PRODUCTION OF FATTY ACID DERIVATIVES
The invention relates to compositions and methods, including polynucleotide sequences, amino acid sequences, recombinant host cells and recombinant host cell cultures engineered to produce fatty acid derivative compositions comprising fatty acids, fatty alcohols, fatty aldehydes, fatty esters, alkanes, terminal olefins, internal olefins or ketones. The fatty acid derivative composition is produced extracellularly with a higher titer, yield or productivity than the corresponding wild type or non-engineered host cell.
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The invention relates to engineered host cells together with vector and strain modifications effective to improve the titer, yield and productivity of fatty acid derivatives relative to “wild-type” or non-engineered host cells. The invention further relates to methods of making and using such modified vectors and strains for the fermentative production of fatty acid derivatives and fatty acid derivative compositions.
BACKGROUND OF THE INVENTIONFatty acid derivatives including fatty aldehydes, fatty alcohols, hydrocarbons (alkanes and olefins), fatty esters (e.g., waxes, fatty acid esters, or fatty esters) and ketones comprise important categories of industrial chemicals and fuels. These molecules and their derivatives have numerous applications including use as surfactants, lubricants, plasticizers, solvents, emulsifiers, emollients, thickeners, flavors, fragrances, and fuels.
Crude petroleum is currently a primary source of raw materials for producing petrochemicals and fuels. The two main classes of raw materials derived from petroleum are short chain olefins (e.g., ethylene and propylene) and aromatics (e.g., benzene and xylene isomers). These raw materials are derived from longer chain hydrocarbons in crude petroleum by cracking it at considerable expense using a variety of methods, such as catalytic cracking, steam cracking, or catalytic reforming. These raw materials can be used to make petrochemicals such as monomers, solvents, detergents, and adhesives, which otherwise cannot be directly refined from crude petroleum.
Petrochemicals, in turn, can be used to make specialty chemicals, such as plastics, resins, fibers, elastomers, pharmaceuticals, lubricants, and gels. Particular specialty chemicals that can be produced from petrochemical raw materials include fatty acids, hydrocarbons, fatty aldehydes, fatty alcohols, esters, ketones, etc.
Hydrocarbons have many commercial uses. For example, shorter chain alkanes and alkenes are used in transportation fuels. Longer chain alkenes are used in plastics, lubricants, and synthetic lubricants. In addition, alkenes are used as a feedstock to produce alcohols, esters, plasticizers, surfactants, tertiary amines, enhanced oil recovery agents, fatty acids, thiols, alkenylsuccinic anhydrides, epoxides, chlorinated alkanes, chlorinated alkenes, waxes, fuel additives, and drag flow reducers.
Esters have many commercial uses. For example, biodiesel, an alternative fuel, is comprised of esters (e.g., fatty acid methyl ester, fatty acid ethyl esters, etc.). Some low molecular weight esters are volatile with a pleasant odor which makes them useful as fragrances or flavoring agents. In addition, esters are used as solvents for lacquers, paints, and varnishes. Furthermore, some naturally occurring substances, such as waxes, fats, and oils are comprised of esters. Esters are also used as softening agents in resins and plastics, plasticizers, flame retardants, and additives in gasoline and oil. In addition, esters can be used in the manufacture of polymers, films, textiles, dyes, and pharmaceuticals.
Aldehydes are used to produce many specialty chemicals. For example, aldehydes are used to produce polymers, resins (e.g., Bakelite), dyes, flavorings, plasticizers, perfumes, pharmaceuticals, and other chemicals, some of which may be used as solvents, preservatives, or disinfectants. In addition, certain natural and synthetic compounds, such as vitamins and hormones, are aldehydes, and many sugars contain aldehyde groups. Fatty aldehydes can be converted to fatty alcohols by chemical or enzymatic reduction.
Fatty alcohols have many commercial uses. The shorter chain fatty alcohols are used in the cosmetic and food industries as emulsifiers, emollients, and thickeners. Due to their amphiphilic nature, fatty alcohols behave as nonionic surfactants, which are useful in personal care and household products, such as, for example, detergents. In addition, fatty alcohols are used in waxes, gums, resins, pharmaceutical salves and lotions, lubricating oil additives, textile antistatic and finishing agents, plasticizers, cosmetics, industrial solvents, and solvents for fats.
Fatty alcohols are aliphatic alcohols consisting of a chain of 8 to 22 carbon atoms. Fatty alcohols usually have even number of carbon atoms and a single alcohol group (—OH) attached to the terminal carbon. Some are unsaturated and some are branched. They are widely used in industrial chemistry. Most fatty alcohols in nature are found as waxes which are esters with fatty acids and fatty alcohols. They are produced by bacteria, plants and animals.
Currently, fatty alcohols are produced via catalytic hydrogenation of fatty acids produced from natural sources, such as coconut oil, palm oil, palm kernel oil, tallow and lard, or by chemical hydration of alpha-olefins produced from petrochemical feedstocks. Fatty alcohols derived from natural sources have varying chain lengths. The chain length of fatty alcohols is important and specific to particular applications. Dehydration of fatty alcohols to alpha-olefins can also be accomplished by chemical catalysis.
Due to the inherent challenges posed by exploring, extracting, transporting and refining petroleum for use in chemical and fuel products, there is a need for a an alternate source which can be produced economically and used for chemical and fuel production. There is also a need for a petroleum replacement that does not cause the type of environmental damage created by the exploring, extracting, transporting and refining petroleum and the burning of petroleum-based fuels.
One method of producing renewable petroleum is by engineering host cells to produce renewable petroleum products. Biologically derived fuels and chemicals offer advantages over petroleum based fuels. Biologically derived chemicals such as hydrocarbons (e.g., alkanes, alkenes, or alkynes), fatty alcohols, esters, fatty acids, fatty aldehydes, and ketones are directly converted from biomass to the desired chemical product.
In order for the use of biologically-derived fatty acid derivatives from fermentable sugars or biomass to be commercially viable as a source for production of renewable chemicals and fuels, the process must be optimized for efficient conversion and recovery of product. The development of biologically derived fuels and chemicals has been a focus of research and development in recent years, however, there remains a need for improvement in the relevant processes and products in order for biologically derived fuels and chemicals to become a commercially viable option. Areas for improvement include the energy efficiency of the production process and product yield. The current invention addresses this need.
SUMMARY OF THE INVENTIONThe present invention provides novel genetically engineered host cells which produce fatty acid derivative compositions at a high titer, yield or productivity; cell cultures comprising such novel genetically engineered host cells and methods of using the same. The invention also provides methods of making compositions comprising fatty acid derivatives by culturing the genetically engineered host cells of the invention, compositions made by such methods, and other features apparent upon further review.
