FIELD: medicinal industry. SUBSTANCE: method involves the alkaline treatment of hydrolytic lignin at 85-90 C, washing off alkaline-soluble compounds by extraction in rising water flow at the rate 0.3-0.6 mm/s at 60-75 C. Neutralization is carried out with carbon dioxide at 40-60 C. Washing off water-soluble components is carried out similar with washing off alkaline-soluble compounds followed by neutralization with acetic acid and isolation of the end product. EFFECT: increased selective capacity of sorbent.
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Authors
Dates
1996-06-10—Published
1992-12-03—Filed