Enhanced efficiency ethanol and sugar conversion processes

• US 9,752,164 B2
• Filed: 06/14/2013
• Issued: 09/05/2017
• Est. Priority Date: 06/15/2012
• Status: Active Grant

• Current Assignee: Microvi Biotech, Inc.
• Original Assignee: Microvi Biotech, Inc.
• Inventors: Razavi-Shirazi, Fatemeh, Razavi, Ameen, Balmer, Norman Louis
• Primary Examiner(s): Lankford, Blaine
• Assistant Examiner(s): Van Buren, Lauren K
• Application Number:
  US13/918,838
• Publication Number:
  US 20130337517A1
• Time in Patent Office: 1,544 Days
• Field of Search: None
• CPC Class Codes: C12N 11/04 entrapped within the carrier, e.g. gel or hollow fibres
• CPC Class Codes: C12N 11/082 obtained by reactions only involving carbon-to-carbon unsaturated bonds
• CPC Class Codes: C12N 11/084 Polymers containing vinyl alcohol units
• CPC Class Codes: C12N 11/087 Acrylic polymers
• CPC Class Codes: C12N 11/089 obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
• CPC Class Codes: C12N 11/093 Polyurethanes
• CPC Class Codes: C12N 11/096 Polyesters; Polyamides
• CPC Class Codes: C12P 2203/00 Fermentation products obtained from optionally pretreated or hydrolyzed cellulosic or lignocellulosic material as the carbon source
• CPC Class Codes: C12P 7/10 substrate containing cellulosic material
• CPC Class Codes: C12P 7/14 Multiple stages of fermentation; Multiple types of microorganisms or re-use of microorganisms
• CPC Class Codes: Y02E 50/10 Biofuels, e.g. bio-diesel

Abstract

Overlay processes are disclosed for making ethanol that not only increase ethanol conversion but do so in a cost effective manner with a reduction in energy requirements per unit of ethanol production. The processes can provide, if desired, higher organic compound as a co-product with ethanol.

Claims

1. A process for producing ethanol by the fermentation of biomass containing carbohydrate comprising:

a. hydrolyzing an admixture of water, enzyme and biomass under hydrolyzing conditions sufficient to convert carbohydrate by enzymatic hydrolysis and provide a hydrolysate containing pentose and hexose;

b. subjecting at least a portion of the hydrolysate of step (a) to fermentation conditions sufficient to convert at least a portion of the hexose to ethanol to provide an ethanol-containing fermentation broth containing solids and pentose, said fermentation conditions comprising the presence of microorganism capable of converting hexose to ethanol, and said ethanol-containing fermentation broth containing solids;

c. fractionating by distillation at least a portion of the ethanol-containing fermentation broth of step (b) to provide an ethanol product fraction and a whole stillage containing water, solids and unfermented sugars comprising pentose;

d. separating at least a portion of the whole stillage of step (c) to provide a thin stillage containing pentose and having an essential absence of solids and to provide a solids-containing fraction;

e. contacting under fermentation conditions in a fermentation zone at least a portion of the thin stillage of step (d) with biocatalyst said biocatalyst comprising;

i. a solid structure of hydrated hydrophilic polymer defining an interior structure having a plurality of interconnected major cavities having a smallest dimension of between about 5 and 100 microns and a Hydration Expansion Volume (HEV), which is calculated in volume percent, of about 1000 or more, and

ii. a population of microorganisms capable of converting pentose to ethanol substantially irreversibly retained in the interior of the solid structure, said population of microorganisms being in a concentration of about 60 grams per liter or more based upon the volume defined by the exterior of the solid structure when fully hydrated, to provide a treated thin stillage having a reduced pentose content and substantially no solids;

f. withdrawing the treated thin stillage from the fermentation zone of step (e) while retaining the biocatalyst in the fermentation zone;

g. evaporating water and ethanol from at least a portion of the treated thin stillage of step (f) to provide a concentrated solubles product and vapor; and

h. passing at least a portion of the evaporated water and ethanol of step (g) to step (a).

2. The process of claim 1 wherein the fermentation of step (b) produces metabolites in addition to ethanol, the fermentation of step (e) converts at least a portion of the metabolites, and an aliquot portion of the treated thin stillage of step (e) is passed to step (a).

3. The process of claim 1 wherein the evaporating of step (g) is conducted in at least two effects, and vapor from at least the first effect is passed to the fractionation of step (c), and vapor from at least the last effect is passed to step (a).

4. The process of claim 1, wherein the thin stillage of step (d) comprises fermentable sugars in a concentration between about 10 and 50 grams per liter.

5. The process of claim 1, wherein the thin stillage of step (d) comprises fermentable sugars in a concentration between about 3 and 40 grams per liter.