Processes and cataylsts for the selective hydrogenation of compounds having carbonyl carbon atoms
US-2024368100-A1 · Nov 7, 2024 · US
US2022089557A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2022089557-A1 |
| Application number | US-202117370697-A |
| Country | US |
| Kind code | A1 |
| Filing date | Jul 8, 2021 |
| Priority date | Sep 24, 2020 |
| Publication date | Mar 24, 2022 |
| Grant date | — |
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Described herein are methods for the continuous preparation of 1,2-di(furan-2-yl)ethane-1,2-diol from furan-2-carbaldehyde. The methods can proceed chemically or electrochemically. In certain examples, the methods further comprise the application of a static mixer. The present methods produce 1,2-di(furan-2-yl)ethane-1,2-diol in greater yield, purity, chemoselectivity, and stereoselectivity than traditional batch methods.
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1 . A method for continuously preparing 1,2-di(furan-2-yl)ethane-1,2-diol from furan-2-carbaldehyde 2 . The method of claim 1 , wherein said method proceeds in a continuous flow system. 3 . The method of claim 1 , comprising: introducing a first reactant stream comprising said furan-2-carbaldehyde into a reactor column comprising a metal; introducing a second reactant stream comprising a catalyst into said reactor column; contacting said first reactant stream with said second reactant stream to form a mixture; and passing said mixture through said column to produce said 1,2-di(furan-2-ypethane-1,2-diol; wherein said method proceeds in the presence of a solvent. 4 . The method of claim 3 , wherein said reactor column comprising said metal comprises a packed bed comprising said metal. 5 . The method of claim 3 , wherein said reactor column comprising a metal comprises a static mixer wherein said metal is deposited on surfaces of said static mixer. 6 . (canceled) 7 . (canceled) 8 . (canceled) 9 . The method of claim 3 , wherein said catalyst is a transition metal salt or a rare earth metal salt. 10 . (canceled) 11 . (canceled) 12 . (canceled) 13 . (canceled) 14 . The method of claim 3 , wherein said method further comprises contacting said mixture with an ion exchange material. 15 . (canceled) 16 . (canceled) 17 . (canceled) 18 . (canceled) 19 . (canceled) 20 . (canceled) 21 . (canceled) 22 . A continuous flow system for preparing 1,2-di(furan-2-yl)ethane-1,2-diol from furan-2-carbaldehyde. 23 . The continuous flow system of claim 22 , wherein said system comprises: a first reactant stream comprising said furan-2-carbaldehyde; a second reactant stream comprising a catalyst; a solvent; and a reactor column comprising a metal. 24 . (canceled) 25 . The continuous flow system of claim 23 , wherein said reactor column comprising a metal comprises a static mixer, wherein said metal is deposited on surfaces of said static mixer. 26 . The continuous flow system of claim 23 , wherein said reactor column comprising a metal comprises a packed bed comprising said metal. 27 . The continuous flow system of claim 23 , further comprising a column comprising an ion exchange material. 28 . The method of claim 1 , wherein said method proceeds by an electrochemical process. 29 . The method of claim 28 , wherein said electrochemical process comprises reductively dimerizing furan-2-carbaldehyde to prepare 1,2-di(furan-2-ypethane-1,2-diol by passing a direct electrical current through an electrolytic cell having an anode and a cathode in contact with an electrolytic medium. 30 . The method of claim 29 , wherein said electrolytic medium comprises an initial electrolysis medium comprising furan-2-carbaldehyde, water, and at least one salt. 31 . (canceled) 32 . (canceled) 33 . (canceled) 34 . The method of claim 29 , wherein said cathode is a static mixer. 35 . (canceled) 36 . The method of claim 29 , wherein an annular tube reactor contains said electrolytic cell, wherein surfaces of said annular tube reactor are said anode. 37 . (canceled) 38 . The method of claim 29 , wherein said electrolytic cell is a parallel plate reactor. 39 . An electrochemical process comprising a static mixer. 40 . The electrochemical process of claim 39 , wherein said process is for continuously preparing 1,2-di(furan-2-yl)ethane-1,2-diol from furan-2-carbaldehyde. 41 . An electrochemical continuous flow system for reductively dimerizing furan-2-carbaldehyde to prepare 1,2-di(furan-2-ypethane-1,2-diol. 42 . The electrochemical continuous flow system of claim 41 , wherein said system comprises an electrolytic cell having an anode and a cathode in contact with an electrolytic medium. 43 . The electrochemical continuous flow system of claim 42 , comprising a static mixer, wherein said static mixer is said cathode. 44 . (canceled) 45 . (canceled) 46 . (canceled) 47 . (canceled) 48 . (canceled)
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