WO2004047984A1 - 触媒体 - Google Patents
触媒体 Download PDFInfo
- Publication number
- WO2004047984A1 WO2004047984A1 PCT/JP2003/014725 JP0314725W WO2004047984A1 WO 2004047984 A1 WO2004047984 A1 WO 2004047984A1 JP 0314725 W JP0314725 W JP 0314725W WO 2004047984 A1 WO2004047984 A1 WO 2004047984A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- catalyst
- porous carrier
- metal
- oxide film
- alkali metal
- Prior art date
Links
- 230000003197 catalytic effect Effects 0.000 title abstract description 12
- 239000003054 catalyst Substances 0.000 claims abstract description 147
- 229910052783 alkali metal Inorganic materials 0.000 claims abstract description 48
- 150000001340 alkali metals Chemical class 0.000 claims abstract description 48
- 239000002245 particle Substances 0.000 claims abstract description 29
- 229910052575 non-oxide ceramic Inorganic materials 0.000 claims abstract description 25
- 239000011225 non-oxide ceramic Substances 0.000 claims abstract description 25
- 239000011521 glass Substances 0.000 claims abstract description 21
- 238000002844 melting Methods 0.000 claims abstract description 20
- 239000000126 substance Substances 0.000 claims abstract description 20
- 150000001875 compounds Chemical class 0.000 claims abstract description 14
- 239000011148 porous material Substances 0.000 claims abstract description 10
- 230000008018 melting Effects 0.000 claims abstract description 4
- 239000010410 layer Substances 0.000 claims description 26
- 229910052751 metal Inorganic materials 0.000 claims description 25
- 239000002184 metal Substances 0.000 claims description 25
- 229910052784 alkaline earth metal Inorganic materials 0.000 claims description 20
- 150000001342 alkaline earth metals Chemical class 0.000 claims description 20
- 239000011241 protective layer Substances 0.000 claims description 18
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 claims description 16
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 14
- 238000005192 partition Methods 0.000 claims description 11
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 claims description 9
- HBMJWWWQQXIZIP-UHFFFAOYSA-N silicon carbide Chemical compound [Si+]#[C-] HBMJWWWQQXIZIP-UHFFFAOYSA-N 0.000 claims description 9
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 claims description 8
- 229910052697 platinum Inorganic materials 0.000 claims description 7
- 229910052710 silicon Inorganic materials 0.000 claims description 7
- 239000010703 silicon Substances 0.000 claims description 7
- 229910010271 silicon carbide Inorganic materials 0.000 claims description 7
- 239000000377 silicon dioxide Substances 0.000 claims description 7
- 239000010936 titanium Substances 0.000 claims description 7
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims description 6
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims description 6
- 229910052719 titanium Inorganic materials 0.000 claims description 6
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 5
- 239000010949 copper Substances 0.000 claims description 5
- 230000005496 eutectics Effects 0.000 claims description 5
- 239000010955 niobium Substances 0.000 claims description 5
- 229910000510 noble metal Inorganic materials 0.000 claims description 5
- 239000010948 rhodium Substances 0.000 claims description 5
- 239000011135 tin Substances 0.000 claims description 5
- 229910052581 Si3N4 Inorganic materials 0.000 claims description 4
- 239000011651 chromium Substances 0.000 claims description 4
- 239000011572 manganese Substances 0.000 claims description 4
- VSZWPYCFIRKVQL-UHFFFAOYSA-N selanylidenegallium;selenium Chemical compound [Se].[Se]=[Ga].[Se]=[Ga] VSZWPYCFIRKVQL-UHFFFAOYSA-N 0.000 claims description 4
- HQVNEWCFYHHQES-UHFFFAOYSA-N silicon nitride Chemical compound N12[Si]34N5[Si]62N3[Si]51N64 HQVNEWCFYHHQES-UHFFFAOYSA-N 0.000 claims description 4
- 229910052727 yttrium Inorganic materials 0.000 claims description 4
- VWQVUPCCIRVNHF-UHFFFAOYSA-N yttrium atom Chemical compound [Y] VWQVUPCCIRVNHF-UHFFFAOYSA-N 0.000 claims description 4
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 claims description 3
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 3
- GYHNNYVSQQEPJS-UHFFFAOYSA-N Gallium Chemical compound [Ga] GYHNNYVSQQEPJS-UHFFFAOYSA-N 0.000 claims description 3
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 claims description 3
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 claims description 3
- 150000001341 alkaline earth metal compounds Chemical class 0.000 claims description 3
- 229910052787 antimony Inorganic materials 0.000 claims description 3
- WATWJIUSRGPENY-UHFFFAOYSA-N antimony atom Chemical compound [Sb] WATWJIUSRGPENY-UHFFFAOYSA-N 0.000 claims description 3
- 229910052804 chromium Inorganic materials 0.000 claims description 3
- 229910017052 cobalt Inorganic materials 0.000 claims description 3
- 239000010941 cobalt Substances 0.000 claims description 3
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 claims description 3
- 229910052802 copper Inorganic materials 0.000 claims description 3
- 239000012530 fluid Substances 0.000 claims description 3
- 229910052733 gallium Inorganic materials 0.000 claims description 3
- 229910052732 germanium Inorganic materials 0.000 claims description 3
- GNPVGFCGXDBREM-UHFFFAOYSA-N germanium atom Chemical compound [Ge] GNPVGFCGXDBREM-UHFFFAOYSA-N 0.000 claims description 3
- 229910052750 molybdenum Inorganic materials 0.000 claims description 3
