High temperature fiber and method of making
US-2024368041-A1 · Nov 7, 2024 · US
US9637418B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9637418-B2 |
| Application number | US-99887509-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 25, 2009 |
| Priority date | Dec 15, 2008 |
| Publication date | May 2, 2017 |
| Grant date | May 2, 2017 |
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In a method for preparing an ester from an hydroxybenzoic acid and a fatty alcohol for use in a binder system for powder injection molding, transesterification of an ester of the hydroxybenzoic acid and a low alcohol using the fatty alcohol is carried out, the fatty alcohol and the ester of the hydroxybenzoic acid and the low alcohol forming a reaction mixture and being used in an essentially equimolar ratio. The transesterification is carried out at a temperature at which the ester of the hydroxybenzoic acid and the low alcohol and the fatty alcohol are present as a homogeneous melt. The binder system for a powder injection molding contains 80 to 98 wt. % of a metal powder and/or a ceramic powder and 1 to 19 wt. % of a polymeric binder component, and 1 to 19 wt. % of at least one ester prepared by the transesterification.
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What is claimed is: 1. A method for preparing an ester, comprising: forming the ester from an hydroxybenzoic acid and a fatty alcohol by transesterification of an ester of the hydroxybenzoic acid and a low alcohol using the fatty alcohol, wherein the fatty alcohol is a mixture of two or more 1-alkanols, wherein each of the two or more 1-alkanols has a carbon number of at least 16, wherein the carbon numbers of at least two of the two or more 1-alkanols differ, wherein the fatty alcohol and the ester of the hydroxybenzoic acid and the low alcohol are used in an essentially equimolar ratio and form a reaction mixture, and wherein the transesterification is carried out at a temperature below 195° C. at which the ester of the hydroxybenzoic acid and the low alcohol and the fatty alcohol are present as a homogeneous melt. 2. The method as recited in claim 1 , wherein each of the two or more 1-alkanols is selected from the group consisting of 1-docosanol, 1-eicosanol, 1-octadecanol. 3. The method as recited in claim 1 , wherein the mixture of two or more 1-alkanols contains at least 90 wt. %, in relation to the mass the ester, of a specific 1-alkanol. 4. The method as recited in claim 2 , wherein the low alcohol which split off during the transesterification is removed from the reaction mixture by distillation. 5. The method as recited in claim 2 , wherein the transesterification is carried out in the presence of a catalyst. 6. The method as recited in claim 5 , wherein the catalyst is an organometallic tin-containing compound. 7. The method as recited in claim 6 , wherein the organometallic tin-containing compound is selected from the group consisting of dibutyl-tin oxide, dibutyl-tin dilaurate or butyl-tin oxide hydroxide. 8. The method as recited in claim 6 , wherein the quantity of catalyst used, in relation to the mass of the reaction mixture, amounts to 0.1 to 1 wt. %. 9. The method as recited in claim 6 , wherein a protective gas stream is led through the reaction mixture. 10. The method as recited in claim 6 , wherein a reducing agent is added to the reaction mixture.
containing an organic binding agent comprising a mixture of, or obtained by reaction of, two or more components other than a solvent or a lubricating agent · CPC title
Phenols containing ester groups · CPC title
based on alkaline earth metal titanates · CPC title
Organic additives · CPC title
by reacting an ester group with a hydroxy group · CPC title
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