Invention Grant
US08981159B2 Continuously operable method for producing carbonyl compounds by means of a catalyst containing a nitroxyl radical
有权
通过含有硝酰自由基的催化剂生产羰基化合物的连续可操作的方法
- Patent Title: Continuously operable method for producing carbonyl compounds by means of a catalyst containing a nitroxyl radical
- Patent Title (中): 通过含有硝酰自由基的催化剂生产羰基化合物的连续可操作的方法
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Application No.: US14110450Application Date: 2011-12-06
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Publication No.: US08981159B2Publication Date: 2015-03-17
- Inventor: Florian Klasovsky , Thomas Haas , Thomas Tacke , Jan Christoph Pfeffer , Michael Rimbach , Michael Volland , Michiel Janssen , Roger Sheldon , Juergen Haberland
- Applicant: Florian Klasovsky , Thomas Haas , Thomas Tacke , Jan Christoph Pfeffer , Michael Rimbach , Michael Volland , Michiel Janssen , Roger Sheldon , Juergen Haberland
- Applicant Address: DE Essen
- Assignee: Evonik Degussa GmbH
- Current Assignee: Evonik Degussa GmbH
- Current Assignee Address: DE Essen
- Agency: Oblon, McClelland, Maier & Neustadt, L.L.P.
- Priority: EP11162077 20110412
- International Application: PCT/EP2011/071911 WO 20111206
- International Announcement: WO2012/139666 WO 20121018
- Main IPC: C07C45/59
- IPC: C07C45/59 ; C07D493/04

Abstract:
The invention relates to a method for the oxidation of a primary or secondary alcohol, preferably to form an aldehyde or ketone, comprising the following steps: a) providing a catalyst composition comprising at least one compound containing a nitroxyl radical, at least one NO source, at least one carbon or mineral acid or an anhydride of a carbon or mineral acid; b) producing a reaction mixture by adding at least one primary or secondary alcohol and a gas comprising oxygen and optionally one or more than one solvent to the catalyst composition from step a) or step e); c) incubating the reaction mixture from step b) at a temperature of between 0 and 100° C. or at the boiling point of the solvent; d) simultaneously with or subsequent to step c): crystallizing the reaction product; and e) recovering the catalyst composition by removing the crystallized reaction product from the reaction mixture obtained in step d).
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