In one embodiment, the invention provides a cultured genetically engineered host cell comprising (a) a polynucleotide sequence encoding one or more of: (i) an acetyl-CoA carboxylase (EC 6.4.1.2) polypeptide, (ii) a FadR polypeptide, (iii) a heterologous iFAB polypeptide, (iv) a sequence having a transposon insertion in the yijP gene, and (v) a heterologous ACP protein; as well as (b) a polynucleotide sequence encoding a fatty acid derivative biosynthetic polypeptide, wherein the genetically engineered host cell produces a fatty acid derivative composition at a higher titer, yield or productivity when cultured in medium containing a carbon source under conditions effective to overexpress the polynucleotide(s) relative to a corresponding wild type host cell propagated under the same conditions as the genetically engineered host cell.
The fatty acid derivative composition includes one or more of a fatty acid, a fatty aldehyde, a fatty alcohol, a fatty ester, an alkane, a terminal olefin, an internal olefin and a ketone.
In one embodiment, the genetically engineered host cell produces a fatty acid derivative composition with a titer, yield or productivity that is at least 3 times greater, at least 5 times greater, at least 8 times greater, or at least 10 times greater than the titer of a fatty acid derivative composition produced by a corresponding wild type (non-engineered) host cell propagated under the same conditions as the genetically engineered host cell (e.g., a titer of from 30 g/L to 250 g/L, a yield of from 10% to 40%, or a productivity of 0.7 mg/L/hr to 3 g/L/hr).
In some embodiments, the fatty acid derivative composition is produced extracellularly.
In other embodiments, the host cell is further engineered to comprise a heterologous acp sequence with or without an introduced sfp gene.
The polynucleotide sequence encoding a fatty acid derivative biosynthetic polypeptide is selected from the group consisting of a polypeptide:
(a) having thioesterase activity, wherein the recombinant host cell synthesizes fatty acids;
(b) having thioesterase activity and carboxylic acid reductase (“CAR”) activity, wherein the recombinant host cell synthesizes fatty aldehydes and fatty alcohols;
(c) having thioesterase activity, carboxylic acid reductase activity and alcohol dehydrogenase activity wherein the recombinant host cell synthesizes fatty alcohols;
(d) having acyl-CoA reductase (“AAR”) activity wherein the recombinant host cell synthesizes fatty aldehydes and fatty alcohols;
(e) having acyl-CoA reductase (“AAR”) activity and alcohol dehydrogenase activity wherein the recombinant host cell synthesizes fatty alcohols;
(f) having fatty alcohol forming acyl-CoA reductase (“FAR”) activity, wherein the recombinant host cell synthesizes fatty alcohols;
(g) having thioesterase activity, carboxylic acid reductase activity and aldehyde decarbonylase activity, wherein the recombinant host cell synthesizes alkanes;
(h) having acyl-CoA reductase (“AAR”) activity and aldehyde decarbonylase activity, wherein the recombinant host cell synthesizes alkanes;
(i) having ester synthase activity wherein the recombinant host cell synthesizes fatty esters;
(j) having thioesterase activity, acyl-CoA synthase activity and ester synthase activity wherein the recombinant host cell synthesizes fatty esters;
(k) having OleA activity, wherein the recombinant host cell synthesizes aliphatic ketones;
(l) having OleABCD activity, wherein the recombinant host cell synthesizes internal olefins; and
(m) having thioesterase activity and decarboxylase activity, wherein the recombinant host cell synthesizes terminal olefins.
These and other embodiments of the present invention will readily occur to those of ordinary skill in the art in view of the disclosure herein.
The invention is based, at least in part, on the discovery that modification of various aspects of the fatty acid biosynthetic pathway in a recombinant host cell facilitates enhanced production of fatty acid derivatives by the host cell.
The invention relates to compositions of fatty acid derivatives having desired characteristics and methods for producing the same. Further, the invention relates to recombinant host cells (e.g., microorganisms), cultures of recombinant host cells, methods of making and using recombinant host cells, for example, use of cultured recombinant host cells in the fermentative production of fatty acid derivatives having desired characteristics.
All patents, publications, and patent applications cited in this specification are herein incorporated by reference as if each individual patent, publication, or patent application was specifically and individually indicated to be incorporated by reference in its entirety for all purposes.
DEFINITIONSAs used in this specification and the appended claims, the singular forms “a,” “an” and “the” include plural referents unless the context clearly dictates otherwise. Thus, for example, reference to “a recombinant host cell” includes two or more such recombinant host cells, reference to “a fatty alcohol” includes one or more fatty alcohols, or mixtures of fatty alcohols, reference to “a nucleic acid coding sequence” includes one or more nucleic acid coding sequences, reference to “an enzyme” includes one or more enzymes, and the like.
Unless defined otherwise, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which the invention pertains. Although other methods and materials similar, or equivalent, to those described herein can be used in the practice of the present invention, the preferred materials and methods are described herein.
In describing and claiming the present invention, the following terminology will be used in accordance with the definitions set out below.
Accession Numbers: Sequence Accession numbers throughout this description were obtained from databases provided by the NCBI (National Center for Biotechnology Information) maintained by the National Institutes of Health, U.S.A. (which are identified herein as “NCBI Accession Numbers” or alternatively as “GenBank Accession Numbers”), and from the UniProt Knowledgebase (UniProtKB) and Swiss-Prot databases provided by the Swiss Institute of Bioinformatics (which are identified herein as “UniProtKB Accession Numbers”).
Enzyme Classification (EC) Numbers: EC numbers are established by the Nomenclature Committee of the International Union of Biochemistry and Molecular Biology (IUBMB), description of which is available on the IUBMB Enzyme Nomenclature website on the World Wide Web. EC numbers classify enzymes according to the reaction catalyzed.
As used herein, the term “nucleotide” refers to a monomeric unit of a polynucleotide that consists of a heterocyclic base, a sugar, and one or more phosphate groups. The naturally occurring bases (guanine, (G), adenine, (A), cytosine, (C), thymine, (T), and uracil (U)) are typically derivatives of purine or pyrimidine, though it should be understood that naturally and non-naturally occurring base analogs are also included. The naturally occurring sugar is the pentose (five-carbon sugar) deoxyribose (which forms DNA) or ribose (which forms RNA), though it should be understood that naturally and non-naturally occurring sugar analogs are also included. Nucleic acids are typically linked via phosphate bonds to form nucleic acids or polynucleotides, though many other linkages are known in the art (e.g., phosphorothioates, boranophosphates, and the like).