- 239000011733 molybdenum Substances 0.000 claims description 3
- 229910052759 nickel Inorganic materials 0.000 claims description 3
- 229910052758 niobium Inorganic materials 0.000 claims description 3
- GUCVJGMIXFAOAE-UHFFFAOYSA-N niobium atom Chemical compound [Nb] GUCVJGMIXFAOAE-UHFFFAOYSA-N 0.000 claims description 3
- 229910052763 palladium Inorganic materials 0.000 claims description 3
- 229910052703 rhodium Inorganic materials 0.000 claims description 3
- MHOVAHRLVXNVSD-UHFFFAOYSA-N rhodium atom Chemical compound [Rh] MHOVAHRLVXNVSD-UHFFFAOYSA-N 0.000 claims description 3
- 229910052706 scandium Inorganic materials 0.000 claims description 3
- SIXSYDAISGFNSX-UHFFFAOYSA-N scandium atom Chemical compound [Sc] SIXSYDAISGFNSX-UHFFFAOYSA-N 0.000 claims description 3
- 229910052718 tin Inorganic materials 0.000 claims description 3
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 claims description 2
- 239000003513 alkali Substances 0.000 claims description 2
- 229910052748 manganese Inorganic materials 0.000 claims description 2
- JBQYATWDVHIOAR-UHFFFAOYSA-N tellanylidenegermanium Chemical compound [Te]=[Ge] JBQYATWDVHIOAR-UHFFFAOYSA-N 0.000 claims description 2
- LEONUFNNVUYDNQ-UHFFFAOYSA-N vanadium atom Chemical compound [V] LEONUFNNVUYDNQ-UHFFFAOYSA-N 0.000 claims description 2
- 150000002736 metal compounds Chemical class 0.000 claims 1
- 230000003449 preventive effect Effects 0.000 abstract 1
- 210000004027 cell Anatomy 0.000 description 46
- MWUXSHHQAYIFBG-UHFFFAOYSA-N Nitric oxide Chemical compound O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 26
- 238000003860 storage Methods 0.000 description 24
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 21
- 239000011591 potassium Substances 0.000 description 21
- 229910052700 potassium Inorganic materials 0.000 description 21
- 238000000034 method Methods 0.000 description 14
- 239000007789 gas Substances 0.000 description 13
- 239000000463 material Substances 0.000 description 13
- 239000000243 solution Substances 0.000 description 10
- 239000004927 clay Substances 0.000 description 9
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 7
- 230000000694 effects Effects 0.000 description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 6
- 238000009792 diffusion process Methods 0.000 description 6
- 229910052744 lithium Inorganic materials 0.000 description 6
- 238000001035 drying Methods 0.000 description 5
- 239000011734 sodium Substances 0.000 description 5
- 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
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 4
- 229920002472 Starch Polymers 0.000 description 4
- 239000011248 coating agent Substances 0.000 description 4
- 238000000576 coating method Methods 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 4
- 229910052878 cordierite Inorganic materials 0.000 description 4
- 230000007423 decrease Effects 0.000 description 4
- JSKIRARMQDRGJZ-UHFFFAOYSA-N dimagnesium dioxido-bis[(1-oxido-3-oxo-2,4,6,8,9-pentaoxa-1,3-disila-5,7-dialuminabicyclo[3.3.1]nonan-7-yl)oxy]silane Chemical compound [Mg++].[Mg++].[O-][Si]([O-])(O[Al]1O[Al]2O[Si](=O)O[Si]([O-])(O1)O2)O[Al]1O[Al]2O[Si](=O)O[Si]([O-])(O1)O2 JSKIRARMQDRGJZ-UHFFFAOYSA-N 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 229910052574 oxide ceramic Inorganic materials 0.000 description 4
- 239000011224 oxide ceramic Substances 0.000 description 4
- 229910052708 sodium Inorganic materials 0.000 description 4
- 239000008107 starch Substances 0.000 description 4
- 235000019698 starch Nutrition 0.000 description 4
- 238000007088 Archimedes method Methods 0.000 description 3
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 3
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 3
- 239000012298 atmosphere Substances 0.000 description 3
- 239000011230 binding agent Substances 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- 229910052791 calcium Inorganic materials 0.000 description 3
- 239000011575 calcium Substances 0.000 description 3
- 239000003795 chemical substances by application Substances 0.000 description 3
- 239000011247 coating layer Substances 0.000 description 3
- 238000011156 evaluation Methods 0.000 description 3
- 238000010304 firing Methods 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 238000000746 purification Methods 0.000 description 3
- 238000012360 testing method Methods 0.000 description 3
- 230000008646 thermal stress Effects 0.000 description 3
- 229910001148 Al-Li alloy Inorganic materials 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 239000004215 Carbon black (E152) Substances 0.000 description 2
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 2
- QCWXUUIWCKQGHC-UHFFFAOYSA-N Zirconium Chemical compound [Zr] QCWXUUIWCKQGHC-UHFFFAOYSA-N 0.000 description 2
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 2
- 229910052788 barium Inorganic materials 0.000 description 2
- DSAJWYNOEDNPEQ-UHFFFAOYSA-N barium atom Chemical compound [Ba] DSAJWYNOEDNPEQ-UHFFFAOYSA-N 0.000 description 2
- 229910052792 caesium Inorganic materials 0.000 description 2
- TVFDJXOCXUVLDH-UHFFFAOYSA-N caesium atom Chemical compound [Cs] TVFDJXOCXUVLDH-UHFFFAOYSA-N 0.000 description 2
- 238000001354 calcination Methods 0.000 description 2
- 239000000919 ceramic Substances 0.000 description 2
- 239000000470 constituent Substances 0.000 description 2
- 230000003247 decreasing effect Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 239000000428 dust Substances 0.000 description 2
