IP Library › Granted Patent US 9,447,280
Granted Patent B2
US 9,447,280 · App. 14/570,815 · Granted Sep 20, 2016

Derivatives of native lignin from annual fibre feedstocks

Inventors: Mikhail Yurevich Balakshin (North Vancouver, CA); Alex Berlin (Burnaby, CA); Humbert Thomas Dellicolli (Hanahan, SC); Chadrick Adam Nathaniel Jordan Grunert (Vancouver, CA); Vera Maximenko Gutman (Burnaby, CA); Darwin Ortiz (Delta, CA); Edward Kendall Pye (Media, PA)
Assignee: FIBRIA INNOVATIONS LTD.
C08L97/005A23K10/32A23L1/3002A61K36/15A61K36/48A61K36/54A61K36/76C07G1/00C08H6/00C08J3/00C08K5/13C08L23/02C08L57/00C09K15/06D21C11/0007D21H11/00C08J2397/00C08L2207/04Y02P20/582Y02P60/877
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Quick Facts
Patent No.
US 9,447,280
App. No.
14/570,815
Granted
Sep 20, 2016
Kind
B2
Abstract

The present invention provides derivatives of native lignin having certain aliphatic hydroxyl content. Surprisingly, it has been found that consistent and predictable antioxidant activity may be provided by selecting for derivatives of native lignin having certain aliphatic hydroxyl content.

Claims (11)

1. A method of producing an annual fibre lignin derivative having an aliphatic hydroxyl content of from about 1 mmol/g to 3.25 mmol/g, a normalized RSI of 15 or greater, and a weight average molecular weight of from about 500 g/mol to about 5000 g/mol, comprising:

a) pulping an annual fibre biomass by a pulping process selected from the group consisting of: steam explosion, acid hydrolysis, ammonia fiber expansion, autohydrolysis, sulphite pulping and modifications thereof, kraft process and modifications thereof, soda pulping and modifications thereof, and organosolv process;

b) heating the pulp;

c) maintaining the elevated temperature for 1 minute or longer;

d) separating the cellulosic pulp from the lignin rich pulp; and

e) recovering derivatives of native lignin, wherein the derivatives have an aliphatic hydroxyl content of from about 1 mmol/g to about 3.25 mmol/g, a weight average molecular weight of from about 500 g/mol to about 5000 g/mol, and a normalized RSI of 15 or greater.

2. The method according to claim 1 , wherein the pulping process is steam explosion.

3. The method according to claim 1 , wherein the pulping process is an organosolv process.

4. The method according to claim 1 , wherein the pulping process is sulphite pulping.

5. The method according to claim 1 , wherein the pulping process is acid hydrolysis.

6. The method according to claim 1 , wherein the pulping process is kraft process and modifications thereof.

Assignments (2)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 28, 2019
From: FIBRIA INNOVATIONS INC.
To: SUZANO CANADA INC.
Reel/Frame 051135/0966 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 19, 2015
From: LIGNOL INNOVATIONS LTD.
To: FIBRIA INNOVATIONS INC.
Reel/Frame 037086/0053 →
Continuity (5)
Continuation 13826817 · Mar 14, 2013
Continuation 12705939 · Feb 15, 2010
Provisional Application 61233345 · Aug 12, 2009
Provisional Application 61182044 · May 28, 2009
Related Publication 20150299951A1 · Oct 22, 2015