As used herein, the term “polynucleotide” refers to a polymer of ribonucleotides (RNA) or deoxyribonucleotides (DNA), which can be single-stranded or double-stranded and which can contain non-natural or altered nucleotides. The terms “polynucleotide,” “nucleic acid sequence,” and “nucleotide sequence” are used interchangeably herein to refer to a polymeric form of nucleotides of any length, either RNA or DNA. These terms refer to the primary structure of the molecule, and thus include double- and single-stranded DNA, and double- and single-stranded RNA. The terms include, as equivalents, analogs of either RNA or DNA made from nucleotide analogs and modified polynucleotides such as, though not limited to methylated and/or capped polynucleotides. The polynucleotide can be in any form, including but not limited to, plasmid, viral, chromosomal, EST, cDNA, mRNA, and rRNA.
As used herein, the terms “polypeptide” and “protein” are used interchangeably to refer to a polymer of amino acid residues. The term “recombinant polypeptide” refers to a polypeptide that is produced by recombinant techniques, wherein generally DNA or RNA encoding the expressed protein is inserted into a suitable expression vector that is in turn used to transform a host cell to produce the polypeptide.
As used herein, the terms “homolog,” and “homologous” refer to a polynucleotide or a polypeptide comprising a sequence that is at least about 50% identical to the corresponding polynucleotide or polypeptide sequence. Preferably homologous polynucleotides or polypeptides have polynucleotide sequences or amino acid sequences that have at least about 80%, 81%, 82%, 83%, 84%, 85%, 86%, 87%, 88%, 89%, 90%, 91%, 92%, 93%, 94%, 95%, 96%, 97%, 98% or at least about 99% homology to the corresponding amino acid sequence or polynucleotide sequence. As used herein the terms sequence “homology” and sequence “identity” are used interchangeably.
One of ordinary skill in the art is well aware of methods to determine homology between two or more sequences. Briefly, calculations of “homology” between two sequences can be performed as follows. The sequences are aligned for optimal comparison purposes (e.g., gaps can be introduced in one or both of a first and a second amino acid or nucleic acid sequence for optimal alignment and non-homologous sequences can be disregarded for comparison purposes). In a preferred embodiment, the length of a first sequence that is aligned for comparison purposes is at least about 30%, preferably at least about 40%, more preferably at least about 50%, even more preferably at least about 60%, and even more preferably at least about 70%, at least about 80%, at least about 90%, or about 100% of the length of a second sequence. The amino acid residues or nucleotides at corresponding amino acid positions or nucleotide positions of the first and second sequences are then compared. When a position in the first sequence is occupied by the same amino acid residue or nucleotide as the corresponding position in the second sequence, then the molecules are identical at that position. The percent homology between the two sequences is a function of the number of identical positions shared by the sequences, taking into account the number of gaps and the length of each gap, that need to be introduced for optimal alignment of the two sequences.
The comparison of sequences and determination of percent homology between two sequences can be accomplished using a mathematical algorithm, such as BLAST (Altschul et al., J. Mol. Biol., 215(3): 403-410 (1990)). The percent homology between two amino acid sequences also can be determined using the Needleman and Wunsch algorithm that has been incorporated into the GAP program in the GCG software package, using either a Blossum 62 matrix or a PAM250 matrix, and a gap weight of 16, 14, 12, 10, 8, 6, or 4 and a length weight of 1, 2, 3, 4, 5, or 6 (Needleman and Wunsch, J. Mol. Biol., 48: 444-453 (1970)). The percent homology between two nucleotide sequences also can be determined using the GAP program in the GCG software package, using a NWSgapdna.CMP matrix and a gap weight of 40, 50, 60, 70, or 80 and a length weight of 1, 2, 3, 4, 5, or 6. One of ordinary skill in the art can perform initial homology calculations and adjust the algorithm parameters accordingly. A preferred set of parameters (and the one that should be used if a practitioner is uncertain about which parameters should be applied to determine if a molecule is within a homology limitation of the claims) are a Blossum 62 scoring matrix with a gap penalty of 12, a gap extend penalty of 4, and a frameshift gap penalty of 5. Additional methods of sequence alignment are known in the biotechnology arts (see, e.g., Rosenberg, BMC Bioinformatics, 6: 278 (2005); Altschul, et al., FEBS J., 272(20): 5101-5109 (2005)).
As used herein, the term “hybridizes under low stringency, medium stringency, high stringency, or very high stringency conditions” describes conditions for hybridization and washing. Guidance for performing hybridization reactions can be found in Current Protocols in Molecular Biology, John Wiley & Sons, N.Y. (1989), 6.3.1-6.3.6. Aqueous and non-aqueous methods are described in that reference and either method can be used. Specific hybridization conditions referred to herein are as follows: 1) low stringency hybridization conditions—6× sodium chloride/sodium citrate (SSC) at about 45° C., followed by two washes in 0.2×SSC, 0.1% SDS at least at 50° C. (the temperature of the washes can be increased to 55° C. for low stringency conditions); 2) medium stringency hybridization conditions—6×SSC at about 45° C., followed by one or more washes in 0.2×SSC, 0.1% SDS at 60° C.; 3) high stringency hybridization conditions—6×SSC at about 45° C., followed by one or more washes in 0.2.×SSC, 0.1% SDS at 65° C.; and 4) very high stringency hybridization conditions—0.5M sodium phosphate, 7% SDS at 65° C., followed by one or more washes at 0.2×SSC, 1% SDS at 65° C. Very high stringency conditions (4) are the preferred conditions unless otherwise specified.
An “endogenous” polypeptide refers to a polypeptide encoded by the genome of the parental microbial cell (also termed “host cell”) from which the recombinant cell is engineered (or “derived”).
An “exogenous” polypeptide refers to a polypeptide which is not encoded by the genome of the parental microbial cell. A variant (i.e., mutant) polypeptide is an example of an exogenous polypeptide.
The term “heterologous” as used herein typically refers to a nucleotide sequence or a protein not naturally present in an organism. For example, a polynucleotide sequence endogenous to a plant can be introduced into a host cell by recombinant methods, and the plant polynucleotide is then a heterologous polynucleotide in a recombinant host cell.
As used herein, the term “fragment” of a polypeptide refers to a shorter portion of a full-length polypeptide or protein ranging in size from four amino acid residues to the entire amino acid sequence minus one amino acid residue. In certain embodiments of the invention, a fragment refers to the entire amino acid sequence of a domain of a polypeptide or protein (e.g., a substrate binding domain or a catalytic domain).
