US20170306358A1 - Compositions and methods for biological production of butane-based compounds from a c1 substrate - Google Patents

Compositions and methods for biological production of butane-based compounds from a c1 substrate Download PDF

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US20170306358A1
US20170306358A1 US15/637,838 US201715637838A US2017306358A1 US 20170306358 A1 US20170306358 A1 US 20170306358A1 US 201715637838 A US201715637838 A US 201715637838A US 2017306358 A1 US2017306358 A1 US 2017306358A1
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methanotrophic bacterium
bacterium
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propylene
coa
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Joshua A. Silverman
Thomas Joseph Purcell
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Calysta Inc
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    • C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P5/00—Preparation of hydrocarbons or halogenated hydrocarbons
    • C12P5/02—Preparation of hydrocarbons or halogenated hydrocarbons acyclic
    • C12P5/026—Unsaturated compounds, i.e. alkenes, alkynes or allenes
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
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    • C12N1/00—Microorganisms, e.g. protozoa; Compositions thereof; Processes of propagating, maintaining or preserving microorganisms or compositions thereof; Processes of preparing or isolating a composition containing a microorganism; Culture media therefor
    • C12N1/20—Bacteria; Culture media therefor
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
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    • C12N9/00—Enzymes; Proenzymes; Compositions thereof; Processes for preparing, activating, inhibiting, separating or purifying enzymes
    • C12N9/14—Hydrolases (3)
    • C12N9/16—Hydrolases (3) acting on ester bonds (3.1)
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
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    • C12N9/00—Enzymes; Proenzymes; Compositions thereof; Processes for preparing, activating, inhibiting, separating or purifying enzymes
    • C12N9/88—Lyases (4.)
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00—Technologies for the production of fuel of non-fossil origin
    • Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel

Definitions

  • Propylene is primarily produced as a by-product of petroleum refining and of ethylene production using a steam cracking process. Propylene is separated from a mixture of hydrocarbons obtained from cracking or other refining processes by fractional distillation. Propylene is typically produced from non-renewable fossil fuels, petroleum, natural gas, and to a lesser extent coal. Propylene can also be produced in on-purpose reactions, such as propane dehydrogenation, metathesis or syngas-to-olefins plants.
  • Propylene is a major industrial chemical intermediate that is converted into a variety of chemicals and plastics. Manufacturers of polypropylene account for nearly two thirds of worldwide propylene demand. Polypropylene is a plastic that is used for the manufacture of films, packaging, caps, closures, and individual parts for the electrical and automotive industry. Propylene is also used to produce chemicals including acrylonitrile, oxo chemicals, propylene oxide, cumene, isopropanol, acrylic acid, butanol, and butanediol.
  • the present disclosure provides non-naturally occurring C 1 metabolizing organisms, wherein the non-naturally occurring C 1 metabolizing organisms convert a C 1 substrate to propylene.
  • the C 1 metabolizing organism is: a non-naturally occurring C 1 metabolizing bacterium; a non-naturally occurring obligate C 1 metabolizing organism; a non-naturally occurring C 1 metabolizing organism, wherein the non-naturally occurring C 1 metabolizing organism does not include Pichia pastoris; a non-naturally occurring methanotrophic or methylotrophic bacterium; a non-naturally occurring syngas utilizing bacterium that naturally possesses the ability to utilize syngas; or a non-naturally occurring CO utilizing bacterium, wherein the non-naturally occurring CO utilizing bacterium naturally possesses the ability to utilize CO.
  • the non-naturally occurring C 1 metabolizing organisms include an exogenous nucleic acid encoding an enzyme capable of decarboxylating crotonic acid (e.g., 4-oxalocrotonate decarboxylase).
  • an enzyme capable of decarboxylating crotonic acid e.g., 4-oxalocrotonate decarboxylase.
  • the non-naturally occurring C 1 metabolizing organisms do not have a functional PHB synthase or a substantial amount of functional PHB synthase.
  • non-naturally occurring C 1 metabolizing organisms include an exogenous nucleic acid encoding a crotonyl CoA thioesterase.
  • the non-naturally occurring C 1 metabolizing organism may be a non-naturally occurring C 1 metabolizing bacterium; a non-naturally occurring obligate C 1 metabolizing organism; a non-naturally occurring C 1 metabolizing organism, wherein the C 1 metabolizing organism does not include Pichia pastoris; a non-naturally occurring methanotrophic or methylotrophic bacterium; a non-naturally occurring syngas utilizing bacterium that naturally possesses the ability to utilize syngas;or a non-naturally occurring CO utilizing bacterium, wherein the non-naturally occurring CO utilizing bacterium naturally possesses the ability to utilize CO.
  • non-naturally occurring C 1 metabolizing organisms include an exogenous nucleic acid encoding a crotonase.
  • the non-naturally occurring C 1 metabolizing organism is: a non-naturally occurring C 1 metabolizing bacterium; a non-naturally occurring obligate C 1 metabolizing organism; a non-naturally occurring C 1 metabolizing organism, wherein the organism does not include Pichia pastoris; a non-naturally occurring methanotrophic or methylotrophic bacterium; a non-naturally occurring syngas utilizing bacterium that naturally possesses the ability to utilize syngas; or a non-naturally occurring CO utilizing bacterium, wherein the CO utilizing bacterium naturally possesses the ability to utilize CO.
  • the present disclosure provides non-naturally occurring microbial organisms, wherein the non-naturally occurring microbial organisms include an exogenous nucleic acid encoding 4-oxalocrotonate decarboxylase, and wherein the non-naturally occurring microbial organisms convert a carbon substrate to propylene.
  • the non-naturally occurring microbial organisms further include an exogenous nucleic acid encoding crotonase, or an exogenous nucleic acid encoding crotonase and an exogenous nucleic acid encoding crotonyl thioesterase.
  • the non-naturally occurring microbial organisms do not have a functional PHB synthase or a substantial amount of functional PHB synthase.
  • FIG. 1 shows an exemplary pathway for synthesis of propylene from acetyl CoA in a genetically modified organism.
  • Enzymes and genes encoding enzymes for transformation of the identified substrates to products include: phaA, phaB, crotonase, crotonyl CoA thioesterase, and 4-oxalocrotonate decarboxylase.
  • FIGS. 2A-D show exemplary 4-oxalocrotonate decarboxylase (4-OD) amino acid sequences that may be used in propylene synthesis pathways as described herein.
  • FIG. 3 shows exemplary crotonyl-CoA thioesterase amino acid sequences that may be used in propylene synthesis pathways as described herein.
  • FIGS. 4A-E show exemplary crotonase amino acid sequences that may be used in propylene synthesis pathways as described herein.
  • FIG. 5 shows SDS-PAGE analysis of heterogeneously expressed 4-OD genes in E. coli.
  • the first lane for each sample shows total cell protein and the second lane for each sample shows soluble protein following lysis and clarification.
  • the arrow on the left shows the approximate migration of 4-OD proteins (note sequence variation causes slight changes in migration for each individual 4-OD sequence).
  • FIG. 6 shows sample 4-OD activity assays run under conditions as described showing decarboxylation of 4-oxalocrotonate.
  • FIG. 7 shows a sample chromatogram of propylene detected on a HP5890 GC-FID under the assay conditions as described.
  • the instant disclosure provides compositions and methods for the biocatalysis of propylene and other desirable intermediates or products from methane or other C 1 substrates using genetically engineered C 1 metabolizing organisms.
  • the instant disclosure also provides compositions and methods for the biocatalysis of propylene from carbon substrates using novel metabolic enzyme(s) in genetically engineered microbial organisms.
  • the term “about” means ⁇ 20% of the indicated range, value, or structure, unless otherwise indicated.
  • the term “consisting essentially of” limits the scope of a claim to the specified materials or steps and those that do not materially affect the basic and novel characteristics of the claimed invention.
  • the terms “a” and “an” as used herein refer to “one or more” of the enumerated components.
  • the use of the alternative should be understood to mean either one, both, or any combination thereof of the alternatives.
  • the terms “include” and “have” are used synonymously, which terms and variants thereof are intended to be construed as non-limiting.
  • the term “comprise” means the presence of the stated features, integers, steps, or components as referred to in the claims, but that it does not preclude the presence or addition of one or more other features, integers, steps, components, or groups thereof.
  • non-naturally occurring when used in reference to a bacterium or an organism means that the bacterium or organism has at least one genetic alternation that is not normally found in a naturally occurring strain of the referenced species, including wild-type strains of the referenced species.
  • Genetic alterations include, for example, modifications introducing expressible nucleic acids encoding proteins or enzymes, other nucleic acid additions, nucleic acid deletions, nucleic acid substitutions, or other functional disruption of the bacterium or organism's genetic material. Such modifications include, for example, coding regions and functional fragments thereof for heterologous or homologous polypeptides for the referenced species.
  • Additional modifications include, for example, non-coding regulatory regions in which the modifications alter expression of a gene or operon.
  • Exemplary enzymes include enzymes within a crotonate synthesis pathway or propylene synthesis pathway.
  • Genetic modifications to nucleic acid molecules encoding enzymes, or functional fragments thereof, can confer a biochemical reaction capability or a metabolic pathway capability to the non-naturally occurring organism that is altered from its naturally occurring state.
  • the term “host” refers to a bacterium or organism that has not yet been genetically modified with the capability to convert a carbon substrate to crotonyl-CoA, crotonic acid, or propylene, as disclosed herein.
  • a host C 1 metabolizing bacterium or organism is selected for transformation with at least one exogenous nucleic acid encoding an enzyme to yield a non-naturally occurring C 1 metabolizing bacterium or organism with the capability to convert a C 1 substrate to crotonyl-CoA, crotonic acid, or propylene.
  • a host microbial organism is selected for transformation with at least one exogenous nucleic acid encoding 4-oxalocrotonate decarboxylase to yield a non-naturally occurring microbial organism with the capability to convert a carbon substrate to propylene.
  • a host bacterium or organism may already possess other genetic modifications conferring it with desired properties, unrelated to propylene synthesis pathways and intermediates disclosed herein.
  • a host bacterium or organism may possess genetic modifications conferring high growth, tolerance of contaminants or particular culture conditions, or ability to metabolize different carbon substrates.
  • microbial organism refers to any prokaryotic or eukaryotic microbial species from the domains of Archaea, Bacteria, or Eukarya.
  • the term is intended to include prokaryotic or eukaryotic cells or organisms having microscopic size.
  • C 1 metabolizing bacterium refers to any bacterium that has the ability to oxidize a C 1 compound (i.e., does not contain carbon-carbon bonds).
  • a C 1 metabolizing bacterium may or may not use other carbon substrates, such as sugars and complex carbohydrates, for energy and biomass.
  • the term “obligate C 1 metabolizing organism” refers to those organisms which exclusively use organic compounds that do not contain carbon-carbon bonds (C 1 substrate) for the generation of energy.
  • C 1 metabolizing organism refers to any organism that has the ability to oxidize a C 1 substrate (i.e., does not contain carbon-carbon bonds) but may or may not use other carbon substrates, such as sugars and complex carbohydrates, for energy and biomass.
  • a C 1 metabolizing organism includes bacteria, yeast (not including Pichia pastoris ), and Archaea.
  • a C 1 metabolizing organism includes C 1 metabolizing bacteria.
  • methanotrophic bacterium refers to any methylotrophic bacterium that has the ability to oxidize methane as its primary carbon and energy source.
  • methylotrophic bacterium refers to any bacterium capable of oxidizing organic compounds that do not contain carbon-carbon bonds.
  • An “obligate methylotrophic bacterium” is a bacterium which is limited to the use of carbon substrates that do not contain carbon-carbon bonds for the generation of energy. Facultative methylotrophs are able to utilize multi-carbon compounds in addition to single carbon substrates.
  • CO utilizing bacterium refers to a bacterium that naturally possesses the ability to oxidize carbon monoxide (CO) as a source of carbon and energy.
  • Carbon monoxide may be utilized from “synthesis gas” or “syngas”, a mixture of carbon monoxide and hydrogen produced by gasification of any organic feedstock, including but not limited to coal, coal oil, natural gas, biomass, and waste organic matter. Syngas may also include CO 2 , methane, and other gases in smaller quantities.
  • CO utilizing bacterium does not include bacteria that must be genetically modified for growth on CO as its carbon source.
  • C 1 substrate or “C 1 compound” refers to any carbon containing molecule or composition that lacks a carbon-carbon bond.
  • C 1 substrates include methane, methanol, formaldehyde, formic acid (formate), carbon monoxide, carbon dioxide, methylated amines (methylamine, dimethylamine, trimethylamine, etc.), methylated thiols, methyl halogens (bromomethane, chloromethane, iodomethane, dichloromethane, etc.), or cyanide.
  • propylene also known as 1-propene, propene, or methylethylene
  • 1-propene 1, 2-propene
  • propene 1, 2-propene
  • methylethylene an unsaturated organic compound having the chemical formula C 3 H 6 and molecular mass of 42.08 g/mol. It has one double bond and is the second simplest member of the alkene class of hydrocarbons.
  • Propylene is a gas at room temperature and atmospheric pressure.
  • Propylene is a structural isomer of cyclopropane.
  • exogenous means that the referenced molecule (e.g., nucleic acid) or referenced activity (e.g., enzyme activity) is introduced into the host bacterium or organism.
  • the molecule can be introduced, for example, by introduction of a nucleic acid into the host genetic material such as by integration into a host chromosome or by introduction of a nucleic acid as non-chromosomal genetic material, such as on a plasmid.
  • introduction of a nucleic acid into the host genetic material such as by integration into a host chromosome or by introduction of a nucleic acid as non-chromosomal genetic material, such as on a plasmid.
  • the term refers to an activity that is introduced into the host reference bacterium or organism. Therefore, the term “endogenous” or “native” refers to a referenced molecule or activity that is present in the host bacterium or organism.
  • the term “heterologous” refers to a molecule or activity that is derived from a source other than the referenced species or strain whereas “homologous” refers to a molecule or activity derived from the host bacterium or organism. Accordingly, a bacterium or organism comprising an exogenous nucleic acid of the invention can utilize either or both a heterologous or homologous nucleic acid.
  • exogenous nucleic acid when more than one exogenous nucleic acid is included in a bacterium or organism that the more than one exogenous nucleic acid refers to the referenced encoding nucleic acid or enzymatic activity, as discussed above. It is also understood, as disclosed herein, that such more than one exogenous nucleic acids can be introduced into the host bacterium or organism on separate nucleic acid molecules, on a polycistronic nucleic acid molecule, on a single nucleic acid molecule encoding a fusion protein, or a combination thereof, and still be considered as more than one exogenous nucleic acid.
  • an organism can be modified to express two or more exogenous nucleic acids encoding a desired pathway enzyme or protein (e.g., propylene pathway enzyme or protein).
  • a desired pathway enzyme or protein e.g., propylene pathway enzyme or protein
  • the two exogenous nucleic acids can be introduced as a single nucleic acid molecule, for example, on a single plasmid, on separate plasmids, can be integrated into the host chromosome at a single site or multiple sites, and still be considered two exogenous nucleic acids.
  • exogenous nucleic acids can be introduced into a host organism in any desired combination, for example, on a single plasmid, on separate plasmids, can be integrated into the host chromosome at a single site or multiple sites, and still be considered as two or more exogenous nucleic acids.
  • the number of referenced exogenous nucleic acids or enzymatic activities refers to the number of encoding nucleic acids or the number of enzymatic activities, not the number of separate nucleic acid molecules introduced into the host organism.
  • nucleic acid refers to a polymeric compound comprised of covalently linked subunits called nucleotides. Nucleic acids include polyribonucleic acid (RNA), polydeoxyribonucleic acid (DNA), both of which may be single or double stranded. DNA includes cDNA, genomic DNA, synthetic DNA, and semi-synthetic DNA.
  • crotonic acid or “trans-2-butenoic acid” refers to a short-chain unsaturated carboxylic acid with the formula CH 3 CH ⁇ CHCO 2 H.
  • crotonic acid includes “crotonate”, a salt or ester of crotonic acid.
  • 4-oxalocrotonate refers to an unsaturated carboxylic acid with the formula HO 2 C(C ⁇ O)CH 2 CH ⁇ CHCO 2 — (keto form) or HO 2 C(COH) ⁇ CHCH ⁇ CHCO 2 — (enol form), which interconvert spontaneously.
  • 4-oxalocrotonate also includes salts or esters, the equivalent molecule with the alternate acid group deprotonated, the doubly unprotonated basic form of the molecule, or the doubly protonated acid form of the molecule.
  • 4-oxalocrotonate decarboxylase or “4-OD” or “4-oxalocrotonate carboxy-lase (2-oxopent-4-enoate-forming)” refers to an enzyme family that catalyzes the decarboxylation of 4-oxalocrotonate to 2-oxopent-4-enoate and CO 2 .
  • 4-OD is involved in the meta-cleavage pathway for the degradation of phenols, modified phenols, and catechols. As disclosed herein, 4-OD is used to catalyze the decarboxylation of crotonic acid to propylene and CO 2 .
  • 4-OD also encompasses mutants or variants of a native 4-OD enzyme that has reduced or eliminated decarboxylation activity on 4-oxalocrotonate, but retains or has increased decarboxylation activity on crotonic acid as a substrate.
  • 4-OD also refers to any enzyme capable of catalyzing the decarboxylation of crotonic acid to propylene and CO 2 .
  • crotonyl CoA thioesterase refers to an enzyme that catalyzes the conversion of crotonyl-CoA to crotonic acid.
  • crotonase or “3-hydroxybutyryl-CoA dehydratase” or “enoyl-CoA hydratase” refers to an enzyme involved in the butyrate/butanol-producing pathway, which catalyzes the dehydration of 3-hydroxybutyryl-CoA to crotonyl-CoA.
  • ⁇ -ketothiolase refers to an enzyme in the PHB synthesis pathway that catalyzes the condensation of two acetyl-CoA molecules to acetoacetyl-CoA. Biosynthesis of PHB in most bacteria is initiated by ⁇ -ketothiolase.
  • acetoacetyl coenzyme A reductase refers to an enzyme in the PHB synthesis pathway that catalyzes the reduction of acetoacetyl-CoA to 3-hydroxybutyryl-CoA.
  • PHB synthase also known as “PHB polymerase” refers to an enzyme in the PHB synthesis pathway that converts a hydroxybutyryl-CoA monomer into polyhydroxybutyrate.
  • polyhydroxybutyrate or “PHB” refers to a homopolymer of hydroxybutyric acid units.
  • PHB is a type of polyhydroxyalkanoate (PHA), which is a biological polyester.
  • PHA polyhydroxyalkanoate
  • Polyhydroxybutyrate is a crystalline thermoplastic synthesized by a broad range of bacteria as a form of energy storage molecule.
  • Poly-3-hydroxybutyrate (P3HB) form is the most common type of PHB, but other PHBs include poly-4-hydroxybutytrate (P4HB), poly(3-hydroxybutyrate-co-4-hydroxybutyrate) (P3HB-co-4HB), or other copolymers.
  • C 1 metabolizing host organisms can be transformed or genetically engineered to produce a product of interest (e.g., propylene, crotonic acid, or crotonyl-CoA).
  • a product of interest e.g., propylene, crotonic acid, or crotonyl-CoA.
  • a C 1 metabolizing organism may be a C 1 metabolizing bacterium, which refers to any bacterium that has the ability to oxidize a C 1 compound.
  • a C 1 metabolizing bacterium may also use other carbon substrates, such as sugars and complex carbohydrates, for energy and biomass.
  • a C 1 metabolizing bacterium includes methanotrophic bacteria (methylotrophic bacterium that has the ability to oxidize methane as an energy source) or methylotrophic bacteria (any bacterium capable of oxidizing organic compounds that do not contain carbon-carbon bonds).
  • Methanotrophic bacteria are classified into three groups based on their carbon assimilation pathways and internal membrane structure: type I (gamma proteobacteria), type II (alpha proteobacteria, and type X (gamma proteobacteria).
  • Type I methanotrophs use the ribulose monophosphate (RuMP) pathway for carbon assimilation whereas type II methanotrophs use the serine pathway.
  • Type X methanotrophs use the RuMP pathway but also express low levels of enzymes of the serine pathway.
  • Methanotrophic bacteria are grouped into several genera: Methylomonas, Methylobacter, Methylococcus, Methylocystis, Methylosinus, Methylomicrobium, Methanomonas, and Methylocella.
  • Exemplary methantrophic bacteria include: Methylococcus capsulatus Bath strain, Methylomonas 16a (ATCC PTA 2402), Methylosinus trichosporium OB3b (NRRL B-11,196), Methylosinus sporium (NRRL B-11,197), Methylocystis parvus (NRRL B-11,198), Methylomonas methanica (NRRL B-11,199), Methylomonas albus (NRRL B-11,200), Methylobacter capsulatus (NRRL B-11,201), Methylobacterium organophilum (ATCC 27,886), Methylomonas sp AJ-3670 (FERM P-2400), Methylocella silvestris, Methylocella palustris (ATCC 700799), Methylocella tundrae, Methylacidiphilum infernorum, Methylibium petroleiphilum, and Meth
  • Methylotrophic bacteria encompass a diverse group, including both gram-negative and gram-positive genera. Methylotrophic bacteria include facultative methylotrophs (have the ability to oxidize organic compounds which do not contain carbon-carbon bonds, but may also utilize other carbon substrates such as sugars and complex carbohydrates), obligate methylotrophs (limited to the use of organic compounds that do not contain carbon-carbon bonds), and methanotrophic bacteria.
  • methylotrophic genera include: Methylophilus, Methylobacillus, Methylobacterium, Hyphomicrobium, Xanthobacter, Bacillus, Paracoccus, Nocardia, Arthrobacter, Rhodopseudomonas, and Pseudomonas.
  • Exemplary methylotrophic bacteria include: Methylobacterium extorquens, Methylobacterium radiotolerans, Methylobacterium populi, Methylobacterium chloromethanicum, Methylobacterium nodulans, Methylomonas clara, Methylibium petroleiphilum, Methylobacillus flagellates, Silicibacter pomeroyi DSS-3, Burkholderia phymatum STM815, Granulibacter bethesdensis NIH1.1, and Paracoccus denitrificans.
  • a C 1 metabolizing bacterium includes bacteria that utilize formate or cyanide or naturally possesses the ability to utilize syngas or carbon monoxide (CO) (Wu et al., PLoS Genet. 1:e65, 2005; Abrini et al., Arch. Microbiol. 161:345, 1994; WO 2008/028055; Tanner et al., Int. J. Syst. Bacteriol. 43:232-236, 1993).
  • CO carbon monoxide
  • Exemplary bacteria that naturally possesses the ability to utilize CO or syngas include Clostridium autoethanogenum, Clostridium ljungdahli, Clostridium ragsdalei, Clostridium carboxydivorans, Butyribacterium methylotrophicum, Clostridium woodii, Clostridium neopropanologen, Pseudomonas carboxidovorans, Rhodospirillum rubrum, Thermincola carboxydiphila, Thermincola potens, Thermoanaerobacter thermohydrosulfuricus, Ralstonia eutropha, and Eurobacterium limosum.
  • a C 1 metabolizing bacterium also includes bacteria that can cleave methyl groups from organic compounds, including choline (de Vries et al., FEMS Microbiol. Rev. 6:57-101, 1990) or the pesticide carbofuran (Topp et al., Appl. Environ. Microbiol. 59:3339-3349, 1993), and utilize them as a sole source of carbon.
  • choline de Vries et al., FEMS Microbiol. Rev. 6:57-101, 1990
  • carbofuran Topp et al., Appl. Environ. Microbiol. 59:3339-3349, 1993
  • C 1 metabolizing organisms include bacteria, yeast (not including Pichia pastoris ), and Archaea.
  • a C 1 metabolizing organism may be obligate or facultative.
  • Examples of C 1 metabolizing organisms include: Methylomonas, Methylobacter, Methylococcus, Methylosinus, Methylocystis, Methylomicrobium, Methanomonas, Methylophilus, Methylobacillus, Methylobacterium, Hyphomicrobium, Xanthobacter, Bacillus, Paracoccus, Nocardia, Arthrobacter, Rhodopseudomonas, Pseudomonas, Candida, Yarrowia, Hansenula, Pichia (not including Pichia pastoris ), Torulopsis, and Rhodotorula.
  • C 1 (carbon monoxide) metabolizing organisms include: Clostridium autoethanogenum, Clostridium ljungdahli, Clostridium ragsdalei, Clostridium carboxydivorans, Butyribacterium methylotrophicum, Clostridium Woodii, and Clostridium neopropanologen.
  • C 1 substrates may be used by the C 1 metabolizing organisms. It is understood to one of skill in the art that selection of a C 1 substrate may be determined by which host organism is selected. For example, obligate methanotrophic bacteria are limited to the use of methane as a carbon source, whereas some methylotrophic bacteria may use a variety of C 1 compounds, such as methane, methanol, methylated amines, halomethanes, and methylated compounds containing sulfur (reviewed in Hanson and Hanson, 1996, Microbiological Rev. 60:439-471).
  • Non-limiting examples of C 1 substrates include: methane, methanol, formaldehyde, formic acid (formate), carbon monoxide, carbon dioxide, methylated amines (methylamine, dimethylamine, trimethylamine, etc.), methylated thiols, or methyl halogens (bromomethane, chloromethane, iodomethane, dichloromethane, etc.).
  • Some facultative methanotrophs and facultative methylotrophs can also grow on multi-carbon compounds.
  • a C 1 metabolizing organism may also be adapted or genetically modified to use a different C 1 substrate in addition to, or instead of its usual C 1 substrate.
  • a C 1 metabolizing organism may be adapted or genetically modified to use a multi-carbon substrate in addition to its usual C 1 substrate.
  • a selected C 1 metabolizing organism may also undergo strain adaptation under selective conditions to identify variants with improved properties for production. Improved properties may include increased growth rate, yield of desired products (e.g., propylene), and tolerance of likely process contaminants.
  • a high growth variant C 1 metabolizing organism which is an organism capable of growth on a C 1 substrate as the sole carbon and energy source and which possesses an exponential phase growth rate that is faster (i.e., shorter doubling time) than its parent, reference, or wild-type organism, is selected ((see, e.g., U.S. Pat. No. 6,689,601).
  • Each of the organisms of this disclosure may be grown as an isolated culture, with a heterologous organism that may aid in growth, or one or more of C 1 metabolizing bacteria may be combined to generate a mixed culture.
  • a variety of microbial host organisms can be transformed or genetically engineered to include a novel metabolic pathway and associated enzymes as described herein to produce propylene from a carbon substrate.
  • Exemplary bacteria include Escherichia coli, Klebsiella oxytoca, Anaerobiospirillum succiniciproducens, Actinobacillus succinogenes, Mannheimia succiniciproducens, Rhizobium etli, Bacillus subtilis, Corynebacterium glutamicum, Gluconobacter oxydans, Zymomonas mobilis, Lactococcus lactis, Lactobacillus plantarum, Streptomyces coelicolor, Clostridium acetobutylicum, Pseudomonas fluorescens, and Pseudomonas putida.
  • Exemplary yeasts or fungi species include Saccharomyces cerevisiae, Schizosaccharomyces pombe, Kluyveromyces lactis, Kluyveromyces marxianus, Aspergillus terreus, Aspergillus niger, Rhizopus arrhizus, Rhizobus oryzae, and Yarrowia lipolytica. It is understood that any suitable microbial host organism can be used to introduce suitable genetic modifications (e.g., nucleic acid encoding 4-OD) to produce propylene.
  • suitable genetic modifications e.g., nucleic acid encoding 4-OD
  • Non-naturally occurring organisms as described herein can be produced by introducing expressible nucleic acid(s) encoding one or more enzymes involved in a desired biosynthetic pathway (e.g., propylene synthesis). Depending on the host organism selected for biosynthesis, nucleic acid(s) for one, some, or all of a particular biosynthetic pathway can be expressed. For example, if a selected host is deficient in one or more enzymes for a desired biosynthetic pathway (e.g., propylene synthesis), then expressible nucleic acid(s) for the deficient enzyme(s) are introduced into the host for subsequent exogenous expression.
  • a desired biosynthetic pathway e.g., propylene synthesis
  • non-naturally occurring organisms of the invention can be produced by introduced exogenous enzyme activities to obtain a desired biosynthetic pathway or a desired biosynthetic pathway can be obtained by introducing one or more exogenous enzyme activities that, together with one or more endogenous enzymes, produces the desired product, such as propylene.
  • non-naturally occurring organisms as described herein can also include other genetic modifications that facilitate or optimize a desired biosynthetic pathway or that confer other useful functions onto the host. For example, if a selected host exhibits endogenous expression of an enzyme that inhibits propylene biosynthetic pathway, then the host may be genetically modified so that it does not produce a functional enzyme or a substantial amount of a functional enzyme.
  • the present disclosure provides a non-naturally occurring C 1 metabolizing bacterium; a non-naturally occurring obligate C 1 metabolizing organism; a non-naturally occurring C 1 metabolizing organism, wherein the non-naturally occurring C 1 metabolizing organism does not include Pichia pastoris; a non-naturally occurring methanotrophic or methylotrophic bacterium; or a non-naturally occurring CO utilizing bacterium, wherein the non-naturally occurring CO utilizing bacterium naturally possesses the ability to utilize CO, wherein the non-naturally occurring C 1 metabolizing bacterium or organism converts a C 1 substrate to propylene.
  • the present disclosure provides a non-naturally occurring C 1 metabolizing organism that is not Pichia pastoris and is capable of converting a C 1 substrate into propylene.
  • the non-naturally occurring C 1 metabolizing organism is not Pichia pastoris and is a C 1 metabolizing bacterium capable of converting a C 1 substrate into propylene.
  • the non-naturally occurring C 1 metabolizing organism is an obligate C 1 metabolizing organism capable of converting a C 1 substrate into propylene.
  • the obligate C 1 metabolizing organism is a C 1 metabolizing bacterium, such as a methanotrophic or methylotrophic bacterium capable of converting a C 1 substrate into propylene.
  • a C 1 metabolizing bacterium may be a syngas utilizing bacterium that naturally possesses the ability to use syngas and convert a C 1 substrate in the syngas into propylene.
  • a C 1 metabolizing bacterium is a CO utilizing bacterium that naturally possesses the ability to use CO and convert the CO into propylene.
  • any of the non-naturally occurring C 1 metabolizing organisms as described herein includes an exogenous nucleic acid encoding an enzyme capable of decarboxylating crotonic acid.
  • the exogenous nucleic acid encoding an enzyme capable of decarboxylating crotonic acid is expressed in a sufficient amount to produce propylene.
  • the exogenous nucleic acid encoding an enzyme capable of decarboxylating crotonic acid encodes 4-oxalocrotonate decarboxylase (4-OD).
  • 4-OD is an enzyme that catalyzes the decarboxylation of 4-oxalocrotonate to 2-oxopent-4-enoate and CO 2 .
  • 4-OD is involved in the meta-cleavage pathway for the degradation of phenols, modified phenols, and catechols.
  • an exogenous nucleic acid encoding 4-OD is used to genetically engineer a novel propylene biosynthesis pathway in a non-naturally occurring organisms; 4-OD is used to catalyze decarboxylation of crotonic acid to propylene and CO 2 (see FIG. 1 ).
  • Sources of 4-OD encoding nucleic acid molecules may include any species, prokaryotic or eukaryotic, where the encoded gene product is capable of catalyzing decarboxylation of crotonic acid to propylene and CO 2 .
  • Exemplary amino acid sequences of 4-OD are shown in FIGS. 2A-D .
  • Non-naturally occurring C 1 metabolizing organisms that have an exogenous nucleic acid encoding an enzyme capable of decarboxylating crotonic acid may also include one or more exogenous nucleic acids to confer a propylene biosynthetic pathway onto the C 1 metabolizing organism.
  • an enzyme capable of decarboxylating crotonic acid e.g., 4-OD
  • one or more exogenous nucleic acids may need to be introduced into the C 1 metabolizing organism along with 4-OD in order to provide a non-naturally occurring C 1 metabolizing organism with the ability to produce crotonic acid, the substrate for propylene conversion by 4-OD.
  • a non-naturally occurring C 1 metabolizing organism that has an exogenous nucleic acid encoding an enzyme capable of decarboxylating crotonic acid may further include an exogenous nucleic acid encoding crotonase and/or an exogenous nucleic acid encoding a crotonyl-CoA thioesterase.
  • An exogenous nucleic acid encoding crotonase and an exogenous nucleic acid encoding crotonyl-CoA thioesterase are expressed in a sufficient amount to produce propylene.
  • a type II methanotrophic bacterium which possesses an endogenous PHB synthesis pathway and produces 3-hydyroxybutyryl-CoA, an intermediate in the PHB synthesis pathway, may comprise exogenous nucleic acids encoding a crotonase and/or a crotonyl-CoA thioesterase in addition to 4-OD (see FIG. 1 ).
  • Crotonase and crotonyl-CoA thioesterase are provided to catalyze the dehydration of 3-hydroxybutyryl-CoA to crotonyl-CoA and conversion of crotonyl-CoA to crotonic acid, respectively.
  • any combination of one or more enzymes that can be used to engineer a propylene biosynthesis pathway can be included in a non-naturally occurring C 1 metabolizing organism of the invention.
  • the present disclosure provides a non-naturally occurring C 1 metabolizing bacterium; a non-naturally occurring obligate C 1 metabolizing organism; a non-naturally occurring C 1 metabolizing organism, wherein the non-naturally occurring C 1 metabolizing organism does not include Pichia pastoris; a non-naturally occurring methanotrophic or methylotrophic bacterium; or a non-naturally occurring CO utilizing bacterium, wherein the non-naturally occurring CO utilizing bacterium naturally possesses the ability to utilize CO, wherein the non-naturally occurring C 1 metabolizing bacterium or organism comprises an exogenous nucleic acid encoding a crotonyl-CoA thioesterase.
  • the present disclosure provides a non-naturally occurring C 1 metabolizing organism that is not Pichia pastoris and includes an exogenous nucleic acid molecule encoding a crotonyl CoA thioesterase.
  • a non-naturally occurring C 1 metabolizing organism that is not Pichia pastoris may be an obligate C 1 metabolizing organism containing an exogenous nucleic acid molecule encoding a crotonyl CoA thioesterase.
  • the C 1 metabolizing organism may be a C 1 metabolizing bacterium or an obligate C 1 metabolizing bacterium containing an exogenous nucleic acid molecule encoding a crotonyl CoA thioesterase.
  • a C 1 metabolizing bacterium is a methanotrophic or methylotrophic bacterium containing an exogenous nucleic acid molecule encoding a crotonyl CoA thioesterase.
  • a C 1 metabolizing bacterium may be a syngas utilizing bacterium that naturally possesses the ability to use syngas and contains an exogenous nucleic acid molecule encoding a crotonyl CoA thioesterase.
  • a C 1 metabolizing bacterium may be a CO utilizing bacterium that naturally possesses the ability to use CO and contains an exogenous nucleic acid molecule encoding a crotonyl CoA thioesterase.
  • Crotonyl-CoA thioesterase refers to an enzyme that catalyzes the conversion of crotonyl-CoA to crotonic acid.
  • Sources of crotonyl-CoA thioesterase encoding nucleic acids may include any species, prokaryotic or eukaryotic, where the encoded gene product is capable of catalyzing the conversion of crotonyl-CoA to crotonic acid. Exemplary amino acid sequences for crotonyl-CoA thioesterase are shown in FIG. 3 .
  • Crotonic acid is an intermediate in the engineered propylene biosynthetic pathway disclosed herein and is a useful product in itself for the preparation of polyvinyl acetate copolymers, a synthetic butyl rubber softener, a variety of resins, fungicides, pharmaceutical intermediates, plasticizers, cosmetic polymers for hair care, and adhesives. Reduction of crotonic acid yields crotonaldehyde. Key products made from crotonaldehyde are sorbic acid, potassium sorbate (a preservative), and trimethylhydroquinone (an intermediate used in Vitamin E manufacture).
  • the present disclosure provides a non-naturally occurring C 1 metabolizing bacterium; a non-naturally occurring obligate C 1 metabolizing organism; a non-naturally occurring C 1 metabolizing organism, wherein the non-naturally occurring C 1 metabolizing organism does not include Pichia pastoris; a non-naturally occurring methanotrophic or methylotrophic bacterium; or a non-naturally occurring CO utilizing bacterium, wherein the non-naturally occurring CO utilizing bacterium naturally possesses the ability to utilize CO, wherein any of the aforementioned non-naturally occurring C 1 metabolizing bacterium or organism includes an exogenous nucleic acid encoding a crotonase.
  • the present disclosure provides a non-naturally occurring C 1 metabolizing organism that is not Pichia pastoris and includes an exogenous nucleic acid molecule encoding a crotonase.
  • the non-naturally occurring C 1 metabolizing organism that is not Pichia pastoris is a C 1 metabolizing bacterium containing an exogenous nucleic acid molecule encoding a crotonase, such as a methanotrophic or methylotrophic bacterium.
  • a C 1 metabolizing bacterium is a syngas utilizing bacterium that naturally possesses the ability to use syngas and contains an exogenous nucleic acid molecule encoding a crotonase.
  • a C 1 metabolizing bacterium is a CO utilizing bacterium that naturally possesses the ability to use CO and contains an exogenous nucleic acid molecule encoding a crotonase.
  • a non-naturally occurring C 1 metabolizing organism is an obligate C 1 metabolizing organism containing an exogenous nucleic acid molecule encoding a crotonase, such as an obligate C 1 metabolizing bacterium.
  • Crotonase also known as 3-hydroxybutyryl-CoA dehydratase, is an enzyme involved in the butyrate/butanol-producing pathway. Crotonase catalyzes the dehydration of 3-hydyroxybutyryl-CoA to crotonyl-CoA. 3-hydroxybutyryl-CoA can be an R or S stereoisomer. Enzymes that produce and convert 3-hydroxybutyryl-CoA have defined stereospecificity preferences.
  • Sources of crotonase encoding nucleic acids may include any species, prokaryotic or eukaryotic, where the encoded gene product is capable of catalyzing dehydration of 3-hydyroxybutyryl-CoA to crotonyl-CoA.
  • Exemplary amino acid sequences for crotonase are shown in FIGS. 4A-E .
  • Crotonyl-CoA is a useful intermediate that can be a substrate for an engineered propylene biosynthetic pathway (via conversion to crotonic acid by crotonyl-CoA thioesterase, which is then converted to propylene by 4-OD) or an engineered butanol/butyraldehyde biosynthetic pathway (via conversion to butyryl-CoA by butyryl-CoA dehydrogenase, which is then converted to butanol or butyraldehyde by bi-functional aldehyde dehydrogenase) (see FIG. 1 ).
  • the invention provides for a non-naturally occurring C 1 metabolizing bacterium; a non-naturally occurring obligate C 1 metabolizing organism; a non-naturally occurring C 1 metabolizing organism, wherein the non-naturally occurring C 1 metabolizing organism does not include Pichia pastoris; a non-naturally occurring methanotrophic or methylotrophic bacterium; or a non-naturally occurring CO utilizing bacterium, wherein the non-naturally occurring CO utilizing bacterium naturally possesses the ability to utilize CO; wherein the non-naturally occurring C 1 metabolizing bacterium or organism converts a C 1 substrate to propylene, and further wherein the non-naturally occurring C 1 metabolizing bacterium or organism does not have a functional PHB synthase or a substantial amount of a functional PHB synthase.
  • a non-naturally occurring C 1 metabolizing organism is a C 1 metabolizing bacterium that does not have a functional PHB synthase or a substantial amount of functional PHB synthase.
  • PHB synthase is a polyhydroxybutyrate synthesis pathway enzyme that converts hydroxybutyryl-CoA monomers into polyhydroxybutyrate (PHB) (see FIG. 1 ).
  • PHB polyhydroxybutyrate
  • Many prokaryotes synthesize PHB as a carbon and energy storage material.
  • Some yeast and other eukaryotic cells may contain small amounts of low molecular mass PHBs.
  • Two PHB synthesis pathways are known in bacteria.
  • PHB is synthesized from acetyl-CoA as a result of sequential action of three enzymes: ⁇ -ketothiolase, acetoacetyl-CoA reductase, and PHB synthase (e.g., Methylobacterium extorquens, Methylosinus trichosporium OB3b, Methylocystis and Methylosinus species).
  • ⁇ -ketothiolase acetoacetyl-CoA reductase
  • PHB synthase e.g., Methylobacterium extorquens, Methylosinus trichosporium OB3b, Methylocystis and Methylosinus species.
