Zirconium-based metal-organic frameworks as catalyst for transfer hydrogenation
US-2017320790-A1 · Nov 9, 2017 · US
US10519124B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10519124-B2 |
| Application number | US-201815962044-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 25, 2018 |
| Priority date | Apr 10, 2014 |
| Publication date | Dec 31, 2019 |
| Grant date | Dec 31, 2019 |
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 herein are methods for synthesizing 1,2,5,6-hexanetetrol (HTO), 1,6 hexanediol (HDO) and other reduced polyols from C5 and C6 sugar alcohols or R glycosides. The methods include contacting the sugar alcohol or R-glycoside with a copper catalyst, most desirably a Raney copper catalyst with hydrogen for a time, temperature and pressure sufficient to form reduced polyols having 2 to 3 fewer hydoxy groups than the starting material. When the starting compound is a C6 sugar alcohol such as sorbitol or R-glycoside of a C6 sugar such as methyl glucoside, the predominant product is HTO. The same catalyst can be used to further reduce the HTO to HDO.
Opening claim text (preview).
What is claimed is: 1. A method of making 2,5-bis(hydroxymethyl)tetrahydrofuran, comprising: contacting a mixture comprising 1,2,5,6-hexanetetrol with an acid catalyst selected from the group consisting of carbonic acid and a water tolerant non-Bronsted Lewis acid in the form of a triflate compound for a time and at a temperature and a pressure sufficient to convert the 1,2,5,6-hexanetetrol to 2,5 bis(hydroxymethyl)tetrahydrofuran. 2. The method of claim 1 , wherein the non-Bronsted Lewis acid is selected from the group consisting of bismuth triflate and scandium triflate. 3. The method of claim 1 , wherein the reaction mixture is heated to a temperature between 110° C. and 150° C. 4. The method of claim 1 , wherein the mixture is contacted with the catalyst under vacuum pressure of between 0.021 MPa and 0.041 MPa (3 and 6 psi). 5. The method of claim 1 , wherein the mixture is contacted with the catalyst under vacuum pressure of less than 0.0023 MPa (0.4 psi). 6. The method of claim 1 , wherein the acid catalyst is present in an amount between 0.5 mol % and 5 mol % based on the amount of the 1,2,5,6-hexanetetrol. 7. The method of claim 1 , further comprising separating the 2,5-bis(hydroxymethyl) tetrahydrofuran from the mixture and contacting the separated 2,5-bis(hydroxymethyl)tetrahydrofuran with a rhenium oxide catalyst further comprising silicon oxide for a time and a temperature sufficient to convert the 2,5-bis(hydroxymethyl)tetrahydrofuran to 1,6 hexanediol.
Carbon compounds · CPC title
Ruthenium · CPC title
Trihydroxylic alcohols, e.g. glycerol · CPC title
Copper · CPC title
by reduction of an oxygen containing functional group · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.