EP2635372A1 - CATALYSEUR D'OXYDATION DE L'AMMONIAC AVEC UNE FAIBLE FORMATION DE SOUS-PRODUIT N2O& xA; - Google Patents
CATALYSEUR D'OXYDATION DE L'AMMONIAC AVEC UNE FAIBLE FORMATION DE SOUS-PRODUIT N2O& xA;Info
- Publication number
- EP2635372A1 EP2635372A1 EP11779617.7A EP11779617A EP2635372A1 EP 2635372 A1 EP2635372 A1 EP 2635372A1 EP 11779617 A EP11779617 A EP 11779617A EP 2635372 A1 EP2635372 A1 EP 2635372A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- catalyst
- catalytic composition
- mixed oxide
- platinum
- scr
- 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.)
- Withdrawn
Links
- 239000003054 catalyst Substances 0.000 title claims abstract description 91
- 238000007254 oxidation reaction Methods 0.000 title claims abstract description 29
- 230000003647 oxidation Effects 0.000 title claims abstract description 28
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 title claims description 76
- 229910021529 ammonia Inorganic materials 0.000 title claims description 38
- 230000015572 biosynthetic process Effects 0.000 title description 4
- 239000006227 byproduct Substances 0.000 title description 4
- 230000003197 catalytic effect Effects 0.000 claims abstract description 37
- 239000000203 mixture Substances 0.000 claims abstract description 37
- 229910000510 noble metal Inorganic materials 0.000 claims abstract description 21
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 claims abstract description 19
- 229910052721 tungsten Inorganic materials 0.000 claims abstract description 19
- 239000010937 tungsten Substances 0.000 claims abstract description 18
- 238000000465 moulding Methods 0.000 claims abstract description 5
- 239000002253 acid Substances 0.000 claims abstract description 4
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 claims description 82
- 229910052697 platinum Inorganic materials 0.000 claims description 36
- 150000001875 compounds Chemical class 0.000 claims description 18
- 230000002378 acidificating effect Effects 0.000 claims description 13
- 239000011248 coating agent Substances 0.000 claims description 12
- 238000000576 coating method Methods 0.000 claims description 12
- 238000000034 method Methods 0.000 claims description 11
- 239000002243 precursor Substances 0.000 claims description 11
- 238000001354 calcination Methods 0.000 claims description 7
- 239000000919 ceramic Substances 0.000 claims description 7
- 239000011230 binding agent Substances 0.000 claims description 6
- 238000002360 preparation method Methods 0.000 claims description 5
- 230000008569 process Effects 0.000 claims description 2
- 239000002904 solvent Substances 0.000 claims description 2
- 239000002131 composite material Substances 0.000 claims 2
- 238000004519 manufacturing process Methods 0.000 abstract 1
- 239000000758 substrate Substances 0.000 abstract 1
- 241000264877 Hippospongia communis Species 0.000 description 30
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 14
- 238000006243 chemical reaction Methods 0.000 description 12
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 12
- 230000000052 comparative effect Effects 0.000 description 11
- 239000010936 titanium Substances 0.000 description 10
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 8
- 238000010521 absorption reaction Methods 0.000 description 8
- 239000010457 zeolite Substances 0.000 description 8
- HLMXWUYOTWZKHB-UHFFFAOYSA-N 2-aminoethanol;platinum Chemical compound [Pt].NCCO HLMXWUYOTWZKHB-UHFFFAOYSA-N 0.000 description 6
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 6
- GQPLMRYTRLFLPF-UHFFFAOYSA-N Nitrous Oxide Chemical compound [O-][N+]#N GQPLMRYTRLFLPF-UHFFFAOYSA-N 0.000 description 6
- 229910021536 Zeolite Inorganic materials 0.000 description 6
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 6
- 239000007789 gas Substances 0.000 description 6
- 239000010970 precious metal Substances 0.000 description 6
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 description 5
- 239000004202 carbamide Substances 0.000 description 5
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 238000005470 impregnation Methods 0.000 description 4
- 229910052757 nitrogen Inorganic materials 0.000 description 4
- 230000009467 reduction Effects 0.000 description 4
- 238000006722 reduction reaction Methods 0.000 description 4