  • PHB synthesis can also be synthesized by: ⁇ -ketothiolase, acetocetyl-CoA reductase, crotonyl-CoA hydratases (crotonases), and PHB synthase (e.g., Methylobacterium rhodesianum ) (see, e.g., Mothes et al., Arch. Microbiol. 161:277-280, 1994; Mothes et al., Can. J. Microbiol. 41:68-72, 1995).
  • Type II methanotrophs accumulate PHB, whereas type I methanotrophs do not.
  • not having a functional PHB synthase means that its gene expression or protein activity has been reduced to undetectable levels. Reducing gene expression or protein activity of PHB synthase may be accomplished by deletion of some or all of the gene's coding sequence, introduction of one or more nucleotides into the gene's open reading frame resulting in translation of a nonsense or non-functional protein product, expressing interfering RNA or antisense sequences that target the gene, or other methods known in the art.
  • not having a substantial amount of a functional PHB synthase means that an organism has at least 40%, 45%, 50%, 55%, 60%, 65%, 70%, 75%, 80%, 85%, 90%, 95%, or 99% less gene expression or protein activity of PHB synthase as compared to a wild type organism that has a polyhydroxybutyrate synthesis pathway.
  • PHB synthase is encoded by phaC or phbC.
  • Exemplary PHB synthase amino acid sequences are provided in Table 1.
  • a non-naturally occurring C 1 metabolizing organism that is capable of converting a C 1 substrate to propylene as disclosed herein does not produce a substantial amount of polyhydroxybutryate.
  • “not producing a substantial amount of polyhydroxybutyrate” means that an organism produces at least 40%, 45%, 50%, 55%, 60%, 65%, 70%, 75%, 80%, 85%, 90%, 95%, or 99% less polyhydroxybutyrate as compared to a wildtype organism that has a polyhydroxybutyrate synthesis pathway.
  • PHB production may be inhibited, allowing more 3-hydroxybutyryl-CoA to be funneled into conversion to crotonyl-CoA by crotonase (see FIG. 1 ).
  • a C 1 metabolizing organism which is not naturally capable of PHB synthesis, may be genetically modified to possess a portion of the PHB synthesis pathway (e.g., ⁇ -ketothiolase and acetoacetyl-CoA reducatase), while excluding PHB synthase functionality.
  • Increased amounts of crotonyl-CoA which is converted to crotonic acid and then to propylene via crotonyl-CoA thioesterase and 4-OD, respectively, may result in increased propylene yields.
  • the present disclosure provides a non-naturally occurring C 1 metabolizing bacterium; a non-naturally occurring obligate C 1 metabolizing organism; a non-naturally occurring C 1 metabolizing organism, wherein the non-naturally occurring C 1 metabolizing organism does not include Pichia pastoris; a non-naturally occurring methanotrophic or methylotrophic bacterium; or a non-naturally occurring CO utilizing bacterium, wherein the non-naturally CO utilizing bacterium naturally possesses the ability to utilize CO; wherein the non-naturally occurring C 1 metabolizing bacterium or organism converts a C 1 substrate to propylene, and further wherein the non-naturally occurring C 1 metabolizing bacterium or organism has a functional ⁇ -ketothiolase and/or a functional acetoacetyl coenzyme A reductase, or has a functional ⁇ -ketothiolase and/or a functional acetoacetyl coenzyme
  • a non-naturally occurring C 1 metabolizing organism is a C 1 metabolizing bacterium that has a functional ⁇ -ketothiolase activity and a functional acetoacetyl coenzyme A reductase activity.
  • a non-naturally occurring C 1 metabolizing organism is a C 1 metabolizing bacterium that does not produce a substantial amount of polyhydroxybutyrate.
  • ⁇ -ketothiolase and acetoacetyl coenzyme A reductase are enzymes in a PHB synthesis pathway that catalyze the condensation of two acetyl-CoA molecules to acetoacetyl-CoA and reduction of acetoacetyl-CoA to 3-hydroxybutyryl-CoA, respectively (see FIG. 1 ).
  • ⁇ -ketothiolase is an enzyme that initiates biosynthesis of PHB in most bacteria.
  • a C 1 metabolizing organism may naturally possess ⁇ -ketothiolase and acetoacetyl coenzyme A reductase as part of an endogenous PHB synthesis pathway.
  • a C 1 metabolizing organism may be genetically modified with exogenous nucleic acids encoding ⁇ -ketothiolase and acetoacetyl coenzyme A reductase. These enzymes allow a C 1 metabolizing organism to produce 3-hydroxybutyryl-CoA, a precursor of propylene in an engineered biosynthetic pathway via crotonyl-CoA and crotonic acid as disclosed herein (i.e., 3-hydroxybutyrl-CoA is substrate of crotonase) (see FIG. 1 ).
  • Exogenous nucleic acids encoding ⁇ -ketothiolase and acetoacetyl coenzyme A reductase are expressed in a sufficient amount to produce propylene.
  • ⁇ -ketothiolase is encoded by phaA or phbA.
  • acetoacetyl coenzyme A reductase is encoded by phaB, hbd, or phbB.
  • Exemplary ⁇ -ketothiolase and acetoacetyl coenzyme A reductase amino acid sequences are provided in Tables 2 and 3, respectively.
  • IDINGGQFMG (SEQ ID NO: 110) gi
  • musacearum NCPPB 4381 gi
  • INGGQHMY (SEQ ID NO: 115) gi
  • a non-naturally occurring C 1 metabolizing organism is a C 1 metabolizing bacterium selected from Methylosinus trichosporium strain OB3b, Methylococcus capsulatus Bath strain, Methylomonas methanica 16A strain, Methylosinus trichosporium (NRRL B-11,196), Methylosinus sporium (NRRL B-11,197), Methylocystis parvus (NRRL B-11,198), Methylomonas methanica (NRRL B-11,199), Methylomonas albus (NRRL B-11,200), Methylobacter capsulatus (NRRL B-11,201), Methylobacterium organophilum (ATCC 27,886), Methylomonas sp AJ-3670 (FERM P-2400), Methylocella silvestris, Methylacidiphilum infernorum
  • a non-naturally occurring C 1 metabolizing organism may be a syngas or CO utilizing bacterium that naturally possesses the ability to utilize syngas or CO, such as Clostridium autoethanogenum, Clostridium ljungdahli, Clostridium ragsdalei, Clostridium carboxydivorans, Butyribacterium methylotrophicum, Clostridium Woodii, Clostridium neopropanologen Ralstonia eutropha, or Eurobacterium limosum.
  • a non-naturally occurring C 1 metabolizing organism may be a methylotrophic bacterium, such as Methylobacterium extorquens, Methylobacterium radiotolerans, Methylobacterium populi, Methylobacterium chloromethanicum, or Methylobacterium nodulans.
  • Methylobacterium extorquens such as Methylobacterium extorquens, Methylobacterium radiotolerans, Methylobacterium populi, Methylobacterium chloromethanicum, or Methylobacterium nodulans.
  • the present disclosure provides non-naturally occurring microbial organisms that have been genetically modified with a novel metabolic pathway for producing propylene from a carbon substrate. More specifically, the non-naturally occurring microbial organisms include an exogenous nucleic acid encoding 4-oxalocrotonate decarboxylase and convert a carbon substrate to propylene. As described previously, 4-OD is used in a novel propylene biosynthetic pathway to catalyze decarboxylation of crotonic acid to propylene and CO 2 (see FIG. 1 ).
  • Sources of 4-OD encoding nucleic acid molecules may include any species, prokaryotic or eukaryotic, where the encoded gene product is capable of catalyzing decarboxylation of crotonic acid to propylene and CO 2 .
  • Exemplary amino acid sequences of 4-OD are shown in FIG. 2 .
  • the present disclosure provides a non-naturally occurring microbial organism containing an exogenous nucleic acid encoding a 4-oxalocrotonate decarboxylase, wherein the non-naturally occurring microbial organism is capable of converting a carbon substrate into propylene.
  • non-naturally occurring microbial organisms that include an exogenous nucleic acid encoding a 4-oxalocrotonate decarboxylase and convert a carbon substrate into propylene may further include an exogenous nucleic acid encoding crotonase, or further include an exogenous nucleic acid encoding a crotonase and an exogenous nucleic acid encoding a crotonyl thioesterase.
  • a microbial organism may or may not have endogenous enzyme(s) that would participate with 4-OD in forming a biosynthetic propylene synthesis pathway.
  • crotonase catalyzes the dehydration of 3-hydyroxybutyryl-CoA to crotonyl-CoA.
  • Crotonyl-CoA thioesterase catalyzes the conversion of crotonyl-CoA to crotonic acid. For example, if a host microbial organism selected is deficient in crotonase, then exogenous expression of crotonase can be included in the microbial organism.
  • a host microbial organism is deficient in crotonase and a thioesterase capable of converting crotonyl-CoA to crotonic acid, then exogenous expression of crotonase and crotonyl-CoA thioesterase can be included in the microbial organism.
  • exogenous expression of all of these enzymes of a propylene biosynthetic pathway may be included, even if the host microbial organism contains at least one of the propylene pathway enzymes (e.g., crotonase or crotonyl thioesterase).
  • expression of exogenous nucleic acids encoding enzymes of the propylene biosynthetic pathway disclosed herein is in a sufficient amount to produce propylene.
  • Sources of crotonase and crotonyl-CoA thioesterase encoding nucleic acids may include any species, prokaryotic or eukaryotic, where the encoded gene products are capable of catalyzing dehydration of 3-hydyroxybutyryl-CoA to crotonyl-CoA and conversion of crotonyl-CoA to crotonic acid, respectively.
  • Exemplary amino acid sequences for crotonase and crotonyl-CoA thioesterase are shown in FIG. 4 and FIG. 3 , respectively.
  • non-naturally occurring microbial organisms as described herein do not have a functional PHB synthase or a substantial amount of functional PHB synthase.
  • propylene synthesis yields may be increased by funneling more 3-hydroxybutyryl-CoA into the propylene pathway via conversion to crotonyl-CoA and to crotonic acid and to propylene (see FIG. 1 ).
  • non-naturally occurring microbial organisms as described herein do not possess an endogenous PHB synthesis pathway
  • non-naturally occurring microbial organisms may be genetically modified to include an exogenous nucleic acid encoding ⁇ -ketothiolase and an exogenous nucleic acid encoding acetoacetyl-CoA reductase to provide the capability of producing 3-hydroxybutyrl-CoA, substrate for the crotonase enzyme in the propylene synthesis pathway described herein.
  • Non-naturally occurring microbial organisms that do possess an endogenous PHB synthesis pathway may also be genetically modified with an exogenous nucleic acid encoding ⁇ -ketothiolase and an exogenous nucleic acid encoding acetoacetyl-CoA reductase to increase expression of these enzymes.
  • ⁇ -ketothiolase is encoded by phaA or phbA.
  • acetoacetyl coenzyme A reductase is encoded by phaB or phbB.
  • Exemplary ⁇ -ketothiolase and acetoacetyl coenzyme A reductase amino acid sequences are provided in Tables 2 and 3, respectively.
  • Nucleic acid sequences encoding for and amino acid sequences for proteins, protein domains and fragments thereof, for proteins described herein, such as 4-OD, crotonase, crotonyl thioesterase, acetoacetyl coenzyme A reductase, or ⁇ -ketothiolase, and domains thereof, that are described herein include natural and recombinantly engineered variants. These variants retain the function and biological activity (including enzymatic activities if applicable) associated with the parent (or wildtype) protein. These variants may have improved function and biological activity (e.g., higher enzymatic activity, improved specificity for substrate) than the parent (or wildtype protein).
  • a variant 4-OD enzyme may be engineered with reduced or eliminated decarboxylation activity on 4-oxalocrotonate, but retains or has increased decarboxylation activity on crotonic acid substrate.
  • Conservative substitutions of amino acids are well known and may occur naturally in the polypeptide (e.g., naturally occurring genetic variants) or may be introduced when the polypeptide is recombinantly produced. Amino acid substitutions, deletions, and additions may be introduced into a polypeptide using well-known and routinely practiced mutagenesis methods (see, e.g., Sambrook et al. Molecular Cloning: A Laboratory Manual, 3d ed., Cold Spring Harbor Laboratory Press, NY 2001).
  • Oligonucleotide-directed site-specific (or segment specific) mutagenesis procedures may be employed to provide an altered polynucleotide that has particular codons altered according to the substitution, deletion, or insertion desired. Deletion or truncation variants of proteins may also be constructed by using convenient restriction endonuclease sites adjacent to the desired deletion. Alternatively, random mutagenesis techniques, such as alanine scanning mutagenesis, error prone polymerase chain reaction mutagenesis, and oligonucleotide-directed mutagenesis may be used to prepare polypeptide variants (see, e.g., Sambrook et al., supra).
  • Differences between a wild type (or parent) nucleic acid or polypeptide and the variant thereof may be determined by methods routinely practiced in the art to determine identity, which are designed to give the greatest match between the sequences tested. Methods to determine sequence identity can be applied from publicly available computer programs. Computer program methods to determine identity between two sequences include, for example, BLASTP, BLASTN (Altschul, S. F. et al., J. Mol. Biol. 215: 403-410 (1990), and FASTA (Pearson and Lipman Proc. Natl. Acad. Sci. USA 85; 2444-2448 (1988). The BLAST family of programs is publicly available from NCBI and other sources ( BLAST Manual, Altschul, S., et al., NCBI NLM NIH Bethesda, Md.
  • Assays for determining whether a polypeptide variant folds into a conformation comparable to the non-variant polypeptide or fragment include, for example, the ability of the protein to react with mono- or polyclonal antibodies that are specific for native or unfolded epitopes, the retention of ligand-binding functions, the retention of enzymatic activity (if applicable), and the sensitivity or resistance of the mutant protein to digestion with proteases (see Sambrook et al., supra). Polypeptides, variants and fragments thereof, can be prepared without altering a biological activity of the resulting protein molecule (i.e., without altering one or more functional activities in a statistically significant or biologically significant manner).
  • substitutions are generally made by interchanging an amino acid with another amino acid that is included within the same group, such as the group of polar residues, charged residues, hydrophobic residues, and/or small residues, and the like.
  • the effect of any amino acid substitution may be determined empirically merely by testing the resulting modified protein for the ability to function in a biological assay, or to bind to a cognate ligand or target molecule.
  • propylene may lead to the biosynthetic production of propylene, including other pathway intermediates (e.g., crotonate or crotonyl-CoA) and downstream products.
  • pathway intermediates e.g., crotonate or crotonyl-CoA
  • propylene undergoes addition reactions relatively easily at room temperature due to the relative weakness of its double bond.
  • propylene may be converted into other downstream products (e.g., polypropylene, propylene oxide).
  • addition reactions may occur spontaneously in the non-naturally occurring microbial organisms or C 1 metabolizing organisms, or the organisms may be further genetically modified to add or enhance addition reaction capability (e.g., to increase conversion to polypropylene or propylene oxide).
  • addition reaction capability e.g., to increase conversion to polypropylene or propylene oxide.
  • methanotrophic bacteria that are genetically modified with a biosynthetic propylene pathway propylene that is produced may spontaneously be oxidized into propylene oxide via a methane-monooxygenase-catalyzed reaction (see, e.g., U.S. Patent Publication 2002/0168733, U.S. Patent Publication 2003/0203456).
  • non-naturally occurring microbial organisms or C 1 metabolizing organisms may comprise further genetic modifications to inhibit or reduce endogenous enzyme activity that catalyze an addition reaction (e.g., to inhibit conversion to propylene oxide).
  • an addition reaction e.g., to inhibit conversion to propylene oxide.
  • non-naturally occurring organisms that spontaneously convert or are genetically modified to convert propylene into a downstream product e.g. propylene oxide
  • the downstream product e.g., propylene oxide
  • the downstream product e.g., propylene oxide
  • the present disclosure provides methods of producing propylene by culturing non-naturally occurring C 1 metabolizing organisms according to any of the embodiments as described herein (e.g., capable of converting a C 1 substrate into propylene), under conditions sufficient to produce propylene.
  • the non-naturally occurring C 1 metabolizing organisms as disclosed herein produce from about 0.1 grams of propylene/L/day to about 50 grams of propylene/L/day.
  • the non-naturally occurring C 1 metabolizing organisms as disclosed herein produce about 0.1 g, 0.5 g, 1 g, 2 g, 3 g, 4 g, 5 g, 6 g, 7 g, 8 g, 9 g, 10 g, 11 g, 12 g, 13 g, 14 g, 15 g, 16 g, 17 g, 18 g, 19 g, 20 g, 25 g, 30 g, 35 g, 40 g, 45 g, 50 g, 55 g, or 60 g propylene/L/day.
  • the present disclosure provides methods of producing propylene in non-naturally occurring microbial organisms according to any of the embodiments as described herein (e.g., having a partially heterologous propylene biosynthetic pathway), by culturing the non-naturally occurring microbial organisms under conditions sufficient to produce propylene.
  • the non-naturally occurring microbial organisms as disclosed herein produce from about 0.1 grams of propylene/L/day to about 50 grams of propylene/L/day.
  • the non-naturally occurring microbial organisms as disclosed herein produce about 0.1 g, 0.5 g, 1 g, 2 g, 3 g, 4 g, 5 g, 6 g, 7 g, 8 g, 9 g, 10 g, 11 g, 12 g, 13 g, 14 g, 15 g, 16 g, 17 g, 18 g, 19 g, 20 g, 25 g, 30 g, 35 g, 40 g, 45 g, 50 g, 55 g, or 60 g propylene/L/day.
  • the non-naturally occurring C 1 metabolizing organisms as disclosed herein produces from about 0.1 grams of crotonic acid/L/day to about 50 grams of crotonic acid/L/day.
  • the non-naturally occurring C 1 metabolizing organism as disclosed herein produces about 0.1 g, 0.5 g, 1 g, 2 g, 3 g, 4 g, 5 g, 6 g, 7 g, 8 g, 9 g, 10 g, 11 g, 12 g, 13 g, 14 g, 15 g, 16 g, 17 g, 18 g, 19 g, 20 g, 25 g, 30 g, 35 g, 40 g, 45 g, 50 g, 55 g, or 60 g crotonic acid/L/day.
  • nucleic acids e.g., a nucleic acid encoding 4-OD, crotonyl-CoA thioesterase, or crotonase
  • nucleic acids may undergo codon optimization to enhance protein expression.
  • Codon optimization refers to alteration of codons in genes or coding regions of nucleic acids for transformation of an organism to reflect the typical codon usage of the host organism without altering the polypeptide for which the DNA encodes. Codon optimization methods for optimum gene expression in heterologous organisms have been previously described (see., e.g., Welch et al., 2009, PLoS One 4:e7002; Gustafsson et al., 2004, Trends Biotechnol. 22:346-353; Wu et al., 2007, Nucl. Acids Res. 35:D76-79; Villalobos et al., 2006, BMC Bioinformatics 7:285; U.S. Patent Publication 2011/0111413; U.S. Patent Publication 2008/0292918).
  • Non-naturally occurring microbial organisms as described herein may be transformed to comprise at least one exogenous nucleic acid to provide the host organism with a new or enhanced activity (e.g., enzymatic activity) or may be genetically modified to remove or substantially reduce an endogenous gene function (e.g., enzymatic activity) using a variety of methods known in the art. Recombinant methods for exogenous expression of nucleic acids in microbial organisms are well known in the art.
  • a non-naturally occurring C 1 metabolizing bacterium; non-naturally occurring obligate C 1 metabolizing organism; non-naturally occurring C 1 metabolizing organism, wherein the organism does not include Pichia pastoris; a non-naturally occurring methanotrophic or methylotrophic bacterium; or a non-naturally occurring CO utilizing bacterium as described herein may be transformed to comprise at least one exogenous nucleic acid to provide the host with a new or enhanced activity (e.g., enzymatic activity) or may be genetically modified to remove or substantially reduce an endogenous gene function (e.g., enzymatic activity) using a variety of methods known in the art. While genetic engineering tools of C 1 metabolizing organisms are not as extensive as for other microbial organisms (e.g., E. coli ), significant advances have been made allowing genetic manipulation of C 1 metabolizing organisms, as summarized below.
  • Transformation refers to the transfer of a nucleic acid (e.g., exogenous nucleic acid) into the genome of a host organism, resulting in genetically stable inheritance.
  • Host organisms containing the transformed nucleic acid are referred to as “non-naturally occurring” or “recombinant” or “transformed” or “transgenic” organisms.
  • Expression systems and expression vectors useful for the expression of heterologous nucleic acids in C 1 metabolizing organisms are known.
  • Vectors or cassettes useful for the transformation of suitable host organisms are available.
  • Bacterial conjugation which refers to a particular type of transformation involving direct contact of donor and recipient cells, is more frequently used for the transfer of nucleic acids into C 1 metabolizing bacteria. Bacterial conjugation involves mixing “donor” and “recipient” cells together in close contact with each other. Conjugation occurs by formation of cytoplasmic connections between donor and recipient bacteria, with unidirectional transfer of newly synthesized donor nucleic acids into the recipient cells.
  • a recipient in a conjugation reaction is any cell that can accept nucleic acids through horizontal transfer from a donor bacterium.
  • a donor in a conjugation reaction is a bacterium that contains a conjugative plasmid, conjugative transposon, or mobilized plasmid.
  • the physical transfer of the donor plasmid can occur through a self-transmissible plasmid or with the assistance of a “helper” plasmid.
  • Conjugations involving C 1 metabolizing bacteria have been previously described in Stolyar et al., 1995, Mikrobiologiya 64:686-691; Motoyama et al., 1994, Appl. Micro. Biotech. 42:67-72; Lloyd et al., 1999, Archives of Microbiology 171:364-370; and Odom et al., PCT Publication WO 02/18617; Ali et al., 2006, Microbiol. 152:2931-2942.
  • heterologous nucleic acid molecules in C 1 metabolizing bacteria is known in the art (see, e.g., U .S. Pat. No. 6,818,424, U.S. Patent Publication 2003/0003528).
  • Mu transposon based transformation of methylotrophic bacteria has been described (see, e.g., Akhverdyan et al., 2011, Appl. Microbiol. Biotechnol. 91:857-871).
  • a mini-Tn7 transposon system for single and multicopy expression of heterologous genes without insertional inactivation of host genes in Methylobacterium has been described (see, e.g. U.S. Patent Publication 2008/0026005).
  • Suitable homologous or heterologous promoters for high expression of exogenous nucleic acids may be utilized.
  • U.S. Pat. No. 7,098,005 describes the use of promoters that are highly expressed in the presence of methane or methanol for heterologous gene expression in C 1 metabolizing bacteria. Additional promoters that may be used include deoxy-xylulose phosphate synthase methanol dehydrogenase operon promoter (Springer et al., 1998, FEMS Microbiol. Lett. 160:119-124); the promoter for PHA synthesis (Foellner et al. 1993, Appl. Microbiol. Biotechnol.
  • Non-native promoters include the lac operon Plac promoter (Toyama et al., 1997, Microbiology 143:595-602) or a hybrid promoter such as Ptrc (Brosius et al., 1984, Gene 27:161-172). Regulation of expression of an exogenous nucleic acid molecule in the host C 1 metabolizing organism may also be utilized. For example, an inducible/regulatable system of recombinant protein expression in methylotrophic and methanotrophic bacteria has been described in US Patent Publication 2010/0221813.
  • C 1 metabolizing organisms may be grown by batch culture and continuous culture methodologies.
  • the cultures are grown in a controlled culture unit, such as a fermentor, bioreactor, hollow fiber membrane bioreactor, or the like.
  • a classical batch culturing method is a closed system where the composition of the media is set at the beginning of the culture and not subject to external alterations during the culture process.
  • the media is inoculated with the desired organism or organism and growth or metabolic activity is permitted to occur without adding anything to the system.
  • a “batch” culture is batch with respect to the addition of carbon source and attempts are often made at controlling factors such as pH and oxygen concentration.
  • the metabolite and biomass compositions of the system change constantly up to the time the culture is terminated.
  • cells moderate through a static lag phase to a high growth logarithmic phase and finally to a stationary phase where growth rate is diminished or halted. If untreated, cells in the stationary phase will eventually die.
  • Cells in log phase are often responsible for the bulk production of end product or intermediate in some systems. Stationary or post-exponential phase production can be obtained in other systems.
  • the Fed-Batch system is a variation on the standard batch system.
  • Fed-Batch culture processes comprise a typical batch system with the modification that the substrate is added in increments as the culture progresses.
  • Fed-Batch systems are useful when catabolite repression is apt to inhibit the metabolism of the cells and where it is desirable to have limited amounts of substrate in the media. Measurement of the actual substrate concentration in Fed-Batch systems is difficult and is therefore estimated on the basis of the changes of measureable factors, such as pH, dissolved oxygen, and the partial pressure of waste gases such as CO2.
  • Batch and Fed-Batch culturing methods are common and known in the art (see, e.g., Thomas D. Brock, Biotechnology: A Textbook of Industrial Microbiology, 2 nd Ed. (1989) Sinauer Associates, Inc., Sunderland, Mass.; Deshpande, 1992, Appl. Biochem. Biotechnol. 36:227, herein incorporated by reference).
  • Continuous cultures are “open” systems where a defined culture media is added continuously to a bioreactor and an equal amount of conditioned media is removed simultaneously for processing. Continuous cultures generally maintain the cells at a constant high liquid phase density where cells are primarily in logarithmic phase growth. Alternatively, continuous culture may be practiced with immobilized cells where carbon and nutrients are continuously added and valuable products, by-products, and waste products are continuously removed from the cell mass. Cell immobilization may be performed using a wide range of solid supports composed of natural and/or synthetic materials.
  • Continuous or semi-continuous culture allows for the modulation of one factor or any number of factors that affect cell growth or end product concentration.
  • one method will maintain a limited nutrient, such as the carbon source or nitrogen level, at a fixed rate and allow all other parameters to modulate.
  • a number of factors affecting growth can be altered continuously while the cell concentration, measured by media turbidity, is kept constant.
  • Continuous systems strive to maintain steady state growth conditions and thus the cell loss due to media being drawn off must be balanced against the cell growth rate in the culture.
  • Culture media must contain carbon substrates for the C 1 metabolizing organisms.
  • Suitable substrates include, but are not limited to C 1 substrates such as methane, methanol, formaldehyde, formic acid (formate), carbon monoxide, carbon dioxide, methylated amines (methylamine, dimethylamine, trimethylamine, etc.), methylated thiols, or methyl halogens (bromomethane, chloromethane, iodomethane, dichloromethane, etc.).
  • a non-naturally occurring C 1 metabolizing organism of any of the disclosed embodiments is capable of growth on methane, methanol, formaldehyde, formic acid, carbon monoxide, carbon dioxide, methylated amines, methylated thiols, or methyl halogens as a carbon source.
  • a culture media may comprise a single C 1 substrate as the sole carbon source for the C 1 metabolizing organism, or comprise a mixture of two or more C 1 substrates (mixed C 1 substrates) as multiple carbon sources for the C 1 metabolizing organism.
  • C 1 metabolizing organisms are known to utilize non-C 1 substrates, such as glucosamine and a variety of amino acids for metabolic activity.
  • non-C 1 substrates such as glucosamine and a variety of amino acids for metabolic activity.
  • Candida species can metabolize alanine or oleic acid (Sulter et al., 1990, Arch. Microbiol. 153:485-489).
  • Methylobacterium extorquens AM1 is capable of growth on a limited number of C2, C3, and C4 substrates (Van Dien et al., 2003, Microbiol. 149:601-609).
  • a C 1 metabolizing organism may be engineered with the ability to utilize alternative carbon substrates.
  • a culture media may comprise a mixture of carbon substrates, with single and multi-carbon compounds (mixed carbon sources), depending on the C 1 metabolizing organism selected.
  • a C 1 substrate provided in a mixed carbon source may be a primary carbon source for a C 1 metabolizing organism.
  • a carbon source may be added to culture media initially, provided to culture media intermittently, or supplied continuously.
  • Propylene or propylene oxide produced by the non-naturally occurring organisms described herein may be dissolved in the liquid phase or present as gas in the headspace of the culture container. Propylene may be mixed with other gases in the headspace, such as O 2 , CO 2 , H 2 O vapor, or methane.
  • Methods for recovering propylene from a gas mixture include for example, continuous liquid-liquid extraction, pervaporation, membrane filtration, membrane separation, reverse osmosis, electrodialysis, distillation, crystallization, centrifugation, extractive filtration, ion exchange chromatography, size exclusion chromatography, adsorption chromatography, and ultrafiltration (see., e.g., Bai et al., 2000, J. Memb. Sci. 174:67-79; Shi et al., 2006, J. Membr. Sci.
  • Methods for measuring propylene and propylene oxide production include HPLC (high performance liquid chromatography), GC-MS (gas chromatography-mass spectrometry), GC-FID (gas chromatography-flame ionization detector) and LC-MS (liquid chromatography-mass spectrometry).
  • HPLC high performance liquid chromatography
  • GC-MS gas chromatography-mass spectrometry
  • GC-FID gas chromatography-flame ionization detector
  • LC-MS liquid chromatography-mass spectrometry
  • the non-naturally occurring organisms as described herein do not produce a substantial amount of polyhydroxybutyrate (PHB).
  • PHB polyhydroxybutyrate
  • “not producing a substantial amount of polyhydroxybutyrate” means that an organism produces at least 40%, 45%, 50%, 55%, 60%, 65%, 70%, 75%, 80%, 85%, 90%, 95%, 99% less polyhydroxybutyrate as compared to a wildtype organism that has a polyhydroxybutyrate synthesis pathway.
  • Methods for determining PHB concentration are well known in the art. Braunegg et al., (1978, European J. Appl. Microbiol. Biotechnol.
  • Additional methods for measuring PHB synthesis may include measuring PHB synthase expression (see., e.g., Langenbach et al., 1997, FEMS Microbiol. Lett. 150:303-309; Solaiman et al., 2008, J. Ind. Microbiol. & Biotechnol. 35:111-120) or enzyme activity (see., e.g., Schubert et al., 1988, J. Bacteriol. 170:5837-5847; Liebergesell et al., 1994, Eur. J. Biochem. 226:71-80; Valentin and Steinbuchel, 1994, Appl. Microbiol. Biotechnol. 40:699-709).
  • a mobilizing plasmid to be conjugated was first transformed into E. coli S17-1 using standard electroporation methods. Transformation was confirmed by selection of kanamycin-resistant colonies on LB-agar containing 20 ⁇ g/mL kanamycin. Transformed colonies were inoculated into LB media containing 20 ⁇ g/mL kanamycin and shaken overnight at 37° C. A 10 mL aliquot of the overnight culture was then collected on a sterile 47 mm nitrocellulose filter (0.2 mm pore size). The E. coli donor strain was washed on the filter with 50 mL sterile NMS media to remove residual media and antibiotic.
  • a sample of the M. trichosporium OB3b recipient strain was inoculated into 100 mL serum bottles containing 20-50 mL NMS media.
  • the headspace of the bottles was then flushed with a 1:1 mixture of oxygen and methane, and the bottles were sealed with butyl butyl rubber septa and crimped.
  • the bottles were shaken continuously in a 30° C. incubator until reaching an OD600 of approximately 0.3.
  • the cells were then collected on the same filter as the E. coli donor strain.
  • the filter was again washed with 50 mL of sterile NMS media.
  • the filter was placed (cells up) on an NMS agar plate containing 0.02% (w/v) proteose peptone and incubated for 24 h at 30° C. in the presence of methane and oxygen. After 24 h, cells were re-suspended in 10 mL sterile (NMS) medium before being concentrated by centrifugation. The pellet was re-suspended in 1 mL sterile NMS media. Aliquots (100 ⁇ l) were spread onto NMS agar plates containing 10 ⁇ g/mL kanamycin.
  • NMS sterile
  • the plates were incubated in sealed chambers containing a 1:1 mixture of methane and oxygen maintained at 30° C.
  • the gas mixture was replenished every 2 days until colonies formed, typically after 7-14 days. Colonies were streaked onto NMS plates containing kanamycin to confirm kanamycin resistance as well as to further isolate transformed methanotroph cells from residual E. coli donor cells.
  • a synthetic cDNA construct of the M. trichosporium OB3b phaC gene was synthesized, incorporating several stop mutations and frame shifts in the 5′ region of the gene. This cDNA construct was cloned into an appropriate vector for conjugation, but lacking an origin of replication that functions in methanotrophs, and introduced into M. trichosporium OB3b using the methods described above. This technique ensures that any kanamycin resistant M. trichosporium OB3b colonies must have been incorporated into the genome by recombination.
  • homologous recombination events are well-established in the art, and typically performed by PCR and sequencing using unique primers in the genome and the vector construct to confirm proper insertion. Homologous recombinants are then grown in the absence of selective pressure (e.g., kanamycin) for several generations, and sensitive clones which have lost the resistance marker are identified by replica plating (or equivalent technique). Approximately 50% of sensitive revertants possess the mutated form of the target gene in place of the wild-type version.
  • selective pressure e.g., kanamycin
  • Loss of phaC function is confirmed by growing the cells under nitrogen limited conditions and measuring PHB content as described in Pieja A J, Rostkowski K H, Criddle C S, Distribution and selection of poly-3-hydroxybutyrate production capacity in methanotrophic proteobacteria. Microb. Ecol. 2011 October; 62(3):564-73. Briefly, the putative knockout clones inoculated into 100 mL serum bottles containing 20-50 mL NMS media. The headspace of the bottles was then flushed with a 1:1 mixture of oxygen and methane, and the bottles were sealed with butyl rubber septa and crimped. The bottles were shaken continuously in a 30° C.
  • PHB concentration determination PHB concentration is measured directly via gas chromatography. For each sample, 5 to 10 mg of freeze-dried biomass is weighed out on an analytical balance, transferred to a 12-ml glass vial, and sealed with a polytetrafluoroethylene (PTFE)-lined plastic cap. 2 mL of methanol acidified with sulfuric acid (3%, vol/vol) and containing 1.0 g/L benzoic acid and 2 ml of chloroform are added to each vial. The vials are shaken gently and then heated at 100° C. for 3.5 h. Once the vials cool to room temperature, 1 ml deionized water is added to each.
  • PTFE polytetrafluoroethylene
  • the vials are subjected to vortex mixing for 30 s and allowed to stand until phase separation is complete.
  • the organic phase is analyzed using an Agilent 6890N gas chromatograph equipped with an HP-5 column [containing (5% phenyl)-methylpolysiloxane; Agilent Technologies] and a flame ionization detector (FID).
  • dl- ⁇ -Hydroxybutyric acid sodium salt is used as a standard.
  • Selected crotonase SEQ ID NO:32
  • crotonyl-CoA thioesterase SEQ ID NO:29
  • 4-oxalocrotonate decarboxylase SEQ ID NO:10 sequences were codon optimized (see Table 4) and synthesized with appropriate promoters.
  • the genes are then cloned and transformed into the phaC knockout strain as described above. Transformation is confirmed by resistance of the cells to antibiotic selection, and gene expression is confirmed by northern blot (to confirm RNA transcription), western blot, or ELISA methods (to confirm protein expression).
  • the headspace gas is refreshed every 2 days as above; however, immediately prior to refreshing the headspace, samples are drawn from both the liquid phase and headspace using a 10 ⁇ L Hamilton syringe and injected into a HP5890 GC equipped with a CP-PoraBOND U 25 m ⁇ 0.32 mm column and an FID maintained at 200° C.
  • the injector is connected in splitless mode and maintained at 250° C.
  • Samples are run with He Gas at 7.3 ml/min as a carrier gas; the oven program is set as follows: hold at 50° C. 1.5 min; ramp to 300° C. at 10° C./min; hold at 300° C. 10 min.
  • Propylene is identified by retention time compared to pure propylene diluted in air or dissolved in pure H 2 O. Samples are also taken to measure optical density of the culture, allowing quantitation of specific propylene production rates per cell. Note that because methane is the only carbon source provided to the cells, all propylene produced must have been derived from methane.
  • a mobilizing plasmid to be conjugated was first transformed into E. coli S17-1 using standard electroporation methods. Transformation was confirmed by selection of kanamycin-resistant colonies on LB-agar containing 20 ⁇ g/mL kanamycin. Transformed colonies were inoculated into LB media containing 20 ⁇ g/mL kanamycin and shaken overnight at 37° C. A 10 mL aliquot of the overnight culture was then collected on a sterile 47 mm nitrocellulose filter (0.2 mm pore size). The E. coli donor strain was washed on the filter with 50 mL sterile NMS to remove residual media and antibiotic.
  • a sample of the M. capsulatus recipient strain was inoculated into 100 mL serum bottles containing 20-50 mL NMS media.
  • the headspace of the bottles was then flushed with a 1:1 mixture of oxygen and methane, and the bottles were sealed with butyl rubber septa and crimped.
  • the bottles were shaken continuously in a 45° C. incubator until reaching an OD600 of approximately 0.3.
  • the cells were then collected on the same filter as the E. coli donor strain.
  • the filter was again washed with 50 mL of sterile NMS media.
  • the filter was placed (cells up) on an NMS agar plate containing 0.02% (w/v) proteose peptone and incubated for 24 h at 37° C.
  • the plates were incubated in sealed chambers containing a 1:1 mixture of methane and oxygen maintained at 45° C.
  • the gas mixture was replenished every 2 days until colonies formed, typically after 7-14 days. Colonies were streaked onto NMS plates containing kanamycin to confirm kanamycin resistance as well as to further isolate transformed methanotroph cells from residual E. coli donor cells.
  • M. capsulatus does not have a native PHA pathway, hence no pathway genes (i.e., phaC) need to be deleted.
  • phaA and phaB function must be introduced to the cells to provide the substrate for the crotonase enzyme (i.e., 3-hydroxybutryl-CoA).
  • Selected phaA (SEQ ID NO:77), phaB (SEQ ID NO:123), crotonase (SEQ ID NO:32), crotonyl-CoA thioesterase (SEQ ID NO:29), and 4-oxalocrotonate decarboxylase (SEQ ID NO:10) sequences were codon optimized (see Table 5) and synthesized with appropriate promoters.
  • the genes are then cloned and transformed into M. capsulatus as described above. Transformation is confirmed by resistance of the cells to antibiotic selection, and gene expression is confirmed by northern blot (to confirm RNA transcription), western blot, or ELISA methods (to confirm protein expression).
  • M. capsulatus transformed with the vector described above are inoculated into 100 mL serum bottles containing 20-50 mL NMS media and 10 ⁇ g/mL kanamycin.
  • the bottle headspace is flushed with a 1:1 mixture of methane and oxygen, and the bottles are sealed with butyl rubber septa and crimped.
  • the bottles are then shaken continuously while being incubated at 42-45° C.
  • the headspace gas is refreshed every 2 days as above; however, immediately prior to refreshing the headspace, samples are drawn from both the liquid phase and headspace using a 10 ⁇ L Hamilton syringe and injected into a HP5890 GC equipped with a CP-PoraBOND U 25 m ⁇ 0.32 mm column and an FID maintained at 200° C.
  • the injector is connected in splitless mode and maintained at 250° C.
  • Samples are run with He Gas at 7.3 ml/min as a carrier gas; the oven program is set as follows: hold at 50° C. 1.5 min; ramp to 300° C. at 10° C./min; hold at 300° C. 10 min.
  • Propylene is identified by retention time compared to pure propylene diluted in air or dissolved in pure H 2 O. Samples are also taken to measure optical density of the culture, allowing quantitation of specific propylene production rates per cell. Note that because methane is the only carbon source provided to the cells, all propylene produced must have been derived from methane.
  • wild-type (wt) M. extorquens is cultured at 30° C. in NMS media supplemented with 1% methanol.
  • Cells of M. extorquens NR-2 grown to the middle logarithmic phase (1.4 ⁇ 10 9 /ml) are harvested by centrifugation at 6,000 ⁇ g for 10 min and washed with electroporation buffer (10 mM Tris-HCl, 2 mM MgCl 2 .6H 2 O, 10% [wt/vol] sucrose [pH 7.5]). Cells are re-suspended in the same buffer at a cell concentration of 7.0 ⁇ 10 10 /ml.
  • the cell suspension and the solution of vector (70 ⁇ g/mL) are mixed at a ratio of 9:1 (vol/vol) in an Eppendorf tube.
  • the mixture (10 ⁇ L) is then transferred into a space between the electrodes of a chamber, where it is equilibrated for 3 min.
  • a 5 ⁇ L aliquot of the mixture is transferred to an Eppendorf tube.
  • 0.2 mL of NMS medium is then added to the tube.
