WO2017153237A1 - Non-woven fibrous material-based honeycomb catalyst - Google Patents

Non-woven fibrous material-based honeycomb catalyst Download PDF

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Publication number
WO2017153237A1
WO2017153237A1 PCT/EP2017/054881 EP2017054881W WO2017153237A1 WO 2017153237 A1 WO2017153237 A1 WO 2017153237A1 EP 2017054881 W EP2017054881 W EP 2017054881W WO 2017153237 A1 WO2017153237 A1 WO 2017153237A1
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WO
WIPO (PCT)
Prior art keywords
honeycomb catalyst
coat
substrate
honeycomb
catalytically active
Prior art date
Application number
PCT/EP2017/054881
Other languages
French (fr)
Inventor
Claus S. JØRGENSEN
Jakob Weiland HØJ
Keld Johansen
Karsten Pedersen
Original Assignee
Haldor Topsøe A/S
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Haldor Topsøe A/S filed Critical Haldor Topsøe A/S
Publication of WO2017153237A1 publication Critical patent/WO2017153237A1/en

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Classifications

    • B01J35/58—
    • 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
    • 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
    • B01D53/9418—Processes characterised by a specific catalyst for removing nitrogen oxides by selective catalytic reduction [SCR] using a reducing agent in a lean exhaust gas
    • 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
    • B01J23/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J23/20—Vanadium, niobium or tantalum
    • B01J23/22—Vanadium
    • 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
    • B01J23/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J23/24—Chromium, molybdenum or tungsten
    • B01J23/28—Molybdenum
    • 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
    • B01J23/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J23/24—Chromium, molybdenum or tungsten
    • B01J23/30—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
    • 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
    • B01J23/40—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group metals
    • B01J23/42—Platinum
    • 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
    • B01J23/40—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group metals
    • B01J23/44—Palladium
    • 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
    • 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
    • B01J35/56—
    • 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
    • B01J37/0215—Coating
    • B01J37/0217—Pretreatment of the substrate before coating
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2251/00—Reactants
    • B01D2251/20—Reductants
    • B01D2251/206—Ammonium compounds
    • B01D2251/2062—Ammonia
    • 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
    • B01D2255/10—Noble metals or compounds thereof
    • B01D2255/102—Platinum group metals
    • B01D2255/1023—Palladium
    • 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
    • B01D2255/20723—Vanadium
    • 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
    • B01D2255/50—Zeolites
    • B01J35/30—
    • 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
    • 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
    • B01J37/0246—Coatings comprising a zeolite

