US4416800A
Expired / Lapsed
US
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Method for producing a catalyst and a carrier therefor including heat-resistant fibers
Assignee: Sakai Chemical Industry Co Ltd
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Filing: 1981-03-19
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Granted: 1983-11-22
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Expires: 2001-03-19
Abstract
Abstract A method is provided for producing a catalyst and a carrier therefor in the form of sheet or honeycomb. The method comprises: beating a heat-resistant fiber such as asbesto fiber in water to form a slurry; mixing the slurry with a catalytically active agent, a carrier material therefor and/or their precursors to fix such materials in the fiber, thus forming a stock; and forming the stock into a sheet and drying the same. The sheet thus obtained may be formed into a honeycomb structure with an improved adhesive.
Inventors
- 👤 Kazunobu Abe
- 👤 Tadao Nakatsuji
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-28 21:27
CPC Classifications
B; B32; B32B; B32B3/00; B32B3/26; B32B3/28; B01; B01D; B01D53/00; B01D53/34; B01D53/92; B01D53/94; B01D53/9404; B01D53/9409; B01D53/9413; B01D53/9418; B01J; B01J35/00; B01J35/50; B01J35/56; B01J35/57; B01J35/58; B32B1/00; B32B19/00; B32B5/00; B32B5/22; B32B5/24; B32B5/26; B32B7/00; B32B7/04; B32B7/12; F; F01; F01N; F01N3/00; F01N3/08; F01N3/10; F01N3/24; F01N3/28; F01N3/2803; F01N3/2825; F01N3/2828; B01D2251/00; B01D2251/20; B01D2251/206; B01D2251/2062; B01D2255/00; B01D2255/20; B01D2255/207; B01D2255/20707; B01D2255/20723; B01D2255/20738; B01D2255/20761; B01D2255/20769; B01D2255/20776; B01D2255/90; B01D2255/92; B01D2255/9202; B32B2262/00; B32B2262/10; B32B2262/101; B32B2262/105; B32B2262/106; B32B2262/108; F01N2330/00; F01N2330/06; Y; Y10; Y10T; Y10T428/00; Y10T428/24; Y10T428/24149
Claims Analysis
Total Claims: 25
Claim 1
Independent Claim
216 words
A method for producing a catalytic material, which consists essentially of admixing (a) a slurry prepared by beating at least one of inorganic fibers of about 1-20 mm in fiber length and of about 0.1-30 microns in diameter selected from the group consisting of asbestos fiber, silica fiber, silica-alumina fiber, chrysotile fiber, rock wool, glass fiber, anthophyllite fiber, potassium titanate fiber, carbon fiber and ceramic fiber, in water, and (b) at least one powdery water-insoluble carrier material selected from the group consisting of titanium oxide and aluminum oxide or a powdery water-insoluble precursor of the carrier material which will be converted into the oxide when calcined, thereby forming a stock material containing the solid components of fiber and carrier material in an amount of 1-10% by weight with about 80-40 parts by weight of fiber in relation to 20-60 parts by weight of carrier material, forming the stock material into a sheet by paper-making means and drying the sheet, and then immersing the sheet or a honeycomb structure manufactured therefrom in an impregnating slurry or solution containing catalytically active agents or their precursors which will be converted into the active agent when calcined, and optionally carrier materials or their precursors which will be converted into the oxide when calcined, and drying the sheet or honeycomb structure.