- 230000004888 barrier function Effects 0.000 description 3
- 239000006185 dispersion Substances 0.000 description 3
- 239000001272 nitrous oxide Substances 0.000 description 3
- 239000004408 titanium dioxide Substances 0.000 description 3
- HZAXFHJVJLSVMW-UHFFFAOYSA-N 2-Aminoethan-1-ol Chemical compound NCCO HZAXFHJVJLSVMW-UHFFFAOYSA-N 0.000 description 2
- ZXVOCOLRQJZVBW-UHFFFAOYSA-N azane;ethanol Chemical compound N.CCO ZXVOCOLRQJZVBW-UHFFFAOYSA-N 0.000 description 2
- 239000000969 carrier Substances 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- RMAQACBXLXPBSY-UHFFFAOYSA-N silicic acid Chemical compound O[Si](O)(O)O RMAQACBXLXPBSY-UHFFFAOYSA-N 0.000 description 2
- 238000011144 upstream manufacturing Methods 0.000 description 2
- 229910052720 vanadium Inorganic materials 0.000 description 2
- 238000010792 warming Methods 0.000 description 2
- VEHXKUNAGOJDJB-UHFFFAOYSA-N (4-formyl-2-methoxyphenyl) 4-methoxybenzoate Chemical compound C1=CC(OC)=CC=C1C(=O)OC1=CC=C(C=O)C=C1OC VEHXKUNAGOJDJB-UHFFFAOYSA-N 0.000 description 1
- 229910018125 Al-Si Inorganic materials 0.000 description 1
- 229910018520 Al—Si Inorganic materials 0.000 description 1
- 229910002651 NO3 Inorganic materials 0.000 description 1
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 1
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- 229910010413 TiO 2 Inorganic materials 0.000 description 1
- SWNSCEABTVLBDE-UHFFFAOYSA-M [Pt]O.CC(O)CN Chemical compound [Pt]O.CC(O)CN SWNSCEABTVLBDE-UHFFFAOYSA-M 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 239000011149 active material Substances 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- LSQZJLSUYDQPKJ-NJBDSQKTSA-N amoxicillin Chemical compound C1([C@@H](N)C(=O)N[C@H]2[C@H]3SC([C@@H](N3C2=O)C(O)=O)(C)C)=CC=C(O)C=C1 LSQZJLSUYDQPKJ-NJBDSQKTSA-N 0.000 description 1
- KHCPSOMSJYAQSY-UHFFFAOYSA-L azane;dichloroplatinum Chemical compound N.N.N.N.Cl[Pt]Cl KHCPSOMSJYAQSY-UHFFFAOYSA-L 0.000 description 1
- NOWPEMKUZKNSGG-UHFFFAOYSA-N azane;platinum(2+) Chemical compound N.N.N.N.[Pt+2] NOWPEMKUZKNSGG-UHFFFAOYSA-N 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 238000010531 catalytic reduction reaction Methods 0.000 description 1
- 239000008119 colloidal silica Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 229910052878 cordierite Inorganic materials 0.000 description 1
- 239000008367 deionised water Substances 0.000 description 1
- 229910021641 deionized water Inorganic materials 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 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 1
- 238000007598 dipping method Methods 0.000 description 1
- LMABILRJNNFCPG-UHFFFAOYSA-L ethane-1,2-diamine;platinum(2+);dichloride Chemical compound [Cl-].[Cl-].[Pt+2].NCCN LMABILRJNNFCPG-UHFFFAOYSA-L 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 239000005431 greenhouse gas Substances 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000006262 metallic foam Substances 0.000 description 1
- 229910052680 mordenite Inorganic materials 0.000 description 1
- 229910017604 nitric acid Inorganic materials 0.000 description 1
- 239000004014 plasticizer Substances 0.000 description 1
- 150000003058 platinum compounds Chemical class 0.000 description 1
- NWAHZABTSDUXMJ-UHFFFAOYSA-N platinum(2+);dinitrate Chemical compound [Pt+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O NWAHZABTSDUXMJ-UHFFFAOYSA-N 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 239000012694 precious metal precursor Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 description 1
- 238000004627 transmission electron microscopy Methods 0.000 description 1
- 150000003658 tungsten compounds Chemical class 0.000 description 1
- CMPGARWFYBADJI-UHFFFAOYSA-L tungstic acid Chemical compound O[W](O)(=O)=O CMPGARWFYBADJI-UHFFFAOYSA-L 0.000 description 1
- GPPXJZIENCGNKB-UHFFFAOYSA-N vanadium Chemical compound [V]#[V] GPPXJZIENCGNKB-UHFFFAOYSA-N 0.000 description 1
Classifications
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- 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
- B01D53/9404—Removing only nitrogen compounds
- B01D53/9409—Nitrogen oxides
- B01D53/9413—Processes characterised by a specific catalyst
-
- 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
- B01D53/9404—Removing only nitrogen compounds
-
- 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