- 229910002804 graphite Inorganic materials 0.000 description 2
- 239000010439 graphite Substances 0.000 description 2
- 238000007602 hot air drying Methods 0.000 description 2
- 229930195733 hydrocarbon Natural products 0.000 description 2
- 150000002430 hydrocarbons Chemical class 0.000 description 2
- -1 hydroxypropoxymethyl Chemical group 0.000 description 2
- 239000001866 hydroxypropyl methyl cellulose Substances 0.000 description 2
- 229920003088 hydroxypropyl methyl cellulose Polymers 0.000 description 2
- UFVKGYZPFZQRLF-UHFFFAOYSA-N hydroxypropyl methyl cellulose Chemical compound OC1C(O)C(OC)OC(CO)C1OC1C(O)C(O)C(OC2C(C(O)C(OC3C(C(O)C(O)C(CO)O3)O)C(CO)O2)O)C(CO)O1 UFVKGYZPFZQRLF-UHFFFAOYSA-N 0.000 description 2
- 235000010979 hydroxypropyl methyl cellulose Nutrition 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 2
- 229910052753 mercury Inorganic materials 0.000 description 2
- 150000002739 metals Chemical class 0.000 description 2
- 229910017604 nitric acid Inorganic materials 0.000 description 2
- FGIUAXJPYTZDNR-UHFFFAOYSA-N potassium nitrate Chemical compound [K+].[O-][N+]([O-])=O FGIUAXJPYTZDNR-UHFFFAOYSA-N 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 238000007789 sealing Methods 0.000 description 2
- 230000035939 shock Effects 0.000 description 2
- 239000011863 silicon-based powder Substances 0.000 description 2
- 229910052726 zirconium Inorganic materials 0.000 description 2
- MGWGWNFMUOTEHG-UHFFFAOYSA-N 4-(3,5-dimethylphenyl)-1,3-thiazol-2-amine Chemical compound CC1=CC(C)=CC(C=2N=C(N)SC=2)=C1 MGWGWNFMUOTEHG-UHFFFAOYSA-N 0.000 description 1
- 229910052684 Cerium Inorganic materials 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- 239000004480 active ingredient Substances 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 239000012300 argon atmosphere Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 239000011324 bead Substances 0.000 description 1
- 230000033228 biological regulation Effects 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- GWXLDORMOJMVQZ-UHFFFAOYSA-N cerium Chemical compound [Ce] GWXLDORMOJMVQZ-UHFFFAOYSA-N 0.000 description 1
- 239000003426 co-catalyst Substances 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 235000014113 dietary fatty acids Nutrition 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 239000000194 fatty acid Substances 0.000 description 1
- 229930195729 fatty acid Natural products 0.000 description 1
- 150000004665 fatty acids Chemical class 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 229910052809 inorganic oxide Inorganic materials 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 238000005304 joining Methods 0.000 description 1
- 238000004898 kneading Methods 0.000 description 1
- 229910052746 lanthanum Inorganic materials 0.000 description 1
- FZLIPJUXYLNCLC-UHFFFAOYSA-N lanthanum atom Chemical compound [La] FZLIPJUXYLNCLC-UHFFFAOYSA-N 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000007791 liquid phase 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
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 229910001092 metal group alloy Inorganic materials 0.000 description 1
- 229910044991 metal oxide Inorganic materials 0.000 description 1
- 150000004706 metal oxides Chemical class 0.000 description 1
- 229920000609 methyl cellulose Polymers 0.000 description 1
- 239000001923 methylcellulose Substances 0.000 description 1
- 239000011859 microparticle Substances 0.000 description 1
- 239000012299 nitrogen atmosphere Substances 0.000 description 1
- JCXJVPUVTGWSNB-UHFFFAOYSA-N nitrogen dioxide Inorganic materials O=[N]=O JCXJVPUVTGWSNB-UHFFFAOYSA-N 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- RVTZCBVAJQQJTK-UHFFFAOYSA-N oxygen(2-);zirconium(4+) Chemical compound [O-2].[O-2].[Zr+4] RVTZCBVAJQQJTK-UHFFFAOYSA-N 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
- CJWLZBLADIYQOV-UHFFFAOYSA-L platinum(2+);dinitrite Chemical compound [Pt+2].[O-]N=O.[O-]N=O CJWLZBLADIYQOV-UHFFFAOYSA-L 0.000 description 1
- 210000001316 polygonal cell Anatomy 0.000 description 1
- 235000010333 potassium nitrate Nutrition 0.000 description 1
- 239000004323 potassium nitrate Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000009257 reactivity Effects 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 238000003756 stirring Methods 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
- 230000001629 suppression Effects 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
- 229920003002 synthetic resin Polymers 0.000 description 1
- 239000000057 synthetic resin 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
- 238000001238 wet grinding Methods 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
- 229910001928 zirconium oxide Inorganic materials 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/86—Catalytic processes
- B01D53/88—Handling or mounting catalysts
- B01D53/885—Devices in general for catalytic purification of waste gases
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/92—Chemical or biological purification of waste gases of engine exhaust gases
- B01D53/94—Chemical or biological purification of waste gases of engine exhaust gases by catalytic processes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
- B01J21/06—Silicon, titanium, zirconium or hafnium; Oxides or hydroxides thereof
- B01J21/066—Zirconium or hafnium; Oxides or hydroxides thereof
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
