hours to dehydrogenate niobium hydride, and this mixture was further reduced at 1100 ° C. for 2 hours at 4 × 10 −3 Pa under reduced pressure. Sintered. After cooling the product temperature to 30 ° C. or lower, the sintered niobium ingot mixed with barium oxide was crushed with a roll granulator to obtain a crushed niobium powder mixed with barium oxide having an average particle size of 95 μm.
500 g of niobium pulverized powder mixed with barium oxide and 1000 g of ion-exchanged water were placed in a polytetrafluoroethylene container and cooled to 15 ° C. or lower. Separately, an aqueous solution prepared by mixing 600 g of 60% nitric acid, 150 g of 30% hydrogen peroxide, and 750 g of ion-exchanged water cooled to 15 ° C. or lower is prepared, and the water temperature exceeds 20 ° C. while stirring 500 g of this aqueous solution. It was dripped in the niobium pulverized powder suspension aqueous solution mixed with barium oxide. After completion of the dropping, stirring was further continued for 1 hour, the mixture was allowed to stand for 30 minutes, and then decanted. After adding 2000 g of ion-exchanged water and stirring for 30 minutes, the mixture was allowed to stand for 30 minutes and then decanted. This operation was repeated 5 times. Further, the niobium pulverized powder was placed in a polytetrafluoroethylene column and washed with water for 4 hours while flowing ion exchange water. The electrical conductivity of the washing water at this time was 0.9 μS / cm.
The niobium crushed powder that had been washed with water was dried at 50 ° C. under reduced pressure, and further, nitrogen was passed under pressure, and nitriding was performed at 300 ° C. for 3 hours to obtain about 350 g of niobium powder. The nitrogen content was 0.28%.
Table 1 shows physical properties of the niobium powder such as tapping density, average particle diameter, angle of repose, BET specific surface area, and average pore diameter.
The niobium powder (about 0.1 g) thus obtained is placed in a tantalum element automatic molding machine (TAP-2R manufactured by Seken Co., Ltd.) hopper and automatically molded with a 0.3 mmφ niobium wire. A molded body was produced so as to be 0.3 cm × 0.18 cm × 0.45 cm. Table 1 shows the appearance and mass variations of the molded body.
Next, these compacts were allowed to stand at 1250 ° C. for 30 minutes under a reduced pressure of 4 × 10 −3 Pa to obtain sintered bodies. 100 sintered bodies were prepared, and subjected to electrolytic conversion for 200 minutes using a 0.1% phosphoric acid aqueous solution at a voltage of 20 V to form a dielectric oxide film on the surface.
Subsequently, an equivalent mixture of 10% aqueous solution of ammonium persulfate and 0.5% aqueous solution of anthraquinone sulfonic acid was brought into contact with the dielectric oxide film, and then contacted with pyrrole vapor was performed at least 5 times to make polypyrrole. The counter electrode (counter electrode) consisting of was formed.
Subsequently, a carbon layer and a silver paste layer were sequentially laminated thereon. Next, after the lead frame was mounted, the whole was sealed with an epoxy resin to produce a chip capacitor. Table 1 shows the capacity appearance rate of this capacitor and the average (n = 100) of the capacitance and LC value of this chip type capacitor. The LC value is a value when 6.3 V is applied for 1 minute at room temperature.
実施例3〜10:実施例1と同様な方法を用いポリメチルメタクリル酸ブチルエステルの平均粒子径、添加量を、また実施例2と同様な方法を用い酸化バリウムの平均粒子径、添加量を、それぞれ変化させ、ニオブ粉、その成形体、焼結体およびコンデンサを作製した。これらのニオブ粉の物理物性、成形体の外観、質量バラツキおよびコンデンサの容量、LCを表1に示す。 Examples 3 to 10: Using the same method as in Example 1, the average particle size and addition amount of polymethylmethacrylic acid butyl ester, and using the same method as in Example 2, the average particle size and addition amount of barium oxide. The niobium powder, its molded body, sintered body, and capacitor were produced by changing each of them. Table 1 shows the physical properties of these niobium powders, the appearance of the molded body, the variation in mass, the capacitance of the capacitors, and the LC.
