Process for the hydroformylation of olefins using a cobalt pre-catalyst

Abstract

Process for the hydroformylation of olefins using a cobalt pre-catalyst.

Claims

1. Process comprising the process steps of: a) adding an olefin; b) adding a cobalt pre-catalyst, wherein the cobalt pre-catalyst is [Co(acac)(C.sub.4H.sub.8O.sub.2).sub.4].sup.+[BF.sub.4].sup.−; c) feeding in synthesis gas; d) heating the reaction mixture from a) to c), with conversion of the olefin to an aldehyde.

2. Process according to claim 1, wherein the olefin is selected from: ethene, propene, 1-butene, cis-2-butene, trans-2-butene, mixture of cis- and trans-2-butene, raffinate 1, raffinate 2, isobutene, 1-pentene, 2-pentene, 2-methyl-1-butene, 2-methyl-2-butene, 1-methylcyclohexene, tetramethylethene, 1-octene, 2-octenes, cyclooctene, di-n-butene, diisobutene, undecenes, dodecenes, triisobutene, tri-n-butene.

3. Process according to claim 1, wherein the olefin is selected from: 1-butene, cis-2-butene, trans-2-butene, isobutene, 1-pentene, 2-pentene, 1-octene, 2-octenes, di-n-butene, diisobutene, triisobutene, tri-n-butene.

4. Process according to claim 1, wherein the Co pre-catalyst is initially charged as a solution.

5. Process according to claim 4, wherein the olefin is added to the initially charged Co pre-catalyst solution.

6. Process according to claim 1, wherein synthesis gas is fed in in process step c) at a pressure in the range from 1 to 8 MPa (10 to 80 bar).

7. Process according to claim 1, wherein synthesis gas is fed in in process step c) at a pressure in the range from 4 to 6 MPa (40 to 60 bar).

8. Process according to claim 1, wherein the reaction mixture is heated in process step d) to a temperature in the range from 80° C. to 180° C.

9. Process according to claim 1, wherein the reaction mixture is heated in process step d) to a temperature in the range from 120° C. to 160° C.

Description

(1) The invention is to be illustrated in detail hereinafter by a working example.

(2) ##STR00001##

(3) A solution of the pre-catalyst (40.1 mL) is added to a 300 mL Premex autoclave equipped with sparging stirrer, and is charged with synthesis gas to 35 bar. The solution is heated up to 160° C. and the pressure is regulated to 50 bar. After 30 minutes, the temperature is lowered to 140° C. The olefin (1-octene) is now added to the catalyst solution by means of a syringe pump, and the reaction solution is stirred at 50 bar at 140° C. for 3 hours. The reaction mixture is then cooled to room temperature and the pressure is released. The yield is determined by gas chromatography.

(4) The reaction was carried out using three different pre-catalysts.

(5) Pre-catalysts (1) and (2) are comparative pre-catalysts.

(6) Pre-catalysts:

(7) (1) Co.sub.2(CO).sub.8

(8) (2) Co(acac).sub.2

(9) (3) [Co(acac)(C.sub.4H.sub.8O.sub.2).sub.4].sup.+[BF.sub.4].sup.−

(10) Reaction Conditions:

(11) T=140° C., p(synthesis gas)=50 bar, t=3 h, olefin=1-octene

(12) The experimental results are listed in the following Table:

(13) TABLE-US-00001 Pre-catalyst Olefin [Co] (mM) T (° C.) t (h) Yield (%) (1) 1-Octene 1 140 3 62.7 (2) 1-Octene 1 140 3 66.9  (3)* 1-Octene 1 140 3 69.3 *process according to the invention

(14) In the process according to the invention using pre-catalyst (3), a better yield was achieved than in the two comparative experiments.

(15) As the working example shows, the object is achieved by the process according to the invention.