Methods for extracting and converting hemicellulose sugars

• US 10,138,217 B2
• Filed: 09/03/2014
• Issued: 11/27/2018
• Est. Priority Date: 09/03/2013
• Status: Active Grant

• Current Assignee: Virdia Ltd
• Original Assignee: Virdia, Inc. (Stora Enso Oyj)
• Inventors: Jansen, Robert, Lapidot, Noa, Hallac, Bassem, Lawson, James Alan, Madsen, Lee, Stout, Brendon, Carden, Adam Tyler, Faison, Michael A, Travisano, Philip, Zviely, Michael
• Primary Examiner(s): Rozof, Timothy R
• Application Number:
  US14/908,458
• Publication Number:
  US 20170210721A1
• Time in Patent Office: 1,546 Days
• CPC Class Codes: C07D 307/50 Preparation from natural products
• CPC Class Codes: C08B 37/0057 beta-D-Xylans, i.e. xylosaccharide, e.g. arabinoxylan, arabinofuronan, pentosans; (beta-1,3)(beta-1,4)-D-Xylans, e.g. rhodymenans; Hemicellulose; Derivatives thereof
• CPC Class Codes: C08H 8/00 Macromolecular compounds derived from lignocellulosic materials pretreatment thereof B27N
• CPC Class Codes: C13K 1/02 obtained by saccharification of cellulosic materials manufacture of fodder A23K10/32
• CPC Class Codes: C13K 11/00 Fructose separation from invert sugar C13K3/00
• CPC Class Codes: C13K 13/002 Xylose

Abstract

The present disclosure relates to methods of producing hemicellulose and conversion products thereof from a biomass. Also provided are hemicellulose products and other conversion products thereof.

Claims

1. A system for producing furfural, wherein the system is configured to produce at least 1.0 ton of furfural for each 2.3 tons of hemicellulose sugars provided, wherein the hemicellulose sugars comprise at least 80% xylose (by weight), wherein the system is configured to catalytically reduce furfural using a dissolved acid catalyst, and wherein the system is configured for processing at least 1.1 tons of hemicellulose sugars per day.

2. The system of claim 1, wherein the hemicellulose sugars comprise at least 1 C6 sugar selected from the group consisting of glucose, mannose, and galactose.

3. The system of claim 1, wherein the hemicellulose sugars further comprise arabinose.

4. The system of claim 1, wherein the hemicellulose sugars comprise at least 90% xylose (wt/wt).

5. The system of claim 1, further comprising a reaction control unit configured to adjust temperature or reaction residence time in a reactor based on chemical composition of the hemicellulose sugars.

6. The system of claim 1, further comprising a dilution control unit that controls:

a) an amount or a concentration of an acid and a salt in an aqueous sugar stream;

b) a concentration of the hemicellulose sugars in the aqueous sugar stream, and

c) an amount of purge water released from the system.

7. The system of claim 6, wherein the dilution control unit adjusts the salt concentration in the aqueous sugar stream to about 5% (wt/wt).

8. The system of claim 6, wherein the dilution control unit adjusts the-concentration of the hemicellulose sugars in the aqueous sugar stream to 2-10% (wt/wt).

9. The system of claim 6, wherein the system comprises a dilution tank operably connected to the dilution control unit and a furfural-depleted aqueous stream from a separation module of the system, and wherein the furfural-depleted aqueous stream comprises water, acid and salt.

10. The system of claim 1, wherein the system comprises an extraction module for extracting hydrophilic impurities from an organic phase solvent by contacting in a counter current mode with an aqueous phase comprising acid and salt.

11. The system of claim 1, wherein the system is configured to recycle at least 60% of a furfural-depleted aqueous solution.

12. The system of claim 1, wherein the system comprises a preheating unit for preheating an organic solvent and an output to transfer the organic solvent to a reactor.

13. The system of claim 1, wherein the system comprises a separation module, wherein the separation module is configured for separating furfural, an aqueous stream, and an organic solvent stream.

14. The system of claim 1, wherein the system comprises a solvent feed tank, a dilution feed tank, a reactor downstream of the solvent feed tank and the dilution feed tank, and a separation module downstream of the reactor;

wherein the separation module is configured for separating furfural, an aqueous stream, and an organic solvent stream;

wherein (i) the solvent feed tank is configured to preheat solvent separated by and exiting from the separation module;

(ii) the dilution feed tank is configured to dilute the hemicellulose sugars with the aqueous stream separated by and exiting from the separation module; and

(iii) the reactor is configured to maintain the preheated solvent and the diluted hemicellulose sugars at a set temperature and pressure thereby converting xylose from the hemicellulose sugars into furfural.

15. The system of claim 14, wherein the separation module comprises one or more distillation columns.

16. The system of claim 1, wherein the system is operable on a continuous basis.

17. The system of claim 1, comprising an aqueous solution recycling loop and an organic solvent recycling loop.

18. The system of claim 1, wherein the system comprises a separation module for separating a reaction mixture into a furfural-enriched product stream, an aqueous stream and an organic solvent stream, wherein (i) the furfural-enriched product stream has a furfural purity of at least 90%;

(ii) the aqueous stream comprises acid and less than 1% (wt/wt) organic solvent and less than 2% (wt/wt) hemicellulose sugars; and

(iii) the organic solvent stream comprises an S5 solvent and less than 1% (wt/wt) non-S5 solvent impurities.