Process for the production of ethanol and butanol

• US 8,697,405 B2
• Filed: 02/19/2009
• Issued: 04/15/2014
• Est. Priority Date: 03/11/2008
• Status: Expired due to Fees

• Current Assignee: Jupeng Bio (HK) Limited
• Original Assignee: Ineos USA LLC (Ineos AG)
• Inventors: Bell, Peter Simpson, Benstead, Stephen John, Turnbull, Neil
• Primary Examiner(s): Kim, Taeyoon
• Assistant Examiner(s): Patury, Srikanth
• Application Number:
  US12/736,102
• Publication Number:
  US 20100330640A1
• Time in Patent Office: 1,881 Days
• Field of Search: 435/161, 435/136, 435/160
• US Class Current: 435/161
• CPC Class Codes: C12P 7/08 produced as by-product or from waste or cellulosic material substrate
• 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
• CPC Class Codes: Y02E 50/30 Fuel from waste, e.g. synthetic alcohol or diesel

Abstract

The present invention relates to a process for the production of ethanol comprising both gasification and fermentation of feedstocks, and, in particular to a process for the production of ethanol comprising: a) passing a biomass feedstock to a first fermentation step wherein it is subjected to anaerobic fermentation at a pH below 6.0 and at a temperature in the range 20 to 700C to convert the biomass to a solution comprising acetic acid as the predominant product, b) passing a gasifiable feedstock to a gasification step wherein it is subjected to gasification to produce a gaseous mixture comprising carbon monoxide and hydrogen, and c) passing the solution comprising acetic acid from step (a) and the gaseous mixture from step (b) to one or more further fermentation steps wherein they are subject to fermentation to produce ethanol.

Claims

1. A process for the production of ethanol and butanol using at least two separate fermentation steps comprising:

a) first fermentation step wherein a biomass feedstock is subjected to anaerobic fermentation in the presence of solventogenic bacteria comprising a mixture of bacterial strains, at a pH below 6.0 and at a temperature in the range 20 to 70 degree C. to convert the biomass feedstock to a first solution comprising acetic acid and butyric acid as the predominant products and a gasifiable feedstock residue;

wherein the ratio of acetic acid to butyric acid is at least 4;

1,

b) treating said first solution predominantly comprising acetic acid and butyric acid of step (a) to produce a second solution by;

(i) separating said first solution from said gasifiable feedstock residue; and

(ii) separating said bacteria from said first solution;

optionally pasteurizing or sterilizing said first solution;

c) passing said gasifiable feedstock residue to a gasification step wherein it is subjected to gasification to produce a gaseous mixture comprising carbon monoxide and hydrogen, and

d) passing said second solution from step (b) and said gaseous mixture from step (c) to one or more fermentation steps in the presence of anaerobic acetogenic bacteria comprising a mixture of bacterial strains to thereby produce ethanol and butanol.

2. A process according to claim 1, wherein the pH in the first fermentation step is maintained in the range 3 to 5.5 and the temperature in the first fermentation step is in the range 40 to 60.degree. C.

3. A process according to claim 1, wherein the first solution comprises a concentration of acetic acid in solution of 1 to 5 wt %.

4. A process according to claim 1, wherein the gasification step (c)-comprising adding methane or coal.

5. A process according to claim 1, wherein gasification step (c) comprises a co-feed comprising of landfill gas which is a mixture of predominantly methane, carbon dioxide and hydrogen sulphide obtained at a landfill site.

6. A process according claim 1 wherein said ethanol and butanol from step (d) comprises ethanol at a concentration of ethanol in solution in the range 1 to 5 wt % and butanol at a concentration of butanol in solution in the range 0.2 to 1 wt %.

7. A process according to claim 1 wherein the ethanol from step (d) is purified to 90-95 wt % ethanol by distillation followed by a drying step to give a >

99 wt % ethanol.