Process for the preparation of N-substituted aminoalkylsilanes

Claim 2

A process for selectively preparing an N-substituted aminoalkylsilane which comprises reacting a primary or secondary amine with a cyanoalkylsilane in the presence of hydrogen gas and a heterogeneous hydrogenation catalyst selected from the group consisting of rhodium, platinum and palladium.

Claim 3

The process of claim 1 wherein the primary or secondary amine is selected from the group of amines having the structural formula: ##STR4## wherein R 1 and R 2 are individually substituted or unsubstituted alkyl or aryl groups having from 1 to 12 carbon atoms; R 3 and R 4 are individually hydrogen or a substituted or unsubstituted alkyl, aryl or alkyleneamine group containing 1 to 12 carbon atoms; A is a divalent 4, 5, or 6 membered chain wherein the chain members are only carbon or carbon and one member selected from the group or oxygen, sulfur, and an amino moiety; x is an integer from 0 to 3; n is an integer from 2 to 4; and z is an integer from 1 to 2.

Claim 4

The process of claim 1 wherein the cyanoalkylsilane is of the formula: (R.sup.1 O).sub.x (R.sup.2).sub.3-x Si(C.sub.n-1 H.sub.2n-2)CN wherein R 1 , R 2 , n and x are as defined in claim 2.

Claim 5

The process of claim 1 wherein the ratio of primary or secondary amine to cyanoalkylsilane is 1 to 10.

Claim 6

The process of claim 1 wherein the hydrogen pressure is from 50 psig to 1000 psig.

Claim 7

The process of claim 1 wherein the reaction temperature is 25° to 180° C.

Claim 8

The process of claim 1 wherein the catalyst is rhodium.

Claim 9

The process of claim 1 wherein the catalyst is platinum.

Claim 10

The process of claim 1 wherein the catalyst is palladium.

Claim 11

The process of claim 1 wherein the reaction takes place in a solvent.

Claim 12

The process of claim 10 wherein the solvent is an aromatic hydrocarbon or aliphatical alcohol.

Claim 13

The process of claim 11 wherein the aliphatic alcohol is methanol or ethanol.

Claim 14

A process for selectively preparing an N-substituted aminoalkylsilane of the formula: ##STR5## which process comprises reacting a primary or secondary amine selected from the group of amines consisting of: ##STR6## with a cyanoalkylsilane of the formula: (R.sup.1 O).sub.x (R.sup.2).sub.3-x Si(C.sub.n-1 H.sub.2n-2)CN wherein R 1 and R 2 are individually substituted or unsubstituted alkyl or aryl groups having from 1 to 12 carbon atoms; R 3 and R 4 are individually hydrogen or a substituted or unsubstituted alkyl, aryl or alkyleneamine group containing 1 to 12 carbon atoms; A is a divalent 4, 5, or 6 membered chain wherein the chain members are only carbon or carbon and one member selected from the group of oxygen, sulfur, and an amino moiety; x is an integer from 0 to 3; n is an integer from 2 to 4; and z is an integer from 1 to 2; at 25° to 180° C. in the presence of hydrogen gas, said hydrogen gas having a pressure of from 50 psig to 1000 psig, and in the presence of a heterogeneous hydrogenation catalyst selected from the group consisting of rhodium, platium and palladium, where the ratio of primary or secondary amine to cyanoalkylsilane is 1 to 10 and where the reaction occurs in an aromatic hydrocarbon or aliphatic alcohol solvent.

Claim 15

A process for selectively preparing an N-substituted aminoalkylsilane of the formula: ##STR5## which process comprises reacting a primary or secondary amine selected from the group of amines consisting of: ##STR6## with a cyanoalkylsilane of the formula: (R.sup.1 O).sub.x (R.sup.2).sub.3-x Si(C.sub.n-1 H.sub.2n-2)CN wherein R 1 and R 2 are individually substituted or unsubstituted alkyl or aryl groups having from 1 to 12 carbon atoms; R 3 and R 4 are individually hydrogen or a substituted or unsubstituted alkyl, aryl or alkyleneamine group containing 1 to 12 carbon atoms; A is a divalent 4, 5, or 6 membered chain wherein the chain members are only carbon or carbon and one member selected from the group of oxygen, sulfur, and an amino moiety; x is an integer from 0 to 3; n is an integer from 2 to 4; and z is an integer from 1 to 2; at 25° to 180° C. in the presence of hydrogen gas, said hydrogen gas having a pressure of from 50 psig to 1000 psig, and in the presence of a heterogeneous hydrogenation catalyst selected from the group consisting of rhodium, platium and palladium, where the ratio of primary or secondary amine to cyanoalkylsilane is 1 to 10 and where the reaction occurs in an aromatic hydrocarbon or aliphatic alcohol solvent.

Claim 16

The process of claim 13 wherein the solvent is methanol or ethanol.

Claim 17

The process of claim 13 wherein the catalyst is rhodium, the temperature is from 100° to 150° C. and the hydrogen pressure is from 400 to 700 psig.

Claim 18

The process of claim 13 wherein the catalyst is platinum, the temperature is from 130° to 170° C. and the hydrogen pressure is from 300 to 750 psig.

Claim 19

The process of claim 13 wherein the catalyst is palladium, the temperature is from 150° to 170° C., the hydrogen pressure is 50 to 750 psig and in the absence of an alkanal solvent.