- B01J23/002—Mixed oxides other than spinels, e.g. perovskite
-
- 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
- B01J23/64—Platinum group metals with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/652—Chromium, molybdenum or tungsten
- B01J23/6527—Tungsten
-
- 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
-
- 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
- B01J37/0201—Impregnation
-
- 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
- B01J37/0201—Impregnation
- B01J37/0205—Impregnation in several steps
-
- 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
- B01J37/0215—Coating
- B01J37/0228—Coating in several steps
-
- 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
- B01J37/0242—Coating followed by impregnation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2255/00—Catalysts
- B01D2255/10—Noble metals or compounds thereof
- B01D2255/102—Platinum group metals
- B01D2255/1021—Platinum
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2255/00—Catalysts
- B01D2255/20—Metals or compounds thereof
- B01D2255/207—Transition metals
- B01D2255/20776—Tungsten
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2255/00—Catalysts
- B01D2255/40—Mixed oxides
- B01D2255/407—Zr-Ce mixed oxides
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/40—Nitrogen compounds
- B01D2257/406—Ammonia
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2258/00—Sources of waste gases
- B01D2258/01—Engine exhaust gases
- B01D2258/012—Diesel engines and lean burn gasoline engines
-
- 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
- B01D53/9459—Removing one or more of nitrogen oxides, carbon monoxide, or hydrocarbons by multiple successive catalytic functions; systems with more than one different function, e.g. zone coated catalysts
- B01D53/9477—Removing one or more of nitrogen oxides, carbon monoxide, or hydrocarbons by multiple successive catalytic functions; systems with more than one different function, e.g. zone coated catalysts with catalysts positioned on separate bricks, e.g. exhaust systems
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02C—CAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
- Y02C20/00—Capture or disposal of greenhouse gases
- Y02C20/10—Capture or disposal of greenhouse gases of nitrous oxide (N2O)
Definitions
- the present invention relates to a catalytic
- a composition comprising a noble metal on an acidic tungsten-containing mixed oxide, a process for the preparation of the catalytic composition and the use of the
- the invention is further based on a shaped catalyst body
- SCR selective catalytic reduction
- Urea used for exhaust aftertreatment usually, a urea solution is atomized into the exhaust stream. The urea is hydrolyzed to ammonia and the
- the oxidation of the ammonia proceeds very rapidly and therefore this reaction can be used to prevent the residual emissions of ammonia after the SCR.
- the catalyst has a high selectivity to N 2 and produces little NO, NO 2 and N 2 O (nitrous oxide).
- N 2 O as a by-product is not legally limited, low N 2 O emissions are still important, because N 2 O is one of the greenhouse gases and thus has a climate-damaging effect.
- Nitrous oxide is classified as having a GWP (Global Warming Potential) of 310, which means that the amount of nitrous oxide in the atmosphere is 310 times greater in terms of global warming
- EP 410440 Bl discloses a V / W / Ti solid extrudate SCR catalyst which is coated in its exit zone with a noble metal.
- EP 544282 B1 discloses a catalyst comprising a combination of a V / W / Ti catalyst and platinum on a zeolite, or platinum on alumina or platinum on S1O 2 . Here a very low platinum concentration is used. In this document it is shown that a pure Pt / mordenite catalyst without V / W / Ti component (see
- Comparative Example 2 shows a negative NO x conversion, ie ammonia partially oxidized back to NO x , whereas a pure V / W / Ti catalyst has a high ammonia slip. Only the combination of both catalysts shows both a high selectivity to N 2 and a low
- EP 1 399 246 B1 discloses a monolith catalyst having a V / W / Ti based SCR component which is based on its
- VWT-SCR catalytically active material of the reduction catalyst
- the platinum is thus applied directly to the V / W / Ti catalyst and not mixed two catalysts as in EP 544282 Bl.
