Process for the production of ethanol and butanol

1. A process for the production of methane, ethanol and butanol using three separate fermentation steps comprising:

a) first fermentation step comprising fermenting initial feedstock to anaerobic fermentation in the presence of acetogenic bacteria, further comprising a mixture of bacterial strains, at a pH below 6.0, at a temperature in the range 20 to 70 degree C., converting said initial feedstock to a product predominantly comprising acetic acid and butyric acid; wherein ratio of acetic acid to butyric acid is at least 2:1;

treating said product predominantly comprising acetic acid and butyric acid to separate a solution comprising the acetic acid and butyric acid by:

(i) separating residual solids; and

(ii) separating bacteria; optionally pasteurizing; optionally sterilizing said solution comprising the acetic acid and butyric acid;

b) second fermentation step comprising fermenting in the presence of solventogenic bacteria said solution comprising the acetic acid and butyric acid from step a) to form ethanol and butanol;

c) third fermentation step comprising a portion of said feedstock to said first fermentation step is anaerobically digested by a methanogenic bacteria to produce methane; optionally a portion of said solution comprising the acetic acid and butyric acid is anaerobically digested by a methanogenic bacteria in said third fermentation step to produce methane.

2. A process for the production of methane, ethanol and butanol using three separate fermentation steps-comprising:

a) first fermentation step comprising fermenting initial feedstock to anaerobic fermentation in the presence of acetogenic bacteria, further comprising a mixture of bacterial strains, at a pH below 6.0, at a temperature in the range 20 to 70 degree C., converting said initial feedstock to a product predominantly comprising acetic acid and butyric acid; wherein ratio of acetic acid to butyric acid is at least 2:1; treating said product predominantly comprising acetic acid and butyric acid to separate a solution comprising the acetic acid and butyric acid by:

(i) separating residual solids; and

(ii) separating bacteria; optionally pasteurizing; optionally sterilizing said solution comprising the acetic acid and butyric acid;

b) second fermentation step comprising fermenting in the presence of solventogenic bacteria said solution comprising the acetic acid and butyric acid from step a) to form ethanol and butanol;

c) third fermentation step comprising a portion of said feedstock to said first fermentation step is anaerobically digested by a methanogenic bacteria to produce methane; optionally a portion of said solution comprising the acetic acid and butyric acid of step a) is anaerobically digested by a methanogenic bacteria in said third fermentation step to produce methane; wherein said methane is passed as a fuel gas to a combined heat and power scheme to provide electricity and low pressure steam which are used to meet the energy requirements of the overall process.

3. A process for the production of methane, ethanol and butanol using three separate fermentation steps-comprising:

a) first fermentation step comprising fermenting initial feedstock to anaerobic fermentation in the presence of acetogenic bacteria, further comprising a mixture of bacterial strains, at a pH below 6.0, at a temperature in the range 20 to 70 degree C., converting said initial feedstock to a product predominantly comprising acetic acid and butyric acid; wherein ratio of acetic acid to butyric acid is at least 2:1; treating said product predominantly comprising acetic acid and butyric acid to separate a solution comprising the acetic acid and butyric acid by:

(i) separating residual solids; and

(ii) separating bacteria; optionally pasteurizing; optionally sterilizing said solution comprising the acetic acid and butyric acid;

b) second fermentation step comprising fermenting in the presence of solventogenic bacteria said solution comprising the acetic acid and butyric acid from step a) to form ethanol and butanol;

c) third fermentation step comprising a portion of said feedstock to said first fermentation step is anaerobically digested by a methanogenic bacteria to produce methane; optionally a portion of said solution comprising the acetic acid and butyric acid of step a) is anaerobically digested by a methanogenic bacteria in said third fermentation step to produce methane; wherein said methane is passed as a fuel gas to a combined heat and power scheme to provide electricity and low pressure steam which are used to meet the energy requirements of the overall process;

d) wherein there is also provided, in parallel to the first fermentation step, a gasification step for the production of carbon monoxide and hydrogen from a gasifiable feedstock.

4. The process of claim 3 , wherein the gasifiable feedstock comprises non-fermentable components of said initial feedstock, which components may either be separated from said initial feedstock prior to the first fermentation step or recovered from the first fermentation step as residual solids, or a combination of both.

5. The process of claim 3 , wherein the carbon monoxide and hydrogen produced in the gasification step are passed to a further fermentation step wherein they are subjected to fermentation in the presence of an anaerobic acetogenic bacteria to produce ethanol.

6. The process of claim 3 , wherein the carbon monoxide and hydrogen produced in the gasification step are passed to a further fermentation step wherein they are subjected to fermentation in the presence of an anaerobic acetogenic bacteria to produce ethanol; wherein the product from this further fermentation step is combined with the ethanol and butanol product from the second fermentation step and passed to product treatment.

7. The process of claim 3 , wherein the carbon monoxide and hydrogen produced in the gasification step are passed to fermentation step of step b) and in which the bacteria is selected so as to be able to convert CO and H2 into ethanol.