Hydrogenation of unsaturated dinitriles for employing palladium and ruthenium catalyst in aqueous tertiary alkanol

Claim 2

A process for the catalytic hydrogenation of an unsaturated dinitrile feedstock comprising at least one unsaturated dinitrile compound of the formula ##EQU8## wherein each R is independently selected from the group consisting of an alkylene radical and an alkylidene radical, R' is an alkyl radical, and the number of carbon atoms in said compound is in the range of 7 to 30; which comprises contacting, at suitable hydrogenation conditions for the at least substantially complete hydrogenation of said at least one unsaturated dinitrile compound, said feedstock with ammonia; hydrogen; a diluent comprising water and at least one unsubstituted tertiary alkanol, the concentration of the water in the diluent being suitable to permit the desired degree of hydrogenation under said hydrogenation conditions; and a catalyst comprising a first catalyst component selected from the group consisting of elemental palladium and palladium compounds which are reducible by hydrogen to elemental palladium at said hydrogenation conditions, and mixtures thereof, and a second catalyst component selected from the group consisting of elemental ruthenium, ruthenium compounds which are reducible by hydrogen to elemental ruthenium at said hydrogenation conditions, and mixtures thereof, to thereby effect the at least substantially complete hydrogenation of said at least one unsaturated dinitrile compound to the corresponding branched-chain saturated aliphatic diamine.

Claim 3

A process in accordance with claim 1 wherein the water constitutes from about 5 to about 25 weight percent of said diluent.

Claim 4

A process in accordance with claim 2 wherein said suitable hydrogenation conditions comprise a weight ratio of the total of palladium and ruthenium present to the unsaturated dinitriles in the range of about 0.001:100 to about 30:100, a mol ratio of ammonia to cyano groups in the range of about 1:1 to about 25:1, a hydrogen pressure in the range of about 500 to about 5000 psig, a weight ratio of the unsaturated dinitriles to the diluent in the range of about 0.001:100 to about 25:100, a weight ratio of palladium to ruthenium in the range of about 0.1:10 to about 10:1, and a temperature in the range of about 100° C to about 300° C.

Claim 5

A process in accordance with claim 3 wherein said diluent consists essentially of water and tertiary butanol.

Claim 6

A process in accordance with claim 1 wherein the water constitutes from about 6 to about 20 weight percent of said diluent.

Claim 7

A process in accordance with claim 5 wherein said suitable hydrogenation conditions comprise a weight ratio of the total of palladium and ruthenium present to the unsaturated dinitriles in the range of about 0.01:100 to about 5:100, a mol ratio of ammonia to cyano groups in the range of about 1:1 to about 25:1, a hydrogen pressure in the range of about 500 to about 5000 psig, a weight ratio of the unsaturated dinitriles to the diluent in the range of about 0.001:100 to about 22:100, a weight ratio of palladium to ruthenium in the range of about 0.1:10 to about 10:1, and a temperature in the range of about 160° C to about 250° C.

Claim 8

A process in accordance with claim 6 wherein each of said alkylene radical, said alkylidene radical and said alkyl radical has from 1 to 15 carbon atoms, and wherein said tertiary alkanol has from 4 to 12 carbon atoms per molecule.

Claim 9

A process in accordance with claim 7 wherein said at least one unsaturated dinitrile compound comprises a mixture of 5-methyl-4-nonenedinitrile, 2,4-dimethyl-4-octenedinitrile, 2,4-dimethyl-3-octenedinitrile, and 2,4,6-trimethyl-3-heptenedinitrile.

Claim 10

A process in accordance with claim 5, wherein said feedstock further comprises at least one unsaturated dinitrile reactant of the formula ##EQU9## wherein each R" is independently selected from the group consisting of an alkylene radical and an alkylidene radical, and the number of carbon atoms in said reactant is in the range of 6 to 30.

Claim 11

A process in accordance with claim 9 wherein said suitable hydrogenation conditions comprise a weight ratio of the total of palladium and ruthenium present to the unsaturated dinitriles in the range of about 0.1:100 to about 0.6:100, a weight ratio of palladium to ruthenium in the range of about 1:1 to about 5:1, a mol ratio of ammonia to cyano groups in the range of about 7:1 to about 15:1, a hydrogen pressure in the range of about 750 to about 3000 psig, a weight ratio of the unsaturated dinitriles to the diluent in the range of about 0.1:100 to about 20:100, and a temperature in the range of about 165° C to about 225° C; wherein said at least one unsaturated dinitrile compound constitutes at least 5 weight percent of the unsaturated dinitriles in said feedstock; wherein said at least one unsaturated dinitrile compound is converted primarily to a saturated diamine having the formula ##EQU10## wherein R and R' are as defined hereinbefore; wherein said at least one unsaturated dinitrile reactant is converted primarily to a saturated diamine having the formula ##EQU11## wherein R" is as defined hereinbefore; and recovering a diamine product containing less than about 1 weight percent unsaturated diamines.

Claim 12

A process in accordance with claim 10 wherein the water constitutes from about 8 to about 16 weight percent of said diluent.

