摘要:
The present invention relates to a chemocatalytic liquid-phase process for the direct single-stage amination of alcohols to primary amines using ammonia in high yields by means of a catalyst system containing at least one transition metal compound and a xantphos ligand.
摘要:
The invention relates to an improved method for releasing an organic acid, preferably a carbon, sulfone or phosphone acid, particularly an alpha or beta hydroxycarbon acid, from the ammonia salt thereof by releasing and removing ammoniac and simultaneous extraction of the released acid, having an amine as a suitable extraction means from the aqueous phase. This method corresponds to a reactive extraction. The reactive extraction of an organic acid from the aqueous ammonia salt solution thereof can be significantly improved by the use of a strip medium or carrier gas, such as nitrogen, air, water vapor or inert gases such as argon. The released ammoniac is removed from the aqueous solution by the continuous gas flow and can be resupplied into a production process. The free acid can be obtained by a method such as distillation, rectification, crystallization, reextraction, chromatography, adsorption or by a membrane method from the extraction means.
摘要:
The invention relates to a method for producing aldehydes and ketones from easily accessible primary and secondary alcohols by oxidation with atmospheric oxygen or pure oxygen using a catalyst system which consists of a derivative of a free nitroxyl radical.
摘要:
The present invention provides a process for preparing primary amines, comprising the steps of A) providing a solution of a primary alcohol in a fluid, non-gaseous phase, B) contacting the phase with free ammonia and/or at least one ammonia-releasing compound and a homogeneous catalyst, and optionally C) isolating the primary amine formed in step B), characterized in that the volume ratio of the volume of the liquid phase to the volume of the gas phase in step B is greater than 0.05 and/or that step B is carried out at pressures greater than 10 bar.