Definitions

  • the present invention relates to a honeycomb shaped cata ⁇ lyst formed of a corrugated substrate composed of a non- woven fibrous material.
  • the invention provides an improved honeycomb shaped catalyst prepared from corrugated sheets of a non- woven fibrous material, preferably provided with a flat liner.
  • a stable honeycomb shaped catalyst can be made of non-woven fibrous material, for instance E-glass fibers as starting material, when coating the material with a first coat layer prior to corrugating and forming the fibrous material into a corrugated sheet.
  • the first coat lay ⁇ er is applied as an aqueous suspension of ceramic material.
  • this invention provides a honeycomb catalyst with a plurality of flow through chan- nels, wherein the honeycomb catalyst comprises a corrugated substrate and optionally a liner applied on the corrugated substrate, the substrate and the optional liner are com- posed of non-woven fibrous material with a first coat of a ceramic material in an amount to result in total weight of the substrate and first coat of between 60-100 g/m 2 and a washcoat layer applied on the first coat, the wash coat contains or is impregnated with one or more catalytically active compounds.
  • the first coat ceramic material comprises preferably tita- nia, silica and/or kaolin.
  • the first coat can be applied on the substrate sheet in form of an aqueous slurry, having a total solid content of 15 - 25 wt%, on one side of the sheet or on both sides of the sheet.
  • the slurry penetrates the sheet.
  • a honeycomb body is formed by stacking up a plurality of the coated and corrugated sheets, or by rolling-up a single coated and corrugated sheet, preferably lined with a flat liner, into a rectangular or cylindrical honeycomb body.
  • the formed honeycomb body has a plurality of par ⁇ allel flow through channels formed by waves of the corru ⁇ gated sheet (s) and the optional liner applied on the corru ⁇ gated sheet ( s ) .
  • the honey ⁇ comb body pre-coated with the first coat is formed by stacking up or rolling up the coated corrugated sheet (s) and the coated liner if present, and is subsequently coated with the washcoat.
  • the washcoat acts as a carrier for the catalytic materials and is used to disperse the materials over a large surface area.
  • Alumina, titania, silica, or mixtures thereof can be used.
  • the washcoat consists of titania.
  • Washcoating of the honeycomb body is usually performed by slurry pickup in the honeycomb body pre-coated with the first coat by pouring the washcoat slurry into the channels of the honeycomb body, or by dipping the body at one side into the washcoat slurry and optionally applying vacuum at the opposite side.
  • the washcoat contains the catalytic active material.
  • the pre-coated and washcoated honey ⁇ comb body is finally impregnated with an aqueous solution containing one or more precursors of the desired catalyti- cally active material, followed by drying and calcination.
  • a honeycomb catalyst according to the invention can be prepared by a method comprising the steps of
  • step e) impregnating the washcoated body with a solution of catalytic active components or precursors thereof, if not contained in the washcoat of step e) ;
  • step (fl) drying and calcining the body of step (el) to obtain the final honeycomb catalyst.
  • Honeycomb catalysts are typically employed in the cleaning of engine exhaust gas.
  • the honeycomb cata ⁇ lyst is shaped as a cylindrical body and canned in a metal housing with a mat between the honeycomb catalyst body and the metallic housing.
  • the cylindrical honeycomb body is radially compressed in order to pro ⁇ vide sufficient friction between the mat and the body and between the mat and the metallic housing.
  • Radially compres- sion typically causes cracks in the coated and calcined body.
  • a further advantage of the first coat provided on the substrate is that the canning process causes a much reduced cracking of the honeycomb body.
  • the canned honeycomb catalyst is as mentioned above typi ⁇ cally used in the catalytically removal of noxious com ⁇ pounds in the exhaust gas, including nitrogen oxides, un- burnt engine fuel and carbon monoxide.
  • the catalytically active com ⁇ pounds of the honeycomb catalyst are active in the removal of noxious compounds in engine exhaust gas.
  • Catalyst compounds active in engine exhaust gas cleaning are per se known in the art.
  • typically em ⁇ ployed catalysts are vanadium oxide, tungsten oxide, palla- dium and platinum, and zeolitic material either used alone or as mixtures thereof.
  • the nitrogen oxides are converted to free nitrogen with a re ⁇ ducing agent, typically ammonia, in the presence of an SCR catalyst by selective, catalytic reduction:
  • Fig. 1 of the drawings is a sectional view of a honeycomb catalyst according to the invention.
  • the substrate 1 of a honeycomb catalyst according to the invention is composed of a corrugated sheet 2 of non-woven fibrous material substrate, optionally provided with a liner (not shown) .
  • Substrate 1 can be rolled-up to a cylindrical body.
  • a first coat layer 3 made of ceramic material is coated on sheet 2.
  • the first coat material can also diffuse through the fibrous material of sheet 2 and forms a first coat lay- er on both sides of sheet 2and within the fibrous material, as shown in Fig.l.
  • a washcoat layer 4 is coated on the first coat layer 3. Washcoat layer 4 contains catalyst par ⁇ ticles 5.

Abstract

A honeycomb catalyst with a plurality of flow through channels, wherein the honeycomb catalyst comprises a corrugated substrate and optionally a liner applied on the corrugated substrate, the substrate and the optional liner are composed of a non-woven fibrous material, such as glass fibres, with a first coat of a ceramic material and a washcoat layer applied on the first coat ceramic material, the washcoat containing one or more catalytically active metals and/or metal oxides, such as vanadium oxide, tunsten oxide, zeolitic material, platinum and/or palladium.

