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AIR2-CT93-0825
Production of 1,3-propandiol From Glycerol Surpluses. Yield Optimisation By Technological Development and By Genetic Strain Improvement |
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Contract No | AIR2-CT93-0825 |
| Total Cost | 380 300 | |
| EC Contribution | 265 150 | |
| Start Date | 01/01/1994 | |
| Duration | 36 months |
Due to increased production of plant oils in developing countries and the larger use by the oleochemical industry, glycerol surpluses are on the world market, which led to a continuous decrease in glycerol prices. In future, the situation on the glycerol market will be even more tense if agricultural rape oil production comes into play as envisaged by several EC countries. In a cooperative research project we propose to develop a biotechnological process to produce 1,3-propanediol (PD) from glycerol by Clostridium butyricum, a harmless microorganism that is widely disseminated in nature. Until now, PD is produced only in negligible amounts due to its high price, however it is a useful component for all types of polycondensates : polyethers, polyesters polyurethanes and additionally can be used as a solvent and chemical intermediate for various compounds. The chemical synthesis of 1,3PD is difficult and costly on the other hand, the microbial conversion of glycerol to 1 3-PD is relatively simple and can lead to a decrease in prices. Natural plastics based on 1,3-PD are expected to be light-insensitive and more biodegradable in comparison to fully synthetic polymers. We propose to exploit enabling technology and expertise developed in our laboratories on the use of Clostridium butyricum to promote technological development and to generate strains with improved fermentation characteristics.
The metabolism of Clostridium butyricum was studied in batch culture
and in chemostat culture using either glucose or glycerol. Under
glycerol limitation and at different growth rates, the production
of 1,3 propanediol was not affected. The main observation for
high dilution rates was the decrease in butyrate concentration
and a concomitant increase in acetate concentration.The marked
change in the acetate/butyrate ratio did not occur either in non
limited glycerol chemostat or in batch culture. The evolution
of this ratio was associated with the specific rate of glycerol
utilization; at a high glycerol uptake rate, the butyrate pathway
may become saturated and the cells initiate the acetic acid formation
a corresponding shift in the activity of the acetate and the butyrate
kinase occured, whereas, high levels of the 1,3 PD oxidoreductase
were detected in all extracts. The dilution rate had almost no
effect on the glycerol conversion into 1,3 PD showing that the
carbon flux distribution through the dehydratase and the 1,3 PD
dehydrogenase was balanced by the flux through the glycerol dehydrogenase
and the dihydroxyacetone kinase. Due to the limitation of the
butyrate pathway, C. butyricum growing on glycerol regenerated
the reducing equivalents via the highly active 1,3 propanediol
oxidoreductase. Our data indicated that the NADH produced by
the glycerol dehydrogenase and the glyceraldehyde -3- phosphate
dehydrogenase was not sufficient for the 1,3 PD formation and
part of the ferredoxin produced by the pyruvate ferredoxin oxido
reductase was reoxidized by the ferredoxin-NAD+ reductase activity
to produce NADH. The phosphoroclastic activities were high when
the m of the clostridium was high, whereas the hydrogenase activities
increased during time fermentation when the m decreased. Ferredoxin-NAD+
reductase and NADH-ferredoxin reductase were always in the same
ratio and exhibited the best activities at the end of the exponential
phase. Hydrogenase and phosphoroclastic activities were significantly
higher in cell-free extracts obtained from cells grown on glucose
than on glycerol. The ferredoxin-NAD+ reductase associated to
a low level of hydrogenase and high activity of the 1,3 PD oxidoreductase
explained the high level of NADH recovery.
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by CPL Press:
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