The invention relates to a process for preparing siloxanes from alkoxy-organosilicon compounds of the general formula (I) and/or (II) in the presence of at least one cationic silicon and/or germanium compound.
Siloxanes are an industrially important compound class that is used in numerous fields of technology. The preparation of siloxanes is therefore an important process in industrial organosilicon chemistry. By way of example, one process that has become established on an industrial scale is the hydrolytic condensation starting from chlorosilanes according to the following reaction equation:
2R3Si—Cl+H2O=>R3Si—O—SiR3+2HCl
Another process that has become established is the hydrolytic condensation of alkoxy group-containing silanes and siloxanes, which are each raw materials produced on an industrial scale:
R3Si—OR+H2O=>R3Si—OH+ROH;
2R3Si—OH=>R3Si—O—SiR3+H2O
However, these hydrolytic condensations always have to be carried out with an excess of water, since silanols formed in the first step then react further to form siloxanes with reformation of water. The condensation of alkoxy group-containing organosilicon compounds also requires hydrochloric acid as catalyst which, together with the water and the alcohol formed, has to be completely removed again after the reaction. This constitutes a disadvantage which makes the hydrolytic condensation process more difficult, particularly in the case of crosslinking reactions. A disadvantage of the hydrolytic condensation of methoxysil(ox)anes is the formation of methanol, which is generally likely to be undesirable because of its toxicity.
Shimada and Jorapur, in Synlett 2010, 23, 1633, describe the synthesis of symmetrical disiloxanes from the alkoxysilanes in the presence of molar amounts of Meerwein's salt (Me3OBF4, Et3OBF4 or Et3OPF6) in acetonitrile and with addition of potassium carbonate. The large amounts of Meerwein's salt that are required make the process uneconomic. During the work-up, large amounts of salts also have to be separated off in a technically complex manner. The process is therefore not suitable for crosslinking processes.
Gautret et al., in Synth. Commun. 1996, 26, 707, describe the transformation of trimethylsilylated diarylcarbinol to hexamethyldisiloxane and bis(diarylmethyl) ether at room temperature in the presence of 1% trifluoroacetic acid as catalyst. This process is also not suitable in principle for crosslinking processes involving formation of Si—O—Si bonds, since these bonds are not stable with respect to strong acids such as trifluoroacetic acid.
The object of the invention was that of providing a process for siloxane preparation which can be used on an industrial scale and in which alkoxy group-containing organosilicon compounds can be linked to form siloxanes without a hydrolysis step.
This object is achieved by a process in which at least one alkoxy-organosilicon compound which is selected from compounds of the general formula (I)
R1R2R3Si—ORx (I),
(SiO4/2)a(RySiO3/2)b[(RxO)SiO3/2]b′(Ry2SiO2/2)c[(RxO)RySiO2/2]c′[(RxO)2SiO2/2]c″(Ry3SiO1/2)d[(RxO)Ry2SiO1/2]d′[(RxO)2RySiO1/2]d″[(RxO)3SiO1/2]d′″ (II),
Preferably, none of the radicals R1, R2 and R3 are hydrogen.
Preferably, the radicals R1, R2 and R3 are independently selected from the group comprising hydrogen, unsubstituted or substituted C1-C12 hydrocarbon radical and unsubstituted or substituted C1-C12 hydrocarbonoxy radical.
Particularly preferably, the radicals R1, R2 and R3 are independently selected from the group comprising methyl, ethyl, vinyl, phenyl, methoxy and ethoxy.
In formulae (I) and (II), the radical Rx is preferably independently selected from the group comprising unsubstituted or substituted C1-C12 hydrocarbon radical, in particular unsubstituted or substituted C1-C6 hydrocarbon radical.
In formulae (I) and (II), Rx is particularly preferably independently selected from the group comprising C1-C6 alkyl radical, vinyl and phenyl.
The indices a, b, b′, c, c′, c″, d, d′, d″, d′″ are preferably independently selected from an integer in the range of 0 to 1000, particularly preferably in the range of 0 to 100.
It has been found that the reaction of the alkoxy-organosilicon compounds of formulae (1) and (II) to form the corresponding siloxanes can be accelerated by the presence of carbonyl compounds and the conversion of matter can also be increased. Accordingly, it may be preferable for the reaction to be performed in the presence of at least one carbonyl compound.
