PROCESS FOR PREPARING AMINOPROPYL ALKOXY SILANES

Abstract: A process for preparing aminopropyl alkoxy silanes comprising reacting an allylamine having at least one active hydrogen atom attached to the amine nitrogen atom with a hydro-alkoxy silane having from 1 to 3 alkoxy groups attached to the silicon atom in the presence of a rhodium complex having inorganic ligands, at least one of said ligands being carbonyl. By this process the desired gamma-isomer can be prepared in a high selectivity and yield within a short reaction time. When the reaction is carried out in the presence of carbon monooxide and/or a cyclic olefinic compound, the selectivity and yield of the gamma-isomer can be further improved. The presence of carbon monooxide in the reaction system further serves to elongate the catalyst life and to reduce the amount of the catalyst to be used.

Description: The present invention relates to a process for preparing aminopropyl alkoxy silanes. More particularly, it relates to a process for preparing aminopropyl alkoxy silanes wherein an allylamine having at least one active hydrogen atom attached to the amine nitrogen atom is reacted with a hydro-alkoxy silane using as a catalyst a rhodium complex having inorganic ligands, at least one of which is CO. Such a rhodium catalyst, which may be briefly referred to herein as a rhodium carbonyl complex, will be described hereinafter in detail. As known in the art, the aminopropyl alkoxy silanes are useful as silane coupling agents. Silane coupling agents are compounds having in their molecule an organic functional group and a hydrolizable group reactive with inorganic materials. Since the silane coupling agents are, due to their functional groups, capable of chemically bonding an organic polymer with an inorganic material, such as silica, thereby remarkably increasing the mechanical strength of the organic polymer, demand for them is increasing as an indispensable material in the development of ultrafashionable composite materials. Gamma-aminopropyl alkoxy silanes are used in the art as the silane coupling agent, and it is known that they can be prepared by hydrosililation of an allylamine, which may be substituted on the nitrogen atom, with a hydro-alkoxy silane. For example, Japanese Patent Laid-open Publication No. 60-81189 discloses a process for the preparation of aminopropyl alkoxy silanes, which comprises reacting an allylamine with a hydro-alkoxy silane using a platinum catalyst, such as chloroplatinic acid, in the presence of a promoter, such as anhydrous sodium carbonate. However, the reaction of an allylamine with a hydro-alkoxy silane in the presence of a platinum catalyst, such as chloroplatinic acid, inevitably produces the corresponding beta-aminopropyl alkoxy silane, which may be referred to herein as the beta-isomer in addition to the desired gamma-aminopropyl alkoxy silane, which may be referred to herein as the gamma-isomer, normally with a ratio of the gamma-isomer to the beta-isomer of from 4 to 6, posing a problem in that the selectivity of the desired gamma-isomer is not satisfactorily high. Japanese Patent Laid-open Publication No. 61-229885 discloses a process for the preparation of aminopropyl alkoxy silanes by reacting an allylamine with a hydro-alkoxy silane in the presence of a catalyst comprising rhodium organic tertiary phosphine complex and optionally triphenylphosphine. By this process gamma-aminopropyl alkoxy silanes can be prepared in a high selectivity. The process is disadvantageous, however, in that a prolonged reaction time is required to achieve a high conversion, and an excessive amount of triphenylphosphine must be used to achieve a high selectivity of the gamma-isomer. J. of Organomet. Chem., 149, 29-36 (1978) deals with the hydrosililation of olefins in the presence of a metallic carbonyl catalyst, such as cobalt-, rhodium-, iridium- and iron-carbonyl compounds and reports that N, N-dimethylaminopropyl triethoxy silane is obtainable in a high yield from N, N-dimethylallylamine and triethoxy silane. It is stated in this article that when an olefinic amine, such as allylamine, is hydrosililated, the sililation