WO2008151823A2 - Catalyseur zéolitique pour la dénitration de gaz d'échappement - Google Patents
Catalyseur zéolitique pour la dénitration de gaz d'échappement Download PDFInfo
- Publication number
- WO2008151823A2 WO2008151823A2 PCT/EP2008/004782 EP2008004782W WO2008151823A2 WO 2008151823 A2 WO2008151823 A2 WO 2008151823A2 EP 2008004782 W EP2008004782 W EP 2008004782W WO 2008151823 A2 WO2008151823 A2 WO 2008151823A2
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- zeolite
- catalyst system
- catalyst
- honeycomb body
- exhaust gases
- Prior art date
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- 239000003054 catalyst Substances 0.000 title claims abstract description 81
- 239000010457 zeolite Substances 0.000 title claims abstract description 55
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 title claims abstract description 39
- 229910021536 Zeolite Inorganic materials 0.000 title claims abstract description 38
- 239000007789 gas Substances 0.000 title claims abstract description 26
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 title 2
- 229910052757 nitrogen Inorganic materials 0.000 title 1
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 claims abstract description 35
- 238000002485 combustion reaction Methods 0.000 claims description 9
- 229910052751 metal Inorganic materials 0.000 claims description 9
- 239000002184 metal Substances 0.000 claims description 9
- 230000003197 catalytic effect Effects 0.000 claims description 7
- 238000004519 manufacturing process Methods 0.000 claims description 7
- 150000002739 metals Chemical class 0.000 claims description 5
- WNLRTRBMVRJNCN-UHFFFAOYSA-N adipic acid Chemical compound OC(=O)CCCCC(O)=O WNLRTRBMVRJNCN-UHFFFAOYSA-N 0.000 claims description 4
- JBKVHLHDHHXQEQ-UHFFFAOYSA-N epsilon-caprolactam Chemical compound O=C1CCCCCN1 JBKVHLHDHHXQEQ-UHFFFAOYSA-N 0.000 claims description 4
- 229910052720 vanadium Inorganic materials 0.000 claims description 3
- 238000004056 waste incineration Methods 0.000 claims description 3
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 claims description 2
- 239000001361 adipic acid Substances 0.000 claims description 2
- 235000011037 adipic acid Nutrition 0.000 claims description 2
- 238000002309 gasification Methods 0.000 claims description 2
- 229910052741 iridium Inorganic materials 0.000 claims description 2
- 229910052742 iron Inorganic materials 0.000 claims description 2
- 229910052759 nickel Inorganic materials 0.000 claims description 2
- 229910017604 nitric acid Inorganic materials 0.000 claims description 2
- 229910052763 palladium Inorganic materials 0.000 claims description 2
- 229910052697 platinum Inorganic materials 0.000 claims description 2
- 229910052703 rhodium Inorganic materials 0.000 claims description 2
- 229910052709 silver Inorganic materials 0.000 claims description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 12
- 238000006243 chemical reaction Methods 0.000 description 11
- GQPLMRYTRLFLPF-UHFFFAOYSA-N Nitrous Oxide Chemical compound [O-][N+]#N GQPLMRYTRLFLPF-UHFFFAOYSA-N 0.000 description 7
- 229910021529 ammonia Inorganic materials 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- 239000011230 binding agent Substances 0.000 description 5
- 150000001768 cations Chemical class 0.000 description 5
- 230000008569 process Effects 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- OWIKHYCFFJSOEH-UHFFFAOYSA-N Isocyanic acid Chemical compound N=C=O OWIKHYCFFJSOEH-UHFFFAOYSA-N 0.000 description 4
- 239000000654 additive Substances 0.000 description 4
- 239000003638 chemical reducing agent Substances 0.000 description 4
- 238000006460 hydrolysis reaction Methods 0.000 description 4
- 239000011148 porous material Substances 0.000 description 4
- 239000000843 powder Substances 0.000 description 4
- 239000010936 titanium Substances 0.000 description 4
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 description 3
- 230000008901 benefit Effects 0.000 description 3
- 239000004202 carbamide Substances 0.000 description 3
- 239000000919 ceramic Substances 0.000 description 3
- 238000000576 coating method Methods 0.000 description 3
- 238000001125 extrusion Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 238000000465 moulding Methods 0.000 description 3
- 239000001272 nitrous oxide Substances 0.000 description 3
- 238000002360 preparation method Methods 0.000 description 3
- 239000012495 reaction gas Substances 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 238000001321 HNCO Methods 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 230000000996 additive effect Effects 0.000 description 2
- 229910052782 aluminium Inorganic materials 0.000 description 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical group [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 2
- XLJMAIOERFSOGZ-UHFFFAOYSA-N anhydrous cyanic acid Natural products OC#N XLJMAIOERFSOGZ-UHFFFAOYSA-N 0.000 description 2
