Engineered imine reductases and methods for the reductive animation of ketone and amine compounds
US-9193957-B2 · Nov 24, 2015 · US
US9518279B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9518279-B2 |
| Application number | US-201314140150-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 24, 2013 |
| Priority date | Dec 27, 2012 |
| Publication date | Dec 13, 2016 |
| Grant date | Dec 13, 2016 |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
The invention relates to a bacterial strain belonging to the genus Rhodococcus which is a producer of a nitrile hydratase. The invention also relates to a method for producing acrylamide by hydration of acrylonitrile using a biomass of the bacterial strain and to a method of culturing the bacterial strain.
Opening claim text (preview).
The invention claimed is: 1. A method for producing acrylamide, the method comprising hydration of acrylonitrile using a biomass of a bacterial strain belonging to the genus Rhodococcus and having a nitrile hydratase activity, wherein hydration is carried out at a working concentration of acrylonitrile which is no more than 0.5%, and the bacterial strain is Rhodococcus aetherivorans VKM Ac-2610D. 2. The method of claim 1 , wherein acrylonitrile is mixed in an aqueous suspension of the biomass of the bacterial strain to form a reaction solution; and hydration is carried out so that the working concentration of acrylonitrile in the reaction solution is maintained at no more than 0.5%. 3. The method of claim 1 , wherein hydration is followed by isolation of acrylamide. 4. The method of claim 1 , wherein the biomass of the bacterial strain is at about 100-1000 g, or 200-1000 g, or 200-800 g, or 300-600 g, or about 400-500 g, or less than 1000 g, or less than 500 g, or less than 400 g on a dry weight of strain per 1 ton of a final product. 5. The method of claim 4 , wherein the final product contains acrylamide at a concentration of at least 40%; or at least 41%; or at least 42%; or at least 43%; or at least 44%; or 40-55%; or 41-55%; 42-55%; or 43-55%; or 44-55%; or at least 45%; or at least 46%; or at least 47%; or 45-55%; or 45-54%; or 45-53%; or 45-52%; or 45-51%; or 45-50%; or 45-49%; or 46-55%; or 46-54%; or 46-53%; or 46-52%; or 46-51%; or 46-50%; or 46-49%; or 47-55%; or 47-54%; or 47-53%; or 47-52%; or 47-51%; or 47-50%; or 47-49%. 6. The method of claim 1 , wherein hydration of acrylonitrile is carried out at a temperature of 10-23° C. 7. The method of claim 1 , wherein hydration of acrylonitrile is carried out at a pH of 6.8-8.4. 8. The method of claim 1 , wherein the biomass of the bacterial strain is at about 100-1000 g on a dry weight of strain per 1 ton of a final product. 9. The method of claim 1 , wherein the biomass of the bacterial strain is at about 200-1000 g on a dry weight of strain per 1 ton of a final product. 10. The method of claim 1 , wherein the biomass of the bacterial strain is at about 200-800 g on a dry weight of strain per 1 ton of a final product. 11. The method of claim 1 , wherein the biomass of the bacterial strain is at about 300-600 g on a dry weight of strain per 1 ton of a final product. 12. The method of claim 1 , wherein the biomass of the bacterial strain is at about 400-500 g on a dry weight of strain per 1 ton of a final product. 13. The method of claim 1 , wherein the biomass of the bacterial strain is less than 1000 g on a dry weight of strain per 1 ton of a final product. 14. The method of claim 1 , wherein the biomass of the bacterial strain is less than 500 g on a dry weight of strain per 1 ton of a final product. 15. The method of claim 1 , wherein the biomass of the bacterial strain is less than 400 g on a dry weight of strain per 1 ton of a final product. 16. The method of claim 4 , wherein the final product contains acrylamide at a concentration of 47-55%. 17. The method of claim 4 , wherein the final product contains acrylamide at a concentration of 47-54%. 18. The method of claim 4 , wherein the final product contains acrylamide at a concentration of 47-52%. 19. The method of claim 4 , wherein the final product contains acrylamide at a concentration of 47-52%. 20. The method of claim 4 , wherein the final product contains acrylamide at a concentration of 47-49%.
Amides, e.g. chloramphenicol {or polyamides; Imides or polyimides; Urethanes, i.e. compounds comprising N-C=O structural element or polyurethanes (peptides C12P21/00 or C07K)} · CPC title
Nitrile hydratase (4.2.1.84) · CPC title
Bacteria; Culture media therefor · CPC title
Chemistry & Metallurgy · mapped topic
Microorganisms {; Processes using microorganisms} · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.