proceeds preferentially on the amine nitrogen atom. This statement means that the metallic carbonyl compounds, such as rhodium carbonyl would be unsuitable as a catalyst for the preparation of an aminopropyl alkoxy silane by hydrosililating an allylamine having at least one active hydrogen atom attached to the amine nitrogen atom with a hydro-alkoxy silane. A process for preparing aminopropyl alkoxy silanes according to the invention comprises reacting an allylamine of the formula [I] wherein R₁ is hydrogen, alkyl having from 1 to 10 carbon atoms, alkenyl having from 2 to 10 carbon atoms, phenyl, substituted phenyl, ―CH₂CH₂NHCH₂CH₂NH₂ or ―CH₂CH₂NH₂, and R₂ is hydrogen or alkyl having from 1 to 6 carbon atoms with a hydro-alkoxy silane of the formula [II] wherein R₃ and R₄ are the same or different, and each represents alkyl having from 1 to 6 carbon atoms and n is 0, 1 or 2, in the presence of a rhodium complex having inorganic ligands and being free from any organic ligand, at least one of said ligands being carbonyl. The reaction according to the invention may be carried out in the presence of carbon monoxide or a cyclic olefinic compound. By doing so the selectivity and yield of the gamma-isomer may be further improved. The presence of carbon monoxide in the reaction system further serves to lengthen the catalyst life and to reduce the amount of the catalyst to be used. A process for preparing aminopropyl alkoxy silanes according to the invention will be fully described hereinafter. Allylamines Allylamines having at least one active hydrogen atom attached to the amine nitrogen atom, as represented by the formula [I], can be used herein. Examples of such allylamines include, for example, allylamine, N-methylallylamine, N-ethylallylamine, 2-methylallylamine, diallylamine and allylethylenediamine. Hydro-alkoxy silanes Hydro-alkoxy silanes having from 1 to 3 alkoxy groups attached to the silicon atom, as represented by the formula [II] can be used herein. Of these, hydro-alkoxy silanes of the formula [II] wherein n is 0 or 1, and R₃ and R₄ each represents methyl or ethyl, are preferred. Examples of hydro-alkoxy silanes of the formula [II] include, for example, triethoxy silane, trimethoxy silane, tripropoxy silane, tributoxy silane, methyl dimethoxy silane, ethyl dimethoxy silane, methyl diethoxy silane, dimethyl methoxy silane, trioctyloxy silane, methyl dioctyloxy silane and dimethyl octyloxy silane. Rhodium carbonyl complex When an allylamine as described above is reacted with a hydro-alkoxy silane as described above according to the invention, use is made, as a catalyst, of a rhodium carbonyl complex having inorganic ligands, at least one of said inorganic ligands being carbonyl. The remaining inorganic ligands possessed by the complex may also be carbonyl, but they may be hydrogen, sulfur, carbon, amine, nitrile, chlorine or thiocarbonyl, for example. Examples of suitable rhodium carbonyl complexes include: (1) [0] valent rhodium carbonyl complex, such as Rh₂(CO)₈, Rh₄(CO)₁₂ and Rh₆(CO)₁₆; (2) anionic rhodium carbonyl complexes, such as Rh(CO)⁴⁻, [Rh₄(CO)₁₁]²⁻, [Rh₆(CO)₁₅]²⁻, [Rh₆(CO)₁₄]⁴⁻, [Rh₇(CO)₁₆]³⁻ and [Rh₁₂(CO)₃₀]²⁻, coupled with (equivalent) cations, such as ammonium, quarternary ammonium, e.g. tetraalkylammonium, and alkali metal ions; (3) rhodium carbonyl complexes having hetero atoms, such as Rh₁₂(CO)₂₅(C)₂, and Rh₈(CO)₁₉C; and; (4) other rhodium carbonyl complexes, such as [Rh₆(CO)₁₅C]²⁻, [Rh₁₇(CO)₃₂(S)₂]³⁻, HRh(CO)₄, [H₃Rh₁₃(CO)₂₄]²⁻ and [H₂Rh₁₃(CO)₂₄]³⁻. Rhodium carbonyl complexes, which can be used herein, are inorganic in that they are free from any organic ligand, such as triphenylphosphine. The rhodium carbonyl complex may be separately prepared and the catalyst so prepared may be added to the reaction system, or it may be formed in the reaction system and the complex so formed in situ may be used as the catalyst. Reaction conditions The allylamine and hydro-alkoxy silane are preferably used in such amounts that a ratio of the allylamine to the hydro-alkoxy silane by mole is within the range from about 1.3: 1 to about 1: 1.3. The reaction may be carried out under atmospheric or elevated