초록 ▼

This invention is for a catalyst for conversion of alkanes having two to six carbon atoms per molecule to aromatics. The catalyst is a MFI zeolite with a crystallite size of less than 15 microns with, in addition to silicon and aluminum, germanium as a framework element. Platinum is deposited on the

This invention is for a catalyst for conversion of alkanes having two to six carbon atoms per molecule to aromatics. The catalyst is a MFI zeolite with a crystallite size of less than 15 microns with, in addition to silicon and aluminum, germanium as a framework element. Platinum is deposited on the zeolite. The zeolite may contain other optional tetravalent and trivalent elements in the zeolite framework. The catalyst is synthesized by preparing a zeolite containing aluminum, silicon, germanium and, optionally, other elements in the framework, calcining the zeolite and depositing platinum on the zeolite. The catalyst may be used for aromatization of alkanes, such as propane, to aromatics, such as benzene, toluene and xylenes.

대표청구항 ▼

1. A process for converting a hydrocarbon feed containing alkanes having two to six carbon atoms per molecule to aromatics comprising contacting the hydrocarbon feed at aromatizing conditions with a catalyst to form the aromatics, wherein the catalyst comprises: a) a MFI zeolite having a crystallite

1. A process for converting a hydrocarbon feed containing alkanes having two to six carbon atoms per molecule to aromatics comprising contacting the hydrocarbon feed at aromatizing conditions with a catalyst to form the aromatics, wherein the catalyst comprises: a) a MFI zeolite having a crystallite size of less than 15 microns andb) platinum deposited on the zeolitewherein germanium is a framework element of the zeolite. 2. The process of claim 1 wherein the MFI zeolite has a crystallite size of more than about 0.2 micron. 3. The process of claim 1 wherein the MFI zeolite has a crystallite size from about 1 micron to about 7 microns. 4. The process of claim 1 wherein the MFI zeolite has a crystallite size from about 1 micron to about 4 microns. 5. The process of claim 1 wherein the MFI zeolite has a crystallite size from about 1.5 micron to about 2 microns. 6. The process of claim 1 wherein tin, lead, zirconium, titanium, vanadium, chromium, gallium, boron, indium, thallium, iron, zinc, phosphorus and combinations thereof are framework elements of the zeolite. 7. The process of claim 1 wherein platinum is present in the range of from 0.05% to 3% by weight. 8. The process of claim 1 wherein platinum is present in the range of from 0.15% to 2% by weight. 9. The process of claim 1 wherein platinum is present in the range of from 0.15% to 1.5% by weight. 10. The process of claim 1 wherein the hydrocarbon feed additionally contains sulfur. 11. A process for converting a hydrocarbon feed containing alkanes having two to six carbon atoms per molecule to aromatics comprising contacting the hydrocarbon feed at aromatizing conditions with a catalyst comprising: a MFI zeolite having a crystallite size of less than 15 microns platinum deposited on the zeolite and sulfur; andwherein germanium is a framework element of the zeolite. 12. The process of claim 1, wherein prior to contact with the feed, the catalyst is pretreated with a sulfur compound. 13. The process of claim 12 wherein the sulfur compound is H2S, CnH2n+2S where n=1-20, CnH2n+1S2 where n=2-22 or CnH2n+1S where n=2-22. 14. The process of claim 1 wherein the process is a dehydrocyclodimerization process operating at a temperature of about 350° C. to 650° C. and a pressure of about 10 to 2000 kPa gauge. 15. The process of claim 1 wherein the catalyst additionally comprises a binder selected from oxides of magnesium, aluminum, titanium, zirconium, thorium, silicon, boron or mixtures thereof. 16. The process of claim 15 wherein the binder is an oxide of silicon (silica). 17. The process of claim 1 wherein the catalyst has the formula |H+Pt|[Si91Ge4Al1O192]-MFI. 18. The process of claim 1 wherein the hydrocarbon feed comprises propane. 19. The process of claim 11 wherein the amount of sulfur on the catalyst is about 10 ppm to about 0.1 weight %.