- Ammonia from exhaust gases wherein the gas is added ammonia and after an SCR the gas is passed over an oxidation catalyst comprising a noble metal and vanadium on a Ti0 2 or A1 2 0 3, Si0 2, Zr0 2, Al-Si oxide, MgO, Hf0 2 or La 2 0 3 support includes. This is therefore also a
- Component with activity to form nitrogen oxides from ammonia for example via a noble metal.
- acidic tungsten-containing oxides are also suitable for the SCR reaction.
- acidic tungsten-containing oxides are also suitable for the SCR reaction.
- W / Ce / Zr mixed oxides see SAE 2007-01-0238, WO 2009/001131 and US 2010/0034717).
- EP 7597865 also discloses the use of similar acidic Ce / Zr / Ti sulfate catalysts and Ti / Zr / Ce / W-SCR catalysts, respectively, followed by a barrier catalyst comprising platinum on a Si / Al oxide.
- Oxidation catalysts oxidize ammonia to both NO x and N 2 O. These oxidation reactions are very fast.
- the aim of ammonia oxidation in the barrier catalyst is the oxidation to nitrogen.
- the object of the present invention was therefore to provide a catalytic composition which is suitable as an ammonia oxidation catalyst and a particularly high selectivity for the ammonia oxidation
- Composition containing a noble metal on an acidic tungsten-containing mixed oxide has a particularly high selectivity for the ammonia oxidation and only at higher
- this is acidic
- Tungsten-containing mixed oxide preferably a Ce / Zr / W mixed oxide, a Y-stabilized Zr / W mixed oxide (Y / Zr / W mixed oxide) or a Ce / Zr / Ti / W mixed oxide, particularly preferably a Ce / Zr / W
- the mixed oxide preferably has a tungsten content of 5 to 15 wt .-%, more preferably 5.5 to 10 wt .-% and most preferably 6 to 7 wt .-% tungsten, based on the total
- the noble metal is preferably platinum.
- Mixed oxide preferably has 0.05 to 1 wt .-% platinum, more preferably 0.06 to 0.75 wt .-% platinum and most preferably 0.07 to 0.5 wt .-% platinum, based on the total Mixed oxide, on.
- no other precious metal is present in the catalytic composition besides platinum.
- the ratio Ce / Zr in the acidic tungsten-containing mixed oxide is preferably in the range of 80:20 to 50:50, more preferably 60:40 to 70:30, still more preferably 65:35. As a result, a precisely matched acidic character of the mixed oxide is obtained, which contributes to the selectivity increase.
- the invention also provides a method for
- a composition comprising the steps of: a) impregnating an acidic mixed oxide with a
- Tungsten precursor compound Tungsten precursor compound
- step b) impregnating the calcined mixed oxide from step b) with a noble metal precursor compound
- the mixed oxide used for example a Ce / Zr mixed oxide used according to the invention, and also the W mixed oxide produced have preferably a BET surface area of 20-250 m 2 / g, preferably 40-100 m 2 / g, most preferably SOSO m 2 / g.
- the BET surface area is determined according to DIN 66132 (according to the method of Brunauer, Emmet and Teller).
- tungsten precursor compound is in principle any tungsten compound, which converts under the action of temperature in the calcination in the corresponding oxide, preferably ammonium metatungstate (NH 4 ) 6 H 2 Wi 2 0 4 o, ammonium tungstate (NH 4 ) i 9 H 2 (W 2 0 7 ) 6 and tungstic acid H 2 W0 4 .
- ammonium metatungstate NH 4 ) 6 H 2 Wi 2 0 4 o
- ammonium tungstate NH 4 ) i 9 H 2 (W 2 0 7 ) 6
- tungstic acid H 2 W0 4 is particularly preferred as the tungsten precursor compound.
- ammonium metatungstate ammonium metatungstate
- Tungsten precursor compound is a whisker, preferably at a temperature of 400 to 800 ° C, more preferably 500 to 600 ° C, most preferably at about
- Mixed oxide which is preferably a ternary mixed oxide.
- Impregnation is preferably by the incipient wetness method, but other methods, e.g. Dipping,
- Spray method and the like can be used.
