Bio-oil fractions composition derived from bio-oil
US-2024381867-A1 · Nov 21, 2024 · US
US2016237194A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2016237194-A1 |
| Application number | US-201415024725-A |
| Country | US |
| Kind code | A1 |
| Filing date | Sep 29, 2014 |
| Priority date | Sep 30, 2013 |
| Publication date | Aug 18, 2016 |
| Grant date | — |
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The present invention relates to a method for increasing the reactivity of lignin, wherein the method comprises the following steps: a) forming, under heating at a temperature of 71-94° C., an aqueous dispersion comprising alkali and lignin, wherein the alkali comprises a hydroxide of an alkali metal; and b) heating the dispersion formed in step a) at a temperature of 50-95° C. for producing alkalated lignin.
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1 . A method for increasing the reactivity of lignin, characterized in that the method comprises the following steps: a) forming, under heating at a temperature of 71-94° C., an aqueous dispersion comprising alkali and lignin, wherein the alkali comprises a hydroxide of an alkali metal; and b) heating the dispersion formed in step a) at a temperature of 50-95° C. for producing alkalated lignin 2 . The method of claim 1 , characterized in that the concentration of alkali is 5-50 weight-%, based on the total weight of the dispersion in step a). 3 . The method of claim 1 2 , characterized in that the concentration of lignin is 10-50 weight-%, based on the total weight of the dispersion in step a). 4 . The method of claim 1 , characterized in that the temperature in step a) is 71-90° C. 5 . The method of claim 1 , characterized in that the temperature in step b) is 60-85° C. 6 . The method of claim 1 , characterized in that step b) is carried out for 15 minutes-24 hours. 7 . The method of claim 1 , characterized in that the method comprises, before step a), the step i) of reacting lignin with a compound selected from the class of phenols. 8 . The method of claim 7 , characterized in that step i) is carried out at a temperature of 100-140° C. for 1-3 hours in the presence of a catalyst. 9 . The method of claim 1 , characterized in that the method comprises, after step b), the step ii) of adding an aldehyde, a derivative of an aldehyde, or a combination thereof to the dispersion formed in step b). 10 . The method of claim 9 , characterized in that the weight ratio of the aldehyde to the lignin in the dispersion from step b) is 0.2-0.7. 11 . The method of claim 9 , characterized in that the aldehyde is formaldehyde. 12 . Lignin obtainable by the method of claim 1 . 13 . A method for producing a binder composition, characterized in that the method comprises the step of: (iii) cooking an aqueous composition comprising reactant components including lignin obtainable by the method of claim 1 , a polymerizable substance and a crosslinking agent in the presence of a catalyst at a temperature of 60-95° C. for polymerizing the reactant components until a binder composition with a predetermined viscosity value is formed. 14 . The method of claim 13 , characterized in that step (iii) comprises cooking the composition at a temperature of 65-90° C. 15 . The method of claim 13 , characterized in that the crosslinking agent is an aldehyde. 16 . The method of claim 13 , characterized in that the polymerizable substance is selected from a group consisting of phenol, cresol, resorcinol and combinations thereof. 17 . The method of claim 13 , characterized in that the catalyst is selected from a group consisting of sodium hydroxide, potassium hydroxide and any mixture thereof. 18 . A binder composition obtainable by the method of claim 13 . 19 . An adhesive composition comprising the binder composition of claim 18 . 20 . (canceled) 21 . (canceled)
Lignin · CPC title
with polyhydric phenols · CPC title
Lignin · CPC title
Macromolecular compounds derived from lignin, e.g. tannins, humic acids · CPC title
with polyhydric phenols · CPC title
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