Claim 13

A process in accordance with claim 11 wherein said first catalyst component is palladium, said second catalyst component is ruthenium, and said diluent consists essentially of water and tertiary butanol.

Claim 14

A process in accordance with claim 12 wherein said feedstock comprises 5-methylene-nonanedinitrile and 5-methyl-4-nonenedinitrile.

Claim 15

A process in accordance with claim 1 further comprising recovering a diamine product containing less than about 1 weight percent unsaturated diamines.

Claim 16

A process in accordance with claim 1 further comprising recovering a diamine product essentially free of unsaturation.

Claim 17

A process for the catalytic hydrogenation of an unsaturated dinitrile feedstock comprising at least one unsaturated dinitrile compound of the formula ##EQU12## wherein each R is independently selected from the group consisting of an alkylene radical and an alkylidene radical, R' is an alkyl radical, and the number of carbon atoms in said compound is in the range of 7 to 30; which comprises contacting, at suitable hydrogenation conditions for the at least substantially complete hydrogenation of said at least one unsaturated dinitrile compound, said feedstock with ammonia; hydrogen; a diluent consisting essentially of water and at least one unsubstituted tertiary aliphatic alcohol having 4 to 12 carbon atoms per molecule, the concentration of water in the diluent being suitable to permit the desired degree of hydrogenation under said hydrogenation conditions; and a catalyst comprising a first catalyst component selected from the group consisting of elemental palladium and palladium compounds which are reducible by hydrogen to elemental palladium at said hydrogenation conditions, and mixtures thereof, and a second catalyst component selected from the group consisting of elemental ruthenium, ruthenium compounds which are reducible by hydrogen to elemental ruthenium at said hydrogenation conditions, and mixtures thereof, to thereby effect the at least substantially complete hydrogenation of said at least one unsaturated dinitrile compound to the corresponding branched-chain saturated aliphatic diamine; said suitable hydrogenation conditions comprising a weight ratio of the total of palladium and ruthenium present to the unsaturated dinitriles in the range of about 0.001:100 to about 30:100, a mol ratio of ammonia to cyano groups in the range of about 1:1 to about 25:1, a hydrogen pressure in the range of about 500 to about 5000 psig, a weight ratio of the unsaturated dinitriles to the diluent in the range of about 0.001:100 to about 25:100, a weight ratio of palladium to ruthenium in the range of about 0.1:10 to about 10:1, and a temperature in the range of about 100°C to about 300°C; and wherein the water constitutes from about 5 to about 25 weight percent of said diluent.

Claim 18

A process for the catalytic hydrogenation of an unsaturated dinitrile feedstock comprising at least one unsaturated dinitrile compound of the formula ##EQU12## wherein each R is independently selected from the group consisting of an alkylene radical and an alkylidene radical, R' is an alkyl radical, and the number of carbon atoms in said compound is in the range of 7 to 30; which comprises contacting, at suitable hydrogenation conditions for the at least substantially complete hydrogenation of said at least one unsaturated dinitrile compound, said feedstock with ammonia; hydrogen; a diluent consisting essentially of water and at least one unsubstituted tertiary aliphatic alcohol having 4 to 12 carbon atoms per molecule, the concentration of water in the diluent being suitable to permit the desired degree of hydrogenation under said hydrogenation conditions; and a catalyst comprising a first catalyst component selected from the group consisting of elemental palladium and palladium compounds which are reducible by hydrogen to elemental palladium at said hydrogenation conditions, and mixtures thereof, and a second catalyst component selected from the group consisting of elemental ruthenium, ruthenium compounds which are reducible by hydrogen to elemental ruthenium at said hydrogenation conditions, and mixtures thereof, to thereby effect the at least substantially complete hydrogenation of said at least one unsaturated dinitrile compound to the corresponding branched-chain saturated aliphatic diamine; said suitable hydrogenation conditions comprising a weight ratio of the total of palladium and ruthenium present to the unsaturated dinitriles in the range of about 0.001:100 to about 30:100, a mol ratio of ammonia to cyano groups in the range of about 1:1 to about 25:1, a hydrogen pressure in the range of about 500 to about 5000 psig, a weight ratio of the unsaturated dinitriles to the diluent in the range of about 0.001:100 to about 25:100, a weight ratio of palladium to ruthenium in the range of about 0.1:10 to about 10:1, and a temperature in the range of about 100°C to about 300°C; and wherein the water constitutes from about 5 to about 25 weight percent of said diluent.

Claim 19

A process in accordance with claim 16 wherein the water constitutes from about 6 to about 20 weight percent of said diluent.

Claim 20

A process in accordance with claim 17 wherein said temperature is in the range of about 160°C to about 250°C.

Claim 21

A process in accordance with claim 18 wherein the water constitutes from 8 to 16 weight percent of said diluent.

Claim 22

A process in accordance with claim 19 wherein said weight ratio of the total of palladium and ruthenium present to the unsaturated dinitriles is in the range of about 0.01:100 to about 5:100.