- 239000012876 carrier material Substances 0.000 description 2
- 238000010531 catalytic reduction reaction Methods 0.000 description 2
- 239000011248 coating agent Substances 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 239000000945 filler Substances 0.000 description 2
- 238000010304 firing Methods 0.000 description 2
- 230000007062 hydrolysis Effects 0.000 description 2
- 239000002243 precursor Substances 0.000 description 2
- 239000000725 suspension Substances 0.000 description 2
- 238000001149 thermolysis Methods 0.000 description 2
- 229910017090 AlO 2 Inorganic materials 0.000 description 1
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- 229910004298 SiO 2 Inorganic materials 0.000 description 1
- 229910004283 SiO 4 Inorganic materials 0.000 description 1
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- GWFXMCXJFOEMNQ-UHFFFAOYSA-N [O].O=[N] Chemical class [O].O=[N] GWFXMCXJFOEMNQ-UHFFFAOYSA-N 0.000 description 1
- 238000003916 acid precipitation Methods 0.000 description 1
- -1 aluminum silicates Chemical class 0.000 description 1
- 150000001450 anions Chemical class 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229910001593 boehmite Inorganic materials 0.000 description 1
- 238000001354 calcination Methods 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 229910010293 ceramic material Inorganic materials 0.000 description 1
- 229910017052 cobalt Inorganic materials 0.000 description 1
- 239000010941 cobalt Substances 0.000 description 1
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 229910052878 cordierite Inorganic materials 0.000 description 1
- 239000013078 crystal Substances 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
- 229910001882 dioxygen Inorganic materials 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 230000001747 exhibiting effect Effects 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- FAHBNUUHRFUEAI-UHFFFAOYSA-M hydroxidooxidoaluminium Chemical compound O[Al]=O FAHBNUUHRFUEAI-UHFFFAOYSA-M 0.000 description 1
- 238000010348 incorporation Methods 0.000 description 1
- 229910001387 inorganic aluminate Inorganic materials 0.000 description 1
- 229910010272 inorganic material Inorganic materials 0.000 description 1
- 239000011147 inorganic material Substances 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 229910052909 inorganic silicate Inorganic materials 0.000 description 1
- 238000003780 insertion Methods 0.000 description 1
- 230000037431 insertion Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 231100000956 nontoxicity Toxicity 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 125000004430 oxygen atom Chemical group O* 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000006722 reduction reaction Methods 0.000 description 1
- 238000007493 shaping process Methods 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
- 230000001960 triggered effect Effects 0.000 description 1
- 230000007306 turnover Effects 0.000 description 1
- LEONUFNNVUYDNQ-UHFFFAOYSA-N vanadium atom Chemical compound [V] LEONUFNNVUYDNQ-UHFFFAOYSA-N 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
- B01D53/8621—Removing nitrogen compounds
- B01D53/8625—Nitrogen oxides
- B01D53/8628—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
- 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
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J29/00—Catalysts comprising molecular sieves
- B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
- B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds 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
- B01J29/00—Catalysts comprising molecular sieves
- B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
- B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
- B01J29/064—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof containing iron group metals, noble metals or copper
-
- 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
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G70/00—Working-up undefined normally gaseous mixtures obtained by processes covered by groups C10G9/00, C10G11/00, C10G15/00, C10G47/00, C10G51/00
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2255/00—Catalysts
- B01D2255/50—Zeolites
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2255/00—Catalysts
- B01D2255/90—Physical characteristics of catalysts
- B01D2255/92—Dimensions
- B01D2255/9202—Linear dimensions
-
- 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
- B01J2229/00—Aspects of molecular sieve catalysts not covered by B01J29/00
- B01J2229/30—After treatment, characterised by the means used
- B01J2229/42—Addition of matrix or binder particles
Definitions
- the present invention relates to a DeNOx catalyst system for treating nitrogen oxides-containing exhaust gases comprising a bulk catalyst of a zeolite, wherein the bulk catalyst is an extrudate in the geometry of a honeycomb body.
