Crystalline zeolite composition (ECR-5) having a cancrinite-like structure and process for its preparation

Claim 2

A crystalline zeolite, being isostructural to cancrinite, in which the twelve-ring channel has a sorption of greater than about 1% by weight hexane, said crystalline zeolite having a composition, in terms of mole ratios of oxides in the range: 1.0 to 1.3 Na.sub.2 O:Al.sub.2 O.sub.3 :2.1 to 8.0 SiO.sub.2.

Claim 3

The zeolite of claim 1 having a composition, in terms of mole ratios of oxides, in the range: 1.0 to 1.3 Na.sub.2 O:Al.sub.2 O.sub.3 :2.4 to 6.0 SiO.sub.2.

Claim 4

The zeolite of claim 1 having a composition, in terms of mole ratios of oxides, in the range: 1.1 to 1.3 Na.sub.2 O:Al.sub.2 O.sub.3 :2.4 to 3.1 SiO.sub.2.

Claim 5

A process for preparing a crystalline zeolite having a composition, in terms of mole ratios of oxides, in the range: 1.0 to 1.3 Na.sub.2 O:Al.sub.2 O.sub.3 :2.1 to 8.0 SiO.sub.2 and being isostructural to cancrinite, in which the twelve-ring channel thereof has a sorption of greater than about 1% by weight hexane, comprising the steps of: (a) preparing a reaction mixture comprising aqueous ammonia, a source of silica-alumina, and sodium hydroxide, said reaction mixture having a composition, in terms of mole ratios of oxides, within the following ranges: Na 2 O:Al 2 O 3 :2 to 17 SiO 2 :Al 2 O 3 :2 to 25 H 2 O:Al 2 O 3 :30 to 450 (H 2 O+NH 3 ):Al 2 O 3 :50 to 600 wherein the ammonia is present in the reaction mixture in an amount of 15 to 30 percent, based on total moles of H 2 O; and (b) maintaining the reaction mixture at a temperature between about 70° and 180° C. and for a time of about 1 to 10 days.

Claim 6

A process for preparing a crystalline zeolite having a composition, in terms of mole ratios of oxides, in the range: 1.0 to 1.3 Na.sub.2 O:Al.sub.2 O.sub.3 :2.1 to 8.0 SiO.sub.2 and being isostructural to cancrinite, in which the twelve-ring channel thereof has a sorption of greater than about 1% by weight hexane, comprising the steps of: (a) preparing a reaction mixture comprising aqueous ammonia, a source of silica-alumina, and sodium hydroxide, said reaction mixture having a composition, in terms of mole ratios of oxides, within the following ranges: Na 2 O:Al 2 O 3 :2 to 17 SiO 2 :Al 2 O 3 :2 to 25 H 2 O:Al 2 O 3 :30 to 450 (H 2 O+NH 3 ):Al 2 O 3 :50 to 600 wherein the ammonia is present in the reaction mixture in an amount of 15 to 30 percent, based on total moles of H 2 O; and (b) maintaining the reaction mixture at a temperature between about 70° and 180° C. and for a time of about 1 to 10 days.

Claim 7

The process of claim 4 wherein the source of silica is a natural or synthetic amorphous aluminosilicate gel or glass.

Claim 8

The process of claim 4 wherein the sources of silica and alumina are a preformed silica-alumina gel having a Si/Al ratio of from 2.2 to 5.0.

Claim 9

The process of claim 6 wherein the preformed silica-alumina gel has a Si/Al ratio of from 1 to 20.

Claim 10

The process of claim 6 wherein the preformed silica-alumina gel is prepared from a reaction mixture comprising sodium silicate, aluminum sulfate, sulfuric acid, water and sodium hydroxide, which has been adjusted to a pH of from 5 to 10, and aged at about 15° to 50° C. for at least about 5 minutes.

Claim 11

The process of claim 4 wherein after step (a) but before step (b) the reaction mixture is blended sufficiently to form a substantially homogeneous mixture.

Claim 12

The process of claim 4 wherein microcrystalline ECR-5 seeds are added to the reaction mixture prior to step (b).

Claim 13

The process of claim 4 wherein the aqueous ammonia contains at least about 15% by weight ammonia.