  • the cell suspension is then incubated for 2 h at 30° C. to allow expression of the antibiotic resistance genes prior to plating on NMS plates containing 1% methanol and 20 ⁇ g/mL kanamycin.
  • the plates were incubated at 30° C. until colonies formed. Colonies were streaked onto duplicate plates to confirm kanamycin resistance as well as to further isolate transformed methylotroph cells from residual E. coli donor cells.
  • insertion cassettes containing a kanamycin resistance marker were constructed with flanking sequences homologous to the areas flanking the phaC gene in the M. extorquens genome.
  • a tetracycline resistance gene was incorporated elsewhere in the plasmid.
  • Transformants were initially selected for resistance to kanamycin, and then screened for sensitivity to tetracycline to identify potential double cross-over recombination events. Correct insertion into and deletion of the phaC gene was confirmed by PCR.
  • Loss of phaC function is confirmed by growing the cells under nitrogen limited conditions and measuring PHA content as described in Pieja A J, Rostkowski K H, Criddle C S, Distribution and selection of poly-3-hydroxybutyrate production capacity in methanotrophic proteobacteria, Microb. Ecol. 2011 October; 62(3):564-73.
  • Selected crotonase SEQ ID NO:32
  • crotonyl-coA thioesterase SEQ ID NO:29
  • 4-oxalocrotonate decarboxylase SEQ ID NO:10 sequences were codon optimized (see Table 6) and synthesized with appropriate promoters.
  • the genes are then cloned and transformed into the phaC knockout strain as described above. Transformation is confirmed by resistance of the cells to antibiotic selection, and gene expression is confirmed by northern blot (to confirm RNA transcription), western blot, or ELISA methods (to confirm protein expression).
  • the headspace gas is refreshed every day; however, immediately prior to refreshing the headspace, samples are drawn from both the liquid phase and headspace using a 10 ⁇ L Hamilton syringe and injected into a HP5890 GC equipped with a CP-PoraBOND U 25 m x 0.32 mm column and an FID maintained at 200° C.
  • the injector is connected in splitless mode and maintained at 250° C.
  • Samples are run with He Gas at 7.3 ml/min as a carrier gas; the oven program is set as follows: hold at 50° C. 1.5 min; ramp to 300° C. at 10° C./min; hold at 300° C. 10 min.
  • Propylene is identified by retention time compared to pure propylene diluted in air or dissolved in pure H 2 O. Samples are also taken to measure optical density of the culture, allowing quantitation of specific propylene production rates per cell. Note that because methanol is the only carbon source provided to the cells, all propylene produced must have been derived from
  • C. autoethanogenum is cultivated anaerobically in modified PETC medium (ATCC medium 1754) at 37° C. in modified PETC media.
  • the modified PETC medium contains (per L) 1 g NH 4 Cl, 0.4 g KCl, 0.2 g MgSO 4 ⁇ 7H 2 O, 0.8 g NaCl, 0.1 g KH 2 PO 4 , 20 mg CaCl 2 ⁇ 2H 2 O, 10 ml trace elements solution (see below), 10 ml Wolfe's vitamin solution (see below), 2 g NaHCO 3 , and 1 mg resazurin. After the pH is adjusted to 5.6, the medium is boiled, dispensed anaerobically, and autoclaved at 121° C. for 15 min.
  • Steel mill waste gas composition: 44% CO, 32% N 2 , 22% CO 2 , 2% H 2
  • the media has a final pH of 5.9 and is reduced with Cystein-HCl and Na 2 S in a concentration of 0.008% (w/v).
  • the trace elements solution consists of 2 g nitrilotriacetic acid (adjusted to pH 6 with KOH before addition of the remaining ingredients), 1 g MnSO 4 , 0.8 g Fe(SO 4 ) 2 (NH 4 ) 2 ⁇ 6H 2 O, 0.2 g CoCl 2 ⁇ 6H 2 O, 0.2 mg ZnSO 4 ⁇ 7H 2 O, 20 mg CuCl 2 ⁇ 2H 2 O, 20 mg NiCl 2 ⁇ 6H 2 O, 20 mg Na 2 MoO 4 ⁇ 2H 2 O, 20 mg Na 2 SeO 4 , and 20 mg Na 2 WO 4 per liter.
  • Wolfe's vitamin solution (Wolin et al., 1963, J. Biol. Chem. 238:2882-2886) contains (per L) 2 mg biotin, 2 mg folic acid, 10 mg pyridoxine hydrochloride, 5 mg thiamine-HCl, 5 mg riboflavin, 5 mg nicotinic acid, 5 mg calcium D-(+)-pantothenate, 0.1 mg vitamin B12, 5 mg p-aminobenzoic acid, and 5 mg thioctic acid.
  • a 50 ml culture of C. autoethanogenum is subcultured to fresh media for 3 consecutive days. These cells are used to inoculate 50 ml PETC media containing 40 mM DL-threonine at an OD600 nm of 0.05. When the culture reaches an OD600 nm of 0.4, the cells are transferred into an anaerobic chamber and harvested at 4,700 ⁇ g and 4° C. The culture is twice washed with ice-cold electroporation buffer (270 mM sucrose, 1 mM MgCl 2 , 7 mM sodium phosphate, pH 7.4) and finally suspended in a volume of 600 ⁇ l fresh electroporation buffer.
  • ice-cold electroporation buffer 270 mM sucrose, 1 mM MgCl 2 , 7 mM sodium phosphate, pH 7.4
  • This mixture is transferred into a pre-cooled electroporation cuvette with a 0.4 cm electrode gap containing 1 ⁇ g of the methylated plasmid mix and immediately pulsed using the Gene pulser Xcell electroporation system (Bio-Rad) with the following settings: 2.5 kV, 600 ⁇ l, and 25 ⁇ F. Time constants of 3.7-4.0 ms are achieved.
  • the culture is transferred into 5 ml fresh media. Regeneration of the cells is monitored at a wavelength of 600 nm using a Spectronic Helios Epsilon Spectrophotometer (Thermo) equipped with a tube holder. After an initial drop in biomass, the cells start growing again.
  • the cells are harvested, suspended in 200 ⁇ l fresh media and plated on selective PETC plates (containing 1.2% BactoTM Agar (BD)) with 4 ⁇ g/ ⁇ l Clarithromycin. After 4-5 days of incubation with 30 psi steel mill gas at 37° C., 15-80 colonies per plate are clearly visible.
  • selective PETC plates containing 1.2% BactoTM Agar (BD)
  • the colonies are used to inoculate 2 ml PETC media containing 4 ⁇ g/ ⁇ l Clarithromycin. When growth occurs, the culture is upscaled into 5 ml and later 50 ml PETC media containing 4 ⁇ g/ ⁇ l Clarithromycin and 30 psi steel mill gas as sole carbon source.
  • a plasmid mini prep is performed from 10 ml culture volume using the QIAprep Spin Miniprep Kit (Qiagen).
  • the quality of the isolated plasmid DNA is sufficient to run a control PCR.
  • the PCR is performed with Illustra PuReTaq Ready-To-GoTM PCR Beads (GE Healthcare) using standard conditions (95° C. for 5 min; 32 cycles of 95° C. for 30 s, 50° C. for 30 s, and 72° C. for 1 min; 72° C. for 10 min).
  • 1 ⁇ l of each of the partly degraded isolated plasmids are re-transformed in E. coli XL1-Blue MRF′ Kan (Stratagene), from where the plasmids can be isolated cleanly and verified by restriction digests.
  • C. autoethanogenum does not have a native PHA pathway, hence no pathway genes need to be deleted.
  • phaA and phaB function must be introduced to the cells to provide the substrate for the crotonase enzyme.
  • Selected phaA (SEQ ID NO:77), phaB (SEQ ID NO:123), crotonase (SEQ ID NO:32), crotonyl-coA thioesterase (SEQ ID NO:29), and 4-oxalocrotonate decarboxylase (SEQ ID NO:10) sequences were codon optimized (see Table 7) and synthesized with appropriate promoters.
  • the genes are then cloned and transformed into C. autoethanogenum as described above. Transformation is confirmed by resistance of the cells to antibiotic selection, and gene expression is confirmed by northern blot (to confirm RNA transcription), western blot, or ELISA methods (to confirm protein expression).
  • C. ethanogenum transformed with the vector described above are used to inoculate 2 ml PETC media containing 4 ⁇ g/ ⁇ l Clarithromycin.
  • the culture is upscaled into 5 ml and later 50 ml PETC media containing 4 ⁇ g/ ⁇ l Clarithromycin and 30 psi steel mill gas as sole carbon source.
  • the bottles are then shaken continuously while being incubated at 37° C.
  • the headspace gas is refreshed every 2 days; however, immediately prior to refreshing the headspace, samples are drawn from both the liquid phase and headspace using a 10 ⁇ L Hamilton syringe and injected into a HP5890 GC equipped with a CP-PoraBOND U 25 m ⁇ 0.32 mm column and an FID maintained at 200° C.
  • the injector is connected in splitless mode and maintained at 250° C.
  • Samples are run with He Gas at 7.3 ml/min as a carrier gas; the oven program is set as follows: hold at 50° C. 1.5 min; ramp to 300° C. at 10° C./min; hold at 300° C. 10 min.
  • Propylene is identified by retention time compared to pure propylene diluted in air or dissolved in pure H 2 O. Samples are also taken to measure optical density of the culture, allowing quantitation of specific propylene production rates per cell. Note that because carbon monoxide is the only carbon source provided to the cells, all propylene produced must have been derived from
  • E. coli strains were transformed by electroporation using the appropriate plasmids. A single colony from a fresh transformation was then used to seed an overnight culture grown in Luria Broth (LB) supplemented with 1.5% (w/v) glucose and appropriate antibiotics at 37° C. in a rotary shaker (200 r.p.m.). Antibiotics were used at a concentration of 50 ⁇ g/ml for strains with a single resistance marker. For strains with multiple resistance markers, kanamycin and chloramphenicol were used at 25 ⁇ g/ml and carbenicillin was used at 50 ⁇ g/ml.
  • 4-OD genes were identified from BLAST searching of the NCBI database using the Pseudomonas putida 4-OD sequence as a starting sequence. 24 individual 4-OD proteins were chosen for expression studies. The proteins were reverse-translated and codon-optimized for E. coli using commercial methods (DNA2.0, Inc. Menlo Park, Calif.). The genes were then cloned under control of a T7 promoter and expressed in E. coli BL21 (DE3). Briefly, single colonies were inoculated into 2 mL cultures of LB containing 50 ⁇ g/mL kanamycin and shaken overnight at 37° C.
  • Lysates were generated by resuspending induced E. coli cell pellet (equivalent to 1 mL culture) in 0.5 mL lysis buffer (20 mM KHPO 4 pH 8.0; 0.3 M KCl; 10% (w/v) glycerol; 0.1% NP-40; 0.5 mg/ml lysozyme; 1 mM PMSF). Cells were sonicated 5 seconds and then centrifuged for 15 min at 15,000 ⁇ g, 4° C. The cleared supernatant was assayed immediately or stored at ⁇ 80° C. for later assay.
  • the assay buffer comprised 100 mM Tris-HCl pH 7.4; 3.3 mM MgSO 4 ; 1 mM 4-oxalocrotonate (the stock solution of 4-oxalocrotonate was pre-equilibrated with a 1:100 dilution of E. coli lysate expressing 4-oxalocrotonate tautomerase from Pseudomonas putida (UniProtKB/Swiss-Prot Accession No. Q01468, geneid 87856) to achieve a distribution of keto and enol forms of 4-oxalocrotonate).
  • Total reaction volume was 200 ⁇ l in a 96 well UV transparent plate and read on a SpectraMax Plate Reader (Molecular Devices). The reaction was initiated by addition of 4-OD containing lysates at 1:10 to 1:1000 final dilutions. Reactions were run at 25° C. Consumption of substrate was monitored by measuring drop in absorbance at 240 nm for the keto tautomer and at 300 nm for the enol tautomer (see FIG. 6 ).
  • the assay buffer comprised 100 mM Tris-HCl pH 7.4; 3.3 mM MgSO 4 ; 87.2 mM crotonic acid. Reactions were initiated by adding lysates to a final concentration of 1:10 to 1:100 in 1 ml volume in a TargetDP vial (2 ml total volume). Reactions were incubated from 12 to 72 hours at room temperature. Generated propylene was detected by injection of 0.5 ⁇ l aqueous phase plus 2 ⁇ l headspace gas onto a HP5890 GC equipped with a CP-PoraBOND U 25 m ⁇ 0.32 mm column and an FID maintained at 200° C. The injector was connected in splitless mode and maintained at 250° C.
  • Selected phaA (SEQ ID NO:77), phaB (SEQ ID NO:123), crotonase (SEQ ID NO:32), crotonyl-coA thioesterase (SEQ ID NO:29), and 4-oxalocrotonate decarboxylase (SEQ ID NO:10) sequences were codon optimized (see Table 8) and synthesized with appropriate promoters.
  • the genes are then cloned and transformed into E. coli strain BL21 (DE3). Transformation is confirmed by resistance of the cells to antibiotic selection, and gene expression is confirmed by northern blot (to confirm RNA transcription), western blot, or ELISA methods (to confirm protein expression).
  • Samples are drawn from both the liquid phase and headspace using a 10 ⁇ L Hamilton syringe and injected into a HP5890 GC equipped with a CP-PoraBOND U 25 m ⁇ 0.32 mm column and an FID maintained at 200° C.
  • the injector is connected in splitless mode and maintained at 250° C.
  • Samples are run with He Gas at 7.3 ml/min as a carrier gas; the oven program is set as follows: hold at 50° C. 1.5 min; ramp to 300° C. at 10° C./min; hold at 300° C. 10 min.
  • Propylene is identified by retention time compared to pure propylene diluted in air or dissolved in pure H 2 O. Samples are also taken to measure optical density of the culture, allowing quantitation of specific propylene production rates per cell.
  • the growth temperature is reduced to 30° C., and the culture flasks are sealed with butyl rubber stoppers to prevent propylene evaporation. Additional glucose (1% (w/v)) is added concurrent with culture sampling after 1 d. Flasks are unsealed for 10 to 30 min every 24 h then resealed after sampling. Samples are drawn from both the liquid phase and headspace using a 10 ⁇ L Hamilton syringe and injected into a HP5890 GC equipped with a CP-PoraBOND U 25 m ⁇ 0.32 mm column and an FID maintained at 200° C. The injector is connected in splitless mode and maintained at 250° C.
  • Samples are run with He Gas at 7.3 ml/min as a carrier gas; the oven program is set as follows: hold at 50° C. 1.5 min; ramp to 300° C. at 10° C./min; hold at 300° C. 10 min.
  • Propylene is identified by retention time compared to pure propylene diluted in air or dissolved in pure H 2 O. Samples are also taken to measure optical density of the culture, allowing quantitation of specific propylene production rates per cell.

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Abstract

The present disclosure relates to biosynthetic methods for producing propylene from C1 substrates (e.g., methane, methanol, carbon monoxide, syngas) and to genetically engineered organisms having propylene biosynthesis capability, as well as engineered organisms having a butyrate/butanol-producing pathway.

Description

    STATEMENT REGARDING SEQUENCE LISTING
  • The Sequence Listing associated with this application is provided in text format in lieu of a paper copy, and is hereby incorporated by reference into the specification. The name of the text file containing the Sequence Listing is 200206_403C1_SEQUENCE_LISTING.txt. The text file is 363 KB, was created on Jun. 28, 2017, and is being submitted electronically via EFS-Web.
    • BACKGROUND
  • Propylene is primarily produced as a by-product of petroleum refining and of ethylene production using a steam cracking process. Propylene is separated from a mixture of hydrocarbons obtained from cracking or other refining processes by fractional distillation. Propylene is typically produced from non-renewable fossil fuels, petroleum, natural gas, and to a lesser extent coal. Propylene can also be produced in on-purpose reactions, such as propane dehydrogenation, metathesis or syngas-to-olefins plants.
  • Propylene is a major industrial chemical intermediate that is converted into a variety of chemicals and plastics. Manufacturers of polypropylene account for nearly two thirds of worldwide propylene demand. Polypropylene is a plastic that is used for the manufacture of films, packaging, caps, closures, and individual parts for the electrical and automotive industry. Propylene is also used to produce chemicals including acrylonitrile, oxo chemicals, propylene oxide, cumene, isopropanol, acrylic acid, butanol, and butanediol.
  • Currently, refinery by-product production of propylene can no longer satisfy market demand. There is a need for alternative processes for on-purpose propylene production, particularly a green process that exhibits increased safety, decreased harmful waste and emissions, and savings in cost and energy compared to petrochemically-derived propylene.
    • SUMMARY
  • In one aspect, the present disclosure provides non-naturally occurring C1 metabolizing organisms, wherein the non-naturally occurring C1 metabolizing organisms convert a C1 substrate to propylene. In certain embodiments, the C1 metabolizing organism is: a non-naturally occurring C1 metabolizing bacterium; a non-naturally occurring obligate C1 metabolizing organism; a non-naturally occurring C1 metabolizing organism, wherein the non-naturally occurring C1 metabolizing organism does not include Pichia pastoris; a non-naturally occurring methanotrophic or methylotrophic bacterium; a non-naturally occurring syngas utilizing bacterium that naturally possesses the ability to utilize syngas; or a non-naturally occurring CO utilizing bacterium, wherein the non-naturally occurring CO utilizing bacterium naturally possesses the ability to utilize CO. In certain aspects, the non-naturally occurring C1 metabolizing organisms include an exogenous nucleic acid encoding an enzyme capable of decarboxylating crotonic acid (e.g., 4-oxalocrotonate decarboxylase). In further aspects, the non-naturally occurring C1 metabolizing organisms do not have a functional PHB synthase or a substantial amount of functional PHB synthase.
  • In another aspect, non-naturally occurring C1 metabolizing organisms include an exogenous nucleic acid encoding a crotonyl CoA thioesterase. The non-naturally occurring C1 metabolizing organism may be a non-naturally occurring C1 metabolizing bacterium; a non-naturally occurring obligate C1 metabolizing organism; a non-naturally occurring C1 metabolizing organism, wherein the C1 metabolizing organism does not include Pichia pastoris; a non-naturally occurring methanotrophic or methylotrophic bacterium; a non-naturally occurring syngas utilizing bacterium that naturally possesses the ability to utilize syngas;or a non-naturally occurring CO utilizing bacterium, wherein the non-naturally occurring CO utilizing bacterium naturally possesses the ability to utilize CO.
  • In yet another aspect, non-naturally occurring C1 metabolizing organisms include an exogenous nucleic acid encoding a crotonase. In certain embodiments, the non-naturally occurring C1 metabolizing organism is: a non-naturally occurring C1 metabolizing bacterium; a non-naturally occurring obligate C1 metabolizing organism; a non-naturally occurring C1 metabolizing organism, wherein the organism does not include Pichia pastoris; a non-naturally occurring methanotrophic or methylotrophic bacterium; a non-naturally occurring syngas utilizing bacterium that naturally possesses the ability to utilize syngas; or a non-naturally occurring CO utilizing bacterium, wherein the CO utilizing bacterium naturally possesses the ability to utilize CO.
  • In another aspect, the present disclosure provides non-naturally occurring microbial organisms, wherein the non-naturally occurring microbial organisms include an exogenous nucleic acid encoding 4-oxalocrotonate decarboxylase, and wherein the non-naturally occurring microbial organisms convert a carbon substrate to propylene. In certain embodiments, the non-naturally occurring microbial organisms further include an exogenous nucleic acid encoding crotonase, or an exogenous nucleic acid encoding crotonase and an exogenous nucleic acid encoding crotonyl thioesterase. In certain embodiments, the non-naturally occurring microbial organisms do not have a functional PHB synthase or a substantial amount of functional PHB synthase.
  • Also disclosed herein are methods of producing propylene in non-naturally occurring organisms described herein, wherein the methods comprise culturing the non-naturally occurring organisms under conditions sufficient to produce propylene.
    • BRIEF DESCRIPTION OF THE DRAWINGS
  • FIG. 1 shows an exemplary pathway for synthesis of propylene from acetyl CoA in a genetically modified organism. Enzymes and genes encoding enzymes for transformation of the identified substrates to products include: phaA, phaB, crotonase, crotonyl CoA thioesterase, and 4-oxalocrotonate decarboxylase.
  • FIGS. 2A-D show exemplary 4-oxalocrotonate decarboxylase (4-OD) amino acid sequences that may be used in propylene synthesis pathways as described herein.
  • FIG. 3 shows exemplary crotonyl-CoA thioesterase amino acid sequences that may be used in propylene synthesis pathways as described herein.
  • FIGS. 4A-E show exemplary crotonase amino acid sequences that may be used in propylene synthesis pathways as described herein.
  • FIG. 5 shows SDS-PAGE analysis of heterogeneously expressed 4-OD genes in E. coli. The first lane for each sample shows total cell protein and the second lane for each sample shows soluble protein following lysis and clarification. The arrow on the left shows the approximate migration of 4-OD proteins (note sequence variation causes slight changes in migration for each individual 4-OD sequence).
  • FIG. 6 shows sample 4-OD activity assays run under conditions as described showing decarboxylation of 4-oxalocrotonate.
  • FIG. 7 shows a sample chromatogram of propylene detected on a HP5890 GC-FID under the assay conditions as described.
    •  DETAILED DESCRIPTION
  • The instant disclosure provides compositions and methods for the biocatalysis of propylene and other desirable intermediates or products from methane or other C1 substrates using genetically engineered C1 metabolizing organisms. The instant disclosure also provides compositions and methods for the biocatalysis of propylene from carbon substrates using novel metabolic enzyme(s) in genetically engineered microbial organisms.
  • Prior to setting forth this disclosure in more detail, it may be helpful to an understanding thereof to provide definitions of certain terms to be used herein. Additional definitions are set forth throughout this disclosure.
  • In the present description, the term “about” means ±20% of the indicated range, value, or structure, unless otherwise indicated. The term “consisting essentially of” limits the scope of a claim to the specified materials or steps and those that do not materially affect the basic and novel characteristics of the claimed invention. It should be understood that the terms “a” and “an” as used herein refer to “one or more” of the enumerated components. The use of the alternative (e.g., “or”) should be understood to mean either one, both, or any combination thereof of the alternatives. As used herein, the terms “include” and “have” are used synonymously, which terms and variants thereof are intended to be construed as non-limiting. The term “comprise” means the presence of the stated features, integers, steps, or components as referred to in the claims, but that it does not preclude the presence or addition of one or more other features, integers, steps, components, or groups thereof.
  • As used herein, the term “non-naturally occurring” when used in reference to a bacterium or an organism means that the bacterium or organism has at least one genetic alternation that is not normally found in a naturally occurring strain of the referenced species, including wild-type strains of the referenced species. Genetic alterations include, for example, modifications introducing expressible nucleic acids encoding proteins or enzymes, other nucleic acid additions, nucleic acid deletions, nucleic acid substitutions, or other functional disruption of the bacterium or organism's genetic material. Such modifications include, for example, coding regions and functional fragments thereof for heterologous or homologous polypeptides for the referenced species. Additional modifications include, for example, non-coding regulatory regions in which the modifications alter expression of a gene or operon. Exemplary enzymes include enzymes within a crotonate synthesis pathway or propylene synthesis pathway. Genetic modifications to nucleic acid molecules encoding enzymes, or functional fragments thereof, can confer a biochemical reaction capability or a metabolic pathway capability to the non-naturally occurring organism that is altered from its naturally occurring state.
  • As used herein, the term “host” refers to a bacterium or organism that has not yet been genetically modified with the capability to convert a carbon substrate to crotonyl-CoA, crotonic acid, or propylene, as disclosed herein. A host C1 metabolizing bacterium or organism is selected for transformation with at least one exogenous nucleic acid encoding an enzyme to yield a non-naturally occurring C1 metabolizing bacterium or organism with the capability to convert a C1 substrate to crotonyl-CoA, crotonic acid, or propylene. A host microbial organism is selected for transformation with at least one exogenous nucleic acid encoding 4-oxalocrotonate decarboxylase to yield a non-naturally occurring microbial organism with the capability to convert a carbon substrate to propylene. A host bacterium or organism may already possess other genetic modifications conferring it with desired properties, unrelated to propylene synthesis pathways and intermediates disclosed herein. For example, a host bacterium or organism may possess genetic modifications conferring high growth, tolerance of contaminants or particular culture conditions, or ability to metabolize different carbon substrates.
  • As used herein, the term “microbial organism,” “microorganism”, “microbes”, or “organism” refers to any prokaryotic or eukaryotic microbial species from the domains of Archaea, Bacteria, or Eukarya. The term is intended to include prokaryotic or eukaryotic cells or organisms having microscopic size.
  • As used herein, the term “C1 metabolizing bacterium” refers to any bacterium that has the ability to oxidize a C1 compound (i.e., does not contain carbon-carbon bonds). A C1 metabolizing bacterium may or may not use other carbon substrates, such as sugars and complex carbohydrates, for energy and biomass.
  • As used herein, the term “obligate C1 metabolizing organism” refers to those organisms which exclusively use organic compounds that do not contain carbon-carbon bonds (C1 substrate) for the generation of energy.
  • As used herein, the term “C1 metabolizing organism” refers to any organism that has the ability to oxidize a C1 substrate (i.e., does not contain carbon-carbon bonds) but may or may not use other carbon substrates, such as sugars and complex carbohydrates, for energy and biomass. A C1 metabolizing organism includes bacteria, yeast (not including Pichia pastoris), and Archaea. A C1 metabolizing organism includes C1 metabolizing bacteria.
  • As used herein, the term “methanotrophic bacterium” refers to any methylotrophic bacterium that has the ability to oxidize methane as its primary carbon and energy source.
  • As used herein, the term “methylotrophic bacterium” refers to any bacterium capable of oxidizing organic compounds that do not contain carbon-carbon bonds. An “obligate methylotrophic bacterium” is a bacterium which is limited to the use of carbon substrates that do not contain carbon-carbon bonds for the generation of energy. Facultative methylotrophs are able to utilize multi-carbon compounds in addition to single carbon substrates.
  • As used herein, the term “CO utilizing bacterium” refers to a bacterium that naturally possesses the ability to oxidize carbon monoxide (CO) as a source of carbon and energy. Carbon monoxide may be utilized from “synthesis gas” or “syngas”, a mixture of carbon monoxide and hydrogen produced by gasification of any organic feedstock, including but not limited to coal, coal oil, natural gas, biomass, and waste organic matter. Syngas may also include CO2, methane, and other gases in smaller quantities. CO utilizing bacterium does not include bacteria that must be genetically modified for growth on CO as its carbon source.
  • As used herein, the term “C1 substrate” or “C1 compound” refers to any carbon containing molecule or composition that lacks a carbon-carbon bond. C1 substrates include methane, methanol, formaldehyde, formic acid (formate), carbon monoxide, carbon dioxide, methylated amines (methylamine, dimethylamine, trimethylamine, etc.), methylated thiols, methyl halogens (bromomethane, chloromethane, iodomethane, dichloromethane, etc.), or cyanide.
  • As used herein, the term “propylene”, also known as 1-propene, propene, or methylethylene, refers to an unsaturated organic compound having the chemical formula C3H6 and molecular mass of 42.08 g/mol. It has one double bond and is the second simplest member of the alkene class of hydrocarbons. Propylene is a gas at room temperature and atmospheric pressure. Propylene is a structural isomer of cyclopropane.
  • As used herein, “exogenous” means that the referenced molecule (e.g., nucleic acid) or referenced activity (e.g., enzyme activity) is introduced into the host bacterium or organism. The molecule can be introduced, for example, by introduction of a nucleic acid into the host genetic material such as by integration into a host chromosome or by introduction of a nucleic acid as non-chromosomal genetic material, such as on a plasmid. When the term is used in reference to expression of an encoding nucleic acid, it refers to introduction of the encoding nucleic acid in an expressible form into the bacterium or organism. When used in reference to an enzymatic activity, the term refers to an activity that is introduced into the host reference bacterium or organism. Therefore, the term “endogenous” or “native” refers to a referenced molecule or activity that is present in the host bacterium or organism. The term “heterologous” refers to a molecule or activity that is derived from a source other than the referenced species or strain whereas “homologous” refers to a molecule or activity derived from the host bacterium or organism. Accordingly, a bacterium or organism comprising an exogenous nucleic acid of the invention can utilize either or both a heterologous or homologous nucleic acid.
  • It is understood that when more than one exogenous nucleic acid is included in a bacterium or organism that the more than one exogenous nucleic acid refers to the referenced encoding nucleic acid or enzymatic activity, as discussed above. It is also understood, as disclosed herein, that such more than one exogenous nucleic acids can be introduced into the host bacterium or organism on separate nucleic acid molecules, on a polycistronic nucleic acid molecule, on a single nucleic acid molecule encoding a fusion protein, or a combination thereof, and still be considered as more than one exogenous nucleic acid. For example, as disclosed herein, an organism can be modified to express two or more exogenous nucleic acids encoding a desired pathway enzyme or protein (e.g., propylene pathway enzyme or protein). Where two exogenous nucleic acids encoding propylene synthesis activity are introduced into a host organism, it is understood that the two exogenous nucleic acids can be introduced as a single nucleic acid molecule, for example, on a single plasmid, on separate plasmids, can be integrated into the host chromosome at a single site or multiple sites, and still be considered two exogenous nucleic acids. Similarly, it is understood that more than two exogenous nucleic acids can be introduced into a host organism in any desired combination, for example, on a single plasmid, on separate plasmids, can be integrated into the host chromosome at a single site or multiple sites, and still be considered as two or more exogenous nucleic acids. Thus, the number of referenced exogenous nucleic acids or enzymatic activities refers to the number of encoding nucleic acids or the number of enzymatic activities, not the number of separate nucleic acid molecules introduced into the host organism.
  • As used herein, “nucleic acid” refers to a polymeric compound comprised of covalently linked subunits called nucleotides. Nucleic acids include polyribonucleic acid (RNA), polydeoxyribonucleic acid (DNA), both of which may be single or double stranded. DNA includes cDNA, genomic DNA, synthetic DNA, and semi-synthetic DNA.
  • As used herein, “crotonic acid” or “trans-2-butenoic acid” refers to a short-chain unsaturated carboxylic acid with the formula CH3CH═CHCO2H. As used herein, crotonic acid includes “crotonate”, a salt or ester of crotonic acid.
  • As used herein, “4-oxalocrotonate” refers to an unsaturated carboxylic acid with the formula HO2C(C═O)CH2CH═CHCO2— (keto form) or HO2C(COH)═CHCH═CHCO2— (enol form), which interconvert spontaneously. As used herein, 4-oxalocrotonate also includes salts or esters, the equivalent molecule with the alternate acid group deprotonated, the doubly unprotonated basic form of the molecule, or the doubly protonated acid form of the molecule.
  • As used herein, “4-oxalocrotonate decarboxylase” or “4-OD” or “4-oxalocrotonate carboxy-lase (2-oxopent-4-enoate-forming)” refers to an enzyme family that catalyzes the decarboxylation of 4-oxalocrotonate to 2-oxopent-4-enoate and CO2. 4-OD is involved in the meta-cleavage pathway for the degradation of phenols, modified phenols, and catechols. As disclosed herein, 4-OD is used to catalyze the decarboxylation of crotonic acid to propylene and CO2. As used herein, 4-OD also encompasses mutants or variants of a native 4-OD enzyme that has reduced or eliminated decarboxylation activity on 4-oxalocrotonate, but retains or has increased decarboxylation activity on crotonic acid as a substrate. 4-OD also refers to any enzyme capable of catalyzing the decarboxylation of crotonic acid to propylene and CO2.
  • As used herein, “crotonyl CoA thioesterase” refers to an enzyme that catalyzes the conversion of crotonyl-CoA to crotonic acid.
  • As used herein, “crotonase” or “3-hydroxybutyryl-CoA dehydratase” or “enoyl-CoA hydratase” refers to an enzyme involved in the butyrate/butanol-producing pathway, which catalyzes the dehydration of 3-hydroxybutyryl-CoA to crotonyl-CoA.
  • As used herein, “β-ketothiolase” refers to an enzyme in the PHB synthesis pathway that catalyzes the condensation of two acetyl-CoA molecules to acetoacetyl-CoA. Biosynthesis of PHB in most bacteria is initiated by β-ketothiolase.
  • As used herein, “acetoacetyl coenzyme A reductase” refers to an enzyme in the PHB synthesis pathway that catalyzes the reduction of acetoacetyl-CoA to 3-hydroxybutyryl-CoA.
  • As used herein, “PHB synthase”, also known as “PHB polymerase”, refers to an enzyme in the PHB synthesis pathway that converts a hydroxybutyryl-CoA monomer into polyhydroxybutyrate.
  • As used herein, “polyhydroxybutyrate” or “PHB” refers to a homopolymer of hydroxybutyric acid units. PHB is a type of polyhydroxyalkanoate (PHA), which is a biological polyester. Polyhydroxybutyrate is a crystalline thermoplastic synthesized by a broad range of bacteria as a form of energy storage molecule. Poly-3-hydroxybutyrate (P3HB) form is the most common type of PHB, but other PHBs include poly-4-hydroxybutytrate (P4HB), poly(3-hydroxybutyrate-co-4-hydroxybutyrate) (P3HB-co-4HB), or other copolymers.
    • C1 Metabolizing Bacteria or Organisms
  • A variety of C1 metabolizing host organisms can be transformed or genetically engineered to produce a product of interest (e.g., propylene, crotonic acid, or crotonyl-CoA).
  • In certain embodiments, a C1 metabolizing organism may be a C1 metabolizing bacterium, which refers to any bacterium that has the ability to oxidize a C1 compound. A C1 metabolizing bacterium may also use other carbon substrates, such as sugars and complex carbohydrates, for energy and biomass. A C1 metabolizing bacterium includes methanotrophic bacteria (methylotrophic bacterium that has the ability to oxidize methane as an energy source) or methylotrophic bacteria (any bacterium capable of oxidizing organic compounds that do not contain carbon-carbon bonds). Methanotrophic bacteria are classified into three groups based on their carbon assimilation pathways and internal membrane structure: type I (gamma proteobacteria), type II (alpha proteobacteria, and type X (gamma proteobacteria). Type I methanotrophs use the ribulose monophosphate (RuMP) pathway for carbon assimilation whereas type II methanotrophs use the serine pathway. Type X methanotrophs use the RuMP pathway but also express low levels of enzymes of the serine pathway. Methanotrophic bacteria are grouped into several genera: Methylomonas, Methylobacter, Methylococcus, Methylocystis, Methylosinus, Methylomicrobium, Methanomonas, and Methylocella. Exemplary methantrophic bacteria include: Methylococcus capsulatus Bath strain, Methylomonas 16a (ATCC PTA 2402), Methylosinus trichosporium OB3b (NRRL B-11,196), Methylosinus sporium (NRRL B-11,197), Methylocystis parvus (NRRL B-11,198), Methylomonas methanica (NRRL B-11,199), Methylomonas albus (NRRL B-11,200), Methylobacter capsulatus (NRRL B-11,201), Methylobacterium organophilum (ATCC 27,886), Methylomonas sp AJ-3670 (FERM P-2400), Methylocella silvestris, Methylocella palustris (ATCC 700799), Methylocella tundrae, Methylacidiphilum infernorum, Methylibium petroleiphilum, and Methylomicrobium alcaliphilum. Methylotrophic bacteria encompass a diverse group, including both gram-negative and gram-positive genera. Methylotrophic bacteria include facultative methylotrophs (have the ability to oxidize organic compounds which do not contain carbon-carbon bonds, but may also utilize other carbon substrates such as sugars and complex carbohydrates), obligate methylotrophs (limited to the use of organic compounds that do not contain carbon-carbon bonds), and methanotrophic bacteria. Examples of methylotrophic genera include: Methylophilus, Methylobacillus, Methylobacterium, Hyphomicrobium, Xanthobacter, Bacillus, Paracoccus, Nocardia, Arthrobacter, Rhodopseudomonas, and Pseudomonas. Exemplary methylotrophic bacteria include: Methylobacterium extorquens, Methylobacterium radiotolerans, Methylobacterium populi, Methylobacterium chloromethanicum, Methylobacterium nodulans, Methylomonas clara, Methylibium petroleiphilum, Methylobacillus flagellates, Silicibacter pomeroyi DSS-3, Burkholderia phymatum STM815, Granulibacter bethesdensis NIH1.1, and Paracoccus denitrificans.
  • A C1 metabolizing bacterium includes bacteria that utilize formate or cyanide or naturally possesses the ability to utilize syngas or carbon monoxide (CO) (Wu et al., PLoS Genet. 1:e65, 2005; Abrini et al., Arch. Microbiol. 161:345, 1994; WO 2008/028055; Tanner et al., Int. J. Syst. Bacteriol. 43:232-236, 1993). Exemplary bacteria that naturally possesses the ability to utilize CO or syngas include Clostridium autoethanogenum, Clostridium ljungdahli, Clostridium ragsdalei, Clostridium carboxydivorans, Butyribacterium methylotrophicum, Clostridium woodii, Clostridium neopropanologen, Pseudomonas carboxidovorans, Rhodospirillum rubrum, Thermincola carboxydiphila, Thermincola potens, Thermoanaerobacter thermohydrosulfuricus, Ralstonia eutropha, and Eurobacterium limosum. A C1 metabolizing bacterium also includes bacteria that can cleave methyl groups from organic compounds, including choline (de Vries et al., FEMS Microbiol. Rev. 6:57-101, 1990) or the pesticide carbofuran (Topp et al., Appl. Environ. Microbiol. 59:3339-3349, 1993), and utilize them as a sole source of carbon.
  • C1 metabolizing organisms include bacteria, yeast (not including Pichia pastoris), and Archaea. A C1 metabolizing organism may be obligate or facultative. Examples of C1 metabolizing organisms include: Methylomonas, Methylobacter, Methylococcus, Methylosinus, Methylocystis, Methylomicrobium, Methanomonas, Methylophilus, Methylobacillus, Methylobacterium, Hyphomicrobium, Xanthobacter, Bacillus, Paracoccus, Nocardia, Arthrobacter, Rhodopseudomonas, Pseudomonas, Candida, Yarrowia, Hansenula, Pichia (not including Pichia pastoris), Torulopsis, and Rhodotorula. Additional examples of C1 (carbon monoxide) metabolizing organisms include: Clostridium autoethanogenum, Clostridium ljungdahli, Clostridium ragsdalei, Clostridium carboxydivorans, Butyribacterium methylotrophicum, Clostridium Woodii, and Clostridium neopropanologen.
  • A variety of C1 substrates may be used by the C1 metabolizing organisms. It is understood to one of skill in the art that selection of a C1 substrate may be determined by which host organism is selected. For example, obligate methanotrophic bacteria are limited to the use of methane as a carbon source, whereas some methylotrophic bacteria may use a variety of C1 compounds, such as methane, methanol, methylated amines, halomethanes, and methylated compounds containing sulfur (reviewed in Hanson and Hanson, 1996, Microbiological Rev. 60:439-471). Non-limiting examples of C1 substrates include: methane, methanol, formaldehyde, formic acid (formate), carbon monoxide, carbon dioxide, methylated amines (methylamine, dimethylamine, trimethylamine, etc.), methylated thiols, or methyl halogens (bromomethane, chloromethane, iodomethane, dichloromethane, etc.). Some facultative methanotrophs and facultative methylotrophs can also grow on multi-carbon compounds. A C1 metabolizing organism may also be adapted or genetically modified to use a different C1 substrate in addition to, or instead of its usual C1 substrate. Alternatively, a C1 metabolizing organism may be adapted or genetically modified to use a multi-carbon substrate in addition to its usual C1 substrate. A selected C1 metabolizing organism may also undergo strain adaptation under selective conditions to identify variants with improved properties for production. Improved properties may include increased growth rate, yield of desired products (e.g., propylene), and tolerance of likely process contaminants. In a particular embodiment, a high growth variant C1 metabolizing organism, which is an organism capable of growth on a C1 substrate as the sole carbon and energy source and which possesses an exponential phase growth rate that is faster (i.e., shorter doubling time) than its parent, reference, or wild-type organism, is selected ((see, e.g., U.S. Pat. No. 6,689,601).
  • Each of the organisms of this disclosure may be grown as an isolated culture, with a heterologous organism that may aid in growth, or one or more of C1 metabolizing bacteria may be combined to generate a mixed culture.