As used herein, the term “mutagenesis” refers to a process by which the genetic information of an organism is changed in a stable manner. Mutagenesis of a protein coding nucleic acid sequence produces a mutant protein. Mutagenesis also refers to changes in non-coding nucleic acid sequences that result in modified protein activity.
As used herein, the term “gene” refers to nucleic acid sequences encoding either an RNA product or a protein product, as well as operably-linked nucleic acid sequences affecting the expression of the RNA or protein (e.g., such sequences include but are not limited to promoter or enhancer sequences) or operably-linked nucleic acid sequences encoding sequences that affect the expression of the RNA or protein (e.g., such sequences include but are not limited to ribosome binding sites or translational control sequences).
Expression control sequences are known in the art and include, for example, promoters, enhancers, polyadenylation signals, transcription terminators, internal ribosome entry sites (IRES), and the like, that provide for the expression of the polynucleotide sequence in a host cell. Expression control sequences interact specifically with cellular proteins involved in transcription (Maniatis et al., Science, 236: 1237-1245 (1987)). Exemplary expression control sequences are described in, for example, Goeddel, Gene Expression Technology: Methods in Enzymology, Vol. 185, Academic Press, San Diego, Calif. (1990).
In the methods of the invention, an expression control sequence is operably linked to a polynucleotide sequence. By “operably linked” is meant that a polynucleotide sequence and an expression control sequence(s) are connected in such a way as to permit gene expression when the appropriate molecules (e.g., transcriptional activator proteins) are bound to the expression control sequence(s). Operably linked promoters are located upstream of the selected polynucleotide sequence in terms of the direction of transcription and translation. Operably linked enhancers can be located upstream, within, or downstream of the selected polynucleotide.
As used herein, the term “vector” refers to a nucleic acid molecule capable of transporting another nucleic acid, i.e., a polynucleotide sequence, to which it has been linked One type of useful vector is an episome (i.e., a nucleic acid capable of extra-chromosomal replication). Useful vectors are those capable of autonomous replication and/or expression of nucleic acids to which they are linked Vectors capable of directing the expression of genes to which they are operatively linked are referred to herein as “expression vectors.” In general, expression vectors of utility in recombinant DNA techniques are often in the form of “plasmids,” which refer generally to circular double stranded DNA loops that, in their vector form, are not bound to the chromosome. The terms “plasmid” and “vector” are used interchangeably herein, in as much as a plasmid is the most commonly used form of vector. However, also included are such other forms of expression vectors that serve equivalent functions and that become known in the art subsequently hereto.
In some embodiments, a recombinant vector further comprises a promoter operably linked to the polynucleotide sequence. In some embodiments, the promoter is a developmentally-regulated, an organelle-specific, a tissue-specific, an inducible, a constitutive, or a cell-specific promoter. The recombinant vector typically comprises at least one sequence selected from the group consisting of (a) an expression control sequence operatively coupled to the polynucleotide sequence; (b) a selection marker operatively coupled to the polynucleotide sequence; (c) a marker sequence operatively coupled to the polynucleotide sequence; (d) a purification moiety operatively coupled to the polynucleotide sequence; (e) a secretion sequence operatively coupled to the polynucleotide sequence; and (f) a targeting sequence operatively coupled to the polynucleotide sequence. In certain embodiments, the nucleotide sequence is stably incorporated into the genomic DNA of the host cell, and the expression of the nucleotide sequence is under the control of a regulated promoter region.
The expression vectors described herein include a polynucleotide sequence described herein in a form suitable for expression of the polynucleotide sequence in a host cell. It will be appreciated by those skilled in the art that the design of the expression vector can depend on such factors as the choice of the host cell to be transformed, the level of expression of polypeptide desired, etc. The expression vectors described herein can be introduced into host cells to produce polypeptides, including fusion polypeptides, encoded by the polynucleotide sequences as described herein. Expression of genes encoding polypeptides in prokaryotes, for example, E. coli, is most often carried out with vectors containing constitutive or inducible promoters directing the expression of either fusion or non-fusion polypeptides. Fusion vectors add a number of amino acids to a polypeptide encoded therein, usually to the amino- or carboxy-terminus of the recombinant polypeptide. Such fusion vectors typically serve one or more of the following three purposes: (1) to increase expression of the recombinant polypeptide; (2) to increase the solubility of the recombinant polypeptide; and (3) to aid in the purification of the recombinant polypeptide by acting as a ligand in affinity purification. Often, in fusion expression vectors, a proteolytic cleavage site is introduced at the junction of the fusion moiety and the recombinant polypeptide. This enables separation of the recombinant polypeptide from the fusion moiety after purification of the fusion polypeptide. In certain embodiments, a polynucleotide sequence of the invention is operably linked to a promoter derived from bacteriophage T5.
In certain embodiments, the host cell is a yeast cell, and the expression vector is a yeast expression vector. Examples of vectors for expression in yeast S. cerevisiae include pYepSec1 (Baldari et al., EMBO J., 6: 229-234 (1987)), pMFa (Kurjan et al., Cell, 30: 933-943 (1982)), pJRY88 (Schultz et al., Gene, 54: 113-123 (1987)), pYES2 (Invitrogen Corp., San Diego, Calif.), and picZ (Invitrogen Corp., San Diego, Calif.).
In other embodiments, the host cell is an insect cell, and the expression vector is a baculovirus expression vector. Baculovirus vectors available for expression of proteins in cultured insect cells (e.g., Sf9 cells) include, for example, the pAc series (Smith et al., Mol. Cell. Biol., 3: 2156-2165 (1983)) and the pVL series (Lucklow et al., Virology, 170: 31-39 (1989)).
In yet another embodiment, the polynucleotide sequences described herein can be expressed in mammalian cells using a mammalian expression vector. Other suitable expression systems for both prokaryotic and eukaryotic cells are well known in the art; see, e.g., Sambrook et al., “Molecular Cloning: A Laboratory Manual,” second edition, Cold Spring Harbor Laboratory, (1989).
As used herein “acyl-CoA” refers to an acyl thioester formed between the carbonyl carbon of alkyl chain and the sulfhydryl group of the 4′-phosphopantethionyl moiety of coenzyme A (CoA), which has the formula R—C(O)S—CoA, where R is any alkyl group having at least 4 carbon atoms.