pressure. The reaction is normally carried out at a temperature of from about 50°C. to about 250°C. If a reaction temperature substantially below 50°C. is used, the desired gamma-isomer will be formed in small amounts. When the reaction temperature increases above 250°C, increasing amounts of the beta-isomer tend to be formed, undesirably lowering the selectivity of the gamma-isomer. Preferred reaction temperatures are from about 100°C to about 200°C. While the rhodium carbonyl complex may be used in an excess amount, it is sufficient for it to be present in the reaction system in an amount on the order of from 10⁻⁷ to 10⁻³ mole per mole of the allylamime, on a rhodium basis. In carrying out the reaction, solvents may or may not be used. When solvents are used, generally, hydrocarbon solvents, such as toluene, xylene, heptane and dodecane are preferred. While the reaction time greatly depends upon the reaction temperature used, it may normally be within the range between about 0.5 and about 2.0 hours. When an allylamine is reacted with a hydro-alkoxy silane in the presence of a rhodium carbonyl complex in accordance with the invention, we have found as shown in the following Examples, that the corresponding gamma-aminopropyl alkoxy silane can be produced in a high selectivity. For example, the gamma-isomer can be produced with a gamma/beta ratio as high as 15 to 16. Further, the reaction rapidly proceeds, and thus, the gamma-isomer can be obtained in a yield as high as 50 to 70%. In contrast, if an allylamine is reacted with a hydro-alkoxy silane, using a chloroplatinic acid catalyst, the yield of the gamma-isomer is on the order of 40-50%, with a gamma/beta ratio of about 4. Further, if an allylamine is reacted with a hydro-alkoxy silane, using rhodium hydride carbonyl tris(triphenylphosphine) complex as a catalyst, the gamma-isomer with a high gamma/beta ratio can only be obtained at the cost of a prolonged reaction time, e.g., 6 hours, owing to a slow reaction velocity. The reaction of an allylamine with a hydro-alkoxy silane, described above, may be carried out in the presence of carbon monoxide, whereby the selectivity and yield of the gamma-isomer may be further improved and the life of the catalyst may be lengthened, and the amount of the catalyst to be used may be reduced. In fact the reaction may effectively proceed in the presence of carbon monoxide even with a minimum amount of the catalyst, with which the reaction does not substantially proceed in the absence of the carbon monoxide. To carry out the reaction in the presence of carbon monoxide, it is necessary to forcibly add the carbon monoxide to the reaction system from the exterior. This may be done either by flowing carbon monoxide through a reaction vessel during the reaction, or by charging the reaction vessel with an appropriate amount of carbon monoxide under pressure prior to the reaction. The reaction of an allylamine with a hydro-alkoxy silane, described above, may be carried out in the presence of a cyclic olefinic compound, whereby the selectivity and yield of the gamma-isomer may be further improved. Further, if carbon monoxide co-exists together with the cyclic olefinic compound in the reaction system, the selectivity and yield of the gamma-isomer may be greatly improved and the life of the catalyst may be lengthened, and the amount of the catalyst to be used may be reduced. Of the cyclic olefinic compounds, those having at least 5 carbon atoms and at least one double bond in the molecule are preferred. Examples of such cyclic olefins include, for example, monocyclic olefins, such as cyclopentene, cyclopentadiene, cyclohexene, cyclohexadiene, cycloheptene, cycloheptadiene, cycloheptatriene, cyclooctene, cyclooctadiene, cyclooctatriene and cyclooctatetraene; and condensed binuclear olefins, such as, norbornene and norbornadiene. When the cyclic olefinic compound is used, it is added to the reaction system preferably in an amount of from about 1 to about 1000 moles, more preferably from about 10 to about 100 moles per mole of the rhodium carbonyl complex used as the catalyst. The presence of the cyclic olefinic compound, in the