実施例11〜22:実施例11〜14及び16〜18は実施例1と同様な方法を用い、実施例15及び19〜22は実施例2と同様な方法を用い、それぞれポリメチルメタクリル酸ブチルエステルまたは酸化バリウムの替わりに表1に示した賦活剤を用い、ニオブ粉、成形体および焼結体を作製した。ニオブ粉の物理物性、成形体の外観、質量バラツキを表1に示す。
次にこれらの成形体を4×10-3Paの減圧下、1250℃で30分間放置することにより焼結体を得た。この焼結体100個を用意し、20Vの電圧で、0.1%リン酸水溶液を用い、200分間電解化成して、表面に誘電体酸化皮膜を形成した。
続いて、過硫酸アンモニウム25質量%を含む水溶液(溶液1)に浸漬した後引き上げ、80℃で30分間乾燥させ、次いで誘電体を形成した焼結体を、3,4−エチレンジオキシチオフェン18質量%を含むイソプロパノール溶液(溶液2)に浸漬した後引き上げ、60℃の雰囲気に10分放置することで酸化重合を行った。これを再び溶液1に浸漬し、さらに前記と同様に処理した。溶液1に浸漬してから酸化重合を行うまでの操作を8回繰り返した後、50℃の温水で10分洗浄を行い、100℃で30分乾燥を行うことにより、導電性のポリ(3,4−エチレンジオキシチオフェン)からなる対電極(対極)を形成した。
引き続き、その上に、カーボン層、銀ペースト層を順次積層した。次にリードフレームを載せた後、全体をエポキシ樹脂で封止して、チップ型コンデンサを作製した。このコンデンサの容量出現率、およびこのチップ型コンデンサの容量とLC値の平均(n=100個)を表1に示す。尚、LC値は室温で6.3V、1分間印加した時の値である。
Examples 11 to 22: Examples 11 to 14 and 16 to 18 use the same method as in Example 1, Examples 15 and 19 to 22 use the same method as in Example 2, and polymethyl butyl methacrylate, respectively. Niobium powder, a molded body, and a sintered body were prepared using the activator shown in Table 1 instead of ester or barium oxide. Table 1 shows the physical properties of the niobium powder, the appearance of the molded body, and the mass variation.
Next, these compacts were allowed to stand at 1250 ° C. for 30 minutes under a reduced pressure of 4 × 10 −3 Pa to obtain sintered bodies. 100 sintered bodies were prepared, and subjected to electrolytic conversion for 200 minutes using a 0.1% phosphoric acid aqueous solution at a voltage of 20 V to form a dielectric oxide film on the surface.
Subsequently, after being immersed in an aqueous solution (solution 1) containing 25% by mass of ammonium persulfate, it is pulled up, dried at 80 ° C. for 30 minutes, and then a sintered body on which a dielectric is formed is obtained by massing 3,4-ethylenedioxythiophene by 18%. After being dipped in an isopropanol solution containing 2% (solution 2), it was pulled up and left in an atmosphere at 60 ° C. for 10 minutes to carry out oxidative polymerization. This was again immersed in solution 1 and further treated in the same manner as described above. The operation from immersion in solution 1 to oxidative polymerization was repeated 8 times, followed by washing with warm water at 50 ° C. for 10 minutes, and drying at 100 ° C. for 30 minutes, whereby conductive poly (3, A counter electrode (counter electrode) composed of 4-ethylenedioxythiophene) was formed.
Subsequently, a carbon layer and a silver paste layer were sequentially laminated thereon. Next, after the lead frame was mounted, the whole was sealed with an epoxy resin to produce a chip capacitor. Table 1 shows the capacity appearance rate of this capacitor and the average (n = 100) of the capacitance and LC value of this chip type capacitor. The LC value is a value when 6.3 V is applied for 1 minute at room temperature.
