Classifications

• • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
  • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
  • F23C—METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
  • F23C13/00—Apparatus in which combustion takes place in the presence of catalytic material
• • 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
  • B01J23/005—Spinels
• • 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
  • B01J23/02—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the alkali- or alkaline earth metals or beryllium
• • 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
  • B01J23/10—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of rare earths
• • 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
• • 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
  • B01J23/26—Chromium
• • 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
  • B01J23/32—Manganese, technetium or rhenium
  • B01J23/34—Manganese
• • 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
  • B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
  • B01J23/74—Iron group metals
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
  • B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
  • B01J23/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
  • B01J23/84—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
  • B01J23/85—Chromium, molybdenum or tungsten
  • B01J23/86—Chromium
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J35/00—Catalysts, in general, characterised by their form or physical properties
  • B01J35/50—Catalysts, in general, characterised by their form or physical properties characterised by their shape or configuration
  • B01J35/56—Foraminous structures having flow-through passages or channels, e.g. grids or three-dimensional monoliths

Definitions

• This invention relates to catalyst systems, compositions and methods for the formulation of such compositions. More, particularly, the invention relates to catalyst systems in which the active material is homogeneously interspersed throughout a monolith structure of ceramic composition.
• catalyst systems for use in applications such as combustors employ surface active materials in the form of pure pellets of the active material, or in the form of a surface coating of the active material on substrates such as ceramics.
• substrates such as ceramics.
• monolithic structures are most advantageous.
• the disadvantages and limitations of conventional monolithic catalyst systems include the problem of loss of the active material by flaking off or volatilization from the substrate with a resulting loss in catalytic activity, or the problem of a change in the mechanical properties of the structures, due to an interaction of the catalyst coating and the monolith.
• the flaking material can cause erosion and damage to turbine blades, or the weakened catalyst/support can undergo therm ostructural failure and enter the turbine, causing damage to the blades.
• Another object is to provide a catalyst system in which the integrity of the monolith structure is maintained during sustained combustion while obviating the problem of undesirable interaction of a catalyst metal with a substrate which results in structural weakening.
• Another object is to provide a catalyst system which provides relatively longer operating life, especially in high temperature applications, and which provides good performance through relatively higher combustion efficiency over a long period of time.
• Another object is to provide a catalyst system which achieves relatively good catalytic activity wherein the light-off temperatures of the systems compare favorably to the light-off temperatures of catalyst systems employing noble metals.
• the invention in summary comprises a system in which the catalytic composition includes a catalytically active material which is homogeneously interspersed throughout a monolith structure of ceramic composition.
• the composition is shaped into a unitary monolith which is employed as the catalyst structure.
• the active material or materials are admixed with a ceramic material, which can be either active or inactive, in finely divided form and then shaped into the monolith structure which ic calcined.
• the combustion process of the invention comprises combusting reactants in the presense of the monolithic catalytic structures.
• the catalyst systems of the invention are comprised in general of a catalytically active metal oxide material homogeneously mixed or interspersed in a ceramic metal oxide material.
• the mixture can be shaped into a unitary monolith of the desired configuration.
• the resulting monolith is thereby comprised throughout of the catalytically active material to provide a catalysis system with a high degree of structural integrity and with improved performance.
• the active material is a metal oxide which is homogeneously mixed throughout an inactive (or less active) metal oxide, which can be a mixed metal oxide.
• inactive (or less active) materials suitable for use in this embodiment include:
• the monolithic catalytic composition is of the perovskite, spinel, corundum or ilmenite crystal structure type in which primary catalytically active metal oxide materials are in intimate admixture with carriers comprising inactive or active metal oxide materials which are capable of forming ceramics.
• the resulting composition comprises a random interspersion of the various possible crystal structures, e.g. of the perovskites, or the spinels, or the corundum, or the ilmenite, as the case may be.