- Suitable noble metal precursor compounds are, for example, ethanolammonium hexahydroxoplatinate, hexachloroplatinic acid, tetrachloroplatinic acid, diaminedinitroplatinate (II),
- Methylethanolamine platinum (I) hydroxide and platinum nitrate with ethanol ammonium hexahydroxoplatinate being most preferred.
- Calcining step preferably at a temperature between 400 and 800 ° C, more preferably between 500 and 600 ° C, most preferably at about 550 ° C, whereby preferably finely divided noble metal is deposited on the mixed oxide.
- the particle size of the deposited noble metal is preferred
- Determination of particle size can be determined by transmission electron microscopy (TEM).
- Calcination may optionally also take place a drying step, for example at temperatures of 50 to 200 ° C, preferably 80 to 150 ° C.
- Another object of the invention is the use of the catalytic composition, as described above or as prepared by the method described above, as
- Oxidation catalyst in particular as ammonia oxidation catalyst.
- the catalytic composition is preferably used together with an SCR catalyst.
- the SCR catalyst is preferably arranged upstream of the catalytic composition according to the invention in the flow direction.
- the catalytic composition (oxidation catalyst) and the SCR catalyst in a single catalyst component
- the component and the composition according to the invention can be accommodated on separate carriers in two separate components.
- the SCR catalyst may be, for example, an SCR active
- the catalytic composition can become a washcoat
- the washcoat is suitable for producing a coated catalyst shaped body.
- Another object is accordingly a catalyst shaped body containing a carrier and the catalytic composition as described above.
- the catalytic composition is at least partially applied as a coating on the carrier, more preferably, the coating is applied to the entire carrier surface.
- the necessary coating techniques are known to the person skilled in the art.
- the catalytic composition is processed into an aqueous coating dispersion. This dispersion may be added as a binder, for example, silica sol.
- the viscosity of the dispersion can be adjusted by suitable additives, so that it is possible to apply the required coating amount, for example, in a single operation on the walls of flow channels. If this is not possible, then the coating be repeated several times, the freshly applied coating is fixed in each case by an intermediate drying. The finished coating is then dried at elevated temperature and calcined for a period of 1 to 4 hours at temperatures between 300 and 600 ° C.
- the catalytic composition can also be added with the addition of suitable auxiliaries such as inorganic binders (e.g.
- the catalytic composition is preferably in the form of a
- the carrier is thus a metallic or
- ceramic support more preferably a so-called
- the support material is preferably either a ceramic such as cordierite or a metal or alloy (Emitec).
- metallic foams Inco can be used as the carrier.
- the shaped catalyst body is installed in a housing having an inlet and outlet opening for an exhaust gas to be cleaned.
- the invention is therefore also a
- the catalyst component may be part of an exhaust gas purification system, preferably further
- Components such as a particulate filter, a upstream oxidation catalyst, a
- Fig. 1 shows the ammonia conversion of the compound according to the invention in comparison with not inventive
- Ammonia light-off temperature can be determined.
- the invention is based on the example 1 and the
- the honeycombs are all 1 "in diameter and 2" in length.
- Comparative Example 1 becomes a catalyst based on
- Example 3 a catalyst based on Pt is prepared on a V / W / Ti-SCR catalyst.
- Example 4 describes the comparison test.
- V 25.3 ml coated with 6.425 g washcoat.
- honeycomb Water amount of water absorption are included.
- the honeycomb is then completely immersed in a platinum inethanolamine solution of this concentration for 10 seconds, in this way via "incipient wetness". impregnated.
- the honeycomb is dried and calcined at 550 ° C.
- a washcoat of 20 kg DT 51D titanium dioxide from Milenium and 26 kg titanium dioxide sol (12%, nitric acid stabilized) from Sachtleben as binder are prepared.
- a honeycomb is coated to 32 g / 1 washcoat and calcined at 450 ° C.
- honeycomb Water amount of water absorption are included.
- the honeycomb is then completely immersed in a platinum ethanolamine solution of this concentration for 10 seconds and impregnated in this way by means of incipient wetness, and the honeycomb is dried at 550.degree
- a washcoat of Fe-BEA zeolite is made to which a colloidal silica sol is added as a binder.
- Ceramic honeycomb is coated to 250 g / 1 washcoat and calcined at 550 ° C.
- honeycomb Water amount of water absorption are included.