実施例23〜25:実施例2と同様な方法を用い、出発原料に、実施例23ではニオブースズ合金粉、実施例24では水素化ニオブ−レニウム合金粉、実施例25では水素化ニオブ−イットリウム−硼素合金粉をそれぞれ用いて、ニオブ粉、焼結体およびコンデンサを作製した。その物理物性および容量、LCを表1に示す。 Examples 23 to 25: Using the same method as in Example 2, the starting materials were Nio Boots alloy powder in Example 23, Niobium hydride-rhenium alloy powder in Example 24, and Niobium yttrium hydride in Example 25. Niobium powder, a sintered body, and a capacitor were prepared using each of boron alloy powders. The physical properties, capacity, and LC are shown in Table 1.
比較例1〜3:ニッケル製坩堝中、80℃で充分に真空乾燥したフッ化ニオブ酸カリウム2000gにナトリウムをフッ化ニオブ酸カリウムの10倍モル量を投入し、アルゴン雰囲気下1000℃で20時間還元反応を行った。反応後冷却させ、還元物を水洗した後に、95%硫酸、水で順次洗浄した後に真空乾燥した。さらにシリカアルミナボール入りのアルミナポットのボールミルを用いて粉砕時間を変化させ粉砕した後、粉砕物を50%硝酸と10%過酸化水素水の3:2(質量比)混合液中に浸漬撹拌した。その後、pHが7になるまで充分水洗して不純物を除去し、真空乾燥した。作製したニオブ粉の平均粒子径は1.3〜10μmであった。
この様にして得られた、それぞれのニオブ粉50gをSUS304製の反応容器に入れ、300℃で2〜4時間窒素を導入し続けて、ニオブ窒化物を得た。
このニオブ粉のタッピング密度、平均粒子径、安息角、BET比表面積、平均細孔直径などの物理物性を表1に示す。
このようにして得られた、ニオブ粉(約0.1g)をタンタル素子自動成形機(株式会社 精研製 TAP−2R)ホッパーに入れ、0.3mmφのニオブ線と共に自動成形を試みた。結果を表1に示す。
Comparative Examples 1 to 3: In a nickel crucible, sodium fluorinated niobate was thoroughly vacuum-dried at 80 ° C., and sodium was added in an
50 g of each niobium powder thus obtained was placed in a reaction vessel made of SUS304, and nitrogen was continuously introduced at 300 ° C. for 2 to 4 hours to obtain niobium nitride.
Table 1 shows physical properties of the niobium powder such as tapping density, average particle diameter, angle of repose, BET specific surface area, and average pore diameter.
The niobium powder (about 0.1 g) thus obtained was placed in a tantalum element automatic molding machine (TAP-2R manufactured by Seken Co., Ltd.) hopper, and automatic molding was attempted with a 0.3 mmφ niobium wire. The results are shown in Table 1.