reaction system, in the amount described above suppresses the formation of by- products other than aminopropyl alkoxy silanes, whereby the yield of the gamma-aminopropyl alkoxy silane is improved. Since the cyclic olefinic compound is not very reactive, almost all of the cyclic olefinic compound added to the reaction system remains unchanged after the reaction has been completed. If desired, the cyclic olefinic compound remaining in the reaction system after the reaction may be recovered for re-use. While the invention is illustrated by the following examples, the invention is not limited thereto. Example 1 A three-neck flask equipped with a reflux condenser, stirring rod and thermometer was charged with 14 grams of allylamine (0.25 mole), 41 grams of triethoxy silane (0.25 mole) and 30 ml. of toluene, and heated in an oil bath maintained at a temperature of 110°C. When the temperature of the mixture reached 85°C., 0.22 gram of tetrarhodium dodecacarbonyl was added to the mixture as a catalyst. About 30 minutes after the addition of the catalyst, the reaction temperature reached 110°C. At the end of the period the reaction mixture was subjected to gas chromatography analysis. It was found that gamma-aminopropyl triethoxy silane was obtained in a yield of 68% on an allylamine basis, while the yield of beta-aminopropyl triethoxy silane was 4.9% on an allylamine basis. Example 2 The reaction of allylamine with triethoxy silane as in Example 1 was repeated, except that 0.3 gram of hexarhodium hexadecacaronyl was used as a catalyst, and xylene was used as a solvent, with other conditions remaining the same. After the completion of the reaction, the reaction mixture was subjected to gas chromatography analysis. It was found that the gamma-isomer was obtained in a yield of 71% on an allylamine basis, while the yield of the beta-isomer was 4.4% on an allylamine basis. Example 3 The reaction of allylamine with triethoxy silane as in Example 1 was repeated, except that 0.38 gram of a tetraethylammonium salt of hexarhodium pentadecacaronyl was used as a catalyst, and xylene was used as a solvent, with other conditions remaining the same. After the completion of the reaction, the reaction mixture was subjected to gas chromatography analysis. It was found that the gamma-isomer was obtained in a yield of 51% on an allylamine basis, while the yield of the beta-isomer was 3.5% on an allylamine basis. Example 4 Example 1 was repeated except that the 41 grams of triethoxy silane was replaced with 30.6 grams of trimethoxy silane (0.25 mole) and the catalyst was used in an amount of 0.2 gram. After the completion of the reaction, the reaction mixture was subjected to gas chromatography analysis. It was found that gamma-aminopropyl trimethoxy silane was obtained in a yield of 62% on an allylamine basis, while the yield of beta-aminopropyl triethoxy silane was 4.0% on an allylamine basis. Example 5 A three-neck flask equipped with a reflux condenser, stirring rod and thermometer was charged with 25 grams of allylethylenediamine (0.25 mole), 41 grams of triethoxy silane (0.25 mole) and 30 ml. of n-dodecane and heated in an oil bath maintained at a temperature of 150°C. When the temperature of the mixture reached 130°C., 0.1 gram of tetrarhodium dodecacarbonyl was added to the reaction mixture as a catalyst. After the temperature of the reaction mixture had reached 150°C., the mixture was maintained at this temperature for 30 minutes. After the completion of the reaction, the reaction mixture was subjected to gas chromatography analysis. It was found that gamma-ethylenediaminopropyl triethoxy silane was obtained in a yield of 63% on an allylethylenediamine basis. Example 6 The reaction of allylamine with triethoxy silane as in Example 1 was repeated, except that 0.41 gram of a tetraethylammonium salt of rhodium tetracarbonyl was used as a catalyst, and instead of the toluene xylene was used as a solvent, with other conditions remaining the same. After the completion of the reaction, the reaction mixture was subjected to gas chromatography analysis. It was found that the gamma-isomer was obtained in a yield of 65% on an allylamine