Patent Application
20240010593
The present invention relates to a process for preparing the dialdehyde of vinylcyclohexene.
US 2009/0171125 A1 describes a process for hydroformylation of cyclic olefins. Here, a Rh catalyst is used.
The present invention has the object of providing a novel hydroformylation process. The process here is to afford an increased yield compared to the method known from the prior art.
This object is achieved by a process according to claim 1.
Process comprising the process steps of:
In this process, process steps a) to e) can be effected in any desired sequence. Typically, however, CO and H2 are added after the co-reactants have been initially charged in steps a) to d).
It is also possible here for process steps c) and d) to be effected in one step, for example by adding PtI2.
In one variant of the process, the Pt compound and the iodine compound are added in one step, by adding PtI2.
The expression (C1-C12)-alkyl encompasses straight-chain and branched alkyl groups having 1 to 12 carbon atoms. These are preferably (C1-C8)-alkyl groups, more preferably (C1-C6)-alkyl, most preferably (C1-C4)-alkyl.
Suitable (C1-C12)-alkyl groups are especially methyl, ethyl, propyl, isopropyl, n-butyl, isobutyl, sec-butyl, tert-butyl, n-pentyl, 2-pentyl, 2-methylbutyl, 3-methylbutyl, 1,2-dimethylpropyl, 1,1-dimethylpropyl, 2,2-dimethylpropyl, 1-ethylpropyl, n-hexyl, 2-hexyl, 2-methylpentyl, 3-methylpentyl, 4-methylpentyl, 1,1-dimethylbutyl, 1,2-dimethylbutyl, 2,2-dimethylbutyl, 1,3-dimethylbutyl, 2,3-dimethylbutyl, 3,3-dimethylbutyl, 1,1,2-trimethylpropyl, 1,2,2-trimethylpropyl, 1-ethylbutyl, 1-ethyl-2-methylpropyl, n-heptyl, 2-heptyl, 3-heptyl, 2-ethylpentyl, 1-propylbutyl, n-octyl, 2-ethylhexyl, 2-propylheptyl, nonyl, decyl.
In one variant of the process, R1 and R4 are —H.
In one variant of the process, R5, R6, R7, R8 are -Ph.
In one variant of the process, R2 and R3 are —(C1-C12)-alkyl.
In one variant of the process, R2 and R3 are —CH3.
In one variant of the process, the compound (I) has the structure (1):
In one variant of the process, the Pt compound is selected from: Pt(II)I2, Pt(IV)I4, diphenyl(1,5-COD)Pt(11), Pt(II)(acac)2, Pt(0)(PPh3)4, Pt(0)(DVTS) solution (CAS: 68478-92-2), Pt(0)(ethylene)(PPh3)2, tris(benzylideneacetone)Pt(0), Pt(II)(OAC)2 solution, Pt(0)(t-Bu)2, Pt(II)(COD)Me2, Pt(II)(COD)I2, Pt(IV)IMe3, Pt(II)(hexafluoroacetylacetonate)2.
In one variant of the process, the Pt compound is selected from: Pt(II)I2, Pt(II)(acac)2.
In one variant of the process, the Pt compound is Pt(II)I2.
In one variant of the process, the iodine compound is selected from: alkali metal halide, alkaline earth metal halide. NH4X, alkylammonium halide, dialkyl halide, trialkyl halide, tetraalkyl halide, cycloalkylammonium halide.
In one variant of the process, the iodine compound is selected from: Pt(II)I2, Lil.
In one variant of the process, PtI2 is added in an amount, measured in mol % based on vinylcyclohexene, so that the value is in the range of 0.1 mol % to 5 mol %.
In one variant of the process, PtI2 is added in an amount, measured in mol % based on vinylcyclohexene, so that the value is in the range of 0.1 mol % to 3 mol %.
In one variant of the process, PtI2 is added in an amount, measured in mol % based on vinylcyclohexene, so that the value is in the range of 0.1 mol % to 1 mol %.
In one variant of the process, this process comprises the additional process step e′): e′) adding a solvent.
In one variant of the process, the solvent is selected from: THF, DCM, ACN, heptane, DMF, toluene, texanol, pentane, hexane, octane, isooctane, decane, dodecane, cyclohexane, benzene, xylene, Marlotherm, propylene carbonate, MTBE, diglyme, triglyme, diethyl ether, dioxane, isopropanol, tert-butanol, isononanol, isobutanol, isopentanol, ethyl acetate.
In one variant of the process, the solvent is selected from: THF, DCM, ACN, heptane, DMF, toluene, texanol.
In one variant of the process, CO and H2 are fed in at a pressure in a range from 1 MPa (10 bar) to 6 MPa (60 bar).
In one variant of the process, CO and H2 are fed in at a pressure in a range from 1 MPa (20 bar) to 6 MPa (50 bar).
In one variant of the process, the reaction mixture is heated to a temperature in the range from 30° C. to 150° C.
In one variant of the process, the reaction mixture is heated to a temperature in the range from 80° C. to 140° C.
In one variant of the process, the process comprises the additional process step g): g) converting the dialdehyde to the diol.
In one variant of the process, the conversion of the dialdehyde to the diol is carried out using “Shvo's catalyst” (CAS 104439-77-2).
In addition to the process, also claimed are the aldehyde mixture (2a) and (2b), and the alcohol mixture (3a) and (3b).
Aldehyde mixture comprising the compounds (2a) and (2b):
Alcohol mixture comprising the compounds (3a) and (3b):
The invention shall be elucidated in more detail hereinbelow with reference to a working example.
mmol of 4-vinylcyclohex-1-ene, 10 ml of absolute toluene, 0.5 mol % PtI2, 2.2 equivalents of xantphos (1) (based on Pt) are placed under argon in a 25 ml steel autoclave from Parr Instruments. The autoclave is pressurized to 40 bar with synthesis gas (CO/H2=1:1) and the reaction started by heating to 120° C. and stirring. This reaction is conducted at 40 bar/120° C. for 3.5 h. The autoclave is then cooled, the pressure released and a GC sample taken.
In a comparative experiment, Rh(acac)(CO)2 was added instead of PtI2. The reaction with Rh(acac)(CO)2 ran over 11 h.
Yield of dialdehyde (2a)+(2b):
PtI2: 92%
Rh(acac)(CO)2: <14%
30 mmol of the isomeric mixture of the dialdehyde, 25 ml of absolute toluene, 176 mg of “Shvo's catalyst” (CAS 104439-77-2) are transferred under argon to a 100 ml Parr pressure autoclave. The autoclave is pressurized to 50 bar with hydrogen and the reaction carried out with stirring at 100° C. for 1 h and at 110° C. for a further 30 minutes. The reaction is then discontinued (autoclave cooled and the pressure released). The reaction solution is transferred to a Schlenk vessel. Two phases are formed, the lower phase is isolated and freed of toluene in vacuo. This gives the isomeric mixture of the diol (3a)+(3b).
Yield of diol (3a)+(3b): 85%
As the experimental results show, the object is achieved by the process according to the invention.
| Number | Date | Country | Kind |
|---|---|---|---|
| 22183349.4 | Jul 2022 | EP | regional |
