# US 8,772,001 B2 · Alcohol product processes

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- Number: US 8,772,001 B2
- Document ID: US8772001B2
- Status: Granted
- Kind: B2
- Application number: 12/138,681
- Filed: 2008-06-13
- Published: 2009-01-15
- Granted: 2014-07-08
- Earliest claimed: 2003-03-10
- Assignees: Novozymes A/S
- Applicants: Hans Sejr Olsen; Sven Pedersen; Rikke Monica Festersen
- Inventors: Hans Sejr Olsen; Sven Pedersen; Rikke Monica Festersen
- Web page: https://patentgrep.com/patent/US8772001B2

## CPC

- C12P 7/06: Ethanol, i.e. non-beverage
- C12C 5/004: {Enzymes}
- C12C 7/04: Preparation or treatment of the mash
- C12N 9/2411: {Amylases}
- C12N 9/2414: {Alpha-amylase (3.2.1.1.)}
- C12N 9/2417: {from microbiological source}
- C12N 9/242: {Fungal source}
- C12N 9/2425: {Beta-amylase (3.2.1.2)}
- C12N 9/2428: {Glucan 1,4-alpha-glucosidase (3.2.1.3), i.e. glucoamylase}
- C12P 7/10: substrate containing cellulosic material
- C12P 19/02: Monosaccharides (2-ketogulonic acid C12P7/60)
- C12P 19/14: produced by the action of a carbohydrase {(EC 3.2.x)}, e.g. by alpha-amylase {, e.g. by cellulase, hemicellulase}
- C12Y 302/01001: Alpha-amylase (3.2.1.1)
- C12Y 302/01003: Glucan 1,4-alpha-glucosidase (3.2.1.3), i.e. glucoamylase
- Y02E 50/10: Biofuels, e.g. bio-diesel
- C12P: FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE {(brewing of beer C12C; producing vinegar C12J; producing specific peptides or proteins C07K; producing enzymes C12N9/00; DNA or RNA concerning genetic engineering, vectors, e.g. plasmids, or their isolation, preparation or purification C12N15/00; measuring or testing processes involving enzymes or microorganisms C12Q; measuring or testing processes involving nucleic acid amplification reactions C12Q1/6844; fermentation processes to form a food composition, A21 or A23; compounds in general, see the relevant compound class, e.g. C01, C07)}
- C12C: BEER; PREPARATION OF BEER BY FERMENTATION (ageing or ripening by storing C12H1/22; methods for reducing the alcohol content after fermentation C12H3/00; methods for increasing the alcohol content after fermentation C12H6/00; venting devices for casks, barrels or the like C12L9/00); PREPARATION OF MALT FOR MAKING BEER; PREPARATION OF HOPS FOR MAKING BEER
- C12N: MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA (microbiological testing media C12Q1/00)
- C12Y: ENZYMES
- Y02E: REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION

## Abstract

Processes for production of an alcohol product from granular starch comprising a pre-treatment at an elevated temperature below the initial gelatinization temperature of the granular starch followed by simultaneous saccharification and fermentation, and optionally recovery of ethanol, are described.

## Claims

### Claim 1

A process for production of an alcohol product comprising the sequential steps of:
(a) holding a slurry comprising water and granular starch in the presence of an acid alpha-amylase and a glucoamylase at a temperature of 0° C. to 20° C. below the initial gelatinization temperature of the granular starch for a period between 5 minutes and 12 hours, and
(b) fermenting the slurry in the presence of an acid alpha-amylase, a glucoamylase and a yeast at a temperature between 10° C. and 35° C. to produce the alcohol product,
wherein step (a) is performed in the presence of a cellulase and a xylanase.

### Claim 2 (depends on 1)

The process of claim 1, further comprising recovering the alcohol product.

### Claim 3 (depends on 1)

The process of claim 1, wherein the alcohol product is fuel ethanol, potable ethanol and/or industrial ethanol.