Claim 2
Independent Claim
216 words
A method for producing a catalytic material, which consists essentially of admixing (a) a slurry prepared by beating at least one of inorganic fibers of about 1-20 mm in fiber length and of about 0.1-30 microns in diameter selected from the group consisting of asbestos fiber, silica fiber, silica-alumina fiber, chrysotile fiber, rock wool, glass fiber, anthophyllite fiber, potassium titanate fiber, carbon fiber and ceramic fiber, in water, and (b) at least one powdery water-insoluble carrier material selected from the group consisting of titanium oxide and aluminum oxide or a powdery water-insoluble precursor of the carrier material which will be converted into the oxide when calcined, thereby forming a stock material containing the solid components of fiber and carrier material in an amount of 1-10% by weight with about 80-40 parts by weight of fiber in relation to 20-60 parts by weight of carrier material, forming the stock material into a sheet by paper-making means and drying the sheet, and then immersing the sheet or a honeycomb structure manufactured therefrom in an impregnating slurry or solution containing catalytically active agents or their precursors which will be converted into the active agent when calcined, and optionally carrier materials or their precursors which will be converted into the oxide when calcined, and drying the sheet or honeycomb structure.
Claim 3
Dependent Claim
19 words
The method as claimed in claim 1, wherein the carrier material has a particle size of about 0.01-50 microns.
Claim 4
Dependent Claim
175 words
The method as claimed in claim 1, wherein the honeycomb structure is manufactured from the sheet with an adhesive which comprises 100 parts by weight of an aqueous colloidal silica solution containing about 10-30% by weight of silica of about 1-100 millimicrons in particle size and about 10-45 millimicrons in average particle size, and 1-50 parts by weight of at least one of finely divided refractory oxide particles selected from the group consisting of silica having specific surface area of 100-400 m 2 /g, primary particle size of 25-150 millimicrons and average particle size of 40-200 millimicrons, alumina having specific surface area of 100-300 m 2 /g, primary particle size of 10-150 millimicrons and average particle size of 30-70 millimicrons, silica-alumina having specific surface area of about 200 m 2 /g, primary particle size of 1-80 millimicrons and average particle size of 10-30 millimicrons, and titania having specific surface area of about 50 m 2 /g, primary particle size of 10-120 millimicrons and average particle size of 15-40 millimicrons, uniformly dispersed in the colloidal solution.
Claim 5
Dependent Claim
32 words
The method as claimed in claim 3, wherein the adhesive further contains 0.01-15 parts by weight of an organic polymer selected from the group consisting of polyethylene oxide, carboxymethylcellulose, methylcellulose and polyvinylalcohol.
Claim 6
Dependent Claim
96 words
The method as claimed in claim 1, wherein the impregnating slurry or solution further contains 1-10 parts by weight of at least one inorganic heat-resistant fiber of about 0.1-30 microns in diameter and about 0.5-5 mm in fiber length selected from the group consisting of asbestos fiber, ceramic fiber, silica fiber, silica-alumina fiber, chrysotile fiber, rock wool, glass fiber, potassium titanate fiber, anthophyllite fiber and carbon fiber, or about 0.5-5 parts by weight of polytetrafluoroethylene fiber, in relation to 100 parts by weight of the total weight of catalytically active agents, carrier materials and their precursors.
Claim 7
Independent Claim
245 words
A method for producing a catalytic material for the reduction of nitrogen oxides in the presence of ammonia, which consists essentially of admixing (a) a slurry prepared by beating at least one of inorganic fibers of about 1-20 mm in fiber length and of about 0.1-30 microns in diameter selected from the group consisting of asbestos fiber, silica fiber, silica-alumina fiber, chrysotile fiber, rock wool, glass fiber, anthophyllite fiber, potassium titanate fiber, carbon fiber and ceramic fiber, in water, and (b) at least one powdery water-insoluble carrier material selected from the group consisting of titanium oxide and aluminum oxide or a powdery water-insoluble precursor of the carrier material which will be converted into the oxide when calcined. thereby forming a stock material containing the solid components of fiber and carrier material in an amount of 1-10% by weight with about 80-40 parts by weight of fiber in relation to 20-60 parts by weight of carrier material, forming the stock material into a sheet by paper-making means and drying the sheet, and then immersing the sheet or a honeycomb structure manufactured therefrom in an impregnating slurry or solution containing at least one catalytically active agent of an oxide selected from the group consisting of Cu, Fe, V, W and Mo or their precursors which will be converted into the oxide when calcined, and optionally carrier materials or their precursors which will be converted into the carrier materials when calcined, and drying the sheet or honeycomb structure.