比較例4〜9:平均粒子径が1μmの酸化バリウムの添加量を変化させて、実施例2と同様な方法で、タッピング密度が0.2〜0.4g/mlおよび2.6〜3.3g/mlのニオブ粉を得た。このものの物理物性を表1に示す。
このようにして得られた、ニオブ粉(約0.1g)をタンタル素子自動成形機(株式会社 精研製 TAP−2R)ホッパーに入れ、0.3mmφのニオブ線と共に自動成形し、大きさがおよそ0.3cm×0.18cm×0.45cmとなるように成形体を作製した。この成形体の外観、質量のばらつきを表1に示す。
次にこれらの成形体を4×10-3Paの真空下、1250℃で30分間放置することにより焼結体を得た。この焼結体100個を用意し、20Vの電圧で、0.1%リン酸水溶液を用い、200分間電解化成して、表面に誘電体酸化皮膜を形成した。
続いて、誘電体酸化被膜の上に、過硫酸アンモニウム10%水溶液とアントラキノンスルホン酸0.5%水溶液の等量混合液を接触させた後、ピロール蒸気を触れさせる操作を少なくとも5回行うことによりポリピロールからなる対電極(対極)を形成した。
引き続き、その上に、カーボン層、銀ペースト層を順次積層した。次にリードフレームを載せた後、全体をエポキシ樹脂で封止して、チップ型コンデンサを作製した。このコンデンサの容量出現率、およびこのチップ型コンデンサの容量とLC値の平均(n=100個)を表1に示す。尚、LC値は室温で6.3V、1分間印加した時の値である。
Comparative Examples 4 to 9: The amount of barium oxide having an average particle diameter of 1 μm was changed, and the tapping density was changed to 0.2 to 0.4 g / ml and 2.6 to 3.3 in the same manner as in Example 2. 3 g / ml of niobium powder was obtained. The physical properties of this product are shown in Table 1.
The niobium powder (about 0.1 g) thus obtained is placed in a tantalum element automatic molding machine (TAP-2R manufactured by Seken Co., Ltd.) hopper and automatically molded with a 0.3 mmφ niobium wire. A molded body was produced so as to be 0.3 cm × 0.18 cm × 0.45 cm. Table 1 shows the appearance and mass variations of the molded body.
Next, these compacts were allowed to stand at 1250 ° C. for 30 minutes under a vacuum of 4 × 10 −3 Pa to obtain sintered bodies. 100 sintered bodies were prepared, and subjected to electrolytic conversion for 200 minutes using a 0.1% phosphoric acid aqueous solution at a voltage of 20 V to form a dielectric oxide film on the surface.
Subsequently, an equivalent mixture of 10% aqueous solution of ammonium persulfate and 0.5% aqueous solution of anthraquinone sulfonic acid was brought into contact with the dielectric oxide film, and then the contact with pyrrole vapor was performed at least 5 times to make polypyrrole. The counter electrode (counter electrode) consisting of was formed.
Subsequently, a carbon layer and a silver paste layer were sequentially laminated thereon. Next, after the lead frame was mounted, the whole was sealed with an epoxy resin to produce a chip capacitor. Table 1 shows the capacity appearance rate of this capacitor and the average (n = 100) of the capacitance and LC value of this chip type capacitor. The LC value is a value when 6.3 V is applied for 1 minute at room temperature.
実施例26〜31:ニオブインゴットの水素化物を粉砕し脱水素することにより平均粒径0.8μmの一次粒子を得た。この一次粒子を焼成、粉砕し、ニオブの造粒粉を得た。この造粒粉0.1gを、別途用意した、長さ10mm、太さ0.3mmのニオブ線と共に、金型(4.0mm×3.5mm×1.8mm)に入れ、タンタル素子自動成形機(株式会社 精研製 TAP−2R)で表2に示したように加重し、成形体を作製した。ついで1300℃で30分間焼結して目的とする焼結体を得た。成形機の加重を調整することによって、表2のように細孔直径分布を持つ焼結体を作成した。実施例26の焼結体の大きさ、比表面積、CV値は各々順に、24.7mm3、1.1m2/g、85000μFV/gであり、他の例の各数値も実施例26の±2%以内であった。 Examples 26 to 31: Primary particles having an average particle diameter of 0.8 μm were obtained by pulverizing and dehydrogenating a hydride of niobium ingot. The primary particles were fired and pulverized to obtain a granulated powder of niobium. 0.1 g of this granulated powder is prepared separately and placed in a mold (4.0 mm × 3.5 mm × 1.8 mm) together with a niobium wire having a length of 10 mm and a thickness of 0.3 mm, and a tantalum element automatic molding machine Weight was applied as shown in Table 2 with TAP-2R (Seken Co., Ltd.) to produce a molded body. Subsequently, it sintered at 1300 degreeC for 30 minutes, and the target sintered compact was obtained. By adjusting the weight of the molding machine, sintered bodies having a pore diameter distribution as shown in Table 2 were prepared. The size, specific surface area, and CV value of the sintered body of Example 26 are 24.7 mm 3 , 1.1 m 2 / g, and 85000 μFV / g, respectively. It was within 2%.
