Zeolite ZSM-18, its synthesis and its use
US-9205421-B2 · Dec 8, 2015 · US
US9468917B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9468917-B2 |
| Application number | US-201514626787-A |
| Country | US |
| Kind code | B2 |
| Filing date | Feb 19, 2015 |
| Priority date | Jun 4, 2014 |
| Publication date | Oct 18, 2016 |
| Grant date | Oct 18, 2016 |
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This disclosure is directed to uses for a new crystalline molecular sieve designated SSZ-100. SSZ-100 is synthesized using a cationic nitrogen-containing organic compound having the following structure:
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 a mole ratio of at least 10 of (1) at least one oxide of at least one tetravalent element to (2) one or more oxides selected from the group consisting of trivalent elements, pentavalent elements, and mixtures thereof, and having, in its calcined form, an X-ray diffraction substantially as shown in the following Table: 2-Theta d-Spacing, nm Relative Intensity 8.48 ± 0.20 1.041 VS 8.98 ± 0.20 0.984 VS 10.04 ± 0.20 0.880 S 12.38 ± 0.20 0.714 W 14.17 ± 0.20 0.625 W 15.85 ± 0.20 0.559 S 17.07 ± 0.20 0.519 W 17.64 ± 0.20 0.503 M 18.68 ± 0.20 0.475 S 19.44 ± 0.20 0.456 W 19.78 ± 0.20 0.449 M 19.98 ± 0.20 0.444 S 20.22 ± 0.20 0.439 W 21.30 ± 0.20 0.417 W 22.80 ± 0.20 0.390 M 23.06 ± 0.20 0.385 M 24.29 ± 0.20 0.366 W 24.99 ± 0.20 0.356 VS. 2. The process of claim 1 , wherein the molecular sieve has a mole ratio of at least 10 of (1) silicon oxide to (2) an oxide selected from boron oxide, aluminum oxide, gallium oxide, indium oxide, iron oxide, and mixtures thereof. 3. 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 a mole ratio of at least 10 of (1) at least one oxide of at least one tetravalent element to (2) one or more oxides selected from the group consisting of trivalent elements, pentavalent elements, and mixtures thereof, and having, in its calcined form, an X-ray diffraction pattern substantially as shown in the following Table: 2-Theta d-Spacing, nm Relative Intensity 8.48 ± 0.20 1.041 VS 8.98 ± 0.20 0.984 VS 10.04 ± 0.20 0.880 S 12.38 ± 0.20 0.714 W 14.17 ± 0.20 0.625 W 15.85 ± 0.20 0.559 S 17.07 ± 0.20 0.519 W 17.64 ± 0.20 0.503 M 18.68 ± 0.20 0.475 S 19.44 ± 0.20 0.456 W 19.78 ± 0.20 0.449 M 19.98 ± 0.20 0.444 S 20.22 ± 0.20 0.439 W 21.30 ± 0.20 0.417 W 22.80 ± 0.20 0.390 M 23.06 ± 0.20 0.385 M 24.29 ± 0.20 0.366 W 24.99 ± 0.20 0.356 VS. 4. The process of claim 3 , wherein the molecular sieve has a mole ratio of at least 10 of (1) silicon oxide to (2) an oxide selected from boron oxide, aluminum oxide, gallium oxide, indium oxide, iron oxide, and mixtures thereof. 5. The process of claim 3 , wherein the light olefins are ethylene, propylene, butylene, or mixtures thereof. 6. The process of claim 5 , wherein the light olefin is ethylene. 7. The process of claim 3 , wherein the oxygenate is methanol, dimethyl ether, or a mixture thereof. 8. The process of claim 7 , wherein the oxygenate is methanol. 9. 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 a mole ratio of at least 10 of (1) at least one oxide of at least one tetravalent element to (2) one or more oxides selected from the group consisting of trivalent elements, pentavalent elements, and mixtures thereof, and having, in its calcined form, an X-ray diffraction pattern substantially as shown in the following Table: 2-Theta
Cross-Sectional Technologies · mapped topic
Manganese · CPC title
containing embedded adsorbents · CPC title
Zeolites · CPC title
Iron · CPC title
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