- B01J23/54—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/56—Platinum group metals
- B01J23/58—Platinum group metals with alkali- or alkaline earth metals
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/02—Impregnation, coating or precipitation
- B01J37/024—Multiple impregnation or coating
- B01J37/0244—Coatings comprising several layers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/02—Impregnation, coating or precipitation
- B01J37/024—Multiple impregnation or coating
- B01J37/0248—Coatings comprising impregnated particles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
- B01J21/06—Silicon, titanium, zirconium or hafnium; Oxides or hydroxides thereof
- B01J21/063—Titanium; Oxides or hydroxides thereof
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J33/00—Protection of catalysts, e.g. by coating
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/50—Catalysts, in general, characterised by their form or physical properties characterised by their shape or configuration
- B01J35/56—Foraminous structures having flow-through passages or channels, e.g. grids or three-dimensional monoliths
Definitions
- the present invention relates to a catalyst that can be suitably used for purifying automobile exhaust gas. More specifically, the present invention relates to a catalyst carrier made of a non-oxide ceramic or the like, in which a nitrogen oxide storage catalyst such as metal oxide is supported. The present invention relates to a catalyst body that can effectively prevent a decrease in catalytic activity when the catalyst body is used. Background art
- N ⁇ x storage catalyst nitrogen oxide storage catalyst which can be (hereinafter, referred to as "the NO x storage catalyst") has been put into practical use.
- N ⁇ x storage catalysts include alkali metals (potassium (K), sodium (Na), lithium (Li), cesium (Cs), etc.), alkaline earth metals (barium (Ba), calcium ( C a) and rare earths (lanthanum (L a), yttrium (Y), etc.) as active ingredients.
- NO x storage capacity potassium which is excellent in nitrogen oxide storage capacity
- Such the NO x storage catalyst is usually used in the form of an oxide Seramitsu consisting click catalyst carrier supported on the catalyst as cordierite.
- catalyst supports made of oxide ceramics are made of alkali metals and alkaline earth metals (hereinafter referred to as “alkali metals”) activated at high temperatures by exhaust gas, especially lithium, sodium, potassium, calcium, etc.
- alkali metals alkali metals activated at high temperatures by exhaust gas, especially lithium, sodium, potassium, calcium, etc.
- the catalyst carrier was easily deteriorated by corrosion, and as the deterioration progressed, cracks occurred in the catalyst support.
- the catalytic performance deteriorates with time because alkali metals and the like are consumed by reacting with the catalyst carrier.
- the surface of the catalyst support is coated with some kind of coating layer.
- Coated Te a method of carrying the NO x storage catalyst over the coating layer has been proposed (e.g., JP-A-1 0 1 3 7 5 9 0 and JP Patent 2 0 0 2 5 9 No. 09 publication). According to these methods, the coating layer suppresses the diffusion of the alkali metal or the like to the catalyst carrier, and furthermore, the reaction between the alkali metal or the like and the catalyst carrier, thereby avoiding the above problem.
- non-oxide ceramics such as silicon carbide have attracted attention as a material constituting a catalyst carrier.
- Non-oxide ceramics have excellent heat resistance and chemical durability, and are unlikely to react with alkali metals, which are NO x storage catalysts, even at high temperatures due to exhaust gas. Therefore, unlike oxide ceramics, there should be no problems such as cracking of the catalyst support or reduction in catalytic activity.
- an alkali metal or the like is supported on a catalyst carrier made of a non-oxide ceramic, cracks do not occur on the catalyst carrier, but the catalyst activity decreases more than expected with respect to the usage time. There was a problem of doing it. Disclosure of the invention
- the present invention has been made in view of the prior art problems as described above, when the catalyst carrier made of non-oxides ceramics was supported alkali metal or the like is the NO x storage catalyst, the catalytic activity
- An object of the present invention is to provide a catalyst body which can effectively prevent the reduction and has an advantageous effect as compared with the conventional one.
- the present inventors have conducted intensive studies to solve the above-mentioned problems, and as a result, have found that in a porous carrier containing non-oxide ceramics or the like as a main component, an oxide unavoidably formed on a part of the surface of the aggregate particles.
- the above problem is solved by disposing an oxide film protective layer made of a substance that does not form a low-melting glass with an alkali metal or the like so as to cover at least a part of the oxide film between the film and the catalyst layer.
- a porous carrier in which a large number of aggregate particles mainly composed of a non-oxide ceramic and Z or a metal are connected to each other in a state having a large number of pores, and an aluminum carrier supported on the porous carrier.
- a catalyst further comprising an oxide film protective layer made of a substance that does not form a low-melting glass with an alkaline earth metal.