As used herein “acyl-ACP” refers to an acyl thioester formed between the carbonyl carbon of alkyl chain and the sulfhydryl group of the phosphopantetheinyl moiety of an acyl carrier protein (ACP). The phosphopantetheinyl moiety is post-translationally attached to a conserved serine residue on the ACP by the action of holo-acyl carrier protein synthase (ACPS), a phosphopantetheinyl transferase. In some embodiments an acyl-ACP is an intermediate in the synthesis of fully saturated acyl-ACPs. In other embodiments an acyl-ACP is an intermediate in the synthesis of unsaturated acyl-ACPs. In some embodiments, the carbon chain will have about 5, 6, 7, 8, 9, 10, 11, 12, 13, 14, 15, 16, 17, 18, 19, 20, 21, 22, 23, 24, 25, or 26 carbons. Each of these acyl-ACPs are substrates for enzymes that convert them to fatty acid derivatives such as those described in
As used herein, the term “fatty acid derivative” means a “fatty acid” or a “fatty acid derivative”, which may be referred to as a “fatty acid or derivative thereof”. The term “fatty acid” means a carboxylic acid having the formula RCOOH. R represents an aliphatic group, preferably an alkyl group. R can comprise between about 4 and about 22 carbon atoms. Fatty acids can be saturated, monounsaturated, or polyunsaturated. A “fatty acid derivative” is a product made in part from the fatty acid biosynthetic pathway of the production host organism. “Fatty acid derivatives” includes products made in part from acyl-ACP or acyl-ACP derivatives. Exemplary fatty acid derivatives include, for example, acyl-CoA, fatty acids, fatty aldehydes, short and long chain alcohols, fatty alcohols, hydrocarbons, esters (e.g., waxes, fatty acid esters, or fatty esters), terminal olefins, internal olefins, and ketones.
A “fatty acid derivative composition” as referred to herein is produced by a recombinant host cell and typically comprises a mixture of fatty acid derivative. In some cases, the mixture includes more than one type of product (e.g., fatty acids and fatty alcohols, fatty acids and fatty acid esters or alkanes and olefins). In other cases, the fatty acid derivative compositions may comprise, for example, a mixture of fatty alcohols (or another fatty acid derivative) with various chain lengths and saturation or branching characteristics. In still other cases, the fatty acid derivative composition comprises a mixture of both more than one type of product and products with various chain lengths and saturation or branching characteristics.
As used herein, the term “fatty acid biosynthetic pathway” means a biosynthetic pathway that produces fatty acids and derivatives thereof. The fatty acid biosynthetic pathway may include additional enzymes to produce fatty acids derivatives having desired characteristics.
As used herein, “fatty aldehyde” means an aldehyde having the formula RCHO characterized by a carbonyl group (C═O). In some embodiments, the fatty aldehyde is any aldehyde made from a fatty alcohol. In certain embodiments, the R group is at least 5, at least 6, at least 7, at least 8, at least 9, at least 10, at least 11, at least 12, at least 13, at least 14, at least 15, at least 16, at least 17, at least 18, or at least 19, carbons in length. Alternatively, or in addition, the R group is 20 or less, 19 or less, 18 or less, 17 or less, 16 or less, 15 or less, 14 or less, 13 or less, 12 or less, 11 or less, 10 or less, 9 or less, 8 or less, 7 or less, or 6 or less carbons in length. Thus, the R group can have an R group bounded by any two of the above endpoints. For example, the R group can be 6-16 carbons in length, 10-14 carbons in length, or 12-18 carbons in length. In some embodiments, the fatty aldehyde is a C6, C7, C8, C9, C10, C11, C12, C13, C14, C15, C16, C17, C18, C19, C20, C21, C22, C23, C24, C25, or a C26 fatty aldehyde. In certain embodiments, the fatty aldehyde is a C6, C7, C8, C9, C10, C11, C12, C13, C14, C15, C16, C17, or C18 fatty aldehyde.
As used herein, “fatty alcohol” means an alcohol having the formula ROH. In some embodiments, the R group is at least 5, at least 6, at least 7, at least 8, at least 9, at least 10, at least 11, at least 12, at least 13, at least 14, at least 15, at least 16, at least 17, at least 18, or at least 19, carbons in length. Alternatively, or in addition, the R group is 20 or less, 19 or less, 18 or less, 17 or less, 16 or less, 15 or less, 14 or less, 13 or less, 12 or less, 11 or less, 10 or less, 9 or less, 8 or less, 7 or less, or 6 or less carbons in length. Thus, the R group can have an R group bounded by any two of the above endpoints. For example, the R group can be 6-16 carbons in length, 10-14 carbons in length, or 12-18 carbons in length. In some embodiments, the fatty alcohol is a C6, C7, C8, C9, C10, C11, C12, C13, C14, C15, C16, C17, C18, C19, C20, C21, C22, C23, C24, C25, or a C26 fatty alcohol. In certain embodiments, the fatty alcohol is a C6, C7, C8, C9, C10, C11, C12, C13, C14, C15, C16, C17, or C18 fatty alcohol.
The R group of a fatty acid derivative, for example a fatty alcohol, can be a straight chain or a branched chain. Branched chains may have more than one point of branching and may include cyclic branches. In some embodiments, the branched fatty acid, branched fatty aldehyde, or branched fatty alcohol is a C6, C7, C8, C9, C10, C11, C12, C13, C14, C15, C16, C17, C18, C19, C20, C21, C22, C23, C24, C25, or a C2-6 branched fatty acid, branched fatty aldehyde, or branched fatty alcohol. In particular embodiments, the branched fatty acid, branched fatty aldehyde, or branched fatty alcohol is a C6, C7, C8, C9, C10, C11, C12, C13, C14, C15, C16, C17, or C18 branched fatty acid, branched fatty aldehyde, or branched fatty alcohol. In certain embodiments, the hydroxyl group of the branched fatty acid, branched fatty aldehyde, or branched fatty alcohol is in the primary (C1) position.
In certain embodiments, the branched fatty acid derivative is an iso-fatty acid derivative, for example an iso-fatty aldehyde, an iso-fatty alcohol, or an antesio-fatty acid derivative, an anteiso-fatty aldehyde, or an anteiso-fatty alcohol. In exemplary embodiments, the branched fatty acid derivative is selected from iso-C7:0, iso-C8:0, iso-C9:0, iso-C10:0, iso-C11:0, iso-C12:0, iso-C13:0, iso-C14:0, iso-C15:0, iso-C16:0, iso-C17:0, iso-C18:0, iso-C19:0, anteiso-C7:0, anteiso-C8:0, anteiso-C9:0, anteiso-C10:0, anteiso-C11:0, anteiso-C12:0, anteiso-C13:0, anteiso-C14:0, anteiso-C15:0, anteiso-C16:0, anteiso-C17:0, anteiso-C18:0, and an anteiso-C19:0 branched fatty alcohol.