The carbonyl compound is preferably selected from compounds of the general formula (III)
Rd—(X)n—CO—(X)n—Rd (III),
As examples of the carbonyl compound (III), mention may be made of:
Particularly preferably, n=0 and Rd is independently hydrogen or a C1-C12 hydrocarbon radical, preferably a C1-C6 alkyl radical, particularly preferably a C1-C4 alkyl radical. In particular, the carbonyl compound is selected from the group comprising acetaldehyde, formaldehyde, acetone and methyl ethyl ketone.
Instead of the aldehydes, use may also be made of the corresponding acetals or ketals since they are in equilibrium with the aldehydes in the presence of the cationic silicon and/or germanium compounds. For example, paraldehyde or acetaldehyde diethyl acetal may be used instead of acetaldehyde, and 1,3,5-trioxane may be used instead of formaldehyde.
The carbonyl compound may be used in a proportion by weight of 0.01% to 500%, preferably 0.1% to 100%, particularly preferably 1% to 50%, based on the weight of the compound of the general formula (I) or (II) or, if mixtures of (I) and (II) are used, based on the total weight of the compounds of the general formula (I) and (II).
The cationic silicon and/or germanium compound used as catalyst is preferably selected from compounds of the general formula (IV)
([M(II)Cp]+)aXa- (IV),
As an alternative or in addition, the cationic silicon and/or germanium compound may be selected from compounds of the general formula (V)
In formulae (IV) and (V), Xa- is preferably monovalent anions where a=1.
As examples of monovalent anions X−, mention may be made of:
Particularly preferably, X− (a=1) is independently selected from the group comprising [B(SiCl3)4]−, compounds of the formula [B(Ra)4]− and compounds of the formula [Al(ORc)4]−, where Rc is independently a fluorinated, aliphatic C3-C12 hydrocarbon radical.
In particular, in formula (IV) the anions X− are selected from the group comprising compounds of the formulae [B(SiCl3)4]− and [B(Ra)4]−, wherein the radicals Ra are independently selected from aromatic C6-C14 hydrocarbon radical in which all hydrogen atoms have been independently substituted by a radical selected from the group comprising fluorine and triorganosilyl radical of the formula —SiRb3, wherein the radicals Rb independently represent C1-C20 alkyl radical.
Very particularly preferably, in formula (IV) the anions X− are selected from the group consisting of the compounds of the formulae [B(SiCl3)4]− and [B(Ra)4]−, wherein the radicals Ra are independently selected from the group consisting of —C6F5, perfluorinated 1- and 2-naphthyl radical, —C6F3(SiRb3)2 and —C6F4(SiRb3), wherein the radicals Rb each independently represent C1-C20 alkyl radical.
As examples of radicals Ra, mention may be made of: m-difluorophenyl radical, 2,2,4,4-tetrafluorophenyl radical, perfluorinated 1-naphthyl radical, perfluorinated 2-naphthyl radical, perfluorobiphenyl radical, —C6F5, —C6H3(m-CF3)2, —C6H4(p-CF3), —C6H2(2,4,6-CF3)3, —C6F3(m-SiMe3)2, —C6F4(p-SiMe3), —C6F4(p-SiMe2t-butyl).
As examples of radicals RV in formula (IVa), mention may be made of:
In formula (IVa), the radicals Rv are preferably independently selected from the group comprising C1-C3 alkyl radical, hydrogen and triorganosilyl radical of the formula —SiRb3, wherein the radicals Rb independently represent C1-C20 alkyl radical.
Particularly preferably, the radicals Rv are independently selected from methyl radical, hydrogen and trimethylsilyl radical.
In particular, the cyclopentadienyl radical from formula (IV) may be pentamethylcyclopentadienyl, tris(trimethylsilyl)cyclopentadienyl and bis(trimethylsilyl)cyclopentadienyl.
According to one embodiment, the cationic silicon and/or germanium compounds are selected from the group comprising silicon(II) and germanium(II) compounds of formula (IV), where Rv is independently selected from the group comprising methyl radical, hydrogen and trimethylsilyl radical, and
In general, Si(II) compounds are less preferred since they are generally more difficult to obtain.