Description

NON-WOVEN FIBROUS MATERIAL-BASED HONEYCOMB CATALYST
The present invention relates to a honeycomb shaped cata¬ lyst formed of a corrugated substrate composed of a non- woven fibrous material.
In particular, the invention provides an improved honeycomb shaped catalyst prepared from corrugated sheets of a non- woven fibrous material, preferably provided with a flat liner.
We have found that a stable honeycomb shaped catalyst can be made of non-woven fibrous material, for instance E-glass fibers as starting material, when coating the material with a first coat layer prior to corrugating and forming the fibrous material into a corrugated sheet. The first coat lay¬ er is applied as an aqueous suspension of ceramic material.
We have additionally found that when the first coat layer is applied on the substrate in an amount resulting in a to¬ tal weight of substrate and coat layer of between 60-100 g/m2 results in an improved stability and stiffness of the paper so that waves formed in the corrugation process sub¬ stantially retain their shape in subsequent forming stages of the final honeycomb catalyst product and operation of the honeycomb catalyst product.
Pursuant to the above finding, this invention provides a honeycomb catalyst with a plurality of flow through chan- nels, wherein the honeycomb catalyst comprises a corrugated substrate and optionally a liner applied on the corrugated substrate, the substrate and the optional liner are com- posed of non-woven fibrous material with a first coat of a ceramic material in an amount to result in total weight of the substrate and first coat of between 60-100 g/m2 and a washcoat layer applied on the first coat, the wash coat contains or is impregnated with one or more catalytically active compounds.
The first coat ceramic material comprises preferably tita- nia, silica and/or kaolin. The first coat can be applied on the substrate sheet in form of an aqueous slurry, having a total solid content of 15 - 25 wt%, on one side of the sheet or on both sides of the sheet.
In both coating methods, the slurry penetrates the sheet.
A honeycomb body is formed by stacking up a plurality of the coated and corrugated sheets, or by rolling-up a single coated and corrugated sheet, preferably lined with a flat liner, into a rectangular or cylindrical honeycomb body. In each case the formed honeycomb body has a plurality of par¬ allel flow through channels formed by waves of the corru¬ gated sheet (s) and the optional liner applied on the corru¬ gated sheet ( s ) . To obtain the final honeycomb catalyst product, the honey¬ comb body pre-coated with the first coat is formed by stacking up or rolling up the coated corrugated sheet (s) and the coated liner if present, and is subsequently coated with the washcoat.
The washcoat acts as a carrier for the catalytic materials and is used to disperse the materials over a large surface area. Alumina, titania, silica, or mixtures thereof can be used. Preferably, the washcoat consists of titania.
Washcoating of the honeycomb body is usually performed by slurry pickup in the honeycomb body pre-coated with the first coat by pouring the washcoat slurry into the channels of the honeycomb body, or by dipping the body at one side into the washcoat slurry and optionally applying vacuum at the opposite side.
There are two possible methods of catalysing the honeycomb body .
In one method the washcoat contains the catalytic active material.
In the other method, the pre-coated and washcoated honey¬ comb body is finally impregnated with an aqueous solution containing one or more precursors of the desired catalyti- cally active material, followed by drying and calcination.
In summary, a honeycomb catalyst according to the invention can be prepared by a method comprising the steps of
(a) providing a sheet of non-woven fibrous material;
(b) coating the sheet with an aqueous suspension of a ce¬ ramic material; partly removing the moisture from the coat¬ ed sheet prior to
(c) corrugating the coated sheet;
(d) rolling-up or stacking up the coated and corrugated sheet (s) into a spiral-wound cylindrical body or staked up rectangular body; (e) washcoating the cylindrical or rectangular body, op¬ tionally containing the catalytic active components or pre¬ cursors thereof and
(f) drying and optionally calcining the washcoated body; or alternatively
(el) impregnating the washcoated body with a solution of catalytic active components or precursors thereof, if not contained in the washcoat of step e) ;
(fl) drying and calcining the body of step (el) to obtain the final honeycomb catalyst.
Honeycomb catalysts are typically employed in the cleaning of engine exhaust gas. For this purpose the honeycomb cata¬ lyst is shaped as a cylindrical body and canned in a metal housing with a mat between the honeycomb catalyst body and the metallic housing. In the canning process the cylindrical honeycomb body is radially compressed in order to pro¬ vide sufficient friction between the mat and the body and between the mat and the metallic housing. Radially compres- sion typically causes cracks in the coated and calcined body. Thus, a further advantage of the first coat provided on the substrate is that the canning process causes a much reduced cracking of the honeycomb body. The canned honeycomb catalyst is as mentioned above typi¬ cally used in the catalytically removal of noxious com¬ pounds in the exhaust gas, including nitrogen oxides, un- burnt engine fuel and carbon monoxide. Thus, it is preferred that the catalytically active com¬ pounds of the honeycomb catalyst are active in the removal of noxious compounds in engine exhaust gas. Catalyst compounds active in engine exhaust gas cleaning are per se known in the art. To name a few, typically em¬ ployed catalysts are vanadium oxide, tungsten oxide, palla- dium and platinum, and zeolitic material either used alone or as mixtures thereof.
When operating the honeycomb shaped catalyst in the removal of nitrogen oxides contained in exhaust or off-gasses, the nitrogen oxides are converted to free nitrogen with a re¬ ducing agent, typically ammonia, in the presence of an SCR catalyst by selective, catalytic reduction:
4 NO + 4 NH3 + 02 → 4 N2 + 6 H20
NO + N02 + 2 NH3 → 2 N2 + 3 H20
Any of the known SCR catalyst compositions will be suitable for use in the invention.
Fig. 1 of the drawings is a sectional view of a honeycomb catalyst according to the invention.
As seen in Fig. 1, the substrate 1 of a honeycomb catalyst according to the invention is composed of a corrugated sheet 2 of non-woven fibrous material substrate, optionally provided with a liner (not shown) . Substrate 1 can be rolled-up to a cylindrical body. A first coat layer 3 made of ceramic material is coated on sheet 2. The first coat material can also diffuse through the fibrous material of sheet 2 and forms a first coat lay- er on both sides of sheet 2and within the fibrous material, as shown in Fig.l. A washcoat layer 4 is coated on the first coat layer 3. Washcoat layer 4 contains catalyst par¬ ticles 5.