The R group of a branched or unbranched fatty acid derivative can be saturated or unsaturated. If unsaturated, the R group can have one or more than one point of unsaturation. In some embodiments, the unsaturated fatty acid derivative is a monounsaturated fatty acid derivative. In certain embodiments, the unsaturated fatty acid derivative is a C6:1, C7:1, C8:1, C9:1, C10:1, C11:1, C12:1, C13:1, C14:1, C15:1, C16:1, C17:1, C18:1, C19:1, C20:1, C21:1, C22:1, C23:1, C24:1, C25:1, or a C26:1 unsaturated fatty acid derivative. In certain embodiments, the unsaturated fatty acid derivative, is a C10:1, C12:1, C14:1, C16:1, or C18:1 unsaturated fatty acid derivative. In other embodiments, the unsaturated fatty acid derivative is unsaturated at the omega-7 position. In certain embodiments, the unsaturated fatty acid derivative comprises a cis double bond.
As used herein, a recombinant or engineered “host cell” is a host cell, e.g., a microorganism used to produce one or more of fatty acid derivatives include, for example, acyl-CoA, fatty acids, fatty aldehydes, short and long chain alcohols, hydrocarbons, fatty alcohols, esters (e.g., waxes, fatty acid esters, or fatty esters), terminal olefins, internal olefins, and ketones.
In some embodiments, the recombinant host cell comprises one or more polynucleotides, each polynucleotide encoding a polypeptide having fatty acid biosynthetic enzyme activity, wherein the recombinant host cell produces a fatty acid derivative composition when cultured in the presence of a carbon source under conditions effective to express the polynucleotides.
As used herein, the term “clone” typically refers to a cell or group of cells descended from and essentially genetically identical to a single common ancestor, for example, the bacteria of a cloned bacterial colony arose from a single bacterial cell.
As used herein, the term “culture” typical refers to a liquid media comprising viable cells. In one embodiment, a culture comprises cells reproducing in a predetermined culture media under controlled conditions, for example, a culture of recombinant host cells grown in liquid media comprising a selected carbon source and nitrogen.
“Culturing” or “cultivation” refers to growing a population of recombinant host cells under suitable conditions in a liquid or solid medium. In particular embodiments, culturing refers to the fermentative bioconversion of a substrate to an end-product. Culturing media are well known and individual components of such culture media are available from commercial sources, e.g., under the Difco™ and BBL™ trademarks. In one non-limiting example, the aqueous nutrient medium is a “rich medium” comprising complex sources of nitrogen, salts, and carbon, such as YP medium, comprising 10 g/L of peptone and 10 g/L yeast extract of such a medium.
The host cell can be additionally engineered to assimilate carbon efficiently and use cellulosic materials as carbon sources according to methods described in U.S. Pat. Nos. 5,000,000; 5,028,539; 5,424,202; 5,482,846; 5,602,030; WO 2010127318. In addition, in some embodiments the host cell is engineered to express an invertase so that sucrose can be used as a carbon source.
As used herein, the term “under conditions effective to express said heterologous nucleotide sequence(s)” means any conditions that allow a host cell to produce a desired fatty acid derivative. Suitable conditions include, for example, fermentation conditions.
As used herein, “modified” or an “altered level of” activity of a protein, for example an enzyme, in a recombinant host cell refers to a difference in one or more characteristics in the activity determined relative to the parent or native host cell. Typically differences in activity are determined between a recombinant host cell, having modified activity, and the corresponding wild-type host cell (e.g., comparison of a culture of a recombinant host cell relative to the corresponding wild-type host cell). Modified activities can be the result of, for example, modified amounts of protein expressed by a recombinant host cell (e.g., as the result of increased or decreased number of copies of DNA sequences encoding the protein, increased or decreased number of mRNA transcripts encoding the protein, and/or increased or decreased amounts of protein translation of the protein from mRNA); changes in the structure of the protein (e.g., changes to the primary structure, such as, changes to the protein's coding sequence that result in changes in substrate specificity, changes in observed kinetic parameters); and changes in protein stability (e.g., increased or decreased degradation of the protein). In some embodiments, the polypeptide is a mutant or a variant of any of the polypeptides described herein. In certain instances, the coding sequence for the polypeptides described herein are codon optimized for expression in a particular host cell. For example, for expression in E. coli, one or more codons can be optimized as described in, e.g., Grosjean et al., Gene 18:199-209 (1982).
The term “regulatory sequences” as used herein typically refers to a sequence of bases in DNA, operably-linked to DNA sequences encoding a protein that ultimately controls the expression of the protein. Examples of regulatory sequences include, but are not limited to, RNA promoter sequences, transcription factor binding sequences, transcription termination sequences, modulators of transcription (such as enhancer elements), nucleotide sequences that affect RNA stability, and translational regulatory sequences (such as, ribosome binding sites (e.g., Shine-Dalgarno sequences in prokaryotes or Kozak sequences in eukaryotes), initiation codons, termination codons).
As used herein, the phrase “the expression of said nucleotide sequence is modified relative to the wild type nucleotide sequence,” means an increase or decrease in the level of expression and/or activity of an endogenous nucleotide sequence or the expression and/or activity of a heterologous or non-native polypeptide-encoding nucleotide sequence.
As used herein, the term “express” with respect to a polynucleotide is to cause it to function. A polynucleotide which encodes a polypeptide (or protein) will, when expressed, be transcribed and translated to produce that polypeptide (or protein). As used herein, the term “overexpress” means to express or cause to be expressed a polynucleotide or polypeptide in a cell at a greater concentration than is normally expressed in a corresponding wild-type cell under the same conditions.
The terms “altered level of expression” and “modified level of expression” are used interchangeably and mean that a polynucleotide, polypeptide, or hydrocarbon is present in a different concentration in an engineered host cell as compared to its concentration in a corresponding wild-type cell under the same conditions.
