초록

A ceramic structure which is pollucite-based and has high refractoriness and high resistance to thermal shock. The inventive structure is suitable in high temperature applications such as a filtering particulates from diesel engine exhaust.

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1. A ceramic structure comprising a first phase Cs 2 O.Al 2 O 3 .4SiO 2 (CAS 4 ), a second phase Cs 2 O.Al 2 O 3 .2SiO 2 (CAS 2 ), and a third phase selected from the group consisting of SrO.Al 2 O 3 .2SiO 2 (SAS 2 ), SrO.SiO 2 (SrSiO 3 ) and combinations thereof, wherein the ceramic

1. A ceramic structure comprising a first phase Cs 2 O.Al 2 O 3 .4SiO 2 (CAS 4 ), a second phase Cs 2 O.Al 2 O 3 .2SiO 2 (CAS 2 ), and a third phase selected from the group consisting of SrO.Al 2 O 3 .2SiO 2 (SAS 2 ), SrO.SiO 2 (SrSiO 3 ) and combinations thereof, wherein the ceramic has a high thermal expansion anisotropy of between 1400-1450 ppm, as calculated from dimensional change ΔL/L o over a temperature range from room temperature to 1000° C., and an average coefficient of thermal expansion from room temperature to 1000° C. of −10×10 −7 /° C. to +25×10 −7 /° C. 2. The ceramic structure of claim 1 wherein the average coefficient of thermal expansion from room temperature to 1000° C. is about −5×10 −7 /° C. to +15×10 −7 /° C. 3. A diesel particulate filter comprising a highly refractory ceramic having a first phase Cs 2 O.Al 2 O 3 .4SiO 2 (CAS 4 ), a second phase Cs 2 O.Al 2 O 3 .2SiO 2 (CAS 2 ), and a third phase third phase selected from the group consisting of SrO.Al 2 O 3 .2SiO 2 (SAS 2 ), SrO.SiO 2 (SrSiO 3 ) and combinations thereof, wherein the ceramic has a high thermal expansion anisotropy from room temperature to 1000° C. and an average coefficient of thermal expansion from room temperature to 1000° C. of −10×10 −7 /° C. to +25×10 −7 /° C., wherein the diesel particulate filter comprises a honeycomb body, the honeycomb having an inlet end and an outlet end and a multiplicity of cells extending from the inlet end to the outlet end, the cells having porous walls, wherein part of the total number of cells at the inlet end are plugged along a portion of their lengths, and the remaining part of cells that are open at the inlet end are plugged at the outlet end along a portion of their lengths, so that an engine exhaust stream passing through the cells of the honeycomb from the inlet end to the outlet end flows into the open cells, through the cell walls, and out of the structure through the open cells at the outlet end. 4. The diesel particulate filter of claim 3 wherein the average coefficient of thermal expansion from room temperature to 1000° C. of −5×10 −7 /° C. to +15×10 −7 /° C. 5. A method of producing a formable mixture, the method comprising combining a dry blend material consisting essentially of 70-90%, by weight, of a glass frit, consisting essentially, expressed in weight percent on an oxide basis, of 60-68% Cs 2 O, wherein a portion of Cs 2 O is substituted with SrO, wherein up to 30% by weight SrO is substituted for Cs 2 O, 29-35% SiO 2 , and optionally 3-5% Al 2 O 3 , and 10-30%, by weight, Al 2 O 3 , a solvent selected from the group consisting of deionized water, an emulsion consisting essentially of, about 95%, by weight, deionized water, about 0.7%, by weight, triethanolamine and about 4.3%, by weight, oleic acid, and combinations thereof, and a polymer selected from the group consisting of a crosslinked polyacrylic acid copolymer, a polyethylene oxide polymer, and combinations thereof. 6. The method of claim 5 wherein the polymer is a crosslinked polyacrylic acid copolymer. 7. The method of claim 5 wherein the glass frit consists essentially, expressed in weight percent on an oxide basis, of 60-68% Cs 2 O, 29-35% SiO 2 , and optionally 3-5% Al 2 O 3 . 