Claims

1. A honeycomb catalyst with a plurality of flow through channels, wherein the honeycomb catalyst comprises a corru- gated substrate and optionally a liner applied on the cor¬ rugated substrate, the substrate and the optional liner are composed of non-woven fibrous material with a first coat of a ceramic material in an amount to result in total weight of the substrate and first coat of between 60-100 g/m2 and a washcoat layer applied on the first coat, the wash coat contains or is impregnated with one or more catalytically active compounds.
2. The honeycomb catalyst of claim 1, wherein the the corrugated substrate comprises one or more sheets of non- woven glassfibers.
3. The honeycomb catalyst of claim 1 or 2, wherein the ceramic material of the first coat comprises titania, sili- ca and/or kaolin.
4. The honeycomb catalyst of claim 1 or 2, wherein the ceramic material of the first coat consists of titania and silica .
5. The honeycomb catalyst according to any one of claims 1 to 4, wherein the honeycomb catalyst is in form of a rolled-up cylindrical body.
6. The honeycomb catalyst according to any one of claims 1 to 5, wherein the washcoat layer comprises titania.
7. The honeycomb catalyst according to any one of claims 1 to 6, wherein the one or more catalytically active com¬ pounds are active in the removal of noxious compounds in engine exhaust gas.
8. The honeycomb catalyst according to any one of claims 1 to 6, wherein the one or more catalytically active com¬ pounds comprise at least one of vanadium oxide, tungsten oxide and zeolitic material.
9. The honeycomb catalyst according to any one of claims 1 to 6, wherein the one or more catalytically active com¬ pounds comprise platinum and/or palladium.
10. The honeycomb catalyst of any one of claims 2 to 9, wherein the glassfibers consist of E-glass.
PCT/EP2017/054881 2016-03-09 2017-03-02 Non-woven fibrous material-based honeycomb catalyst WO2017153237A1 (en)

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Application Number Priority Date Filing Date Title
DKPA201600145 2016-03-09
DKPA201600145 2016-03-09

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Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4416800A (en) * 1978-09-12 1983-11-22 Sakai Chemical Industry Co., Ltd. Method for producing a catalyst and a carrier therefor including heat-resistant fibers
US5194414A (en) * 1991-01-21 1993-03-16 Toshimi Kuma Method of manufacturing a gas absorbing element or a catalyst carrier having a honeycomb structure
EP1195196A1 (en) * 2000-10-06 2002-04-10 Akzo Nobel N.V. Catalyst carrier comprising a fibre paper impregnated with micro fibres, process for its production and its uses
US20090025553A1 (en) * 2001-01-05 2009-01-29 Questair Technologies Inc. Adsorbent coating compositions, laminates and adsorber elements comprising such compositions and methods for their manufacture and use
EP2373405A1 (en) * 2008-12-08 2011-10-12 Haldor Topsøe A/S Method and catalyst for removal of nitrogen oxides in a flue gas
US20150151293A1 (en) * 2012-06-06 2015-06-04 Haldor Topsøe A/S Scr catalyst and method of preparation thereof

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4416800A (en) * 1978-09-12 1983-11-22 Sakai Chemical Industry Co., Ltd. Method for producing a catalyst and a carrier therefor including heat-resistant fibers
US5194414A (en) * 1991-01-21 1993-03-16 Toshimi Kuma Method of manufacturing a gas absorbing element or a catalyst carrier having a honeycomb structure
EP1195196A1 (en) * 2000-10-06 2002-04-10 Akzo Nobel N.V. Catalyst carrier comprising a fibre paper impregnated with micro fibres, process for its production and its uses
US20090025553A1 (en) * 2001-01-05 2009-01-29 Questair Technologies Inc. Adsorbent coating compositions, laminates and adsorber elements comprising such compositions and methods for their manufacture and use
EP2373405A1 (en) * 2008-12-08 2011-10-12 Haldor Topsøe A/S Method and catalyst for removal of nitrogen oxides in a flue gas
US20150151293A1 (en) * 2012-06-06 2015-06-04 Haldor Topsøe A/S Scr catalyst and method of preparation thereof

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