As used herein, the term “titer” refers to the quantity of fatty acid derivative produced per unit volume of host cell culture. In any aspect of the compositions and methods described herein, a fatty acid derivative is produced at a titer of about 25 mg/L, about 50 mg/L, about 75 mg/L, about 100 mg/L, about 125 mg/L, about 150 mg/L, about 175 mg/L, about 200 mg/L, about 225 mg/L, about 250 mg/L, about 275 mg/L, about 300 mg/L, about 325 mg/L, about 350 mg/L, about 375 mg/L, about 400 mg/L, about 425 mg/L, about 450 mg/L, about 475 mg/L, about 500 mg/L, about 525 mg/L, about 550 mg/L, about 575 mg/L, about 600 mg/L, about 625 mg/L, about 650 mg/L, about 675 mg/L, about 700 mg/L, about 725 mg/L, about 750 mg/L, about 775 mg/L, about 800 mg/L, about 825 mg/L, about 850 mg/L, about 875 mg/L, about 900 mg/L, about 925 mg/L, about 950 mg/L, about 975 mg/L, about 1000 mg/L, about 1050 mg/L, about 1075 mg/L, about 1100 mg/L, about 1125 mg/L, about 1150 mg/L, about 1175 mg/L, about 1200 mg/L, about 1225 mg/L, about 1250 mg/L, about 1275 mg/L, about 1300 mg/L, about 1325 mg/L, about 1350 mg/L, about 1375 mg/L, about 1400 mg/L, about 1425 mg/L, about 1450 mg/L, about 1475 mg/L, about 1500 mg/L, about 1525 mg/L, about 1550 mg/L, about 1575 mg/L, about 1600 mg/L, about 1625 mg/L, about 1650 mg/L, about 1675 mg/L, about 1700 mg/L, about 1725 mg/L, about 1750 mg/L, about 1775 mg/L, about 1800 mg/L, about 1825 mg/L, about 1850 mg/L, about 1875 mg/L, about 1900 mg/L, about 1925 mg/L, about 1950 mg/L, about 1975 mg/L, about 2000 mg/L (2 g/L), 3 g/L, 5 g/L, 10 g/L, 20 g/L, 30 g/L, 40 g/L, 50 g/L, 60 g/L, 70 g/L, 80 g/L, 90 g/L, 100 g/L or a range bounded by any two of the foregoing values. In other embodiments, a fatty acid derivative is produced at a titer of more than 100 g/L, more than 200 g/L, more than 300 g/L, or higher, such as 500 g/L, 700 g/L, 1000 g/L, 1200 g/L, 1500 g/L, or 2000 g/L. The preferred titer of fatty acid derivative produced by a recombinant host cell according to the methods of the invention is from 5 g/L to 200 g/L, 10 g/L to 150 g/L, 20 g/L to 120 g/L and 30 g/L to 100 g/L. The titer may refer to a particular fatty acid derivative or a combination of fatty acid derivatives produced by a given recombinant host cell culture.
As used herein, the “yield of fatty acid derivative produced by a host cell” refers to the efficiency by which an input carbon source is converted to product (i.e., fatty alcohol or fatty aldehyde) in a host cell. Host cells engineered to produce fatty acid derivatives according to the methods of the invention have a yield of at least 3%, at least 4%, at least 5%, at least 6%, at least 7%, at least 8%, at least 9%, at least 10%, at least 11%, at least 12%, at least 13%, at least 14%, at least 15%, at least 16%, at least 17%, at least 18%, at least 19%, at least 20%, at least 21%, at least 22%, at least 23%, at least 24%, at least 25%, at least 26%, at least 27%, at least 28%, at least 29%, or at least 30% or a range bounded by any two of the foregoing values. In other embodiments, a fatty acid derivative or derivatives is produced at a yield of more than 30%, 40%, 50%, 60%, 70%, 80%, 90% or more. Alternatively, or in addition, the yield is about 30% or less, about 27% or less, about 25% or less, or about 22% or less. Thus, the yield can be bounded by any two of the above endpoints. For example, the yield of a fatty acid derivative or derivatives produced by the recombinant host cell according to the methods of the invention can be 5% to 15%, 10% to 25%, 10% to 22%, 15% to 27%, 18% to 22%, 20% to 28%, or 20% to 30%. The yield may refer to a particular fatty acid derivative or a combination of fatty acid derivatives produced by a given recombinant host cell culture.
As used herein, the term “productivity” refers to the quantity of a fatty acid derivative or derivatives produced per unit volume of host cell culture per unit time. In any aspect of the compositions and methods described herein, the productivity of a fatty acid derivative or derivatives produced by a recombinant host cell is at least 100 mg/L/hour, at least 200 mg/L/hour, at least 300 mg/L/hour, at least 400 mg/L/hour, at least 500 mg/L/hour, at least 600 mg/L/hour, at least 700 mg/L/hour, at least 800 mg/L/hour, at least 900 mg/L/hour, at least 1000 mg/L/hour, at least 1100 mg/L/hour, at least 1200 mg/L/hour, at least 1300 mg/L/hour, at least 1400 mg/L/hour, at least 1500 mg/L/hour, at least 1600 mg/L/hour, at least 1700 mg/L/hour, at least 1800 mg/L/hour, at least 1900 mg/L/hour, at least 2000 mg/L/hour, at least 2100 mg/L/hour, at least 2200 mg/L/hour, at least 2300 mg/L/hour, at least 2400 mg/L/hour, or at least 2500 mg/L/hour. For example, the productivity of a fatty acid derivative or derivatives produced by a recombinant host cell according to the methods of the may be from 500 mg/L/hour to 2500 mg/L/hour, or from 700 mg/L/hour to 2000 mg/L/hour. The productivity may refer to a particular fatty acid derivative or a combination of fatty acid derivatives produced by a given recombinant host cell culture.
As used herein, the term “total fatty species” and “total fatty acid product” may be used interchangeably herein with reference to the amount of fatty alcohols, fatty aldehydes and fatty acids, as evaluated by GC-FID as described in International Patent Application Publication WO 2008/119082. The same terms may be used to mean fatty esters and free fatty acids when referring to a fatty ester analysis.
As used herein, the term “glucose utilization rate” means the amount of glucose used by the culture per unit time, reported as grams/liter/hour (g/L/hr).
As used herein, the term “carbon source” refers to a substrate or compound suitable to be used as a source of carbon for prokaryotic or simple eukaryotic cell growth. Carbon sources can be in various forms, including, but not limited to polymers, carbohydrates, acids, alcohols, aldehydes, ketones, amino acids, peptides, and gases (e.g., CO and CO2). Exemplary carbon sources include, but are not limited to, monosaccharides, such as glucose, fructose, mannose, galactose, xylose, and arabinose; oligosaccharides, such as fructo-oligosaccharide and galacto-oligosaccharide; polysaccharides such as starch, cellulose, pectin, and xylan; disaccharides, such as sucrose, maltose, cellobiose, and turanose; cellulosic material and variants such as hemicelluloses, methyl cellulose and sodium carboxymethyl cellulose; saturated or unsaturated fatty acids, succinate, lactate, and acetate; alcohols, such as ethanol, methanol, and glycerol, or mixtures thereof. The carbon source can also be a product of photosynthesis, such as glucose. In certain preferred embodiments, the carbon source is biomass. In other preferred embodiments, the carbon source is glucose. In other preferred embodiments the carbon source is sucrose.
