Renewable olefins from a mixture of acetic acid and propionic acid
US-9212106-B2 · Dec 15, 2015 · US
US9610575B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9610575-B2 |
| Application number | US-201213880034-A |
| Country | US |
| Kind code | B2 |
| Filing date | Aug 16, 2012 |
| Priority date | Aug 16, 2012 |
| Publication date | Apr 4, 2017 |
| Grant date | Apr 4, 2017 |
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Some embodiments in the present disclosure generally relate to catalytic silica-polyvinyl alcohol composites, silica structures therefrom, and/or microreactors therefrom. Some embodiments in the present disclosure generally relate to porous substrates that can have at least one pore with a catalyst associated with the inside of the pore.
Opening claim text (preview).
What is claimed is: 1. A microreactor comprising: a sintered silica body formed from a sintered silica material; a channel formed in an exterior surface of the sintered silica body, the channel extending into the sintered silica body a depth from the exterior surface, and a width and length across the sintered silica body, wherein the channel defines a flow path across the exterior surface of the sintered silica body; a plurality of pores in the sintered silica material that extend internally through at least a portion of the sintered silica body, wherein at least one pore of the plurality of pores has an average diameter of about 1 nm to about 100 nm, and wherein the at least one pore is in fluid communication with the channel; and at least one catalyst on an internal surface of the at least one pore, wherein the catalyst on the internal surface of the at least one pore is in fluid communication with the channel within the sintered silica body. 2. The microreactor of claim 1 , wherein the channel is transparent or semi-transparent. 3. The microreactor of claim 2 , wherein the channel is optically transparent under vacuumed ultraviolet to infrared range. 4. The microreactor of claim 1 , wherein the at least one catalyst comprises at least one transition metal. 5. The microreactor of claim 4 , wherein the at least one transition metal comprises at least one of Rh, Pt, Ag, Ir, Au, Cu, or Zn. 6. The microreactor of claim 1 , wherein the at least one catalyst is adsorbed onto the internal surface in the at least one pore. 7. The microreactor of claim 1 , wherein the at least one catalyst comprises an organic catalyst. 8. The microreactor of claim 1 , wherein the at least one catalyst is in a continuous layer over part or substantially all of a surface of the channel. 9. The microreactor of claim 1 , wherein the depth of the channel into the exterior surface of the sintered material is greater than an average diameter of the at least one pore. 10. The microreactor of claim 1 , comprising one or more electrodes. 11. The microreactor of claim 10 , wherein the one or more electrodes comprise a conductive material stamped onto the sintered silica material. 12. The microreactor of claim 1 , wherein the microreactor comprises a plurality of channels, wherein two or more channels join together at one or more junction(s).
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