    • Microbial Organisms
  • A variety of microbial host organisms can be transformed or genetically engineered to include a novel metabolic pathway and associated enzymes as described herein to produce propylene from a carbon substrate. Exemplary bacteria include Escherichia coli, Klebsiella oxytoca, Anaerobiospirillum succiniciproducens, Actinobacillus succinogenes, Mannheimia succiniciproducens, Rhizobium etli, Bacillus subtilis, Corynebacterium glutamicum, Gluconobacter oxydans, Zymomonas mobilis, Lactococcus lactis, Lactobacillus plantarum, Streptomyces coelicolor, Clostridium acetobutylicum, Pseudomonas fluorescens, and Pseudomonas putida. Exemplary yeasts or fungi species include Saccharomyces cerevisiae, Schizosaccharomyces pombe, Kluyveromyces lactis, Kluyveromyces marxianus, Aspergillus terreus, Aspergillus niger, Rhizopus arrhizus, Rhizobus oryzae, and Yarrowia lipolytica. It is understood that any suitable microbial host organism can be used to introduce suitable genetic modifications (e.g., nucleic acid encoding 4-OD) to produce propylene.
    • Non-Naturally Occurring Organisms
  • Non-naturally occurring organisms as described herein can be produced by introducing expressible nucleic acid(s) encoding one or more enzymes involved in a desired biosynthetic pathway (e.g., propylene synthesis). Depending on the host organism selected for biosynthesis, nucleic acid(s) for one, some, or all of a particular biosynthetic pathway can be expressed. For example, if a selected host is deficient in one or more enzymes for a desired biosynthetic pathway (e.g., propylene synthesis), then expressible nucleic acid(s) for the deficient enzyme(s) are introduced into the host for subsequent exogenous expression. Alternatively, if a selected host exhibits endogenous expression of some pathway genes, but is deficient in others, then an encoding nucleic acid is needed for the deficient enzyme(s) to achieve the desired biosynthesis. Thus, non-naturally occurring organisms of the invention can be produced by introduced exogenous enzyme activities to obtain a desired biosynthetic pathway or a desired biosynthetic pathway can be obtained by introducing one or more exogenous enzyme activities that, together with one or more endogenous enzymes, produces the desired product, such as propylene. In some embodiments, non-naturally occurring organisms as described herein can also include other genetic modifications that facilitate or optimize a desired biosynthetic pathway or that confer other useful functions onto the host. For example, if a selected host exhibits endogenous expression of an enzyme that inhibits propylene biosynthetic pathway, then the host may be genetically modified so that it does not produce a functional enzyme or a substantial amount of a functional enzyme.
  • In certain embodiments, the present disclosure provides a non-naturally occurring C1 metabolizing bacterium; a non-naturally occurring obligate C1 metabolizing organism; a non-naturally occurring C1 metabolizing organism, wherein the non-naturally occurring C1 metabolizing organism does not include Pichia pastoris; a non-naturally occurring methanotrophic or methylotrophic bacterium; or a non-naturally occurring CO utilizing bacterium, wherein the non-naturally occurring CO utilizing bacterium naturally possesses the ability to utilize CO, wherein the non-naturally occurring C1 metabolizing bacterium or organism converts a C1 substrate to propylene.
  • In certain embodiments, the present disclosure provides a non-naturally occurring C1 metabolizing organism that is not Pichia pastoris and is capable of converting a C1 substrate into propylene. In certain embodiments, the non-naturally occurring C1 metabolizing organism is not Pichia pastoris and is a C1 metabolizing bacterium capable of converting a C1 substrate into propylene.
  • In certain embodiments, the non-naturally occurring C1 metabolizing organism is an obligate C1 metabolizing organism capable of converting a C1 substrate into propylene. In certain embodiments, the obligate C1 metabolizing organism is a C1 metabolizing bacterium, such as a methanotrophic or methylotrophic bacterium capable of converting a C1 substrate into propylene. In further embodiments, a C1 metabolizing bacterium may be a syngas utilizing bacterium that naturally possesses the ability to use syngas and convert a C1 substrate in the syngas into propylene. In still further embodiments, a C1 metabolizing bacterium is a CO utilizing bacterium that naturally possesses the ability to use CO and convert the CO into propylene.
  • In certain embodiments, any of the non-naturally occurring C1 metabolizing organisms as described herein includes an exogenous nucleic acid encoding an enzyme capable of decarboxylating crotonic acid. The exogenous nucleic acid encoding an enzyme capable of decarboxylating crotonic acid is expressed in a sufficient amount to produce propylene.
  • In further embodiments, the exogenous nucleic acid encoding an enzyme capable of decarboxylating crotonic acid encodes 4-oxalocrotonate decarboxylase (4-OD). 4-OD is an enzyme that catalyzes the decarboxylation of 4-oxalocrotonate to 2-oxopent-4-enoate and CO2. 4-OD is involved in the meta-cleavage pathway for the degradation of phenols, modified phenols, and catechols. As disclosed herein, an exogenous nucleic acid encoding 4-OD is used to genetically engineer a novel propylene biosynthesis pathway in a non-naturally occurring organisms; 4-OD is used to catalyze decarboxylation of crotonic acid to propylene and CO2 (see FIG. 1). Sources of 4-OD encoding nucleic acid molecules may include any species, prokaryotic or eukaryotic, where the encoded gene product is capable of catalyzing decarboxylation of crotonic acid to propylene and CO2. Exemplary amino acid sequences of 4-OD are shown in FIGS. 2A-D.
  • Non-naturally occurring C1 metabolizing organisms that have an exogenous nucleic acid encoding an enzyme capable of decarboxylating crotonic acid (e.g., 4-OD) may also include one or more exogenous nucleic acids to confer a propylene biosynthetic pathway onto the C1 metabolizing organism. For example, depending on which C1 metabolizing host organism is selected, one or more exogenous nucleic acids may need to be introduced into the C1 metabolizing organism along with 4-OD in order to provide a non-naturally occurring C1 metabolizing organism with the ability to produce crotonic acid, the substrate for propylene conversion by 4-OD. In certain embodiments, a non-naturally occurring C1 metabolizing organism that has an exogenous nucleic acid encoding an enzyme capable of decarboxylating crotonic acid (e.g., 4-OD) may further include an exogenous nucleic acid encoding crotonase and/or an exogenous nucleic acid encoding a crotonyl-CoA thioesterase. An exogenous nucleic acid encoding crotonase and an exogenous nucleic acid encoding crotonyl-CoA thioesterase are expressed in a sufficient amount to produce propylene. In a specific example, a type II methanotrophic bacterium, which possesses an endogenous PHB synthesis pathway and produces 3-hydyroxybutyryl-CoA, an intermediate in the PHB synthesis pathway, may comprise exogenous nucleic acids encoding a crotonase and/or a crotonyl-CoA thioesterase in addition to 4-OD (see FIG. 1). Crotonase and crotonyl-CoA thioesterase are provided to catalyze the dehydration of 3-hydroxybutyryl-CoA to crotonyl-CoA and conversion of crotonyl-CoA to crotonic acid, respectively. It is understood that any combination of one or more enzymes that can be used to engineer a propylene biosynthesis pathway can be included in a non-naturally occurring C1 metabolizing organism of the invention.
  • In certain embodiments, the present disclosure provides a non-naturally occurring C1 metabolizing bacterium; a non-naturally occurring obligate C1 metabolizing organism; a non-naturally occurring C1 metabolizing organism, wherein the non-naturally occurring C1 metabolizing organism does not include Pichia pastoris; a non-naturally occurring methanotrophic or methylotrophic bacterium; or a non-naturally occurring CO utilizing bacterium, wherein the non-naturally occurring CO utilizing bacterium naturally possesses the ability to utilize CO, wherein the non-naturally occurring C1 metabolizing bacterium or organism comprises an exogenous nucleic acid encoding a crotonyl-CoA thioesterase.
  • In certain embodiments, the present disclosure provides a non-naturally occurring C1 metabolizing organism that is not Pichia pastoris and includes an exogenous nucleic acid molecule encoding a crotonyl CoA thioesterase. In further embodiments, a non-naturally occurring C1 metabolizing organism that is not Pichia pastoris, may be an obligate C1 metabolizing organism containing an exogenous nucleic acid molecule encoding a crotonyl CoA thioesterase. In still further embodiments, the C1 metabolizing organism may be a C1 metabolizing bacterium or an obligate C1 metabolizing bacterium containing an exogenous nucleic acid molecule encoding a crotonyl CoA thioesterase. In some embodiments, a C1 metabolizing bacterium is a methanotrophic or methylotrophic bacterium containing an exogenous nucleic acid molecule encoding a crotonyl CoA thioesterase. In certain embodiments, a C1 metabolizing bacterium may be a syngas utilizing bacterium that naturally possesses the ability to use syngas and contains an exogenous nucleic acid molecule encoding a crotonyl CoA thioesterase. In some embodiments, a C1 metabolizing bacterium may be a CO utilizing bacterium that naturally possesses the ability to use CO and contains an exogenous nucleic acid molecule encoding a crotonyl CoA thioesterase.
  • Crotonyl-CoA thioesterase refers to an enzyme that catalyzes the conversion of crotonyl-CoA to crotonic acid. Sources of crotonyl-CoA thioesterase encoding nucleic acids may include any species, prokaryotic or eukaryotic, where the encoded gene product is capable of catalyzing the conversion of crotonyl-CoA to crotonic acid. Exemplary amino acid sequences for crotonyl-CoA thioesterase are shown in FIG. 3. Crotonic acid is an intermediate in the engineered propylene biosynthetic pathway disclosed herein and is a useful product in itself for the preparation of polyvinyl acetate copolymers, a synthetic butyl rubber softener, a variety of resins, fungicides, pharmaceutical intermediates, plasticizers, cosmetic polymers for hair care, and adhesives. Reduction of crotonic acid yields crotonaldehyde. Key products made from crotonaldehyde are sorbic acid, potassium sorbate (a preservative), and trimethylhydroquinone (an intermediate used in Vitamin E manufacture).
  • In certain embodiments, the present disclosure provides a non-naturally occurring C1 metabolizing bacterium; a non-naturally occurring obligate C1 metabolizing organism; a non-naturally occurring C1 metabolizing organism, wherein the non-naturally occurring C1 metabolizing organism does not include Pichia pastoris; a non-naturally occurring methanotrophic or methylotrophic bacterium; or a non-naturally occurring CO utilizing bacterium, wherein the non-naturally occurring CO utilizing bacterium naturally possesses the ability to utilize CO, wherein any of the aforementioned non-naturally occurring C1 metabolizing bacterium or organism includes an exogenous nucleic acid encoding a crotonase.
  • In certain embodiments, the present disclosure provides a non-naturally occurring C1 metabolizing organism that is not Pichia pastoris and includes an exogenous nucleic acid molecule encoding a crotonase. In certain embodiments, the non-naturally occurring C1 metabolizing organism that is not Pichia pastoris is a C1 metabolizing bacterium containing an exogenous nucleic acid molecule encoding a crotonase, such as a methanotrophic or methylotrophic bacterium. In some embodiments, a C1 metabolizing bacterium is a syngas utilizing bacterium that naturally possesses the ability to use syngas and contains an exogenous nucleic acid molecule encoding a crotonase. In some embodiments, a C1 metabolizing bacterium is a CO utilizing bacterium that naturally possesses the ability to use CO and contains an exogenous nucleic acid molecule encoding a crotonase. In further embodiments, a non-naturally occurring C1 metabolizing organism is an obligate C1 metabolizing organism containing an exogenous nucleic acid molecule encoding a crotonase, such as an obligate C1 metabolizing bacterium.
  • Crotonase, also known as 3-hydroxybutyryl-CoA dehydratase, is an enzyme involved in the butyrate/butanol-producing pathway. Crotonase catalyzes the dehydration of 3-hydyroxybutyryl-CoA to crotonyl-CoA. 3-hydroxybutyryl-CoA can be an R or S stereoisomer. Enzymes that produce and convert 3-hydroxybutyryl-CoA have defined stereospecificity preferences. Sources of crotonase encoding nucleic acids may include any species, prokaryotic or eukaryotic, where the encoded gene product is capable of catalyzing dehydration of 3-hydyroxybutyryl-CoA to crotonyl-CoA. Exemplary amino acid sequences for crotonase are shown in FIGS. 4A-E. Crotonyl-CoA is a useful intermediate that can be a substrate for an engineered propylene biosynthetic pathway (via conversion to crotonic acid by crotonyl-CoA thioesterase, which is then converted to propylene by 4-OD) or an engineered butanol/butyraldehyde biosynthetic pathway (via conversion to butyryl-CoA by butyryl-CoA dehydrogenase, which is then converted to butanol or butyraldehyde by bi-functional aldehyde dehydrogenase) (see FIG. 1).
  • In certain embodiments, the invention provides for a non-naturally occurring C1 metabolizing bacterium; a non-naturally occurring obligate C1 metabolizing organism; a non-naturally occurring C1 metabolizing organism, wherein the non-naturally occurring C1 metabolizing organism does not include Pichia pastoris; a non-naturally occurring methanotrophic or methylotrophic bacterium; or a non-naturally occurring CO utilizing bacterium, wherein the non-naturally occurring CO utilizing bacterium naturally possesses the ability to utilize CO; wherein the non-naturally occurring C1 metabolizing bacterium or organism converts a C1 substrate to propylene, and further wherein the non-naturally occurring C1 metabolizing bacterium or organism does not have a functional PHB synthase or a substantial amount of a functional PHB synthase.
  • In certain embodiments, a non-naturally occurring C1 metabolizing organism according to any of the embodiments disclosed herein is a C1 metabolizing bacterium that does not have a functional PHB synthase or a substantial amount of functional PHB synthase.
  • PHB synthase is a polyhydroxybutyrate synthesis pathway enzyme that converts hydroxybutyryl-CoA monomers into polyhydroxybutyrate (PHB) (see FIG. 1). Many prokaryotes synthesize PHB as a carbon and energy storage material. Some yeast and other eukaryotic cells may contain small amounts of low molecular mass PHBs. Two PHB synthesis pathways are known in bacteria. In one pathway, PHB is synthesized from acetyl-CoA as a result of sequential action of three enzymes: β-ketothiolase, acetoacetyl-CoA reductase, and PHB synthase (e.g., Methylobacterium extorquens, Methylosinus trichosporium OB3b, Methylocystis and Methylosinus species). PHB synthesis can also be synthesized by: β-ketothiolase, acetocetyl-CoA reductase, crotonyl-CoA hydratases (crotonases), and PHB synthase (e.g., Methylobacterium rhodesianum) (see, e.g., Mothes et al., Arch. Microbiol. 161:277-280, 1994; Mothes et al., Can. J. Microbiol. 41:68-72, 1995). Generally, Type II methanotrophs accumulate PHB, whereas type I methanotrophs do not. As used herein, “not having a functional PHB synthase” means that its gene expression or protein activity has been reduced to undetectable levels. Reducing gene expression or protein activity of PHB synthase may be accomplished by deletion of some or all of the gene's coding sequence, introduction of one or more nucleotides into the gene's open reading frame resulting in translation of a nonsense or non-functional protein product, expressing interfering RNA or antisense sequences that target the gene, or other methods known in the art. As used herein, “not having a substantial amount of a functional PHB synthase” means that an organism has at least 40%, 45%, 50%, 55%, 60%, 65%, 70%, 75%, 80%, 85%, 90%, 95%, or 99% less gene expression or protein activity of PHB synthase as compared to a wild type organism that has a polyhydroxybutyrate synthesis pathway.
  • In a specific embodiment, PHB synthase is encoded by phaC or phbC. Exemplary PHB synthase amino acid sequences are provided in Table 1. In another specific embodiment, a non-naturally occurring C1 metabolizing organism that is capable of converting a C1 substrate to propylene as disclosed herein does not produce a substantial amount of polyhydroxybutryate. As used herein, “not producing a substantial amount of polyhydroxybutyrate” means that an organism produces at least 40%, 45%, 50%, 55%, 60%, 65%, 70%, 75%, 80%, 85%, 90%, 95%, or 99% less polyhydroxybutyrate as compared to a wildtype organism that has a polyhydroxybutyrate synthesis pathway. By knocking out PHB function in C1 metabolizing organisms with an endogenous PHB synthesis pathway through genetic modification (e.g., allelic exchange of phaC or phbC with non-functional gene), PHB production may be inhibited, allowing more 3-hydroxybutyryl-CoA to be funneled into conversion to crotonyl-CoA by crotonase (see FIG. 1). Alternatively, a C1 metabolizing organism, which is not naturally capable of PHB synthesis, may be genetically modified to possess a portion of the PHB synthesis pathway (e.g., β-ketothiolase and acetoacetyl-CoA reducatase), while excluding PHB synthase functionality. Increased amounts of crotonyl-CoA, which is converted to crotonic acid and then to propylene via crotonyl-CoA thioesterase and 4-OD, respectively, may result in increased propylene yields.
  • TABLE 1
    Exemplary PHB Synthase Sequences
    Genbank
    Accession # Gene Name Amino Acid Sequence (SEQ ID NO: #)
    gi|53719168 poly-beta- MQQLFESWLGAWRSFADPARAAAGDAPSPSPSPFAAFQPPQPFAFAMPAMPPMPDWS
    hydroxybutyrate GAAASFAGLAPVASVPPARLQKLQADYSRDCLALIQQASAATPTVPELKDRRFSADAWKASP
    polymerase AHGFAAAWYLLNARYLQELADALETDPKTRERIRFTVQQWTAAASPSNFLALNPEAQKNLV
    [Burkholderia ETQGESLRLGMMNLLADMQRGKISQTDESQFVVGKNLAVTPGAVVYENDLIQLIQYTPTTA
    pseudomallei TVFERPLLIVPPCINKFYILDLQPENSLVAHALSCGHQVFLVSWRNADASVAHKTWDDYIDEG
    K96243] LLAAIDVVQQVSGREQINTLGFCVGGTMLATALAVLAARGEHPAASMTLLTSMLDFSDTGIL
    DVFVDEAHVQMREQTIGGKGGAPAGLMRGVEFANTFSFLRPNDLVWNYVVDNYLKGRTP
    APFDLLYWNGDSTSLPGPMYAWYLRNTYLENKLREPDALTVCGEPVDLSRIDVPTFIYGSRED
    HIVPWQTAYASTSLLTGPLKFVLGASGHIAGVINPPAKRKRSYWSYDASAKELPESANDWLD
    AAVEHPGSWWPVWIEWLDQYGGKKVKPRAHLGCARFPVIEPAPGRYVLQRD (SEQ ID
    NO: 54)
    gi|296445329 poly(R)- MTAGRRSTAGAKRRPPHLRDAAETKLVVEEPPPAENADVSLLEAPRVNGARVAAAAPAQKK
    hydroxyalkanoic KTGKVRAKPRAPVQEPPVQEPPVREPTAEAPREAMIAIATPPAAPTAEERRLELQAAAALVA
    acid GAAAELTEAQRRSLMGQLQALEPAPPAPAPVLTPAAPPEIPAAPQRKPARDYQAGAAESTA
    synthase, HDFEIIAENLARLVDQGRKALAAAVGGMEPGDTRSELASNVADATKTLGAVAERWMAKPE
    class I QAVAAQADLLTGLSAIWSQTLRRFSGADVPPVVPADPSDKRFSAPEWRDNPFFDCLRQSYA
    [Methylosinus LTTHWASEAVERTDGLDPQTKSKAAFYTRLIASALSPSNFVATNPELLRATLDARGENLVRG
    trichosporium MKMLTEDLSAGRGMLKLRQSDESKFELGVDMASTPGKVVYRTPVMELIQYAPSTETVYERP
    OB3b] LLIVPPWINKFYVLDLNREKSFVRWATGKGLTVFVVSWVNPDESQADKGFDAYMKEGVLAA
    LDAVQKATGAPHVAAAGYCVGGTMLAATLAYLAEKGDDRIDSVTFLATQVDFTDAGDMQ
    VFIDEARLAALDEAMSRTGYLEGVKMATTFNMLRPNELFWTYFVNNYMKGVEPAAFDLLT
    WNSDCTRIPRANHLFYLRYCYIENALSQGRMVIDGVTLNLRKVKIPIYELAAKEDHIAPARSVF
    TGAKYFGGEVRYVLAGAGHIAGVVNPPDKHKYQYWTGGPPMGAYEDWVKAAKESKGSW
    WDDWHDWITSQAPEQVAARIPGEGGLKALCDAPGDYVRVRA (SEQ ID NO: 55)
    gi|296445763 Poly-beta- MVVVDFAGRAGRLQEPAAEASPNPPAPVEEPPRRAYPIGEVPSFDTLDRAARAVAARFTQG
    hydroxybutyrate VSPLAQMSAWLDFATHLALAPGRQIELGLAAAQSAAALAYFSAETLAGRAEAGPFVSEPHD
    polymerase RRFVDPGWDAPPFSLWKQGFLATEHWWRLATRETRGMTRSDAARVGFMAEQWLGAFSP
    domain SNIAWANPAVVERTREEGGANLVRGAENFAEDLLRLVLRAPNGHGEFEVGVDVAATPGEVI
    protein FRNELIELIQYGPSTETVHAEPILIVPAWIMKYYVLDLRPQNSLVRYLTAQGFTVFMISWRNPG
    [Methylosinus PEDRDLTFDDYRVSGVLAALSAIDAVRPGSKVHACGYCLGGTLLSIAAAAMARDGDARLASIS
    trichosporium LLAAQTDFSEPGELMLFVDAAQVAFLEDMMWDQGVLDTRQMAGAFAALRSNDLVWGKA
    OB3b] VQDYLLGERRKPNDLMAWSADQTRMPYRMHSQYLRGLFLENRLTAGRYAVEGEVVALKDI
    SAPMFVVGTTSDHIAPWRSVYKASLFTDCELTFVLTSGGHNAGVVSEPGRSGRSYHVGLRRP
    GDFYVGPDKWLAAARLAEGSWWPEWAAWLAARSGDERVAPPTMGARGYPPLYPAPGRY
    VHQA (SEQ ID NO: 56)
    gi|52841292 phbC gene MSAMKGLEKQCCPKKRILTQSQELQEGVDFSCCAPADRGTSDNFFPFFTRLVQANLAKWTA
    product GISPAAIGSSYSTWLWQLAQSPGVLWELAFYPVFHAKDCINNIVCVERAADGKDVRFKKDS
    [Legionella WQPMPWRLFAEGFLQMEDWWRRATTDVPGLPNQVERTVSFWARQCLDALSPSNFVWS
    pneumophila NPDLFHEAMRTGGLNLIQGGQIALEDWLEKLTGAPPTGSEHFIPGKQVAITPGRVVFQNHLI
    subsp. ELIQYEAQTKTVYKEPILILPAWIMKYYILDLSPHNSLVKWLVSQGHTVFIISWRNPDKEDQDL
    pneumophila GMDDYYRQGAMAAIDAVSTLFPETKINLMGYCLGGTLAMITAAAMGRDKDERLNSLTLLA
    str. AQGDFTEAGELMLFVTESQVDFLKSMMREQGYLDTKQMAGSFQMLRAYDLIWSKMVQD
    Philadelphia YMHGMRRGMIDLTAWNADATRMPYKMHSEYLEKLFLRNDFAEGRYTVEGKPVAAENIKLP
    1] VFAVSTEKDHVAPWQSVYKIHLMTEGDVTFVLTGGGHNAGIISEPGHPGRSYRVHEQKQGE
    AYLNPESWLAMAERREGSWWREWNEWLVQQNTKKRIASSVMNPSLPEAPGTYVLQK
    (SEQ ID NO: 57)
    gi|148359804 PHA synthase MKKTTEKPINKTKEMPASSKKEILNPLEQTPSPEQSDPIFRFIDKLYQANLGKLTAGISPAALGT
    [Legionella AYYSWFAQLLQSPGSMLRLAYYPLLHANDYLSNLFKYDKPRDGKDVRFHTENWSYYPWRL
    pneumophila WAEQFLQFEDWCLQASSKVPGIPLHVKRTVTFSTRQILDALSPSNFVLTNPDLLQETIRSNGQ
    str. Corby] NLIRGTELAFQDFVEKITGSPPAGVENFIPGKQVAVTKGKVVYSNHLIELIQYTPQTEKVYKEPI
    LILPAWIMKYYILDLLPENSLVNWLVRQGHTVFIVSWRNPTKEDRNLGLDDYYKLGAMDAIN
    AVSNAIPHTKIHLMGYCLGGTLALLTAAAMAHDHDNRLKTLSLLAAQGDFIDAGELLLFITKS
    EVSFLKSMMWEQGYLDTKQMSGTFQMLRSYDLIWSKMVQDYMHGTQRGMIPLLAWNA
    DATRMPYKMHSEYLEKLFLNNDFAEGRFILDGKPVVGENIRIPAFVVSTEKDHVAPWKSVYK
    THLLINSDITFVLTNGGHNAGIVSEPGHEGRYYRIRERKMDSTYLDPTNWLKKAELREGSWW
    IAWHDWLVNHSSQKQVSAPKLDKKLPNAPGKYVLQK (SEQ ID NO: 58)
    gi|326404096 poly(3- MPGFATFDRLSRAMFARISQGVSPLAVADAWTDWALHLELALGKQEALAMRAATFLLRLG
    hydroxyalkanoate) FWLPRAAIGEPENPPLRPPEGDRRFADEGWSAYPFNAIVQGFLVADDWWREATRQVPGLV
    polymerase RRHEAEVAFMARQILDIAAPTNIPWLNPEIIRRTLQEGGFNLLRGWSNWIEDAERLLAGQGP
    [Acidiphilium YGAEAFPVGEVVATTAGKVVYRNELMELIQYAPATAKVTAEPVLIVPAWIMKYYILDLTPETS
    multivorum LVRYLVTNGHTVFIISWINPDRHDRNVGLDDYRRHGVMAALDAVSRIVPDRAIHACGYCLG
    AIU301] GTILAIAAATMARDHDDRLASLTLLAAQTDFADAGDLMLFLDERQFLLLEDLMWDQGYLDT
    RQMAGAFQALRSNELVWSRLIRNYMLGERDRMTPLSAWNSDQTRMPARMHSEYLRGLFL
    ENRLSAGRFAVEGRVIALRDIRVPLFAVATTRDHIAPWRSVYKIALFADTDITFVLASGGHNV
    GVVNPPNQSIGTFQILTRRHGERYVDPDTWATLAPERQGSWWPAWRDWIGGVGTGCAA
    DPPPMAAPSRGLPVLGDAPGAYVHER (SEQ ID NO: 59)
    gi|330826932 poly-beta- MPDTFSAAALADQLDTQFHAALARRFFSLSPAAGMLAASDWALHLAVSPGKCMALARLAL
    hydroxybutyrate RQSEELAGYARERMTAGADPQLRHGVQPPAQDRRFAAPEWQQWPFNYMHQSFLLTQQ
    polymerase WWAAATHGVKGVEKHHENVVAFAARQLLDVFSPGNQLATNPVVLQRTLQQGGANLLRG
    domain- ALNAADDLQRLAAGKPPAGTEDFVVGRDVAVTPGKVVLRNRLVELIQYTPTTEAVHPEPVLI
    containing VPAWIMKYYILDLSPHNSLIRYLVDQGHTVFCLSWKNPGYEDRDLGLDDYLKLGFHAALDAV
    protein NAIVPKRKVHATGYCLGGTLLAIAAAAMARDGDARLASLSLFAAQTDFSEPGELGLFIDESQV
    [Alicycliphilus NLLEAQMTQTGYLKASQMAGAFQMLRSYDLLWSRLVNEYLLGERTPMNDLMAWNADAT
    denitrificans RMPARMHAQYLRRLLLDDDLSRGRYPVGGKPVSLSDITLPIFMVGTLTDHVAPWRSVHKLH
    K601] HLTTTEITFALTSGGHNAGIVNPPGNPRRHYQLRTRPAGGNYMAPDDWLAAAPAAQGSW
    WPAWQEWLQARSGKPVAPPHMGARGYKAGADAPGHYVLEK (SEQ ID NO: 60)
    gi|222110509 poly-beta- MSNVATHGKADLAQPEACRPDTLDTLANAWRARSTGGLSPAAGLLAWYDWALHLSLSPG
    hydroxybutyrate KQRSLIEKGLHKQQRLARYALRVASAHDCPTCIEPLEQDRRFAAPAWQQWPFNVIHQGFLL
    polymerase QQQWWHNATTGVRGVSRHHENMVTFAGRQWLDMWSPSNFIWTNPEVLHAITQSGGA
    domain- NLWRGAMNFLEDARRLALDDAPAGVEGFEVGKDVAVTPGKVVFRNHLIELIQYSPTTPDVH
    containing AEPVLIVPSWIMKYYILDLSPHNSMVKYLVDQGHTVFILSWKNPTAADRDLGLEDYRWLGV
    protein MDALDAVTAIVPERKVQAVGYCLGGTLLAIAAAAMARDGDERLQSLTLLASETDFRESGEIAL
    [Acidovorax FIDDSQLAWLEAGMWDKGYLDGKQMAGAFQMLNSRDLIWSRRVREYLLGERQTFNDLM
    ebreus TPSY] AWNADVTRMPYRMHSEYLRRLYLDNDLAEGRYRVGGRPVALADIEVPMFIVGTVRDHVAP
    WPSVYKMHLLSDAELTFVLTSGGHNAGVVSEPGHPRRSFQIATRAAGDRYIDPQLWRAETP
    MNEGSWWPAWQQWLAQRSAGRVAPPAMGGTQAPLGDAPGTYVAMR (SEQ ID
    NO: 61)
    gi|39937303 phaC gene MMLQTSPPAPSAASQQIQSPARHHGPSDSDRTLHATLAPLTGGLSPTALTLAYADWLSHLF
    product WAPTQRMDLVNDALRRGTQLAEASIGQTAPWSLIAPQPQDRRFSAPEWREPPFNLMAQG
    [Rhodopseudomonas FLLAEQWWHDATTNIRGVSEQNEKIVEFATRQMLDVWAPSNFALTNPEVLRRTVSTEGRNL
    palustris ADGFRNWWEDLLELMAHEPKHDFVVGKDVAVTPGKVVYSNKLIELIQYAPATETVRPEPILI
    CGA009] VPAWIMKYYILDLSPHNSLVKYLTEQGYTVFMISWRNPTAADRDVSLEDYRRLGVMAALDTI
    GAILPDRPVHAVGYCLGGTMLSIAAAAMGRDGDSRLKSITLFAAQTDFTEAGELTLFINESQV
    AFLEDMMWNRGVLDTTQMSGAFQILRSNDLIWSRLVHEYLMGVRSEPNDLMAWNADAT
    RMPYRMHSEYLRKLFLDNDLAEGRYVVDGRPIALSDIHTPIFVVGTQRDHVAPWRSTFKIHLL
    ADADVTFCLTGGGHNAGIVSPPSPKAHGYQVMTKEADGPYVGPDDWLKQAPHAEGSWW
    TEWVHWLGTRSGEPVAPPRIGLPDVDPGALPNAPGSYVLQT (SEQ ID NO: 62)
    gi|172063316 poly-beta- MKASVTRAPRGNESIRPSGAVEPESSMTQCPQAGTTPAEQWNRAAHANVAAMTFGLSPV
    hydroxybutyrate SLALAMLDWGAHLAVSPGKCFDLAMQACVAAVAPAADQCEAEAGEADPTGLAVHAGQA
    polymerase DPRFAAPAWAGWPFHVYRDSFLSIQRWWRDATHGVPGVERHHEELVGFAARQWLDACS
    domain- PGNFLATNPVVLDATMCSGGANLAAGALNWLEDAKALLERAGGTHAHDARTYLPGRDVAI
    containing TPGRVVWRNALCELLQYEPTTARVAREPILIVPSWIMKYYILDLQPHNSLIRFLVDAGYTVFAV
    protein SWRNPGAEARDLGLDDYLRDGCMAALDAARSVCGGAVHTVGYCLGGTLLAIVAAALARDG
    [Burkholderia RQHEALRSVTLLAAQTDFSEPGELGLFIDASELSALDALMWRQGYLDGAQMSAAFQLLNAR
    ambifaria DLIWSRMMSEYLLGTRTKPNDLMSWNADTTRMPYRMHSEYLTRLFLDNDLAVGRYCVDG
    MC40-6] RPVALSDIDVPTFVVGTERDHVSPWGSVYKLHLLTHHALTFVLTSGGHNAGIVSEPGHPGRH
    YRRATREPGAPYRSRHDFVRGTTAVDGSWWTCWRDWLHERSSGDVPARTPAAGFDAAP
    GTYVLET (SEQ ID NO: 63)
    gi|1730539 PHAC_METEX MGTERTNPAAPDFETIARNANQLAEVFRQSAAASLKPFEPAGQGALLPGANLQGASEIDEM
    RecName: TRTLTRVAETWLKDPEKALQAQTKLGQSFAALWASTLTRMQGAVTEPVVQPPPTDKRFAH
    Full = Poly(3- ADWSANPVFDLIKQSYLLLGRWAEEMVETAEGIDEHTRHKAEFYLRQLLSAYSPSNFVMTNP
    hydroxyalkanoate) ELLRQTLEEGGANLMRGMKMLQEDLEAGGGQLRVRQTDLSAFTFGKDVAVTPGEVIFRND
    polymerase; LMELIQYAPTTETVLKRPLLIVPPWINKFYILDLNPQKSLIGWMVSQGITVFVISWVNPDERH
    Short = PHA RDKDFESYMREGIETAIDMIGVATGETDVAAAGYCVGGTLLAVTLAYQAATGNRRIKSATFL
    polymerase; TTQVDFTHAGDLKVFADEGQIKAIEERMAEHGYLEGARMANAFNMLRPNDLIWSYVVNNY
    AltName: VRGKAPAAFDLLYWNADATRMPAANHSFYLRNCYLNNTLAKGQMVLGNVRLDLKKVKVP
    Full = PHA VFNLATREDHIAPALSVFEGSAKFGGKVDYVLAGSGHIAGVVAPPGPKAKYGFRTGGPARGR
    synthase; FEDWVAAATEHPGSWWPYWYKWLEEQAPERVPARIPGTGALPSLAPAPGTYVRMKA
    AltName: (SEQ ID NO: 64)
    Full = Polyhydroxy-
    alkanoic
    acid synthase
    gi|16125629 poly-beta- MVETLSANLARAAVTAQGAIAEAALRQADRPAALTPDPFHVAPALNEVMTRLAAQPDRLM
    hydroxybutyrate RAQADLFGQYMELWQTAARRAAGEDVAPVVAPAAGDKRFNDPDWASNPMFDLMKQSY
    polymerase LLSSNWLNGLIAEVDGVDPATKRRVEFFTKMLTDAFSPSNFLISNPAALREVVQTQGQSLVR
    [Caulobacter GMENFAADLERGGGQLAISQTDLAKFKVGENVATAPGKVVYQNDILQLLQFDPTTDTVCEIP
    crescentus LLIFPPWINKFYIMDLRPENSMIRWLTAQGFTVFVASWVNPDQTLAAKTFEDYMVEGIYDA
    CB15] AQQVMTQCGVDRVNTVGYCIGGTLLSVALAHMAARGDKRINSATFFAAQQDFAEAGDLLL
    FTNEEWLQSIEQQMDQAGGFLPSQSMADTFNALRGNDLIWSFFVSNYLMGKEPRPFDLLF
    WNADQTRMPKALHLFYLRNFYKDNALTTGKLSLGGERLDLSKVKIPIYVQSSKDDHIAPYRSV
    YRGARAFGGPVTFTMAGSGHIAGVINHPDARKYQHWTNSELPADVSEWIAGAHEHPGSW
    WPHWAAWLKARSGDQVPARDPAKGKLKPLEDAPGSFVLVKSQP (SEQ ID NO: 65)
    gi|170744156 unnamed MLATSPTQSSAAIPARPPALRLVPPVAAAGPVRDAAEPGDDLHDAGQAIDQAAHAAVARLT
    protein GGLSPAALANAWLDWSVHAAFSPGKQAELAAKAFRKGQRLQSFLWRNLLVGAQAEPCIEP
    product LPQDHRFDDPAWRTWPFCLYQQGFLLTQQWWHNATTGVRGVARAHEEIVAFTARQMLD
