Catalyst for propylene production, method for producing same, and method for producing propylene
US-9205415-B2 · Dec 8, 2015 · US
US9757716B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9757716-B2 |
| Application number | US-201314648476-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 22, 2013 |
| Priority date | Dec 21, 2012 |
| Publication date | Sep 12, 2017 |
| Grant date | Sep 12, 2017 |
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A molecular sieve having the framework structure of ZSM-5 is produced using one or more of 1,4-bis(N-pentylpyrrolidinium)butane dications, 1,5-bis(N-pentylpyrrolidinium)pentane dications, and 1,6-bis(N-pentylpyrrolidinium)hexane dications as a structure directing agent.
Opening claim text (preview).
The invention claimed is: 1. A process for producing a molecular sieve having the structure of ZSM-5, the process comprising: (i) preparing a synthesis mixture capable of forming said molecular sieve, said synthesis mixture comprising a source of an alkali or alkaline earth metal (M), a source of an oxide of a tetravalent element Y, optionally a source of a trivalent element X, water, and a directing agent (Q) comprising one or more of 1,4-bis(N-pentylpyrrolidinium)butane dications, 1,5-bis(N-pentylpyrrolidinium)pentane dications, and 1,6-bis(N-pentylpyrrolidinium)hexane dications, and said synthesis mixture having a composition, in terms of mole ratios, within the following ranges: YO 2 /X 2 O 3 at least 20; H 2 O/YO 2 10 to 60; OH − /YO 2 0.20 to 0.60; M/YO 2 0.05 to 0.40; and Q/YO 2 0.05 to 0.20; (ii) heating said synthesis mixture under crystallization conditions, including a temperature of from 80° C. to 200° C., and a time from 1 day to 21 days, until crystals of said molecular sieve are formed; and (iii) recovering said molecular sieve from step (ii), wherein (a) 1,4-bis(N-pentylpyrrolidinium)butane dications which can be represented by the following formula: (b) 1,5-bis(N-pentylpyrrolidinium)pentane dications can be represented by the following formula: and (c) 1,6-bis(N-pentylpyrrolidinium)hexane dications can be represented by the following formula: wherein said tetravalent element Y comprises silicon, and said trivalent element X comprises aluminum. 2. The process of claim 1 , wherein said synthesis mixture has a composition, in terms of mole ratios, within the following ranges: YO 2 /X 2 O 3 at least 24; H 2 O/YO 2 20 to 50; OH − /YO 2 0.25 to 0.50; M/YO 2 0.1 to 0.40; and Q/YO 2 0.05 to 0.20. 3. The process of claim 1 , wherein said synthesis mixture also contains seeds. 4. The process of claim 3 , wherein said synthesis mixture comprises from about 0.01 ppm by weight to about 10,000 ppm by weight of seeds. 5. The process of claim 3 , wherein said synthesis mixture comprises from about 100 ppm by weight to about 5,000 ppm by weight of seeds. 6. The process of claim 3 , wherein said seeds comprise a crystalline material having the structure of ZSM-5. 7. The process of claim 1 and further comprising the step of removing at least part of said directing agent from the molecular sieve crystals recovered in step (iii).
characterised by their crystalline properties, e.g. semi-crystalline (catalysts comprising carbon B01J21/18; molecular sieves B01J29/00) · CPC title
Scanning electron microscopy; Transmission electron microscopy · CPC title
X-ray diffraction · CPC title
Catalysts comprising molecular sieves {(molecular sieves per se C01B)} · CPC title
Crystalline silica-polymorphs, e.g. silicalites {dealuminated aluminosilicate zeolites} · CPC title
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