Claim 8
Independent Claim
245 words
A method for producing a catalytic material for the reduction of nitrogen oxides in the presence of ammonia, which consists essentially of admixing (a) a slurry prepared by beating at least one of inorganic fibers of about 1-20 mm in fiber length and of about 0.1-30 microns in diameter selected from the group consisting of asbestos fiber, silica fiber, silica-alumina fiber, chrysotile fiber, rock wool, glass fiber, anthophyllite fiber, potassium titanate fiber, carbon fiber and ceramic fiber, in water, and (b) at least one powdery water-insoluble carrier material selected from the group consisting of titanium oxide and aluminum oxide or a powdery water-insoluble precursor of the carrier material which will be converted into the oxide when calcined. thereby forming a stock material containing the solid components of fiber and carrier material in an amount of 1-10% by weight with about 80-40 parts by weight of fiber in relation to 20-60 parts by weight of carrier material, forming the stock material into a sheet by paper-making means and drying the sheet, and then immersing the sheet or a honeycomb structure manufactured therefrom in an impregnating slurry or solution containing at least one catalytically active agent of an oxide selected from the group consisting of Cu, Fe, V, W and Mo or their precursors which will be converted into the oxide when calcined, and optionally carrier materials or their precursors which will be converted into the carrier materials when calcined, and drying the sheet or honeycomb structure.
Claim 9
Dependent Claim
18 words
The method as claimed in claim 6, wherein the carrier material has a particle size of 0.01-50 microns.
Claim 10
Dependent Claim
176 words
The method as claimed in claim 6, wherein the honeycomb structure is manufactured from the sheet with an adhesive which comprises 100 parts by weight of an aqueous colloidal silica solution containing about 10-30 % by weight of silica of about 1-100 millimicrons in particle size and about 10-45 millimicrons in average particle size, and 1-50 parts by weight of at least one of finely divided refractory oxide particles selected from the group consisting of silica having specific surface area of 100-400 m 2 /g, primary particle size of 25-150 millimicrons and average particle size of 40-200 millimicrons, alumina having specific surface area of 100-300 m 2 /g, primary particle size of 10-150 millimicrons and average particle size of 30-70 millimicrons, silica-alumina having specific surface area of about 200 m 2 /g, primary particle size of 1-80 millimicrons and average particle size of 10-30 millimicrons, and titania having specific surface area of about 50 m 2 g/, primary particle size of 10-120 millimicrons and average particle size of 15-40 millimicrons, uniformly dispersed in the colloidal solution.
Claim 11
Dependent Claim
32 words
The method as claimed in claim 8, wherein the adhesive further contains 0.01-15 parts by weight of an organic polymer selected from the group consisting of polyethylene oxide, carboxymethylcellulose, methylcellulose and polyvinylalcohol.
Claim 12
Dependent Claim
96 words
The method as claimed in claim 6, wherein the impregnating slurry or solution further contains 1-10 parts by weight of at least one inorganic heat-resistant fiber of about 0.1-30 microns in diameter and about 0.5-5 mm in fiber length selected from the group consisting of asbestos fiber, ceramic fiber, silica fiber, silica-alumina fiber, chrysotile fiber, rock wool, glass fiber, potassium titanate fiber, anthophyllite fiber and carbon fiber, or about 0.5-5 parts by weight of polytetrafluoroethylene fiber, in relation to 100 parts by weight of the total weight of catalytically active agents, carrier materials and their precursors.
