Abstract An improved process for the production of aliphatic or cycloaliphatic dialdehydes or acetals of the same by reaction of an aliphatic or cycloaliphatic conjugated diene with carbon monoxide and hydrogen in the presence of a rhodium catalyst which is modified with a tertiary phosphine or phosphite at a temperature of from 70° to 160° C and at a pressure of from 100 to 600 atmospheres, the improvement consisting in using as catalyst a rhodium complex which contains carbon monoxide, a tertiary organic phosphine or tertiary organic phosphite and a halogen atom as ligands. Aliphatic and cycloaliphatic dialdehydes or the acetals of the same are suitable for the production of the corresponding diols which may be used in the production of polymers and particularly of polyurethanes.
A process for production of bis-(dimethyl) acetals of hexane dialdehydes with formation of monoaldehydes and residues being substantially suppressed which comprises hydroformylation butadiene with hydrogen and carbon monoxide at a temperature of 100°-140° C and a pressure of 200-400 atmospheres in the presence of a catalytic amount in the range of 10 to 1000 ppm, calculated as rhodium metal and based on the reaction mixture, of a catalyst of the formula X Rh (CO) L.sub.2 in which X is chlorine, bromine, or iodine and L is triphenylphosphine or triphenylphosphite, the ratio of Rh to P in said catalyst being in the range of 1:2 to 1:100 in methanol as the solvent, the amount of said methanol being in molar excess in the range of 100% to 1000% mol percent for each formyl group to be formed in the hydroformylation reaction.
Claim 2
Dependent Claim
140 words
A process for production of bis-(dimethyl) acetals of hexane dialdehydes with formation of monoaldehydes and residues being substantially suppressed which comprises hydroformylation butadiene with hydrogen and carbon monoxide at a temperature of 100°-140° C and a pressure of 200-400 atmospheres in the presence of a catalytic amount in the range of 10 to 1000 ppm, calculated as rhodium metal and based on the reaction mixture, of a catalyst of the formula X Rh (CO) L.sub.2 in which X is chlorine, bromine, or iodine and L is triphenylphosphine or triphenylphosphite, the ratio of Rh to P in said catalyst being in the range of 1:2 to 1:100 in methanol as the solvent, the amount of said methanol being in molar excess in the range of 100% to 1000% mol percent for each formyl group to be formed in the hydroformylation reaction.
Claim 3
Dependent Claim
14 words
A process as claimed in claim 1, wherein X in said formula is chlorine.
Claim 4
Dependent Claim
25 words
A process as claimed in claim 1 wherein the ratio of Rh to P in said catalyst is in the range of 1:5 to 1:50.