8. The method of claim 5 wherein up to 2%, by weight, Li 2 O is substituted for Cs 2 O. 9. The method of claim 5 wherein up to 30%, by weight, SrO, is substituted for Cs 2 O. 10. The method of claim 9 wherein the polymer is an aqueous-based cellulose ether polymer. 11. The method of claim 10 wherein the aqueous-based cellulose ether polymer is selected from the group consisting of methylcellulose or hydroxylpropyl methylcellulose. 12. The method of claim 11 wherein the solvent is an emulsion cons isting essentially of, about 95%, by weight, deionized water, about 0.7%, by weight, triethanolamine and about 4.3% by weight, oleic acid, and the polymer is methylcellulose. 13. The method of claim 5 comprising the additional step of shaping the mixture by extrusion into a monolithic structure. 14. The method of claim 13 wherein the mixture is shaped by extrusion. 15. The method of claim 14 wherein the mixture is extruded into a honeycomb. 16. A method of making a monolithic structure for high temperature filtration applications, the method comprising:a) forming a mixture comprising:i) about 50-85%, by weight, dry blend consisting essentially of:1) 70-90%, by weight, of a glass frit consisting essentially, expressed in weight percent on an oxide basis, of 60-68% Cs 2 O wherein a portion of Cs 2 O is substituted with SrO, wherein up to 30% by weight SrO is substituted for Cs 2 O, 29-35% SiO 2 , and optionally 3-5% Al 2 O 3 ; and,2) 10-30%, by weight, Al 2 O 3 ; and,ii) 15-30%, by weight, of a solvent selected from the group consisting of deionized water, an emulsion consisting essentially of, about 95%, by weight, deionized water, about 0.7%, by weight, triethanolamine and about 4.3% by weight, oleic acid, and combinations thereof;iii) 0.1-8%, by weight, of a polymer selected from the group consisting of a crosslinked polyacrylic acid copolymer, a polyethylene oxide polymer, and combinations thereof; and,iv) 0-25%, by weight, of a pore former;b) shaping the mixture to form a green body; and,c) firing the green honeycomb structure in an electric furnace at a temperature of about 1350 to 1550° C. over a period of about 6 to 12 hours, and held at a maximum temperature for about 4 to 12 hours to form a fired structure comprising ceramic having a first phase Cs 2 O.Al 2 O 3 .4SiO 2 (CAS 4 ), a second phase Cs 2 O.Al 2 O 3 .2SiO 2 (CAS 2 ), and a third phase third phase selected from the group consisting of SrO.Al 2 O 3 .2SiO 2 (SAS 2 ), SrO.SiO 2 (SrSiO 3 ) and combinations thereof. 17. The method of claim 16 wherein dry blend consists essentially of about 85%, by weight, glass fit and about 15%, by weight, alumina. 18. The method of claim 16 wherein up to 2%, by weight, Li 2 O is substituted for Cs 2 O. 19. The method of claim 18 wherein the polymer is added at 0.1-4%, by weight. 20. The method of claim 19 wherein the polymer is crosslinked polyacrylic acid copolymer. 21. The method of claim 16 wherein up to 30%, by weight, SrO, is substituted for Cs 2 O. 22. The method of claim 16 wherein the aqueous-based cellulose ether polymer is selected from the group consisting of methylcellulose or hydroxylpropyl methylcellulose. 23. The method of claim 22 wherein the solvent is an emulsion consisting essentially of, about 95%, by weight, deionized water, about 0.7%, by weight, triethanolamine and about 4.3% by weight, oleic acid, and the polymer is methylcellulose. 24. The method of claim 16 wherein the pore former is graphite. 25. The method of claim 16 wherein the mixture is shaped by extrusion into a honeycomb structure having an inlet end and an outlet end and a multiplicity of cells extending from the inlet end to the outlet end, the cells having porous walls. 26. The method of claim 25 wherein every other cell is plugged to form a wall-flow filter.