Способ получени α,β-ненасыщенных кетонов

摘要

Production of alpha , beta -unsaturated ketones by reaction of aldehydes with ketones in the liquid phase in a tubular reactor is such that: (i) the catalyst is in the continuous phase and at least one starting material is in a disperse phase; and (ii) the loading factor of the tubular reactor is ≥ 0.8. Production of alpha , beta -unsaturated ketones of formula (I) by reaction of aldehydes of formula (II) with ketones of formula (III) in the liquid phase in a tubular reactor is such that (i) the catalyst is in the continuous phase and at least one starting material is in a disperse phase; and (ii) the loading factor of the tubular reactor is ≥ 0.8. R<1> and R<2> = optionally unsaturated aliphatic or aliphatic-cycloaliphatic 1-20 (especially 1-16)C hydrocarbyl or optionally unsaturated cycloaliphatic 5-12C hydrocarbyl (which can contain alkyl substituents or an endoalkylene group), araliphatic 7-15C hydrocarbyl such as benzyl or aromatic hydrocarbyl such as phenyl; and R<3> = H or 1-10C aliphatic hydrocarbyl.; further, R<1> and R<3>, together with both adjacent C atoms can be members of an alicyclic ring and also one or more methylene groups not alpha to a carbonyl group can be substituted in R<1> R<3> by an O or S atom