Claim 14

A process for preparing a crystalline zeolite having a composition, in terms of mole ratios of oxides, in the range: 1.0 to 1.3 Na.sub.2 O.sub.3 :Al.sub.2 O.sub.3 :2.2 to 6.0 SiO.sub.2 and being isostructural with cancrinite, in which the twelve-ring channel thereof has a sorption greater than about 1% by weight hexane, which process comprises: (a) preparing a reaction mixture comprising aqueous ammonia, a preformed alumina-silica gel having a Al/Si ratio of 1 to 10, and sodium hydroxide, said reaction mixture having a composition, in terms of mole ratios of oxides, within the following ranges: Na 2 O:Al 2 O 3 :2.0 to 17 SiO 2 :Al 2 O 3 :2 to 25 H 2 O:Al 2 O 3 :30 to 450 (H 2 O+NH 3 ):Al 2 O 3 :50 to 600 wherein the aqueous ammonia is present in the reaction mixture in an amount of about 15 to 30 percent, based on total moles of H 2 O; (b) blending the reaction mixture sufficiently to form a substantially homogeneous mixture; and (c) maintaining the reaction mixture at a temperature of 70° to 180° C. for 1 to 10 days until crystals of the zeolite are formed.

Claim 15

A process for preparing a crystalline zeolite having a composition, in terms of mole ratios of oxides, in the range: 1.0 to 1.3 Na.sub.2 O.sub.3 :Al.sub.2 O.sub.3 :2.2 to 6.0 SiO.sub.2 and being isostructural with cancrinite, in which the twelve-ring channel thereof has a sorption greater than about 1% by weight hexane, which process comprises: (a) preparing a reaction mixture comprising aqueous ammonia, a preformed alumina-silica gel having a Al/Si ratio of 1 to 10, and sodium hydroxide, said reaction mixture having a composition, in terms of mole ratios of oxides, within the following ranges: Na 2 O:Al 2 O 3 :2.0 to 17 SiO 2 :Al 2 O 3 :2 to 25 H 2 O:Al 2 O 3 :30 to 450 (H 2 O+NH 3 ):Al 2 O 3 :50 to 600 wherein the aqueous ammonia is present in the reaction mixture in an amount of about 15 to 30 percent, based on total moles of H 2 O; (b) blending the reaction mixture sufficiently to form a substantially homogeneous mixture; and (c) maintaining the reaction mixture at a temperature of 70° to 180° C. for 1 to 10 days until crystals of the zeolite are formed.

Claim 16

A process for preparing a crystalline cancrinite zeolite in which the twelve-ring channel thereof has a sorption greater than about 1% by weight hexane, which process comprises the steps of: (a) preparing a reaction mixture comprising aqueous ammonia, a source of silica, metakaolin, sodium hydroxide, said reaction mixture having a composition, in terms of mole ratio of oxides, within the following ranges: Na 2 O:Al 2 O 3 :2 to 17 SiO 2 :Al 2 O 3 :2 to 25 H 2 O:Al 2 O 3 :30 to 450 (H 2 O+NH 3 ):Al 2 O 3 :50 to 600 wherein the ammonia is present in the reaction mixture in an amount of 15 to 30 percent, based on total moles of H 2 O; and (b) maintaining the reaction mixture at a temperature between about 70° and 180° C. for 1 to 10 days until crystals of the zeolite are formed.

Claim 17

A process for preparing a crystalline cancrinite zeolite in which the twelve-ring channel thereof has a sorption greater than about 1% by weight hexane, which process comprises the steps of: (a) preparing a reaction mixture comprising aqueous ammonia, a source of silica, metakaolin, sodium hydroxide, said reaction mixture having a composition, in terms of mole ratio of oxides, within the following ranges: Na 2 O:Al 2 O 3 :2 to 17 SiO 2 :Al 2 O 3 :2 to 25 H 2 O:Al 2 O 3 :30 to 450 (H 2 O+NH 3 ):Al 2 O 3 :50 to 600 wherein the ammonia is present in the reaction mixture in an amount of 15 to 30 percent, based on total moles of H 2 O; and (b) maintaining the reaction mixture at a temperature between about 70° and 180° C. for 1 to 10 days until crystals of the zeolite are formed.