Method for the production of aldehydes
View Patent ↗The invention relates to a hydroformylation method, whereby the homogeneous liquid reactor discharge is first supplied to a gas/liquid separator and then run through an extraction column with a counter-current of synthesis gas and finally fed to an evaporator. The invention is characterised in that the homogeneous liquid mass flow is supplied to the upper section of the extraction column at a temperature above 90° C.
1. A process for reacting olefinically unsaturated compounds with synthesis gas in the presence of a catalyst solution comprising rhodium and organic phosphorus(III) compounds in a hydroformylation reactor, in which the homogeneous, liquid reactor output comprising crude aldehyde and catalyst is passed to a gas/liquid separator and the homogeneous, liquid stream obtained is treated in an extraction column operated in countercurrent with synthesis gas and the liquid output from the extraction column is fed into a vaporizer in which crude aldehyde and catalyst solution are separated from one another, wherein synthesis gas is added to the homogeneous, liquid stream obtained from the gas/liquid separator before this stream enters the extraction column, and the homogeneous, liquid stream is introduced at a temperature of from 110 to 150° C., into the upper part of the extraction column.
2. The process of claim 1 , wherein synthesis gas is fed into the hydroformylation reactor at one or more feed points.
3. The process of claim 1 wherein the synthesis gas fed to the hydroformylation reactor is composed of fresh synthesis gas and the synthesis gas is recirculated via the extraction column.
4. The process of claim 1 wherein fresh synthesis gas is introduced into the middle part of the hydroformylation reactor and the synthesis gas which is recirculated via the extraction column is fed in via the lower part of the hydroformylation reactor.
5. The process of claim 1 wherein the homogeneous liquid stream obtained from the gas/liquid separator is introduced on the first tray of the extraction column, counted from the top of the column.
6. The process of claim 1 wherein the extraction column is a tray column, a column containing ordered packing or a column containing random packing elements.
7. The process of claim 1 wherein the extraction column has 10 to 40, theoretical plates.
8. The process of claim 1 wherein the concentration of organic phosphorous(III) compounds in the homogeneous reaction solution is from 15 to 60% by weight, based on the homogeneous reaction solution.
9. The process of claim 8 , wherein the concentration of organic phosphorus(III) compounds in the homogeneous reaction solution is from 25 to 50% by weight, based on the homogeneous reaction solution.
10. The process of claim 1 wherein the rhodium concentration of the homogeneous reaction solution is from 1 to 1000 ppm, based on the homogeneous reaction solution.
11. The process of claim 10 , wherein the rhodium concentration of the homogenous reaction is from 10 to 800 ppm, based on the homogeneous reaction solution.
12. The process of claim 7 wherein the extraction column has 15 to 25 theoretical plates.