Microbial respiration of chloroxyanions as a source of oxygen for bioprocessing
12624360 ยท 2026-05-12
Assignee
Inventors
Cpc classification
C12Y107/02001
CHEMISTRY; METALLURGY
C12N9/0069
CHEMISTRY; METALLURGY
International classification
Abstract
Aerobic microbial processes comprise culturing microbes comprising a (per)chlorate respiration pathway in a bioreactor in a bioprocess employing microbial respiration of chloroxyanions as a source of oxygen for the bioprocess, in the absence of external addition of molecular oxygen.
Claims
1. A method of aerobic microbial processing comprising: culturing microbes comprising a (per)chlorate respiration pathway in a bioreactor in a bioprocess employing microbial respiration of chloroxyanions as a source of oxygen for the bioprocess, in the absence of external addition of molecular oxygen, wherein the microbes are genetically engineered to comprise an operative microbial (per)chlorate respiration pathway encoding: (i) a perchlorate reductase which effects reduction of (per)chlorate to chlorite (ClO.sub.2.sup.); (ii) a chlorite dismutase which effects dismutation of the chlorite into chloride and molecular oxygen (O.sub.2); and (iii) a cytochrome oxidase which effects reduction of the molecular oxygen; wherein the pathway enables the engineered microbe to grow in the bioreactor with (per)chlorate as its sole electron acceptor in the absence of oxygen, wherein the microbes are obligately aerobic methanotrophs, that are Methylocystis trichosporium, and the bioprocess converts methane (CH.sub.4) into polyhydroxybutyrate (PHB).
Description
BRIEF DESCRIPTION OF THE DRAWINGS
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DESCRIPTION OF PARTICULAR EMBODIMENTS OF THE INVENTION
(6) Unless contraindicated or noted otherwise, in these descriptions and throughout this specification, the terms a and an mean one or more, the term or means and/or. It is understood that the examples and embodiments described herein are for illustrative purposes only and that various modifications or changes in light thereof will be suggested to persons skilled in the art and are to be included within the spirit and purview of this application and scope of the appended claims. All publications, patents, and patent applications cited herein, including citations therein, are hereby incorporated by reference in their entirety for all purposes.
(7) This invention takes advantage of the unique oxygen biogenesis biochemical pathway associated respiration of the chloroxyanions chlorate (ClO.sub.3.sup.) and perchlorate (ClO.sub.4.sup.) [collectively denoted (per)chlorate]. The invention provides for aerobic microbial processes in the absence of external addition of molecular oxygen. Canonical microbial (per)chlorate respiration is an energetically favorable process that involves three steps: (i) the reduction of (per)chlorate to chlorite (ClO.sub.2.sup.) by the perchlorate reductase; (ii) disputation of chlorite into chloride and molecular oxygen (O.sub.2) by the chlorite dismutase; and (iii) reduction of molecular oxygen by the cytochrome oxidase. In this way (per)chlorate respiring organisms can enzymatically produce oxygen under anoxic conditions. This provides organisms endowed with this pathway with a unique metabolic versatility, allowing them to use (per)chlorate not only as an electron acceptor but also as a co-substrate in oxygenase driven reactions in the absence of externally added oxygen. This pathway is well characterized with known biochemistry and genes. We have previously engineered this pathway into Shewanella species allowing the engineered strain to grow with chlorate as its sole electron acceptor in the absence of oxygen. An exemplary application of this invention is shown in
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(9) 67% dry wt biomass possible e.g. Wendlandt et al. (J Biotechnol. 2001 Mar. 30; 86(2):127-33) showed Methylocystis trichosporium sp. GB25 on methane at 3 atm yielded 4 g L.sup.1H.sup.1 biomass and 2 g L.sup.1 PHB with a yield of 0.55 g g.sup.1 CH.sub.4. Glucose gives a yield of 0.3 to 0.4 gm PHB per gm glucose.
(10) General Principle: 4n/x C.sub.xH.sub.yO.sub.z.fwdarw.(C.sub.4H.sub.6O.sub.2)n+n[2y/x3] H.sub.2O+n[1/2(y2z)/x]O.sub.2
(11) CH.sub.4=>X=1; y=4; z=0
(12) 4n CH.sub.4+[n+n5/2]O.sub.2.fwdarw.(C.sub.4H.sub.6O.sub.2)n+n5 H.sub.2O
(13) For example, If n=2 then:
(14) 8 CH.sub.4+7O.sub.2.fwdarw.(C.sub.4H.sub.6O.sub.2).sub.2+10 H.sub.2O
(15) Features: oxygen (energy) intensive process often leading to high risk (explosive) pressurized conditions in a bioreactor
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