Process for converting raffinate butenes to propylene
US-11926587-B2 · Mar 12, 2024 · US
US2017001925A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2017001925-A1 |
| Application number | US-201615190950-A |
| Country | US |
| Kind code | A1 |
| Filing date | Jun 23, 2016 |
| Priority date | Jul 2, 2015 |
| Publication date | Jan 5, 2017 |
| Grant date | — |
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Embodiments of a metathesis process for producing propylene comprise providing a metathesis catalyst comprising an amorphous mesoporous silica foam impregnated with metal oxides, where the metathesis catalyst has a pore size distribution of at least 3 nm to 40 nm and a total pore volume of at least 0.700 cm 3 /g. The process further involves producing a product stream comprising propylene by contacting a feed stream comprising butene with the metathesis catalyst.
Opening claim text (preview).
What is claimed is: 1 . A metathesis process for producing propylene comprising: providing a metathesis catalyst comprising an amorphous mesoporous silica foam impregnated with metal oxides, where the metathesis catalyst has a pore size distribution of at least 3 nm to 40 nm and a total pore volume of at least 0.700 cm 3 /g; and producing a product stream comprising propylene by contacting a feed stream comprising butene with the metathesis catalyst. 2 . The process of claim 1 further comprising tri-block copolymer structuring agent, where the tri-block copolymer structuring agent is poly(ethylene glycol)-block-poly(propylene glycol)-block-poly(ethylene glycol) structure. 3 . The process of claim 2 where the metathesis catalyst catalyzes isomerization of 2-butene to 1-butene followed by cross-metathesis of 2-butene and 1-butene into a metathesis product stream comprising propylene 4 . The process of claim 3 where at least 90% of the 2-butene is converted to 1-butene via isomerization. 5 . The process of claim 1 where the pore size distribution is from at least 4 nm to 10 nm and the total pore volume is from at least 0.800 cm 3 /g to 1.5 cm 3 /g. 6 . The process of claim 1 where the metathesis catalyst has a total acidity from 0.125 mmol/g to 0.500 mmol/g, and a surface area of 400 to 500 m 2 /g. 7 . The process of claim 1 where the metal oxide is an oxide of molybdenum, rhenium, tungsten, or combinations thereof. 8 . The process of claim 1 where the metal oxide is tungsten oxide. 9 . The process of claim 8 where the metathesis catalyst has a molar ratio for silica to tungsten oxide of 1 to 50. 10 . The process of claim 8 where the metathesis catalyst comprises from 5 to 15% by weight tungsten oxide. 11 . A metathesis catalyst for producing propylene comprising an amorphous mesoporous silica foam with impregnated metal oxides, where the metathesis catalyst has a pore size distribution of at least 3 nm to 40 nm and a total pore volume of at least 0.700 cm 3 /g. 12 . The metathesis catalyst of claim 11 further comprising a tri-block copolymer structuring agent, where the tri-block copolymer structuring agent is poly(ethylene glycol)-block-poly(propylene glycol)-block-poly(ethylene glycol) structure. 13 . The metathesis catalyst of claim 11 where the pore size distribution is from at least 4 nm to 10 nm, and the total pore volume is from at least 0.800 cm 3 /g to 1.5 cm 3 /g. 14 . The metathesis catalyst of claim 11 where the metathesis catalyst has a total acidity from 0.125 mmol/g to 0.500 mmol/g. 15 . The metathesis catalyst of claim 11 where the metal oxide is an oxide of molybdenum, rhenium, tungsten, or combinations thereof. 16 . The metathesis catalyst of claim 11 where the metal oxide is tungsten oxide. 17 . The metathesis catalyst of claim 16 where the metathesis catalyst has a molar ratio for silica to tungsten oxide of 1 to 50. 18 . The metathesis catalyst of claim 11 where the metathesis catalyst comprises from 5 to 15% by weight metal oxide. 19 . The metathesis catalyst of claim 11 where the metathesis catalyst has a pore size ranging from 2 nm to 4 nm. 20 . The metathesis catalyst of claim 11 where the metathesis catalyst has a surface area of 400 to 500 m 2 /g.
Impregnation · CPC title
using catalysts, e.g. selective catalysts · CPC title
Tungsten · CPC title
Rhenium · CPC title
Molybdenum · CPC title
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