Flow Reactor Vessels and Reactor Systems
US-2017326525-A1 · Nov 16, 2017 · US
US10280136B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10280136-B2 |
| Application number | US-201816133100-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 17, 2018 |
| Priority date | Nov 28, 2014 |
| Publication date | May 7, 2019 |
| Grant date | May 7, 2019 |
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A continuous flow process for the preparation of one or more esters of lactic acid and 2-hydroxy-3-butenoic acid or α-hydroxy methionine analogs from a sugar in the presence of a solid Lewis acid catalyst and a solvent comprising an organic solvent and water. The invention provides a stabilized Lewis acid catalyst for use in a continuous reaction process, where the water is present in an amount of up to or equal to 10 vol. % of the organic solvent.
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What is claimed is: 1. A continuous flow process for the preparation of an α-hydroxy methionine analogue from a sugar selected from one or more of the group consisting of glucose, fructose, mannose, sucrose, xylose, erythrose, erythrulose, threose and glycolaldehyde, in the presence of a compound comprising sulphur, solid Lewis acid catalyst and a solvent comprising an organic solvent and water, wherein the water is present in an amount of up to or equal to 10 vol. % of the organic solvent, and wherein the solid Lewis acid catalyst has a framework structure, which is selected from the group consisting of BEA, MFI, FAU, MOR, FER, MWW, MCM-41 and SBA-15. 2. The process according to claim 1 , wherein the compound comprising sulfur is selected from the group consisting of C 1 -C 5 alkyl thiol, C 1 -C 5 alkyl thiol salts, dimethylmercaptan and dimethyl disulfide. 3. The process according to claim 1 , wherein the vol. % of water present in the organic solvent is from 0.25 to 10 vol. %. 4. A process according to claim 1 , wherein the solid Lewis acid catalyst is calcined after 450 hours. 5. A process according to claim 1 , wherein the solid Lewis acid comprises an active metal selected from one or more of the group consisting of Sn, Ti, Pb, Zr, Ge and Hf. 6. A process according to claim 1 , wherein the solid Lewis acid catalyst is selected from the group consisting of Sn-BEA, Sn-MFI, Sn-FAU, Sn-MOR, Sn-MWW, Sn-MCM-41 and Sn-SBA-15. 7. A process according to claim 1 , wherein the solid Lewis acid catalyst comprises Sn and the loss of Sn from the solid Lewis acid catalyst is less than or equal to 0.11% of the initial amount of Sn per hour on stream. 8. A process according to claim 1 , wherein the solid Lewis acid catalyst comprises Sn and the loss of Sn from the solid Lewis acid catalyst is less than 8% of the initial amount of Sn after 50 hours on stream. 9. A process according to claim 1 , wherein the yield of α-hydroxy methionine analogue ester is greater than 20% after 10 hours on stream. 10. A process according to claim 1 , wherein an alkaline earth metal or alkali metal ion is present in the process. 11. A process according to claim 1 , wherein the solvent is selected from one or more of the group consisting of methanol, ethanol, 1-propanol, 1-butanol and isopropanol. 12. A process according to claim 1 , wherein the temperature of the process is from 140° C. to 200° C. 13. A process according to claim 1 , wherein at least a fraction of the water is introduced to the solvent by mixing the organic solvent with an aqueous sugar solution. 14. A process according to claim 1 , wherein the aqueous sugar solution is a sugar syrup with a sugar dry matter content of 30% or higher. 15. A continuous flow process for the preparation of an alpha-hydroxy methionine analogue from a sugar selected from one or more of the group consisting of glucose, fructose, mannose, sucrose, xylose, erythrose, erythrulose, threose and glycolaldehyde, in the presence of a compound comprising Sulphur, a solid Lewis acid catalyst and a solvent comprising an organic solvent and water, wherein the vol. % of water present in the organic solvent is from 0.25 to 10 vol. % and at least a fraction of the water is introduced to the solvent by mixing the organic solvent with an aqueous sugar solution, and wherein the solid Lewis acid catalyst is Sn-BEA. 16. A process according to claim 15 , wherein the alpha-hydroxy methionine analogue is 2-hydroxy-4-(methylthio)butanoic acid. 17. A process according to claim 15 , wherein the alpha-hydroxy methionine analogue is selected from the group consisting of 2-hydroxy-4-(methylthio)butanoic acid methyl ester, 2-hydroxy-4-(methylthio)butanoic acid ethyl ester, 2-hydroxy-4-(methylthio)butanoic acid propyl ester, 2-hydroxy-4-(methylthio)butanoic acid butyl ester, 2-hydroxy-4-(methylthio)butanoic acid isopropyl ester, 2-hydroxy-4-(methylthio)butanoic acid pentyl ester, 2-hydroxy-4-(methylthio)butanoic acid hexyl ester, and 2-hydroxy-4-(methylthio)butanoic acid heptyl ester, 2-hydroxy-4-(methylthio)butanoic acid octyl ester and 2-hydroxy-4-(methylthio)butanoic acid 2-ethylhexyl ester.
by splitting of carbon-to-carbon bonds and redistribution, e.g. disproportionation or migration of [IMAGE cpc-sch-C07C-0963.gif] groups between different molecules · CPC title
by addition of thiols to unsaturated compounds · CPC title
Lactic acid esters · CPC title
by oxidation-reduction of aldehydes, e.g. Tishchenko reaction · CPC title
of unsaturated hydroxy carboxylic acids · CPC title
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