Method for producing methionine and/or 2-hydroxy-4-(methylthio) butanoic acid
US-2019077750-A1 · Mar 14, 2019 · US
US11897836B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11897836-B2 |
| Application number | US-202017618145-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jun 8, 2020 |
| Priority date | Jun 13, 2019 |
| Publication date | Feb 13, 2024 |
| Grant date | Feb 13, 2024 |
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The present invention relates to a process for the preparation of methionine comprising the step of contacting a solution or suspension comprising 2-amino-4-(methylthio)butanenitrile and/or 2-amino-4-(methylthio)butaneamide with water in the presence of a catalyst to give a methionine comprising mixture, wherein the catalyst comprises CeO2 comprising particles, wherein the CeO2 comprising particles have a BET surface area of from 175 to 300+/−10% m2/g measured according to DIN ISO 9277-5 (2003), a mean maximum Feret diameter x Fmax , mean of from 3+/−10% to 40+/−10% nm and a mean minimum Feret diameter x Fmin , mean of from 2+/−10% to 30+/−10% nm, both measured according to DIN ISO 9276-6 (2012).
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The invention claimed is: 1. A process for producing methionine, the process comprising contacting a solution or suspension comprising at least one selected from the group consisting of 2-amino-4-(methylthio)butanenitrile and 2-amino-4-(methylthio)butaneamide with water in the presence of a catalyst to give a methionine comprising mixture, wherein the catalyst comprises CeO 2 comprising particles, wherein the CeO 2 comprising particles have a BET surface area of 225+/−10% to 300+/−10% m 2 /g measured according to DIN ISO 9277-5 (2003), a mean maximum Feret diameter x Fmax, mean of 3+/−10% to 40+/−10% nm, a mean minimum Feret diameter x Fmin, mean of 2+/−10% to 30+/−10% nm, and a mean aspect ratio x Fmin, mean /x Fmax, mean of 0.55+/−10% to 0.80+/−10%, each measured according to DIN ISO 9276-6 (2012). 2. The process of claim 1 , wherein the catalyst comprises 25 to 100 wt.-% CeO 2 , based on a total weight of the catalyst. 3. The process of claim 1 , wherein the CeO 2 comprising particles comprise 50 to 100 wt.-% CeO 2 , based on a total weight of the CeO 2 comprising particles. 4. The process of claim 1 , wherein the BET surface area of the CeO 2 comprising particles is 225+/−10% to 265+/−10% m 2 /g. 5. The process of claim 1 , wherein the CeO 2 comprising particles have a lattice plane distance of 0.24+/−10% to 0.32+/−10% nm. 6. The process of claim 1 , wherein the CeO 2 comprising particles comprise octahedral particles. 7. The process of claim 1 , wherein the CeO 2 comprising particles have a mean equivalent circular diameter x A, mean of 3+/−10% to 30+/−10% nm, measured according to DIN ISO 9276-6 (2012). 8. The process of claim 1 , wherein the CeO 2 comprising particles have a crystallinity of at least 50%. 9. The process of claim 1 , wherein the contacting is performed at a temperature no greater than 90° C. with a 2-amino-4-(methylthio)butanenitrile comprising solution or suspension. 10. The process of claim 1 , further comprising contacting the methionine comprising mixture with water in the presence of the catalyst. 11. The process of claim 10 , wherein the contacting of the methionine comprising mixture is performed at a temperature of 70 to 140° C. 12. The process of claim 1 , further comprising separating the catalyst from the methionine comprising mixture by a continuous cross flow filtration. 13. The process of claim 1 , wherein the method further comprises vacuum distilling the methionine comprising mixture or stripping the with water vapor following the contacting.
by reactions not involving the formation of sulfide groups · CPC title
with amino groups bound to the carbon skeleton · CPC title
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