Process for purifying lignocellulosic feedstocks

Patent metadata

Field	Value
Publication number	US-9862893-B2
Application number	US-201213469906-A
Country	US
Kind code	B2
Filing date	May 11, 2012
Priority date	May 12, 2011
Publication date	Jan 9, 2018
Grant date	Jan 9, 2018

Abstract

The present invention includes methods for removing mineral acids, mineral salts and contaminants, such as metal impurities, ash, terpenoids, stilbenes, flavonoids, proteins, and other inorganic products, from a lignocellulosic feedstock stream containing organic acids, carbohydrates, starches, polysaccharides, disaccharides, monosaccharides, sugars, sugar alcohols, phenols, cresols, and other oxygenated hydrocarbons, in a manner that maintains a portion of the organic acids and other oxygenated hydrocarbons in the product stream.

First claim

We claim:

1. A method for purifying a biomass-derived feedstock stream, the method comprising:
a. providing a feedstock stream having components comprising (i) water, (ii) mineral acids and/or mineral salts, (iii) one or more species of contaminants selected from the group consisting of terpenoids, stilbenes, flavonoids, proteinaceous materials, metal impurities, ash, and mixtures thereof, and (iv) a mixture of oxygenated hydrocarbons comprising one or more biomass-derived organic acids and one or more biomass-derived oxygenated hydrocarbons selected from the group consisting of carbohydrates, starches, polysaccharides, disaccharides, monosaccharides, sugars, sugar alcohols, sugar degradation products, alditols, polyols, triols, diols, mono-oxygenates, phenols, cresols, and mixtures thereof;
b. providing an anion exchange unit modified with one or more anion modifiers selected from the group consisting of acetic acid, formic acid, propionic acid, malic acid, citric acid, oxalic acid, lactic acid, butyric acid, valeric acid, hexanoic acid, heptanoic acid, aconitic acid, caproic acid, 2-furoic acid, vanillic acid, syringic acid, protocatechuic acid, ferulic acid, p-coumaric acid, sinapic acid, gallic acid, glucuronic acid, galacturonic acid, cellobiouronic acid, aldonic acids, aldaric acids, salts thereof and mixtures thereof, before contact of the anion exchange unit with components of the feedstock stream;
c. providing a cation exchange unit in a form selected from the group consisting of hydrogen, sodium, potassium, calcium, ammonium, and mixtures thereof;
d. contacting components of the feedstock stream with the anion exchange unit and the cation exchange unit to remove greater than 80% of the mineral salts, mineral acids or contaminants from the feedstock stream, thereby producing a product stream comprising water, greater than 90% of the organic acids from the feedstock stream and greater than 90% of the biomass-derived oxygenated hydrocarbons from the feedstock stream; and
e. recycling a portion of the organic acids from the product stream to provide the anion modifier.

2. The method of claim 1 wherein the anion exchange unit and the cation exchange unit are admixed.

3. The method of claim 1 wherein the feedstock stream contacts at least one of the anion exchange unit and the cation exchange unit in a column.

4. The method of claim 1 wherein the feedstock stream contacts at least one of the anion exchange unit and the cation exchange unit in the form of a slurry.

5. The method of claim 1 wherein greater than 90% of the mineral acids, mineral salts or contaminants are removed from the feedstock stream.

6. The method of claim 1 wherein greater than 95% of the mineral acids, mineral salts or contaminants are removed from the feedstock stream.

7. The method of claim 1 wherein essentially all of the mineral acids, mineral salts or contaminants are removed from the feedstock stream.

8. The method of claim 1 further comprising regenerating the anion exchange unit or the cation exchange unit with one or more regenerants, thereby producing an effluent stream comprising the mineral acids, mineral salts or contaminants.

9. The method of claim 1 further comprising concentrating the product stream by evaporation.

10. The method of claim 1 wherein the feedstock stream further comprises an insoluble fraction, the method further comprising filtering the feedstock stream to remove the insoluble fraction prior to contacting the feedstock stream with the anion exchange unit and cation exchange unit.