    [Methylobacterium GVSPSNHPLTNPVVLNATLASGGANLVLGALNALEDARRGLAGLKPAGAERFAVGREVAVT
    sp. 4- EGEVVYRNDLIELIQYAPKTGAVRPEPVLIVPAWIMKYYILDLSPENSLVRHLVGQGFTVFMIS
    46] WRNPGPADRDVSFDDYRRLGVMAALDAVSAIRPGRAVHAAGYCLGGTLLSIAAATMARDG
    DARLASLTLFAAQVDFTEAGELTLFINESQISFLESLMRSEGVLDSKQMAGAFQLLRSNDLIW
    SRIVNSYLLGRREAVTDLMAWNADATRMPARMHAEYLRRLFLDNDLAEGRLRVEGRPVAL
    TDIRAPIFAVGTEKDHVAPWRSVFKLTLMTDADVTFLLASGGHNAGIVSEPGHRGRHYRVHS
    RAATDRYVDPDSWLDLARLEQGSWWPEWASWLAERSGPPEPPPPMGLPGAPTLGPAPG
    RYVREA (SEQ ID NO: 66)
    gi|146340526 Poly-beta- MTDVPNNTNPQKTFDAEAFATNIARAMESSGKALAAYLKPRETGEVQDRPPTELTEVVKSFT
    hydroxybutyrate AVADYWLSDKDRASDIQTKLAKGYLDLWGSAARRLAGEEAPPAISPSPRDKRFADPEWKSN
    polymerase QFYDFVMQAYLLTTQWAQDLVHNAEGLDPHTRKKAEFYVNQITNALAPSNFVMTNPEVM
    [Bradyrhizobium RQTVASSGDNLVRGMQMLAEDIEAGKGTLKIRQSDPANLEVGVNMATTPGKVIFQNEMM
    sp. ORS QLIQYAPTTETVLRTPLLIVPPWINKFYILDLRPEKSFIKWCVDQGLTVFVISWVNPDKKLGTKT
    278] WEDYMKEGPLTAMDVIEKVTGEMKVHTMGYCVGGTMLATTLAWLADKRRQRVTSATFLA
    AQVDFTHAGDLLVFVDETQISALERDMQASGVLEGSKMAMAFNMLRSNDLIWSYVVNNYL
    KGQPPQAFDLLHWNSDATRMSAANHSYYLRNCYLENRLTTGTMVLDNTLLDLSKVKVPVY
    NLATREDHIAPADSVLYGSQFFGGPVKYVLSGSGHIAGVVNPPSSGKYQYWTNDQIHDISLK
    DWMKGAQEHKGSWWPDWREWLGQLDPEQVPARSVGSEAYPPIEDAPGSYVRVRA
    (SEQ ID NO: 67)
    gi|126463677 unnamed MSDMKWNAEGAPAYGQALDRAARAAIAGMTRGLAPSVLATAALDWMMHLAAAPGKQA
    protein ELWEKAATASAALMQAGLQPHEAPVRDRRYASEAWNRQPFAALRDSFLLTEDWWQTATT
    product GLRGMDRAHEAALSFSVRQMLDVWSPSNNPFLNPEVLARTTETRGANLMQGAMNFAGD
    [Rhodobacter MARLATGVPMDEGGFRIGETLAATPGKVVLRTHLMELIQYSPTTREVHPEPVLIVPAWIMKY
    sphaeroides YILDLSEQNSLVRWLVAQGFTVFMISWRNPESEDRDLGLIDYLDQGPRAALKAIQTITGAPKV
    ATCC 17029] HAAGYCLGGTLLSIMAARMAHDHDERLASMTLFAAQVDFSEAGELALFISEAQVALLEDM
    MWHQGYLDSDQMSGAFTLLRSNDLIWSRMIHEYMMGERPHPNDLMTWNADSTRMPYR
    MHSEYLRQLFLENRFAEGKFELEGHALSLTELRLPILAVGTETDHVAPWRSVFKIQRLTETETT
    FVLTSGGHNAGIVSEPGHPRRHFRIATTGRDDPYRDADEWFAETAPVEGSWWPAWGAWL
    AERSTPKGKLPPMGNARGGYPALCEAPGTYILQR (SEQ ID NO: 68)
    gi|359401847 putative MKGLKIMVEAQIPGVGDPLDGLAETMDRAAGAMIAQATFGLSPATLAQAVSDWMLHLAA
    poly-beta- SPGKQTQLAAKALRKMTRLGDYAMRSATDAQAARAIEPLPQDRRFADPAWASAPFNLVSQ
    hydroxyalkanoate AFLLNQQWWHAATTGITGVTAHHEEMVAFAVRQWLDTVAPTNFLATNPVLQQRILETGG
    synthase QCLADGLRNWMTDVEALMRGLPPAGTEAFQVGETLATAEGKVVYRNRLMELIQYAPTTEQ
    [Novosphingobium ARPEPILIVPAWIMKYYILDLSPENSLVQWLTAQGFTVFMISWHNPGSTDRDLEMADYLQLG
    pentaromativorans PMAALDAVAAITGGASVHAAGYCLGGTLLAIAAAAMARDGDDRLASLTLLAAQTEFCEPGE
    US6-1] LGLFIDEGQLSLLENMMWGRGYLDSAQMGGAFQMLRSNDLVWSRVLTTYLMGEREPMN
    DLMAWNADGTRMPYAMHSQYLRRLFLEDDLAEGRFQVNGRPIALSVLRWPMFVVGTERD
    HVAPWRSVFKIHRLTGAPIDFVLTSGGHNAGIVSEPGHPGRSYRLLTREADGAALDPDAWLD
    AAPRHEGSWWTAWGDWLAKLSGNAGTPPPMGATDKGYAPLADAPGHFVLER (SEQ ID
    NO: 69)
    gi|581529 PHA synthase MLDHVHKKLKSTLDPIGWGPAVTSVAGRAVRNPQAVTAATAEYAGRLAKIPAAATRVFNA
    [Rhodococcus NDPDAPMPVDPRDRRFSDTAWQENPAYFSLLQSYLATRAYVEELTEAGSGDPLQDGKARQ
    ruber] FANLMFDALAPSNFLWNPGVLTRAFETGGASLLRGARYAAHDILNRGGLPLKVDSDAFTVG
    ENLAATPGKVVFRNDLIELIQYAPQTEQVHAVPILAAPPWINKYYILDLAPGRSLAEWAVQH
    GRTVFMISYRNPDESMRHITMDDYYVDGIATALDVVEEITGSPKIEVLSICLGGAMAAMAAA
    RAFAVGDKRVSAFTMLNTLLDYSQVGELGLLTDPATLDLVEFRMRQQGFLSGKEMAGSFD
    MIRAKDLVFNYWVSRWMKGEKPAAFDILAWNEDSTSMPAEMHSHYLRSLYGRNELAEGLY
    VLDGQPLNLHDIACDTYVVGAINDHIVPWTSSYQAVNLLGGDVRYVLTNGGHVAGAVNPP
    GKRVWFKAVGAPDAESGTPLPADPQVWDEAATRYE HSWWEDWTAWSNKRAGELVAPP
    AMGSTAHPPLEDAPGTYVFS (SEQ ID NO: 70)
    gi|227823933 poly-beta- MKTGDRPVLAADRARQAGSARAIAAQSALPCENDGADGEAFRAIDRMREALSATATGGLS
    hydroxybutyrate PAALTLAFFDWSIHLASAPGKRMELAHMAAQNWGLLLTYMAAAATRPDAPPCIEALPGDN
    polymerase RFRAEGWQKQPYTVWAQAFLLGQQWWHNVTRNVPGMTPHHEDVVSFTARQWLDVFS
    domain PSNIPFANPEVIHKAMETGGANFTQGFRNWLEDVGRLATKQRPVGTEAFRVGHDTAATPG
    protein KVVYRNHLIELIQYAPATEEVLAEPILIVPAWIMKYYILDLSPHNSLIRYLVAQGHTVFCISWRN
    [Sinorhizobium PSAKDRDLTLDDYRRLGILAALDAVSAIVPERKIHATGYCLGGTLLAIAAAAMARTEDQRLAS
    fredii VTLFAAQTDFSEPGELALFIDHSQLHFLDSLMWHSGCLSADQMAGAFQLLRTNDLVWSRLV
    NGR234] HDYLIGKRTPMTDLMAWNADPTHMPYRMHAEYLQRLYLDNELAAGRFIVDGRPAHLQNIR
    VPMFVVGTERDHVAPWHSVYKIHYLTDTDVTFVLTSGGHNAGIVSEPDHPGRGFRIALTRES
    DSSVSADEWVAAATSKDGSWWPDWVEWLAGHSAPKRVTPPVIGAPERGYPPIDDAPGTY
    VHQR (SEQ ID NO: 71)
    gi|332526305 poly-beta- MHNPNVAAAVLADPALDPALAAARRLDSHFHAAVAPAFSGLSPISLALAWQDWALHLATQ
    hydroxybutyrate PATALALVARAQQSWLQAWGEMLGQAEPGNGDARFAAPAWRQWPWAPVVHGWHAT
    polymerase- ERWWQDATDLRGVDPHHREVVRFFARQWLDMLAPSNAGLANPEVLQRTAERGGANLVD
    like protein GTLHALDGWRRQHGLEPLRTPERRYEPGVDVAVTPGQVVWRNHLVELIQYLPLTASVQAEP
    [Rubrivivax VFIVPSWIMKYYILDLSPHNSFVKWLVEQGHTVFILSWRNPDESDALLAMQDYLELGIFDPLA
    benzoatilyticus QIARMIPGRRVHACGYCLGGTLLSLAAAALARPGRIARAELLPELASVSLLAAETDFTEPGEM
    JA2] GVLIDESQVTLLEDMMAERGFLTGAQMAGSFAYLHSRDQVWSRRLREFWLGEPDSPNDL
    MAWNADLTRMPAAMHSEYLRRCYLRNEIAEGRFPVEGRAVSLSDIAAPMFVVGTEKDHVS
    PWKSVYKIHRLADTTITFVLTSGGHNAGIVSEPGHANRRYRMATREVDGAWVDPEAWAEQ
    APRHEGSWWTAWHEWLLAQGSGETAKARTPAKADVVCAAPGTYVYQCWRD (SEQ ID
    NO: 72)
    gi|154253888 unnamed MTKNKKGNTSSTIVPALDMQAHMAWAQAWSSISPESSLLAWTDWASHLANSPGKQSELL
    protein AFAGSLSEQWMSLLKKSLVSPDQEVASPEPSPTNDRRFNDPAWDQWPYNLFRSSFLIQSKW
    product WEQATQGVWGVDPQHERLLAFGAKQWLEMVSPTNSALFNPVVLKKTIEEQGANLARGM
    [Parvibaculum SNFLDDLRRQLSGEPPAGTENFVVGRDVAVTEGKVVLRNQLIELIQYTPTTEKVHPEPILIIPA
    lavamentivorans WIMKYYVLDLSPHNSLIRYLVAQGHTVFCISWKNPDAGDRDLGMDEYLEFGLRAALDAVTSI
    DS-1] VPEQGIHAAGYCLGGTLLAIGASAMARDGDTRLVSVSLLAAQTDFSEPGELSLFINESQVALL
    EASMAQTGYLTSDQMSGAFQLLRSYDLIWSRMIDEYLLGDRRPMTDLMAWNADGTRLPA
    KMHSQYLRRLYLNNDLSAGRYPVTGRPVSVGDIAVPVFCVGTASDHIAPWRSVYKLHLLSSA
    ELTFVLTTGGHNGGIVSEPGRGKRQYQIHTRAAGDGYMAPDEWQATAQTHLDSWWPAW
    SAWLRERSGEGVAPPLMGAESRGYPTICDAPGKYVRS (SEQ ID NO: 73)
    gi|53716799 phbC gene MDTRHAPESGAPDAPLPAHPPASYAPESPYRIFDLAKEASVAKLTSGLSPASLQLALADWLIH
    product LAAAPGKRAELATLALRHAALLGQYLLEAATGRTPAAPAQPSPGDRRFRAGAWQLEPYRFW
    [Burkholderia HQSFLLAEQWWRAATRDVPGVSPHHEDVVAFSARQMLDTFAPANYVATNPEIAQRTALT
    mallei ATCC GGANLAQGVWNYLDDVRRLITKQPPAGAEQFELGRNLATTPGRVVFRNHLIELLQYSPTTPD
    23344] VYAQPVLIVPAWIMKYYILDLSAHNSLIRYLVGEGHTVFCISWRNVDASDRDLSLDDYRKLGV
    MDALDTIGAIVPGEKIHATGYCLGGTLLSIAAAAMANTGDDRLASITLLAAQTDFAEPGELQL
    FIDDSEIHFLESMMWERGYLGAHQMAGSFQLLMSNDLIWSRVIHDYLLGERTPMIDLMAW
    NADSTRMPYRMHSEYLRHLFLDNDLATNRYVIDGQTVSVHNIRAPFFVVGTEHDHIAPWRS
    VYKIHYLSGSDVTFVLTAGGHNAGIVSEPGHAKRHYRMKMTAAAAPSISPDEWLAGATDFE
    GSWWPAWHAWLARHSSPQRVAPPPLGKPGAHTLGDAPGTYVFQK (SEQ ID NO: 74)
    gi|365891729 putative MSDAKSAAEDANSVAREFVREDHELDKAFSAVLARLTGGISPAALSMAYLDWACHLAAAPQ
    poly-beta- RQLDIARDAWQGARQLAERSLHFADSNRVPWDLIKPQANDHRFSKPQWGMQPFNLFAQ
    hydroxybutyrate AFLLGEDWWHKATTNIRGVDPANEAVVDFSLRQLLDMFAPSNFAATNPEVVEKIFQSGGE
    polymerase NLVFGWQNWLSDLMQVLQPGQASRSAEFVPGETVATAPGKVVFRNQLIELIQYAPTTAEV
    (Poly(3- RPEPILIVPAWIMKYYILDLSQHNSLVRYLTDQGFTVFMISWRNPDAKDRDIAFDDYRSMGV
    hydroxybutyrate) MAALSEIGKIVPGAQIHAAGYCLGGTLLSITAAAMAREGDTRLKTITLFAAQTDFTEAGELTLFI
    polymerase) NESQVAFLEDMMWERGYLDTTQMAGAFQLLRSNDLIWSRVSRDYLLGERAHPSDLMAW
    (PHB/PHA NADATRLPYRMHSEYLRKLFLNNDLAEGRYRVEGKPVSLSDIHTPMFVVGTLRDHVAPWKS
    polymerase) TYKIHYEVDADVTFVLASGGHNAGIVAPPHEQGHSHQVRTKAADAPYLGPDEWQSTSPRIE
    (PHB/PHA GSWWPTWLDWLAQRSGPLDAPPRLGTEGSHELGNAPGEYVHS (SEQ ID NO: 75)
    synthase)(Poly(3-
    hydroxyalkanoate)
    polymerase)
    (Polyhydroxy-
    alkanoic acid
    synthase)
    [Bradyrhizobium
    sp. STM
    3809]
    gi|338984011 Poly(R)- MAEQQNPRTEAPNLPDPAAFSRTMADIAARSQRIVAEWLQRQHEADVAIDPLNIGSAFME
    hydroxyalkanoic MMARLMANPASLIEAQIGFWQDYVTLWQHSTRRIMGIETQPVVPPDPRDKRFQHEEWKE
    acid NEIFDFIRQSYLLSARFVQDVVRRVDGLDPKTAQKVDFYARQFVDAMSPSNFALTNPQVLRK
    synthase, TAETGGENLLRGLSNLLRDLEAGRGQLHIRMTDAEAFSVGGNIAVTPGKVVYRNELMELIQY
    class I APATTTAHKTPLVIFPPWINKFYILDLRPKNSFIRWAVEQGHTVFVASWVNPDERLAEKDFA
    [Acidiphilium DYMKLGVFAALDAIEQATGERQVNAIGYCLGGTLLAATLAVMARRRDSRIKSATFLVTLTDF
    sp. PM] ADVGELGVFIDEEQLAALEDRMNRRGYLEGSAMATTFNMLRSNDLIWSFVVNNYLLGNETF
    PFDLLYWNSDSTRMPAAMHSFYLRNMYQKNLLSQADAITLDGTPVDLRRIKVPVYFLSCRED
    HIAPWASTYRATQLMAGPKRFVLAASGHIAGVINPPGSGKYNHFVNATLPANAEDWFAGA
    TEVAGSWWPDWQRWIAAQGRGEVPARTPGDGALPALADAPGDYVKVRSA (SEQ ID
    NO: 76)
  • In certain embodiments, the present disclosure provides a non-naturally occurring C1 metabolizing bacterium; a non-naturally occurring obligate C1 metabolizing organism; a non-naturally occurring C1 metabolizing organism, wherein the non-naturally occurring C1 metabolizing organism does not include Pichia pastoris; a non-naturally occurring methanotrophic or methylotrophic bacterium; or a non-naturally occurring CO utilizing bacterium, wherein the non-naturally CO utilizing bacterium naturally possesses the ability to utilize CO; wherein the non-naturally occurring C1 metabolizing bacterium or organism converts a C1 substrate to propylene, and further wherein the non-naturally occurring C1 metabolizing bacterium or organism has a functional β-ketothiolase and/or a functional acetoacetyl coenzyme A reductase, or has a functional β-ketothiolase and/or a functional acetoacetyl coenzyme A reductase activity (i.e., has enzymes that perform the function of β-ketothiolase and acetoacetyl coenzyme A reductase).
  • In certain embodiments, a non-naturally occurring C1 metabolizing organism according to any of the embodiments disclosed herein is a C1 metabolizing bacterium that has a functional β-ketothiolase activity and a functional acetoacetyl coenzyme A reductase activity.
  • In certain embodiments a non-naturally occurring C1 metabolizing organism according to any of the embodiments disclosed herein is a C1 metabolizing bacterium that does not produce a substantial amount of polyhydroxybutyrate.
  • β-ketothiolase and acetoacetyl coenzyme A reductase are enzymes in a PHB synthesis pathway that catalyze the condensation of two acetyl-CoA molecules to acetoacetyl-CoA and reduction of acetoacetyl-CoA to 3-hydroxybutyryl-CoA, respectively (see FIG. 1). β-ketothiolase is an enzyme that initiates biosynthesis of PHB in most bacteria. A C1 metabolizing organism may naturally possess β-ketothiolase and acetoacetyl coenzyme A reductase as part of an endogenous PHB synthesis pathway. Alternatively, a C1 metabolizing organism may be genetically modified with exogenous nucleic acids encoding β-ketothiolase and acetoacetyl coenzyme A reductase. These enzymes allow a C1 metabolizing organism to produce 3-hydroxybutyryl-CoA, a precursor of propylene in an engineered biosynthetic pathway via crotonyl-CoA and crotonic acid as disclosed herein (i.e., 3-hydroxybutyrl-CoA is substrate of crotonase) (see FIG. 1). Exogenous nucleic acids encoding β-ketothiolase and acetoacetyl coenzyme A reductase are expressed in a sufficient amount to produce propylene. In a specific embodiment, β-ketothiolase is encoded by phaA or phbA. In another specific embodiment, acetoacetyl coenzyme A reductase is encoded by phaB, hbd, or phbB. Exemplary β-ketothiolase and acetoacetyl coenzyme A reductase amino acid sequences are provided in Tables 2 and 3, respectively.
  • TABLE 2
    Exemplary β-ketothiolase Amino Acid Sequences
    Genbank Gene Name/
    Accession # Organism Amino Acid Sequence (SEQ ID NO: #)
    gi|52209583 acetyl-CoA MTDVVIVSAARTAVGKFGGSLAKIAAPELGASVIRAVLERAGVKPEQVSEVILGQVLTAGSG
    acetyltransferase QNPARQALIAAGLPNAVPGMTINKVCGSGLKAVMLAANAVVAGDAEIVVAGGQENMSA
    [Burkholderia APHVLPGSRDGFRMGDAKLVDSMIVDGLWDVYNKYHMGITAENVAKEYGITREAQDQF
    pseudomallei AALSQNKAEAAQKAGRFDDEIVPIEIPQRKGEPLRFATDEFVRHGVTAESLASLKPAFAKEG
    K96243] TVTAANASGINDGAAAVLVMSAKKAEALGLEPLARIKAYANAGVDPSVMGMGPVPASRR
    CLERAGWSVGDLDLMEINEAFAAQALAVHKQMGWDTSKVNVNGGAIAIGHPIGASGCRI
    LVTLLHEMLKRDAKRGLASLCIGGGMGVALALERP (SEQ ID NO: 77)
    gi|296445575 acetyl-CoA MTTEIVIVSAARTAVGSFNGAFGATPAHELGAVAVKAAIERAGLAPADIDEVILGQVLGAA
    acetyltransferase QGQNPARQAAIKAGVPQEKTAFGINQVCGSGLRAVALAAQQIQAGDASVIVAGGQESMS
    [Methylosinus LSQHSAHMRAGTKMGDVKFVDTMIVDGLTDAFNNYHMGITAENVAAKWQISRAEQDAF
    trichosporium AVASQNKAEAAQKAGKFKDEIVPFTVSTRKGDVIVDQDEYIKHGVTLEGVAKLKPAFTKEGT
    OB3b] VTAANASGLNDGAAALVVMSAAEAARRGLTPLARIASWATAGVDPSVMGSGPIPASRKA
    LEKAGWKIGDLDLVEANEAFAAQALAVNKDLGWDPAIVNVNGGAIAIGHPIGASGARVLT
    TLLYELARRGGKRGLATLCIGGGMGVALTIER (SEQ ID NO: 78)
    gi|296444966 acetyl-CoA MSAVDPIVIVGAARTPIGALLGELKNATAPQLGAAAIRAATERAGLAPERVDDVLMGCVLS
    acetyltransferase AGLGQAPARQAALGAGLADTTGCVTINKMCGSGMKALMLAHDQLLAGSSRAIVAGGME
    [Methylosinus SMSNAPYLLGRARVGYRMGHGRLIDHMFLDGLEDAYDEGKLMGAFAEDCATTHQFTREK
    trichosporium QDDYATASLRRAQQAAASGAFDWETTPVATHDRKTSATVTRDELPASAKIENIASLKPAFR
    OB3b] DGGTVTAANSSAISDGAAALALMRRSEAERASLAPLAIVRAHATHAGPPHLFPIAPIGAIAKL
    CERAGWPLTSVDLFEINEAFAVVVLAAMRELYLPHEKVNVHGGACALGHPIGASGARIVVT
    LLAALRKYDLRRGVAALCIGGGEATAMAIETIV (SEQ ID NO: 79)
    gi|296445504 acetyl-CoA MPEAYIYDAVRTPRGRGKPNGSLHEVSSLGLAVAALSALKQRNRLDGAPVDDVILGCVDPV
    acetyltransferase GEAGGDIARAAAIASGFGYEVPGVQINRFCASGLDAVNFAAAQIMSGQHELTIGGGVESM
    [Methylosinus SRVGIGASGGAWPADPAIAIPSYFMPQGVSADLIATKYGFSRNDVDAYAMQSQQRAARA
    trichosporium WEEQRFARSVTPVKDVNGLTILDHDEHMRPSTDMQSLGALKPAFAFLAEQAGFDAVAIQ
    OB3b] AHPDVEKINYVHHAGNSSGIVDGAAAVLLGSKEAGEKAGLTPRARIRAFANIGSEPALMLT
    GPVDVTKKLLAKAGMTFGDIDLVEVNEAFAAVVLRFLQAFSLDDSKVNVNGGAIALGHPLG
    ATGAMLVGTALDELERSGKGVALVTLCIGAGMGTATIIERV (SEQ ID NO: 80)
    gi|23502628 phbA-1 gene MSDPKSIVIASAARTAVGAFNGAFANVPAHELGAVAIKAALERAGVDAADVDEVILGQVLT
    product AGEGQNPARQAAMGAGCPKETTAFAINQLCGSGLRAVALGMQQIVSGDAKIIVAGGQES
    [Brucella suis MSMAPHCAYLRSGVKMGDFKMIDTMLKDGLTDAFHGYHMGITAENIARQWQLSRSEQ
    1330] DEFALASQHKAEAAQKAGRFDEEIVPFTVKARKGDVVVSADEYIRPGTTMEVLAKLKPAFD
    KEGTVTAGNASGINDGAAAVVLMDAGEAARRGVKPLARIVSWATAGVDPSIMGTGPIPA
    TRKALEKAGWSVGDLDLVEANEAFAAQSCAVVRDLGLNPEIVNVNGGAIAIGHPIGASGAR
    VLTTLLYEMERRDAKRGLATLCIGGGMGVALCVERD (SEQ ID NO: 81)
    gi|260682683 acetyl-CoA MGVMNMREVVIASAARTAVGSFGGAFKSVSAVELGVTAAKEAIKRANITPDMIDESLLGG
    acetyltransferase VLTAGLGQNIARQIALGAGIPVEKPAMTINIVCGSGLRSVSMASQLIALGDADIMLVGGAE
    [Clostridium NMSMSPYLVPSARYGARMGDAAFVDSMIKDGLSDIFNNYHMGITAENIAEQWNITREEQ
    difficile DELALASQNKAEKAQAEGKFDEEIVPVVIKGRKGDTVVDKDEYIKPGTTMEKLAKLRPAFKK
    CD196] DGTVTAGNASGINDGAAMLVVMAKEKAEELGIEPLATIVSYGTAGVDPKIMGYGPVPATK
    KALEAANMTIEDIDLVEANEAFAAQSVAVIRDLNIDMNKVNVNGGAIAIGHPIGCSGARILT
    TLLYEMKRRDAKTGLATLCIGGGMGTTLIVKR (SEQ ID NO: 82)
    gi|147904014 acetyl-CoA MNSGEETVVIISAARTPIGSFNGALSTLPAHTLGSTVIKEVLKRATIKPEEVSEVIFGQVLTAG
    acetyltransferase AGQNPARQASVAAGVPYSIPAWSCQMICGSGLKAVSLGAQSIKTGEADIVVAGGMENMS
    2 QAPHLVHMRAGVKAGDVSLQDSIICDGLNDAFYKYHMGITAENVAKQWQITREEQDQLA
    [Xenopus VQSQNRTEAAQKAGYFDKEIVPVSVPSRKGPVEVKVDEFPRHGSNVEAMSKLKPYFLKDGS
    laevis] GTVTPANASGINDGAAAVVLIKESEARRRGLTPMARIVASAQAGLDPSIMGVGPIAAIRKA
    VEKAGWSLDDIDLFEINEAFAAQALAVVKDLGLNPEKVNCQGGAVALGHPLGMSGCRILV
    TLLYALERTGGKKGVAALCIGGGMGIAMCVERTS (SEQ ID NO: 83)
    gi|358447737 acetyl-CoA MRDVVIVAARRTAIGTFGGGLSSLSADQLGTAVIKALMEETGVAGDQINEVVLGQVLTAGV
    acetyltransferase GQNPARQSAINAGIPASVPAMTINKVCGSGLKAVHMAVQAIRCGDAEMMIAGGQESMS
    [Marinobacter QAPHVLPNSRNGQRMGNWSMVDTMIKDGLWDAFNDYHMGITAENIVEKYGISRDEQD
    manganoxydans EFAAASQQKAAAAREAGYFDGQIVPVSIPQRKGDPIVVDRDEGPRDGVTAEGLGKLRAAF
    Mnl7-9] KKDGTVTAGNASSLNDGAAAVMVCSAEKAKELGLTPIATIKAYANAGVDPTIMGTGPIPAS
    QRCLKLAGWSTEDLDLVEANEAFAAQAISVNRDMGWDTGKVNVNGGAIALGHPIGASGC
    RILVSLLHEMVRRDVHKGLATLCIGGGMGVALAVER (SEQ ID NO: 84)
    gi|294011684 acetyl-CoA C- MPLSDIVITAAKRTAVGGFMGAFGSTPAHELGRTAILAALAQAGVAPEEVDEVILGQVLTA
    acetyltransferase GQGQNPARQAAVNAGIPVERTAIGVNQLCGSGLRAVALAAQAIRAGDARIMVAGGQES
    [Sphingobium MSLAPHAQYLRGGAKMGPISLVDTMTHDGLTDAFNNYHMGITAENLAEKYQISREAQDV
    japonicum FSVGSQNKAEAARASGRFKDEIAPVTVKGRKGDTIVDTDEYIRAGATLEAMQSLRPAFRKD
    UT26S] GTVTAANASGINDGAAALVLMSAEEAAKRDALVLARIASFATCGVDPSIMGIGPAPASRQA
    LAKAGWSLADLDLIEANEAFAAQALAVGQELGWDAEKVNVNGGAIAIGHPIGASGARVLT
    TLIYEMQKRDAKKGLATLCIGGGMGVAMCIER (SEQ ID NO: 85)
    gi|212696567 hypothetical MTRKVVIASAARTPVGSFGGALKSQSAADLGIVAAKAAIERAGIKPEDIDETVLGCVLQAGL
    protein GQNVARQISLGAGIPETTPAMTINKVCGSGLRTVSLAAQMILAGDVDVVLAGGAESMSNA
    ANHYDR0_01105 PFLLNEARWGARMGNKKLVDEMITDGLWDVYNDYHMGVTAENVAEKYGITREMQDDL
    [Anaerococcus AAVSQQRASKARAEGRFKDEIAPVEIKDRKGNVTVVEDDEYIRDGVTQEGISKLRPAFIKDG
    hydrogenalis TVTAANASGINDGAACLVVMSEEKAKELGVKPLATIVSYASAGVDPKVMGTGPIPSSKKAL
    DSM 7454] EKAGWKVEDLDLVESNEAFAAQSYAVRNEMGFDPEKTNVNGGAIAIGHPIGGSGARILTTL
    LFEMQKRDSKKGLATLCIGGGMGTALVVER (SEQ ID NO: 86)
    gi|351728760 acetyl-CoA MEDIVIVSAARTAVGKFGGALAKTPATELGAIVIREAIARAGLSSDQIGEVIMGQVLAAGVG
    acetyltransferase QNPARQASMKAGVAKETPALTINAVCGSGLKAVMLAAQAVAWGDSEIVVAGGQESMSL
    [Acidovorax APHVLPGSRDGQRMGDWKLIDTMIVDGLWDVYNQYHMGITAENVAKAHGITREMQDA
    radicis N35] LALGSQQKAAAAQDAGKFVDEIVGVSLAQKKGDPILFNADEYLNRKTNAEALAGLRPAFDK
    AGSVTAGNASGLNDGAAAVVVMSAKKAAALGLKPLARIAAFGTSGLDPATMGMGPVPAS
    RKALQRAGWNAADVDLFELNEAFAAQACAVNKELAIDPAKVNVNGGAIAIGHPIGASGCR
    ILVTLLHEMQRRDAKKGLAALCIGGGMGVSLALER (SEQ ID NO: 87)
    gi|295687835 acetyl-CoA MSDVVIVSAARTPVGSFNGALSSLPASELGRVAIEAAISRAGLQPSDVDEVILGQVLQAGAG
    acetyltransferase QGPARQASVKAGIPVESPAWSLNQLCGSGLRAVALAAQQIAAGDAAVVVAGGQESMSQ
    [Caulobacter APHAQNLRGGQKMGDLSFVDTMIKDGLWDAFHGYHMGQTAENIASRWQITRADQDAF
    segnis ATCC AVASQNKAEAAQKAGKFDAEIAPVTIKGRKGDTVVDKDEYIRHGVTLESISGLKPAFTKEGS
    21756] VTAANASGLNDGAAALVLMSAEEAQKRGLKPLARIASWANAGVEPEIMGTGPIPASKKAL
    EKAGWTVADLDLVESNEAFAAQSLCVVRELGLDPAKVNVNGGAIAIGHPIGASGARVLTTL
    LHEMKRSGAQKGLATLCIGGGMGVAMCVEAV (SEQ ID NO: 88)
    gi|374996374 unnamed MRDVVIVSAVRTPVGSFCGALGQIPAAELGAIAVKEAINRAGITPEQVDEVILGNVLQAGLG
    protein QNPARQASIKAGIPQEVPSWTLNKVCGSGLKTVVCAAQAIMTGDADIVVAGGMENMSLA
    product PYVLTKARTGYRMGNDTVIDSMINDGLTDAFNNYHMGITAENIAEQFNISREEQDRYSVRS
    [Desulfosporosinus QNRAEAAIIAGKFNEEIVPVSIPQRKGDPVVVSQDEFPRFGATYEAIAKLRPAFKKDGTVTAA
    orientis NASGINDGAAAIVVMAKEKAEELGLTPLATIKSWASAGVDPKIMGTGPIPASRKALEKAGLS
    DSM 765] IDDIDVVEANEAFASQTLSVAQGLNLDPEKTNVNGGAIALGHPVGASGTRILVTLLHEMKRS
    NAHRGLATLCIGGGQGVALIVER (SEQ ID NO: 89)
    gi|330941564 acetyl-CoA MHDVVIVAATRTAVGSFQGSLASVAAVDLGAAVIRQLLARTGVDGAQVDEVIMGQVLTA
    acetyltransferase GAGQNPARQAAIKAGLPFSVPAMTLNKVCGSGLKALHLATQAIRCGDAEIIIAGGQENMSL
    [Pseudomonas SNYVLPGARTGLRMGHASMVDTMITDGLWDAFNDYHMGITAENLAQQYDISREAQDEF
    syringae pv. AALSQQKALAAIEAGRFVDEITPILIPQRKGDPLSFATDEQPRAGTTAETLAKLKPAFKKDGT
    pisi str. 1704B] VTAGNASSLNDGAAAVMLMSAARAEQLGLPVLARIAAYANAGVDPAIMGIGPVSATRRCL
    NKAGWSLADLDLIEANEAFAAQSLSVGKELGLDPQKLNVNGGAIALGHPIGASGCRVLVTL
    LHEMIRRDVKKGLATLCIGGGQGVALALER (SEQ ID NO: 90)
    gi|27375337 atoB gene MPMSDDVVIVSAARTPVGSFNGAFATLPAHDLGAVAIKAALERGGIEPGRVSEVIMGQILT
    product AAQGQNPARQASIAAGIPVESPAWGVNQLCGSGLRTVALGYQALLNGDSEIVVAGGQES
    [Bradyrhizobium MSMAPHAQYLRGGVKMGALEFIDTMIKDGLWDAFNGYHMGNTAENVARQWQITRAQ
    japonicum QDEFAVASQQKAEAAQKAGKFNDEIVPVTIKTRKGDVVVSADEYPRHGATLDAMAKLRPA
    USDA 110] FEKDGTVTAGSASGINDGAAAVVLMTAKQAAKEGKKPLARIVSWAQAGVDPKIMGSGPIP
    ASRAALKKAGWNVGDLDLIEANEAFAAQACAVNKDLGWDTSKVNVNGGAIAIGHPVGAS
    GARVLVTLLHEMQKRDSKKGLATLCIGGGMGIAMCLARD (SEQ ID NO: 91)
    gi|163738904 Acetyl-CoA C- MTNVVIASAARTAVGSFGGAFAKTPAHDLGAAVLQAVVERAGIDKSEVSETILGQVLTAAQ
    acetyltransferase GQNPARQAHINAGLPQESAAWSLNQVCGSGLRAVALAAQHIQLGDAAIVCAGGQENMT
    [Phaeobacter LSPHAANLRAGHKMGDMSYIDTMIRDGLWDAFNGYHMGQTAENVAEKWQISREMQD
    gallaeciensis EFAVASQNKAEAAQKAGKFADEIAAFTVKTRKGDIIVDQDEYIRHGATIEAMQKLRPAFAK
    BS107] DGSVTAANASGLNDGAAATLLMSADDAEKRGIEPLARIASYATAGLDPSIMGVGPIYASRK
    ALEKAGWSVDDLDLVEANEAFAAQACAVNKDMGWDPAIVNVNGGAIAIGHPIGASGCR
    VLNTLLFEMKRRDAKKGLATLCIGGGMGVAMCVERP (SEQ ID NO: 92)
    gi|7766963 A Chain A, SIVIASAARTAVGSFNGAFANTPAHELGATVISAVLERAGVAAGEVNEVILGQVLPAGEGQ
    Unliganded NPARQAAMKAGVPQEATAWGMNQLCGSGLRAVALGMQQIATGDASIIVAGGMESMS
    Biosynthetic MAPHCAHLRGGVKMGDFKMIDTMIKDGLTDAFYGYHMGTTAENVAKQWQLSRDEQDA
    Thiolase From FAVASQNKAEAAQKDGRFKDEIVPFIVKGRKGDITVDADEYIRHGATLDSMAKLRPAFDKE
    Zoogloea GTVTAGNASGLNDGAAAALLMSEAEASRRGIQPLGRIVSWATVGVDPKVMGTGPIPASRK
    Ramigera ALERAGWKIGDLDLVEANEAFAAQACAVNKDLGWDPSIVNVNGGAIAIGHPIGASGARIL
    NTLLFEMKRRGARKGLATLCIGGGMGVAMCIESL (SEQ ID NO: 93)
    gi|218892041 atoB gene MQDVVIVAATRTAVGSFQGSLAGIPAPELGAAVIRRLLEQTGLDAGQVDEVILGQVLTAGS
    product GQNPARQAAIKAGLPVGVPAMTLNKVCGSGLKALHLGAQAIRCGDAEVIVAGGQENMSL
    [Pseudomonas APYVMPGARTGLRMGHAKLVDSMIEDGLWDAFNDYHMGITAENLAEKYGLSREEQDAF
    aeruginosa AAASQQKAIAAIEGGRFRDEITPIQVPQRKGEPLSFDTDEQPRAGTTVEALAKLKPAFRKDG
    LESB58] SVTAGNASSLNDGAAAVLLMSAAKAKALGLPVLARIASYASAGVDPAIMGIGPVSATRRAL
    DKAGWSLEQLDLIEANEAFAAQSLAVGRELGWDAARVNVNGGAIALGHPIGASGCRVLVT
    LLHEMIRRDAKKGLATLCIGGGQGVALTLARD (SEQ ID NO: 94)
    gi|374292777 phbA3 gene MTEVVIAGAARTPIGSFNGALSAVPAHVLGEVAIREALARAKTDAAEVDEVILGQILTAGQG
    product QNPARQAAVNAGIPVEATAMGINQLCGSGLRAVALGYQAIKNGDADVLVVGGQESMSM
    [Azospirillum APHVMHLRNGTKMGSAELLDTMLRDGLTDAFHGYHMGTTAENVAQKWQLTREEQDAF
    lipoferum 413] AAASQQKAEAAQKAGRFKDEIVPVTIKGRKGDVVVSDDEYPKHGTTPESLAKLRPAFSKDG
    TVTAGNASGINDGAAALVLMTAENAAKRGVTPLARIVSWATAGVDPAIMGTGPIPASRKA
    LEKAGWTVDDLDLIEANEAFAAQALSVNKDLGWDTSKVNVNGGAIALGHPVGASGARVL
    TTLLYEMQKRDAKKGLATLCIGGGMGIALCVQRD (SEQ ID NO: 95)
    gi|17546351 phbA gene MTDVVIVSAVRTAVGKFGGSLAKIPAPELGAAVIREALSRAKVAPDQVSEVIMGQVLTAGS
    product GQNPARQALIKAGLPDMVPGMTINKVCGSGLKAVMLAANAIVAGDADIVVAGGQENMS
    [Ralstonia AAPHVLPGSRDGFRMGDTKLIDSMIVDGLWDVYNQYHMGITAENVAKQYGITREAQDAF
    solanacearum AVASQNKAEAAQKSGRFNDEIVPILIPQRKGDPIAFAQDEFVRHGATLESMTGLKPAFDKA
    GM11000] GTVTAANASGLNDGGAAVVVMSAARAKELGLTPLATIRAYANAGVDPKVMGMGPVPAS
    KRCLSRAGWSVGDLDLMEINEAFAAQALAVHQQMGWDTAKVNVNGGAIAIGHPIGASG
    CRILVTLLHEMQKRDAKKGLASLCIGGGMGVALAVERP (SEQ ID NO: 96)
    gi|221198056 Acetyl-CoA MTDVVIVSAARTAVGKFGGSLAKVAAPELGATVIRAVLERAGVKPEQVSEVIMGQVLTAGS
    acetyltransferase GQNPARQSLIKAGLPSAVPGMTINKVCGSGLKAVMLAANAIVAGDAEIVVAGGQENMSA
    [Burkholderia APHVLPGSRDGFRMGDAKLVDTMIVDGLWDVYNQYHMGITAENVAKEYGITREEQDAF
    multivorans AALSQNKAEAAQKAGRFNDEIVPVSIPQRKGEPLQFATDEFVRHGVTAESLAGLKPAFAKD
    CGD2M] GTVTAANASGINDGAAAVLVMSAQKAQALGLTPLARIKAYANAGVDPSVMGMGPVPAS
    RRCLERAGWTPGDLDLMEINEAFAAQALAVHKQMGWDTSKVNVNGGAIAIGHPIGASG
    CRILVTLLHEMVKRDAKRGLASLCIGGGMGVALAVERP (SEQ ID NO: 97)
    gi|163852882 acetyl-CoA MAASEDIVIVGAARTPVGSFAGAFGSVPAHELGATAIKAALERAGVSPDDVDEVIFGQVLT
    acetyltransferase AAAGQNPARQAAIAAGIPEKATAWGLNQVCGSGLRTVAVGMQQIANGDAKVIVAGGQE
    [Methylobacterium SMSLSPHAQYLRGGQKMGDLKLVDTMIKDGLWDAFNGYHMGQTAENVAQAFQLTREQ
    extorquens QDQFAVRSQNKAEAARKEGRFKEEIVPVTVKGRKGDTVVDTDEYIRDGATVEAMAKLKPA
    PA1] FAKDGTVTAANASGLNDGAAALVLMSASEAERRGITPLARIVSWATAGVDPKVMGTGPIP
    ASRKALEKAGWKPADLDLIEANEAFAAQALAVNKDMGWDDEKVNVNGGAIAIGHPIGAS
    GARVLITLLHELKRRDAKKGLATLCIGGGMGVAMCVERV (SEQ ID NO: 98)
    gi|169344179 acetyl-CoA MREVVIASAVRTALGSFGGSLKDVPAVDLGALVIKEALNKAGVKPECVDEVLMGNVIQAGL
    acetyltransferase GQNPARQAAVKAGLPVEIPSMTINKVCGSGLRCVALAAQMIKAGDADVIVAGGMENMS
    [Clostridium QGPYVLRTARFGQRMGDGKMVDAMVNDALTDAFNGYHMGITAENIAEQWGLTREMQ
    perfringens C DEFAANSQIKAEAAIKAGKFKDEIVPVVIPQRKGDPIVFDTDEFPRFGTTAEKLAKLRPAFKK
    str. JG51495] DGTVTAGNASGINDGAAALVVMSAEKAKELGVTPICKIVSYGSKGLDPSIMGYGPFYATKK
    ALEGTGLKVEDLDLIEANEAFAAQSLAVAKDLEFDMSKVNVNGGAIALGHPVGASGARILV
    TLLHEMMKRDAKRGLATLCIGGGMGTALIVER (SEQ ID NO: 99)
    gi|345869447 acetyl-CoA MSENIVIVDAGRTAIGTFGGSLSSLPATELGTTVLKALLARTGIAPDQIDEVILGQVLTAGVG
    acetyltransferase QNPARQTTLKAGLPHAVPAMTINKVCGSGLKAVHLAMQAVACGDADIVIAGGQECMSQ
    [Thiorhodococcus SSHVLPRSRDGQRMGDWKMVDTMIVDGLWDAFNQYHMGVTAENIAKQFGFTREAQD
    drewsii TFAAESQQKAEAAIKAGRFKDEIVPVSIPQRKGDPLVVDTDEFPRAGTTAAGLGKLRPAFDK
    AZ1] EGTVTAGNASGINDGAAMVVVMKESKAKELGLKPMARIVAFASAGVDPAIMGTGPIPAST
    KCLEKAGWTPADLDLIEANEAFAAQAMSVNKEMGWDLSKVNVNGGAISLGHPIGASGAR
    VLVTLLHEMQHRDAKKGLATLCIGGGQGVALAVERL (SEQ ID NO: 100)
  • TABLE 3
    Exemplary Acetoacetyl Coenzyme A Reductase Amino Acid Sequences
    Genbank Gene Name/
    Accession # Organism Amino Acid Sequence (SEQ ID NO: #)
    gi|52209584 acetoacetyl- MSQRIAYVTGGMGGIGTSICQRLHKDGFRVVAGCGPNSPRRVKWLEDQKALGFDFYAS
    CoA EGNVGDWDSTKQAFDKVKAEVGEIDVLVNNAGITRDVVFRKMTREDWQAVIDTNLTSL
    reductase FNVTKQVIDGMVERGWGRIINISSVNGQKGQFGQTNYSTAKAGIHGFTMSLAQEVATK
    [Burkholderia GVTVNTVSPGYIGTDMVKAIRPDVLEKIVATIPVRRLGSPDEIGSIVAWLASEESGFSTGAD
    pseudomallei FSLNGGLHMG (SEQ ID NO: 101)
    K96243]
    gi|296445576 acetoacetyl- MGRTAVVTGGTRGIGEAISKALKAAGYNVAATYAGNDEAANKFKDATGIPVYKFDVSDY
    CoA DACAAALAAIETDLGPVDVLVNNAGITKDRLFHKMELAQWRAVIDTNLNSLFNVTRPVI
    reductase NGMRDRGFGRIIVISSINGQKGQAGQTNYSASKAGDIGFVKALAQESAAKGITVNAIAPG
    [Methylosinus YIATEMVKAVPQEVLDKHIIPHIAVGRLGEPEEIARAVVFLASDEAGFITGSTLTINGGQYLT
    trichosporium (SEQ ID NO: 102)
    OB3b]
    gi|206559226 putative MTKRIAVVTGGMGGLGEAVSIRLNDAGHRVVVTYSPNNTGADRWLTEMHAAGREFHA
    Acetoacetyl- YPVDVADHDSCQQCIEKIVRDVGPVDILVNNAGITRDMTLRKLDKVNWDAVIRTNLDSV
    CoA FNMTKPVCDGMVERGWGRIVNISSVNGSKGSVGQTNYAAAKAGMHGFTKSLALEIAR
    reductase KGVTVNTVSPGYLATKMVTAIPQDILDTKILPQIPAGRLGKPEEVAALVAYLCSEEAGFVT
    [Burkholderia GSNIAINGGQHMH (SEQ ID NO: 103)
    cenocepacia
    J2315]
    gi|340047249 acetoacetyl- MRKIALITGSKGGIGSAISTQLVSEGYRVIATYYTGNYQCALDWFNEKQFTEDQVRLLELD
    CoA VTNTEECAERLAKLLEEEGTIDVVVNNAGITRDSVFKKMPHQAWKEVIDTNLNSVFNVT
    reductase QPLFAAMCEKGFGRIINISSVNGLKGQFGQTNYSAAKAGMIGFSKALAAEGARYGVTVN
    family protein VIAPGYTLTPMVEQMRAEVLQSIVDQVPMKRLAKPEEIANAVSYLASDAAYITGETLSVN
    [Vibrio GGLYMR (SEQ ID NO: 104)
    cholerae
    HE48]
    gi|356882300 acetoacetyl- MARVAVVTGGTRGIGEAISVALKNAGYVVAANYAGNDEKAKEFSARTGIAVYKFDVSDF
    coA reductase DAVKDGIAKISAELGPVDVVVNNAGITRDGVIHRMTPQQWNDVIATNLTSCFNLCRNVI
    [Azospirillum DGMRERGFGRIVNIGSVNGQAGQYGQVNYAAAKSGIHGFTKALAQEGAAKGVTVNAI
    brasilense APGYIDTDMVRAVPPNVLEKIVARIPVGRLGKAEEIARGVLFLVGDDAGFITGSTLSINGG
    Sp245] QHMY (SEQ ID NO: 105)
    gi|356881146 acetoacetyl- MSQKIALVTGAMGGLGTAICQALAKDGYIVAANCLPNFEPAAAWLGQQEALGFKFYVA
    coA reductase EGDVSDFESCKAMVAKIEADLGPVDILVNNAGITRDKFFAKMEKAQWDAVIATNLSSLF
    [Azospirillum NVTQQVSAKMAERGWGRIINISSVNGVKGQAGQTNYSAAKAGVIGFTKALAAELATKG
    brasilense VTVNAIAPGYIGTDMVMAIREDIRQAITDSVPMKRLGRPDEIGGAVSYLASEIAGYVTGST
    Sp245] LNINGGLNYQ (SEQ ID NO: 106)
    gi|119897313 phbB1 gene MSRVALVTGGMGGLGEAICIKLAALGYRVVTTYSPGNSKAAEWLQAMNNMGYGFRGY
    product PCDVSDFDSCKACIAQVTEEVGPIDVLVNNAGITRDMTFKKMTKADWDAVISTNLDSVF
    [Azoarcus sp. NMTKQVMDGMVERKWGRVINVSSVNGQKGAFGQTNYSAAKAGMHGFTKALALEVA
    BH72] RSGVTVNTISPGYIGTKMVMAIPQEILESKILPQIPVSRLGKPEEIAGLVAYLSSDEAAFVTG
    ANISINGGQHMF (SEQ ID NO: 107)
    gi|194289469 acetyacetyl- MTQRIAYVTGGMGGIGTAICQRLARDGFRVVAGCGPNSPRREKWLEQQKALGFDFVAS
    CoA EGNVADWDSTKAAFDKVKAEVGEVDVLINNAGITRDVVFRKMTRADWDAVIDTNLTSL
    reductase FNVTKQVIDGMADRGWGRIVNISSVNGQKGQFGQTNYSTAKAGLHGFTMALAQEVAT
    [Cupriavidus KGVTVNTVSPGYIATDMVKAIRQDVLDKIVGTIPVKRLGEPEEIASICAWLASEESGFSTGA
    taiwanensis DFSLNGGLHMG (SEQ ID NO: 108)
    LMG 19424]
    gi|307609363 hypothetical MDKMIAIVTGGTGGIGSAISQRLADSYQVVACYYKDGRHEEAKKWQDEQKQLGYDIDIV
    protein YGDIAQYSDCEKITSLVMERYGRIDVLVNNAGITKDCSLRKMTPQQWQQVLDANLTSVF
    LPW_06391 NMTRNVVPVMLERGYGRIISISSINGRKGQFGQCNYASTKAALFGFTKSLALEVASKGITV
    [Legionella NTVSPGYIETPMLAALKEDVLNSIISSIPVGRLGYPKEIADAVAFLASPDSGFITGANLDVN
    pneumophila GGQYM (SEQ ID NO: 109)
    130b]
    gi|352104657 acetoacetyl- MTNQAPVAWVTGGTGGIGTAICRSLADAGYLVVAGYHNPDKAKTWLETQRADGYNNI
    CoA ELSGVDLSDHNACLEGAREIHDKYGPISVLVNCAGITRDGTMKKMSYEQWYEVLDTNLN
    reductase SVFNTCRSVIEMMLENGYGRIINISSINGRKGQFGQVNYAAAKAGMHGLTMSLAQETAT
    [Halomonas KGITVNTVSPGYIATDMIMNIPEKVREAIRETIPVKRYGTPEEIGRLVTFLADKESGFITGAN
    sp. HAL1] IDINGGQFMG (SEQ ID NO: 110)
    gi|289671313 acetoacetyl- MTSRVALVTGGTGGIGTAICKRLADQGHRVASNFRNEEKARDWQQRMQAQGYAFALF
    CoA RGDVASSEHARALVEEVEASLGPIEVLVNNAGITRDTTFHRMTAEQWHEVINTNLNSVF
    reductase NVTRPVIEGMRKRGWGRVIQISSINGLKGQYGQANYAAAKAGMHGFTISLARENAAFG
    [Xanthomonas VTVNTVSPGYVATDMVMAVPEEVRAKIVADIPTGRLGRPEEIAYAVAFLVAEEAAWITGS
    campestris NLDINGGHHMGW (SEQ ID NO: 111)
    pv.
