Processes for producing cellulose pulp, sugars, and co-products from lignocellulosic biomass

Patent metadata

Field	Value
Publication number	US-9347176-B2
Application number	US-201314044784-A
Country	US
Kind code	B2
Filing date	Oct 2, 2013
Priority date	Oct 4, 2012
Publication date	May 24, 2016
Grant date	May 24, 2016

Abstract

The GreenBox+ technology is suitable to extract hemicellulose sugars prior to pulping of biomass into pulp products. The revenue obtainable from the sugar stream can significantly improve the economics of a pulp and paper mill. An initial extraction and recovery of sugars is followed by production of a pulp product with similar or better properties. Other co-products such as acetates and furfural are also possible. Some variations provide a process for co-producing pulp and hemicellulosic sugars from biomass, comprising: digesting the biomass in the presence of steam and/or hot water to extract hemicellulose into a liquid phase; washing the extracted solids, thereby generating a liquid wash filtrate and washed solids; separating the liquid wash filtrate from the washed solids; refining the washed solids at a refining pH of about 4 or higher, thereby generating pulp; and hydrolyzing the hemicellulose to generate hemicellulosic fermentable sugars.

First claim

What is claimed is:

1. A process for co-producing corrugated medium pulp or paper pulp as well as hemicellulosic sugars from biomass, said process comprising:
(a) providing lignocellulosic biomass comprising cellulose, hemicellulose, and lignin;
(b) digesting said biomass in the presence of steam and/or hot water to extract at least a portion of said hemicellulose into a liquid phase, thereby generating extracted solids, wherein step (b) does not include a chemical pulping method;
(c) separating at least some of said liquid phase from said extracted solids;
(d) washing said extracted solids with water at a washing pH of about 7 or less, thereby generating a liquid wash filtrate and washed solids;
(e) separating at least some of said liquid wash filtrate from said washed solids;
(f) refining said washed solids at a refining pH of 4 to 6.5, thereby generating corrugated medium pulp or paper pulp; and
(g) hydrolyzing said hemicellulose contained in said liquid phase and/or in said liquid wash filtrate, in the presence of a hydrolysis catalyst, to generate hemicellulosic sugars,
wherein step (c) is performed prior to step (d), wherein said liquid phase separated in step (c) and said liquid wash filtrate are separately processed and not later combined.

2. The process of claim 1 , wherein step (b) is conducted at a digestor temperature selected from about 140° C. to about 220° C.

3. The process of claim 1 , wherein step (b) is conducted at a digestor residence time selected from about 1 minute to about 60 minutes.

4. The process of claim 1 , wherein step (b) is conducted at a digestor pH from about 2 to about 6.

5. The process of claim 1 , wherein said corrugated medium pulp or paper pulp yield on biomass is from about 75% to about 95% by weight.

6. The process of claim 1 , wherein said washing in step (d) utilizes fresh water.

7. The process of claim 1 , wherein said washing in step (d) utilizes alkali-free recycled water.

8. The process of claim 1 , wherein steps (b) and (d) are carried out in a single unit.

9. The process of claim 1 , wherein said refining pH is selected from 4 to 6.

10. The process of claim 1 , wherein said refining pH is selected from 6 to 6.5.

11. The process of claim 1 , wherein said hydrolysis catalyst comprises one or more compounds selected from the group consisting of sulfur dioxide, sulfurous acid, sulfuric acid, lignosulfonic acid, and combinations or derivatives thereof.

12. The process of claim 1 , wherein said hydrolysis catalyst comprises hemicellulase enzymes.

13. The process of claim 1 , wherein said corrugated medium pulp or paper pulp is characterized by a concora of about 25 lbf or higher.

14. The process of claim 1 , wherein said corrugated medium pulp or paper pulp is characterized by a ring crush strength of about 25 (lbf/6 in) or higher.

15. The process of claim 1 , wherein said corrugated medium pulp or paper pulp is characterized by a breaking length of about 2.0 km or higher.

16. The process of claim 1 , wherein at least a portion of said corrugated medium pulp or paper pulp is hydrolyzed to generate glucose.

17. The process of claim 1 , said process further comprising recovering an acetic acid or acetate co-product.

18. The process of claim 1 , wherein at least a portion of said corrugated medium pulp or paper pulp is converted to corrugated medium or paper.

Assignees

• Api Ip Holdings Llc

Inventors

• Retsina Theodora
• Pylkkanen Vesa
• Rutherford Steven R

Classifications

• D21C11/0007

  Recovery of by-products, i.e. compounds other than those necessary for pulping, for multiple uses or not otherwise provided for (volatile compounds obtained by decomposition of spent liquors in order to regenerate them D21C11/125; compounds obtained by fractionating the liquors in order to regenerate them D21C11/0042) · CPC title

• D21C3/20

  with organic solvents {or in solvent environment} · CPC title

• C08H8/00

  Macromolecular compounds derived from lignocellulosic materials {(pretreatment thereof B27N)} · CPC title

• D21C3/222

  Use of compounds accelerating the pulping processes · CPC title

• D21C3/08

  calcium bisulfite · CPC title