Method for aluminum incorporation into high-silica zeolites prepared in fluoride media
US-2017113940-A1 · Apr 27, 2017 · US
US11565943B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11565943-B2 |
| Application number | US-202117173712-A |
| Country | US |
| Kind code | B2 |
| Filing date | Feb 11, 2021 |
| Priority date | Feb 11, 2021 |
| Publication date | Jan 31, 2023 |
| Grant date | Jan 31, 2023 |
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A method is disclosed making a molecular of TON framework type having unique properties. The method uses 1,3,4-trimethylimidazolium cations as a structure directing agent and a combined source of silicon and aluminum selected from alumina-coated silica and aluminosilicate zeolites. The obtained molecular sieve can be used in processes for dewaxing paraffinic hydrocarbon feedstocks.
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The invention claimed is: 1. A method of synthesizing a molecular sieve having a TON framework, the method comprising: (1) forming a reaction mixture comprising: (a) a combined source of silicon and aluminum, where the combined source of silicon and aluminum is selected from the group consisting of an alumina-coated silica, an aluminosilicate zeolite having an FAU framework, and a mixture thereof; (b) a structure directing agent (Q) comprising 1,3,4-trimethylimidazolium cations; (c) a source of hydroxide ions; (d) water; and (e) seeds; and (2) subjecting the reaction mixture to crystallization conditions sufficient to form crystals of the molecular sieve having a TON framework. 2. The method of claim 1 , wherein the reaction mixture has a composition, in terms of molar ratios, as follows: SiO 2 /Al 2 O 3 30 to 170 Q/SiO 2 0.03 to 0.50 OH/SiO 2 0.05 to 1.00 H 2 O/SiO 2 5 to 100. 3. The method of claim 1 , wherein the reaction mixture has a composition, in terms of molar ratios, as follows: SiO 2 /Al 2 O 3 35 to 130 Q/SiO 2 0.04 to 0.30 OH/SiO 2 0.10 to 0.50 H 2 O/SiO 2 10 to 50. 4. The method of claim 1 , wherein the aluminosilicate zeolite having an FAU framework is zeolite Y. 5. The method of claim 1 , wherein the source of hydroxide ions comprises an alkali metal hydroxide. 6. The method of claim 5 , wherein the alkali metal is lithium, sodium, potassium, or a mixture thereof. 7. The method of claim 6 , wherein a molar ratio of alkali metal cation/SiO 2 is in a range of from 0.1 to 1.0. 8. The method of claim 1 , wherein the seeds comprise a molecular sieve having a TON framework. 9. The method of claim 1 , wherein the reaction mixture comprises from 0.01 ppm by weight to 10,000 ppm by weight of the seeds. 10. The method of claim 1 , wherein the reaction mixture further comprises a separate source of silicon. 11. The method of claim 10 , wherein the separate source of silicon comprises colloidal silica, precipitated silica, fumed silica, an alkali metal silicate, a tetraalkyl orthosilicate, or a mixture thereof. 12. The method of claim 1 , wherein the crystallization conditions include a temperature of from 125° C. to 200° C. and a time of from 1 day to 10 days.
Pressure · CPC title
Spatial velocity, e.g. LHSV, WHSV · CPC title
Temperature · CPC title
using at least one organic template directing agent · CPC title
Crystalline aluminosilicate zeolites; Isomorphous compounds thereof; Direct preparation thereof; Preparation thereof starting from a reaction mixture containing a crystalline zeolite of another type, or from preformed reactants; After-treatment thereof · CPC title
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