Bio-oil fractions composition derived from bio-oil
US-2024381867-A1 · Nov 21, 2024 · US
US9963555B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9963555-B2 |
| Application number | US-201514976796-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 21, 2015 |
| Priority date | Dec 30, 2011 |
| Publication date | May 8, 2018 |
| Grant date | May 8, 2018 |
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Compositions comprising lignin and low levels of undesirable impurities, such as compounds containing sulfur, nitrogen, or metals, are disclosed.
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What is claimed is: 1. A phenolic resin: wherein at least a portion of said phenolic resin is produced by a reaction with a phenol substitute; wherein said phenol substitute comprises: lignin; and wherein said phenol substitute is a composition produced by a two stage process, said two stage process comprising: a first stage comprising: providing a mixture comprising lignocellulosic biomass and water; and heating said mixture to a first temperature of about 130° C. to about 250° C. and maintaining said first temperature for a period of about 0.5 min to about 5 hours, thereby producing a first solids fraction and a first liquid fraction; and a second stage comprising: subjecting said first solids fraction obtained from said first stage to a supercritical or near-critical fluid under a pressure of about 40 bar to about 300 bar; wherein said supercritical or near-critical fluid comprises water; wherein said supercritical or near-critical fluid is at a temperature of about 374° C. to about 600° C.; wherein said subjecting step elevates said first solids fraction to a second temperature of about 250° C. to about 450° C.; wherein said first solids fraction is maintained at said second temperature for a period of about 0.05 sec to about 10 sec, thereby producing a second solids fraction and a second liquid fraction; and wherein said composition comprises said second solids fraction. 2. The phenolic resin of claim 1 , wherein said lignin has an average particle size less than about 500 microns. 3. The phenolic resin of claim 1 , wherein said first stage employs a pressure of about 4 bar to about 100 bar. 4. The phenolic resin of claim 1 , wherein said second stage employs a pressure of about 40 bar to about 260. 5. The phenolic resin of claim 1 , wherein said phenol substitute comprises less than about 150 mg of sulfur per kg of said lignin. 6. The phenolic resin of claim 1 , wherein said second stage employs supercritical water. 7. The phenolic resin of claim 1 , wherein said composition is prepared without the addition of acid. 8. The phenolic resin of claim 1 , wherein said lignin is present in said phenol substitute at a level of at least 30% by weight, based on the total weight of said phenol substitute, as measured by pyrolysis molecular beam mass spectrometry; or wherein said lignin is present in said phenol substitute in an amount greater than about 50 wt. %, based on the weight of said phenol substitute, as measured by NREL procedures. 9. The phenolic resin of claim 1 , wherein said first stage employs a digester and a steam explosion unit. 10. A phenol formaldehyde resin comprising: a reaction product of phenol and formaldehyde; and an extender, wherein said extender comprises: lignin; and wherein said extender is a composition produced by a two stage process, said two stage process comprising: a first stage comprising: providing a mixture comprising lignocellulosic biomass and water; and heating said mixture to a first temperature of about 130° C. to about 250° C. and maintain said first temperature for a period of about 0.5 min to about 5 hours, thereby producing a first solids fraction and a first liquid fraction; and a second stage comprising: subjecting said first solids obtained from said first stage to a supercritical or near-critical fluid under a pressure of about 40 bar to about 300 bar; wherein said supercritical or near-critical fluid comprises water; wherein said supercritical or near-critical fluid is at a temperature of about 374° C. to about 600° C.; wherein said subjecting step elevates said first solids fraction to a second temperature of about 250° C. to about 450° C.; wherein said first solids fraction is maintained at said second temperature for a period of about 0.05 sec to about 10 sec, thereby producing a second solids fraction and a second liquid fraction; and wherein said composition comprises said second solids fraction. 11. The phenol formaldehyde resin of claim 10 , wherein said lignin has an average particle size less than about 500 microns. 12. The phenol formaldehyde resin of claim 10 , wherein said first stage employs a pressure of about 4 bar to about 100 bar. 13. The phenol formaldehyde resin of claim 10 , wherein said second stage employs a pressure of about 40 bar to about 260 bar. 14. The phenol formaldehyde resin of claim 10 , wherein said extender comprises less than about 150 mg of sulfur per kg of said lignin. 15. The phenol formaldehyde resin of claim 10 , wherein said second stage employs supercritical water. 16. The phenol formaldehyde resin of claim 10 , wherein said composition is prepared without the addition of acid. 17. The phenol formaldehyde resin of claim 10 , wherein said lignin is present in said extender at a level of at least 30% by weight, based on the total weight of said extender, as measured by pyrolysis molecular beam mass spectrometry; or wherein said lignin is present in said extender in an amount greater than about 50 wt. %, based on the weight of said extender, as measured by NREL procedures. 18. The phenol formaldehyde resin of claim 10 , wherein said first stage employs a digester and a steam explosion unit. 19. Plywood or a particle board comprising the phenolic resin of claim 1 . 20. Plywood or a particle board comprising the phenol formaldehyde resin of claim 10 . 21. The phenolic resin of claim 1 , wherein said second stage employs a pressure of about 230 bar to about 300 bar. 22. The phenol formaldehyde resin of claim 10 , wherein said second stage employs a pressure of about 230 bar to about 300 bar.
Macromolecular compounds derived from lignin, e.g. tannins, humic acids · CPC title
Low-molecular-weight derivatives of lignin (high-molecular-weight derivatives of lignin {C08H6/00}) · CPC title
Compositions of lignin-containing materials (of polysaccharides C08L1/00 - C08L5/00) · CPC title
with natural products, oils, bitumens, residues · CPC title
Macromolecular compounds derived from lignocellulosic materials {(pretreatment thereof B27N)} · CPC title
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