Claim 13
Independent Claim
208 words
A method for producing a catalyst for the oxidation of carbon monoxide and hydrocarbons to carbon dioxide and water, which consists essentially of admixing (a) a slurry prepared by beating at least one of inorganic fibers of about 1-20 mm in fiber length and of about 0.1-30 microns in diameter selected from the group consisting of asbestos fiber, silica fiber, silica-alumina fiber, chrysotile fiber, rock wool, glass fiber, anthophyllite fiber, potassium titanate fiber, carbon fiber and ceramic fiber, in water, and (b) at least one powdery water-insoluble carrier material selected from the group consisting of titanium oxide and aluminum oxide or a powdery water-insoluble precursor of the carrier material which will be converted into the oxide when calcined, thereby forming a stock material containing the solid components of fiber and carrier material in an amount of 1-10% by weight with about 80-40 parts by weight of fiber in relation to 20-60 parts by weight of carrier material, forming the stock material into a sheet by paper-making means and drying the sheet, and then immersing the sheet or a honeycomb structure manufactured therefrom in an impregnating slurry or solution which contains a compound of platinum, drying and calcining the sheet or honeycomb, and reducing the platinum compound to platinum.
Claim 14
Independent Claim
208 words
A method for producing a catalyst for the oxidation of carbon monoxide and hydrocarbons to carbon dioxide and water, which consists essentially of admixing (a) a slurry prepared by beating at least one of inorganic fibers of about 1-20 mm in fiber length and of about 0.1-30 microns in diameter selected from the group consisting of asbestos fiber, silica fiber, silica-alumina fiber, chrysotile fiber, rock wool, glass fiber, anthophyllite fiber, potassium titanate fiber, carbon fiber and ceramic fiber, in water, and (b) at least one powdery water-insoluble carrier material selected from the group consisting of titanium oxide and aluminum oxide or a powdery water-insoluble precursor of the carrier material which will be converted into the oxide when calcined, thereby forming a stock material containing the solid components of fiber and carrier material in an amount of 1-10% by weight with about 80-40 parts by weight of fiber in relation to 20-60 parts by weight of carrier material, forming the stock material into a sheet by paper-making means and drying the sheet, and then immersing the sheet or a honeycomb structure manufactured therefrom in an impregnating slurry or solution which contains a compound of platinum, drying and calcining the sheet or honeycomb, and reducing the platinum compound to platinum.
Claim 15
Dependent Claim
19 words
The method as claimed in claim 11, wherein the carrier material has a particle size of about 0.01-50 microns.
Claim 16
Dependent Claim
38 words
The method as claimed in claim 11, wherein the sheet or honeycomb is immersed in an aqueous solution which contains chloroplatinic acid, which is then dried, calcined, and then the chloroplatinic acid is reduced in a hydrogen atmosphere.
Claim 17
Dependent Claim
174 words
The method as claimed in claim 11, wherein the honeycomb structure is manufactured from a sheet with an adhesive which comprises 100 parts by weight of an aqueous colloidal silica solution containing about 10-30% by weight of silica of about 1-100 millimicrons in particle size and about 10-45 millimicrons in average particle size, and 1-50 parts by weight of at least one finely divided refractory oxide particles selected from the group consisting of silica having specific surface area of 100-400 m 2 /g, primary particle size of 25-150 millimicrons and average particle size of 40-200 millimicrons, alumina having specific surface area of 100-300 m 2 /g, primary particle size of 10-150 millimicrons and average particle size of 30-70 millimicrons, silica-alumina having specific surface area of about 200 m 2 /g, primary particle size of 1-80 millimicrons and average particle size of 10-30 millimicrons, and titania having specific surface area of about 50 m 2 /g, primary particle size of 10-120 millimicrons and average particle size of 15-40 millimicrons, uniformly dispersed in the colloidal solution.
Claim 18
Dependent Claim
32 words
The method as claimed in claim 11, wherein the adhesive further contains 0.01-15 parts by weight of an organic polymer selected from the group consisting of polyethylene oxide, carboxymethylcellulose, methylcellulose and polyvinylalcohol.