• a catalytically active base metal oxide of the perovskite crystal structure ABO 3 forms a solid solution with another material (either active or inactive) comprising a metal oxide of the perovskite structure ABO 3 suitable for formation of a ceramic.
• the perovskite structure is comprised of cations of different types of metals, one of type A and another of Type B and in which the cations are of different size with the smaller cations in the ccp array occupying the octahedral holes formed exclusively by the oxide ions.
• M Ca, or Sr
• Another embodiment of the invention provides a primary catalytically active metal oxide of the spinel crystal structure in solid solution with a spinel structured compound which is suitable for formation of a ceramic.
• the spinel crystal structure takes the form A[B 2 ] O 4 or the inverse structure B[AB] O 4 .
• oxide cermet such as the following spinel cermet example can be used:
• a primary catalytically active base metal oxide of either the corundum B 2 O 3 or ilmenite ABO 3 crystal structures forms a solid solution with another material (either active or inactive) comprising a metal oxide of the corundum crystal structure suitable for formation of a ceramic.
• Examples of the primary active corundum oxides include:
• An example of a corundum structured compound suitable for use in this embodiment as the ceramic carrier comprises alumina.
• Examples of solid solutions formed between eorundum structured active compounds and the ilmenite structured carrier comprises Cr 2 O 3 :Al 2 O 3 (1:5 mole ratio) and Fe .85 Mg .15 TiO 3 : Al 2 O 3 (1:9 mole ratio).
• Al 2 O 3 Fe 2 O 3 (3:1 mole ratio)
• Al 2 O 3 Co 2 O 3 (5:1 mole ratio) stabilized with Yttria (2% by weight)
• One method of formulating the catalyst systems of the invention comprises selection of the starting material in a predetermined proportion according to the mole weight formula of the composition desired for the resulting monolith structure.
• the starting compounds are pulverized and intermixed, such as by a ball mill or other method, to insure complete dispersion and a small particle size on the order of 10 to 20 microns.
• the mixture of powder is then formed into the shape which is desired for the particular ceramic technique which is to be used to form the catalyst structure.
• the mixture is then fired at a temperature of at least 1000° C.
• a method of molding the catalyst structure to a desired shape would be to form an aqueous or organic slurry with the reactive powders and a binder, pour the slurry into a mold, apply heat to drive off the water and binder, and then sinter at the high temperature.
• Another example would be to apply a coating of such a mixture to a substrate such as paper formed into the desired shape and then burn the paper off.
• one of the starting materials is a pure compound such as alumina
• Another example for use where one of the starting materials is a pure compound such as alumina would be to press the powders together into the desired shape and then cause them to react.
• a perovskitebased catalyst system which is a solid solution of LaAlO 3 and LaCrO 3 .
• Ammonium dichromate (NH 4 ) 2 Cr 2 O 3 is dissolved in deionized water. Added to that solution is the appropriate mole percentage of La 2 O 3 . Added to that mixture is a reactive alumina in the appropriate mole percentage.
• the resulting mixture is dried at about 150° C to form a sludge, then calcined at a temperature above about 600° C.
• the resulting powder is ball milled and than recalcined above 1300° C. A sample of the recalcined material may be checked by X-ray diffraction. If reaction is not complete, the powder is recalcined until the desired state is achieved.
• the powder which has been made is a completely reacted composition of the base metal oxide.
• the reacted powder is ball milled with water or other suitable liquid to develope a rheology suited to the chosen forming method, then formed and shaped into the desired unitary configuration.
• Another method for making materials suitable for this invention is by gelling solutions of the proper composition of the desired metals.
• the gel may be spray-dried to provide a powder of the proper rheology for further processing.
• the shaping step may be carried out by formation of a water-based slip (with appropriate organic binders and dispersants) and then casting, extruding, molding or pressing the material into the desired shape.
• This step may comprise coating of the slip onto a paper, polymer or sponge substrate, after which the substrate can be removed as by firing.
• the final step in this method is calcining the resultant monolith material in the range of 1100-1600° C. It is preferable to calcine in an oxidizing atmosphere. However, with constituents having oxides such as Cr 2 O 3 , which have some volatility, it may be necessary to calcine under an inert atmosphere such as argon. If the material is calcined under a forming gas to reduce the chance of oxide vaporization, a sample of it must be checked by X-ray diffraction to make sure that segregated reduced phases have not been introduced.
• the following is a specific example of a method of forming a catalyst system with a corundum-based active ceramic.
• appropriate mole percentages of (NH 4 ) 2 Cr 2 O 7 and Al 2 O 3 (reactive) are added to deionized water using suitable dispersants.
• the slurry is dried at 150° C to a sludge, the sludge is calcined at a temperature of 600° C and the resulting powder is ball milled.
