Dehydrogenation of alkanols to increase yield of aromatics
US-2015133705-A1 · May 14, 2015 · US
US9808784B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9808784-B2 |
| Application number | US-201314904658-A |
| Country | US |
| Kind code | B2 |
| Filing date | Aug 2, 2013 |
| Priority date | Jul 24, 2013 |
| Publication date | Nov 7, 2017 |
| Grant date | Nov 7, 2017 |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
Disclosed is a novel adsorbent having excellent adsorption durability and high adsorption efficiency while having improved durability, thereby improving a carbon dioxide (CO2) separation process. A mesoporous cellular foam impregnated with an iron (Fe)-substituted heteropolyacid includes a mesoporous cellular foam support and an Fe-substituted heteropolyacid, and the mesoporous cellular foam impregnated with an Fe-substituted heteropolyacid has superior CO2 adsorption performance and exhibits excellent reproduction performance even after CO2 adsorption and desorption are performed several times through temperature changes, thereby enabling efficient and economical CO2 separation.
Opening claim text (preview).
The invention claimed is: 1. A mesoporous cellular foam impregnated with an iron-substituted heteropolyacid, the mesoporous cellular foam comprising: a mesoporous cellular foam support; and an iron-substituted heteropolyacid. 2. The mesoporous cellular foam of claim 1 , wherein a weight of the iron-substituted heteropolyacid is about 50% to about 90% of a weight of the mesoporous cellular foam support. 3. The mesoporous cellular foam of claim 1 , wherein a weight of the iron-substituted heteropolyacid is about 70% of a weight of the mesoporous cellular foam support. 4. The mesoporous cellular foam of claim 1 , wherein a molar ratio of ammonium (NH 4 ) to silicon (Si) in the mesoporous cellular foam support is 6:1. 5. The mesoporous cellular foam of claim 1 , wherein the molecular formula of the iron-substituted heteropolyacid is Fe 2.0 SiW 12 O 40 . 6. A method of preparing a mesoporous cellular foam impregnated with an iron-substituted heteropolyacid, the method comprising: providing distilled water; dissolving 0.1 g of iron-substituted heteropolyacid (Fe-HPA) per 10 ml of the distilled water to prepare an aqueous solution; adding a mesoporous cellular foam support having a weight of a larger value than that of the iron-substituted heteropolyacid in the aqueous solution; stirring the aqueous solution to which the support is added; and drying the stirred aqueous solution at a temperature in a range of about 90° C. to about 110° C. for about 9 hours to about 11 hours. 7. The method of claim 6 , wherein a weight of the iron-substituted heteropolyacid is about 50% to about 90% of a weight of the mesoporous cellular foam support. 8. The method of claim 6 , wherein a weight of the iron-substituted heteropolyacid is about 70% of the mesoporous cellular foam support. 9. A method of separating carbon dioxide by using a mesoporous cellular foam impregnated with an iron-substituted heteropolyacid, the method comprising: adsorbing carbon dioxide by contacting a carbon dioxide-mixed gas with the mesoporous cellular foam of claim 1 at a temperature in a range of about 25° C. to about 75° C.; and desorbing carbon dioxide by placing the mesoporous cellular foam impregnated with an iron-substituted heteropolyacid which adsorbed carbon dioxide at a temperature in a range of about 100° C. to about 120° C. 10. The method of claim 9 , wherein the adsorbing carbon dioxide is performed at 50° C. 11. The method of claim 9 , wherein the desorbing carbon dioxide is performed at 110° C. 12. The method of claim 9 , wherein a weight of the iron-substituted heteropolyacid of the mesporous cellular foam is about 50% to about 90% of a weight of the mesoporous cellular foam support of the mesporous cellular foam. 13. The method of claim 9 , wherein a weight of the iron-substituted heteropolyacid of the mesporous cellular foam is about 70% of a weight of the mesoporous cellular foam support of the mesporous cellular foam. 14. The method of claim 9 , wherein a molar ratio of ammonium (NH 4 ) to silicon (Si) in the mesoporous cellular foam support of the mesporous cellular foam is 6:1. 15. The method of claim 9 , wherein the molecular formula of the iron-substituted heteropolyacid of the mesporous cellular foam is Fe 2.0 SiW 12 O 40 .
being in the range 2-50 nm, i.e. mesopores · CPC title
derived from different types of monomers, e.g. linear or branched copolymers, block copolymers, graft copolymers · CPC title
Polymeric adsorbents · CPC title
comprising oxides or hydroxides of metals not provided for in group B01J20/04 · CPC title
by adsorption, e.g. preparative gas chromatography {(solid sorbent compositions B01J20/00, preparation of inorganic compounds or elements C01)} · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.