Method for carrying out multiphase aldol condensation reactions to give mixed α, β-unsaturated aldehydes
View Patent ↗The invention relates to a continuous method for carrying out a multiphase aldol condensation reaction to obtain mixed α,β-unsaturated aldehydes by reacting a mixture of two aliphatic aldehydes having different numbers of carbon atoms, i.e. 2 to 5, in the molecule in a vertical tubular reactor in a concurrent flow in the presence of an aqueous solution of a basically reacting compound. In said method, the aldehyde mixture is dispersed in the aqueous phase in the form of drops, and the aqueous solution of the basically reacting compound flows through the tubular reactor as a continuous phase in laminar conditions.
1. Continuous process for performing a polyphasic aldol condensation reaction to give mixed α,β-unsaturated aldehydes in a tubular reactor by reaction of two aliphatic aldehydes which have different carbon numbers and contain 2 to 5 carbon atoms in the molecule, characterized in that the aliphatic aldehydes are mixed separately in a molar ratio of 1:1 to 5:1, then the aldehyde mixture and an aqueous solution of a basic compound are introduced via the base into an upright tubular reactor in cocurrent mode, the aqueous solution of the basic compound forming the continuous phase which flows through the tubular reactor under laminar conditions, and the aldehyde mixture forming the phase dispersed in droplet form in the continuous phase and the aldol condensation reaction being performed at a temperature up to 90° C. and the tubular reactor being operated with a space velocity V/Vh of the aldehyde mixture per unit reactor volume and time of 0.1 to 1.3.
2. Process according to claim 1 , characterized in that the aliphatic aldehydes are mixed separately in a molar ratio of 1:1 to 3:1.
3. Process according to claim 1 , characterized in that the aldol condensation reaction is performed at temperatures of 10° C. to 65° C.
4. Process according to claim 1 , characterized in that 10 to 140 parts by weight of basic compound are used per 100 parts by weight of aldehyde mixture, calculated as the pure substance.
5. Process according to claim 1 , characterized in that the ratio of the mass flow rate of the aldehyde mixture to that of the aqueous solution of the basic compound is in the range of 1 to (5-56).
6. Process according to claim 1 , characterized in that the aliphatic aldehydes used are acetaldehyde, propionaldehyde, n-butyraldehyde, isobutyraldehyde, n-pentanal, 2-methylbutanal or 3-methylbutanal.
7. Process according to claim 1 , characterized in that the aldol condensation reaction is performed with acetaldehyde and n-butyraldehyde, with acetaldehyde and n-pentanal, or with n-butyraldehyde and n-pentanal.
8. Process according to claim 1 , characterized in that the dispersed droplets of the aldehyde mixture in the continuous phase satisfy the condition A r ≦1.83·K F,Δρ 0.275 .
9. Process according to claim 1 , characterized in that the aldol condensation reaction is performed at temperatures of 30° C. to 60° C.
10. Process according to claim 1 , characterized in that 20 to 60 parts by weight of basic compound are used per 100 parts by weight of aldehyde mixture, calculated as the pure substance.
11. Process according to claim 1 , characterized in that the ratio of the mass flow rate of the aldehyde mixture to that of the aqueous solution of the basic compound is in the range of 1 to (10-32).
12. Continuous process for performing a polyphasic aldol condensation reaction to give mixed α,β-unsaturated aldehydes in a tubular reactor by reaction of two different aliphatic aldehydes selected from acetaldehyde, propionaldehyde, n-butyr-aldehyde, isobutyraldehyde, n-pentanal, 2-methylbutanal or 3-methylbutanal, characterized in that the aliphatic aldehydes are mixed separately in a molar ratio of 1:1 to 3:1, then the aldehyde mixture and an aqueous solution of a basic compound are introduced via the base into an upright tubular reactor in cocurrent mode, the aqueous solution of the basic compound forming the continuous phase which flows through the tubular reactor under laminar conditions, and the aldehyde mixture forming the phase dispersed in droplet form in the continuous phase and the aldol condensation reaction being performed at a temperature up to 90° C. and the tubular reactor being operated with a space velocity V/Vh of the aldehyde mixture per unit reactor volume and time of 0.1 to 1.3.
13. Process according to claim 12 , characterized in that the aldol condensation reaction is performed at temperatures of 10° C. to 65° C.
14. Process according to claim 12 , characterized in that 10 to 140 parts by weight of basic compound are used per 100 parts by weight of aldehyde mixture, calculated as the pure substance.
15. Process according to claim 12 , characterized in that the ratio of the mass flow rate of the aldehyde mixture to that of the aqueous solution of the basic compound is in the range of 1 to (5-56).
16. Process according to claim 12 , characterized in that the aldol condensation reaction is performed with acetaldehyde and n-butyraldehyde, with acetaldehyde and n-pentanal, or with n-butyraldehyde and n-pentanal.
17. Process according to claim 12 , characterized in that the dispersed droplets of the aldehyde mixture in the continuous phase satisfy the condition A r ≦1.83·K F,Δρ 0.275 .