Processes using molecular sieve SSZ-27
US-9505627-B1 · Nov 29, 2016 · US
US2016340199A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2016340199-A1 |
| Application number | US-201514719059-A |
| Country | US |
| Kind code | A1 |
| Filing date | May 21, 2015 |
| Priority date | May 21, 2015 |
| Publication date | Nov 24, 2016 |
| Grant date | — |
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A method for making a new crystalline molecular sieve designated SSZ-27 is disclosed. SSZ-27 is synthesized using a hexamethyl [4.3.3.0] propellane-8,11-diammonium cation as a structure directing agent.
Opening claim text (preview).
1 . A method of preparing molecular sieve SSZ-27, comprising: (a) preparing a reaction mixture containing: (1) at least one source of silicon; (2) at least one source of aluminum; (3) at least one source of an element selected from Groups 1 and 2 of the Periodic Table; (4) hydroxide ions; (5) hexamethyl [4.3.3.0] propellane-8-11-diammonium cations; and (6) water; and (b) subjecting the reaction mixture to crystallization conditions sufficient to form crystals of the molecular sieve. 2 . The method of claim 1 , wherein the molecular sieve is prepared from a reaction mixture comprising, in terms of mole ratios, the following: SiO 2 /Al 2 O 3 20 to 80 M/SiO 2 0.05 to 0.50 Q/SiO 2 0.10 to 0.40 OH/SiO 2 0.25 to 0.60 H 2 O/SiO 2 10 to 60 wherein M is selected from the group consisting of elements from Groups 1 and 2 of the Periodic Table and Q is a hexamethyl [4.3.3.0] propellane-8,11-diammonium cation. 3 . The method of claim 1 , wherein the molecular sieve is prepared from a reaction mixture comprising, in terms of mole ratios, the following: SiO 2 /Al 2 O 3 20 to 35 M/SiO 2 0.15 to 0.30 Q/SiO 2 0.10 to 0.30 OH/SiO 2 0.25 to 0.50 H 2 O/SiO 2 20 to 50 wherein M is selected from the group consisting of elements from Groups 1 and 2 of the Periodic Table and Q is a hexamethyl [4.3.3.0] propellane-8,11-diammonium cation. 4 . The method of claim 1 , wherein the molecular sieve comprises hexamethyl [4.3.3.0] propellane-8,11-diammonium cations within its pore structure. 5 . The molecular sieve of claim 1 , wherein the molecular sieve has a SiO 2 /Al 2 O 3 mole ratio of from 20 to 80. 6 . The molecular sieve of claim 1 , wherein the molecular sieve has a SiO 2 /Al 2 O 3 mole ratio of from 20 to 35. 7 . The method of claim 1 , wherein the crystallization conditions include a temperature between 150° C. and 180° C. 8 . The method of claim 1 , wherein the molecular sieve has, in its as-synthesized form, an X-ray diffraction pattern including the lines shown in the following Table: 2-Theta d-Spacing, nm Relative Intensity 7.57 ± 0.20 1.167 W 8.62 ± 0.20 1.025 W 9.35 ± 0.20 0.946 M 9.83 ± 0.20 0.900 W 13.55 ± 0.20 0.653 W 14.80 ± 0.20 0.598 W 15.27 ± 0.20 0.580 W 16.25 ± 0.20 0.545 W 17.72 ± 0.20 0.500 W 19.76 ± 0.20 0.449 M 20.50 ± 0.20 0.433 W 21.08 ± 0.20 0.421 S 21.30 ± 0.20 0.417 M 21.93 ± 0.20 0.405 S 22.95 ± 0.20 0.387 VS.
characterised by their crystalline properties, e.g. semi-crystalline (catalysts comprising carbon B01J21/18; molecular sieves B01J29/00) · CPC title
Catalysts comprising molecular sieves {(molecular sieves per se C01B)} · CPC title
of types characterised by their specific structure not provided for in groups B01J29/08 - B01J29/65 · CPC title
using at least one organic template directing agent · CPC title
X-ray diffraction · CPC title
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