実施例32〜34:一次粒子を分級することにより、一次粒子の平均粒径を0.5μmとした以外は、実施例26〜28と同様にして焼結体を得た。実施例32の焼結体の大きさ、比表面積、CV値は各々順に、24.9mm3、1.5m2/g、125000μFV/gであり、他の例の各数値も実施例32の±1%以内であった。作製した焼結体の細孔直径分布を表2に記載した。 Examples 32-34: Sintered bodies were obtained in the same manner as in Examples 26-28, except that the primary particles were classified to make the average particle size of the primary particles 0.5 μm. The size, specific surface area, and CV value of the sintered body of Example 32 were 24.9 mm 3 , 1.5 m 2 / g, and 125000 μFV / g, respectively. It was within 1%. The pore diameter distribution of the produced sintered body is shown in Table 2.
実施例35:造粒粉の代りに実施例4と同様にして得たニオブ粉を用い、実施例31と同様にして焼結体を得た。実施例35の焼結体の大きさ、比表面積、CV値は各々順に、24.8mm3、1.2m2/g、78000μFV/gであった。作製した焼結体の細孔直径分布を表2に記載した。 Example 35: A niobium powder obtained in the same manner as in Example 4 was used instead of the granulated powder, and a sintered body was obtained in the same manner as in Example 31. The size, specific surface area, and CV value of the sintered body of Example 35 were 24.8 mm 3 , 1.2 m 2 / g, and 78000 μFV / g, respectively. The pore diameter distribution of the produced sintered body is shown in Table 2.
比較例10〜12:実施例26〜28で使用したニオブ造粒粉の代わりに、塩化ニオブをマグネシウムで還元して得たニオブ粉を1100℃で熱処理して得たニオブ粉とした以外は実施例26〜28と同様にして焼結体を作製した。作製した比較例10の焼結体の大きさ、比表面積,CV値は各々順に、24.3mm3、0.8m2/g、84000μFV/gであり、他の実施例の諸数値も比較例10の±2%以内であった。作製した焼結体の細孔直径分布を表2に記載した。 Comparative Examples 10-12: Implemented except that niobium powder obtained by reducing niobium chloride with magnesium instead of the niobium granulated powder used in Examples 26-28 was heat treated at 1100 ° C. Sintered bodies were produced in the same manner as in Examples 26 to 28. The size, specific surface area, and CV value of the produced sintered body of Comparative Example 10 were 24.3 mm 3 , 0.8 m 2 / g, and 84000 μFV / g, respectively. Within 10 ± 2%. The pore diameter distribution of the produced sintered body is shown in Table 2.
実施例36:実施例21及び実施例26〜35で焼結体を作製した方法で、同様の焼結体を各々で60個作製し、各焼結体を0.1%燐酸水溶液中で80℃,1000分,20Vで化成し、焼結体表面に誘電体酸化皮膜層を形成した。次にこの化成済み焼結体を各々30個づつに分け、各30個組の焼結体に表3に示したA,Bの2種類の陰極剤を含浸させた後、カーボンペースト、銀ペーストを順に積層し、エポキシ樹脂で封口してチップ型コンデンサを作製した。作製したコンデンサの容量出現率および耐湿値を表4に示した。 Example 36: The method of producing sintered bodies in Example 21 and Examples 26 to 35 was used to produce 60 similar sintered bodies each, and each sintered body was 80 in 0.1% phosphoric acid aqueous solution. Chemical conversion was carried out at 20 ° C. for 1000 minutes, and a dielectric oxide film layer was formed on the surface of the sintered body. Next, the formed sintered body is divided into 30 parts each, and each set of 30 sintered bodies is impregnated with two kinds of cathode agents A and B shown in Table 3, and then carbon paste, silver paste Were sequentially laminated and sealed with an epoxy resin to produce a chip-type capacitor. Table 4 shows the capacity appearance rate and the moisture resistance value of the manufactured capacitors.