    musacearum
    NCPPB 4381]
    gi|330824321 acetoacetyl- MNTTQRTALVTGGNRGLGAAIARALHDAGHRVIVTHTPGNTTIGQWQQAQATQGYKF
    CoA AAYGVDVSNYESTQELARRIHADGHRIDILVNNAGITRDATLRKLDKAGWDAVLRTNLDS
    reductase MFNVTKPFIDPMVERGWGRIVNISSINGSKGQFGQTNYSAAKAGVHGFTKALAQEVAR
    [Alicycliphilus KGVTVNTVSPGYLATEMVMAVREDMRQKIIDAIPVGRLGQPDEIAALVAFIASEAAAFM
    denitrificans TGSNVAMNGGQHMY (SEQ ID NO: 112)
    K601]
    gi|146278501 acetoacetyl- MSKVALVTGGSRGIGAAISLALKNAGYTVAANYAGNDEAAQKFTAETGIKTYKWSVADY
    CoA DACAEGIARVEAELGPVAVLVNNAGITRDSMFHKMTREQWKEVIDTNLSGLFNMTHPV
    reductase WSGMRDRKFGRIINISSINGQKGQAGQANYSAAKAGDLGFTKALAQEGARAGITVNAIC
    [Rhodobacter PGYIGTEMVRAIDEKVLNERIIPQIPVGRLGEPEEIARCVVFLASDDAGFITGSTITANGGQ
    sphaeroides YFT (SEQ ID NO: 113)
    ATCC 17025]
    gi|67458545 phbB gene MSEIAIVTGGTRGIGKATALELKNKGLTVVANFFSNYDAAKEMEEKYGIKTKCWNVADFE
    product ECRQAVKEIEEEFKKPVSILVNNAGITKDKMLHRMSHQDWNDVINVNLNSCFNMSSSV
    [Rickettsia MEQMRNQDYGRIVNISSINAQAGQVGQTNYSAAKAGIIGFTKALARETASKNITVNCIAP
    felis GYIATEMVGAVPEDVLAKIINSIPKKRLGQPEEIARAVAFLVDENAGFITGETISINGGHN
    URRWXCal2] MI (SEQ ID NO: 114)
    gi|94497737 Acetoacetyl- MSRVAIVTGGTRGIGEAISLALKEMGYAVAANYAGNDEKAKAFTDKTGIAAFKWDVGD
    CoA HQACLDGCAQVAEVLGPVDIVVNNAGITRDGVLAKMSFDDWNEVMRINLGGCFNMA
    reductase KACFGGMRERGWGRIVNIGSINGQAGQYGQVNYAAAKSGIHGFTKALAQEGAKYGVT
    [Sphingomonas VNAIAPGYIDTDMVAAVPAPVLEKIVAKIPVGRLGQAHEIARGVAFFCSEDGGFVTGSTLS
    sp. SKA58] INGGQHMY (SEQ ID NO: 115)
    gi|28901060 acetoacetyl- MKKVALITGSKGGIGSAISSQLVNDGYRVIATYFTGNYECALEWFNSKGFTKDQVRLFELD
    CoA VTNTAECAEKLAQLLEEEGTIDVVVNNAGITRDGVFKKMTAQAWNDVINTNLNSLFNVT
    reductase QPLFAAMCEKGGGRVINISSVNGLKGQFGQANYSAAKAGMIGFSKALAYEGARSGVTV
    [Vibrio NVIAPGYTGTPMVEQMKPEVLESITNQIPMKRLATPEEIAASVSFLVSDAGAYITGETLSV
    parahaemolyticus NGGLYMH (SEQ ID NO: 116)
    RIMD
    2210633]
    gi|161522918 acetoacetyl- MSAKRVAFVTGGMGGLGAAISRRLHDVGMTVAVSHTEGNDHVATWLTHEREAGRTF
    CoA HAFEVDVADYDSCRQCASRVLAEFGRVDVLVNNAGITHDATFVKMTKSMWDAVLRTN
    reductase LDGMFNMTKPFVPGMIEGGFGRIVNIGSVNGSRGAYGQTNYAAAKAGIHGFTKALALEL
    [Burkholderia ARHGVTVNTVAPGYLATAMLETVPKEVLDTKILPQIPVGRLGNPDEIAALVAFLCSDAAAF
    multivorans ATGAEFDVNGGMHMK (SEQ ID NO: 117)
    ATCC 17616]
    gi|161524658 acetyacetyl- MSQRIAYVTGGMGGIGTSICQRLSKDGFKVVAGCGPNSPRRVKWLEEQKALGFDFIASE
    CoA GNVGDWDSTKAAFDKVKAEVGEIDVLVNNAGITRDVVFRKMTHEDWTAVIDTNLTSLF
    reductase NVTKQVIDGMVERGWGRIINISSVNGQKGQFGQTNYSTAKAGIHGFTMALAQEVATKG
    [Burkholderia VTVNTVSPGYIGTDMVKAIRPDVLEKIVATIPVRRLGTPEEIGSIVAWLASNDSGFATGAD
    multivorans FSLNGGLHMG (SEQ ID NO: 118)
    ATCC 17616]
    gi|351728759 3-ketoacyl- MSQKVAYVTGGMGGIGTAICQRLHKEGFKVIAGCGPTRDHAKWLAEQKALGYTFYASV
    (acyl-carrier- GNVGDWDSTVEAFGKTKAEHGTIDVLVNNAGITRDRMFLKMSREDWDAVIETNLNSM
    protein) FNVTKQVVADMVEKGWGRIVNISSVNGEKGQAGQTNYSAAKAGMHGFSMALAQELA
    reductase TKGVTVNTVSPGYIGTDMVKAIRPDVLEKIVATVPVKRLGEPSEIASIIAWLASEEGGYATG
    [Acidovorax ADFSVNGGLHMG (SEQ ID NO: 119)
    radicis N35]
    gi|240140211 phaB gene MAQERVALVTGGTRGIGAAISKRLKDKGYKVAANYGGNDEAANAFKAETGIPVFKFDVG
    product DLASCEAGIKAIEAELGPIDILVNNAGITRDGAFHKMTFEKWQAVIRTNLDSMFTCTRPLI
    [Methylobacterium EGMRSRNFGRIIIISSINGQKGQAGQTNYSAAKAGVIGFAKALAQESASKGVTVNVVAPG
    extorquens YIATEMVMAVPEDIRNKIISTIPTGRLGEADEIAHAVEYLASDEAGFVNGSTLTINGGQHF
    AM1] V (SEQ ID NO: 120)
    gi|148258780 3-oxoacyl- MARVALVTGGTRGIGAAISKALKAAGHKVAANYGGNDAAAEKFKSETEIPVYKWDVSSF
    ACP DACAEGIKKVEAELGPVDILVNNAGITRDTAFHKMTLEQWSAVINTNLGSLFNMTRPVIE
    reductase GMRARKFGRIINISSINGQKGQFGQVNYSAAKAGDIGFTKALALETAKAGITVNVICPGYI
    [Bradyrhizobium NTEMVQAVPKDVLEKAILPLIPVGRLGEPEEIARAVVFLAADEAGAITGSTLSINGGQYMA
    sp. BTAi1] (SEQ ID NO: 121)
    gi|126728325 Acetoacetyl- MARVALVTGGSRGIGEAISKALKAEGYTVAATYAGNDEKAAAFTADTGIKTYKWNVADY
    CoA ESSKAGIAQVEADLGPIDVVVANAGITRDAPFHKMTPAQWNEVIDTNLTGVFNTVHPV
    reductase WPGMRERKFGRIIVISSINGQKGQFAQVNYAATKAGDLGIVKSLAQEGARAGITANAICP
    [Sagittula GYIATEMVMAVPEKVRESIIGQIPAGRLGEPEEIARCVVFLASDDAGFINGSTISANGAQF
    stellata E-37] FV (SEQ ID NO: 122)
    gi|15895965 hbd gene MKKVCVIGAGTMGSGIAQAFAAKGFEVVLRDIKDEFVDRGLDFINKNLSKLVKKGKIEEA
    product TKVEILTRISGTVDLNMAADCDLVIEAAVERMDIKKQIFADLDNICKPETILASNTSSLSITE
    VASATKRPDKVIGMHFFNPAPVMKLVEVIRGIATSQETFDAVKETSIAIGKDPVEVAEAPG
    FVVNRILIPMINEAVGILAEGIASVEDIDKAMKLGANHPMGPLELGDFIGLDICLAIMDVLY
    SETGDSKYRPHTLLKKYVRAGWLGRKSGKGFYDYSK (SEQ ID NO: 123)
  • In certain embodiments, a non-naturally occurring C1 metabolizing organism according to any of the embodiments disclosed herein is a C1 metabolizing bacterium selected from Methylosinus trichosporium strain OB3b, Methylococcus capsulatus Bath strain, Methylomonas methanica 16A strain, Methylosinus trichosporium (NRRL B-11,196), Methylosinus sporium (NRRL B-11,197), Methylocystis parvus (NRRL B-11,198), Methylomonas methanica (NRRL B-11,199), Methylomonas albus (NRRL B-11,200), Methylobacter capsulatus (NRRL B-11,201), Methylobacterium organophilum (ATCC 27,886), Methylomonas sp AJ-3670 (FERM P-2400), Methylocella silvestris, Methylacidiphilum infernorum, Methylomicrobium alcaliphilum, or Methylibium petroleiphilum.
  • In certain embodiments, a non-naturally occurring C1 metabolizing organism may be a syngas or CO utilizing bacterium that naturally possesses the ability to utilize syngas or CO, such as Clostridium autoethanogenum, Clostridium ljungdahli, Clostridium ragsdalei, Clostridium carboxydivorans, Butyribacterium methylotrophicum, Clostridium Woodii, Clostridium neopropanologen Ralstonia eutropha, or Eurobacterium limosum.
  • In certain embodiments, a non-naturally occurring C1 metabolizing organism may be a methylotrophic bacterium, such as Methylobacterium extorquens, Methylobacterium radiotolerans, Methylobacterium populi, Methylobacterium chloromethanicum, or Methylobacterium nodulans.
  • In another embodiment, the present disclosure provides non-naturally occurring microbial organisms that have been genetically modified with a novel metabolic pathway for producing propylene from a carbon substrate. More specifically, the non-naturally occurring microbial organisms include an exogenous nucleic acid encoding 4-oxalocrotonate decarboxylase and convert a carbon substrate to propylene. As described previously, 4-OD is used in a novel propylene biosynthetic pathway to catalyze decarboxylation of crotonic acid to propylene and CO2 (see FIG. 1). Sources of 4-OD encoding nucleic acid molecules may include any species, prokaryotic or eukaryotic, where the encoded gene product is capable of catalyzing decarboxylation of crotonic acid to propylene and CO2. Exemplary amino acid sequences of 4-OD are shown in FIG. 2.
  • In certain embodiments, the present disclosure provides a non-naturally occurring microbial organism containing an exogenous nucleic acid encoding a 4-oxalocrotonate decarboxylase, wherein the non-naturally occurring microbial organism is capable of converting a carbon substrate into propylene.
  • In certain embodiments, non-naturally occurring microbial organisms that include an exogenous nucleic acid encoding a 4-oxalocrotonate decarboxylase and convert a carbon substrate into propylene may further include an exogenous nucleic acid encoding crotonase, or further include an exogenous nucleic acid encoding a crotonase and an exogenous nucleic acid encoding a crotonyl thioesterase. Depending on the host microbial organism selected, a microbial organism may or may not have endogenous enzyme(s) that would participate with 4-OD in forming a biosynthetic propylene synthesis pathway. As described in detail previously, crotonase catalyzes the dehydration of 3-hydyroxybutyryl-CoA to crotonyl-CoA. Crotonyl-CoA thioesterase catalyzes the conversion of crotonyl-CoA to crotonic acid. For example, if a host microbial organism selected is deficient in crotonase, then exogenous expression of crotonase can be included in the microbial organism. In another example, if a host microbial organism is deficient in crotonase and a thioesterase capable of converting crotonyl-CoA to crotonic acid, then exogenous expression of crotonase and crotonyl-CoA thioesterase can be included in the microbial organism. However, it is understood that exogenous expression of all of these enzymes of a propylene biosynthetic pathway (i.e., 4-OD, crotonase, and crotonyl-CoA thioesterase) may be included, even if the host microbial organism contains at least one of the propylene pathway enzymes (e.g., crotonase or crotonyl thioesterase). Expression of exogenous nucleic acids encoding enzymes of the propylene biosynthetic pathway disclosed herein is in a sufficient amount to produce propylene. Sources of crotonase and crotonyl-CoA thioesterase encoding nucleic acids may include any species, prokaryotic or eukaryotic, where the encoded gene products are capable of catalyzing dehydration of 3-hydyroxybutyryl-CoA to crotonyl-CoA and conversion of crotonyl-CoA to crotonic acid, respectively. Exemplary amino acid sequences for crotonase and crotonyl-CoA thioesterase are shown in FIG. 4 and FIG. 3, respectively.
  • In a further embodiment, non-naturally occurring microbial organisms as described herein do not have a functional PHB synthase or a substantial amount of functional PHB synthase. As described in detail previously, by inhibiting or reducing PHB function in a microbial organism, propylene synthesis yields may be increased by funneling more 3-hydroxybutyryl-CoA into the propylene pathway via conversion to crotonyl-CoA and to crotonic acid and to propylene (see FIG. 1).
  • Additionally, if non-naturally occurring microbial organisms as described herein do not possess an endogenous PHB synthesis pathway, then non-naturally occurring microbial organisms may be genetically modified to include an exogenous nucleic acid encoding β-ketothiolase and an exogenous nucleic acid encoding acetoacetyl-CoA reductase to provide the capability of producing 3-hydroxybutyrl-CoA, substrate for the crotonase enzyme in the propylene synthesis pathway described herein. Non-naturally occurring microbial organisms that do possess an endogenous PHB synthesis pathway may also be genetically modified with an exogenous nucleic acid encoding β-ketothiolase and an exogenous nucleic acid encoding acetoacetyl-CoA reductase to increase expression of these enzymes. In a specific embodiment, β-ketothiolase is encoded by phaA or phbA. In another specific embodiment, acetoacetyl coenzyme A reductase is encoded by phaB or phbB. Exemplary β-ketothiolase and acetoacetyl coenzyme A reductase amino acid sequences are provided in Tables 2 and 3, respectively.
  • Nucleic acid sequences encoding for and amino acid sequences for proteins, protein domains and fragments thereof, for proteins described herein, such as 4-OD, crotonase, crotonyl thioesterase, acetoacetyl coenzyme A reductase, or β-ketothiolase, and domains thereof, that are described herein include natural and recombinantly engineered variants. These variants retain the function and biological activity (including enzymatic activities if applicable) associated with the parent (or wildtype) protein. These variants may have improved function and biological activity (e.g., higher enzymatic activity, improved specificity for substrate) than the parent (or wildtype protein). For example, a variant 4-OD enzyme may be engineered with reduced or eliminated decarboxylation activity on 4-oxalocrotonate, but retains or has increased decarboxylation activity on crotonic acid substrate. Conservative substitutions of amino acids are well known and may occur naturally in the polypeptide (e.g., naturally occurring genetic variants) or may be introduced when the polypeptide is recombinantly produced. Amino acid substitutions, deletions, and additions may be introduced into a polypeptide using well-known and routinely practiced mutagenesis methods (see, e.g., Sambrook et al. Molecular Cloning: A Laboratory Manual, 3d ed., Cold Spring Harbor Laboratory Press, NY 2001). Oligonucleotide-directed site-specific (or segment specific) mutagenesis procedures may be employed to provide an altered polynucleotide that has particular codons altered according to the substitution, deletion, or insertion desired. Deletion or truncation variants of proteins may also be constructed by using convenient restriction endonuclease sites adjacent to the desired deletion. Alternatively, random mutagenesis techniques, such as alanine scanning mutagenesis, error prone polymerase chain reaction mutagenesis, and oligonucleotide-directed mutagenesis may be used to prepare polypeptide variants (see, e.g., Sambrook et al., supra).
  • Differences between a wild type (or parent) nucleic acid or polypeptide and the variant thereof, may be determined by methods routinely practiced in the art to determine identity, which are designed to give the greatest match between the sequences tested. Methods to determine sequence identity can be applied from publicly available computer programs. Computer program methods to determine identity between two sequences include, for example, BLASTP, BLASTN (Altschul, S. F. et al., J. Mol. Biol. 215: 403-410 (1990), and FASTA (Pearson and Lipman Proc. Natl. Acad. Sci. USA 85; 2444-2448 (1988). The BLAST family of programs is publicly available from NCBI and other sources (BLAST Manual, Altschul, S., et al., NCBI NLM NIH Bethesda, Md.
  • Assays for determining whether a polypeptide variant folds into a conformation comparable to the non-variant polypeptide or fragment include, for example, the ability of the protein to react with mono- or polyclonal antibodies that are specific for native or unfolded epitopes, the retention of ligand-binding functions, the retention of enzymatic activity (if applicable), and the sensitivity or resistance of the mutant protein to digestion with proteases (see Sambrook et al., supra). Polypeptides, variants and fragments thereof, can be prepared without altering a biological activity of the resulting protein molecule (i.e., without altering one or more functional activities in a statistically significant or biologically significant manner). For example, such substitutions are generally made by interchanging an amino acid with another amino acid that is included within the same group, such as the group of polar residues, charged residues, hydrophobic residues, and/or small residues, and the like. The effect of any amino acid substitution may be determined empirically merely by testing the resulting modified protein for the ability to function in a biological assay, or to bind to a cognate ligand or target molecule.
  • It is understood that the non-naturally occurring microbial organisms or C1 metabolizing organisms that have been genetically modified as described herein may lead to the biosynthetic production of propylene, including other pathway intermediates (e.g., crotonate or crotonyl-CoA) and downstream products. Like other alkenes, propylene undergoes addition reactions relatively easily at room temperature due to the relative weakness of its double bond. Through polymerization, oxidation, halogenations and hydrohalogenation, alkylation, hydration, oligomerization, and hydroformylation reactions, which are well known to a person of skill in the art, propylene may be converted into other downstream products (e.g., polypropylene, propylene oxide). These addition reactions may occur spontaneously in the non-naturally occurring microbial organisms or C1 metabolizing organisms, or the organisms may be further genetically modified to add or enhance addition reaction capability (e.g., to increase conversion to polypropylene or propylene oxide). For example, in methanotrophic bacteria that are genetically modified with a biosynthetic propylene pathway, propylene that is produced may spontaneously be oxidized into propylene oxide via a methane-monooxygenase-catalyzed reaction (see, e.g., U.S. Patent Publication 2002/0168733, U.S. Patent Publication 2003/0203456). Alternatively, the non-naturally occurring microbial organisms or C1 metabolizing organisms may comprise further genetic modifications to inhibit or reduce endogenous enzyme activity that catalyze an addition reaction (e.g., to inhibit conversion to propylene oxide). In non-naturally occurring organisms that spontaneously convert or are genetically modified to convert propylene into a downstream product (e.g. propylene oxide), there may be little propylene product to recover and measure, and the downstream product (e.g., propylene oxide) may be recovered and measured as a surrogate for propylene production.
    • Methods of Producing Crotonic Acid or Propylene in Non-Naturally Occurring C1 Metabolizing Organisms
  • In certain embodiments, the present disclosure provides methods of producing propylene by culturing non-naturally occurring C1 metabolizing organisms according to any of the embodiments as described herein (e.g., capable of converting a C1 substrate into propylene), under conditions sufficient to produce propylene. In a specific embodiment, the non-naturally occurring C1 metabolizing organisms as disclosed herein produce from about 0.1 grams of propylene/L/day to about 50 grams of propylene/L/day. In another embodiment, the non-naturally occurring C1 metabolizing organisms as disclosed herein produce about 0.1 g, 0.5 g, 1 g, 2 g, 3 g, 4 g, 5 g, 6 g, 7 g, 8 g, 9 g, 10 g, 11 g, 12 g, 13 g, 14 g, 15 g, 16 g, 17 g, 18 g, 19 g, 20 g, 25 g, 30 g, 35 g, 40 g, 45 g, 50 g, 55 g, or 60 g propylene/L/day.
  • Additionally, the present disclosure provides methods of producing propylene in non-naturally occurring microbial organisms according to any of the embodiments as described herein (e.g., having a partially heterologous propylene biosynthetic pathway), by culturing the non-naturally occurring microbial organisms under conditions sufficient to produce propylene. In a specific embodiment, the non-naturally occurring microbial organisms as disclosed herein produce from about 0.1 grams of propylene/L/day to about 50 grams of propylene/L/day. In another embodiment, the non-naturally occurring microbial organisms as disclosed herein produce about 0.1 g, 0.5 g, 1 g, 2 g, 3 g, 4 g, 5 g, 6 g, 7 g, 8 g, 9 g, 10 g, 11 g, 12 g, 13 g, 14 g, 15 g, 16 g, 17 g, 18 g, 19 g, 20 g, 25 g, 30 g, 35 g, 40 g, 45 g, 50 g, 55 g, or 60 g propylene/L/day.
  • Also disclosed herein are methods of producing crotonic acid by culturing non-naturally occurring C1 metabolizing organisms under conditions sufficient to produce crotonic acid, wherein the organisms include an exogenous nucleic acid encoding crotonyl-CoA thioesterase. In a specific embodiment, the non-naturally occurring C1 metabolizing organisms as disclosed herein produces from about 0.1 grams of crotonic acid/L/day to about 50 grams of crotonic acid/L/day. In another embodiment, the non-naturally occurring C1 metabolizing organism as disclosed herein produces about 0.1 g, 0.5 g, 1 g, 2 g, 3 g, 4 g, 5 g, 6 g, 7 g, 8 g, 9 g, 10 g, 11 g, 12 g, 13 g, 14 g, 15 g, 16 g, 17 g, 18 g, 19 g, 20 g, 25 g, 30 g, 35 g, 40 g, 45 g, 50 g, 55 g, or 60 g crotonic acid/L/day.
    • Codon Optimization
  • Expression of recombinant proteins is often difficult outside their original host. For example, variation in codon usage bias has been observed across different species of bacteria (Sharp et al., 2005, Nucl. Acids. Res. 33:1141-1153). Over-expression of recombinant proteins even within their native host may also be difficult. In certain embodiments of the invention, nucleic acids (e.g., a nucleic acid encoding 4-OD, crotonyl-CoA thioesterase, or crotonase) that are to be introduced into organisms of the invention may undergo codon optimization to enhance protein expression. Codon optimization refers to alteration of codons in genes or coding regions of nucleic acids for transformation of an organism to reflect the typical codon usage of the host organism without altering the polypeptide for which the DNA encodes. Codon optimization methods for optimum gene expression in heterologous organisms have been previously described (see., e.g., Welch et al., 2009, PLoS One 4:e7002; Gustafsson et al., 2004, Trends Biotechnol. 22:346-353; Wu et al., 2007, Nucl. Acids Res. 35:D76-79; Villalobos et al., 2006, BMC Bioinformatics 7:285; U.S. Patent Publication 2011/0111413; U.S. Patent Publication 2008/0292918).
    • Transformation Methods
  • Non-naturally occurring microbial organisms as described herein may be transformed to comprise at least one exogenous nucleic acid to provide the host organism with a new or enhanced activity (e.g., enzymatic activity) or may be genetically modified to remove or substantially reduce an endogenous gene function (e.g., enzymatic activity) using a variety of methods known in the art. Recombinant methods for exogenous expression of nucleic acids in microbial organisms are well known in the art. Such methods can be found described in, for example, Sambrook et al., Molecular Cloning: A Laboratory Manual, Third Ed., Cold Spring Harbor Laboratory, New York (2001); and Ausubel et al., Current Protocols in Molecular Biology, John Wiley and Sons, Baltimore, Md. (1999).
  • A non-naturally occurring C1 metabolizing bacterium; non-naturally occurring obligate C1 metabolizing organism; non-naturally occurring C1 metabolizing organism, wherein the organism does not include Pichia pastoris; a non-naturally occurring methanotrophic or methylotrophic bacterium; or a non-naturally occurring CO utilizing bacterium as described herein may be transformed to comprise at least one exogenous nucleic acid to provide the host with a new or enhanced activity (e.g., enzymatic activity) or may be genetically modified to remove or substantially reduce an endogenous gene function (e.g., enzymatic activity) using a variety of methods known in the art. While genetic engineering tools of C1 metabolizing organisms are not as extensive as for other microbial organisms (e.g., E. coli), significant advances have been made allowing genetic manipulation of C1 metabolizing organisms, as summarized below.
  • Transformation refers to the transfer of a nucleic acid (e.g., exogenous nucleic acid) into the genome of a host organism, resulting in genetically stable inheritance. Host organisms containing the transformed nucleic acid are referred to as “non-naturally occurring” or “recombinant” or “transformed” or “transgenic” organisms.
  • Expression systems and expression vectors useful for the expression of heterologous nucleic acids in C1 metabolizing organisms are known. Vectors or cassettes useful for the transformation of suitable host organisms are available.
  • Electroporation of C1 metabolizing bacteria has been previously described in Toyama et al., 1998, FEMS Microbiol. Lett. 166:1-7 (Methylobacterium extorquens); Kim and Wood, 1997, Appl. Microbiol. Biotechnol. 48:105-108 (Methylophilus methylotrophus AS1); Yoshida et al., 2001, Biotechnol. Lett. 23:787-791 (Methylobacillus sp. strain 12S), and US2008/0026005 (Methylobacterium extorquens).
  • Bacterial conjugation, which refers to a particular type of transformation involving direct contact of donor and recipient cells, is more frequently used for the transfer of nucleic acids into C1 metabolizing bacteria. Bacterial conjugation involves mixing “donor” and “recipient” cells together in close contact with each other. Conjugation occurs by formation of cytoplasmic connections between donor and recipient bacteria, with unidirectional transfer of newly synthesized donor nucleic acids into the recipient cells. A recipient in a conjugation reaction is any cell that can accept nucleic acids through horizontal transfer from a donor bacterium. A donor in a conjugation reaction is a bacterium that contains a conjugative plasmid, conjugative transposon, or mobilized plasmid. The physical transfer of the donor plasmid can occur through a self-transmissible plasmid or with the assistance of a “helper” plasmid. Conjugations involving C1 metabolizing bacteria have been previously described in Stolyar et al., 1995, Mikrobiologiya 64:686-691; Motoyama et al., 1994, Appl. Micro. Biotech. 42:67-72; Lloyd et al., 1999, Archives of Microbiology 171:364-370; and Odom et al., PCT Publication WO 02/18617; Ali et al., 2006, Microbiol. 152:2931-2942.
  • Expression of heterologous nucleic acid molecules in C1 metabolizing bacteria is known in the art (see, e.g., U .S. Pat. No. 6,818,424, U.S. Patent Publication 2003/0003528). Mu transposon based transformation of methylotrophic bacteria has been described (see, e.g., Akhverdyan et al., 2011, Appl. Microbiol. Biotechnol. 91:857-871). A mini-Tn7 transposon system for single and multicopy expression of heterologous genes without insertional inactivation of host genes in Methylobacterium has been described (see, e.g. U.S. Patent Publication 2008/0026005).
  • Various methods for inactivating, knocking-out, or deleting endogenous gene function in C1 metabolizing organisms may be used. Allelic exchange using suicide vectors to construct deletion/insertional mutants in slow growing C1 metabolizing bacteria have also been described in Toyama and Lidstrom, 1998, Microbiol. 144:183-191; Stolyar et al., 1999, Microbiol. 145:1235-1244; Ali et al., 2006, Microbiology 152:2931-2942; Van Dien et al., 2003, Microbiol. 149:601-609.
  • Suitable homologous or heterologous promoters for high expression of exogenous nucleic acids may be utilized. For example, U.S. Pat. No. 7,098,005 describes the use of promoters that are highly expressed in the presence of methane or methanol for heterologous gene expression in C1 metabolizing bacteria. Additional promoters that may be used include deoxy-xylulose phosphate synthase methanol dehydrogenase operon promoter (Springer et al., 1998, FEMS Microbiol. Lett. 160:119-124); the promoter for PHA synthesis (Foellner et al. 1993, Appl. Microbiol. Biotechnol. 40:284-291); or promoters identified from native plasmid in methylotrophs (EP296484). Non-native promoters include the lac operon Plac promoter (Toyama et al., 1997, Microbiology 143:595-602) or a hybrid promoter such as Ptrc (Brosius et al., 1984, Gene 27:161-172). Regulation of expression of an exogenous nucleic acid molecule in the host C1 metabolizing organism may also be utilized. For example, an inducible/regulatable system of recombinant protein expression in methylotrophic and methanotrophic bacteria has been described in US Patent Publication 2010/0221813.
  • Methods of screening are disclosed in Brock, supra. Selection methods for identifying allelic exchange mutants are known in the art (see, e.g., U .S. Patent Publication No. 2006/0057726, Stolyar et al., 1999, Microbiol. 145:1235-1244; and Ali et al., 2006, Microbiology 152:2931-2942.
    • Culture Methods
  • A variety of culture methodologies may be used for the C1 metabolizing organisms described herein. For example, C1 metabolizing organisms, particularly methanotrophic or methylotrophic bacteria, may be grown by batch culture and continuous culture methodologies. In certain embodiments, the cultures are grown in a controlled culture unit, such as a fermentor, bioreactor, hollow fiber membrane bioreactor, or the like.
  • A classical batch culturing method is a closed system where the composition of the media is set at the beginning of the culture and not subject to external alterations during the culture process. Thus, at the beginning of the culturing process, the media is inoculated with the desired organism or organism and growth or metabolic activity is permitted to occur without adding anything to the system. Typically, however, a “batch” culture is batch with respect to the addition of carbon source and attempts are often made at controlling factors such as pH and oxygen concentration. In batch systems, the metabolite and biomass compositions of the system change constantly up to the time the culture is terminated. Within batch cultures, cells moderate through a static lag phase to a high growth logarithmic phase and finally to a stationary phase where growth rate is diminished or halted. If untreated, cells in the stationary phase will eventually die. Cells in log phase are often responsible for the bulk production of end product or intermediate in some systems. Stationary or post-exponential phase production can be obtained in other systems.
  • The Fed-Batch system is a variation on the standard batch system. Fed-Batch culture processes comprise a typical batch system with the modification that the substrate is added in increments as the culture progresses. Fed-Batch systems are useful when catabolite repression is apt to inhibit the metabolism of the cells and where it is desirable to have limited amounts of substrate in the media. Measurement of the actual substrate concentration in Fed-Batch systems is difficult and is therefore estimated on the basis of the changes of measureable factors, such as pH, dissolved oxygen, and the partial pressure of waste gases such as CO2. Batch and Fed-Batch culturing methods are common and known in the art (see, e.g., Thomas D. Brock, Biotechnology: A Textbook of Industrial Microbiology, 2nd Ed. (1989) Sinauer Associates, Inc., Sunderland, Mass.; Deshpande, 1992, Appl. Biochem. Biotechnol. 36:227, herein incorporated by reference).
  • Continuous cultures are “open” systems where a defined culture media is added continuously to a bioreactor and an equal amount of conditioned media is removed simultaneously for processing. Continuous cultures generally maintain the cells at a constant high liquid phase density where cells are primarily in logarithmic phase growth. Alternatively, continuous culture may be practiced with immobilized cells where carbon and nutrients are continuously added and valuable products, by-products, and waste products are continuously removed from the cell mass. Cell immobilization may be performed using a wide range of solid supports composed of natural and/or synthetic materials.
  • Continuous or semi-continuous culture allows for the modulation of one factor or any number of factors that affect cell growth or end product concentration. For example, one method will maintain a limited nutrient, such as the carbon source or nitrogen level, at a fixed rate and allow all other parameters to modulate. In other systems, a number of factors affecting growth can be altered continuously while the cell concentration, measured by media turbidity, is kept constant. Continuous systems strive to maintain steady state growth conditions and thus the cell loss due to media being drawn off must be balanced against the cell growth rate in the culture. Methods of modulating nutrients and growth factors for continuous culture processes, as well as techniques for maximizing the rate of product formation, are well known in the art, and a variety of methods are detailed by Brock, supra.
  • Culture media must contain carbon substrates for the C1 metabolizing organisms. Suitable substrates include, but are not limited to C1 substrates such as methane, methanol, formaldehyde, formic acid (formate), carbon monoxide, carbon dioxide, methylated amines (methylamine, dimethylamine, trimethylamine, etc.), methylated thiols, or methyl halogens (bromomethane, chloromethane, iodomethane, dichloromethane, etc.). In certain embodiments, a non-naturally occurring C1 metabolizing organism of any of the disclosed embodiments is capable of growth on methane, methanol, formaldehyde, formic acid, carbon monoxide, carbon dioxide, methylated amines, methylated thiols, or methyl halogens as a carbon source.