Claim 19
Dependent Claim
96 words
The method as claimed in claim 11, wherein the impregnating slurry or solution further contains 1-10 parts by weight of at least one inorganic heat-resistant fiber of about 0.1-30 microns in diameter and about 0.5-5 mm in fiber length selected from the group consisting of asbestos fiber, ceramic fiber, silica fiber, silica-alumina fiber, chrysotile fiber, rock wool, glass fiber, potassium titanate fiber, anthophyllite fiber and carbon fiber, or about 0.5-5 parts by weight of polytetrafluoroethylene fiber, in relation to 100 parts by weight of the total weight of catalytically active agents, carrier materials and their precursors.
Claim 20
Independent Claim
202 words
A method for producing a catalytic material, which consists essentially of admixing (a) a slurry prepared by beating at least one of inorganic fibers of about 1-20 mm in fiber length and of about 0.1-30 microns in diameter selected from the group consisting of asbestos fiber, silica fiber, silica-alumina fiber, chrysotile fiber, rock wool, glass fiber, anthophyllite fiber, potassium titanate fiber, carbon fiber and ceramic fiber, in water, and (b) at least one powdery water-insoluble carrier material selected from the group consisting of titanium oxide and aluminum oxide or a powdery water-insoluble precursor of the carrier material which will be converted into the oxide when calcined, thereby forming a stock material containing the solid components of fiber and carrier material in an amount of 1-10% by weight with about 80-40 parts by weight of fiber in relation to 20-60 parts by weight of carrier material, forming the stock material into a sheet by paper-making means and drying the sheet, and then immersing the sheet or a honeycomb structure manufactured therefrom in an impregnating slurry or solution containing carrier materials and catalytically active agents or their precursors which will be converted into their oxides when calcined and drying the sheet or honeycomb structure.
Claim 21
Independent Claim
202 words
A method for producing a catalytic material, which consists essentially of admixing (a) a slurry prepared by beating at least one of inorganic fibers of about 1-20 mm in fiber length and of about 0.1-30 microns in diameter selected from the group consisting of asbestos fiber, silica fiber, silica-alumina fiber, chrysotile fiber, rock wool, glass fiber, anthophyllite fiber, potassium titanate fiber, carbon fiber and ceramic fiber, in water, and (b) at least one powdery water-insoluble carrier material selected from the group consisting of titanium oxide and aluminum oxide or a powdery water-insoluble precursor of the carrier material which will be converted into the oxide when calcined, thereby forming a stock material containing the solid components of fiber and carrier material in an amount of 1-10% by weight with about 80-40 parts by weight of fiber in relation to 20-60 parts by weight of carrier material, forming the stock material into a sheet by paper-making means and drying the sheet, and then immersing the sheet or a honeycomb structure manufactured therefrom in an impregnating slurry or solution containing carrier materials and catalytically active agents or their precursors which will be converted into their oxides when calcined and drying the sheet or honeycomb structure.
Claim 22
Independent Claim
226 words
A method for producing a catalytic material for the reduction of nitrogen oxides in the presence of ammonia, which consists essentially of admixing (a) a slurry prepared by beating at least one of inorganic fibers of about 1-20 mm in fiber length and of about 0.1-30 microns in diameter selected from the group consisting of asbestos fiber, silica fiber, silica-alumina fiber, chrysotile fiber, rock wool, glass fiber, anthophyllite fiber, potassium titanate fiber, carbon fiber and ceramic fiber, in water, and (b) at least one powdery water-insoluble carrier material selected from the group consisting of titanium oxide and aluminum oxide or a powdery water-insoluble precursor of the carrier material which will be converted into the oxide when calcined, thereby forming a stock material containing the solid components of fiber and carrier material in an amount of 1-10% by weight with about 80-40 parts by weight of fiber in relation to 20-60 parts by weight of carrier material, forming the stock material into a sheet by paper-making means and drying the sheet, and then immersing the sheet or a honeycomb structure manufactured therefrom in an impregnating slurry or solution containing carrier materials and a catalytically active agent selected from the group consisting of Cu, Fe, V, W and Mo or their precursors which will be converted into their oxides when calcined and drying the sheet or honeycomb structure.