比較例13:比較例9〜12で焼結体を作製した方法で、同様の焼結体を各々で60個作製し、各焼結体を0.1%燐酸水溶液中で80℃,1000分,20Vで化成し、焼結体表面に誘電体酸化皮膜層を形成した。次にこの化成済み焼結体を各々30個づつに分け、各30個組の焼結体に表3に示したAの陰極剤を含浸させた後、カーボンペースト、銀ペーストを順に積層し、エポキシ樹脂で封口してチップ型コンデンサを作製した。作製したコンデンサの容量出現率および耐湿値を表4に示した。 Comparative Example 13: In the method in which the sintered bodies were prepared in Comparative Examples 9 to 12, 60 similar sintered bodies were each prepared, and each sintered body was 80 ° C. for 1000 minutes in a 0.1% phosphoric acid aqueous solution. , 20 V, and a dielectric oxide film layer was formed on the surface of the sintered body. Next, each of the formed sintered bodies is divided into 30 pieces, and each set of 30 sintered bodies is impregnated with the cathode agent of A shown in Table 3, and then a carbon paste and a silver paste are sequentially laminated, A chip capacitor was fabricated by sealing with an epoxy resin. Table 4 shows the capacity appearance rate and the moisture resistance value of the manufactured capacitors.
実施例37:実施例2と同様な方法で、原料水素化ニオブ粉の粉砕スラリーを得た。この水素化ニオブ粉の平均粒径は、0.6μmであった。このスラリーを遠心沈降させた後、デカンテーションして上澄みを除去した。無水アセトンをスラリー濃度40質量%になるように添加し良く懸濁させたのち、遠心沈降させ、上澄みを除去した。この操作を3回繰り返した。無水アセトンをスラリー濃度が60質量%になるように添加し良く懸濁した。このスラリーをSUS製のポットに入れ、平均粒径が1.4μmと23μmの酸化バリウムをニオブに対してそれぞれ15質量%および10質量%添加した。更にジルコニアボールを加えて、振とう混合機で1時間混合した。ジルコニアボールを除去した混合物をニオブ製のバットに入れ、1×102Pa、50℃の条件で乾燥した。実施例2と同様な操作で酸化バリウム混合のニオブ焼結塊、およびニオブ解砕粉を得た。
15℃以下に冷却したイオン交換水1000gに、この酸化バリウム混合のニオブ解砕粉500gを撹拌しながら、水温が20℃を超えないように添加した。添加終了後、更に1時間撹拌を継続し、30分静置した後デカンテーションした。イオン交換水2000gを加え、30分撹拌の後、30分静置し、デカンテーションした。この作業を5回繰り返し、さらに、ニオブ解砕粉をポリテトラフルオロエチレン製のカラムに入れイオン交換水を流しながら4時間水洗浄をおこなった。この時の洗浄水の電気伝導度は、0.5μS/cmであった。
水洗浄を終了したニオブ解砕粉を、減圧下、50℃で乾燥し、更に加圧下、窒素を流通させ、300℃で3時間、窒化処理を行い、約350gのニオブ粉を得た。 窒素含有量は、0.30%であった。このニオブ粉のタッピング密度、平均粒子径、安息角、BET比表面積、平均細孔直径などの物理物性を表5に示す。実施例2と同様な操作で成形体を作成した。この成形体の外観、質量のばらつきを表5に示す。
更に、実施例2と同様な操作で誘電皮膜を形成させた後、つい電極を形成し、カーボン層、銀ペースト層を積層させた。次にリードフレームを載せた後、全体をエポキシ樹脂で封止して、チップ型コンデンサを作製した。このコンデンサの容量出現率、およびこのチップ型コンデンサの容量とLC値の平均(n=100個)を表5に示す。
Example 37 A ground slurry of niobium hydride powder was obtained in the same manner as in Example 2. The average particle diameter of the niobium hydride powder was 0.6 μm. The slurry was spun down and decanted to remove the supernatant. Anhydrous acetone was added to a slurry concentration of 40% by mass and suspended well, followed by centrifugal sedimentation, and the supernatant was removed. This operation was repeated three times. Anhydrous acetone was added to a slurry concentration of 60% by mass and suspended well. This slurry was put in a SUS pot, and 15 mass% and 10 mass% of barium oxide having an average particle diameter of 1.4 μm and 23 μm were added to niobium, respectively. Further, zirconia balls were added and mixed for 1 hour with a shaking mixer. The mixture from which the zirconia balls were removed was placed in a niobium bat and dried under conditions of 1 × 10 2 Pa and 50 ° C. A niobium sintered lump mixed with barium oxide and a niobium pulverized powder were obtained in the same manner as in Example 2.
