Masking method for honeycomb formed body, plugged portion forming method for honeycomb formed body, and manufacturing method of honeycomb fired product
US-11260558-B2 · Mar 1, 2022 · US
US11505503B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11505503-B2 |
| Application number | US-202016849407-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 15, 2020 |
| Priority date | Apr 18, 2019 |
| Publication date | Nov 22, 2022 |
| Grant date | Nov 22, 2022 |
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Batch mixtures comprising alumina trihydrate for forming ceramic honeycomb bodies comprised of cordierite and methods of manufacturing honeycomb bodies from such batch mixtures are provided.
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What is claimed is: 1. A method of manufacturing a ceramic honeycomb article comprising cordierite, the method comprising: extruding a cordierite-forming mixture through a die to form a green honeycomb article, the mixture comprising a liquid, a binder and a plurality of inorganic components comprising: an alumina source comprising alumina trihydrate (Al(OH) 3 ) in an amount of from 5 wt. % to about 35 wt. % with respect to the inorganic components, the alumina source further comprising boehmite (AlOOH), or calcined alumina, or a combinations of boehmite (AlOOH) and calcined alumina; and particulate silica having a D90 particle size less than 15 pm and greater than 0.5 pm in an amount of from 5 wt. % to about 30 wt. % with respect to the inorganic components, wherein the mixture is free of clay; wherein the inorganic components further comprise talc; and heating the green honeycomb article to expose the green honeycomb article to temperatures for times sufficient to form a honeycomb article having a cordierite phase. 2. The method of claim 1 , wherein surfaces of the die in contact with the mixture are worn down by the extruding at a slower rate than for surfaces of a die in contact with a nearly identical mixture except that the nearly identical mixture does not contain alumina trihydrate but contains a different alumina source in place of alumina trihydrate. 3. The method of claim 1 , wherein the mixture further comprises an amount of pore former material present in an amount of from 0% by weight and 15% by weight as a superaddition to a dry weight of the plurality of inorganic components, and, wherein upon firing, the ceramic article is provided with a porosity of at least 45% as measured by mercury porosimetry. 4. The method of claim 3 , wherein, upon firing, the ceramic article comprises a porosity of at least about 55% as measured by mercury porisimetry. 5. The method of claim 4 , wherein the pore former material comprises one or more of starches, starch-based materials, cellulose-based compounds, graphite, activated carbon, coke, synthetic polymers, and naturally occurring polymers. 6. The method of claim 5 , whreein the pore former material consists essentially of graphite. 7. The method of claim 1 , wherein the green honeycomb article exhibits a linear shrinkage of less than about 8% upon firing into the ceramic article at a temperature in a range of from about 1300° C. to about 1450° C. for a period of time of from about 1 to about 200 hours. 8. The method of claim 1 , wherein the alumina trihydrate (Al(OH) 3 ) is present in an amount of from 5 wt % to about 25 wt % with respect to the inorganic components, and the particulate silica is present in an amount of from 10 wt % to about 30 wt %. 9. The method of claim 1 , wherein the alumina trihydrate (Al(OH) 3 ) is present in an amount of from 5 wt % to about 20 wt % with respect to the inorganic components, and the particulate silica is present in an amount of from 12 wt % to about 25 wt %. 10. The method of claim 1 , wherein the alumina trihydrate (Al(OH) 3 ) is present in an amount of from 8 wt % to about 18 wt % with respect to the inorganic components, and the particulate silica is present in an amount of from 12 wt % to about 25 wt %. 11. The method of claim 1 , wherein the particulate silica has a median particle size in a range of from about 0.001 μm to about 10 μm.
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