basis, while the yield of the beta-isomer was 4.3% on an allylamine basis. Example 7 The reaction of allylamine with triethoxy silane as in Example 1 was repeated, except that 0.251 gram of a tetraethylammonium salt of tetrarhodium undecacarbonyl was used as a catalyst, and instead of the toluene xylene was used as a solvent, with other conditions remaining the same. After the completion of the reaction, the reaction mixture was subjected to gas chromatography analysis. It was found that the gamma-isomer was obtained in a yield of 68% on an allylamine basis, while the yield of the beta-isomer was 4.4% on an allylamine basis. Comparative Example 1 A four-neck flask equipped with a reflux condenser, dropping funnel, stirring rod and thermometer was charged with 41 grams of triethoxy silane (0.25 mole) and a solution of chloroplatinic (IV) acid as a catalyst, in isopropyl alcohol in an amount to provide 2 × 10⁻⁵ mole of platinum. To the mixture heated in an oil bath maintained at a temperature of 120°C, 14 grams of allylamine (0.25 mole) was dropwise added over one hour from the dropping funnel. The mixture was maintained at 120°C. for 9 hours. After the completion of the reaction, the reaction mixture was subjected to gas chromatography analysis. It was found that gamma-aminopropyl triethoxy silane was obtained in a yield of 44% on an allylamine basis, while the yield of beta-aminopropyl triethoxy silane was 10% on an allylamine basis. Comparative Example 2 A four-neck flask equipped with a reflux condenser, dropping funnel, stirring rod and thermometer was charged with 41 grams of triethoxy silane (0.25 mole) and 1.4 grams of rhodium hydride carbonyl-tris(triphenylphosphine) as a catalyst. The mixture was heated to a temperature of 110°C. and 14 grams of allylamine (0.25 mole) was dropwise added over one hour from the dropping funnel. The mixture was maintained at 110°C. for a further hour. At the end of the period, it was revealed by gas chromatography that gamma-aminopropyl triethoxy silane was produced in a yield of 34% on an allylamine basis. The reaction mixture was maintained for further 4 hours. At the end of the period the yields of gamma- and beta-aminopropyl triethoxy silanes reached 71% and 6.9% on an allylamine basis, respectively. Example 8 A 200 ml. flask equipped with a stirrer, thermometer, dropping funnel, CO inlet tube and reflux condenser having a CO outlet tube, was charged with 41 grams of triethoxy silane (0.25 mole), 1.9 milligrams of tetrarhodium dodecacarbonyl (2.5 × 10⁻⁶ mole) and 30 ml. of toluene. While passing carbon monoxide through the flask at a rate of 10 ml./min., the mixture was heated to a temperature of 110°C. under stirring. To the mixture 14 grams of allylamine (0.25 mole) was dropwise added in 2 minutes. After the addition of the allylamine the CO flush, heating and stirring were continued for 30 minutes. It was revealed by gas chromatography that gamma-aminopropyl triethoxy silane was obtained in a yield of 62% on an allylamine basis, while the yield of beta-aminopropyl triethoxy silane was 4% on an allylamine basis. Example 9 Example 8 was repeated except that 30 ml. of nonane was used as a solvent, the allylamine was replaced with 25 grams of N-allylethylenediamine and the reaction mixture was heated to a temperature of 150°C. instead of 120°C. Gas chromatography revealed that the yields of N-(gamma-triethoxysilylpropyl) ethylenediamine and N-(beta-triethoxysilylpropyl) ethylenediamine were 60% and 5% on a starting amine basis, respectively. Example 10 Example 8 was repeated except that the catalyst was replaced with 2.7 milligrams of hexarhodium hexadecacarbonyl (2.5 × 10⁻⁶ mole) and no solvent was used. Gas chromatography revealed that the yields of gamma- and beta-aminopropyl triethoxy silanes were 63% and 4% on a starting amine basis, respectively. Example 11 Example 8 was repeated except that the catalyst was replaced with 3.1 milligrams of a tetraethylammonium salt of hexarhodium pentadecacarbonyl (2.5 × 10⁻⁶ mole) and the triethoxy silane was replaced with 30.5 grams of trimethoxy silane which was dropwise added in admixture with the allylamine. Gas chromatography