Post-treatment of deboronated zeolite beta
US-2015344317-A1 · Dec 3, 2015 · US
US9505627B1 · US · B1
| Field | Value |
|---|---|
| Publication number | US-9505627-B1 |
| Application number | US-201615098450-A |
| Country | US |
| Kind code | B1 |
| Filing date | Apr 14, 2016 |
| Priority date | May 21, 2015 |
| Publication date | Nov 29, 2016 |
| Grant date | Nov 29, 2016 |
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Uses for a new crystalline molecular sieve designated SSZ-27 are 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).
The invention claimed is: 1. In a process for separating gases using a membrane containing a molecular sieve, the improvement comprising using as the molecular sieve a molecular sieve having in its calcined form, an X-ray diffraction pattern including the lines listed in the following table: 2-Theta d-Spacing, nm Relative Intensity 7.50 ± 0.20 1.177 W 8.65 ± 0.20 1.021 W 9.47 ± 0.20 0.933 VS 9.94 ± 0.20 0.889 M 13.47 ± 0.20 0.657 M 14.86 ± 0.20 0.596 M 16.07 ± 0.20 0.551 W 16.37 ± 0.20 0.541 W 17.92 ± 0.20 0.495 W 19.92 ± 0.20 0.445 W 20.66 ± 0.20 0.430 W 21.14 ± 0.20 0.420 W 21.34 ± 0.20 0.416 W 22.07 ± 0.20 0.402 M 23.17 ± 0.20 0.384 M. 2. A process for the production of light olefins from a feedstock comprising an oxygenate or mixture of oxygenates, the process comprising reacting the feedstock at effective conditions over a catalyst comprising a molecular sieve having, in its calcined form, an X-ray diffraction pattern including the lines listed in the following table: 2-Theta d-Spacing, nm Relative Intensity 7.50 ± 0.20 1.177 W 8.65 ± 0.20 1.021 W 9.47 ± 0.20 0.933 VS 9.94 ± 0.20 0.889 M 13.47 ± 0.20 0.657 M 14.86 ± 0.20 0.596 M 16.07 ± 0.20 0.551 W 16.37 ± 0.20 0.541 W 17.92 ± 0.20 0.495 W 19.92 ± 0.20 0.445 W 20.66 ± 0.20 0.430 W 21.14 ± 0.20 0.420 W 21.34 ± 0.20 0.416 W 22.07 ± 0.20 0.402 M 23.17 ± 0.20 0.384 M. 3. The process of claim 2 , wherein the light olefins are ethylene, propylene, butylene, or mixtures thereof. 4. The process of claim 2 , wherein the oxygenate is methanol, dimethyl ether, or a mixture thereof. 5. A process for producing methylamine or dimethylamine comprising reacting methanol, dimethyl ether, or a mixture thereof, and ammonia in the gaseous phase in the presence of a catalyst comprising a molecular sieve having, in its calcined form, an X-ray diffraction pattern including the lines listed in the following table: 2-Theta d-Spacing, nm Relative Intensity 7.50 ± 0.20 1.177 W 8.65 ± 0.20 1.021 W 9.47 ± 0.20 0.933 VS 9.94 ± 0.20 0.889 M 13.47 ± 0.20 0.657 M 14.86 ± 0.20 0.596 M 16.07 ± 0.20 0.551 W 16.37 ± 0.20 0.541 W 17.92 ± 0.20 0.495 W 19.92 ± 0.20 0.445 W 20.66 ± 0.20 0.430 W 21.14 ± 0.20 0.420 W 21.34 ± 0.20 0.416 W 22.07 ± 0.20 0.402 M 23.17 ± 0.20 0.384 M.
Zeolites · CPC title
for storing hydrocarbons · CPC title
Processes characterised by a specific catalyst · CPC title
by elimination of water · CPC title
containing arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium · CPC title
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