Alternatively or additionally, the cationic silicon and/or germanium compounds may be selected from the group of the cationic silicon(IV) and germanium(IV) compounds of the general formula (V), where Rw is independently selected from the group comprising C1-C6 alkyl radical and phenyl radical;
The reactants of formulae (I) and/or (II), the catalyst (formulae IV and V) and any carbonyl compound (formula III) may be brought into contact with one another in any desired sequence. Preferably, “bring into contact” means that the reactants and the catalyst are mixed, with the mixing being performed in a manner known to those skilled in the art.
The reaction according to the invention may be carried out without solvent or with addition of one or more solvents. The proportion of the solvent or solvent mixture, based on the total amount by weight of the compounds of formula (I) and (II), is preferably at least 0.01% by weight and not more than 1000 times the amount by weight, particularly preferably at least 0.1% by weight and not more than 100 times the amount by weight, very particularly preferably at least 1% by weight and not more than 10 times the amount by weight.
Solvents used may preferably be aprotic solvents, for example hydrocarbons such as pentane, hexane, heptane, cyclohexane or toluene, chlorohydrocarbons such as dichloromethane, chloroform, chlorobenzene or 1,2-dichloroethane, ethers such as diethyl ether, methyl tert-butyl ether, anisole, tetrahydrofuran or dioxane, or nitriles such as acetonitrile or propionitrile. Preference is given to solvents or solvent mixtures having a boiling point or boiling range of up to 120° C. at 0.1 MPa. The solvents are preferably chlorinated and non-chlorinated aromatic or aliphatic hydrocarbons.
If a solvent or a carbonyl compound of the general formula (III) is used, then in a preferred embodiment the catalyst of the general formula (IV) and/or (V) is dissolved in the solvent or in the carbonyl compound and then mixed with the compound of the general formula (I) and/or (II).
The pressure during the reaction may be freely selected by those skilled in the art; the reaction may be carried out under ambient pressure or under reduced or elevated pressure. The pressure is preferably in a range of 0.01 bar to 100 bar, particularly preferably in a range of 0.1 bar to bar; very particularly preferably, the reaction is carried out at ambient pressure.
201 mg of trimethylethoxysilane (formula (I) where R1═R2═R3=Me, Rx=Et) was dissolved in 405 mg of dichloromethane, admixed with 8.9 mg of catalyst of formula (V) where Z=Si, Y=1,8-naphthalenediyl, Rw=Ph and Me, where Ph:Me=1:1, and X=B(C6F5)4 and heated to 70° C. for 18 h. This formed 90 mol % each of hexamethyldisiloxane and diethyl ether based on trimethylethoxysilane used.
200 mg of dimethyldiethoxysilane (formula (I) where R1═R2=Me, R3═OEt, Rx=Et) was dissolved in 412 mg of dichloromethane, admixed with 7.1 mg of catalyst of formula (V) where Z=Si, Y=1,8-naphthalenediyl, Rw=Ph and Me, where Ph:Me=1:1, and X═B(C6F5)4 and heated to 70° C. for 18 h. This formed the oligomers EtO—(SiMe2-O)n—SiMe2-OEt, where n=1 to 10, and diethyl ether. The conversion was 85%.
205 mg of methyltriethoxysilane (formula (I) where R1=Me, R2═R3=OEt, Rx=Et) was dissolved in 417 mg of dichloromethane, admixed with 5.2 mg of catalyst of formula (V) where Z═Si, Y=1,8-naphthalenediyl, Rw=Ph and Me, where Ph:Me=1:1, and X═B(C6F5)4 and heated to 70° C. for 24 h. This formed oligomeric siloxanes and diethyl ether. The conversion was 85%.
The experiment according to Example 1 was repeated using 8.0 mg of the catalyst of formula (V) where Z═Si, Y=1,8-naphthalenediyl, Rw=Me, and X═B(C6F5)4. The reaction time at 70° C. was 2 days. This formed 95% each of hexamethyldisiloxane and diethyl ether.
The experiment according to Example 2 was repeated using 6.2 mg of the catalyst of formula (V) where Z═Si, Y=1,8-naphthalenediyl, Rw=Me and X═B(C6F5)4. The reaction time at 70° C. was 2 days. This formed the oligomers EtO—(SiMe2-O)n—SiMe2-OEt, where n=1 to 10, and diethyl ether. The conversion was 70%.