- Nitrogen oxides that are produced during combustion processes are among the main causes of acid rain and the associated environmental damage, and are the cause of the so-called summer smog, which leads to damage to health. Their emission should be prevented by removing them from the exhaust gases before they are released to the environment.
- Sources of nitrogen oxide emissions into the environment are mainly motor vehicle traffic and incinerators, in particular power plants with furnaces or stationary internal combustion engines and waste incineration plants.
- a reduction in NO x emissions can, for. B. in automotive engines by engine-side settings or power plants with boiler firing by using very pure fuels or by optimizing the combustion systems are achieved, but these firing measures both technical and economic limits set.
- the aim is the most complete removal of NO x and N 2 O with little technical effort by novel catalyst systems.
- the denitrification of exhaust gases is also referred to as DeNOx.
- SCR selective catalytic reduction
- Hydrocarbons (HC-SCR) or ammonia (NH 3 -SCR) or NH 3 precursors such as urea (AdBlue®) are usually used as reducing agents.
- the principle is based on the fact that selected reducing agents selectively reduce nitrogen oxides in the presence of oxygen.
- Selective means that the oxidation of the reducing agent is preferred (selective), which takes place with the oxygen nitrogen oxides and not with the molecular oxygen present in the exhaust much more abundant.
- Ammonia or ammonia precursors have proven themselves as reducing agents with the highest selectivity.
- urea is used in particular because of its non-toxicity, which likewise has very good solubility in water and can therefore simply be added to the exhaust gas as water solution to be metered.
- NH 3 and isocyanic acid are formed in a thermolysis reaction:
- catalysts consist either completely of the catalytically active component, which are what are known as bulk catalysts, which are also known to the person skilled in the art as unsupported catalysts, or the actual active component is applied to a carrier material, then it is referred to as coating catalysts.
- Catalyst systems can be broadly distinguished in powder, shaped body and monolith catalysts, which are optionally coated.
- the shaped-body catalysts mostly consist of ceramic particles or zeolites which are extruded into shaped bodies. Typical dimensions are here z.
- B cylindrical moldings of 1.5 to 2.5 mm in diameter and 1.0 to 5.0 mm in length.
- the ceramic materials are often alumina or silica.
- These catalysts are mostly used in fixed bed reactors. Important parameters of fixed bed reactors are, in addition to the catalytic activity, the bulk density, the pressure loss properties and the surface of the catalyst. Furthermore, the design effort that is necessary for the preparation of the catalyst, an important economic parameter.
- a honeycomb body is produced, which is optionally coated with a so-called washcoat.
- the main body consists in this case mostly of a mineral ceramic, e.g. Cordierite, or a metal.
- the washcoat is a powder suspension which i.a. Contains ceramic powder to obtain a large surface area. This powder suspension is applied to the honeycomb, dried and then impregnated with an active component and then activated by calcination.
- Important parameters here, in addition to the catalytic activity, are the cell density, i. the number of channels per inflow unit and pressure loss at the catalyst. Other parameters are the surface of the catalyst and the design effort for the preparation of the catalyst.
- the catalytically active component consists of the oxides of vanadium or titanium (V / Ti oxides), in a zeolite system.
- V / Ti oxides vanadium or titanium
- metal-exchanged zeolites also called metal-doped zeolites
- SCR catalysts metal-exchanged zeolites
- metal-doped zeolites have proven to be active SCR catalysts employable over a wide temperature range. They are mostly non-toxic and produce less N 2 O and SO 3 than the usual catalysts based on V 2 Os.
- Both catalyst systems d. H.
- the system based on zeolites and that based on V / Ti oxides are characterized in practice by, among other things, different catalyst geometries.
- the catalyst packages are made from cylindrical extrudates.
- honeycomb extrudates of various dimensions are typically used in which the channels have a square footprint.
