Production of jet fuel-range hydrocarbons from cellulosic biomass
US-2015376511-A1 · Dec 31, 2015 · US
US9139545B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9139545-B2 |
| Application number | US-201314401199-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jun 10, 2013 |
| Priority date | Jun 11, 2012 |
| Publication date | Sep 22, 2015 |
| Grant date | Sep 22, 2015 |
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The diallyl ether derivatives of the cis and trans stereoisomers of 2,5-bis(hydroxymethyl)tetrahydrofuran are produced. These materials are expected to be useful for making a variety of biobased polymers. Processes are further described for producing these diallyl ether derivatives in substantially quantitative yields.
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The invention claimed is: 1. (2R,5S)-2,5-bis((allyloxy)methyl)tetrahydrofuran. 2. (2S,5S)-2,5-bis((allyloxy)methyl)tetrahydrofuran. 3. A process for making a diallyl ether derivative of at least one of the cis and trans stereoisomers of 2,5-bis(hydroxymethyl)tetrahydrofuran, comprising reacting at least one of the cis and trans isomers of 2,5-bis(hydroxymethyl)tetrahydrofuran with a Brønsted base whose conjugate acid has an acid dissociation constant pK a greater than 16 to form at least one corresponding conjugate base of an isomer of 2,5-bis(hydroxymethyl)tetrahydrofuran, then reacting the conjugate base or bases so formed with allyl bromide to form the corresponding diallyl ether derivative. 4. The process according to claim 3 , wherein the yield of the diallyl ether derivative or derivatives is substantially quantitative. 5. The process as in claim 3 , wherein the Brønsted base is a Bronsted base whose conjugate acid has an acid dissociation constant pK a of at least about 18. 6. The process as in claim 5 , wherein the Bronsted base is potassium t-butoxide and is reacted with the at least one of the cis and trans isomers of 2,5-bis(hydroxymethyl)tetrahydrofuran. 7. The process as in any one of claims 3 - 6 , which is carried out in a nonaqueous solvent system and in the absence of water. 8. The process as in claim 7 , carried out at a temperature of about 25 degrees Celsius or less. 9. The process as in claim 8 , carried out at a temperature of about 20 degrees Celsius or less. 10. The process as in claim 7 , wherein allyl bromide is added gradually over time. 11. The process as in claim 10 , wherein not more than about 13.3 percent of the allyl bromide is added per minute.
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