Catalysts and methods for polyester production
US-2015368394-A1 · Dec 24, 2015 · US
US9421527B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9421527-B2 |
| Application number | US-201414513529-A |
| Country | US |
| Kind code | B2 |
| Filing date | Oct 14, 2014 |
| Priority date | Feb 13, 2014 |
| Publication date | Aug 23, 2016 |
| Grant date | Aug 23, 2016 |
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.
A hydrogenation catalyst and a method of hydrogenating a hydrocarbon compound as a substrate using the same are provided. The hydrogenation catalyst includes inorganic nanoparticles and a nitrogen-doped reduced graphene oxide support for supporting the inorganic nanoparticles, and the hydrocarbon compound is derived from a biomass and contains a functional group. Therefore, the hydrogenation catalyst which exhibits a high conversion rate and high selectivity, is stable, and can be easily separated after a hydrogenation reaction, and whose catalytic activities are not significantly altered even when recovered and repeatedly recycled can be provided. The method of hydrogenating a hydrocarbon compound in which hydrogen can be directly produced in a reactor using formic acid as a hydrogen source without supplying additional hydrogen gas and simultaneously be used under normal pressure can also be provided.
Opening claim text (preview).
What is claimed is: 1. A hydrogenation catalyst, comprising: inorganic nanoparticles; and a nitrogen-doped reduced graphene oxide support for supporting the inorganic nanoparticles; wherein the inorganic nanoparticles comprise silver nanoparticles, palladium nanoparticles, and Fe 3 O 4 nanoparticles. 2. The hydrogenation catalyst of claim 1 , wherein the inorganic nanoparticles have an average particle size of 3 to 10 nm. 3. The hydrogenation catalyst of claim 1 , wherein the hydrogenation catalyst comprises the inorganic nanoparticle at 1 to 5 atomic %. 4. A method of manufacturing a hydrogenation catalyst, comprising: obtaining a nitrogen-doped reduced graphene oxide by reacting a nitrogen-containing compound with a colloidal suspension of graphene oxide; obtaining a dispersion of the nitrogen-doped reduced graphene oxide by dispersing the nitrogen-doped reduced graphene oxide in water; dispersing the dispersion of the nitrogen-doped reduced graphene oxide by adding an aqueous solution of an inorganic nanoparticle precursor to the dispersion of the nitrogen-doped reduced graphene oxide, wherein the inorganic nanoparticle precursor comprises salts of silver, palladium and iron; and adding a reducing agent to perform a reaction. 5. The method of claim 4 , wherein the inorganic nanoparticle precursor is selected from the group consisting of a chloride, a sulfate, a nitrate, a carbonate of the inorganic nanoparticle, and a mixture thereof. 6. The method of claim 4 , wherein the reducing agent is selected from the group consisting of hydrazine, hydrazine hydrate, a borohydride, sodium borohydride, and a mixture thereof. 7. A method of hydrogenating a biomass-derived hydrocarbon compound, comprising: a hydrogenation operation of allowing a hydrocarbon compound as a substrate to react with the catalyst of claim 1 in the presence of a hydrogen source, wherein the hydrocarbon compound is derived from a biomass and contains a functional group. 8. The method of claim 7 , wherein the hydrogen source is formic acid. 9. The method of claim 7 , wherein the hydrogenation operation is performed without supplying hydrogen gas from the outside of a reactor. 10. The method of claim 7 , wherein the hydrogenation operation is performed under reaction conditions of 80 to 130° C. and 6 to 12 hours. 11. The method of claim 7 , wherein the hydrogen source is used at an equivalent content of 1.5 to 3.5 moles, based on the total content of the substrate. 12. The method of claim 7 , wherein the hydrocarbon catalyst is used at a content of 1.8 to 4.0 g per mole of a reaction product, based on the total content of the inorganic nanoparticles included in the catalyst. 13. The method of claim 7 , wherein the substrate is at least one compound selected from the group consisting of an aromatic compound containing a carbonyl group, a hydrocarbon compound containing an alkene group, a hydrocarbon compound containing an alkyne group, and a hydrocarbon compound containing a nitro group. 14. The method of claim 13 , wherein the substrate is vanillin. 15. The method of claim 7 , wherein the catalyst comprises the inorganic nanoparticles having an average particle size of 3 to 10 nm. 16. The method of claim 7 , wherein the catalyst comprises the inorganic nanoparticle at a content of 1 to 5 atomic %. 17. The method of claim 7 , further comprising: recovering the catalyst after the hydrogenation operation. 18. The method of claim 17 , wherein the recovering of the catalyst is performed using at least one method selected from the group consisting of centrifugation, filtration, and a magnetic method.
Indexing scheme associated with group B01J35/00, related to the analysis techniques used to determine the catalysts form or properties · CPC title
Compounds characterised by their crystallite size · CPC title
Scanning electron microscopy; Transmission electron microscopy · CPC title
Nanoparticles · CPC title
X-ray diffraction · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.