The experiment according to Example 3 was repeated using 5.2 mg of the catalyst of formula (V) where Z═Si, Y=1,8-naphthalenediyl, Rw=Me and X═B(C6F5)4. The reaction time at 70° C. was 2 days. This formed oligomeric siloxanes and diethyl ether. The conversion was 45%.
154 mg of methyltrimethoxysilane (formula (I) where R1=Me, R2═R3═OMe, Rx=Me) was admixed with 1.0 mg of Cp*Ge+B(C6F5)4− (formula (IV)) in 100 mg of dichloromethane and left to stand for 24 h. After this time, 1% of 1,1,3,3-tetramethoxydimethyldisiloxane had formed. 4 mg of methyl ethyl ketone (formula (III)) was then added, and the solution was again left to stand for 24 h. After this time, 14% of 1,1,3,3-tetramethoxydimethyldisiloxane and 2% of pentamethoxy-1,3,5-trimethyltrisiloxane had formed.
134 mg of dimethoxydimethylsilane (formula (I) where R1═R2=Me, R3═OMe, Rx=Me) was admixed with 1.0 mg of Cp*Ge+B(C6F5)4− (formula (IV)) in 100 mg of dichloromethane and left to stand for 24 h. After this time, 2.5% of 1,3-dimethoxytetramethyldisiloxane had formed. 5 mg of methyl ethyl ketone (formula (III)) was then added and the solution was again left to stand for 24 h. After this time, 16% of 1,5-dimethoxytetramethyldisiloxane and 5% of 1,7-dimethoxyhexamethyltrisiloxane had formed.
136 mg of trimethylethoxysilane (formula (I) where R1═R2═R3=Me, Rx=Et) was admixed with 1.1 mg of Cp*Ge+B(C6F5)4− (formula (IV)) in 100 mg of dichloromethane and left to stand for 24 h. After this time, 2.5% of 1,3-dimethoxytetramethyldisiloxane had formed. 5.5 mg of methyl ethyl ketone was then added, and the solution was again left to stand for 24 h. After this time, 11% of hexamethyldisiloxane had formed.
341 mg of MSE 100 is mixed with a solution of 0.18 mg of Cp*Ge+B(C6F5)4− (0.053% by weight based on MSE 100) in 70 μl of dichloromethane in an NMR tube with shaking. The sample is cooled to 2° C. and 21 mg of acetaldehyde (formula (III)), which has also been cooled to 2° C., is added. The NMR tube is sealed and left to stand for 3 h at 23° C. Dilution is performed with CD2Cl2 and the sample is analyzed by NMR spectroscopy. The signal at δ□□□3.2 ppm indicates the formation of dimethyl ether. MSE 100 is a siloxane that is formed from MeSi(OMe)3 by hydrolytic condensation and comprises 31% by weight of methoxy groups.
231 mg of acetaldehyde (formula (III)) and 2506 mg of MSE 100 are mixed in a SpeedMixer. 1.3 mg of Cp*Ge+B(C6F5)4− (0.052% by weight based on MSE 100) dissolved in 200 μl of dichloromethane is added to this mixture and the latter is mixed for approx. 2 min in the SpeedMixer, with the mixture having cured completely.
The experiment according to Example 10 is repeated without the addition of acetaldehyde. The sample is still liquid after the mixing and has cured after 24 h at 23° C.
2520 mg of MSE 100 and 127 mg of acetone (formula (III), 5% by weight based on MSE 100) are mixed in a SpeedMixer. 1.2 mg of Cp(SiMe3)3Ge+B(SiCl3)4− (formula (IV), 0.048% by weight based on MSE 100) dissolved in 180 μl of dichloromethane is added to this mixture and the latter is mixed again for approx. 2 min in the SpeedMixer. After 5 h at 23° C. the mixture has cured and is colorless.
2565 mg of MSE 100 and 130 mg of acetone (formula (III), 5% by weight based on MSE 100) are mixed in a SpeedMixer. 0.27 mg of Cp(SiMe3)3Ge+B(SiCl3)4− (formula (IV), 0.011% by weight based on MSE 100), without added solvent, is then added to this mixture and the latter is mixed again for approx. 2 min in the SpeedMixer. After 5 h at 23° C. the mixture has cured and is colorless.
