Rate/kinetic selective multiple bed adsorption process cycle
US-11883775-B2 · Jan 30, 2024 · US
US11148121B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11148121-B2 |
| Application number | US-201716081314-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 17, 2017 |
| Priority date | May 31, 2016 |
| Publication date | Oct 19, 2021 |
| Grant date | Oct 19, 2021 |
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A method and apparatus for removing a volatile component from a mixture are disclosed. The method and apparatus employ a crosslinked elastomer with a glass transition temperature ≤+25° C. as the sorbent.
Opening claim text (preview).
The invention claimed is: 1. A method for depleting a volatile component in a mixture comprising the volatile component and at least one other component, the method comprising 1) sorbing at least some of the volatile component into bulk of a nonporous crosslinked polyorganosiloxane elastomer, thereby forming a depleted mixture containing less of the volatile component than the mixture before sorbing and enriching the nonporous crosslinked polyorganosiloxane elastomer with sorbed volatile component thereby forming an enriched crosslinked elastomer, wherein during step 1), at least some of the volatile component is in gas phase, 2) desorbing at least some of the sorbed volatile component from the enriched crosslinked elastomer, thereby forming a desorbed volatile component and a regenerated elastomer containing less of the sorbed volatile component than the enriched crosslinked elastomer prior to desorbing, and 3) using the regenerated elastomer as all or a portion of the nonporous crosslinked polyorganosiloxane elastomer in repeating step 1), and 4) directing one or both of the depleted mixture during and/or after step 1) and the desorbed volatile component during and/or after step 2); where the volatile component has a vapor pressure less than a vapor pressure of the at least one other component in the mixture and the volatile component is a cyclic polyorganosiloxane with a degree of polymerization from 3 to 12, a silane, or a noncyclic polyorganosiloxane with a degree of polymerization up to 14. 2. The method of claim 1 , where the volatile component is a cyclic polyorganosiloxane with a degree of polymerization from 3 to 12. 3. The method of claim 1 , where the at least one other component of the mixture comprises a non-volatile organic liquid or a non-volatile polyorganosiloxane liquid. 4. The method of claim 1 , where the mixture is a process vapor stream and the depleted mixture is a depleted process vapor. 5. The method of claim 1 , where the nonporous crosslinked polyorganosiloxane elastomer has a form selected from thin films, coated support materials, nanorods, particulates, and fibers. 6. The method of claim 1 , wherein the nonporous crosslinked polyorganosiloxane elastomer is prepared by a method comprising: 1) combining ingredients and crosslinking to form the nonporous crosslinked polyorganosiloxane elastomer in the presence of a solvent, and 2) thereafter removing the solvent. 7. The method of claim 6 , where the ingredients in step 1) comprise: (A) a hydrosilylation catalyst, (B) a polyorganosiloxane having an average, per molecule, of two or more silicon bonded aliphatically unsaturated hydrocarbon groups, (C) a crosslinker having an average, per molecule, of more than two silicon bonded hydrogen atoms, optionally (D) an inhibitor, and (E) the solvent; and step 2) is performed by heating the composition.
Water · CPC title
Regeneration of sorbents, filters · CPC title
obtained otherwise than by reactions only involving carbon to carbon unsaturated bonds, e.g. obtained by polycondensation (macromolecular compounds obtained otherwise than by reactions only involving unsaturated carbon-to-carbon bonds per se C08G) · CPC title
of CO2 · CPC title
Volatile compounds, e.g. benzene · CPC title
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