- Cylindrical extrudates are commonly used in fixed bed reactors with one or more catalyst beds.
- Fixed bed reactors are characterized by a low geometric surface and because of the high flow resistance by a high pressure drop and by low design effort.
- Honeycomb catalysts are commonly used in so-called frame reactors.
- Frame reactors are characterized by a high surface area, by low pressure loss and by a high design effort in the production.
- the object of the present invention was to provide a zeolite-based catalyst system for removing nitrogen oxides and nitrous oxide from an exhaust gas stream having a high surface area and exhibiting a low pressure drop, wherein the catalyst system is to be produced with a low design cost.
- the object is achieved by a catalyst system for the treatment of nitrogen oxides-containing exhaust gases, which comprises a mass catalyst of a zeolite, wherein the mass catalyst is an extrudate which assumes the geometry of a honeycomb body and wherein the weight fraction of zeolite in the extrusion mass of the extrudate between 20 and 95%, preferably between 30 and 60%, and the zeolite is a catalytically active zeolite.
- a honeycomb body is to be understood as meaning a shaped body which has parallel channels which are separated from one another by walls.
- the channels may have an arbitrary polygonal base, e.g. a square, rectangular or hexagonal. Particularly preferred are rectangular base areas, as these simplify the production process and allow a space-saving arrangement of individual moldings in frame reactors. With the base of the channels, the area is meant, which is flowed through vertically.
- the zeolite mass catalyst is characterized by a higher specific catalyst mass in the reaction space, by a significantly lower loss of catalytic activity due to attrition of the catalyst surface, as in the case of coating catalysts the case would be, and by a significantly simplified manufacturing process.
- the reactors with catalyst system according to the invention have the advantage that the pressure loss, ie the pressure difference between the reaction gas at the reactor outlet and at the reactor inlet, is significantly lower is. Furthermore, the catalyst system according to the invention is characterized by an increased geometric surface on the reaction gas side, by less "fouling" of the reactor on the reaction gas side and by improved process gas flow.
- the monolithic catalysts are additionally characterized by greatly reduced dust formation and thus triggered catalyst losses during loading and unloading of the reactor as well as the possibility of replacing parts of the catalyst bed in the operating time of the catalyst.
- zeolite in the context of the present invention as defined by the International Mineralogical Association (D.S. Coombs et al., Can. Mineralogist, 35, 1997, 1571) is a crystalline substance from the group of aluminum silicates with a spatial network structure of the general formula
- the zeolite structure contains cavities and channels characteristic of each zeolite.
- the zeolites are classified according to their topology into different structures (see above). Splits.
- the zeolite framework contains open cavities in the form of channels and cages which are normally occupied by water molecules and extra framework cations that can be exchanged.
- An aluminum atom has an excess negative charge which is compensated by these cations.
- the interior of the pore system represents the catalytically active surface. The more aluminum and the less silicon a zeolite contains, the denser the negative charge in its lattice and the more polar its inner surface.
- the pore size and structure are determined by the Si / Al ratio, which determines most of the catalytic character of a zeolite, in addition to the parameters of preparation (use or type of template, pH, pressure, temperature, presence of seed crystals) ,
- the negative charge is compensated by the incorporation of cations in the pores of the zeolite material.
- the zeolites are mainly distinguished by the geometry of the cavities formed by the rigid network of SiO4 / AlO4 tetrahedra.
- the entrances to the cavities are formed by 8, 10 or 12 "rings" (narrow, medium and large pore zeolites).
- Certain zeolites show a uniform structure structure (eg ZSM-5 with MFI topology) with linear or zigzagging channels, in others close behind the Poreno réelleen larger cavities, z. B. in the Y and A zeolites, with the topologies FAU and LTA.
- any zeolite in particular any 10 and 12 "ring" zeolite, can be used in the context of the present invention.
- the metal content or degree of exchange of a zeolite is significantly determined by the metal species present in the zeolite. This allows the zeolite to be doped with only a single metal or with different metals.
- the preferred metals for exchange and doping are catalytically active metals such as Fe, Ce, Co, Ni, Ag, V, Rh, Pd, Pt, Ir. According to the invention, very particular preference is given to zeolites containing iron or cobalt species.