11. The method of claim 1 wherein the biomass-derived oxygenated hydrocarbon is derived from at least one member selected from the group consisting of hemicellulose, cellulose, lignin, corn stover, wheat straw, barley straw, canola straw, oat straw, rice straw, soybean stover, grass, bagasse, switch grass, miscanthus, sorghum, wood, saw dust, beet pulp, algae, forest waste, and agricultural waste.

12. The method of claim 1 wherein the organic acid is derived from a lignocellulosic hydrolysate.

13. The method of claim 1 wherein the organic acid is derived from one or more of the biomass-derived oxygenated hydrocarbons.

14. A method for purifying a biomass-derived feedstock stream, the method comprising:
a. providing a feedstock stream having components comprising (i) water, (ii) mineral acids and/or mineral salts, (iii) one more species of contaminants selected from the group consisting of terpenoids, stilbenes, flavonoids, proteinaceous materials, metal impurities, ash, and mixtures thereof, and (iv) a mixture of oxygenated hydrocarbons comprising one or more biomass-derived organic acids and one or more biomass-derived oxygenated hydrocarbons selected from the group consisting of carbohydrates, starches, polysaccharides, disaccharides, monosaccharides, sugars, sugar alcohols, sugar degradation products, alditols, polyols, triols, diols, mono-oxygenates, phenols, cresols, and mixtures thereof;
b. providing an anion exchange unit comprising an anion resin modified with one or more anion modifiers selected from the group consisting of acetic acid, formic acid, propionic acid, malic acid, citric acid, oxalic acid, lactic acid, butyric acid, valeric acid, hexanoic acid, heptanoic acid, aconitic acid, caproic acid, 2-furoic acid, vanillic acid, syringic acid, protocatechuic acid, ferulic acid, p-coumaric acid, sinapic acid, gallic acid, glucuronic acid, galacturonic acid, cellobiouronic acid, aldonic acids, aldaric acids, salts thereof and mixtures thereof, before contact of the anion exchange unit with components of the feedstock stream;
c. providing a cation exchange unit comprising a cation resin modified with a cation modifier;
d. contacting components of the feedstock stream with the anion exchange unit and the cation exchange unit to remove greater than 80% of the mineral salts, mineral acids or contaminants from the feedstock stream, thereby producing a first product stream comprising water, greater than 90% of the organic acids from the feedstock stream and greater than 90% of the biomass-derived oxygenated hydrocarbons from the feedstock stream; and
e. recycling a portion of the organic acids from the product stream to provide the anion modifier.

15. The method of claim 14 , further comprising:
f. contacting the anion resin and cation resin with water to produce a second product stream comprising a portion of the biomass-derived oxygenated hydrocarbons from the feedstock stream.

16. The method of claim 15 further comprising:
g. regenerating the anion resin with an anion regenerant, and the cation resin with a cation regenerant, to produce a concentrated anion regenerant stream and a concentrated cation regenerant stream.

17. The method of claim 16 further comprising:
h. rinsing the anion exchange resin and the cation exchange resin with water to produce a dilute anion regenerant stream and a dilute cation regenerant stream.

18. The method of claim 17 further comprising:
i. contacting the anion resin and cation resin with a stream selected from the group consisting of the feedstock stream, second product stream, or a mixture thereof, to produce a third product stream comprising a portion of the biomass-derived oxygenated hydrocarbons from the feedstock stream.

19. The method of claim 14 wherein the cation modifier is selected from the group consisting of hydrogen, sodium, potassium, calcium, ammonium, and mixtures thereof.

20. The method of claim 16 wherein the anion regenerant is derived from the product stre

Assignees

• Gray Matthew
• Matthes Megan
• Nelson Thomas
• Held Andrew
• Virent Inc

Inventors

• Gray Matthew
• Matthes Megan
• Nelson Thomas
• Held Andrew

Classifications

• C10G17/02 Primary

  with acids or acid-containing liquids, e.g. acid sludge · CPC title

• C10G2300/1014

  of vegetal origin · CPC title

• Y02P30/20

  using bio-feedstock · CPC title

• C10G2300/201

  Impurities · CPC title

• C13K1/02

  obtained by saccharification of cellulosic materials (manufacture of fodder A23K10/32) · CPC title