- the porous carrier silicon carbide (S i C), metal silicon bonded silicon carbide (S i - S i C) , at least one material selected from silicon nitride (S i 3 N 4)
- the substance that does not form a low-melting glass with the Al-Li metal and / or the Al-earth metal is a compound of at least one element selected from the elements belonging to Group A below. 1]
- Group A scandium (S c), titanium (T i), vanadium (V), chromium (one C, manganese (Mn), iron (F e), cobalt (Co), nickel (N i), copper ( Cu), zinc (Zn), gallium (Ga), germanium (Ge), yttrium (Y), zirconium (Zr), niobium (Nb), molybdenum (Mo), tin (Sn), and antimony (Sb) )
- the substance that does not form a low-melting glass with the alkali metal and / or the alkaline earth metal is at least selected from zirconium (Zr) and titanium (Ti) among the elements belonging to Group A.
- the catalyst layer is formed of at least one noble metal element selected from platinum (Pt), palladium (Pd), and rhodium (Rh), in addition to the alkali metal and / or alkaline earth metal compound.
- porous carrier is a honeycomb-shaped one having a plurality of cells defined as partition walls and serving as a fluid flow path.
- FIG. 1 is a schematic view showing an example of a honeycomb-shaped porous carrier.
- FIG. 2 is a schematic diagram showing an example of a honeycomb-shaped porous carrier provided with a plugging portion.
- the present inventors when developing a catalyst body of the present invention, firstly, the non-oxide ceramic or Ranaru catalyst support Al force Li metals which is originally the NO x storage catalytic despite difficult reaction, alkali We examined the reason why the catalyst activity decreases more than expected with the use time when metal is supported.
- the catalyst carrier made of non-oxide ceramics does not easily react with alkali metals and the like, but an oxide film is inevitably formed on a part of the surface of the aggregate particles constituting the catalyst carrier. It has been found that the oxide film reacts with an alkali metal to form a low-melting glass. Due to this phenomenon, the alkali metal and the like are incorporated into the low-melting glass, so that the catalyst activity is rapidly reduced.
- an oxide is formed between an oxide film inevitably formed on a part of the surface of aggregate particles and a catalyst layer.
- An oxide film protective layer made of a material that does not form a low-melting glass with an alkali metal or the like is arranged so as to cover at least a part of the film.
- main component means that the component accounts for 50% by mass or more of the total mass of all the components.
- the catalyst body of the present invention comprises: a porous carrier in which a large number of aggregate particles containing a non-oxide ceramic and / or a metal as a main component are mutually connected in a state having a large number of pores; A supported catalyst layer containing a compound of alkali metal and / or alkaline earth metal, wherein the porous carrier is provided on a part of the surface of the aggregate particles.
- the metal alloy having an unavoidably formed oxide film, disposed between the oxide film and the catalyst layer so as to cover at least a part of the oxide film; And / or a catalyst body further comprising an oxide film protective layer made of a material that does not form a low-melting glass with an alkaline earth metal.
- the “porous carrier” referred to in the present invention is a carrier for supporting a catalyst layer, and is composed of a porous body in which a large number of aggregate particles are mutually bonded in a state having a large number of pores. It is.
- the “aggregate particles” constituting the “porous carrier” referred to in the present invention those containing non-oxide ceramics and / or metals as main components are applicable.
- the present invention has an object to suppress the reaction of the oxide film is inevitably formed on a part of the surface of the aggregate particles, an alkali metal or the like and which is carried as the NO x storage catalyst Therefore, it is necessary for the aggregate particles to have such a property that such an oxide film is inevitably formed. Therefore, the “porous carrier” in the present invention is composed of non-oxide ceramic containing silicon element and / or metal silicon as a main component, more specifically, silicon carbide, metal silicon-bonded silicon carbide It is preferable that at least one substance selected from silicon nitride is used as a main component.
- the configuration of the present invention is particularly effective when the main component of the above-mentioned oxide film is silica having high reactivity with an alkali metal or the like. This is because an oxide film containing silica as a main component is inevitably formed on the surface.
- the ⁇ porous carrier '' in the present invention preferably has a porosity of 40 to 90%, more preferably 45 to 80%, and more preferably 50 to 70%. Especially preferred. If the porosity is less than the above range, the pressure loss may be increased when a function as a filter is added to the catalyst body, as described later. It is not preferable in that the required strength may not be obtained.
- the porosity can be controlled by the firing temperature and the composition of the raw materials.
- porous material having a high porosity can be produced by burning out the material during firing to form pores.
- porosity referred to in the present specification is, of course, the porosity before the catalyst layer is supported, and means a value measured by the Archimedes method.
- the shape of the porous carrier is not particularly limited, and may be a pellet, a bead, a ring, a foam, or the like which is usually used as a catalyst carrier.
- a function as a filter it is possible to design the filter characteristics (pressure loss, etc.) with high accuracy. It is preferably a honeycomb shape having the same.
- honeycomb shape in the present invention means that a plurality of cells 3 serving as a fluid flow path are formed by being partitioned by extremely thin partition walls 4 like a porous carrier 1 shown in FIG. Shape.
- the overall shape of the honeycomb is not particularly limited. For example, in addition to the cylindrical shape shown in FIG. Examples of the shape include a columnar shape.