revealed that the yields of gamma- and beta-aminopropyl trimethoxy silanes were 65% and 5% on a starting amine basis, respectively. Comparative Example 3 Example 8 was repeated except that the carbon monoxide was not caused to flow through the flask and the reaction was carried out under an atmosphere of nitrogen sealed in the flask. It was revealed by gas chromatography that little of both the gamma- and beta-isomers had been produced. Example 12 A 200 ml. flask equipped with a stirrer, thermometer, dropping funnel, CO inlet tube and reflux condenser having a CO outlet tube, was flushed with carbon monoxide and charged with 1.9 milligrams of tetrarhodium dodecacarbonyl (2.5 × 10⁻⁶ mole), 0.027 gram of 1,5 cyclooctadiene (2.5 × 10⁻⁴ mole) and 60 ml. of xylene. While passing carbon monooxide through the flask at a rate of 10 ml./min., the mixture was heated to a temperature of 120°C. under stirring. To the mixture a mixture of 41 grams of triethoxy silane (0.25 mole) and 14 grams of allylamine (0.25 mole) was dropwise added over a period of 30 minutes. After the addition of the reactants, the reaction was carried out at a temperature of 120°C. for 2.5 hours under CO flush and stirring. It was revealed by gas chromatography that gamma-aminopropyl triethoxy silane was obtained in a yield of 75% on an allylamine basis, while the yield of beta-aminopropyl triethoxy silane was 7.5% on an allylamine basis. Example 13 Example 12 was repeated except that the catalyst was replaced with 3.0 milligrams of hexarhodium hexadecacarbonyl (2.8 × 10⁻⁶ mole). Gas chromatography revealed that the yields of gamma- and beta-aminopropyl triethoxy silanes were 76% and 7.4% on a allylamine basis, respectively. Example 14 Example 12 was repeated except that the triethoxy silane was replaced with 30.6 grams of trimethoxy silane (0.25 mole). Gas chromatography revealed that the yields of gamma- and beta-aminopropyl trimethoxy silanes were 69% and 6.5% on a allylamine basis, respectively. Example 15 A three-neck flask equipped with a reflux condenser, stirring rod and thermometer was charged with 14 grams of allylamine (0.25 mole), 41 grams of triethoxy silane (0.25 mole), 0.32 gram of 1,5-cyclooctadieme (2.9 × 10⁻³ mole) and 30 ml. of toluene, and heated in an oil bath maintained at a temperature of 100°C. When the temperature of the mixture reached 85°C., 0.22 gram of tetrarhodium dodecacarbonyl (2.9 × 10⁻⁴ mole) was added to the mixture as a catalyst. About 60 minutes after the addition of the catalyst, the reaction temperature reached 110°C. At the end of the period the reaction mixture was subjected to gas chromatography analysis. It was found that gamma-aminopropyl triethoxy silane was obtained in a yield of 78% on an allylamine basis, while the yield of beta-aminopropyl triethoxy silane was 5.6% on an allylamine basis. Example 16 A 200 ml. flask equipped with a stirrer, thermometer, dropping funnel, CO inlet tube and reflux condenser having a CO outlet tube, was flushed with carbon monoxide, charged with 1.9 milligrams of tetrarhodium dodecacarbonyl (2.5 × 10⁻⁶ mole), 14 grams of allylamine (0.25 mole) and 60 ml. of xylene, and heated in an oil bath maintained at a temperature of 110°C. Thereafter, 41 grams of triethoxy silane (0.25 mole) was dropwise added to the mixture from the dropping funnel over 30 minutes. The reaction was continued at a temperature of 110°C. for 2 hours under stirring and CO flush. It was revealed by gas chromatography that gamma-aminopropyl triethoxy silane was obtained in a yield of 58% on an allylamine basis, while the yield of beta-aminopropyl triethoxy silane was 4.9% on an allylamine basis. It can be seen from the foregoing that we have prepared gamma-aminopropyl alkoxy silanes in a high selectivity and yield within a short period of reaction time. When the reaction is carried out in the presence of carbon monoxide and/or a cyclic olefinic compound, the selectivity and yield of the gamma-isomer can be greatly improved. In addition, the presence of carbon monoxide in the reaction system serves to remarkably lengthen the catalyst life and to greatly reduce the amount of the catalyst to be used.