500 g of niobium pulverized powder mixed with barium oxide was added to 1000 g of ion-exchanged water cooled to 15 ° C. or lower while stirring so that the water temperature did not exceed 20 ° C. After completion of the addition, stirring was further continued for 1 hour, and the mixture was allowed to stand for 30 minutes and then decanted. After adding 2000 g of ion-exchanged water and stirring for 30 minutes, the mixture was allowed to stand for 30 minutes and decanted. This operation was repeated 5 times, and the niobium pulverized powder was placed in a polytetrafluoroethylene column and washed with water for 4 hours while flowing ion exchange water. The electrical conductivity of the washing water at this time was 0.5 μS / cm.
The niobium crushed powder that had been washed with water was dried at 50 ° C. under reduced pressure, and further, nitrogen was passed under pressure, and nitriding was performed at 300 ° C. for 3 hours to obtain about 350 g of niobium powder. The nitrogen content was 0.30%. Table 5 shows the physical properties of the niobium powder such as tapping density, average particle diameter, angle of repose, BET specific surface area, and average pore diameter. A molded body was prepared in the same manner as in Example 2. Table 5 shows variations in appearance and mass of the molded body.
Further, after a dielectric film was formed by the same operation as in Example 2, an electrode was formed and a carbon layer and a silver paste layer were laminated. Next, after the lead frame was mounted, the whole was sealed with an epoxy resin to produce a chip capacitor. Table 5 shows the capacity appearance rate of this capacitor, and the average (n = 100) of the capacity and LC value of this chip capacitor.
実施例38〜44:実施例37と同様な方法で、添加する賦活剤の種類、混合する2種類の平均粒径、および添加量を変化させて賦活剤混合のニオブ解砕粉を得た。賦活剤を溶出する溶媒を、水、酸、アルカリ、イオン交換樹脂を含む溶液、硝酸アンモニウム溶液、エチレンジアミン4酢酸を含む溶液の中から選び、実施例37と同様な方法で賦活剤を溶出して、ニオブ粉を得た。その物理物性を表5に示す。更に実施例37と同様な方法で、成形体、焼結体を作成して、チップ型コンデンサを作成した。成形体の外観、質量のばらつき、コンデンサの容量とLCの平均を表5に示す。 Examples 38 to 44: In the same manner as in Example 37, the type of activator to be added, the two types of average particle sizes to be mixed, and the amount added were changed to obtain niobium crushed powder mixed with an activator. The solvent for eluting the activator is selected from water, acid, alkali, a solution containing an ion exchange resin, an ammonium nitrate solution, and a solution containing ethylenediaminetetraacetic acid, and the activator is eluted in the same manner as in Example 37. Niobium powder was obtained. The physical properties are shown in Table 5. Further, a molded body and a sintered body were prepared by the same method as in Example 37, and a chip capacitor was prepared. Table 5 shows the appearance, mass variation, capacitor capacity, and LC average of the molded body.
