FP6Reintegration grant2007–2008

IONICMEM · Pervaporation and Nanofiltration with Ionic Liquids

FP6 — Marie Curie Actions (Human Resources and Mobility)

Duration
2007-02-01 → 2008-01-31
EU contribution
€40,000
Participants
1
Scheme
ERG

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Results in brief

Final Activity Report Summary - IONICMEM (Pervaporation and nanofiltration with ionic liquids)

Clostridium acetobutylicum, a gram-positive bacteria, is a well known for its ability to produce the solvents acetone and butanol. Large-scale fermentation systems based on the clostridial fermentation supplied the majority of the total requirement of these solvents until 1950. Due to the limitation of the productivity of the fermentation process by environmental conditions, e. g. toxicity of accumulated butanol, and the lower cost of petrochemical procedures the industrial fermentation was discontinued. A fermentation system developed by Bahl et al. (1982) permits now a reproducible and stable production of acetone and butanol. Cells are grown in a chemostat culture, with excess of glucose, a pH below 5 and phosphate limitation. Using a pervaporation separation technique we were able to remove the solvents continuously out of the fermentation system leading to an increase of the growth of the bacteria as well as a higher yield of acetone and butanol. Supported ionic liquid-Polydimethylsiloxane blend membrane was used as a selective barrier in pervaporation process at 37 degrees Celsius. The ultrafiltration membrane (pore size 0.06 mm) was impregnated by 15 wt% of novel ionic liquid ([(C3H7)4N][B(CN)4]) and 85 wt% of polydimethylsiloxane. The selected supported ionic liquid membrane indicates a very high stability over six months during all measurements. Using this membrane we were able to remove butanol and acetone from the culture supernatant more effectively as described by others (Qureshi et al. 1992, Soni et al. 1987, Liu et al. 2004). We were able to remove more butan-1-ol and acetone than the C. acetobutylicum was able to produce. Overall solvent productivity of fermentation connected with continuous product removal by pervaporation was 2.34 g/(lh). To prove the effectiveness of our set-up we ran the fermentation reaction on the limiting values of butan-1-ol concentration (15.82 g/l) to see, if the bacteria could still be alive under these conditions. We proved experimentally that this concentration was already deadly for the bacteria. Considered together, a C. acetobutylicum continuous fermentation set up used with a together with the indicated pervaporation technique would guarantee an increase in fermentation stability and higher production of BIObutanol.

Data: CORDIS, © European Union

Project objective

The aim of this proposal is to combine the recent development in the field of membrane technology, e. g. in nanofiltration, supported liquid membranes and pervaporation, with the use of ionic liquids (ILs) for providing novel solutions in downstream process sing or process intensification.ILs are currently explored as new reaction media for chemical synthesis or electrochemical applications and have emerged as a new class of solvents in the last decade. ILs seem to have a large potential in downstream process sing, especially when applied in a form that requires only a small amount of them, e.g. in supported liquid membranes.The special property of ILs is their non-measurable vapour pressure at ambient temperature that makes their application in liquid membrane s attractive for pervaporation. Simultaneous determination of solute transport through ionic liquids as supported liquid membrane is one of the preconditions of understanding of this new process.After the generalization, the valuable experimental data can be used both for the preparation of new pervaporation membranes based on ionic liquids and for the increase of the efficiency of the separation process and protection of the environment.

Original text from CORDIS.

Participants

  • INSTITUTE OF CHEMICAL PROCESS FUNDAMENTALS · PRAGUE 6CoordinatorCzechia

Links

Data: CORDIS, © European Union