### Claim 4 (depends on 1)

The process of claim 1, wherein the temperature during step (b) is between 29° C. and 35° C.

### Claim 5 (depends on 1)

The process of claim 1, wherein the pH during step (a) is in the range of 3-7.

### Claim 6 (depends on 1)

The process of claim 1, wherein the pH during step (b) is in the range of 3-7.

### Claim 7 (depends on 1)

The process of claim 1, wherein the starch slurry has 5-60% DS granular starch.

### Claim 8 (depends on 1)

The process of claim 1, wherein the granular starch is obtained from tubers, roots, stems, fruits, seeds or whole grain.

### Claim 9 (depends on 1)

The process of claim 1, wherein the granular starch is obtained from corn, cobs, wheat, barley, rye, milo, sago, cassaya, manioc, tapioca, sorghum, rice or potatoes.

### Claim 10 (depends on 1)

The process of claim 1, wherein the granular starch is obtained from cereals.

### Claim 11 (depends on 1)

The process of claim 1, wherein the granular starch is obtained from dry milling or wet milling of whole grain.

### Claim 12 (depends on 1)

The process of claim 1, wherein the acid alpha-amylase and the glucoamylase are present in step (a) in a ratio of between 0.3 and 5.0 Acid Fungal Alpha-amylase Units/AmyloGlucosidase Units (AFAU/AGU).

### Claim 13 (depends on 1)

The process of claim 1, wherein the acid alpha-amylase and the glucoamylase are present in step (b) in a ratio of between 0.3 and 5.0 Acid Fungal Alpha-amylase Units/AmyloGlucosidase Units (AFAU/AGU).

### Claim 14 (depends on 1)

The process of claim 1, wherein the acid alpha-amylase is an acid fungal alpha-amylase.

### Claim 15 (depends on 14)

The process of claim 14, wherein the acid fungal alpha-amylase is obtained from a strain of Aspergillus.

### Claim 16 (depends on 1)

The process of claim 1, wherein the acid alpha-amylase is an acid bacterial alpha-amylase.

### Claim 17 (depends on 16)

The process of claim 16, wherein the acid bacterial alpha-amylase is derived from a strain of B. amyloliquefaciens, B. licheniformis, or B. stearothermophilus.

### Claim 18 (depends on 1)

The process of claim 1, wherein the glucoamylase is obtained from a strain of Aspergillus, Clostridium, or Talaromyces.

### Claim 19 (depends on 1)

The process of claim 1, wherein the glucoamylase is obtained from a strain of Aspergillus niger.

### Claim 20 (depends on 1)

The process of claim 1, further comprising performing step (a) in the presence of a phytase.

### Claim 21 (depends on 1)

The process of claim 1, further comprising performing step (b) in the presence of phytase.

### Claim 22 (depends on 1)

The process of claim 1, further comprising performing steps (a) and (b) in the presence of a phytase.

### Claim 23 (depends on 1)

The process of claim 1, wherein step (b) is performed in the presence of a cellulase and a xylanase.

### Claim 24 (depends on 1)

The process of claim 1, wherein the period in step (a) is between 5 minutes and 1¼ hours.

### Claim 25 (depends on 1)

The process of claim 1, wherein the period in step (a) is between 5 minutes and 1 hour.

### Claim 26 (depends on 1)

The process of claim 1, wherein the period in step (a) is between 40 minutes and 1 hour.

### Claim 27 (depends on 1)

The process of claim 1, wherein the period in step (a) is between 50 minutes and 1 hour.

### Claim 28 (depends on 1)

The process of claim 1, wherein the fermentation in step (b) is for a period between 20 and 250 hours.

### Claim 29 (depends on 1)

The process of claim 1, wherein the temperature during step (a) is 45 to 62° C.

### Claim 30 (depends on 1)

The process of claim 1, further comprising performing step (b) in the presence of a protease.
