Processing biomass

Patent metadata

Field	Value
Publication number	US-2016201151-A1
Application number	US-201514897931-A
Country	US
Kind code	A1
Filing date	Jul 21, 2015
Priority date	Jul 21, 2014
Publication date	Jul 14, 2016
Grant date	—

Abstract

Biomass feedstocks (e.g., plant biomass, animal biomass, and municipal waste biomass) are processed to produce useful products, such as fuels. For example, systems are described that can be useful for separating solids from liquids of bioprocessed biomass material slurries. For example, filtration systems are described that include multiple centrifuges, e.g., multiple tandem centrifuges.

First claim

1 . A filtration method comprising:
utilizing a first centrifuge to remove a first portion of solids from a first slurry of saccharified biomass, producing a second slurry, and utilizing a second centrifuge to remove a second portion of solids from the second slurry, producing a third slurry.

2 . The method of claim 1 , wherein the first centrifuge is operated at a first G-Force and the second centrifuge is operated at a second, different G-Force.

3 . The method of claim 1 , wherein the first G-Force is between about 500 g and about 3000 g.

4 . The method of claim 2 , wherein the second G-Force is between about 2000 g and about 5000 g.

5 . The method of claim 1 , wherein the first slurry contains between about 1 wt. % and 40 wt. % solids.

6 . The method of claim 1 , wherein the second slurry contains between about 1 wt. % and about 10 wt. % solids.

7 . The method of claim 1 , wherein the second slurry contains less than half the solids as compared to the first slurry.

8 . The method of claim 1 , wherein the third slurry contains less than about 3 wt. % solids.

9 . The method of claim 1 , wherein the third slurry contains less than about half the solids as compared to the second slurry.

10 . The method of claim 1 , wherein the first slurry has a median particle size of greater than 100 μm.

11 . The method of claim 1 , wherein the second slurry has a median particle size less than about 100 μm.

12 . The method of claim 1 , wherein the third slurry has a median particle size less than about 10 μm.

13 . The method of claim 1 , wherein the median particle size of the first slurry is greater than the median particle size of the second slurry.

14 . The method of claim 1 , wherein the median particle size of the second slurry is larger than the median particle size of the third slurry.

15 . The method of claim 1 , wherein prior to utilizing the first and/or the second centrifuge, proteins are denatured or precipitated and are substantially removed from said first and/or second slurry.

16 . The method of claim 1 , wherein prior to utilizing the first and/or second centrifuge, proteins are not removed and are left in the solution as dissolved material in the first and/or second slurry.

17 . The method of claim 1 , wherein prior to utilizing the first and/or second centrifuge, proteins are denatured and left in the slurry as a suspension in the first and or second slurry.

18 . The method of claim 1 , wherein the saccharified biomass is fermented prior to utilizing the first centrifuge to remove the first solids.

19 . The method of claim 1 , wherein the first portion of solids is washed and the washing fluid is returned to the first, second and/or third slurry.

20 . The method of claim 1 , wherein the second portion of solids is washed and the washing fluid is returned to the first, the second and/or the third slurry.

21 . The method of claim 1 , further comprising utilizing a third centrifuge to remove a third portion of solids from the third slurry.

22 . A method of processing a slurry, the method comprising:
processing saccharified biomass material through a first and a second centrifuge wherein the slurry is processed at an average rate of at least 10 gal/min.

23 . The method of claim 22 , wherein processing produces a slurry with less than about 3% solids.

24 . The method of claim 22 , wherein the first centrifuge is operated a higher G-Force than the second centrifuge.

Assignees

• Xyleco Inc

Inventors

• Medoff Marshall
• Masterman Thomas Craig
• Roditi Solomon I

Classifications

• Y02E50/10

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

• C13B20/16 Primary

  by physical means, e.g. osmosis or filtration · CPC title

• B01D61/58 Primary

  Multistep processes · CPC title

• C13K13/002

  Xylose · CPC title

• B01D61/02

  Reverse osmosis; Hyperfiltration {; Nanofiltration} · CPC title