- ⁇ , ⁇ , and ⁇ positions which are the locations of exchange sites (also referred to as "interchangeable.”
- Reaction accessible especially when using MFI, BEA, FER, MOR, MTW and TRI zeolites.
- the free passage area flowing through the exhaust gas flow flowing perpendicularly is between 20 and 80%, preferably between 60 and 80% and most preferably about 70%.
- This passage area is calculated from the quotient of the area freely flowed through by the exhaust gas flow divided by the inflow surface of the catalyst body.
- the catalyst body is to be understood as the object which arises after extrusion and drying and immediately before insertion into a frame. Too large a passage area would make the catalyst body unstable because the walls would be too narrow and therefore unstable. at Too small a passage area, the pressure loss of the process or combustion gas would be too large over the Formkorper.
- the cell density of the honeycomb body is between 1 and 200 per cm 2 , preferably between 2 and 50 per cm 2 .
- the cell density is calculated from the number of channels per start-up unit.
- the honeycomb body contains a mixture of zeolite, binder, filler and additive.
- the zeolite represents the catalytically active component.
- the proportion by weight of zeolite in the honeycomb body is, as stated above, between 20 and 95%, preferably between 30 and 60%.
- the binder is made of an inorganic material, e.g. Boehmite, which allows the shaping process.
- the weight fraction of the binder is between 5 and 60%, preferably between 20 and 40%.
- the filling material consists of a porous carrier material, e.g. Alumina, with a weight fraction of the honeycomb body of 0 to 40%, preferably between 10 and 30%.
- the additive consists of a material which affects the physical properties of the honeycomb or the mixture of components e.g. a Tixotropiersch with a weight proportion between 0 and 10%. The proportion by weight is calculated from the quotient of the mass of zeolite divided by the total mass of the honeycomb body.
- An extrudable mass is produced by mixing zeolite with water, binders and possibly inert filler material and additives. Binders and additives are chosen so that they influence the properties of the mixture, eg the flow properties, so that the extrusion process and the drying process tion and hardening process during production is made possible.
- the honeycomb body is in the form of a cylinder.
- the honeycomb body has a diameter of 10 to 500 mm, preferably of 200 to 400 mm, and / or a height of 10 to 500 mm, preferably of 200 to 400 mm.
- the height of the honeycomb body is here and below equivalent to the passage of the exhaust gas flow through the honeycomb body.
- the height of the honeycomb body is crucial for the conversion of nitrogen oxides contained in the exhaust gas or nitrous oxide contained in the exhaust gas, since the contact time increases with the height of the honeycomb body , Too small highs mean too little turnover and too high altitudes are on the one hand not economical and on the other hand associated with a higher pressure loss.
- the preferred dimensions of the honeycomb bodies are particularly suitable for the use of the inventive catalyst systems for the treatment of exhaust gases from internal combustion engines.
- the honeycomb body of the catalyst system according to the invention has a cuboid shape.
- the cuboid honeycomb body has a side length of 10 to 500 mm, preferably 50 to 200 mm, and / or a height of 10 to 500 mm, preferably 150 up to 300 mm.
- the advantage of cuboid honeycomb bodies lies in special installation requirements and in a space saving.
- the advantages of the dimensions are the same as the pre ⁇ parts of the dimensions of the cylindrical honeycomb body.
- the catalyst systems according to the invention are used for the catalytic treatment of exhaust gases from combustion or incineration plants as well as plants for the production of nitric acid, adipic acid or caprolactam.
- the catalyst systems of the present invention find use for the catalytic removal of nitrogen oxides from exhaust gases from gasification and combustion processes, e.g. Waste incineration plants or for denitrification of motor vehicle exhaust gases.