- the honeycomb cell shape (cell shape in a cross section perpendicular to the cell formation direction) is not particularly limited.
- a hexagonal cell, a triangular cell, or the like may be used.
- the shape of the catalyst layer can be given, but by using a circular cell or a polygonal cell having a square shape or more, the thickness of the catalyst at the corners can be reduced in the cell cross section, and the thickness of the catalyst layer can be made uniform. .
- Hexagonal cells are preferred in consideration of cell density, aperture ratio, and the like.
- the cell density of the honeycomb is not particularly limited, but when it is used as a catalyst carrier as in the present invention, the cell density is in the range of 6 to 150 cells Z square inch (0.9-233 cells, cm 2 ). It is preferable that The thickness of the partition walls is preferably in the range of 20 to 200 / xm.
- the catalyst body of the present invention when the porous carrier has a honeycomb shape as described above, the catalyst body further includes a plugging portion for alternately plugging the inlet end face and the outlet end face of the plurality of cells. It is preferred that it is.
- a function as a filter can be added to the catalyst body (catalyst-carrying filter).
- the porous carrier 21 further provided with a sealing portion 22 for alternately sealing C and, when the gas to be treated is introduced into the cell 23 from the inlet side end face B, dust and patitilate are separated from the partition wall 2.
- the porous carrier when the porous carrier has a honeycomb shape as described above, the porous carrier is composed of a plurality of honeycomb segments, and the plurality of honeycomb segments are integrally joined ( (Conjugated body).
- Cordierite which is an oxide ceramic, is representative of the ceramic constituting the porous carrier in the catalyst body and the catalyst-carrying filter, but the non-oxide ceramic constituting the porous carrier in the catalyst body of the present invention is .
- Cordierite which is an oxide ceramic
- the non-oxide ceramic constituting the porous carrier in the catalyst body of the present invention is Compared to cordierite Since the coefficient of thermal expansion is large, thermal stress due to temperature distribution increases. Therefore, by adopting the structure of the bonded body as described above, the thermal stress can be dispersed, and cracks due to the thermal stress can be prevented, and the thermal shock resistance of the catalyst body can be improved.
- the size of each segment lay preferred that the cross-sectional area (cross section perpendicular to cell Le formation direction) is 9 0 0 ⁇ 1 0 0 0 0 mm 2, 9 0 more preferably 0 to a 5 0 0 0 mm 2, 9 0 0 3 particularly preferably 6 a 0 0 mm 2, 7 0 vol% or more of the catalyst body, composed of segments of this size It is preferred that
- the “porous carrier” in the present invention includes, for example, a non-oxide ceramic, an aggregate particle material made of Z or a metal, water, an organic binder (hydroxypropoxymethyl cellulose, methylcellulose, etc.), if desired, a pore-forming agent (Graphite, starch, synthetic resin, etc.), surfactants (ethylene glycol, fatty acid stones, etc.), etc. are mixed and kneaded to form a kneaded clay, and the kneaded clay is formed into a desired shape and dried.
- the molded body can be obtained by calcining the molded body to obtain a calcined body, and then calcining the calcined body.
- a method of forming the porous carrier into a honeycomb or a dog a method of extruding the clay prepared as described above using a die having a desired cell shape, partition wall thickness, and cell density is preferably used. Can be used.
- a honeycomb-shaped porous carrier is formed by extrusion, dried, and then dried. A method of filling the cell opening with a kneaded clay having the same composition as the kneaded clay may be used.
- the “oxide film protective layer” in the present invention is made of a substance that does not form a low-melting glass with an alkali metal and Z or an alkaline earth metal, and covers at least a part of the above-described oxide film. It is formed so that. In a portion where the oxide film protective layer is disposed between a part of the oxide film and the catalyst layer, the above-described oxide film and the catalyst layer are confirmed.
- isolation oxide film and NO x since it is possible to suppress the reaction between the supported alkali metal such as storage catalyst, Al force Li metal ing from non-oxide ceramics such as catalyst support It is possible to effectively prevent the catalyst activity from lowering even when the catalyst is carried.
- the porous carrier is made of a non-oxide ceramic or the like, the constituent material of the porous carrier itself does not react with the alkali metal or the like. Therefore, a configuration in which the entire surface of the porous carrier is covered with the oxide film protective layer is not essential, and is characterized in that it is sufficient to cover at least a part of the oxide film.
- oxide ceramics cordierite, etc.
- the entire surface of the catalyst carrier is coated in some way because the material itself of the catalyst carrier reacts with an alkali metal or the like. A configuration of covering with a layer is required.
- the “substance that does not form a low-melting glass with the Al-Li metal and Z or the Al-earth metal” according to the present invention includes, specifically, at least one selected from the elements belonging to Group A below.
- the elements belonging to Group A include compounds species of elements, in forming the oxide film protective layer, oxide colloidal particles microparticles such as (Jirukonia (Z r 0 2) sol, titania (T I_ ⁇ 2) zo le, etc.)
- oxide colloidal particles microparticles such as (Jirukonia (Z r 0 2) sol, titania (T I_ ⁇ 2) zo le, etc.)
- the elements belonging to the following group A those which are compounds of at least one element selected from zirconium and titanium are preferable in that they are relatively easy to use (for example, zirconia, titania, etc.).