  • A culture media may comprise a single C1 substrate as the sole carbon source for the C1 metabolizing organism, or comprise a mixture of two or more C1 substrates (mixed C1 substrates) as multiple carbon sources for the C1 metabolizing organism. Additionally, some C1 metabolizing organisms are known to utilize non-C1 substrates, such as glucosamine and a variety of amino acids for metabolic activity. For example, some Candida species can metabolize alanine or oleic acid (Sulter et al., 1990, Arch. Microbiol. 153:485-489). Methylobacterium extorquens AM1 is capable of growth on a limited number of C2, C3, and C4 substrates (Van Dien et al., 2003, Microbiol. 149:601-609). Alternatively, a C1 metabolizing organism may be engineered with the ability to utilize alternative carbon substrates. Hence, it is contemplated that a culture media may comprise a mixture of carbon substrates, with single and multi-carbon compounds (mixed carbon sources), depending on the C1 metabolizing organism selected. In certain embodiments, a C1 substrate provided in a mixed carbon source may be a primary carbon source for a C1 metabolizing organism. A carbon source may be added to culture media initially, provided to culture media intermittently, or supplied continuously.
    • Propylene Separation and Recovery
  • Propylene or propylene oxide produced by the non-naturally occurring organisms described herein may be dissolved in the liquid phase or present as gas in the headspace of the culture container. Propylene may be mixed with other gases in the headspace, such as O2, CO2, H2O vapor, or methane. Methods for recovering propylene from a gas mixture have been previously described, and include for example, continuous liquid-liquid extraction, pervaporation, membrane filtration, membrane separation, reverse osmosis, electrodialysis, distillation, crystallization, centrifugation, extractive filtration, ion exchange chromatography, size exclusion chromatography, adsorption chromatography, and ultrafiltration (see., e.g., Bai et al., 2000, J. Memb. Sci. 174:67-79; Shi et al., 2006, J. Membr. Sci. 282:115-123; Membranes: Separation of Organic Vapors from Gas Streams, by Ohlrogge and Sturken, Ullmann's Encyclopedia of Industrial Chemistry, 2002, Wiley-VCH Verlag GmbH & Co., KGaA; U.S. Pat. No. 4,348,476; Hou et al., 1984, Applied Microbio. and Biotechnol. 19:1-4; each of the preceding references are incorporated herein by reference, in their entirety). A person skilled in the art can adapt propylene recovery methods used in fluidic cracking process (see, e.g., U.S. Pat. No. 3,893,905; U.S. Pat. No. 6,308,532; U.S. Pat. No. 6,730,142; U.S. Pat. No. 7,875,758) to recover propylene from a fermentation off-gas mixture.
    • Measuring Propylene Production
  • Methods for measuring propylene and propylene oxide production are well known in the art and include HPLC (high performance liquid chromatography), GC-MS (gas chromatography-mass spectrometry), GC-FID (gas chromatography-flame ionization detector) and LC-MS (liquid chromatography-mass spectrometry). Methods of measuring propylene and propylene oxide concentration have also been described in, for example, Brown et al., 1963, Anal. Chem. 35:2172-2176; Lin et al., 2000, J. Am. Chem. Soc. 122:11275-11285; Lee and Hwang, J. Membrane Sci. 73:37-45; U.S. Patent Publication 2010/0197986; U.S. Patent Publication 2003/0203456; U.S. Patent Publication 2002/0168733; Stanley and Dalton, 1992, Biocatalysis & Biotransformation 6:163-175; each of which is incorporated herein by reference in its entirety).
    • Measuring PHB Production
  • In certain embodiments, the non-naturally occurring organisms as described herein do not produce a substantial amount of polyhydroxybutyrate (PHB). As used herein, “not producing a substantial amount of polyhydroxybutyrate” means that an organism produces at least 40%, 45%, 50%, 55%, 60%, 65%, 70%, 75%, 80%, 85%, 90%, 95%, 99% less polyhydroxybutyrate as compared to a wildtype organism that has a polyhydroxybutyrate synthesis pathway. Methods for determining PHB concentration are well known in the art. Braunegg et al., (1978, European J. Appl. Microbiol. Biotechnol. 6:29-37) describe a gas chromatographic method for determining PHB concentration comprising a mild acid or alkaline methanolysis of PHB directly without previous extraction from the cells, which is followed by gas chromatography of the 3-hydroxybutyric acid methylester. A quantitative staining method for detecting PHB in viable cells has also been described (see., e.g., Tyo et al., 2006, Appl. Environ. Microbiol. 72:3412-3417). Stopped-flow attenuated total reflection FT-IR spectrometry has been used to determine intracellular PHB content in bacteria (see., e.g., Jarute et al., 2004, Anal. Chem. 76:6353-6358). Additional methods for measuring PHB have been described in Huang and Reusch, 1996, J. Biol. Chem. 271:22196-22202; Henneke et al., 2005, Bioprocess & Biosystems Engineering 27:359-364; Pieja et al., 2011, Appl. Environ. Microbiol. 77:6012-6019; Taguchi et al., 2001, FEMS Microbiol. Letters 198:65-71.
  • Additional methods for measuring PHB synthesis may include measuring PHB synthase expression (see., e.g., Langenbach et al., 1997, FEMS Microbiol. Lett. 150:303-309; Solaiman et al., 2008, J. Ind. Microbiol. & Biotechnol. 35:111-120) or enzyme activity (see., e.g., Schubert et al., 1988, J. Bacteriol. 170:5837-5847; Liebergesell et al., 1994, Eur. J. Biochem. 226:71-80; Valentin and Steinbuchel, 1994, Appl. Microbiol. Biotechnol. 40:699-709).
    • EXAMPLES Example 1 Methylosinus Trichosporium Methanotroph Preparation of NMS Media.
      • MgSO4.7H2O . . . 1.0 g
      • CaCl2.6H2O . . . 0.20 g
      • Chelated Iron Solution (see below) . . . 2.0 ml
      • KNO3. . . 1.0 g
      • Trace Element Solution (see below) . . . 0.5 ml
      • KH2PO4 . . . 0.272 g
      • Na2HPO4.12H2O . . . 0.717 g
      • Purified Agar (e.g., Oxoid L28) . . . 12.5 g
      • Distilled deionized water . . . 1.0 L
      • Adjust pH to 6.8. Autoclave at 121° C. for 15 minutes.
    Chelated Iron Solution:
      • Ferric (III) ammonium citrate* . . . 0.1 g
      • EDTA, sodium salt . . . 0.2 g
      • HCl (concentrated) . . . 0.3 ml
      • Distilled deionized water . . . 100.0 ml
      • *0.5 g of Ferric (III) chloride may be substituted.
      • Use 2.0 ml of this chelated iron solution per liter of final medium.
    Trace Element Solution:
      • EDTA . . . 500.0 mg
      • FeSO4.7H2O . . . 200.0 mg
      • ZnSO4.7H2O . . . 10.0 mg
      • MnCl2.4H2O . . . 3.0 mg
      • H3BO3 . . . 30.0 mg
      • CoCl2.6H2O . . . 20.0 mg
      • CaCl2.2H2O . . . 1.0 mg
      • NiCl2.6H2O . . . 2.0 mg
      • Na2MoO4.2H2O . . . 3.0 mg
      • Distilled water . . . 1.0 L
      • Autoclave at 121° C. for 15 minutes.
  • Growth and Conjugations. The procedure for conjugating plasmids from E. coli into methanotrophs was based on the method developed by Martin, H. & Murrell, J. C. (1995), FEMS Microbiol. Lett. 127: 243-248.
  • Briefly, a mobilizing plasmid to be conjugated was first transformed into E. coli S17-1 using standard electroporation methods. Transformation was confirmed by selection of kanamycin-resistant colonies on LB-agar containing 20 μg/mL kanamycin. Transformed colonies were inoculated into LB media containing 20 μg/mL kanamycin and shaken overnight at 37° C. A 10 mL aliquot of the overnight culture was then collected on a sterile 47 mm nitrocellulose filter (0.2 mm pore size). The E. coli donor strain was washed on the filter with 50 mL sterile NMS media to remove residual media and antibiotic.
  • In parallel, a sample of the M. trichosporium OB3b recipient strain was inoculated into 100 mL serum bottles containing 20-50 mL NMS media. The headspace of the bottles was then flushed with a 1:1 mixture of oxygen and methane, and the bottles were sealed with butyl butyl rubber septa and crimped. The bottles were shaken continuously in a 30° C. incubator until reaching an OD600 of approximately 0.3. The cells were then collected on the same filter as the E. coli donor strain. The filter was again washed with 50 mL of sterile NMS media. The filter was placed (cells up) on an NMS agar plate containing 0.02% (w/v) proteose peptone and incubated for 24 h at 30° C. in the presence of methane and oxygen. After 24 h, cells were re-suspended in 10 mL sterile (NMS) medium before being concentrated by centrifugation. The pellet was re-suspended in 1 mL sterile NMS media. Aliquots (100 μl) were spread onto NMS agar plates containing 10 μg/mL kanamycin.
  • The plates were incubated in sealed chambers containing a 1:1 mixture of methane and oxygen maintained at 30° C. The gas mixture was replenished every 2 days until colonies formed, typically after 7-14 days. Colonies were streaked onto NMS plates containing kanamycin to confirm kanamycin resistance as well as to further isolate transformed methanotroph cells from residual E. coli donor cells.
  • Deletion of phaC. A synthetic cDNA construct of the M. trichosporium OB3b phaC gene was synthesized, incorporating several stop mutations and frame shifts in the 5′ region of the gene. This cDNA construct was cloned into an appropriate vector for conjugation, but lacking an origin of replication that functions in methanotrophs, and introduced into M. trichosporium OB3b using the methods described above. This technique ensures that any kanamycin resistant M. trichosporium OB3b colonies must have been incorporated into the genome by recombination.
  • Identification of homologous recombination events is well-established in the art, and typically performed by PCR and sequencing using unique primers in the genome and the vector construct to confirm proper insertion. Homologous recombinants are then grown in the absence of selective pressure (e.g., kanamycin) for several generations, and sensitive clones which have lost the resistance marker are identified by replica plating (or equivalent technique). Approximately 50% of sensitive revertants possess the mutated form of the target gene in place of the wild-type version.
  • Loss of phaC function is confirmed by growing the cells under nitrogen limited conditions and measuring PHB content as described in Pieja A J, Rostkowski K H, Criddle C S, Distribution and selection of poly-3-hydroxybutyrate production capacity in methanotrophic proteobacteria. Microb. Ecol. 2011 October; 62(3):564-73. Briefly, the putative knockout clones inoculated into 100 mL serum bottles containing 20-50 mL NMS media. The headspace of the bottles was then flushed with a 1:1 mixture of oxygen and methane, and the bottles were sealed with butyl rubber septa and crimped. The bottles were shaken continuously in a 30° C. incubator until reaching an OD600 of approximately 0.3-0.6 to ensure the cells are in logarithmic phase growth. Cells are collected by centrifugation at 4,816×g (4,700 rpm) for 8 min, washed once with nitrogen-free NMS media medium, and re-suspended in nitrogen-free NMS medium to induce PHB production. 20-50 mL aliquots of washed cells are then transferred to serum bottles, sealed, and methane and oxygen added as described above. Cultures are then incubated at 30° C. on orbital shakers at 150 rpm. Assays for optical density and PHB production are performed every 1 to 2 h for the first 20 h.
  • PHB concentration determination. PHB concentration is measured directly via gas chromatography. For each sample, 5 to 10 mg of freeze-dried biomass is weighed out on an analytical balance, transferred to a 12-ml glass vial, and sealed with a polytetrafluoroethylene (PTFE)-lined plastic cap. 2 mL of methanol acidified with sulfuric acid (3%, vol/vol) and containing 1.0 g/L benzoic acid and 2 ml of chloroform are added to each vial. The vials are shaken gently and then heated at 100° C. for 3.5 h. Once the vials cool to room temperature, 1 ml deionized water is added to each. The vials are subjected to vortex mixing for 30 s and allowed to stand until phase separation is complete. The organic phase is analyzed using an Agilent 6890N gas chromatograph equipped with an HP-5 column [containing (5% phenyl)-methylpolysiloxane; Agilent Technologies] and a flame ionization detector (FID). dl-β-Hydroxybutyric acid sodium salt is used as a standard.
  • Introduction of Propylene pathway. Selected crotonase (SEQ ID NO:32), crotonyl-CoA thioesterase (SEQ ID NO:29), and 4-oxalocrotonate decarboxylase (SEQ ID NO:10) sequences were codon optimized (see Table 4) and synthesized with appropriate promoters. The genes are then cloned and transformed into the phaC knockout strain as described above. Transformation is confirmed by resistance of the cells to antibiotic selection, and gene expression is confirmed by northern blot (to confirm RNA transcription), western blot, or ELISA methods (to confirm protein expression).
  • TABLE 4
    Codon Optimized Sequences for M. trichosporium OB3b
    Reference
    Sequence Codon optimized sequence (SEQ ID NO: #)
    crotonase ATGGAGCTGAATAACGTCATCCTGGAAAAAGAAGGCAAGGTCGCGGTCGTCACGATCAACC
    GCCCCAAGGCTCTGAACGCGCTCAATAGCGACACCCTCAAAGAGATGGACTACGTCATCGGC
    GAGATCGAGAACGACTCCGAGGTGCTGGCCGTCATCCTCACCGGAGCGGGCGAGAAGTCGT
    TCGTGGCTGGGGCGGATATCAGCGAGATGAAAGAGATGAATACCATTGAAGGCCGCAAGTT
    CGGCATCCTGGGCAACAAGGTGTTCCGTCGCCTGGAGCTGCTGGAGAAGCCGGTCATTGCG
    GCGGTGAATGGCTTCGCGCTCGGCGGTGGCTGCGAGATCGCGATGTCGTGCGACATCCGCA
    TCGCCTCGTCGAACGCCCGCTTCGGACAGCCGGAAGTCGGCCTCGGCATCACGCCCGGATTC
    GGCGGCACTCAGCGCCTCAGCCGCCTGGTGGGCATGGGCATGGCTAAGCAGCTGATCTTCA
    CGGCGCAGAACATCAAGGCTGACGAGGCGCTCCGCATCGGCCTGGTCAACAAGGTGGTGG
    AGCCGTCGGAACTCATGAACACGGCGAAAGAGATTGCGAACAAAATCGTGTCGAATGCGCC
    GGTGGCGGTCAAGCTGAGCAAGCAGGCGATCAACCGTGGCATGCAGTGCGATATCGACACT
    GCGCTCGCCTTCGAGTCCGAGGCGTTCGGCGAGTGCTTCTCCACCGAAGATCAGAAAGATGC
    TATGACCGCCTTCATCGAAAAGCGGAAGATCGAGGGCTTCAAGAACCGC (SEQ ID NO: 124)
    crotonyl-CoA ATGCATCGCACCTCGAACGGCTCCCATGCCACGGGTGGCAATCTCCCCGACGTCGCCTCGCA
    thioesterase TTACCCCGTGGCGTACGAGCAGACCCTGGACGGCACCGTGGGCTTCGTCATCGATGAGATG
    ACGCCCGAGCGTGCCACCGCCTCGGTGGAAGTTACCGACACGCTCCGCCAGCGCTGGGGCC
    TCGTCCACGGCGGTGCTTACTGTGCGTTGGCGGAGATGCTGGCCACGGAAGCCACGGTCGC
    CGTGGTGCATGAGAAGGGCATGATGGCGGTCGGCCAGTCGAATCACACCAGCTTCTTCCGC
    CCTGTGAAAGAGGGCCACGTGCGTGCCGAGGCCGTGCGTATTCACGCGGGCTCGACCACGT
    GGTTCTGGGACGTCAGCCTGCGGGACGACGCGGGTCGCCTCTGCGCCGTGTCGTCGATGTC
    CATCGCGGTCCGCCCTCGCCGTGAC (SEQ ID NO: 125)
    4-oxalocrotonate ATGTCCACGACCAGCATCACCCCGGATGAGATCGCCCAGGTGCTGCTGGCTGGCGAGCGCA
    decarboxylase ACCGCACCGAGGTGGCGCAGTTCTCGGCGAGCCACCCCGACCTCGACGTCCGGACGGCCTA
    TGCGGCCCAGCGCGCTTTCGTCCAGGCCAAGCTGGATGCGGGCGAGCAGCTCGTCGGCTAT
    AAGCTGGGCCTGACCAGCCGCAACAAGCAGCGCGCCATGGGCGTCGACTGCCCGCTGTATG
    GCCGCGTCACGTCCTCGATGCTCGCGACGTATGGCGATCCCATCCCGTTCGACCGCTTCATCC
    ATCCGCGCGTCGAATCGGAGATCGCGTTCCTGCTCAAGCAGGATGTGACCGCTCCGGCGACC
    GTGTCGTCGGTCCTCGCGGCCACCGACGTCGTGTTCGGAGCGGTCGACGTGCTCGACTCGC
    GCTACGAGGGGTTCAAGTTCACGCTCGAGGATGTCGTGGCCGATAACGCGAGCGCGGGAG
    CGTTCTACCTCGGACCGGTCGCCCGTCCGGCCACCGAGCTCCGCCTCGACCTGCTGGGATGC
    ATCGTTCGCGTGGACGGCGAGGTCACCATGACCGCCGCTGGTGCGGCCGTCATGGGCCATC
    CCGCCGCGGCGGTCGCGTGGCTCGCCAACCAGCTCGCGCTCGAGGGCGAATCGCTGAAGGC
    CGGACAGCTGATCTTCTCGGGTGGCGTCACTGCGCCCGTCCCGGTCGTTCCTGGCGGCAGCG
    TCACGTTCGAGTTCGATGGCCTGGGCGTCATCGAGGTGGCTGGCGCC (SEQ ID NO: 126)
  • Production of Propylene from methane. phaC-deleted M. trichosporium transformed with a vector containing genes encoding crotonase and 4-oxalocrotonate decarboxylase are inoculated into 100 mL serum bottles containing 20-50 mL NMS media and 10 ug/mL kanamycin. The bottle headspace is flushed with a 1:1 mixture of methane and oxygen, and the bottles are sealed with butyl rubber septa and crimped. The bottles are then shaken continuously while being incubated at 30° C. The headspace gas is refreshed every 2 days as above; however, immediately prior to refreshing the headspace, samples are drawn from both the liquid phase and headspace using a 10 μL Hamilton syringe and injected into a HP5890 GC equipped with a CP-PoraBOND U 25 m×0.32 mm column and an FID maintained at 200° C. The injector is connected in splitless mode and maintained at 250° C. Samples are run with He Gas at 7.3 ml/min as a carrier gas; the oven program is set as follows: hold at 50° C. 1.5 min; ramp to 300° C. at 10° C./min; hold at 300° C. 10 min. Propylene is identified by retention time compared to pure propylene diluted in air or dissolved in pure H2O. Samples are also taken to measure optical density of the culture, allowing quantitation of specific propylene production rates per cell. Note that because methane is the only carbon source provided to the cells, all propylene produced must have been derived from methane.
    • Example 2 Methylococcus Capsulatus Bath Strain Methanotroph
  • Growth and Conjugations. The procedure for conjugating plasmids from E. coli into M. capsulatus was based on the method reported in Ali, H. & Murrell, J. C. Development and validation of promoter-probe vectors for the study of methane monooxygenase gene expression in Methylococcus capsulatus Bath. Microbiol. 155:761-771, 2009.
  • Briefly, a mobilizing plasmid to be conjugated was first transformed into E. coli S17-1 using standard electroporation methods. Transformation was confirmed by selection of kanamycin-resistant colonies on LB-agar containing 20 μg/mL kanamycin. Transformed colonies were inoculated into LB media containing 20 μg/mL kanamycin and shaken overnight at 37° C. A 10 mL aliquot of the overnight culture was then collected on a sterile 47 mm nitrocellulose filter (0.2 mm pore size). The E. coli donor strain was washed on the filter with 50 mL sterile NMS to remove residual media and antibiotic.
  • In parallel, a sample of the M. capsulatus recipient strain was inoculated into 100 mL serum bottles containing 20-50 mL NMS media. The headspace of the bottles was then flushed with a 1:1 mixture of oxygen and methane, and the bottles were sealed with butyl rubber septa and crimped. The bottles were shaken continuously in a 45° C. incubator until reaching an OD600 of approximately 0.3. The cells were then collected on the same filter as the E. coli donor strain. The filter was again washed with 50 mL of sterile NMS media. The filter was placed (cells up) on an NMS agar plate containing 0.02% (w/v) proteose peptone and incubated for 24 h at 37° C. in the presence of methane and oxygen. After 24 h, cells were re-suspended in 10 mL sterile (NMS) medium before being concentrated by centrifugation. The pellet was re-suspended in 1 mL sterile NMS media. Aliquots (100 μl ) were spread onto NMS agar plates containing 10 μg/mL kanamycin.
  • The plates were incubated in sealed chambers containing a 1:1 mixture of methane and oxygen maintained at 45° C. The gas mixture was replenished every 2 days until colonies formed, typically after 7-14 days. Colonies were streaked onto NMS plates containing kanamycin to confirm kanamycin resistance as well as to further isolate transformed methanotroph cells from residual E. coli donor cells.
  • Introduction of Propylene synthesis pathway. Note that M. capsulatus does not have a native PHA pathway, hence no pathway genes (i.e., phaC) need to be deleted. However, phaA and phaB function must be introduced to the cells to provide the substrate for the crotonase enzyme (i.e., 3-hydroxybutryl-CoA).
  • Selected phaA (SEQ ID NO:77), phaB (SEQ ID NO:123), crotonase (SEQ ID NO:32), crotonyl-CoA thioesterase (SEQ ID NO:29), and 4-oxalocrotonate decarboxylase (SEQ ID NO:10) sequences were codon optimized (see Table 5) and synthesized with appropriate promoters. The genes are then cloned and transformed into M. capsulatus as described above. Transformation is confirmed by resistance of the cells to antibiotic selection, and gene expression is confirmed by northern blot (to confirm RNA transcription), western blot, or ELISA methods (to confirm protein expression).
  • TABLE 5
    Codon Optimized Sequences for M. capsulatus
    Reference
    Sequence Codon Optimized Sequence (SEQ ID NO: #)
    phaA ATGACCGACGTGGTCATCGTGTCGGCAGCCCGCACAGCAGTGGGTAAATTCGGCGGCT
    CGCTGGCCAAGATCGCAGCCCCGGAGCTGGGCGCCTCGGTCATCCGAGCGGTATTGGA
    ACGAGCCGGAGTGAAGCCCGAGCAGGTGTCGGAAGTCATCTTGGGCCAAGTGCTTACT
    GCCGGCAGCGGCCAAAACCCAGCCCGGCAGGCGTTGATCGCCGCAGGGCTCCCGAAC
    GCCGTCCCGGGCATGACGATCAACAAGGTGTGTGGCAGCGGCCTCAAGGCGGTCATGC
    TCGCGGCCAATGCGGTCGTAGCAGGGGACGCGGAAATCGTCGTGGCAGGCGGCCAGG
    AAAACATGAGCGCTGCGCCGCACGTGCTGCCCGGCTCCCGCGACGGCTTCCGGATGGG
    AGACGCCAAGTTGGTGGATTCAATGATCGTTGACGGGTTGTGGGACGTTTACAACAAG
    TACCATATGGGCATCACCGCAGAAAATGTGGCGAAAGAATATGGTATCACCCGCGAGG
    CCCAGGACCAGTTCGCCGCCTTGAGCCAGAACAAGGCCGAAGCTGCCCAGAAAGCGG
    GTCGCTTCGACGATGAAATCGTACCGATCGAAATCCCGCAACGGAAGGGCGAGCCCCT
    GCGCTTCGCGACCGATGAATTCGTCCGGCACGGGGTCACGGCCGAGTCCCTCGCGAGC
    CTCAAGCCGGCCTTCGCCAAAGAAGGCACCGTGACCGCCGCTAACGCGAGCGGCATCA
    ACGACGGCGCAGCCGCAGTCCTGGTTATGTCGGCGAAGAAGGCCGAAGCCCTGGGGC
    TGGAGCCCCTGGCCCGGATCAAGGCGTACGCCAATGCGGGAGTGGATCCGTCCGTAAT
    GGGAATGGGCCCTGTCCCCGCCTCGCGACGGTGCCTGGAGCGCGCAGGGTGGTCGGT
    AGGCGACCTCGATCTCATGGAGATCAATGAAGCGTTCGCGGCTCAGGCGCTCGCGGTG
    CACAAGCAGATGGGCTGGGATACCTCGAAGGTTAACGTGAACGGCGGTGCCATCGCG
    ATCGGCCACCCCATCGGGGCCTCAGGCTGCCGCATCCTGGTCACCCTGCTGCATGAAAT
    GCTGAAGCGCGATGCCAAGCGGGGACTGGCGTCGCTCTGCATCGGCGGTGGCATGGG
    TGTCGCCTTGGCCCTCGAGCGGCCG(SEQ ID NO: 127)
    pha B ATGAAGAAGGTGTGCGTCATCGGAGCCGGCACCATGGGTTCCGGGATCGCGCAGGCCT
    TTGCCGCCAAGGGCTTCGAAGTGGTGCTGCGTGACATCAAAGACGAGTTCGTCGACCG
    TGGTTTGGATTTCATCAACAAGAACCTGTCGAAACTCGTCAAGAAAGGCAAGATCGAA
    GAGGCAACGAAGGTTGAGATTCTCACCCGTATAAGCGGGACGGTGGACCTGAACATG
    GCGGCTGATTGTGACCTGGTGATCGAAGCCGCGGTGGAACGCATGGACATCAAGAAG
    CAGATCTTCGCAGATCTGGACAATATCTGCAAGCCAGAGACGATTCTTGCGAGCAATAC
    CAGCAGTCTGTCCATCACCGAGGTCGCATCCGCGACGAAACGGCCGGACAAAGTGATC
    GGCATGCACTTCTTCAACCCTGCGCCCGTCATGAAGTTGGTGGAAGTGATCCGGGGCAT
    CGCCACAAGCCAGGAAACCTTCGACGCTGTGAAAGAGACGTCGATCGCGATCGGGAAA
    GACCCGGTCGAGGTGGCGGAAGCACCCGGCTTCGTCGTCAATCGGATCCTGATCCCGA
    TGATCAATGAAGCAGTCGGCATCTTGGCCGAGGGCATTGCCAGCGTCGAAGATATCGA
    CAAGGCCATGAAGCTGGGCGCCAACCATCCGATGGGACCCCTGGAACTGGGAGACTTC
    ATCGGGCTGGACATCTGCCTGGCCATCATGGACGTTCTCTACAGCGAAACGGGCGACTC
    GAAGTATCGCCCGCATACCCTGCTGAAGAAATACGTCCGTGCAGGCTGGCTGGGACGC
    AAGTCCGGCAAGGGCTTCTACGACTATTCCAAG(SEQ ID NO: 128)
    crotonase ATGGAACTTAACAATGTGATCCTGGAGAAAGAAGGTAAAGTCGCCGTGGTGACCATTA
    ATCGCCCCAAGGCCCTGAACGCCCTGAATTCTGACACGCTGAAAGAAATGGACTACGT
    GATCGGCGAAATCGAGAACGACTCCGAGGTGCTGGCCGTGATCCTGACCGGCGCAGG
    CGAAAAGTCGTTCGTTGCCGGAGCGGATATCTCCGAGATGAAAGAGATGAACACCATT
    GAGGGCAGGAAGTTCGGCATCCTGGGCAATAAAGTCTTTCGCCGGCTCGAGCTCCTGG
    AGAAGCCGGTAATTGCCGCCGTTAATGGCTTCGCGCTCGGTGGCGGATGTGAAATCGC
    GATGAGCTGCGACATCCGCATAGCGAGTAGTAACGCGCGGTTCGGCCAGCCCGAGGTC
    GGCCTGGGCATCACGCCCGGATTCGGTGGCACTCAGCGGCTGTCGCGCCTGGTGGGCA
    TGGGGATGGCCAAGCAGCTGATCTTCACCGCGCAGAACATCAAAGCCGACGAAGCCCT
    GCGCATAGGGTTGGTGAACAAAGTCGTGGAGCCGAGCGAGTTGATGAACACCGCCAA
    AGAGATCGCCAACAAGATCGTCTCGAACGCACCGGTCGCGGTGAAATTGTCGAAGCAG
    GCCATCAACCGCGGCATGCAGTGCGATATCGATACCGCCCTCGCCTTCGAGTCGGAAGC
    CTTTGGTGAATGCTTCTCCACCGAAGATCAAAAAGACGCCATGACCGCCTTCATAGAGA
    AGCGCAAGATCGAGGGTTTTAAGAACCGG(SEQ ID NO: 129)
    crotonyl-CoA ATGCATCGGACCAGCAACGGCAGCCACGCCACAGGTGGCAATCTGCCGGACGTCGCTA
    thioesterase GCCACTATCCGGTCGCCTACGAGCAGACCCTTGATGGGACGGTGGGCTTCGTGATCGA
    CGAGATGACGCCAGAGCGAGCGACCGCTAGCGTCGAAGTCACCGATACGTTGCGGCA
    GCGGTGGGGCCTGGTCCATGGCGGTGCGTATTGCGCGCTTGCCGAAATGCTGGCCACC
    GAGGCTACCGTCGCCGTCGTCCACGAAAAGGGGATGATGGCGGTTGGTCAGTCGAACC
    ATACGTCGTTCTTTCGTCCCGTGAAAGAGGGCCACGTGCGGGCAGAAGCCGTCCGTATT
    CACGCCGGCAGCACCACCTGGTTCTGGGATGTTTCGCTGCGCGATGACGCCGGCAGGC
    TGTGCGCCGTCAGTTCCATGTCAATCGCCGTCCGTCCACGCCGGGAT (SEQ ID NO: 130)
    4-oxalocrotonate ATGTCGACGACGTCCATTACCCCGGACGAGATTGCCCAGGTGCTGCTCGCTGGGGAAC
    decarboxylase GGAACCGCACCGAAGTGGCCCAGTTCTCCGCGTCCCATCCGGACCTGGATGTTCGCACC
    GCCTATGCCGCCCAGCGTGCTTTTGTCCAGGCCAAGCTGGACGCGGGAGAGCAGCTCG
    TCGGCTACAAGCTGGGCCTTACGAGTCGGAACAAGCAGCGTGCCATGGGTGTGGACTG
    CCCGCTGTACGGGCGAGTGACGAGCTCTATGCTGGCGACCTACGGGGACCCGATCCCG
    TTTGACCGCTTCATCCATCCGCGGGTCGAAAGCGAGATTGCGTTCCTGTTGAAACAGGA
    CGTGACCGCTCCGGCCACCGTGTCGTCCGTTCTGGCCGCCACGGACGTCGTCTTTGGCG
    CGGTCGACGTACTGGACTCCCGGTACGAAGGCTTCAAGTTCACCCTCGAAGATGTGGT
    GGCCGACAACGCCAGCGCTGGCGCGTTCTATCTCGGACCCGTGGCACGTCCCGCTACC
    GAGTTGCGCCTGGACTTGTTGGGGTGCATCGTACGTGTGGACGGCGAAGTCACGATGA
    CCGCGGCTGGCGCAGCCGTGATGGGCCACCCGGCAGCGGCAGTGGCCTGGCTCGCGA
    ACCAGCTGGCGCTGGAAGGGGAATCCCTGAAAGCCGGTCAACTGATCTTCTCGGGTGG
    GGTCACGGCACCCGTCCCTGTGGTGCCTGGCGGATCGGTGACCTTCGAGTTCGATGGC
    CTTGGCGTGATCGAGGTGGCCGGAGCA (SEQ ID NO: 131)
  • Production of Propylene from methane. M. capsulatus transformed with the vector described above are inoculated into 100 mL serum bottles containing 20-50 mL NMS media and 10 μg/mL kanamycin. The bottle headspace is flushed with a 1:1 mixture of methane and oxygen, and the bottles are sealed with butyl rubber septa and crimped. The bottles are then shaken continuously while being incubated at 42-45° C. The headspace gas is refreshed every 2 days as above; however, immediately prior to refreshing the headspace, samples are drawn from both the liquid phase and headspace using a 10 μL Hamilton syringe and injected into a HP5890 GC equipped with a CP-PoraBOND U 25 m×0.32 mm column and an FID maintained at 200° C. The injector is connected in splitless mode and maintained at 250° C. Samples are run with He Gas at 7.3 ml/min as a carrier gas; the oven program is set as follows: hold at 50° C. 1.5 min; ramp to 300° C. at 10° C./min; hold at 300° C. 10 min. Propylene is identified by retention time compared to pure propylene diluted in air or dissolved in pure H2O. Samples are also taken to measure optical density of the culture, allowing quantitation of specific propylene production rates per cell. Note that because methane is the only carbon source provided to the cells, all propylene produced must have been derived from methane.
    • Example 3 Methylobacterium Extorquens Methylotroph
  • Growth and Transformation. The procedure for introducing plasmids into M. extorquens has been demonstrated in Ueda S., Matsumoto S., Shimizu S., and Yamane T., Transformation of a Methylotrophic Bacterium, Methylobacterium extorquens, with a Broad-Host-Range Plasmid by Electroporation, Appl. Environ. Microbiol., 1991, April; 57(4): 924-926.
  • Briefly, wild-type (wt) M. extorquens is cultured at 30° C. in NMS media supplemented with 1% methanol. Cells of M. extorquens NR-2 grown to the middle logarithmic phase (1.4×109/ml) are harvested by centrifugation at 6,000×g for 10 min and washed with electroporation buffer (10 mM Tris-HCl, 2 mM MgCl2.6H2O, 10% [wt/vol] sucrose [pH 7.5]). Cells are re-suspended in the same buffer at a cell concentration of 7.0×1010/ml. The cell suspension and the solution of vector (70 μg/mL) are mixed at a ratio of 9:1 (vol/vol) in an Eppendorf tube. The mixture (10 μL) is then transferred into a space between the electrodes of a chamber, where it is equilibrated for 3 min. After being subjected to 10 pulses of a 10 kV/cm electric field for 300 μsec/pulse, a 5 μL aliquot of the mixture is transferred to an Eppendorf tube. 0.2 mL of NMS medium is then added to the tube. The cell suspension is then incubated for 2 h at 30° C. to allow expression of the antibiotic resistance genes prior to plating on NMS plates containing 1% methanol and 20 μg/mL kanamycin.
  • The plates were incubated at 30° C. until colonies formed. Colonies were streaked onto duplicate plates to confirm kanamycin resistance as well as to further isolate transformed methylotroph cells from residual E. coli donor cells.
  • Deletion of phaC. The deletion of the phaC gene has been described in Korotkova N., Lidstrom M. E., Connection between poly-beta-hydroxybutyrate biosynthesis and growth on C(1) and C(2) compounds in the methylotroph Methylobacterium extorquens AM1, J. Bacteriol. 2001 February; 183(3):1038-46.
  • Briefly, insertion cassettes containing a kanamycin resistance marker were constructed with flanking sequences homologous to the areas flanking the phaC gene in the M. extorquens genome. A tetracycline resistance gene was incorporated elsewhere in the plasmid. Transformants were initially selected for resistance to kanamycin, and then screened for sensitivity to tetracycline to identify potential double cross-over recombination events. Correct insertion into and deletion of the phaC gene was confirmed by PCR.
  • Loss of phaC function is confirmed by growing the cells under nitrogen limited conditions and measuring PHA content as described in Pieja A J, Rostkowski K H, Criddle C S, Distribution and selection of poly-3-hydroxybutyrate production capacity in methanotrophic proteobacteria, Microb. Ecol. 2011 October; 62(3):564-73.
  • Introduction of Propylene synthesis pathway. Selected crotonase (SEQ ID NO:32), crotonyl-coA thioesterase (SEQ ID NO:29), and 4-oxalocrotonate decarboxylase (SEQ ID NO:10) sequences were codon optimized (see Table 6) and synthesized with appropriate promoters. The genes are then cloned and transformed into the phaC knockout strain as described above. Transformation is confirmed by resistance of the cells to antibiotic selection, and gene expression is confirmed by northern blot (to confirm RNA transcription), western blot, or ELISA methods (to confirm protein expression).
  • TABLE 6
    Codon Optimized Sequences for M. extorquens
    Reference
    Sequence Codon Optimized Sequence (SEQ ID NO: #)
    crotonase ATGGAGCTGAACAACGTCATCCTCGAAAAAGAGGGCAAGGTGGCGGTCGTCACCATC
    AACCGCCCCAAGGCCCTCAACGCGCTCAACAGCGACACGCTCAAAGAAATGGATTAC
    GTCATCGGCGAGATCGAGAACGATTCCGAGGTGCTCGCCGTGATCCTCACCGGTGCG
    GGCGAAAAGTCGTTCGTGGCGGGTGCGGATATCTCCGAAATGAAAGAAATGAACACG
    ATCGAGGGCCGGAAGTTCGGCATCCTCGGCAACAAGGTTTTCCGCCGTCTCGAGTTGT
    TGGAGAAGCCGGTCATTGCCGCCGTGAATGGCTTCGCCCTCGGTGGTGGCTGCGAGA
    TCGCCATGAGCTGCGACATCCGGATCGCGTCGAGCAACGCCCGTTTCGGCCAGCCGG
    AAGTCGGCTTGGGCATCACCCCGGGCTTCGGCGGCACGCAGCGCCTCTCGCGGCTCG
    TCGGCATGGGCATGGCCAAGCAGCTCATCTTCACCGCCCAGAATATCAAGGCGGACG
    AGGCGCTGCGCATTGGCCTCGTTAACAAGGTCGTGGAGCCCTCGGAGCTCATGAACA
    CCGCGAAAGAGATCGCGAACAAGATCGTGTCCAACGCACCGGTGGCCGTCAAGCTCT
    CGAAGCAGGCCATCAACCGCGGCATGCAGTGCGATATCGACACCGCGCTCGCGTTCG
    AGAGCGAGGCGTTCGGGGAGTGCTTCTCGACCGAAGATCAGAAGGACGCCATGACC
    GCCTTCATCGAGAAGCGCAAGATCGAAGGCTTCAAGAACCGC (SEQ ID NO: 132)
    crotonyl-coA ATGCACCGCACCTCGAACGGCTCGCACGCCACCGGTGGCAACCTGCCGGACGTCGCCT
    thioesterase CGCATTACCCGGTCGCGTACGAACAGACCCTGGACGGGACGGTGGGCTTCGTCATCG
    ATGAGATGACGCCCGAGCGCGCGACGGCCTCGGTCGAGGTGACCGACACGCTCCGCC
    AGCGCTGGGGCCTCGTCCACGGCGGTGCGTACTGCGCCCTCGCCGAGATGCTCGCCA
    CCGAGGCGACGGTGGCCGTGGTCCATGAGAAGGGCATGATGGCGGTGGGGCAGAGC
    AACCACACGAGCTTCTTTCGCCCGGTGAAAGAGGGCCACGTCCGCGCAGAGGCCGTG
    CGCATCCACGCGGGCTCCACCACCTGGTTTTGGGATGTGTCGCTGCGCGATGACGCAG
    GCCGCCTTTGCGCCGTGTCCAGCATGTCGATCGCGGTGCGGCCCCGCCGCGAC (SEQ
    ID NO: 133)
    4-oxa locrotonate ATGAGCACCACGTCGATCACCCCGGACGAGATCGCGCAGGTGCTGCTGGCAGGCGAG
    decarboxylase CGCAACCGGACCGAGGTCGCCCAGTTCAGCGCCTCGCACCCGGACCTCGACGTGCGC
    ACGGCGTATGCTGCGCAGCGGGCGTTCGTGCAGGCCAAGCTCGATGCCGGCGAGCA
    GTTGGTCGGCTACAAGCTCGGCCTGACCTCGCGGAATAAGCAGCGGGCCATGGGCGT
    CGACTGCCCGTTGTATGGTCGCGTCACCAGCAGCATGCTGGCGACCTACGGCGACCCC
    ATCCCCTTCGACCGCTTCATCCATCCGCGCGTCGAATCGGAAATCGCCTTCCTGCTGAA
    GCAGGATGTCACCGCCCCGGCCACCGTCTCGTCGGTCCTCGCCGCGACCGACGTCGTT
    TTCGGCGCTGTCGACGTGCTGGATAGCCGCTACGAGGGCTTCAAGTTCACGCTGGAA
    GATGTGGTCGCGGACAACGCCAGCGCCGGAGCCTTCTACCTCGGTCCCGTCGCCCGTC
    CGGCCACGGAGCTCCGGCTCGACTTGCTCGGCTGCATCGTCCGGGTCGACGGCGAGG
    TTACCATGACCGCAGCGGGAGCCGCCGTGATGGGCCACCCCGCAGCCGCGGTGGCCT
    GGCTCGCCAACCAGCTCGCCCTCGAGGGCGAGTCGCTGAAAGCCGGCCAGCTGATCT
    TCAGCGGCGGTGTGACGGCGCCGGTCCCCGTCGTGCCCGGTGGCTCGGTCACCTTCG
    AGTTCGACGGACTGGGCGTCATCGAGGTGGCCGGCGCC
    (SEQ ID NO: 134)
  • Production of Propylene from methanol. phaC-deleted M. extorquens transformed with a vector containing genes encoding crotonase and 4-oxalocrotonate decarboxylase are inoculated into 100 mL sealed flasks containing 20-50 mL NMS media, 125 mM methanol, 50 μg/mL rifamycin, and 10 μg/mL kanamycin. The flask headspace is flushed with oxygen and sealed to prevent loss of the propylene product. The flasks are then shaken continuously while being incubated at 30° C. The headspace gas is refreshed every day; however, immediately prior to refreshing the headspace, samples are drawn from both the liquid phase and headspace using a 10 μL Hamilton syringe and injected into a HP5890 GC equipped with a CP-PoraBOND U 25 m x 0.32 mm column and an FID maintained at 200° C. The injector is connected in splitless mode and maintained at 250° C. Samples are run with He Gas at 7.3 ml/min as a carrier gas; the oven program is set as follows: hold at 50° C. 1.5 min; ramp to 300° C. at 10° C./min; hold at 300° C. 10 min. Propylene is identified by retention time compared to pure propylene diluted in air or dissolved in pure H2O. Samples are also taken to measure optical density of the culture, allowing quantitation of specific propylene production rates per cell. Note that because methanol is the only carbon source provided to the cells, all propylene produced must have been derived from methanol.
