Epoxidation process

Claim 3

The method of claim 1 wherein the alkyl aryl secondary alcohol is α-methyl benzyl alcohol.

Claim 4

The method of claim 1 wherein said oxidant mixture is produced by contacting the alkyl aryl secondary alcohol with molecular oxygen.

Claim 5

The method of claim 1 wherein said olefin is a C 2 -C 30 olefin.

Claim 6

The method of claim 1 wherein the organorhenium oxide catalyst is selected from the group consisting of: (a) compounds having the general formula R.sup.1.sub.a Re.sub.b O.sub.c wherein a is 1-6, b is 1-4, c is 1-14, Re has a valance of from 5-7, and R 1 is alkyl or aralkyl; (b) compounds having the general formula (R.sup.2 Re).sub.d O.sub.e R.sup.3.sub.f ·L.sub.g wherein d is 1 or 2, e is an integer of from 1 to 3·d, f is 0 or an integer of from 1 to 2·d, g is an integer of from 1 to 3·d, Re has a valance of 5 to 7, R 2 is alkyl or aralkyl, R 3 is alkyl, aralkyl, or aryl, and L is an ligand containging 1 to 3 heteroatoms selected from O and N and coordinated to Re; (c) substances having the general formula (polymer).sub.h ·(R.sup.4.sub.i Re.sub.j O.sub.k).sub.l wherein the polymer has ligand sites containing 1 to 3 heteroatoms selected from O and N and coordinated to Re, the ratio ##EQU3## represents the molar ratio of ##EQU4## and is from 0.01 to 10, i is an integer of from 1 to 6, j is an integer of from 1 to 4, k is an integer of from 1 to 14, Re has a valence of from 5 to 7, and R 4 is alkyl or aralkyl; and (d) mixtures thereof.

Claim 7

The method of claim 1 wherein the oxidant mixture additionally comprises an alkyl aryl ketone.

Claim 8

The method of claim 1 wherein the oxidant mixture additionally comprises water.

Claim 9

The method of claim 1 wherein said contacting is carried out at a temperature in the range of from about -30° C. to 100° C.

Claim 10

The method of claim 1 wherein the concentration of hydrogen peroxide in said oxidant mixture is from about 1 to 10 weight percent.

Claim 11

The method of claim 1 wherein the concentration of alkyl aryl secondary alcohol in said oxidant mixture is at least about 30 weight percent.

Claim 12

The method of claim 1 wherein the molar ratio of hydrogen peroxide to olefin is from about 1:10 to 10:1.

Claim 13

The method of claim 1 wherein the molar ratio of Re in the organorhenium oxide catalyst to hydrogen peroxide is from about 0.01:100 to 1:100.

Claim 16

The method of claim 13 wherein the C 2 -C 30 olefin has the general structure ##STR5## wherein R 5 , R 6 , R 7 , and R 8 are the same or different and are selected from the group consisting of hydrogen, C 1 -C 6 alkyl, C 6 -C 15 aryl, and C 7 -C 20 aralkyl.

Claim 17

The method of claim 13 wherein the C 2 -C 30 olefin is selected from the group consisting of ethylene, propylene, isobutylene, 2-butene, 1-butene, allyl alcohol, cyclohexene, allyl chloride, styrene, 1-octene, butadiene, 1-pentene, 2-pentene, 2,3-dimethyl-2-butene, 2-methyl-2-butene, cyclooctene, stilbene, phenyl allyl ether, α-methyl sytrene, methallyl alcohol, 1-decene, 1-dodecene, 1-hexadecene, 1-hexene, methyl allyl ether, and norbornene.

Claim 18

The method of claim 13 wherein R 2 is methyl, d is 1, e is 3, and f is 0.

Claim 19

The method of claim 13 wherein the ligand is selected from the group consisting of tertiary amines, tertiary amine oxides, aromatic azacycles, and aromatic azacycle oxides.

Claim 20

The method of claim 13 wherein the ligand is selected from the group consisting of pyridine and pyridine N-oxide.

Claim 21

An integrated process for the production of an epoxide comprising the steps of (a) contacting an alkyl aryl secondary alcohol with molecular oxygen under conditions effective to form an oxidant mixture comprised of the alkyl aryl secondary alcohol, an alkyl aryl ketone, and hydrogen peroxide; and (b) contacting the oxidant mixture with an olefin and an organorhenium oxide catalyst under conditions effective to epoxidize the olefin to form an epoxide.

