Cycloalkane oxidation catalysts and method to produce alcohols and ketones
Disclosed is a method of oxidizing a cycloalkane to form a product mixture containing a corresponding alcohol and ketone, said method comprising contacting a cycloalkane with a hydroperoxide in the presence of a catalytic effective amount of a crystalline MWW-type titanosilicate catalyst. Hydroperoxides may notably be tert-butyl hydroperoxide, tert-amyl hydroperoxide, cumene hydroperoxide, ethylbenzene hydroperoxide, cyclohexyl hydroperoxide, methylcyclohexyl hydroperoxide, tetralin hydroperoxide, isobutylbenzene hydroperoxide, and ethylnaphthalene hydroperoxide.
1. A method of oxidizing a cycloalkane to form a product mixture containing a corresponding alcohol and ketone, said method comprising contacting a cycloalkane with a hydroperoxide in the presence of a catalytically effective amount of a crystalline MWW-type titanosilicate catalyst.
2. A method according to claim 1 , in which the hydroperoxide is chosen in the group consisting of: tert-butyl hydroperoxide, tert-amyl hydroperoxide, cumene hydroperoxide, ethylbenzene hydroperoxide, cyclohexyl hydroperoxide, methylcyclohexyl hydroperoxide, tetralin hydroperoxide, isobutylbenzene hydroperoxide, and ethylnaphthalene hydroperoxide.
3. A method according to claim 1 , in which the hydroperoxide is added to the cycloalkane at the start of the step of contacting.
4. A method according to claim 1 , in which the hydroperoxide is generated in situ by reaction of a cycloalkane with oxygen or an oxygen generator.
5. A method according to claim 1 , in which the MWW structure is represented by the following chemical composition formula:
x TiO 2 .(1− x )SiO 2 ,
wherein x is between 0.0001 and 0.5.
6. A method according to claim 1 , in which the catalyst further comprises one or more heteroatoms from the group consisting of the elements of Periods IB, IVB, VB, VIB, VIIB, VIIIB and VA.
7. A method according to claim 1 , in which the contacting is at a temperature of between 20 and 200° C.
8. A method according to claim 1 , in which pure oxygen, air, oxygen-enriched air, oxygen-depleted air, or oxygen diluted with an inert gas is used in a reaction medium.
9. A method according to claim 1 , in which the catalyst is used in a range of between 1 and 10 wt. %, in relation to the total weight of the reaction medium.