• the remaining steps are carried out as set forth in the above example for the perovskite-based system.
• the following is a specific example of a method of forming a spinel-based metal oxide catalyst system which is a solid solution of MgAl 2 O 4 and NiAl 2 O 4 .
• Mg(OH) 2 . 3H 2 O is dispersed in deionized water, and to that mixture are added suitable quantities of reactive Al 2 O 3 and Ni(CO 3 ).
• the product is then dried at 150° C to a sludge, and the sludge is calcined at a temperature range of 1000° C - 1300° C.
• the remaining steps are carried out as in the above-described example for the method of preparing the perovskite-based system.
• a common catalytic substrate having several percent (preferably from 1 to 10% but up to 25%) of a catalytically active metal oxide is added to the material before monolith formation.
• a catalytically active metal oxide for example, nickel oxide in yttria-stabilized zireonia; nickel oxide or chromium oxide in mullite or cordierite or zircon mullite; LaCrO 3 and mullite; MgCr 2 O 4 and alumina; or nickel oxide or Co 2 O 3 and alumina.
• the material is then shaped as described above in connection with the perovskite-based system. Longer times at calcining temperatures may be required to insure that any solid state reaction is complete during formulation.
• Another preferred embodiment of the present invention is the use of eatalytically-active oxide composition as both the catalytic and the structural materials. Although there are many advantages to be gained by mixing active materials with less-active materials, it is often desirable to use the active oxide composition for the catalytic and structural materials. An example of this is the use of LaCrO 3 as the performing catalytically active, electricallyconducting monolith material. Example I
• Oxide powders of MgAl 2 O 4 and NiAl 2 O 4 (3:1 mole ratio) were prepared by pressing the powders into discs and calcining in the manner described above.
• the disc size was 2-1/4" in diameter and 1-1/4" long with 18 to 30 holes of 0.25" diameter drilled axially to form gas flow passages.
• the resulting monolith structure was tested in a eombustor using air and natural gas reactants under fuel-lean conditions down to a minimum preheat of 325° F. Blowout of the catalyst bed did not occur at the highest throughput attained, 849,000 hr -1 space velocity.
• the catalyst was also tested on lean diesel fuel and sustained combustion to a minimum preheat of 590° F. During the diesel fuel test blowout did not occur during maximum throughput at a space velocity of 1,152,000 hr -1 .
• Powders of LaAlO 3 and LaCrO 3 (3:1 mole ratio) were pressed and calcined into discs shaped as described for Example 1.
• the catalyst was tested in a eombustor using reactants of air and natural gas as well as diesel fuel. The test results are depicted in Table II.
• Powders of MgAl 2 O 4 and Fe 3 O 4 (3:1 mole ratio) were pressed and calcined into pellets shaped as described in Example I.
• the catalyst was tested in a eombustor on lean natural gas and lean diesel fuel. The test results are set forth in Table III.
• Powders of MgAl 2 O 4 and MgCr 2 O 4 (3:1 mole ratio) were pressed and calcined into the shape of tubes 2" in length having nominal dimensions of 1/4" OD and
• Powders of Al 2 O 3 and Cr 2 O 3 (9:1 mole ratio) were pressed and calcined into the shape of tubes 2" in length having nominal dimensions of 1/4" OD and 1/8" ID.
• a plurality of the tubes were bundled, wrapped together and supported in the manner described above for example IV. Platinum was added to the front segment to promote light-off.
• the catalyst structure was tested on air and natural gas. The results of the test are depicted in Table V.
• the catalyst system compositions of the present invention provide good performance with high combustion efficiency over a long period of time.
• the catalytic monolith maintains its structural integrity in operation without loss of catalytic activity through flake-off or volatilization.
• There is no problem of interaction of base metal catalysts with the substrate nor is there the problem of degradation of surface area due to growth in crystallite size of the active component when in operation so that there is a relatively longer life, especially in high temperature applications.
• the manufacturing process is relatively less expensive in that there are fewer steps to formulate the monolith structure as compared to existing techniques of manufacturing a substrate, applying a wash coat and then applying the catalyst.

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• Chemical & Material Sciences (AREA)
• Engineering & Computer Science (AREA)
• Chemical Kinetics & Catalysis (AREA)
• Materials Engineering (AREA)
• Organic Chemistry (AREA)
• Combustion & Propulsion (AREA)
• Mechanical Engineering (AREA)
• General Engineering & Computer Science (AREA)
• Catalysts (AREA)
• Exhaust Gas Treatment By Means Of Catalyst (AREA)
• Gas Burners (AREA)

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• 1979
  • 1979-10-03 DE DE792953867T patent/DE2953867A1/de not_active Withdrawn
  • 1979-10-03 BR BR7909042A patent/BR7909042A/pt unknown
  • 1979-10-03 WO PCT/US1979/000813 patent/WO1981000970A1/en unknown
  • 1979-10-03 GB GB8116257A patent/GB2072035B/en not_active Expired
  • 1979-10-03 JP JP80500827A patent/JPS56501233A/ja active Pending

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