Patent Application
20240383833
The present invention relates to a process for preparing an acetal from an olefin using an iodine-alkyl compound.
It was an object of the present invention to provide a process for preparing an acetal from an olefin. The intention here is to achieve a good yield.
This object is achieved by a process according to claim 1.
Process comprising the process steps of:
In this process, process steps a) to f) 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 e).
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.
The expression (C6-C20)-aryl encompasses mono- or polycyclic aromatic hydrocarbyl radicals having 6 to 20 carbon atoms. These are preferably (C6-C14)-aryl, more preferably (C6-C10)-aryl.
Suitable (C6-C20)-aryl groups are especially phenyl, naphthyl, indenyl, fluorenyl, anthracenyl, phenanthrenyl, naphthacenyl, chrysenyl, pyrenyl, coronenyl. Preferred (C6-C20)-aryl groups are phenyl, naphthyl and anthracenyl.
In one variant of the process, R2, R3, R5, R6, R7, R8 are selected from: —(C1-C12)-alkyl, —(C6-C20)-aryl.
In one variant of the process, R5, R6, R7, R8 are —(C6-C20)-aryl.
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, R1 and R4 are —H.
In one variant of the process, the compound (I) has the structure (1):
In one variant of the process, the Pt compound is Pt(II)(COD)Me2.
In one variant of the process, the iodine-alkyl compound is selected from: ICH2CH2I, CH3I, CH2l2, CHI3, Cl4, I2CHCHI2, I3CCl3, ICH2CH2CH2I, ICH2CH2CH2CH2I, ICH2CH2CH2CH2CH2I.
In one variant of the process, the iodine-alkyl compound is selected from: ICH2CH2l, CH3I.
In one variant of the process, the iodine-alkyl compound is ICH2CH2I.
In one variant of the process, the iodine-alkyl compound is CH3I.
In one variant of the process, the alcohol in process step e) is selected from: methanol, ethanol, 1-propanol, 1-butanol, ethane-1,2-diol, propane-1,2-diol.
In one variant of the process, the alcohol in process step e) is MeOH.
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 3 MPa (30 bar) to 5 MPa (50 bar).
In one variant of the process, the reaction mixture is heated to a temperature in the range from 50° C. to 150° C.
In one variant of the process, the reaction mixture is heated to a temperature in the range from 70° C. to 130° C.
In one variant of the process, the olefin is selected from: ethene, propene, 1-butene, cis- and/or trans-2-butene, isobutene, 1,3-butadiene, 1,2-butadiene, 1-pentene, cis- and/or trans-2-pentene, 2-methyl-1-butene, 3-methyl-1-butene, 2-methyl-2-butene, hexene, tetramethylethylene, heptene, 1-octene, 2-octene, di-n-butene, tri-n-butene, 1,7-octadiene, 1,9-decadiene, methyl 9-decenoate (9-Dame) or mixtures thereof.
In one variant of the process, the olefin has two double bonds.
In one variant of the process, the olefin has two terminal double bonds.
In one variant of the process, this process comprises the additional process step f):
In one variant of the process, the solvent is selected from: THF, MTBE, DCM, ACN, heptane, DMF, toluene, xylene, mesitylene, dibenzyltoluene.
The invention is to be elucidated in detail hereinafter with reference to working examples.
The olefin, an inert solvent, the alcohol, the Pt compound, the ligand and the halogen compound are placed in a stainless steel autoclave from Parr Instruments under argon. Synthesis gas CO/H2 (1:1) is injected and the reaction is conducted at the chosen reaction temperature while stirring. After the end of the reaction time, the autoclave is cooled down to room temperature, the residual pressure is released, and a GC sample for determination of the yield of target product is taken and analysed.
4.1 mmol of butadiene (3.2 ml of 8.3% stock solution in toluene), 80 mmol of MeOH (3.2 ml), 7 ml of toluene, 1.2 mol % of Pt(II)(COD)Me2 (16.7 mg), 1.2 mol % of Xantphos (1) (29 mg) and 1.2 mol % of XCH2CH2X or 2.4 mol % of CH3X are introduced into a 25 ml autoclave from Parr under argon. Synthesis gas CO: H2=1:1 is injected to 40 bar and heated. The reaction is conducted while stirring. After the reaction has ended, the autoclave is cooled down, the pressure is released and the reaction solution is transferred into a Schlenk vessel. 10 mml of CH2Cl2 (0.6 ml) is added, and a 1H NMR analysis and a GC analysis are carried out.
4.1 mmol butadiene, 1.2 mol % Pt(II)(COD)Me2, 1.2 mol % Xantphos (1), solvent: toluene, alcohol: MeOH, p(CO/H2): 40 bar (4 MPa).
These experimental results are listed in the table below.
As shown by the experimental results, the object is achieved by the process according to the invention.
| Number | Date | Country | Kind |
|---|---|---|---|
| 23173655.4 | May 2023 | EP | regional |
