发明名称 |
Method for the production of 2-hydroxy-4-(methylthio)butyronitrile from 3-(methylthio)propanal and hydrogen cyanide |
摘要 |
A method for the production of 2-hydroxy-4-methylthiobutyric acid by hydrolysis of 2-hydroxy-4-(methylthio)butyronitrile is provided. 3-Methylmercaptopropionaldehyde is reacted with hydrogen cyanide in the presence of a base as catalyst in a main reaction zone of the multizone reactor to form a reaction mixture comprising the 2-hydroxy-4-(methylthio)butyronitrile, unreacted 3-methylmercaptopropionaldehyde, the catalyst and residual amounts of gaseous hydrogen cyanide. The residual gaseous hydrogen cyanide is removed from the main reaction zone to an absorption and post-reaction zone of the reactor which comprises a mixture of 3-methylmercaptopropionaldehyde and the catalyst; and the gaseous hydrogen cyanide is further reacted with the 3-methylmercaptopropionaldehyde in the absorption and post reaction zone. A molar ratio of hydrogen cyanide to 3-(methylthio)propanal in the main reaction zone is from 0.98 to 1.03. |
申请公布号 |
US9133113(B2) |
申请公布日期 |
2015.09.15 |
申请号 |
US201414227418 |
申请日期 |
2014.03.27 |
申请人 |
EVONIK DEGUSSA GmbH |
发明人 |
Buss Dieter;Steurenthaler Martin;Rinner Michael R.;Kretz Stephan;Hasselbach Hans Joachim;Finkeldei Caspar-Heinrich;Koerfer Martin;Zacchi Pablo |
分类号 |
C07C319/20 |
主分类号 |
C07C319/20 |
代理机构 |
Oblon, McClelland, Maier & Neustadt, L.L.P. |
代理人 |
Oblon, McClelland, Maier & Neustadt, L.L.P. |
主权项 |
1. A process for producing 2-hydroxy-4-methylthiobutyric acid, the process comprising:
hydrolysis of 2-hydroxy-4-(methylthio)butyronitrile to obtain the 2-hydroxy-4-methylthiobutyric acid; wherein the 2-hydroxy-4-(methylthio)butyronitrile is obtained by a process comprising: reacting 3-methylmercaptopropionaldehyde with hydrogen cyanide in the presence of a base as catalyst in a main reaction zone of a multizone reactor to form a reaction mixture comprising the 2-hydroxy-4-(methylthio)butyronitrile, unreacted 3-methylmercaptopropionaldehyde, the catalyst and residual amounts of gaseous hydrogen cyanide; removing the residual gaseous hydrogen cyanide from the main reaction zone to an absorption and post-reaction zone of the reactor which comprises a mixture of 3-methylmercaptopropionaldehyde and the catalyst; further reacting the gaseous hydrogen cyanide with the 3-methylmercaptopropionaldehyde in the absorption and post-reaction zone; and removing the 2-hydroxy-4-(methylthio)butyronitrile from the multizone reactor. |
地址 |
Essen DE |