Catalyst for the conversion of oxygenates to olefins and a process for preparing said catalyst
A catalyst for the conversion of oxygenates, such as alcohols or ethers, to olefins consists essentially of a selected SUZ-4 zeolite that has a Si/Al ratio of at least 20, preferably between 20 and 500, especially between 20 and 100. The basic SUZ-4 zeolite is prepared in a manner known per se, whereafter the Si/Al ratio is increased to the desired value. The selected SUZ-4 zeolite catalyst of the invention has a longer life time and a better product selectivity than the conventional/standard SUZ-4 zeolite catalysts.
1. A zeolite catalyst for converting above 99% of oxygenates to olefins, wherein said catalyst is selective to production of C2 and C3 alkenes and consists essentially of a SUZ-4 needle-shaped zeolite, wherein the zeolite has a bulk molar Si/Al ratio of between above 20 and 500.
2. Catalyst according to claim 1 , wherein the zeolite has a bulk molar Si/Al ratio up to 100.
3. A process for the preparation of the needle-shaped catalyst according to claim 1 , said method comprising the steps of:
(a) providing a conventional/standard SUZ-4 zeolite gel having a bulk molar Si/Al ratio of less than 20,
(b) adjusting the Si/Al ratio of the conventional/standard SUZ-4 zeolite with a bulk molar ratio of less than 20, either contacting the gel with a different level of aluminum dissolved in a KOH to increase the Si/Al ratio to above 20, and crystallizing (b) to obtain a SUZ-4 zeolite having an Si/Al ratio of greater than 20 and needle shaped crystals, or contacting the gel of step (b) with steam at a temperature of 400-700° C., followed by washing to form needle-shaped crystals.
4. Process according to claim 3 , wherein step (b) is performed for 1-12 hours by feeding 1-20 g H 2 O per g of catalyst per hour.
5. Process according to claim 3 , wherein the SUZ-4 catalyst resulting from step (b) is washed with an aqueous acid solution.
6. A method of converting oxygenates to olefins comprising contacting the catalyst according to claim 1 with a C 1 to C 4 oxygenate to produce an olefin.
7. The method according to claim 6 , wherein the oxygenates are selected from the group consisting of C1 to C4 alcohols.
8. The method according to claim 7 , wherein the oxygenate is methanol.