- Group A scandium, titanium, vanadium, chromium, manganese, iron, cobalt, nickel, copper, zinc, gallium, germanium, yttrium, zirconium, niobium, molybdenum, tin, and antimony
- the phrase “does not form a low-melting glass with an alkali metal and / or alkaline earth metal” in the present invention is more specifically described as follows: an alkali metal and an oxide of Z or an alkaline earth metal; A substance that does not form a low-melting glass with lithium metal and / or alkaline earth metal ”, which means that the eutectic point of silica is 800 ° C. or more.
- the reason why the eutectic point is 800 ° C or more is to take into account the temperature conditions of the environment where the catalyst is actually installed (exhaust gas system of automobiles). If the eutectic point is 800 ° C. or higher, it is considered that the oxide film protective layer does not substantially react with the alkali metal and the like. Therefore, the reaction between the oxide film and an alkali metal or the like can be suppressed, and a decrease in catalytic activity can be effectively prevented.
- the method for forming the oxide film protective layer is not particularly limited.
- a coating containing “a substance that does not form a low-melting glass with an alkali metal and / or an alkaline earth metal” on the porous carrier is used.
- a method of baking by heat treatment at a high temperature may be used.
- the “catalyst layer” in the present invention is a layer containing a compound of an alkali metal and / or an alkaline earth metal, which is a NO x storage catalyst, and is supported on a porous carrier.
- the types of the alkali metal and the alkaline earth metal supported as the NO x storage catalyst are not particularly limited.
- the metal include calcium, barium, and strontium.
- potassium is particularly suitable because it has excellent NO x storage ability in a high temperature range.
- the catalyst layer according to the present invention contains at least one compound of a noble metal element selected from platinum, palladium, and rhodium in addition to the above-mentioned alkali metal and the compound of Z or alkaline earth metal.
- a noble metal element selected from platinum, palladium, and rhodium in addition to the above-mentioned alkali metal and the compound of Z or alkaline earth metal.
- These noble metals or by reacting the nitrogen monoxide in the exhaust gas (NO) and oxygen (0 2) to generate nitrogen dioxide (N 0 2) prior to ⁇ alkali metal or the like occludes nitrogen oxides
- the nitrogen oxides can be made harmless by reacting them with the combustible components in the exhaust gas, thereby improving the purification ability of the nitrogen oxides. Is preferred.
- the catalyst components such as alkali metals and noble metals in a highly dispersed state
- it is preferable that the catalyst components are once supported on a heat-resistant inorganic oxide having a large specific surface area, such as alumina, and then supported on a porous carrier. .
- the catalyst body of the present invention comprises a catalyst component other than the NO x storage catalyst represented by a three-way catalyst, a co-catalyst represented by cerium (C e) and / or zirconium oxide, and HC (Hydro Carbon) adsorption wood or the like, other purification material to be applied to an exhaust gas system may be one that is both supported and the NO x storage catalyst.
- the NO x storage catalyst and these it is more preferable that the components are stacked and supported so that each component becomes an independent layer.
- the NO x storage catalytic Toko these of cleansing material is supported on a separate carrier, it is also preferable to use in appropriate combination of these within the exhaust system.
- the method for forming the catalyst layer is not particularly limited, but examples include a method in which a catalyst solution containing a catalyst component is wash-coated on the porous carrier on which the oxide film protective layer has been formed, followed by heat treatment at a high temperature and baking. .
- the average particle size of the aggregate particle material in the following Examples and Comparative Examples was measured by the X-ray transmission method using the Stokes liquid phase sedimentation method as the measurement principle.
- Measuring device for example, manufactured by Shimadzu Corporation
- aggregate particles a total of 100 parts by mass of 80 parts by mass of silicon carbide powder having an average particle size of 50 m and 20 parts by mass of metal silicon powder having an average particle size of 5 m was prepared. Then, 100 parts by mass of hydroxypropyl methylcellulose as an organic binder, 10 parts by mass of starch as a pore-forming agent, and an appropriate amount of water were added to 100 parts by mass of the aggregate particles, and a vacuum was added. The mixture was mixed by a kneading machine and kneaded to prepare a kneaded clay.
- the above clay is extruded using a die having a cell shape, a partition wall thickness, and a cell density described below, and then formed into a honeycomb shape, and then dried by a drying method combining hot air drying and microwave drying.
- a honeycomb formed body was obtained.
- the overall shape of the obtained molded body is a square having an end face (cell opening face) of 35 mm X 35 mm, a length of 152 mm, and a cell shape of 1.2 mm X 1.2 mm.
- Square cell, the partition wall thickness was 3 10 rn, the cell density was 46.5 cells / cm 2 (300 cells Z square inch), and the total number of cells was 57 6 cells. .
- the above compact was calcined (degreased) in an air atmosphere at about 400 ° C for 5 hours.
- a calcined body was obtained, and the calcined body was calcined at about 150 ° C. for 2 hours in an argon atmosphere to obtain a porous carrier (metal silicon-bonded silicon carbide).
- This porous support had a porosity of 52% as measured by the Archimedes method and an average pore diameter of 20 m as measured by the mercury intrusion method.
- This porous carrier is referred to as “carrier 1”. (Carrier 2)
- aggregate particles 100 parts by mass of metal silicon powder having an average particle diameter of 20 m was prepared. Then, 100 parts by mass of hydroxypropyl methylcellulose as an organic binder, 10 parts by mass of starch as a pore-forming agent, and an appropriate amount of water were added to 100 parts by mass of the aggregate particles. The mixture was kneaded with a kneader and kneaded to prepare a clay.