2531 mg of MSE 100 and 125 mg of methyl ethyl ketone (formula (III), 5% by weight based on MSE 100) are mixed in a SpeedMixer. 1.1 mg of Cp(SiMe3)3Ge+B(SiCl3)4− (formula (IV), 0.043% by weight based on MSE 100) dissolved in 190111 of dichloromethane is then added to this mixture and the latter is mixed again for approx. 2 min in the SpeedMixer. After 5 h at 23° C. the mixture has cured and is colorless.
2560 mg of MSE 100 and 126 mg of methyl ethyl ketone (formula (III), 5% by weight based on MSE 100) are mixed in a SpeedMixer. 0.29 mg of Cp(SiMe3)3Ge+B(SiCl3)4− (formula (IV), 0.011% by weight based on MSE 100), without added solvent, is then added to this mixture and the latter is mixed again for approx. 2 min in the SpeedMixer. After 5 h at 23° C. the mixture has cured and is colorless.
2602 mg of MSE 100 and 129 mg of methyl ethyl ketone (formula (III), 5% by weight based on MSE 100) are mixed in a SpeedMixer. 1.4 mg of Cp(SiMe3)3Ge+B(C6F5)4− (formula (IV), 0.054% by weight based on MSE 100), without added solvent, is then added to this mixture and the latter is mixed again for approx. 2 min in the SpeedMixer. After approx. 4 h at 23° C. the mixture has cured and is colorless.
2529 mg of MSE 100 and 134 mg of acetaldehyde diethyl acetal (5% by weight based on MSE 100) are mixed in a SpeedMixer. 1.1 mg of Cp(SiMe3)3Ge+B(SiCl3)4− (formula (IV), 0.043% by weight based on MSE 100), without added solvent, is then added to this mixture and the latter is mixed again for approx. 2 min in the SpeedMixer. After approx. 4 h at 23° C. the mixture has cured and is colorless.
2536 mg of MSE 100 and 129 mg of paraldehyde (5% by weight based on MSE 100) are mixed in a SpeedMixer. 1.2 mg of Cp(SiMe3)3Ge+B(C6F5)4− (formula (IV), 0.047% by weight based on MSE 100), without added solvent, is then added to this mixture and the latter is mixed for approx. 2 min in the SpeedMixer. The mixture has cured after approx. 4 h at 23° C.
The experiment in Example 19 is repeated. After the mixing, the sample is heated to 50° C. and has cured after approx. 1 h at this temperature.
2563 mg of MSE 100 and 130 mg of DMC (formula (III), 5% by weight based on MSE 100) are mixed in a SpeedMixer. 0.5 mg of Cp*Ge+B(C6F5)4− (formula (IV), 0.02% by weight based on MSE 100), without added solvent, is then added to this mixture and the latter is mixed for approx. 2 min in the SpeedMixer. The mixture has cured after approx. 7 h at 23° C.
2533 mg of Silres IC 368 and 242 mg of acetaldehyde (formula (III), 10% by weight based on Silres IC 368) are mixed in a SpeedMixer. 1.2 mg of Cp(SiMe3)3Ge+B(C6F5)4− (formula (IV), 0.05% by weight based on Silres IC 368) in 200 μl of dichloromethane is then added to this mixture and the latter is mixed for approx. 2 min in the SpeedMixer. The mixture has cured after approx. 24 h at 23° C. Silres IC 368 is a hydrolytic condensate of PhSi(OMe)3 and MeSi(OMe)3 in the ratio 62:38 that comprises 14% by weight of methoxy groups.
2528 mg of Silres IC 368 and 131 mg of paraldehyde (5% by weight based on Silres IC 368) are mixed in a SpeedMixer. 1.2 mg of Cp(SiMe3)3Ge+B(C6F5)4− (formula (IV), 0.047% by weight based on Silres IC 368) in 200 μl of dichloromethane is then added to this mixture and the latter is mixed for approx. 2 min in the SpeedMixer. The mixture has cured after approx. 24 h at 23° C.
Example 23 is repeated using TRASIL instead of Silres IC 368. The mixture has cured after approx. 24 h at 23° C. TRASIL is a hydrolytic condensate of MeSi(OEt)3 with a molar ratio of EtO:Me=0.7:1.
Filing Document | Filing Date | Country | Kind |
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PCT/EP2020/073525 | 8/21/2020 | WO |