Microaerobic cultures for converting glycerol to chemicals
View Patent ↗Glycerol or other reduced carbon sources may be used as a feedstock for the microbial production of chemical products under certain microaerobic conditions. For example, such production may occur under microaerobic or microrespiratory conditions in which electron acceptors are consumed in the reaction as quickly as they are added. In such reactions, the reaction product is at least as reduced as carbon source. Further, during such a reaction, at least some of the carbon source is used to generate cell mass. In addition, microorganisms with modified genomes are provided for carrying out the methods herein.
1. An Escherichia coli strain comprising:
a disruption in one or more of a adhE gene (encoding alcohol dehydrogenase), a pta gene (encoding phosphate acetyltransferase), a poxB gene (encoding pyruvate oxidase), a ppc gene (encoding phospoenolpyruvate carboxylase) or a dhaK gene (encoding dihydroxyacetone kinase subunit K);
an exogenous Citrobacter freundii dhaKL gene (encoding dihydroxyacetone kinase subunits KL); and
an exogenous Actinobacillus succinogenes pckA gene (encoding phosphoenolpyruvate carboxykinase).
2. An Escherichia coli strain comprising:
an overexpressed gldA gene (encoding glycerol dehydrogenase) or an overexpressed dhaKLM operon (encoding dihydroxyacetone kinase subunits KLM);
a disruption in at least one of a frdA , frdB , frdC, or frdD gene (encoding fumarate reductase); and
a disruption in a pta gene or a disruption in a poxB gene.
3. An Escherichia coli strain comprising:
an overexpressed gldA gene or an overexpressed dhaKLM operon; and
a disruption in one or more of a adhE gene, a pta gene, a poxB gene; a frdA gene, afrdB gene, frdC gene, or a frdD gene.
4. A method of culturing bacteria to produce a metabolite, comprising the following steps:
a. inoculating a culture medium comprising glycerol as a feedstock with a bacteria capable of producing a metabolite, said bacteria being selected from the bacteria of claim 1 , and
b. cultivating said bacteria under microaerobic conditions of ≦20 mg O 2 /L/h, but not aerobic or anaerobic conditions, in said reactor so as to convert said glycerol into a metabolite, wherein the conversion of glycerol into the metabolite does not consume more reducing equivalents than it produces.
5. The method of claim 4 , wherein said bacteria is E. coli comprising Δpta, ΔfrdA and overexpressed gldA and dhaKLM.
6. The method of claim 4 , wherein said metabolite is selected from the groups consisting of ethanol, lactate, succinate, propionate, alanine, and combinations thereof.
7. The method of claim 4 , wherein said metabolite is selected from the groups consisting of ethanol, lactate, propionate, succinate, and combinations thereof.