Alcohol dehydration employing a zinc aluminate catalyst

Claim 2

The dehydration to an olefin of a dehydratable saturated alcohol which comprises subjecting the same to dehydrating conditions in the presence of a zinc aluminate dehydration catalyst having an approximate molar ratio of ZnO to Al 2 O 3 of one, said catalyst having been heated in air for a sufficient time and at a sufficient temperature to form a catalytically active zinc aluminate suitable for said dehydration.

Claim 3

A process according to claim 1 wherein the alcohol contains from 2 to about 25 carbon atoms per molecule.

Claim 4

A process according to claim 2 wherein the alcohol is represented by the formula: ##STR5## wherein each of R, R', R", and R"' is independently chosen from a group consisting of hydrogen, alkyl radicals, cycloalkyl radicals, said radicals contain from 1 to about 23 carbon atoms per radical, any of said alkyl or cycloalkyl radicals can contain aryl or substituted aryl radicals with the substituents being one or more or a mixture of alkyl or alkoxy radicals and with the limitation that said aryl or substituted aryl radicals must be located at least two carbon atoms from the alcohol oxygen, and any two of R, R', R", and R"' can be combined to form a mono- or bicyclic system with the limitation that any cyclic ring bearing an alcohol group must contain at least 4 carbon atoms in the ring.

Claim 5

A process according to claim 3 wherein the alcohol contains from 5 to about 25 carbon atoms per molecule and is represented by the formula: ##STR6## wherein each of R IV and R V is independently chosen from a group consisting of alkyl radicals containing from 1 to about 20 carbon atoms per radical and wherein R IV and R V can be taken together to form a mono- or bicyclic system having at least 4 carbon atoms in a ring bearing an alcohol group.

Claim 6

A process according to claim 1 wherein the alcohol is at least one selected from: ______________________________________ ethanol 1-hexadecanol 2-methyl-1-pentanol 1-propanol 1-octadecanol 2-ethyl-1-hexanol 2-propanol 1-eicosanol 2-methyl-1-decanol 1-butanol 1-docosanol 2-ethyl-1-octadecanol 2-butanol 1-pentacosanol 2-methyl-1-eicosanol 1-pentanol cyclobutanol 2-methyl-1-docosanol 2-pentanol cyclopentanol cyclobutylmethanol 3-pentanol cyclohexanol cyclopentylmethanol 3-methyl-1- cyclooctanol cyclohexylmethanol butanol 1-hexanol cyclodocecanol cyclotetradecylmethanol 2-hexanol cyclodocosanol bicyclo[2.2.1]hept-2- 3-hexanol 4-methyl-2-pentanol ylmethanol 1-heptanol 5,5-dimethyl-1-hexanol bicyclo[2.2.2] 1-octanol 5-phenyl-1-pentanol oct-2-ylmethanol 2-octanol 8-phenyl-2-octanol 1-nonanol 2-methyl-2-pentanol 2-nonanol 1-methyl-1-cyclohexanol 1-decanol 2-methyl-1-cyclohexanol 1-undecanol bicyclo[2.2.2]octan-2-ol 1-dodecanol bicyclo[3.2.0]heptan-3-ol 1-tridecanol bicyclo[2.2.1]heptan-2-ol 1-tetradecanol 2-methyl-1-butanol 2-tetradecanol 2-ethyl-1-butanol ______________________________________

Claim 7

A process according to claim 1 wherein the catalyst is prepared by mixing together ZnO and Al 2 O 3 in a molar ratio in the approximate range 1/0.95 to 1/1.1.

Claim 8

A process according to claim 1 wherein the catalyst prior to use is calcined at a temperature in the approximate range 700-1400° C. for about 0.1 to about 30 hours.

Claim 9

A process according to claim 7 wherein the catalyst is calcined at a temperature in the approximate range 800-1200° C. for a period of time of from about 1 to about 20 hours.

Claim 10

A process according to claim 1 wherein the dehydration to olefin is affected at a temperature in the approximate range 200-600° C.

Claim 11

A process according to claim 9 wherein the dehydration is affected in the approximate range of from 250-450 ° C.

Claim 12

A process according to claim 1 wherein 2-methyl-1-butanol is converted to 2-methyl-1-butene.

Claim 13

A process according to claim 1 wherein the alcohol is 1-pentanol.

Claim 14

A process according to claim 1 wherein the alcohol is 2-pentanol.

Claim 15

A process according to claim 1 wherein the alcohol is 3-methyl-1-butanol.

Claim 16

A process according to claim 1 wherein the alcohol is cyclohexanol.