Method for manufacturing carboxylic acid
US-2015368176-A1 · Dec 24, 2015 · US
US10087131B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10087131-B2 |
| Application number | US-201615564566-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 23, 2016 |
| Priority date | Apr 8, 2015 |
| Publication date | Oct 2, 2018 |
| Grant date | Oct 2, 2018 |
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A process for the production of glycolic acid or derivatives thereof from formaldehyde comprising reacting formaldehyde with carbon monoxide and water in the presence of a silica catalyst, wherein from about 200 to about 5000 ppm of an alkyl silyl sulfonic acid is supplied to the reaction.
Opening claim text (preview).
The invention claimed is: 1. A process for the production of glycolic acid or derivatives thereof from formaldehyde comprising reacting formaldehyde with carbon monoxide and water in the presence of a silica catalyst, wherein from about 200 to about 5000 ppm of an alkyl silyl sulfonic acid is supplied to the reaction. 2. The process according to claim 1 , wherein the silica is porous. 3. The process according to claim 1 , wherein the silica has a surface area of from about 250 to about 500 m2 and a pore volume of from about 0.2 to 1 cc/g. 4. The process according to claim 1 , wherein the silica is functionalised. 5. The process according to claim 4 , wherein the functionalization is the presence of acid groups tethered to the silica support. 6. The process according to claim 5 , wherein the acid groups are alkyl sulfonic acid groups. 7. The process according to claim 1 , wherein the alkyl silyl sulfonic acid is trihydroxysilylalkyl sulfonic acid, such as trihydroxysilylpropyl sulfonic acid, or trihydroxysilylethyl sulfonic acid. 8. The process according to claim 1 , wherein the alkyl silyl sulfonic acid is supplied in a recycle product stream. 9. The process according to claim 1 , wherein the alkyl silyl sulfonic acid is added in an amount of from about 300 ppm to about 500 ppm. 10. The process according to claim 1 , wherein the water is present in an amount from the stoichiometric requirement to a molar ratio of about 4:1 water:formaldehyde. 11. The process according to claim 1 , wherein the reaction is carried out in the presence of a solvent. 12. The process according to claim 11 , wherein the solvent is water, a carboxylic acid, or a sulphone. 13. The process according to claim 1 , wherein the process is carried out at a temperature of from about 50° C. to about 400° C. 14. The process according to claim 1 , wherein the process is carried out at a pressure of from about 1 to about 1000 bara. 15. The process according to claim 12 , wherein the carboxylic acid is propionic acid and the sulphone is 2,3,4,5-tetrahydrothiophene-1, 1-dioxide. 16. The process according to claim 13 where the process is carried out at a temperature of from about 100° C. to about 250° C. 17. The process according to claim 14 where the process is carried out at a pressure of from about 10 to about 200 bara.
on an oxygen-containing group in organic compounds, e.g. alcohols · CPC title
containing silicon (ligands in coordination complexes B01J31/1608) · CPC title
by solid-liquid treatment; by chemisorption · CPC title
Silica · CPC title
by reaction with carbon monoxide · CPC title
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