Claims: 1. A process for preparing aminopropyl alkoxy silanes comprising reacting an allylamine of the formula [I] wherein R₁ is hydrogen, alkyl having from 1 to 10 carbon atoms, alkenyl having from 2 to 10 carbon atoms, phenyl, substituted phenyl, ―CH₂CH₂NHCH₂CH₂NH₂ or ―CH₂CH₂NH₂, and R₂ is hydrogen or alkyl having from 1 to 6 carbon atoms with a hydro-alkoxy silane of the formula [II] wherein R₃ and R₄ are the same or different and each represents alkyl having from 1 to 6 carbon atoms, and n is 0, 1 or 2, in the presence of a rhodium complex having inorganic ligands and being free from any organic ligand, at least one of said ligands being carbonyl. 2. A process according to claim 1 in which the allylamine is selected from allylamine, N-methyl-allylamine, N-ethylallylamine, 2-methylallylamine, diallylamine and allylethylenediamine. 3. A process according to claim 1 or claim 2 in which the hydrosilane is selected from triethoxy silane, trimethoxy silane, tripropoxy silane, tributoxy silane, methyl dimethoxy silane, ethyl dimethoxy silane, methyl diethoxy silane, dimethyl methoxy silane, trioctyloxy silane, methyl dioctyloxy silane and dimethyl octyloxy silane. 4. A process according to any one of claims 1 to 3 in which the rhodium complex is selected from tetrarhodium dodecacarbonyl, hexarhodium hexadecacarbonyl, tetraethylammonium salt of rhodium tetracarbonyl, tetraethylammonium salt of hexarhodium pentadecacarbonyl and tetraethylammonium salt of tetrarhodium undecacarbonyl. 5. A process according to any one of claims 1 to 4 in which the reaction is carried out in the presence of carbon monoxide. 6. A process according to any one of claims 1 to 5 in which the reaction is carried out in the presence of a cyclic olefinic compound. 7. A process according to claim 6 in which the cyclic olefinic compound is selected from cyclopentene, cyclopentadiene, cyclohexene, cyclohexadiene, cycloheptene, cycloheptadiene, cycloheptatriene, cyclooctene, cyclooctadiene, cyclooctatriene, cyclooctatetraene, norbornene and norbornadiene. 8. A process according to any one of claims 1 to 7 in which the reaction is carried out at a temperature between 50°C and 250°C and preferably between 100°C and 200°C. 9. The use of a process according to any one of claims 1 to 8 in the manufacture of a silane coupling agent. 10. The use of a process according to any one of claims 1 to 8 as an intermediate stage in the manufacture of a composite material.

Inventors: IMAI, CHICHIRO, OKAMOTO, NOBUKAZU, OKUMURA, YOSHIHARU, SHIOZAWA, KOUJI, TAKAI, HARUKO, TAKATSUNA, KAZUTOSHI
Applicants: TONEN CORPORATION
Application year: 1988
Main classification: C07F7
IPC codes: C07F7