Claim 23
Independent Claim
226 words
A method for producing a catalytic material for the reduction of nitrogen oxides in the presence of ammonia, which consists essentially of admixing (a) a slurry prepared by beating at least one of inorganic fibers of about 1-20 mm in fiber length and of about 0.1-30 microns in diameter selected from the group consisting of asbestos fiber, silica fiber, silica-alumina fiber, chrysotile fiber, rock wool, glass fiber, anthophyllite fiber, potassium titanate fiber, carbon fiber and ceramic fiber, in water, and (b) at least one powdery water-insoluble carrier material selected from the group consisting of titanium oxide and aluminum oxide or a powdery water-insoluble precursor of the carrier material which will be converted into the oxide when calcined, thereby forming a stock material containing the solid components of fiber and carrier material in an amount of 1-10% by weight with about 80-40 parts by weight of fiber in relation to 20-60 parts by weight of carrier material, forming the stock material into a sheet by paper-making means and drying the sheet, and then immersing the sheet or a honeycomb structure manufactured therefrom in an impregnating slurry or solution containing carrier materials and a catalytically active agent selected from the group consisting of Cu, Fe, V, W and Mo or their precursors which will be converted into their oxides when calcined and drying the sheet or honeycomb structure.
Claim 24
Independent Claim
223 words
A method for producing a catalyst for the oxidation of carbon monoxide and hydrocarbons to carbon dioxide and water, which consists essentially of admixing (a) a slurry prepared by beating at least one of inorganic fibers of about 1-20 mm in fiber length and of about 0.1-30 microns in diameter selected from the group consisting of asbestos fiber, silica fiber, silica-alumina fiber, chrysotile fiber, rock wool, glass fiber, anthophyllite fiber, potassium titanate fiber, carbon fiber and ceramic fiber, in water, and (b) at least one powdery water-insoluble carrier material selected from the group consisting of titanium oxide and aluminum oxide or a powdery water-insoluble precursor of the carrier material which will be converted into the oxide when calcined, thereby forming a stock material containing the solid components of fiber and carrier material in an amount of 1-10% by weight with about 80-40 parts by weight of fiber in relation to 20-60 parts by weight of carrier material, forming the stock material into a sheet by paper-making means and drying the sheet, and then immersing the sheet or a honeycomb structure manufactured therefrom in an impregnating slurry or solution containing carrier materials or their precursors which will be converted into their oxides when calcined and a compound of platinum, and drying and calcining the sheet or honeycomb, and reducing the platinum compound to platinum.
Claim 25
Independent Claim
223 words
A method for producing a catalyst for the oxidation of carbon monoxide and hydrocarbons to carbon dioxide and water, which consists essentially of admixing (a) a slurry prepared by beating at least one of inorganic fibers of about 1-20 mm in fiber length and of about 0.1-30 microns in diameter selected from the group consisting of asbestos fiber, silica fiber, silica-alumina fiber, chrysotile fiber, rock wool, glass fiber, anthophyllite fiber, potassium titanate fiber, carbon fiber and ceramic fiber, in water, and (b) at least one powdery water-insoluble carrier material selected from the group consisting of titanium oxide and aluminum oxide or a powdery water-insoluble precursor of the carrier material which will be converted into the oxide when calcined, thereby forming a stock material containing the solid components of fiber and carrier material in an amount of 1-10% by weight with about 80-40 parts by weight of fiber in relation to 20-60 parts by weight of carrier material, forming the stock material into a sheet by paper-making means and drying the sheet, and then immersing the sheet or a honeycomb structure manufactured therefrom in an impregnating slurry or solution containing carrier materials or their precursors which will be converted into their oxides when calcined and a compound of platinum, and drying and calcining the sheet or honeycomb, and reducing the platinum compound to platinum.
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| 3.5 Years (Year 4) | 1986-11-21 | 1987-05-23 | 1987-11-22 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1990-11-21 | 1991-05-23 | 1991-11-22 | $3760.00 | Window Closed / Lapsed |
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