Method for manufacturing vinylalkoxysilanes

Claim 2

A process for producing a vinylalkoxysilane which comprises (i) gradually feeding to a reaction zone an alkoxysilane of the formula HSi(OR') n R" 3-n where R' and R" can individually be the same or different and are selected from primary alkyl groups of 1 to 6 carbon atoms and n is 1, 2 or 3, said reaction zone containing an alkyne of the formula RC.tbd.CH where R is hydrogen or a monovalent hydrocarbon radical of 1 to 10 carbon atoms and a platinum hydrosilation catalyst; (ii) contacting said alkyne and said alkoxysilane in said reaction zone in the presence of said platinum hydrosilation catalyst and less than 0.1 weight percent ionic chloride and alkyl amine to form vinylalkoxysilane; and (iii) recovering said vinylalkoxysilane from said reaction zone.

Claim 3

A process for producing a vinylalkoxysilane which comprises (i) co-feeding to a reaction zone an alkyne of the formula RC.tbd.CH where R is hydrogen or a monovalent hydrocarbon radical of 1 to 10 carbon atoms and an alkoxysilane of the formula HSi(OR') n R" 3-n where R' and R" can individually be the same or different and are selected from primary alkyl groups of 1 to 6 carbon atoms and n is 1, 2 or 3; (ii) contacting said alkyne and said alkoxysilane in said reaction zone in the presence of a platinum hydrosilation catalyst and less than 0.1 weight percent ionic chloride and alkyl amine to form vinylalkoxysilane; and (iii) recovering a product stream containing said vinylalkoxysilane from said reaction zone.

Claim 4

A process for producing a vinylalkoxysilane which comprises (i) co-feeding to a reaction zone an alkyne of the formula RC.tbd.CH where R is hydrogen or a monovalent hydrocarbon radical of 1 to 10 carbon atoms and an alkoxysilane of the formula HSi(OR') n R" 3-n where R' and R" can individually be the same or different and are selected from primary alkyl groups of 1 to 6 carbon atoms and n is 1, 2 or 3; (ii) contacting said alkyne and said alkoxysilane in said reaction zone in the presence of a platinum hydrosilation catalyst and less than 0.1 weight percent ionic chloride and alkyl amine to form vinylalkoxysilane; and (iii) recovering a product stream containing said vinylalkoxysilane from said reaction zone.

Claim 5

The process of claim 2 wherein said alkyne is acetylene.

Claim 6

The process of claim 1, 2 or 3 wherein R' and R" are selected from primary alkyl groups of 1 to 4 carbon atoms.

Claim 7

The process of claim 1, 2 or 3 wherein said alkoxysilane is selected from the group consisting of trimethoxysilane, triethoxysilane, tris(methoxyethoxy)silane, tributoxysilane, methyldimethoxysilane, dimethylmethoxysilane, methyldiethoxysilane, tripropoxysilane, tripentoxysilane, and tris(2-ethylhexoxy)silane.

Claim 8

The process of claim 1, 2 or 3 wherein said alkoxysilane is selected from trimethoxysilane and triethoxysilane.

Claim 9

The process of claim 1, 2 or 3 where said platinum hydrosilation catalyst is chloroplatinic acid.

Claim 10

The process of claim 1, 2 or 3 where said reaction zone is at a pressure of less than 75 psia.

Claim 11

The process of claim 8 wherein said pressure is less than 25 psia.

Claim 12

The process of claim 1, 2 or 3 wherein said reaction zone has a temperature between about 50° and about 150° C.

Claim 13

The process of claim 10 wherein said temperature is between about 85° and about 150° C.

Claim 14

The process of claim 1, 2 or 3 wherein said alkoxysilane is produced by direct reaction between silicon and methanol.

Claim 15

The process of claim 1, 2 or 3 wherein said contacting is done in the presence of a solvent selected from the group consisting of cumene, toluene, xylene, o-dichlorobenzene, vinylalkoxysilane, bis(alkoxysilyl)alkane and mixtures thereof.

Claim 16

The process of claim 7 wherein said reaction zone contains phenothiazine.

Claim 17

A continuous process for producing a vinylalkoxysilane which comprises (i) co-feeding into a reaction zone an alkyne and an alkoxysilane wherein said alkyne is fed into said reaction zone at a rate which keeps the molar ratio of said alkyne to said alkoxysilane in said reaction zone between about 1.0 to 10.0, said alkyne having a formula RC.tbd.CH where R is hydrogen or a monovalent hydrocarbon radical of 1 to 10 carbon atoms and said alkoxysilane having a formula HSi(OR') n R" 3- n where R' and R" can individually be the same or different and are selected from primary alkyl groups of 1 to 6 carbon atoms and n is 1, 2 or 3, (ii) contacting said alkyne and said alkoxysilane in said reaction zone in the presence of a platinum hydrosilation catalyst and less than 0.1 weight percent ionic chloride and alkyl amine to form vinylalkoxysilane; and (iii) simultaneously removing a product stream containing said vinylalkoxysilane from said reaction zone.

Claim 18

A continuous process for producing a vinylalkoxysilane which comprises (i) co-feeding into a reaction zone an alkyne and an alkoxysilane wherein said alkyne is fed into said reaction zone at a rate which keeps the molar ratio of said alkyne to said alkoxysilane in said reaction zone between about 1.0 to 10.0, said alkyne having a formula RC.tbd.CH where R is hydrogen or a monovalent hydrocarbon radical of 1 to 10 carbon atoms and said alkoxysilane having a formula HSi(OR') n R" 3- n where R' and R" can individually be the same or different and are selected from primary alkyl groups of 1 to 6 carbon atoms and n is 1, 2 or 3, (ii) contacting said alkyne and said alkoxysilane in said reaction zone in the presence of a platinum hydrosilation catalyst and less than 0.1 weight percent ionic chloride and alkyl amine to form vinylalkoxysilane; and (iii) simultaneously removing a product stream containing said vinylalkoxysilane from said reaction zone.

Claim 19

The process of claim 15 wherein said alkyne is acetylene.

Claim 20

The process of claim 16 wherein said alkoxysilane is selected from trimethoxysilane and triethoxysilane.

Claim 21

The process of claim 17 where said platinum hydrosilation catalyst is chloroplatinic acid.

Claim 22

The process of claim 18 where said reaction zone is at an acetylene pressure of less than about 75 psia.

Claim 23

The process of claim 15 wherein said reaction zone has a temperature between about 50° and about 150° C.

Claim 24

The process of claim 16 or 17 wherein said alkoxysilane is produced by direct reaction between silicon and methanol.

Claim 25

The process of claim 15 wherein the feed rate of said alkyne keeps the molar ratio in said reaction zone between 1.0 and 5.0.

Claim 26

The process of claim 18 wherein said reaction zone contains phenothiazine.

Claim 27

The process of claim 16 or 19 wherein said acetylene is feed into said reaction zone at a rate needed to maintain a substantially constant pressure in said reaction zone.