IP Library Granted Patent US 10,787,527
Granted Patent B2
US 10,787,527 · App. 16/175,213 · Granted Sep 29, 2020

Polymeric acid catalysts and uses thereof

Inventors: John M. Geremia (Watertown, MA); Brian M. Baynes (Winchester, MA); Ashish Dhawan (Naperville, IL)
Assignee: Cadena Bio, Inc.
C08F8/36B01J31/06C08F8/24C08F8/30C08F8/32C08F8/40C08F8/42C08F8/44C08F12/18C08F212/08C08F212/14C08F226/08C08G8/28C08H8/00
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Quick Facts
Patent No.
US 10,787,527
App. No.
16/175,213
Granted
Sep 29, 2020
Kind
B2
Abstract

Disclosed are methods for producing a downstream product from cellulosic material by: a) contacting the cellulosic material with a polymer and a solvent to form a reaction mixture, where the polymer includes acidic monomers and ionic monomers connected to form a polymeric backbone, and each of the ionic monomers independently comprises at least one nitrogen-containing cationic group or at least one phosphorous-containing cationic group; b) degrading the cellulosic material in the reaction mixture to produce a liquid phase and a solid phase, where the liquid phrase includes one or more sugars, and where the solid phase includes residual cellulosic material; and c) using the one or more sugars to produce the downstream product.

Claims (19)

1. A method for producing a downstream product from cellulosic material, the method comprising:

a) contacting the cellulosic material with a polymer and a solvent to form a reaction mixture, wherein the polymer comprises acidic monomers and ionic monomers connected to form a polymeric backbone, and each of the ionic monomers independently comprises at least one nitrogen-containing cationic group or at least one phosphorous-containing cationic group;

b) degrading the cellulosic material in the reaction mixture to produce a liquid phase and a solid phase, wherein the liquid phase comprises one or more sugars, and wherein the solid phase comprises residual cellulosic material; and

c) using the one or more sugars to produce the downstream product.

2. The method of claim 1 , further comprising isolating at least a portion of the liquid phase from the solid phase.

3. The method of claim 2 , further comprising recovering the one or more sugars from the isolated liquid phase.

4. The method of claim 1 , wherein the solvent comprises water.

5. The method of claim 1 , wherein the one or more sugars are one or more monosaccharides, one or more oligosaccharides, or a mixture thereof.

6. The method of claim 5 , wherein the one or more sugars are selected from the group consisting of glucose, galactose, fructose, xylose, and arabinose.

7. The method of claim 1 , further comprising pretreating the cellulosic material before contacting the cellulosic material with the polymer.

8. The method of claim 7 , wherein the pretreatment of the cellulosic material is selected from the group consisting of washing, solvent-extraction, solvent-swelling, comminution, milling, steam pretreatment, explosive steam pretreatment, dilute acid pretreatment, hot water pretreatment, alkaline pretreatment, lime pretreatment, wet oxidation, wet explosion, ammonia fiber explosion, organosolvent pretreatment, biological pretreatment, ammonia percolation, ultrasound, electroporation, microwave, supercritical CO 2 , supercritical H 2 O, ozone, gamma irradiation, and combinations thereof.

9. The method of claim 1 , the residual cellulosic material has a degree of polymerization of less than 300.

10. The method of claim 1 , wherein the degrading of the cellulosic material to produce the one or more sugars occurs at a first-order rate constant of at least 0.001 per hour.

11. The method of claim 1 , wherein each of the acidic monomers comprises at least one Bronsted-Lowry acid.

12. The method of claim 11 , wherein the Bronsted-Lowry acid at each occurrence in the polymer is independently selected from the group consisting of sulfonic acid, phosphonic acid, acetic acid, isophthalic acid, boronic acid, and perfluorinated acid.

13. The method of claim 1 , wherein the downstream product comprises a biofuel, a vitamin, a lipid, or a protein.

14. The method of claim 13 , wherein the downstream product comprises a biofuel, and the biofuel comprises ethanol.

15. The method of claim 1 , wherein steps b) and c) comprise separate hydrolysis and fermentation (SHF), simultaneous saccharification and fermentation (SSF), simultaneous saccharification and co-fermentation (SSCF), hybrid hydrolysis and fermentation (HHF), separate hydrolysis and co-fermentation (SHCF), hybrid hydrolysis and co-fermentation (HHCF), or direct microbial conversion (DMC).

16. The method of claim 1 , wherein bacteria or yeast are used to ferment the one or more sugars to produce the downstream products.

Assignments (7)
CORRECTIVE ASSIGNMENT TO CORRECT THE THE SECOND ASSIGNOR NAME PREVIOUSLY RECORDED AT REEL: 061404 FRAME: 0320. ASSIGNOR(S) HEREBY CONFIRMS THE ASSIGNMENT. Recorded Oct 18, 2022
From: KALEIDO BIOSCIENCES, INC.; CADENA BIO, INC.
To: HERCULES CAPITAL, INC.
Reel/Frame 061700/0414 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Sep 10, 2022
From: HERCULES CAPITAL, INC.
To: DSM NUTRITIONAL PRODUCTS, LLC
Reel/Frame 061362/0001 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Sep 9, 2022
From: KALEIDO BIOSCIENCES, INC.; CARDENA BIO, INC.
To: HERCULES CAPITAL, INC.
Reel/Frame 061404/0320 →
CHANGE OF NAME Recorded Jun 12, 2020
From: MIDORI RENEWABLES, INC.
To: MIDORI USA, INC.
Reel/Frame 052928/0363 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 12, 2020
From: GEREMIA, JOHN M.; BAYNES, BRIAN M.
To: MIDORI RENEWABLES, INC.
Reel/Frame 052922/0374 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 12, 2020
From: DHAWAN, ASHISH
To: MIDORI RENEWABLES, INC.
Reel/Frame 052922/0436 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 12, 2020
From: MIDORI USA, INC.
To: CADENA BIO, INC.
Reel/Frame 052922/0658 →
Continuity (5)
Continuation 14730143 · Jun 3, 2015
Continuation 13406490 · Feb 27, 2012
Provisional Application 61447311 · Feb 28, 2011
Provisional Application 61522351 · Aug 11, 2011
Related Publication 20190062468A1 · Feb 28, 2019
Cited By (4)
US 12,410,206 US 12,508,274 US 12,514,267 US 12,661,366