    • Example 4 Clostridiuma Utoethanogenum
  • Growth and transformation. C. autoethanogenum is cultivated anaerobically in modified PETC medium (ATCC medium 1754) at 37° C. in modified PETC media.
  • The modified PETC medium contains (per L) 1 g NH4Cl, 0.4 g KCl, 0.2 g MgSO4×7H2O, 0.8 g NaCl, 0.1 g KH2PO4, 20 mg CaCl2×2H2O, 10 ml trace elements solution (see below), 10 ml Wolfe's vitamin solution (see below), 2 g NaHCO3, and 1 mg resazurin. After the pH is adjusted to 5.6, the medium is boiled, dispensed anaerobically, and autoclaved at 121° C. for 15 min. Steel mill waste gas (composition: 44% CO, 32% N2, 22% CO2, 2% H2) or equivalent synthetic mixtures are used as carbon source. The media has a final pH of 5.9 and is reduced with Cystein-HCl and Na2S in a concentration of 0.008% (w/v).
  • The trace elements solution consists of 2 g nitrilotriacetic acid (adjusted to pH 6 with KOH before addition of the remaining ingredients), 1 g MnSO4, 0.8 g Fe(SO4)2(NH4)2×6H2O, 0.2 g CoCl2×6H2O, 0.2 mg ZnSO4×7H2O, 20 mg CuCl2×2H2O, 20 mg NiCl2×6H2O, 20 mg Na2MoO4×2H2O, 20 mg Na2SeO4, and 20 mg Na2WO4 per liter.
  • Wolfe's vitamin solution (Wolin et al., 1963, J. Biol. Chem. 238:2882-2886) contains (per L) 2 mg biotin, 2 mg folic acid, 10 mg pyridoxine hydrochloride, 5 mg thiamine-HCl, 5 mg riboflavin, 5 mg nicotinic acid, 5 mg calcium D-(+)-pantothenate, 0.1 mg vitamin B12, 5 mg p-aminobenzoic acid, and 5 mg thioctic acid.
  • Growth experiments are carried out in a volume of 100 ml PETC media in plastic-coated 500-ml-Schott Duran® GL45 bottles with butyl rubber stoppers and 200 kPa steel mill waste gas as sole energy and carbon source. Growth is monitored by measuring the optical density at 600 nm (OD600 nm).
  • Transformation methods for C. autoethanogenum are performed as described in U.S. Patent Publication 2011/0236941.
  • Briefly, to make competent cells, a 50 ml culture of C. autoethanogenum is subcultured to fresh media for 3 consecutive days. These cells are used to inoculate 50 ml PETC media containing 40 mM DL-threonine at an OD600 nm of 0.05. When the culture reaches an OD600 nm of 0.4, the cells are transferred into an anaerobic chamber and harvested at 4,700×g and 4° C. The culture is twice washed with ice-cold electroporation buffer (270 mM sucrose, 1 mM MgCl2, 7 mM sodium phosphate, pH 7.4) and finally suspended in a volume of 600 μl fresh electroporation buffer. This mixture is transferred into a pre-cooled electroporation cuvette with a 0.4 cm electrode gap containing 1 μg of the methylated plasmid mix and immediately pulsed using the Gene pulser Xcell electroporation system (Bio-Rad) with the following settings: 2.5 kV, 600 μl, and 25 μF. Time constants of 3.7-4.0 ms are achieved. The culture is transferred into 5 ml fresh media. Regeneration of the cells is monitored at a wavelength of 600 nm using a Spectronic Helios Epsilon Spectrophotometer (Thermo) equipped with a tube holder. After an initial drop in biomass, the cells start growing again. Once the biomass has doubled from that point, the cells are harvested, suspended in 200 μl fresh media and plated on selective PETC plates (containing 1.2% Bacto™ Agar (BD)) with 4 μg/ μl Clarithromycin. After 4-5 days of incubation with 30 psi steel mill gas at 37° C., 15-80 colonies per plate are clearly visible.
  • The colonies are used to inoculate 2 ml PETC media containing 4 μg/ μl Clarithromycin. When growth occurs, the culture is upscaled into 5 ml and later 50 ml PETC media containing 4 μg/ μl Clarithromycin and 30 psi steel mill gas as sole carbon source.
    • Confirmation of Successful Transformation:
  • To verify the DNA transfer, a plasmid mini prep is performed from 10 ml culture volume using the QIAprep Spin Miniprep Kit (Qiagen). The quality of the isolated plasmid DNA is sufficient to run a control PCR. The PCR is performed with Illustra PuReTaq Ready-To-Go™ PCR Beads (GE Healthcare) using standard conditions (95° C. for 5 min; 32 cycles of 95° C. for 30 s, 50° C. for 30 s, and 72° C. for 1 min; 72° C. for 10 min). As a further control, 1 μl of each of the partly degraded isolated plasmids are re-transformed in E. coli XL1-Blue MRF′ Kan (Stratagene), from where the plasmids can be isolated cleanly and verified by restriction digests.
  • Introduction of Propylene synthesis pathway. Note that C. autoethanogenum does not have a native PHA pathway, hence no pathway genes need to be deleted. However, phaA and phaB function must be introduced to the cells to provide the substrate for the crotonase enzyme.
  • Selected phaA (SEQ ID NO:77), phaB (SEQ ID NO:123), crotonase (SEQ ID NO:32), crotonyl-coA thioesterase (SEQ ID NO:29), and 4-oxalocrotonate decarboxylase (SEQ ID NO:10) sequences were codon optimized (see Table 7) and synthesized with appropriate promoters. The genes are then cloned and transformed into C. autoethanogenum as described above. Transformation is confirmed by resistance of the cells to antibiotic selection, and gene expression is confirmed by northern blot (to confirm RNA transcription), western blot, or ELISA methods (to confirm protein expression).
  • TABLE 7
    Codon Optimized Sequences for C. autoethanogenum
    Reference
    Sequence Codon Optimized Sequence (SEQ ID NO: #)
    phaA ATGACAGATGTAGTGATAGTTTCAGCAGCTAGAACAGCTGTTGGTAAATTCGGTGGTTC
    GTTAGCGAAAATAGCTGCTCCTGAATTAGGAGCTTCAGTAATTAGAGCTGTATTAGAAA
    GAGCAGGTGTAAAACCTGAGCAAGTGTCTGAAGTCATATTAGGGCAAGTCTTGACTGCA
    GGGTCAGGTCAGAATCCTGCAAGACAAGCCTTAATAGCTGCGGGACTTCCTAATGCAGT
    ACCTGGGATGACAATCAATAAAGTTTGTGGATCAGGTCTAAAAGCAGTTATGTTGGCTG
    CAAATGCGGTTGTAGCTGGAGACGCTGAAATAGTTGTGGCGGGTGGACAAGAAAACAT
    GAGTGCAGCACCACATGTTCTACCTGGCAGTAGAGATGGATTTCGAATGGGAGATGCAA
    AGCTAGTAGATAGCATGATAGTAGATGGATTATGGGATGTTTACAATAAGTATCATATG
    GGAATAACTGCAGAAAATGTAGCAAAAGAATATGGAATTACACGTGAAGCTCAAGACCA
    ATTTGCAGCACTTTCACAGAATAAGGCTGAAGCAGCACAAAAAGCTGGAAGATTTGATG
    ATGAAATAGTTCCTATTGAAATTCCACAAAGAAAGGGAGAACCACTTAGATTTGCCACTG
    ATGAATTTGTAAGGCATGGAGTAACAGCTGAATCTCTTGCAAGTTTGAAACCAGCGTTTG
    CCAAAGAGGGAACTGTGACTGCTGCTAATGCTTCAGGCATAAATGATGGAGCTGCAGCA
    GTCCTTGTTATGTCTGCGAAGAAAGCAGAAGCTCTTGGCCTTGAACCTTTGGCACGTATT
    AAGGCTTATGCCAATGCTGGAGTTGATCCTTCTGTTATGGGAATGGGACCTGTACCGGCA
    AGTAGAAGATGCCTAGAAAGAGCAGGATGGAGTGTAGGTGATTTAGATCTTATGGAGA
    TTAATGAGGCTTTTGCTGCACAAGCGTTGGCTGTTCATAAGCAAATGGGTTGGGATACAT
    CAAAAGTTAATGTAAATGGCGGTGCAATAGCAATTGGACATCCAATAGGAGCATCTGGT
    TGCAGAATACTTGTTACTCTTCTTCATGAAATGTTGAAAAGAGATGCTAAAAGAGGTTTA
    GCATCATTATGTATAGGTGGTGGCATGGGAGTAGCTTTAGCATTAGAAAGACCG(SEQ
    ID NO: 135)
    pha B ATGAAAAAGGTTTGTGTTATAGGTGCAGGTACTATGGGTTCAGGTATTGCTCAGGCATTT
    GCAGCCAAAGGGTTTGAAGTTGTTTTAAGGGACATAAAAGATGAATTCGTGGATAGGG
    GATTAGATTTTATAAATAAGAACTTAAGTAAGCTTGTAAAGAAGGGCAAAATTGAAGAG
    GCTACTAAAGTAGAAATCTTGACGAGAATAAGTGGTACCGTAGATCTTAACATGGCTGC
    AGATTGTGATTTAGTTATTGAAGCTGCGGTCGAAAGAATGGACATTAAGAAACAGATTTT
    TGCAGACTTAGATAACATATGTAAGCCAGAAACTATCTTAGCCAGTAATACAAGCTCATT
    ATCAATTACTGAAGTAGCAAGTGCGACAAAAAGGCCTGATAAAGTAATTGGAATGCATT
    TCTTTAATCCAGCACCTGTTATGAAATTAGTGGAAGTTATAAGGGGAATAGCAACTTCAC
    AAGAAACTTTTGATGCAGTGAAAGAAACCTCAATTGCAATAGGTAAAGACCCCGTTGAA
    GTTGCTGAAGCACCAGGTTTTGTTGTTAATAGAATACTAATACCAATGATAAATGAAGCA
    GTTGGAATCCTTGCAGAAGGTATAGCAAGTGTAGAAGATATTGACAAAGCAATGAAATT
    AGGTGCAAACCATCCAATGGGTCCTTTGGAATTAGGAGATTTCATTGGATTAGATATATG
    TTTAGCAATAATGGATGTACTATATTCTGAGACTGGAGATTCTAAGTACAGGCCTCATAC
    TTTACTTAAGAAATATGTAAGGGCGGGATGGTTAGGAAGAAAGTCTGGAAAGGGCTTTT
    ATGATTATAGTAAG(SEQ ID NO: 136)
    crotonase ATGGAACTTAACAATGTAATACTTGAAAAAGAAGGCAAAGTAGCTGTTGTAACAATAAA
    CAGGCCAAAAGCTCTAAATGCACTTAATTCCGACACTCTTAAAGAAATGGATTACGTTAT
    AGGTGAGATAGAAAATGATTCTGAAGTACTAGCTGTAATACTTACAGGTGCTGGTGAGA
    AATCATTTGTGGCAGGAGCAGATATTTCTGAAATGAAAGAAATGAATACTATTGAGGGG
    AGAAAATTCGGGATACTTGGAAACAAGGTTTTTAGAAGGTTAGAATTACTTGAGAAACC
    AGTAATAGCTGCCGTAAATGGATTTGCATTAGGTGGCGGATGTGAAATAGCAATGTCAT
    GCGATATCCGAATCGCATCTTCTAATGCAAGATTTGGGCAACCTGAAGTTGGATTAGGAA
    TCACTCCCGGATTTGGCGGTACACAAAGACTTAGCAGATTAGTAGGTATGGGAATGGCT
    AAGCAACTAATTTTTACGGCTCAGAACATAAAAGCAGATGAAGCTCTTAGGATTGGACTT
    GTGAATAAAGTAGTAGAACCGTCGGAGCTTATGAATACAGCAAAAGAAATTGCAAACAA
    AATAGTAAGTAATGCACCAGTGGCAGTTAAACTTTCGAAACAAGCAATCAATAGGGGCA
    TGCAATGCGATATAGATACGGCTTTGGCATTTGAAAGTGAAGCATTTGGGGAATGTTTTT
    CAACGGAAGATCAAAAAGATGCTATGACAGCCTTTATTGAGAAAAGAAAGATAGAGGG
    ATTTAAGAATAGA (SEQ ID NO: 137)
    crotonyl-coA ATGCACAGAACATCTAATGGATCACATGCAACAGGTGGCAATCTACCAGATGTTGCAAG
    thioesterase TCATTATCCGGTAGCTTATGAACAGACATTAGATGGAACCGTTGGTTTTGTGATAGATGA
    AATGACTCCAGAAAGAGCTACAGCTTCCGTCGAGGTAACTGATACATTACGTCAGAGGT
    GGGGTTTGGTTCATGGTGGAGCATATTGTGCTCTTGCGGAAATGTTGGCTACTGAAGCA
    ACAGTTGCAGTTGTACATGAAAAAGGTATGATGGCAGTTGGTCAATCTAATCACACCAG
    CTTTTTCAGGCCAGTTAAAGAAGGTCATGTTAGAGCCGAGGCGGTTAGGATACATGCAG
    GAAGTACAACCTGGTTTTGGGATGTTTCTTTAAGAGATGATGCTGGTAGATTATGTGCTG
    TTAGCAGTATGTCCATTGCAGTAAGACCAAGAAGAGAT (SEQ ID NO: 138)
    4-oxalocrotonate ATGAGCACTACTAGTATAACACCAGATGAAATTGCTCAAGTACTATTAGCTGGAGAAAG
    decarboxylase AAATAGAACAGAAGTAGCACAGTTTTCAGCTTCACACCCGGATTTAGATGTAAGAACGG
    CTTATGCTGCTCAAAGAGCATTTGTTCAAGCAAAACTTGATGCAGGAGAGCAGTTAGTA
    GGCTATAAGCTTGGACTTACATCTAGGAATAAACAAAGAGCTATGGGTGTAGATTGCCC
    ACTTTATGGAAGAGTTACGTCCTCTATGTTGGCCACATATGGAGATCCAATACCATTCGA
    CAGATTCATACATCCTAGAGTTGAGTCTGAAATTGCATTCTTATTGAAACAAGATGTTACT
    GCTCCTGCTACAGTATCATCCGTACTTGCTGCAACTGATGTAGTTTTTGGTGCAGTGGAT
    GTTTTGGATTCAAGATATGAAGGATTTAAGTTTACTCTAGAAGATGTAGTTGCAGATAAT
    GCCAGTGCAGGAGCTTTTTACCTTGGACCTGTTGCTAGACCTGCTACAGAGTTAAGACTT
    GATTTACTAGGATGTATAGTTAGAGTTGACGGAGAAGTTACAATGACAGCGGCTGGTGC
    CGCTGTTATGGGACACCCTGCTGCTGCTGTAGCATGGTTAGCTAATCAACTTGCACTTGA
    GGGTGAAAGCTTGAAGGCAGGTCAGCTTATCTTTAGCGGTGGGGTCACTGCTCCTGTTC
    CAGTAGTTCCTGGTGGAAGCGTGACCTTTGAATTTGATGGCCTAGGTGTAATAGAAGTA
    GCAGGAGCC (SEQ ID NO: 139)
  • Production of Propylene from carbon monoxide. C. ethanogenum transformed with the vector described above are used to inoculate 2 ml PETC media containing 4 μg/ μl Clarithromycin. When growth occurs, the culture is upscaled into 5 ml and later 50 ml PETC media containing 4 μg/ μl Clarithromycin and 30 psi steel mill gas as sole carbon source. The bottles are then shaken continuously while being incubated at 37° C. The headspace gas is refreshed every 2 days; however, immediately prior to refreshing the headspace, samples are drawn from both the liquid phase and headspace using a 10 μL Hamilton syringe and injected into a HP5890 GC equipped with a CP-PoraBOND U 25 m×0.32 mm column and an FID maintained at 200° C. The injector is connected in splitless mode and maintained at 250° C. Samples are run with He Gas at 7.3 ml/min as a carrier gas; the oven program is set as follows: hold at 50° C. 1.5 min; ramp to 300° C. at 10° C./min; hold at 300° C. 10 min. Propylene is identified by retention time compared to pure propylene diluted in air or dissolved in pure H2O. Samples are also taken to measure optical density of the culture, allowing quantitation of specific propylene production rates per cell. Note that because carbon monoxide is the only carbon source provided to the cells, all propylene produced must have been derived from carbon monoxide.
    • Example 5 Escherichia Coli Heterotroph
  • Growth and Transformation. Growth and transformation methods for E. coli are well-known in the art. E. coli strains were transformed by electroporation using the appropriate plasmids. A single colony from a fresh transformation was then used to seed an overnight culture grown in Luria Broth (LB) supplemented with 1.5% (w/v) glucose and appropriate antibiotics at 37° C. in a rotary shaker (200 r.p.m.). Antibiotics were used at a concentration of 50 μg/ml for strains with a single resistance marker. For strains with multiple resistance markers, kanamycin and chloramphenicol were used at 25 μg/ml and carbenicillin was used at 50 μg/ml.
  • Cloning and expression of 4-OD genes. 4-OD genes were identified from BLAST searching of the NCBI database using the Pseudomonas putida 4-OD sequence as a starting sequence. 24 individual 4-OD proteins were chosen for expression studies. The proteins were reverse-translated and codon-optimized for E. coli using commercial methods (DNA2.0, Inc. Menlo Park, Calif.). The genes were then cloned under control of a T7 promoter and expressed in E. coli BL21 (DE3). Briefly, single colonies were inoculated into 2 mL cultures of LB containing 50 μg/mL kanamycin and shaken overnight at 37° C. 1 mL of the saturated overnight culture was then inoculated into 200 mL LB containing 50 μg/mL kanamycin in a 2 L flask. The flasks were then shaken at 37° C. for 3-4 hours until an OD600 of 0.5-1.0 was reached. The cultures were induced by addition of 1 mM IPTG and shaken for additional 3 h at 37° C. Cells were harvested by centrifugation and analyzed by SDS-PAGE to confirm protein expression (see FIG. 5). Activity in cell lysates was confirmed by measuring decarboxylation activity on 4-oxalocrotonate (see FIG. 6).
    • 4-OD Lysate Preparation
  • Lysates were generated by resuspending induced E. coli cell pellet (equivalent to 1 mL culture) in 0.5 mL lysis buffer (20 mM KHPO4 pH 8.0; 0.3 M KCl; 10% (w/v) glycerol; 0.1% NP-40; 0.5 mg/ml lysozyme; 1 mM PMSF). Cells were sonicated 5 seconds and then centrifuged for 15 min at 15,000×g, 4° C. The cleared supernatant was assayed immediately or stored at −80° C. for later assay.
    • 4-Oxalocrotonate Decarboxylation Activity Assay
  • The assay buffer comprised 100 mM Tris-HCl pH 7.4; 3.3 mM MgSO4; 1 mM 4-oxalocrotonate (the stock solution of 4-oxalocrotonate was pre-equilibrated with a 1:100 dilution of E. coli lysate expressing 4-oxalocrotonate tautomerase from Pseudomonas putida (UniProtKB/Swiss-Prot Accession No. Q01468, geneid 87856) to achieve a distribution of keto and enol forms of 4-oxalocrotonate). Total reaction volume was 200 μl in a 96 well UV transparent plate and read on a SpectraMax Plate Reader (Molecular Devices). The reaction was initiated by addition of 4-OD containing lysates at 1:10 to 1:1000 final dilutions. Reactions were run at 25° C. Consumption of substrate was monitored by measuring drop in absorbance at 240 nm for the keto tautomer and at 300 nm for the enol tautomer (see FIG. 6).
    • Crotonate Decarboxylation Assay
  • The assay buffer comprised 100 mM Tris-HCl pH 7.4; 3.3 mM MgSO4; 87.2 mM crotonic acid. Reactions were initiated by adding lysates to a final concentration of 1:10 to 1:100 in 1 ml volume in a TargetDP vial (2 ml total volume). Reactions were incubated from 12 to 72 hours at room temperature. Generated propylene was detected by injection of 0.5 μl aqueous phase plus 2 μl headspace gas onto a HP5890 GC equipped with a CP-PoraBOND U 25 m×0.32 mm column and an FID maintained at 200° C. The injector was connected in splitless mode and maintained at 250° C. Samples were run with He Gas at 7.3 ml/min as a carrier gas; the oven program was set as follows: hold at 50° C. 1.5 min; ramp to 300° C. at 10° C./min; hold at 300° C. 10 min. Propylene was identified by retention time compared to pure propylene diluted in air or dissolved in pure H2O (see FIG. 7).
    • Introduction of Propylene Synthesis Pathway
  • Introduction of the pathway is performed essentially as described in Bond-Watts et al., Enzyme mechanism as a kinetic control element for designing synthetic biofuel pathways. Nat. Chem. Biol. 7: 222-227, 2011.
  • Selected phaA (SEQ ID NO:77), phaB (SEQ ID NO:123), crotonase (SEQ ID NO:32), crotonyl-coA thioesterase (SEQ ID NO:29), and 4-oxalocrotonate decarboxylase (SEQ ID NO:10) sequences were codon optimized (see Table 8) and synthesized with appropriate promoters. The genes are then cloned and transformed into E. coli strain BL21 (DE3). Transformation is confirmed by resistance of the cells to antibiotic selection, and gene expression is confirmed by northern blot (to confirm RNA transcription), western blot, or ELISA methods (to confirm protein expression).
  • TABLE 8
    Codon Optimized Sequences for E. coli
    Reference
    Sequence Codon Optimized Sequence (SEQ ID NO: #)
    phaA ATGACCGACGTGGTGATCGTGAGCGCTGCGCGCACGGCGGTTGGCAAGTTTGGTGGTA
    GCCTGGCGAAGATCGCGGCACCGGAGTTGGGCGCCAGCGTTATTCGTGCCGTCCTGGAA
    CGCGCAGGTGTGAAACCGGAGCAGGTGAGCGAAGTGATCCTGGGTCAAGTGCTGACCG
    CAGGCAGCGGTCAAAACCCGGCACGTCAAGCCTTGATTGCCGCAGGTCTGCCAAACGCT
    GTTCCGGGCATGACCATTAACAAAGTGTGTGGTTCTGGTCTGAAAGCGGTGATGCTGGC
    TGCGAACGCGGTTGTCGCCGGTGATGCGGAAATTGTGGTCGCGGGTGGCCAGGAGAAT
    ATGTCCGCAGCTCCGCACGTGCTGCCGGGCAGCCGTGACGGTTTCCGTATGGGCGATGC
    TAAATTGGTAGATAGCATGATTGTTGACGGCTTGTGGGACGTGTATAACAAATATCACAT
    GGGTATCACCGCGGAAAACGTTGCGAAAGAGTACGGTATCACCCGTGAGGCGCAGGAC
    CAGTTTGCCGCACTGAGCCAGAACAAGGCCGAAGCGGCGCAAAAAGCAGGCCGTTTTG
    ATGATGAGATCGTTCCGATTGAGATTCCGCAGCGTAAAGGTGAACCGCTGCGCTTCGCT
    ACCGACGAGTTTGTCCGTCACGGCGTTACCGCCGAATCCCTGGCCTCTTTGAAACCGGCG
    TTTGCTAAAGAGGGTACCGTCACCGCGGCAAACGCAAGCGGTATTAACGATGGCGCAGC
    AGCTGTCCTGGTTATGTCCGCGAAGAAGGCAGAAGCGTTGGGCCTGGAGCCGCTGGCTC
    GCATTAAAGCATATGCCAATGCCGGCGTTGATCCGAGCGTTATGGGCATGGGTCCGGTC
    CCGGCAAGCCGTCGTTGCCTGGAGCGTGCAGGCTGGTCCGTTGGCGACCTGGATCTGAT
    GGAGATCAATGAAGCCTTCGCAGCGCAGGCGCTGGCAGTGCACAAGCAGATGGGTTGG
    GACACCAGCAAGGTTAATGTCAATGGTGGCGCAATCGCCATTGGCCATCCTATCGGTGC
    GAGCGGTTGTCGTATTTTGGTTACCCTGCTGCATGAAATGCTGAAACGCGACGCCAAGC
    GTGGCCTGGCTAGCCTGTGCATCGGTGGTGGTATGGGTGTGGCGCTGGCGCTGGAACG
    TCCA (SEQ ID NO: 140)
    pha B ATGAAGAAAGTATGCGTCATCGGTGCGGGCACCATGGGCAGCGGTATTGCGCAGGCGT
    TTGCAGCCAAGGGCTTCGAGGTGGTCCTGCGCGATATCAAAGATGAGTTCGTTGATCGC
    GGTTTGGACTTCATCAACAAAAACCTGAGCAAGCTGGTTAAGAAGGGTAAGATCGAAGA
    GGCGACGAAGGTTGAAATTCTGACCCGCATCAGCGGTACTGTTGACCTGAATATGGCGG
    CAGACTGCGATTTGGTTATTGAAGCTGCGGTCGAGCGTATGGACATTAAGAAGCAGATT
    TTCGCCGATCTGGACAACATTTGTAAGCCGGAGACGATTCTGGCGAGCAACACCAGCAG
    CTTGAGCATTACCGAGGTGGCCTCTGCCACGAAGCGTCCGGATAAGGTCATCGGTATGC
    ACTTCTTTAACCCGGCTCCGGTGATGAAACTGGTCGAGGTGATCCGCGGTATTGCTACCA
    GCCAAGAAACGTTTGACGCTGTGAAAGAGACGTCGATCGCTATCGGCAAGGATCCGGTT
    GAGGTGGCAGAAGCTCCGGGTTTTGTGGTGAATCGCATCCTGATCCCGATGATCAACGA
    GGCCGTAGGTATCCTGGCCGAGGGTATTGCCTCTGTGGAAGATATCGACAAGGCGATGA
    AACTGGGTGCTAATCACCCGATGGGTCCGTTGGAGCTGGGTGACTTCATCGGTCTGGAC
    ATTTGTCTGGCGATCATGGACGTTCTGTACTCTGAGACGGGCGACAGCAAATATCGCCCG
    CACACCCTGCTGAAAAAGTACGTTCGTGCTGGTTGGCTGGGTCGTAAGTCTGGCAAAGG
    CTTCTACGATTACAGCAAG(SEQ ID NO: 141)
    crotonase ATGGAGCTGAATAATGTGATTCTGGAGAAAGAGGGCAAAGTCGCTGTTGTTACGATTAA
    CCGCCCGAAGGCATTGAACGCCCTGAACAGCGATACCCTGAAAGAGATGGATTACGTGA
    TTGGCGAGATCGAAAACGACAGCGAAGTTCTGGCCGTCATTCTGACTGGTGCCGGTGAA
    AAGAGCTTTGTCGCGGGTGCAGATATTAGCGAGATGAAAGAGATGAATACGATCGAAG
    GTCGTAAATTCGGTATCCTGGGCAATAAAGTCTTTCGTCGTTTGGAACTGCTGGAGAAAC
    CTGTCATCGCTGCCGTGAATGGCTTCGCGCTGGGCGGTGGCTGCGAGATTGCAATGAGC
    TGCGATATCCGTATCGCGAGCAGCAATGCGCGTTTCGGTCAACCGGAAGTGGGTCTGGG
    TATCACGCCGGGTTTTGGTGGCACCCAACGCCTGAGCCGTTTGGTTGGCATGGGTATGG
    CAAAACAACTGATCTTTACCGCGCAGAACATCAAAGCAGATGAAGCTCTGCGCATTGGCT
    TGGTCAATAAGGTGGTTGAGCCGAGCGAACTGATGAACACGGCGAAAGAGATCGCGAA
    CAAGATCGTGAGCAATGCACCGGTGGCCGTCAAACTGAGCAAACAGGCCATCAATCGTG
    GTATGCAATGTGATATCGACACCGCGCTGGCATTCGAAAGCGAGGCATTTGGTGAGTGC
    TTCAGCACGGAAGATCAAAAGGATGCAATGACGGCGTTCATTGAAAAACGTAAGATTGA
    AGGCTTCAAGAACCGC (SEQ ID NO: 142)
    crotonyl-coA ATGCATCGTACGAGCAACGGCAGCCACGCCACCGGTGGCAATCTGCCTGATGTCGCGAG
    thioesterase CCATTATCCGGTTGCATACGAACAGACCCTGGACGGCACCGTCGGTTTCGTGATTGACGA
    AATGACTCCGGAGCGTGCCACCGCGAGCGTTGAGGTCACCGATACCCTGCGCCAGCGTT
    GGGGTCTGGTTCATGGTGGTGCATATTGTGCGTTGGCAGAGATGTTGGCGACTGAAGCG
    ACCGTCGCAGTAGTCCATGAAAAGGGCATGATGGCGGTGGGCCAAAGCAATCACACCA
    GCTTTTTCCGTCCGGTTAAAGAGGGCCATGTTCGCGCAGAGGCGGTGCGTATTCACGCG
    GGTAGCACGACCTGGTTCTGGGACGTTAGCCTGCGCGATGACGCAGGTCGTCTGTGTGC
    AGTTAGCAGCATGTCTATTGCTGTCCGTCCGCGTCGCGAC (SEQ ID NO: 143)
    4-oxa locrotonate ATGAGCACCACGAGCATTACCCCGGACGAAATCGCGCAGGTTCTGCTGGCAGGCGAGC
    decarboxylase GTAATCGCACCGAGGTGGCGCAATTTTCTGCGTCGCACCCGGATTTGGATGTCCGTACCG
    CGTACGCGGCACAACGTGCGTTCGTTCAGGCTAAACTGGACGCAGGTGAACAACTGGTC
    GGTTACAAATTGGGTCTGACGTCTCGTAATAAGCAGCGCGCAATGGGTGTCGACTGCCC
    GCTGTACGGCCGTGTTACCAGCAGCATGCTGGCCACCTATGGTGATCCGATTCCGTTTGA
    CCGCTTTATTCACCCACGTGTGGAGTCCGAAATTGCGTTCCTGCTGAAGCAAGATGTGAC
    CGCACCGGCGACGGTCAGCAGCGTTCTGGCAGCGACTGACGTCGTGTTTGGCGCGGTTG
    ACGTCCTGGATAGCCGTTACGAGGGCTTCAAGTTCACCCTGGAAGATGTTGTTGCAGAC
    AATGCATCTGCGGGTGCTTTCTATCTGGGTCCAGTTGCACGTCCAGCGACGGAGCTGCGT
    CTGGATCTGCTGGGTTGCATTGTGCGCGTCGACGGCGAAGTGACCATGACCGCAGCGGG
    TGCCGCGGTTATGGGCCACCCGGCAGCGGCCGTTGCGTGGCTGGCCAATCAGCTGGCCC
    TGGAAGGTGAAAGCCTGAAGGCGGGTCAGCTGATCTTCAGCGGTGGTGTCACTGCGCC
    GGTCCCGGTTGTGCCGGGTGGCAGCGTGACCTTCGAGTTTGACGGCCTGGGTGTCATCG
    AAGTGGCAGGTGCA (SEQ ID NO: 144)
  • Production of Propylene from glycerol. Overnight cultures of freshly transformed E. coli strains are grown for 12-16 h in Terrific Broth (TB) at 37° C. and used to inoculate TB (50 ml) with 1.5% (w/v) glycerol and appropriate antibiotics to an optical density at 600 nm (OD600) of 0.05 in a 250 ml-baffled flask. The cultures are grown at 37° C. in a rotary shaker (200 r.p.m.) and induced with IPTG (1.0 mM) and L-arabinose (0.2% (w/v) (these inducers are dependent on the promoters used for plasmid construction; choice of inducer are apparent to those of skill in the art) at OD600=0.35-0.45. At this time, the growth temperature is reduced to 30° C., and the culture flasks are sealed with butyl rubber stoppers to prevent propylene evaporation. Additional glucose (1% (w/v)) is added concurrent with culture sampling after 1 d. Flasks are unsealed for 10 to 30 min every 24 h then resealed after sampling. Samples are drawn from both the liquid phase and headspace using a 10 μL Hamilton syringe and injected into a HP5890 GC equipped with a CP-PoraBOND U 25 m×0.32 mm column and an FID maintained at 200° C. The injector is connected in splitless mode and maintained at 250° C. Samples are run with He Gas at 7.3 ml/min as a carrier gas; the oven program is set as follows: hold at 50° C. 1.5 min; ramp to 300° C. at 10° C./min; hold at 300° C. 10 min. Propylene is identified by retention time compared to pure propylene diluted in air or dissolved in pure H2O. Samples are also taken to measure optical density of the culture, allowing quantitation of specific propylene production rates per cell.
  • Production of Propylene from glucose. Overnight cultures of freshly transformed E. coli strains are grown for 12-16 h in Terrific Broth (TB) at 37° C. and used to inoculate TB (50 ml) with 1.5% (w/v) glucose replacing the standard glycerol supplement and appropriate antibiotics to an optical density at 600 nm (OD600) of 0.05 in a 250 ml-baffled flask. The cultures are grown at 37° C. in a rotary shaker (200 r.p.m.) and induced with IPTG (1.0 mM) and L-arabinose (0.2% (w/v)) at OD600=0.35-0.45. At this time, the growth temperature is reduced to 30° C., and the culture flasks are sealed with butyl rubber stoppers to prevent propylene evaporation. Additional glucose (1% (w/v)) is added concurrent with culture sampling after 1 d. Flasks are unsealed for 10 to 30 min every 24 h then resealed after sampling. Samples are drawn from both the liquid phase and headspace using a 10 μL Hamilton syringe and injected into a HP5890 GC equipped with a CP-PoraBOND U 25 m×0.32 mm column and an FID maintained at 200° C. The injector is connected in splitless mode and maintained at 250° C. Samples are run with He Gas at 7.3 ml/min as a carrier gas; the oven program is set as follows: hold at 50° C. 1.5 min; ramp to 300° C. at 10° C./min; hold at 300° C. 10 min. Propylene is identified by retention time compared to pure propylene diluted in air or dissolved in pure H2O. Samples are also taken to measure optical density of the culture, allowing quantitation of specific propylene production rates per cell.
  • The disclosure of U.S. Provisional Application No. 61/702,534, filed on Sep. 18, 2012, and U.S. Non-provisional Application No. 14/429,327, filed on Mar. 18, 2015, are incorporated herein by reference in their entirety.
  • The various embodiments described above can be combined to provide further embodiments. All of the U.S. patents, U.S. patent application publications, U.S. patent applications, foreign patents, foreign patent applications and non-patent publications referred to in this specification and/or listed in the Application Data Sheet, including U.S. Provisional Application No. 61/702,534 filed on Sep. 18, 2012, are incorporated herein by reference, in their entirety. Aspects of the embodiments can be modified, if necessary to employ concepts of the various patents, applications and publications to provide yet further embodiments.
  • These and other changes can be made to the embodiments in light of the above-detailed description. In general, in the following claims, the terms used should not be construed to limit the claims to the specific embodiments disclosed in the specification and the claims, but should be construed to include all possible embodiments along with the full scope of equivalents to which such claims are entitled. Accordingly, the claims are not limited by the disclosure.

Claims (20)

What is claimed is:
1. A modified methanotrophic bacterium, wherein the modified methanotrophic bacterium comprises:
(a) a heterologous nucleic acid molecule encoding a crotonase, wherein the modified methanotrophic bacterium produces crotonyl-CoA from a C1 substrate comprising methane; and
(b) a parent methanotrophic bacterium selected from Methylosinus trichosporium OB3b, Methylococcus capsulatus Bath, Methylomonas methanica 16a, Methylosinus trichosporium, Methylosinus sporium, Methylocystis parvus, Methylomonas methanica, Methylomonas albus, Methylobacter capsulatus, Methylobacterium organophilum, Methylomonas sp AJ-3670, Methylocella silvestris, Methylomicrobium alcaliphilum, or a growth variant thereof; and
wherein the modified methanotrophic bacterium produces n-butanol, butyraldehyde, or 1,4-butanediol.
2. The modified methanotrophic bacterium of claim 1, wherein the methanotrophic bacterium is an obligate methanotrophic bacterium.
3. The modified methanotrophic bacterium of claim 1, wherein the heterologous nucleic acid molecule further encodes a butyryl-CoA dehydrogenase, whereby a butyryl-CoA intermediate is produced and the modified methanotrophic bacterium produces n-butanol, butyraldehyde, or both.
4. The modified methanotrophic bacterium of claim 3, wherein the heterologous nucleic acid molecule further encodes an aldehyde dehydrogenase, and the modified methanotrophic bacterium produces n-butanol, butyraldehyde, or both.
5. The modified methanotrophic bacterium of claim 1, wherein the heterologous nucleic acid molecule further encodes a crotonyl-CoA hydratase, whereby a hydroxybutyryl-CoA intermediate is produced and the modified methanotrophic bacterium produces 1,4-butanediol.
6. The modified methanotrophic bacterium of claim 4, wherein the modified methanotrophic bacterium does not have a functional PHB synthase or a substantial amount of functional PHB synthase.
7. The modified methanotrophic bacterium of claim 5, wherein the modified methanotrophic bacterium does not have a functional PHB synthase or a substantial amount of functional PHB synthase.
8. The modified methanotrophic bacterium of claim 6, wherein the PHB synthase is encoded by phaC or phbC.
9. The modified methanotrophic bacterium of claim 7, wherein the PHB synthase is encoded by phaC or phbC.
10. The modified methanotrophic bacterium of claim 4, wherein the modified methanotrophic bacterium has a functional β-ketothiolase activity and a functional acetoacetyl coenzyme A reductase activity.
11. The modified methanotrophic bacterium of claim 5, wherein the modified methanotrophic bacterium has a functional β-ketothiolase activity and a functional acetoacetyl coenzyme A reductase activity.
12. The modified methanotrophic bacterium of claim 10, wherein the β-ketothiolase is encoded by phaA or phbA.
13. The modified methanotrophic bacterium of claim 10, wherein the acetoacetyl coenzyme A reductase is encoded by phaB or phbB.
14. The modified methanotrophic bacterium of claim 11, wherein the β-ketothiolase is encoded by phaA or phbA.
15. The modified methanotrophic bacterium of claim 11, wherein the acetoacetyl coenzyme A reductase is encoded by phaB or phbB.
16. The modified methanotrophic bacterium of claim 6, wherein the modified methanotrophic bacterium does not produce a substantial amount of polyhydroxybutyrate.
17. The modified methanotrophic bacterium of claim 7, wherein the modified methanotrophic bacterium does not produce a substantial amount of polyhydroxybutyrate.
18. The modified methanotrophic bacterium of claim 1, wherein the C1 substrate comprising methane comprises natural gas.
19. A method for producing n-butanol and/or butyraldehyde, comprising culturing the modified methanotrophic bacterium of claim 1 on a C1 substrate comprising methane under conditions sufficient to produce n-butanol and/or butyraldehyde.
20. A method for producing 1,4-butanediol, comprising culturing the modified methanotrophic bacterium of claim 1 on a C1 substrate comprising methane under conditions sufficient to produce 1,4-butanediol.
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