Claim 22

An integrated process for the production of an epoxide comprising the steps of (a) contacting an alkyl aryl secondary alcohol with molecular oxygen under conditions effective to form an oxidant mixture comprised of the alkyl aryl secondary alcohol, an alkyl aryl ketone, and hydrogen peroxide; and (b) contacting the oxidant mixture with an olefin and an organorhenium oxide catalyst under conditions effective to epoxidize the olefin to form an epoxide.

Claim 23

The method of claim 19 comprising the additional step of separating the epoxide from the alkyl aryl secondary alcohol and the alkyl aryl ketone.

Claim 24

The method of claim 20 comprising the additional step of reacting the alkyl aryl ketone with hydrogen in the presence of a transition metal hydrogenation catalyst under conditions effective to convert the alkyl aryl ketone to the alkyl aryl secondary alcohol.

Claim 25

The method of claim 19 wherein the alkyl aryl secondary alcohol is α-methyl benzyl alcohol.

Claim 26

The method of claim 19 wherein step (a) is carried out in the liquid phase.

Claim 27

The method of claim 19 wherein the concentration of hydrogen peroxide in the oxidant stream is from about 1 to 10 weight percent.

Claim 28

An integrated process for the production of an epoxide comprising the steps of (a) contacting α-methyl benzyl alcohol with molecular oxygen in the liquid phase under conditions effective to form an oxidant mixture comprised of at least about 30 weight percent α-methyl benzyl alcohol, acetophenone, from about 1 to 10 weight percent hydrogen peroxide, and water; (b) contacting the oxidant mixture with a C 2 -C 30 olefin and an organorhenium oxide catalyst having the general formula (R.sup.2 Re).sub.d O.sub.e R.sup.3.sub.f ·L.sub.g wherein d is 1 or 2, e is an integer of from 1 to 3·d, f is 0 or an integer of from 1 ti 2·d, g is an integer of from 1 to 3·d, Re has a valence of from 5 to 7, R 2 is alkyl or aralkyl, R 3 is alkyl, aralkyl, or aryl, and L is a ligand containing from 1 to 3 heteroatoms selected from O and N and coordinated to Re at a temperature of from about -30° C. to 100° C. to form an epoxide, the molar ratio of hydrogen peroxide:olefin being from about 1:10 ti 10:1, and the molar ratio of Re in the organorhenium oxide catalyst to hydrogen peroxide being from about 0.01:100 to 1:100; (c) separating the epoxide form the α-methyl benzyl alcohol and acetophenone; and (d) reacting the acetophenone with hydrogen in the presence of a transition metal hydrogenation catalyst to convert the acetophenone to α-methyl benzyl alcohol.

Claim 29

An integrated process for the production of an epoxide comprising the steps of (a) contacting α-methyl benzyl alcohol with molecular oxygen in the liquid phase under conditions effective to form an oxidant mixture comprised of at least about 30 weight percent α-methyl benzyl alcohol, acetophenone, from about 1 to 10 weight percent hydrogen peroxide, and water; (b) contacting the oxidant mixture with a C 2 -C 30 olefin and an organorhenium oxide catalyst having the general formula (R.sup.2 Re).sub.d O.sub.e R.sup.3.sub.f ·L.sub.g wherein d is 1 or 2, e is an integer of from 1 to 3·d, f is 0 or an integer of from 1 ti 2·d, g is an integer of from 1 to 3·d, Re has a valence of from 5 to 7, R 2 is alkyl or aralkyl, R 3 is alkyl, aralkyl, or aryl, and L is a ligand containing from 1 to 3 heteroatoms selected from O and N and coordinated to Re at a temperature of from about -30° C. to 100° C. to form an epoxide, the molar ratio of hydrogen peroxide:olefin being from about 1:10 ti 10:1, and the molar ratio of Re in the organorhenium oxide catalyst to hydrogen peroxide being from about 0.01:100 to 1:100; (c) separating the epoxide form the α-methyl benzyl alcohol and acetophenone; and (d) reacting the acetophenone with hydrogen in the presence of a transition metal hydrogenation catalyst to convert the acetophenone to α-methyl benzyl alcohol.

Claim 30

The method of claim 25 wherein the C 2 14 C 30 olefin is propylene.

Claim 31

The method of claim 25 wherein the organorhenium oxide catalyst has a methyl group attached to Re.

Claim 32

The method of claim 25 wherein L is selected from the group consisting of tertiary amines, tertiary amine oxides, aromatic azacycles, and aromatic azacycle oxides.

Claim 33

The method of claim 25 wherein the temperature is from about 20° C. to 60° C.