Chabazite synthesis method including organic and inorganic structure directing agents and chabazite zeolite with flake-like morphology

1. A method of synthesizing a zeolite having a CHA crystalline framework, the method comprising:

preparing a mixture of water, an aluminum source, a silica source, a source of an organic structure directing agent, and an inorganic structure-directing agent to form a synthesis gel, wherein the inorganic structure-directing agent is a source of potassium cations; and

subjecting the synthesis gel to a crystallization process to crystallize the zeolite having the CHA crystalline framework,

wherein the source of the organic structure-directing agent is N,N,N-trimethyl-1-adamantylammonium hydroxide (TMAda) and an amount of TMAda and an amount of the potassium cation source is such that a molar ratio of potassium cations to N,N,N-trimethyl-1-adamantylammonium cations are in a molar ratio ranging from about 1 to about 20.

2. The method of claim 1 , wherein the source of the potassium cations is potassium hydroxide.

3. The method of claim 1 , wherein preparing comprises:

a first mixing step comprising adding the source of the organic structure-directing agent, the source of the inorganic structure-directing agent, and the source of aluminum to the water to form an aluminum-containing aqueous solution;

mixing the aqueous solution for a first time period; and

a second mixing step comprising adding the source of silicon to the aluminum-containing aqueous solution and mixing for a second time period to form an aluminosilicate-containing solution.

4. The method of claim 1 , wherein the crystallization process comprises mixing the synthesis gel at a temperature ranging from about 140° C. to about 200° C. for a time period of from about 24 hours to about 6 days.

5. The method of claim 1 , wherein a OH/Si ratio of the synthesis gel is from about 0.1 to about 0.5.

6. The method of claim 1 , wherein a ratio of the silicon source to the aluminum source to TMAda to the potassium cation source to the water is represented by the formula:

1SiO 2 /0.033Al 2 O 3 /X TMA da OH/0.5*(0.5−X)K 2 O/44 H 2 O;

wherein the value of X is from 0.01 to 0.25.

7. The method of claim 1 , wherein:

the zeolite having the CHA crystalline framework is an intergrowth zeolite comprising a first CHA phase and a second CHA phase;

the first CHA phase and the second CHA phase each independently have a unit cell volume of from about 2338 Å 3 to 2489 Å 3 ; and

the unit cell volume of the first CHA phase is different from the unit cell volume of the second CHA phase.

8. The method of claim 7 , wherein:

the first CHA phase and the second CHA phase each independently have a silica-to-alumina ratio (SAR) of from about 4 to about 100; and

the SAR of the first CHA phase is different from the SAR of the second CHA phase.

9. The method of claim 7 , wherein:

the first CHA phase represents from about 5% to about 95% of the intergrowth zeolite;

the first CHA phase has a potassium cation to aluminum ratio of greater than 0.5; and

the second CHA phase has a potassium cation to aluminum ratio of less than about 0.5.

10. The method of claim 7 , wherein the intergrowth zeolite crystal size ranges from about 0.1 to about 15 μm.

11. A method of synthesizing a zeolite material having a CHA crystalline framework and a predominantly flake-like morphology, the method comprising:

preparing a mixture of water, an aluminum source, a silicon source, an organic structure directing agent, and an inorganic structure directing agent to form a synthesis gel, wherein the inorganic structure directing agent comprises potassium cations; and

subjecting the synthesis gel to a crystallization process to crystallize the zeolite material,

wherein the inorganic structure directing agent is potassium hydroxide and the organic structure directing agent is N,N,N-trimethyl-1-adamantylammonium hydroxide (TMAdaOH), and an amount of TMAdaOH and an amount of potassium cations present in the synthesis ge I is such that a molar ratio of potassium cations to TMAdaOH is about 10 or greater.

12. The method of claim 11 , wherein preparing comprises:

a first mixing step comprising adding the organic structure-directing agent, the inorganic structure-directing agent, and the source of aluminum to the water to form an aluminum-containing aqueous solution;

mixing the aqueous solution for a first time period; and

a second mixing step comprising adding the source of silicon to the aluminum-containing aqueous solution and mixing for a second time period to form an aluminosilicate-containing solution.

13. The method of claim 11 , wherein the crystallization process comprises mixing the synthesis gel at a temperature ranging from about 100° C. to about 200° C. for a time period ranging from about 12 hours to about 6 days.

14. The method of claim 13 , wherein the temperature ranges from about 160° C. to about 180° C.

15. The method of claim 11 , wherein the organic structure-directing agent further comprises at least one selected from the group consisting of trimethylcyclohexylammonium hydroxide, tetraethylammonium hydroxide, benzyltrimethylammonium hydroxide, 1,1,3,5-tetramethylpiperidinium hydroxide, choline hydroxide, N,N-dimethyl piperidinium hydroxide, trimethyl-2-ammonium exo-norbornane, and N-methyl-3-quinuclidinol.

16. The method of claim 11 , wherein the source of aluminum selected from the group consisting of a zeolite, aluminum isopropoxide, and aluminum hydroxide.

17. The method of claim 11 , wherein the source of silicon is selected from the group consisting of colloidal silica, a silicon alkoxide, fumed silica, amorphous silica, and an aluminosilicate, and combination thereof.