- the honeycomb is then completely immersed in a platinum ethanolamine solution of this concentration for 10 seconds and impregnated in this way by means of incipient wetness, and the honeycomb is dried at 550.degree
- a washcoat of W stabilized titania DT 52 and 2.5% V 2 O 5 is prepared.
- a ceramic honeycomb is coated to 200 g / 1 washcoat and calcined at 450 ° C.
- honeycomb Water amount of water absorption are included.
- the honeycomb is then completely immersed for 10 s in a platinum ethanolamine solution of this concentration and impregnated in this way via "incipient wetness".
- the honeycomb is dried and at 450 ° C
- the catalysts were tested in a glass tube reactor (internal diameter 27 mm) under the following conditions:
- Catalysts other than the catalyst containing no SCR component (TiO 2 , Comparative Example 1) meet this requirement.
- Ammonia is formed by ammonia oxidation. At low temperature, the reaction is selective, as it dominates the SCR function. As the temperature increases, the oxidation becomes so fast that more ammonia is readily oxidized before it enters the SCR can selectively react with the NO x . The higher this temperature, at which this negative NO x conversion, ie more ammonia oxidation to NO x , takes place, the better is the
- N 2 O Outlet concentration in ppm shown.
- N 2 O is an undesirable by-product. It can be clearly seen that the catalyst according to the invention (squares) only exceeds the 5 ppm N 2 O at 250 ° C., ie N 2 O forms only at a higher temperature and with a maximum of 20 ppm at 300 ° C. the lowest N 2 0 Having formation.
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- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
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Abstract
L'invention concerne une composition catalytique comprenant un métal noble sur un oxyde mixte acide contenant du tungstène, un procédé pour la fabrication de la composition catalytique et l'utilisation de la composition catalytique en tant que catalyseur d'oxydation. La présente invention concerne en outre un corps moulé de catalyseur, qui comprend la composition catalytique sur un support, un washcoat contenant la composition catalytique selon la présente invention et l'utilisation du washcoat pour la fabrication d'un corps moulé de catalyseur revêtu.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE102010050312A DE102010050312A1 (de) | 2010-11-03 | 2010-11-03 | Ammoniak-Oxidationskatalysator mit geringer N2O Nebenproduktbildung |
PCT/EP2011/068976 WO2012059423A1 (fr) | 2010-11-03 | 2011-10-28 | Catalyseur d'oxydation de l'ammoniac avec une faible formation de sous-produit n2o |
Publications (1)
Publication Number | Publication Date |
---|---|
EP2635372A1 true EP2635372A1 (fr) | 2013-09-11 |
Family
ID=44913261
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP11779617.7A Withdrawn EP2635372A1 (fr) | 2010-11-03 | 2011-10-28 | CATALYSEUR D'OXYDATION DE L'AMMONIAC AVEC UNE FAIBLE FORMATION DE SOUS-PRODUIT N2O& xA; |
Country Status (5)
Country | Link |
---|---|
US (1) | US9573097B2 (fr) |
EP (1) | EP2635372A1 (fr) |
CN (1) | CN103459013B (fr) |
DE (1) | DE102010050312A1 (fr) |
WO (1) | WO2012059423A1 (fr) |
Families Citing this family (15)
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JP5732297B2 (ja) * | 2011-03-31 | 2015-06-10 | エヌ・イーケムキャット株式会社 | アンモニア酸化触媒、および排気ガス浄化装置並びに排気ガス浄化方法 |
EP2878359B1 (fr) * | 2013-11-29 | 2016-04-13 | Umicore Ag & Co. Kg | Utilisation d'oxydes mixtes comme composants de stockage d'oxygène |
EP2878368B1 (fr) * | 2013-11-29 | 2019-05-22 | Umicore Ag & Co. Kg | Matériau de stockage de l'oxygène |
US8883102B1 (en) * | 2014-01-14 | 2014-11-11 | Ford Global Technologies, Llc | Methods for controlling nitrous oxide emissions |