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Environmental & Geological Engineering (AREA)
- Materials Engineering (AREA)
- General Chemical & Material Sciences (AREA)
- Biomedical Technology (AREA)
- Crystallography & Structural Chemistry (AREA)
- Analytical Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Combustion & Propulsion (AREA)
- Catalysts (AREA)
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
Abstract
L'invention concerne des systèmes catalytiques alternatifs d'élimination des NOx servant à traiter des gaz d'échappement contenant des oxydes d'azote, le catalyseur comprenant un catalyseur massique composé d'un zéolite et ce catalyseur massique étant un produit d'extrusion présentant une géométrie de corps alvéolaire. L'invention concerne en outre des utilisations du système catalytique selon l'invention.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE102007027676A DE102007027676A1 (de) | 2007-06-15 | 2007-06-15 | Zeolithischer Katalysator zur Entstickung von Abgasen |
DE102007027676.3 | 2007-06-15 |
Publications (2)
Publication Number | Publication Date |
---|---|
WO2008151823A2 true WO2008151823A2 (fr) | 2008-12-18 |
WO2008151823A3 WO2008151823A3 (fr) | 2009-04-30 |
Family
ID=39942829
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/EP2008/004782 WO2008151823A2 (fr) | 2007-06-15 | 2008-06-13 | Catalyseur zéolitique pour la dénitration de gaz d'échappement |
Country Status (2)
Country | Link |
---|---|
DE (1) | DE102007027676A1 (fr) |
WO (1) | WO2008151823A2 (fr) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2020030204A1 (fr) | 2018-08-07 | 2020-02-13 | Vysoká Škola Báňská - Technická Univerzita Ostrava | Procédé de préparation d'un catalyseur pour l'élimination d'oxyde nitreux de gaz industriels usés et catalyseur préparé par ce procédé |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0205813A2 (fr) * | 1985-04-22 | 1986-12-30 | Klaus Rennebeck | Catalyseur, en particulier pour purification de gaz d'échappement, procédé et dispositif pour sa fabrication |
WO1994027709A1 (fr) * | 1993-05-28 | 1994-12-08 | Engelhard Corporation | Catalyseur utilise dans la decomposition de l'oxyde azote |
US6413898B1 (en) * | 1999-12-28 | 2002-07-02 | Corning Incorporated | Zeolite/alumina catalyst support compositions and method of making the same |
EP1852174A1 (fr) * | 2006-05-02 | 2007-11-07 | Argillon GmbH | Catalyseur extrudé massique non-supporté et son procédé de fabrication |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3841990A1 (de) * | 1988-12-14 | 1990-06-21 | Degussa | Verfahren zur reduktion von stickoxiden aus abgasen |
DK0548499T3 (da) * | 1991-11-02 | 1996-02-05 | Degussa | Fremgangsmåde til oxidativ rensning af afgangsgasser, der indeholder nitrogenoxider |
DE19721440A1 (de) * | 1997-05-21 | 1998-11-26 | Degussa | Verfahren zur Reinigung eines mageren Abgases und Katalysatorsystem hierfür |
JP4771639B2 (ja) * | 1999-12-29 | 2011-09-14 | コーニング インコーポレイテッド | 高強度および高表面積の触媒、触媒支持体または吸着体組成物 |
-
2007
- 2007-06-15 DE DE102007027676A patent/DE102007027676A1/de not_active Withdrawn
-
2008
- 2008-06-13 WO PCT/EP2008/004782 patent/WO2008151823A2/fr active Application Filing
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0205813A2 (fr) * | 1985-04-22 | 1986-12-30 | Klaus Rennebeck | Catalyseur, en particulier pour purification de gaz d'échappement, procédé et dispositif pour sa fabrication |
WO1994027709A1 (fr) * | 1993-05-28 | 1994-12-08 | Engelhard Corporation | Catalyseur utilise dans la decomposition de l'oxyde azote |
US6413898B1 (en) * | 1999-12-28 | 2002-07-02 | Corning Incorporated | Zeolite/alumina catalyst support compositions and method of making the same |
EP1852174A1 (fr) * | 2006-05-02 | 2007-11-07 | Argillon GmbH | Catalyseur extrudé massique non-supporté et son procédé de fabrication |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2020030204A1 (fr) | 2018-08-07 | 2020-02-13 | Vysoká Škola Báňská - Technická Univerzita Ostrava | Procédé de préparation d'un catalyseur pour l'élimination d'oxyde nitreux de gaz industriels usés et catalyseur préparé par ce procédé |
Also Published As
Publication number | Publication date |
---|---|
WO2008151823A3 (fr) | 2009-04-30 |
DE102007027676A1 (de) | 2008-12-18 |
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