CPC C12P 7/625 (2013.01) [C12M 23/34 (2013.01); C12M 29/02 (2013.01); C12M 29/08 (2013.01); C12M 29/18 (2013.01); C12M 29/20 (2013.01); C12M 43/04 (2013.01); C12M 47/02 (2013.01); C12N 1/12 (2013.01); C12N 1/20 (2013.01); C12N 1/205 (2021.05); C12P 1/04 (2013.01); C12P 3/00 (2013.01); C12P 5/023 (2013.01); C12P 7/065 (2013.01); C12P 7/08 (2013.01); C12P 7/16 (2013.01); C12P 7/40 (2013.01); C12P 7/54 (2013.01); C12P 7/6463 (2013.01); C12P 7/649 (2013.01); C12P 21/00 (2013.01); C25B 1/04 (2013.01); C25B 15/02 (2013.01); Y02E 50/10 (2013.01); Y02E 50/30 (2013.01); Y02E 60/36 (2013.01); Y02P 20/133 (2015.11); Y02W 30/40 (2015.05)] | 18 Claims |
1. A biological and chemical method to form an organic chemical product, comprising:
introducing an inorganic carbon compound and/or an organic compound containing only one carbon atom into a bioreactor comprising an environment suitable for maintaining oxyhydrogen microorganisms from genus Xanthobacter, wherein the environment comprises the oxyhydrogen microorganisms in a liquid culture medium; and
converting the inorganic carbon compound and/or the organic compound containing only one carbon atom into biomass and/or an organic chemical product comprising a lipid, an amino acid, a peptide, and/or a protein within the environment via a carbon-fixing step that carries out at least one chemosynthetic carbon-fixing reaction utilizing the oxyhydrogen microorganisms;
wherein the at least one chemosynthetic carbon-fixing reaction is at least partially driven by chemical and/or electrochemical energy provided by electron donors comprising gaseous H2 and electron acceptors comprising gaseous O2,
wherein O2 gas is introduced into a first column comprising the oxyhydrogen microorganisms and liquid culture medium within the environment by sparging, bubbling, and/or diffusion of said O2 gas, and H2 gas and/or syngas containing the H2 gas is introduced into a second column comprising the oxyhydrogen microorganisms and liquid culture medium within the environment by sparging, bubbling, and/or diffusion of said H2 gas and/or syngas, wherein the first and second columns are separated from each other, a headspace of the first column and a headspace of the second column are isolated from each other by the liquid culture medium, and there is a liquid connection between the first and second columns comprising the liquid culture medium, and wherein the liquid culture medium circulates between the first and second columns,
wherein the carbon-fixing reaction is maintained using a continuous influx and removal of the liquid culture medium and/or biomass from the environment,
wherein surplus biomass is removed from the environment in order to maintain a constant population and cell density of said oxyhydrogen microorganisms in the liquid culture medium, and
wherein the biomass and/or the organic chemical product is separated from the liquid culture medium and processed into a fuel product, a nutritional product, an animal feed, a fertilizer, a soil additive, a soil stabilizer, a carbon source for fermentations, and/or a nutrient source for growth of other microbes or organisms.
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