Fermentable sugar from the hydrolysis of carbohydrate polymer

• US 4,421,856 A
• Filed: 11/12/1981
• Issued: 12/20/1983
• Est. Priority Date: 11/12/1981
• Status: Expired due to Fees

• Current Assignee: National Distillers and Chemical Corporation
• Original Assignee: National Distillers and Chemical Corporation
• Inventors: Miller, Franklyn D., Muller, Werner C.
• Primary Examiner(s): Smith, William F.
• Application Number:
  US06/320,277
• Time in Patent Office: 768 Days
• Field of Search: 435/161, 435/163, 435/165, 127/37, 127/38, 127/39, 127/40, 127/36, 127/56, 203/19, 203/DIG. 13
• US Class Current: 435/161
• CPC Class Codes: C12F 3/10 from distillery slops
• CPC Class Codes: C12P 7/06 Ethanol, i.e. non-beverage
• CPC Class Codes: C13K 1/02 obtained by saccharification of cellulosic materials manufacture of fodder A23K10/32
• CPC Class Codes: C13K 1/06 obtained by saccharification of starch or raw materials containing starch
• CPC Class Codes: Y02E 50/10 Biofuels, e.g. bio-diesel
• CPC Class Codes: Y10S 203/14 Ejector-eductor

Abstract

The yield of fermentable sugar, largely glucose (dextrose), resulting from the acid catalyzed hydrolysis of a carbohydrate polymer such as starch or cellulose can be significantly increased by the addition to the hydrolysate under acid hydrolysis conditions of water soluble non-fermentable carbohydrate such as stillage recovered from a downstream ethanol distillation facility.

Claims

1. In the acid hydrolysis of carbohydrate polymer in which an aqueous slurry of carbohydrate polymer selected from the group consisting of starch and cellulose is hydrolyzed at elevated pressure and temperature in the presence of an acid catalyst to provide a hydrolysate comprising a sterile aqueous solution of fermentable sugar, the improvement which comprises carrying out hydrolysis in the presence of added aqueous water soluble non-fermentable carbohydrate.

2. The process of claim 1 wherein a preliminary hydrolysis step is followed by a further hydrolysis step and following said preliminary hydrolysis the temperature and pressure of the partial hydrolysate is at least partially reduced.

3. The process of claim 1 wherein the carbohydrate polymer is starch derived from wet milled cereal grain or starch derived from amylaceous root or tuber.

4. The process of claim 1 wherein the carbohydrate polymer is cellulose.

5. The process of claim 1 wherein the carbohydrate polymer is starch derived from wet milled corn or milo.

6. The process of claim 1 wherein the hydrolysate is fermented to provide dilute aqueous ethanol, the dilute aqueous ethanol is concentrated by distillation and the stillage resulting from said distillation is used as the source of added water soluble non-fermentable carbohydrate in the hydrolysis of a further quantity of hydrolysate.

7. The process of claim 1 wherein the carbohydrate polymer feed is slurried with stillage.

8. The process of claim 6 wherein the acid hydrolysis catalyst is neutralized with base prior to subjecting the hydrolysate to fermentation.

9. The process of claim 8 wherein salt resulting from neutralization of hydrolysis catalyst is reconverted to acid by contact with a strong acid ion exchange resin.