Stabilized and dealuminated omega zeolite

Claim 2

In a process for the catalytic cracking of hydrocarbons comprising contacting a hydrocarbon feedstock under cracking conditions with a cracking catalyst, the improvement wherein the catalyst contains an Ω zeolite whose SiO 2 /Al 2 O 3 molar ratio is higher than 10, whose sodium content is lower than 0.3% by weight, whose crystalline parameters "a" and "c" are respectively lower than 1.814 nm and 0.760 nm and which further exhibits a nitrogen adsorption capacity at 77 K (under a partial pressure P/Po equal to 0.19) higher than 5% by weight, said zeolite having a lattice of mesopores of radii ranging from 1.5 nm to 14 nm, the volume of the mesopores being equal to 5-70% of the zeolite total pore volume.

Claim 3

A process according to claim 1, wherein the crystalline parameter a of the Ω zeolite ranges from 1.814 nm to 1.794 nm, the crystalline parameter c being from 0.760 nm to 0.749 nm.

Claim 4

A process according to claim 2, wherein the sodium content of the zeolite is lower than 0.01% by weight.

Claim 5

A process according to claim 2, wherein the Ω zeolite exhibits a nitrogen adsorption capacity of 77 K (under a partial pressure P/Po equal to 0.19) higher than 11% by weight, said zeolite having a lattice of mesopores whose radii range from 2 nm to 6 nm, the volume of the mesopores being equal to 5-50% of the zeolite total pore volume.

Claim 6

A process according to claim 1, wherein the catalyst is produced from a synthetic omega zeolite containing alkali cations and organic cations and having a SiO 2 /Al 2 O 3 molar ratio of 6.5-10, said treatment comprising: (a) a first step wherein the zeolite is subjected (i) to a removal of organic cations by roasting the zeolites for more than 20 minutes, in an inert gas and oxygen, wherein the molar content of oxygen is higher than 2%, and the temperature is 450°-650° C., (ii) to a removal of alkali metal cations by at least one cation exchange at 0°-150° C., in a solution of an ionizable ammonium salt, (b) a second step wherein the product of (a) is subjected to at least one roasting, at a temperature of 500°-900° C., in the presence of steam, for a time of more than 1/2 hour, and to at least one acid etching at a temperature of 0°-150° C., wherein the normality of the acid is 0.1-10N and the volume/weight ratio is 2-10 cm 3 /g, for a time of more than 1/2 hour.

Claim 7

A process according to claim 5, wherein, during the second step, the synthetic zeolite is subjected to at least one roasting in air or inert atmosphere at a temperature from 500° to 850° C., the temperature of the acid etching being from 0° to 150° C.

Claim 8

A process according to claim 1, wherein the catalyst contains at least one metal from the rare-earths group.

Claim 9

A process according to claim 2, wherein the catalyst contains at least one metal from the rare-earths group.

Claim 10

A process according to claim 3, wherein the catalyst contains at least one metal from the rare-earths group.

Claim 11

A process according to claim 4, wherein the catalyst contains at least one metal from the rare-earths group.

Claim 12

A process according to claim 5, wherein in step (b) the zeolite is roasted for more than 1 hour and the normality of the acid is 0.5-2N.

Claim 13

A process according to claim 5, wherein in step (b) the zeolite is roasted for 2 hours at 600°-650° C.