Production of ethanol

• US 4,287,303 A
• Filed: 11/13/1979
• Issued: 09/01/1981
• Est. Priority Date: 11/13/1979
• Status: Expired due to Term

• Current Assignee: ALFA Laval AB
• Original Assignee: ALFA Laval AB
• Inventors: Ehnstrom, Lars K. J., Keim, Carroll R., Dahlberg, Bengt I.
• Primary Examiner(s): Penland, R. B.
• Application Number:
  US06/093,068
• Time in Patent Office: 658 Days
• Field of Search: 435/165, 435/162, 435/161, 435/163, 426/492, 426/493, 426/14, 426/16, 426/11, 426/62
• US Class Current: 435/162
• CPC Class Codes: C12N 1/02 Separating microorganisms from their culture media
• CPC Class Codes: C12P 7/06 Ethanol, i.e. non-beverage
• CPC Class Codes: Y02E 50/10 Biofuels, e.g. bio-diesel

Abstract

In the production of ethanol in plants, comprising a fermenter, a centrifugal separator for the recirculation of the yeast to the fermenter and a plant for the separation of a yeast-free flow, coming from the centrifugal separator, into one flow, rich in ethanol, and into one residual flow, the substrate, that is fed to the fermenter must be rid of solid substance, like fibres etc. In the separation of such solid substance a certain amount of substrate has been lost according to the methods utilized hitherto, or an unnecessarily high consumption of water and energy has occurred. According to the invention the solid substance, which is separated from the raw material flow, is washed, preferably countercurrently with said residual flow, which in turn, enriched in substrate, is fed to the fermenter. If a distillative method is used for said separation the residual flow is called slop.

Claims

1. In the method of producing ethanol from a carbohydrate-containing substrate mixed with non-fermentable solids, said method including the steps of continuously separating said substrate and solids into a flow rich in said solids and a substrate flow free from said solids, passing said substrate flow to a fermenter to produce ethanol by fermentation of said carbohydrate in the presence of yeast, withdrawing continuously from the fermenter a discharge stream of fermentation liquor containing yeast and ethanol, centrifugally separating said discharge stream continuously into at least a yeast concentrate flow and a yeast-free ethanol-containing flow, recirculating said yeast concentrate flow to the fermenter, and continuously separating said yeast-free flow into an ethanol-enriched flow and a residual flow, the improvement which comprises contacting at least part of said residual flow with said flow rich in solids to form a mixture, continuously separating said mixture in a plurality of separators into solids from which remaining substrate has been substantially removed and a flow enriched in substrate, and returning said flow enriched in substrate to the fermenter.

2. The method of claim 1, in which said mixture is separated by at least one separating step with a sieve means while said solids are retained against passage through the sieve means.

3. The method of claim 1, in which said mixture is separated by at least one centrifugal separator having a rotor journalled horizontally in bearings and a conveying screw arranged coaxially within the rotor for discharging said solids.

4. The method of claim 1, in which said contacting is effected by passing said residual flow and said flow rich in solids in countercurrent relation to each other through a plurality of separating means connected in series.