Two-stage continuous process for producing a solvent
The present invention relates to a two stage continuous microbiological process for the production of solvents such as acetone, butanol and ethanol. The process involves the use of a solventogenic bacteria such as clostridia . In the first(acidogenic) stage, the culture vessel is fed with fresh growth media at dilution rates that support fast growth and acid production. The culture flows into the second (solventogenic) stage, which is a separate culture vessel or vessels, designed to provide the culture with sufficient residence time to convert acids into solvents. This vessel can be tubular or a series of linked batch vessels.
1. A two-stage process for the production of a solvent using an acid- and solvent-producing micro-organism, comprising the steps:
(i) culturing the micro-organism under acidogenic conditions in a liquid medium in a first culture vessel and using a pH auxostat to control the following:
the pH of the liquid medium in the first culture vessel; and
the flow rate of fresh media which is introduced into the first culture vessel,
wherein the pH auxostat has:
(a) separate feeds for alkali and fresh media, or
(b) a feed from fresh media that has a pH which is higher than the pH of the liquid medium in the first culture vessel;
(ii) transferring a portion of the liquid medium from the first culture vessel to a second culture vessel or series of linked culture vessels; and
(iii) culturing the same micro-organism under solventogenic conditions in the second culture vessel(s) for a time which is sufficient for solvent to be produced,
and optionally isolating one or more solvents which are produced in the second culture vessel(s).
2. A process as claimed in claim 1 , wherein the micro-organism is an aero-tolerant bacterium.
3. A process as claimed in claim 1 , wherein the micro-organism is a solventogenic Clostridium.
4. A process as claimed in claim 3 , wherein the micro-organism is Clostridium beijerinckii, Clostridium acetobutylicum, C. saccharobutylicum or C. saccharoperbutylacetonicum.
5. A process as claimed in claim 1 , wherein the pH of the first culture vessel is pH 5.5-7.0.
6. A process as claimed in claim 1 , wherein the first culture vessel is connected directly to the second culture vessel(s), and wherein liquid media is transferred continuously from the first to the second culture vessel(s).
7. A process as claimed in claim 1 , wherein the pH of the second culture vessel is pH 4.5-6.0.
8. A process as claimed in claim 1 , wherein one or more of the second culture vessels is in the form of a long tubular vessel, a series of linked batch vessels or a single batch vessel.
9. A process as claimed in claim 1 , wherein cells are separated from a portion of the liquid medium which has been removed from one or more of the second culture vessels and the cells are returned to one or more of the second culture vessels.
10. A process as claimed in claim 1 , wherein solvent(s) are recovered from the second culture vessel by liquid-liquid extraction, gas stripping, vacuum evaporation, vacuum distillation, pervaporation, ion-exchange adsorption and/or distillation.
11. A process as claimed in claim 10 , wherein the solvent extraction is by liquid extraction which is performed in situ in one or more of the second culture vessels.
12. A process as claimed in claim 1 , wherein the solvent is acetone, butanol or ethanol.