Method of processing lignocellulosic material using an alkaline delignification agent

Patent metadata

Field	Value
Publication number	US-10604777-B2
Application number	US-201415103764-A
Country	US
Kind code	B2
Filing date	Dec 11, 2014
Priority date	Dec 11, 2013
Publication date	Mar 31, 2020
Grant date	Mar 31, 2020

Abstract

The present disclosure relates to a method for obtaining sugar and lignin fractions from lignocellulosic materials and to a method for producing fermentation products using the sugars obtained from the lignocellulose. The present disclosure relates to a method for improving the sugar yield in the enzymatic hydrolysate by introducing a pre-treatment step of hydrothermal hydrolysis and an alkaline delignification step.

First claim

The invention claimed is:

1. Method for fractionation of a lignocellulosic material, the method comprising:
a) Subjecting the lignocellulosic material to an autohydrolysis treatment wherein hemicellulose is at least partially removed from the lignocellulosic material to produce a mixture containing a first liquid phase and a first solid phase;
b) Separating the first solid phase from the first liquid phase;
c) Subjecting the first solid phase to a delignification treatment in a presence of alkaline delignification agent to produce a mixture containing a second solid phase and a second liquid phase containing solubilized lignin, wherein delignification takes place without steam explosion, and wherein the concentration of delignification agent is from 0.1 to 10 wt %, based on the amount of dry matter in first solid phase;
d) Separating the second solid phase from the second liquid phase; and
e) Subjecting the second solid phase to an enzymatic hydrolysis treatment in a presence of enzymes capable of hydrolyzing hemicellulose and cellulose fractions of the second solid phase to produce a mixture containing a third liquid phase and a third solid phase, and
wherein the lignin is precipitated from the second liquid phase by lowering a pH of a mixture and the precipitated lignin is recovered by a separation method which includes filtration, and wherein the second solid phase is not treated with any acid prior to enzymatic hydrolysis.

2. The method according to claim 1 , wherein the alkaline delignification agent is selected from a group consisting of:
sodium hydroxide, sodium carbonate, potassium hydroxide, potassium carbonate, calcium hydroxide, calcium carbonate, lithium hydroxide, lithium carbonate, ammonium hydroxide, ammonia, sodium sulphide, and the corresponding hydrates.

3. The method according to claim 1 , wherein the alkaline delignification agent is added to the first solid phase to obtain a suspension having a pH of above 7.

4. The method according to claim 1 , wherein the autohydrolysis treatment is conducted in conditions corresponding to severity of between 2.0 and 4.5.

5. The method according to claim 1 , wherein the first solid phase is subjected to a steam explosion before said delignification treatment.

6. The method according to claim 1 comprising:
a step of concentrating the third liquid phase.

7. The method for production of microbial lipid according to claim 1 , the method comprising:
a) subjecting the lignocellulosic material to a treatment wherein hemicellulose is at least partially removed from the lignocellulosic material to produce a mixture containing a first liquid phase and a first solid phase;
b) separating the first solid phase from the first liquid phase;
c) subjecting the first solid phase to a delignification treatment in a presence of alkaline delignification agent to produce a mixture containing a second solid phase and a second liquid phase containing solubilized lignin;
d) separating the second solid phase from the second liquid phase; and
e) subjecting the second solid phase to an enzymatic hydrolysis treatment to hydrolyze hemicellulose and cellulose fractions of the second solid phase to produce a mixture containing a third liquid phase of enzymatic hydrolysate and a third solid phase.

8. The method according to claim 1 , wherein the concentration of delignification agent is from 0.1 to 4 wt %, based on the amount of dry matter in first solid phase.

9. The method according to claim 1 , wherein the alkaline delignification agent is added to the first solid phase to obtain a suspension having a pH of between 10 and 13.

10. The method according to claim 1 , wherein the autohydrolysis treatment is conducted in conditions corresponding to severity of between 3.0 and 4.1.

11. The method according to claim 1 , wherein the autohydrolysis treatment is conducted in conditions corresponding to severity of between 3.5 and 4.0.

12. A method for production of microbial lipid, the method comprising:
(i) providing a cultivation medium containing the third liquid phase produced in the method of claim 1 ;
(ii) providing a fermentation broth by inoculating the cultivation medium with an oleaginous microbe;
(iii) incubating said medium inoculated with said oleaginous microbe allowing lipid to accumulate; and
(iv) recovering the lipid from said oleaginous microbe.

Assignees

• Neste Oyj

Inventors

• Vainio Heidi
• Pihlajaniemi Ville
• Sipponen Mika
• Pastinen Ossi
• Lehtomäki Ilkka
• Laakso Simo
• Myllymäki Olavi
• Koskinen Perttu

Classifications

• C12P19/14 Primary

  produced by the action of a carbohydrase {(EC 3.2.x)}, e.g. by alpha-amylase {, e.g. by cellulase, hemicellulase} · CPC title

• C12P19/02

  Monosaccharides (2-ketogulonic acid C12P7/60) · CPC title

• C12P7/64

  Fats; Fatty oils; Ester-type waxes; Higher fatty acids, i.e. having at least seven carbon atoms in an unbroken chain bound to a carboxyl group; Oxidised oils or fats · CPC title

• C12P2201/00

  Pretreatment of cellulosic or lignocellulosic material for subsequent enzymatic treatment or hydrolysis · CPC title

• Y02E50/10

  Biofuels, e.g. bio-diesel · CPC title