実施例45〜47:実施例37と同様な方法を用い、出発原料に実施例45はニオブ−ネオジム合金粉、実施例46はニオブ−タングステン合金粉、実施例47はニオブ−タンタル合金粉を用い、それぞれニオブ合金粉を得た。その物理物性を表5に示す。更に実施例37と同様な方法で、成形体、焼結体を作成して、チップ型コンデンサを作成した。成形体の外観、質量のばらつき、コンデンサの容量とLCの平均を表5に示す。 Examples 45 to 47: Using the same method as in Example 37, as starting materials, Example 45 uses niobium-neodymium alloy powder, Example 46 uses niobium-tungsten alloy powder, and Example 47 uses niobium-tantalum alloy powder. In each case, a niobium alloy powder was obtained. The physical properties are shown in Table 5. Further, a molded body and a sintered body were prepared by the same method as in Example 37, and a chip capacitor was prepared. Table 5 shows the appearance, mass variation, capacitor capacity, and LC average of the molded body.
実施例48〜58:実施例37〜47で作成したニオブ粉を用いて実施例2と同様な方法でニオブ焼結体を作成した。その焼結体の細孔直径分布を表6に示す。 Examples 48 to 58: Niobium sintered bodies were prepared in the same manner as in Example 2 using the niobium powder prepared in Examples 37 to 47. Table 6 shows the pore diameter distribution of the sintered body.
実施例59〜69:実施例48〜58で作作製したニオブ焼結体を各々100個作製し、各焼結体を0.1%燐酸水溶液中で80℃,1000分,20Vで化成し、焼結体表面に誘電体酸化皮膜層を形成した。次にこの化成済み焼結体を表3に示したAの陰極剤を含浸させた後、カーボンペースト、銀ペーストを順に積層し、エポキシ樹脂で封口してチップ型コンデンサを作製した。作製したコンデンサの容量出現率およびESRを表7に示す。 Examples 59 to 69: 100 niobium sintered bodies produced in Examples 48 to 58 were produced, and each sintered body was formed in a 0.1% phosphoric acid aqueous solution at 80 ° C. for 1000 minutes at 20 V. A dielectric oxide film layer was formed on the surface of the sintered body. Next, the formed sintered body was impregnated with the cathode agent A shown in Table 3, and then a carbon paste and a silver paste were laminated in order and sealed with an epoxy resin to produce a chip type capacitor. Table 7 shows the capacity appearance rate and ESR of the manufactured capacitor.
比較例14〜17:比較例9〜12で作製したニオブ焼結体を各々100個作製し、各焼結体を0.1%燐酸水溶液中で80℃,1000分,20Vで化成し、焼結体表面に誘電体酸化皮膜層を形成した。次にこの化成済み焼結体を表3に示したAの陰極剤を含浸させた後、カーボンペースト、銀ペーストを順に積層し、エポキシ樹脂で封口してチップ型コンデンサを作製した。作製したコンデンサの容量出現率およびESRを表7に示す。 Comparative Examples 14 to 17: 100 niobium sintered bodies prepared in Comparative Examples 9 to 12 were prepared, and each sintered body was formed in a 0.1% phosphoric acid aqueous solution at 80 ° C. for 1000 minutes at 20 V, and then sintered. A dielectric oxide film layer was formed on the bonded surface. Next, the formed sintered body was impregnated with the cathode agent A shown in Table 3, and then a carbon paste and a silver paste were laminated in order and sealed with an epoxy resin to produce a chip type capacitor. Table 7 shows the capacity appearance rate and ESR of the manufactured capacitor.
1 細孔A
2 細孔B
1 Pore A
2 Pore B
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