- the above clay is extruded using a die having a cell shape, a partition wall thickness, and a cell density described below, and then formed into a honeycomb shape, and then dried by a drying method combining hot air drying and microwave drying. Thus, a honeycomb formed body was obtained.
- the overall shape of the obtained molded body is a square cell with an end surface (cell opening surface) of 35 mm x 35 mm and a length of 152 mm, and a cell shape of 1.2 mm x 1.2 mm
- the thickness of the partition wall was 3 10 ⁇
- the cell density was 46.5 cells / cm 2 (300 cell square inches)
- the total number of cells was 576 cells.
- the molded body is calcined (degreased) in an air atmosphere at about 400 ° C. for 5 hours to obtain a calcined body.
- the calcined body is heated in a nitrogen atmosphere at about 1450 ° C. for 2 hours.
- a porous carrier was obtained (silicon nitride).
- This porous carrier had a porosity of 52% as measured by the Archimedes method and an average pore diameter of 10 / im as measured by the mercury intrusion method.
- This porous carrier is referred to as “carrier 2”.
- An oxide film protective layer was formed so as to cover at least a part of the oxide film.
- the coating amount was defined by the mass per unit volume of the porous carrier, and was any of 5 g / L, 25 g / L, and 50 g / L. When the coat amount did not reach the predetermined value in one wash coat, the wash coat was repeated until the coat amount reached the predetermined value. Then heat at 700 ° C for 1 hour Burning was performed by performing the treatment.
- the amount of potassium supported was adjusted to be 20 gZL per volume of the porous carrier.
- the relationship between the amount of alumina and platinum and potassium is as follows: at the stage where the catalyst solution is wet-coated on a porous carrier serving as a catalyst carrier and finally subjected to heat treatment, the supporting amount of the power rim is 20 g / L (porous material). (Per carrier volume), the platinum was adjusted to be 30 gZc ft (1.06 g / L) (mass based on platinum element per porous carrier volume).
- the amount of alumina sol added was such that the solid content was 5% by mass of the total alumina in terms of alumina, and the water was added as appropriate so that the catalyst solution had a viscosity that facilitated wet coating.
- a porous carrier serving as a catalyst carrier was immersed in the obtained catalyst solution, and excess liquid in the cell was blown off, followed by drying.
- the obtained potassium support was heat-treated in an electric furnace at 600 ° C. for 1 hour to prepare a catalyst.
- Comparative Example 1 was obtained by forming the catalyst layer without forming the oxide film protective layer on the carrier 1
- Comparative Example was obtained by forming the catalyst layer without forming the oxide film protective layer on the carrier 2.
- the catalyst body of the present invention comprises an oxide film and a catalyst layer which are inevitably formed on a part of the surface of aggregate particles in a porous carrier mainly composed of a non-oxide ceramic or the like.
- An oxide film protective layer made of a substance that does not form a low-melting glass with an alkali metal or the like so as to cover at least a part of the oxide film. Since was, when the catalyst carrier made of non-oxide ceramics was supported alkali metal such as a N 0 x storage catalyst, it is possible to effectively prevent a reduction in catalytic activity.
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Abstract
Description
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AU2003284415A AU2003284415A1 (en) | 2002-11-22 | 2003-11-19 | Catalytic article |
EP03775839A EP1566214B1 (en) | 2002-11-22 | 2003-11-19 | Catalyst body |
US10/535,702 US7348289B2 (en) | 2002-11-22 | 2003-11-19 | Catalyst body |
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JP2002338745A JP4567285B2 (ja) | 2002-11-22 | 2002-11-22 | 排ガス浄化用触媒体 |
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EP (1) | EP1566214B1 (ja) |
JP (1) | JP4567285B2 (ja) |
KR (1) | KR100767247B1 (ja) |
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- 2003-11-19 EP EP03775839A patent/EP1566214B1/en not_active Expired - Lifetime
- 2003-11-19 AU AU2003284415A patent/AU2003284415A1/en not_active Abandoned
- 2003-11-19 WO PCT/JP2003/014725 patent/WO2004047984A1/ja active Application Filing
- 2003-11-19 PL PL376377A patent/PL216209B1/pl unknown
- 2003-11-19 US US10/535,702 patent/US7348289B2/en not_active Expired - Lifetime
- 2003-11-19 KR KR1020057009239A patent/KR100767247B1/ko not_active IP Right Cessation
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Also Published As
Publication number | Publication date |
---|---|
EP1566214B1 (en) | 2013-02-27 |
EP1566214A1 (en) | 2005-08-24 |
PL216209B1 (pl) | 2014-03-31 |
KR20050085113A (ko) | 2005-08-29 |
JP2004167440A (ja) | 2004-06-17 |
US20060014636A1 (en) | 2006-01-19 |
PL376377A1 (en) | 2005-12-27 |
JP4567285B2 (ja) | 2010-10-20 |
AU2003284415A1 (en) | 2004-06-18 |
KR100767247B1 (ko) | 2007-10-17 |
EP1566214A4 (en) | 2009-08-26 |
US7348289B2 (en) | 2008-03-25 |
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