SE1550223A1 (sv) | 2014-02-28 | 2015-08-29 | Scania Cv Ab | Avgasbehandlingssystem och förfarande för behandling av en avgasström |
SE539803C2 (en) | 2015-06-05 | 2017-12-05 | Scania Cv Ab | A method and a system for determining a composition of a gas mix in a vehicle |
SE539133C2 (sv) | 2015-08-27 | 2017-04-11 | Scania Cv Ab | Avgasbehandlingssystem och förfarande för behandling av en avgasström |
KR102097094B1 (ko) | 2015-08-27 | 2020-04-03 | 스카니아 씨브이 악티에볼라그 | 배기가스 스트림 처리를 위한 방법 및 배기 처리 시스템 |
SE539131C2 (sv) | 2015-08-27 | 2017-04-11 | Scania Cv Ab | Förfarande och avgasbehandlingssystem för behandling av en avgasström |
SE539130C2 (sv) | 2015-08-27 | 2017-04-11 | Scania Cv Ab | Förfarande och avgasbehandlingssystem för behandling av en avgasström |
SE539134C2 (sv) | 2015-08-27 | 2017-04-11 | Scania Cv Ab | Avgasbehandlingssystem och förfarande för behandling av en avgasström |
SE539129C2 (en) | 2015-08-27 | 2017-04-11 | Scania Cv Ab | Process and system for processing a single stream combustion exhaust stream |
EP3784391A1 (fr) * | 2018-04-23 | 2021-03-03 | BASF Corporation | Catalyseur de réduction catalytique sélective pour le traitement d'un gaz d'échappement d'un moteur diesel |
CN111135827A (zh) * | 2020-01-08 | 2020-05-12 | 中自环保科技股份有限公司 | 一种用于当量燃烧天然气发动机尾气的氨氧化催化剂及其制备方法 |
DE102020207311B4 (de) | 2020-06-11 | 2022-09-08 | Volkswagen Aktiengesellschaft | Ammoniak-Sperrkatalysator, Abgasnachbehandlungssystem und Verfahren zur Abgasnachbehandlung |
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US20100034717A1 (en) * | 2006-10-23 | 2010-02-11 | Katja Adelmann | Vanadium-free catalyst for selective catalytic reduction and process for it's preparation |
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US5120695A (en) | 1989-07-28 | 1992-06-09 | Degusaa Aktiengesellschaft (Degussa Ag) | Catalyst for purifying exhaust gases from internal combustion engines and gas turbines operated at above the stoichiometric ratio |
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US5409681A (en) | 1991-11-27 | 1995-04-25 | Babcock-Hitachi Kabushiki Kaisha | Catalyst for purifying exhaust gas |
CA2103876A1 (fr) | 1992-08-27 | 1994-02-28 | Stuart Leon Soled | Zircone modifiee par un oxyde de tungstene et de la silice renfermant un metal du groupe viii comme catalyseur acide |
AU688351B2 (en) | 1993-07-22 | 1998-03-12 | Mobil Oil Corporation | Modified solid oxide catalyst and process for producing same |
JP4290240B2 (ja) * | 1998-05-27 | 2009-07-01 | ジョンソン・マッセイ・ジャパン・インコーポレイテッド | 排気ガス浄化用触媒および排気ガス浄化方法 |
KR100392943B1 (ko) | 2001-05-16 | 2003-07-28 | (주)케이에이치 케미컬 | 디젤엔진 배기가스의 정화용 촉매 |
EP1264628A1 (fr) | 2001-06-09 | 2002-12-11 | OMG AG & Co. KG | Catalyseur Redox pour la réduction catalytique sélective des oxydes d'azote contenus dans les gaz d'échapement des moteurs Diesel au moyen d'ammoniaque et procédé pour le préparer |
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2011
- 2011-10-28 EP EP11779617.7A patent/EP2635372A1/fr not_active Withdrawn
- 2011-10-28 WO PCT/EP2011/068976 patent/WO2012059423A1/fr active Application Filing
- 2011-10-28 CN CN201180053217.3A patent/CN103459013B/zh not_active Expired - Fee Related
- 2011-10-28 US US13/883,088 patent/US9573097B2/en not_active Expired - Fee Related
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Also Published As
Publication number | Publication date |
---|---|
CN103459013B (zh) | 2016-08-31 |
DE102010050312A1 (de) | 2012-05-03 |
CN103459013A (zh) | 2013-12-18 |
US20130343975A1 (en) | 2013-12-26 |
WO2012059423A1 (fr) | 2012-05-10 |
US9573097B2 (en) | 2017-02-21 |
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