Production of ethanol

• US 4,358,536 A
• Filed: 02/22/1980
• Issued: 11/09/1982
• Est. Priority Date: 02/27/1979
• Status: Expired due to Term

• Current Assignee: ALFA Laval AB
• Original Assignee: ALFA Laval AB
• Inventors: Thorsson, Conny R., Viira, Indrek J.
• Primary Examiner(s): BASCOMB JR, WILBUR
• Application Number:
  US06/123,716
• Time in Patent Office: 991 Days
• Field of Search: 435/161, 435/162, 435/163-165, 159/47 R, 159/24 A, 159/17 R, 426/11, 426/14, 426/494, 426/493, 426/11, 203/19, 203/87, 203/22, 203/25, 203/47, 203/27, 203/95, 203/DIG. 13, 203/71-85, 202/174, 202/153
• US Class Current: 435/161
• CPC Class Codes: C12P 7/06 Ethanol, i.e. non-beverage
• CPC Class Codes: Y02E 50/10 Biofuels, e.g. bio-diesel
• CPC Class Codes: Y10S 203/14 Ejector-eductor

Abstract

A flow of fermenting liquor from a fermentor is separated into a yeast concentrate flow, which is recirculated to the fermentor, and a yeast-free flow which is separated in a simple evaporator unit into a first ethanol-enriched vapor flow and a first liquid bottom flow. The first vapor flow is treated to produce the desired ethanol while a major part of the first liquid bottom flow is recirculated to the fermentor. A minor, residual part of the latter flow is fed to a stripping unit where it is separated into a second ethanol-enriched vapor flow and a second liquid bottom flow exhausted of ethanol.

Claims

1. In the production of ethanol from a substrate containing carbohydrate, the method which comprises the continuous steps of delivering the substrate to a fermentor to provide a fermenting liquor, feeding a flow of said liquor from the fermentor to a separating unit and there separating the liquor into a yeast concentrate flow and a yeast-free flow, recirculating said yeast concentrate flow to the fermentor, feeding said yeast-free flow to a simple evaporator unit and there separating it into a first ethanol-enriched vapor flow and a first liquid bottom flow, treating said first vapor flow to produce ethanol of a desired quality, recirculating a major part of said first liquid bottom flow to the fermentor, feeding a minor residual part of said first liquid bottom flow to a stripping unit, and separating said residual part in the stripping unit into a second ethanol-enriched vapor flow and a second liquid bottom flow exhausted of ethanol.

2. The method of claim 1, comprising also feeding at least a major part of said second ethanol-enriched vapor flow to said evaporator unit.

3. The method of claim 1, comprising also combining at least part of said second ethanol-enriched vapor flow with said first ethanol-enriched vapor flow.

4. The method of claim 1, in which said first vapor flow is treated in a rectifying column to produce said ethanol of a desired quality, the method comprising also feeding at least part of said second vapor flow to said rectifying column as a heating medium.

5. The method of claim 1, in which said first vapor flow is treated in a rectifying column to produce said ethanol of a desired quality, the method comprising also feeding at least part of at least one of said first and second vapor flows to a thermo compressor, and heating said rectifying column by said thermo compressor.

6. The method of claim 1, in which said treating of said first vapor flow includes feeding at least part of it to the lowest distilling stage in a rectifying column, the method comprising also recirculating a liquid flow from said lowest stage to the evaporator unit.

7. The method of claim 1, in which the energy for the separation in said evaporator unit is supplied at least partly in the form of external live steam.

8. The method of claim 1, in which at least part of the energy for the separation in said evaporator unit is supplied indirectly by heat exchange.

9. The method of claim 8, in which external steam is used for said heat exchange.

10. The method of claim 1, in which said stripping unit includes a plurality of evaporator stages coupled in series, the vapor flow from one evaporator stage being fed to the previous stage while the bottom flow from said previous stage is fed to said one stage.

11. The method of claim 1, in which at least one of said separations is performed at substantially atmospheric pressure.

12. The method of claim 1, in which at least one of said separations is performed at subatmospheric pressure.

13. The method of claim 1, in which said simple evaporator unit and said stripping unit are combined in a single column, said yeast-free flow being fed to the upper portion of the column where the evaporator unit is located, said first liquid bottom flow being discharged from the column at a level located at the lower portion of the evaporator unit and being divided to form said major part and said minor residual part, said minor residual part of said first bottom flow being fed to the lower portion of said column where said stripping unit is located, said second ethanol-enriched vapor flow passing upwardly in said lower portion of the column and leaving the stripping unit at about said level.

14. The method of claim 13, in which said second ethanol-enriched vapor flow is passed directly through said level and into the evaporator unit.