Method for making molecular sieve SSZ-95
US-10052619-B2 · Aug 21, 2018 · US
US10272422B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10272422-B2 |
| Application number | US-201816108007-A |
| Country | US |
| Kind code | B2 |
| Filing date | Aug 21, 2018 |
| Priority date | May 21, 2014 |
| Publication date | Apr 30, 2019 |
| Grant date | Apr 30, 2019 |
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A new crystalline molecular sieve designated SSZ-95 is disclosed. In general, SSZ-95 is synthesized from a reaction mixture suitable for synthesizing MTT-type molecular sieves and maintaining the mixture under crystallization conditions sufficient to form product. The product molecular sieve is subjected to a pre-calcination step, and ion-exchange to remove extra-framework cations, and a post-calcination step. The molecular sieve has a MTT-type framework and a H-D exchangeable acid site density of 0 to 50% relative to molecular sieve SSZ-32.
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What is claimed is: 1. A molecular sieve having a MTT-type framework, a mole ratio of 20 to 70 of silicon oxide to aluminum oxide, a total micropore volume of between 0.005 and 0.02 cc/g; and a H-D exchangeable acid site density of up to 50% relative to SSZ-32. 2. The molecular sieve of claim 1 , wherein the molecular sieve has a mole ratio of 20 to 50 of silicon oxide to aluminum oxide. 3. The molecular sieve of claim 1 , wherein the molecular sieve has a total micropore volume of between 0.008 and 0.018 cc/g. 4. The molecular sieve of claim 1 , wherein the molecular sieve has an external surface area of between 200 and 250 m 2 /g; and a BET surface area of between 240 and 280 m 2 /g. 5. The molecular sieve of claim 1 , wherein the molecular sieve has a H-D exchangeable acid site density of 0.5 to 30% relative to molecular sieve SSZ-32. 6. The molecular sieve of claim 5 , wherein the molecular sieve has a total micropore volume of between 0.008 and 0.018 cc/g. 7. The molecular sieve of claim 5 , wherein the molecular sieve has an external surface area of between 200 and 250 m 2 /g; and a BET surface area of between 240 and 280 m 2 /g. 8. The molecular sieve of claim 1 , wherein the molecular sieve has a H-D exchangeable acid site density of 2 to 25% relative to molecular sieve SSZ-32. 9. The molecular sieve of claim 8 , wherein the molecular sieve has a total micropore volume of between 0.008 and 0.018 cc/g. 10. The molecular sieve of claim 8 , wherein the molecular sieve has an external surface area of between 200 and 250 m 2 /g; and a BET surface area of between 240 and 280 m 2 /g. 11. The molecular sieve of claim 1 , made by a process comprising the steps of: (a) providing as-made, structure directing agent-containing molecular sieve SSZ-32x having a silicon-to-alumina ratio of 20 to 70; (b) subjecting the molecular sieve to a pre-calcination step at a temperature below the full decomposition temperature of the structure directing agent, for a time sufficient to convert at least a portion of the structure directing agent to a decomposition residue; (c) ion-exchanging the pre-calcined molecular sieve to remove extra-framework cations; and (d) subjecting the molecular sieve to a post-calcination step at a temperature below the full decomposition temperature of the structure directing agent, for a time sufficient to convert at least a portion of the structure directing agent to a decomposition residue; wherein the post-calcined molecular sieve has a cumulative weight loss (CWL) of 0<CWL≤10 wt. % and a total micropore volume of between 0.005 and 0.02 cc/g. 12. The molecular sieve of claim 11 , wherein the post-calcined molecular sieve has a cumulative weight loss of between 4 and 9 wt. %. 13. The molecular sieve of claim 11 , wherein the post-calcined molecular sieve has a cumulative weight loss of between 5 and 8.5 wt. %. 14. The molecular sieve of claim 11 , wherein the molecular sieve has a total micropore volume of between 0.008 and 0.018 cc/g. 15. The molecular sieve of claim 11 , wherein the molecular sieve has an external surface area of between 200 and 250 m 2 /g; and a BET surface area of between 240 and 280 m 2 /g.
Synthetic zeolitic molecular sieves · CPC title
Decomposition and pyrolysis · CPC title
Pore volume · CPC title
to stabilize the molecular sieve structure · CPC title
Operations & Transport · mapped topic
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