Method for the continuous production of aldehydes
AssigneeBASF SE
InventorsMartin Volland, Thomas Mackewitz, Wolfgang Ahlers, Ansgar Schäfer, Wolfgang Richter, Rocco Paciello
Life of this patent
Estimating the term…
Loading patent…
AssigneeBASF SE
InventorsMartin Volland, Thomas Mackewitz, Wolfgang Ahlers, Ansgar Schäfer, Wolfgang Richter, Rocco Paciello
Estimating the term…
The invention relates to a method for the continuous production of aldehydes by the isomerising hydroformylation in a homogenous phase of olefin compositions by means of a synthesis gas, in the presence of a homogeneous rhodium catalyst that is complexed with an organophosphorus ligand containing oxygen atoms and/or nitrogen atoms and a free ligand. The production is carried out at high temperature and high pressure in a multi-stage reaction system consisting of at least two reaction zones. According to the method, the olefin composition is first reacted in a first reaction zone or a group of several first reaction zones at a total pressure of between 10 and 40 bar, using a synthesis gas with a CO/H2 molar ratio of between 4:1 and 1:2 until a 40 to 95% conversion of the α-olefins is obtained.
A process for the continuous preparation of an aldehyde having from 5 to 21 carbon atoms by isomerizing hydroformylation in the homogeneous phase of an olefin composition having from 4 to 20 carbon atoms and comprising an α-olefin or an olefin having internal double bonds by means of a synthesis gas in the presence of a homogeneous rhodium catalyst complexed with an oxygen- and/or nitrogen-containing organophosphorus ligand and free ligand at elevated temperature and elevated pressure in a multistage reaction system comprising at least two reaction zones, wherein the olefin composition is firstly reacted with the synthesis gas having a CO/H2 molar ratio of from 4:1 to 1:2 at a total pressure of from 10 to 40 bar in a group of one or more first reaction zones to a conversion of the α-olefin of from 40 to 95% and the hydroformylation mixture from this group of one or more first reaction zones is reacted with the synthesis gas having a CO/H2 molar ratio of from 1:4 to 1:1000 at a total pressure of from 5 to 30 bar in a group of one or more downstream reaction zones, where the total pressure in the one or more downstream reaction zones is in each case from 1 to (T1−Tf) bar lower than in the preceding reaction zone, where T1 is the total pressure in the preceding reaction zone and Tf is the total pressure in the reaction zone downstream of the one or more first reaction zones, with the proviso that the difference T1−Tf is greater than 1 bar, and the CO partial pressure in the one or more downstream reaction zones is in each case lower than in the reaction zone preceding this reaction zone wherein the catalyst used is a complex of rhodium with a phosphoramidite ligand of the formula I
A process for the continuous preparation of an aldehyde having from 5 to 21 carbon atoms by isomerizing hydroformylation in the homogeneous phase of an olefin composition having from 4 to 20 carbon atoms and comprising an α-olefin or an olefin having internal double bonds by means of a synthesis gas in the presence of a homogeneous rhodium catalyst complexed with an oxygen- and/or nitrogen-containing organophosphorus ligand and free ligand at elevated temperature and elevated pressure in a multistage reaction system comprising at least two reaction zones, wherein the olefin composition is firstly reacted with the synthesis gas having a CO/H2 molar ratio of from 4:1 to 1:2 at a total pressure of from 10 to 40 bar in a group of one or more first reaction zones to a conversion of the α-olefin of from 40 to 95% and the hydroformylation mixture from this group of one or more first reaction zones is reacted with the synthesis gas having a CO/H2 molar ratio of from 1:4 to 1:1000 at a total pressure of from 5 to 30 bar in a group of one or more downstream reaction zones, where the total pressure in the one or more downstream reaction zones is in each case from 1 to (T1 −Tf) bar lower than in the preceding reaction zone, where T1 is the total pressure in the preceding reaction zone and Tf is the total pressure in the reaction zone downstream of the one or more first reaction zones, with the proviso that the difference T1 −Tf is greater than I bar, and the CO partial pressure in the one or more downstream reaction zones is in each case lower than in the reaction zone preceding this reaction zone wherein the catalyst used is a complex of rhodium with a phosphoramidite ligand of the formula Ia
Dependencies are inferred from the claim text.