Modified lignin manufacturing method, modified lignin, and modified lignin-including resin composition material
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example 1
(1) Reaction Process
[0139]29.5 parts by mass of a second generation ethanol saccharification residue (lignin content: 66% by mass) (29.5 g, 19.5 g of lignin), 180 parts by mass of phenol, and 1 part by mass of phosphoric acid were placed in a 1.0 L pressure tight vessel capable of performing agitation, and heated, and the agitation was started at the time when phenol was melted. The heating was continuously performed, and the content was heated to 200° C. for 4 hours.
(2) Purification Process
(2-1) Filtration
[0140]A 1.0 L hot pressure filtration device having set thereto No. 5C filter paper was fabricated and heated with warm water of 60 to 90° C. The total amount of the reaction liquid obtained in the reaction process was placed therein and filtered by pressurizing to 0.1 to 0.4 MPa with compressed air or nitrogen. The filtered solid was washed with phenol.
(2-2) Distillation
[0141]The filtrate obtained through the filtration was distilled by heating (100 to 130° C.) under reduced pres...
example 2
[0145]The same procedure as in Example 1 was performed except that 78 parts by mass of phenol was used, the acid catalyst was not used, and the reaction time was 2 hours, so as to provide a modified lignin 2 (amount of modified lignin: 17.7 g, yield: 91.4%).
example 3
[0146]The same procedure as in Example 2 was performed except that the reaction time was 4 hours, so as to provide a modified lignin 3 (amount of modified lignin: 18.9 g, yield: 97.2%).
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