초록 ▼

A process for improving the catalyst life of zeolites employed in the conversion of alcohols (e.g. methanol) and/or their ether derivatives (e.g., dimethyl ether) wherein a suitable zeolite is modified in a 2-stage procedure by providing a controlled low amount of a coke precursor deposit on the ext

A process for improving the catalyst life of zeolites employed in the conversion of alcohols (e.g. methanol) and/or their ether derivatives (e.g., dimethyl ether) wherein a suitable zeolite is modified in a 2-stage procedure by providing a controlled low amount of a coke precursor deposit on the external surface of the zeolite, and then heating this treated zeolite in an inert gas at specifically controlled temperatures for a minimum time is disclosed. A process of employing this modified zeolite to produce lower olefins is also disclosed.

대표청구항 ▼

1. A process for modifying a crystalline shape selective acidic metalosilicate zeolite free of coke deposits thereon, wherein said metal of the metalosilicate is selected from the group consisting of aluminum, gallium and mixtures thereof to improve the catalyst life thereof when said modified zeoli

1. A process for modifying a crystalline shape selective acidic metalosilicate zeolite free of coke deposits thereon, wherein said metal of the metalosilicate is selected from the group consisting of aluminum, gallium and mixtures thereof to improve the catalyst life thereof when said modified zeolite is used to convert a hydrocarbon feed comprising at least one member selected from the group consisting of monohydric alcohols having from 1 to about 4 carbon atoms, ethers derived from said alcohols, and mixtures thereof, to an olefin containing product at a conversion reaction temperature of from about 300° to about 350° C., which zeolite, prior to said modification, is: (a) capable of catalyzing said hydrocarbon conversion reaction; (b) has a channel size and structure such as to permit (i) entry of the hydrocarbon feed into the zeolite and diffusion to the active acid sites within the zeolite, and (ii) formation of olefin products within said zeolite and diffusion of said products out of the zeolite; and (c) hydrothermally stable at temperatures of at least about 290° C.; which process comprises: (A) contacting said zeolite with coke precursor forming hydrocarbon feed from a period of from about 0.5 to about 4 hours, said coke precursor forming hydrocarbon feed being (i) comprised of at least one member selected from the group consisting of monohydric alcohols having from 1 to about 4 carbon atoms, ethers derived from said alcohols, olefins having from about 1 to about 5 carbon atoms, and mixtures thereof; and (ii) heated to a temperature of from about 320° to about 350° C.; and (B) contacting the zeolite, treated in accordance with Step (A), with an inert gas heated to a temperature of from about 350° to about 425° C. for a period of at least 1 hour, the inert gas being selected from the group consisting of nitrogen, helium, argon, methane and mixtures thereof. 2. The process of claim 1 wherein Step (A) of the zeolite modification is conducted by contacting said zeolite with a vaporized coke precursor forming hydrocarbon feed selected from the group consisting of ethylene, propylene, butene, methanol, dimethyl ether, propanol, butanol and mixtures thereof, at a temperature of from about 330° to about 340° C. for a period of from about 1 to about 2 hours. 3. The process of claim 1 wherein in Step (A) of the zeolite modification said coke precursor forming hydrocarbon is methanol and said inert gas in Step (B) is nitrogen. 4. The process of any one of claims 1 to 3 wherein the zeolite which is modified is ZSM-5.