As used herein, the term “biomass” refers to any biological material from which a carbon source is derived. In some embodiments, a biomass is processed into a carbon source, which is suitable for bioconversion. In other embodiments, the biomass does not require further processing into a carbon source. The carbon source can be converted into a biofuel. An exemplary source of biomass is plant matter or vegetation, such as corn, sugar cane, or switchgrass. Another exemplary source of biomass is metabolic waste products, such as animal matter (e.g., cow manure). Further exemplary sources of biomass include algae and other marine plants. Biomass also includes waste products from industry, agriculture, forestry, and households, including, but not limited to, fermentation waste, ensilage, straw, lumber, sewage, garbage, cellulosic urban waste, and food leftovers. The term “biomass” also can refer to sources of carbon, such as carbohydrates (e.g., monosaccharides, disaccharides, or polysaccharides).
As used herein, the term “isolated,” with respect to products (such as fatty acids and derivatives thereof) refers to products that are separated from cellular components, cell culture media, or chemical or synthetic precursors. The fatty acids and derivatives thereof produced by the methods described herein can be relatively immiscible in the fermentation broth, as well as in the cytoplasm. Therefore, the fatty acids and derivatives thereof can collect in an organic phase either intracellularly or extracellularly.
As used herein, the terms “purify,” “purified,” or “purification” mean the removal or isolation of a molecule from its environment by, for example, isolation or separation. “Substantially purified” molecules are at least about 60% free (e.g., at least about 70% free, at least about 75% free, at least about 85% free, at least about 90% free, at least about 95% free, at least about 97% free, at least about 99% free) from other components with which they are associated. As used herein, these terms also refer to the removal of contaminants from a sample. For example, the removal of contaminants can result in an increase in the percentage of fatty acid derivatives in a sample. For example, when a fatty acid derivative is produced in a recombinant host cell, the fatty acid derivative can be purified by the removal of host cell proteins. After purification, the percentage of fatty acid derivative in the sample is increased. The terms “purify,” “purified,” and “purification” are relative terms which do not require absolute purity. Thus, for example, when a fatty acid derivative is produced in recombinant host cells, a purified fatty acid derivative is a fatty acid derivative that is substantially separated from other cellular components (e.g., nucleic acids, polypeptides, lipids, carbohydrates, or other hydrocarbons).
General Overview of the InventionIn the compositions and methods of the invention, the production of a desired fatty acid derivative composition (e.g., acyl-CoA, fatty acids, fatty aldehydes, short and long chain alcohols, hydrocarbons, fatty alcohols, esters (e.g., waxes, fatty acid esters, or fatty esters), terminal olefins, internal olefins, and ketones is enhanced by modifying the expression of one or more genes involved in a biosynthetic pathway for fatty acid, fatty ester, alkane, alkene, olefin, or fatty alcohol, production, degradation and/or secretion.
The invention provides recombinant host cells which have been engineered to provide enhanced fatty acid biosynthesis relative to non-engineered or native host cells (for example by strain improvements, as further described herein below).
The disclosure identifies polynucleotides useful in the recombinant host cells, methods, and compositions of the invention; however it will be recognized that absolute sequence identity to such polynucleotides is not necessary. For example, changes in a particular polynucleotide sequence can be made and the encoded polypeptide screened for activity. Such changes typically comprise conservative mutations and silent mutations (such as, for example, codon optimization). Modified or mutated (i.e., mutant) polynucleotides and encoded variant polypeptides can be screened for a desired function, such as, an improved function compared to the parent polypeptide, including but not limited to increased catalytic activity, increased stability, or decreased inhibition (e.g., decreased feedback inhibition), using methods known in the art. The disclosure identifies enzymatic activities involved in various steps (i.e., reactions) of the fatty acid biosynthetic pathways described herein according to Enzyme Classification (EC) number, and provides exemplary polypeptides (i.e., enzymes) categorized by such EC numbers, and exemplary polynucleotides encoding such polypeptides. Such exemplary polypeptides and polynucleotides, which are identified herein by Accession Numbers and/or Sequence Identifier Numbers (SEQ ID NOs), are useful for engineering fatty acid pathways in parental host cells to obtain the recombinant host cells described herein. It is to be understood, however, that polypeptides and polynucleotides described herein are exemplary and non-limiting. The sequences of homologues of exemplary polypeptides described herein are available to those of skill in the art using databases such as, for example, the Entrez databases provided by the National Center for Biotechnology Information (NCBI), the ExPasy databases provided by the Swiss Institute of Bioinformatics, the BRENDA database provided by the Technical University of Braunschweig, and the KEGG database provided by the Bioinformatics Center of Kyoto University and University of Tokyo, all which are available on the World Wide Web.
A variety of host cells can be modified to contain a fatty acid biosynthetic pathway such as those described herein, resulting in recombinant host cells suitable for the production of fatty acid derivatives. It is understood that a variety of cells can provide sources of genetic material, including polynucleotide sequences that encode polypeptides suitable for use in a recombinant host cell provided herein.
Strain ImprovementsIn order generate a high titer, yield, and productivity of fatty acid derivatives, a number of modifications were made to the production host cells.
FadR is a key regulatory factor involved in fatty acid degradation and fatty acid biosynthetic pathways (Cronan et al., Mol. Microbiol., 29(4): 937-943 (1998)). The E. coli ACS enzyme FadD and the fatty acid transport protein FadL are essential components of a fatty acid uptake system. FadL mediates transport of fatty acids into the bacterial cell, and FadD mediates formation of acyl-CoA esters. When no other carbon source is available, exogenous fatty acids are taken up by bacteria and converted to acyl-CoA esters, which can bind to the transcription factor FadR and derepress the expression of the fad genes that encode proteins responsible for fatty acid transport (FadL), activation (FadD), and β-oxidation (FadA, FadB, FadE, and FadH). When alternative sources of carbon are available, bacteria synthesize fatty acids as acyl-ACPs, which are used for phospholipid synthesis, but are not substrates for β-oxidation. Thus, acyl-CoA and acyl-ACP are both independent sources of fatty acids can result in different end-products (Caviglia et al., J. Biol. Chem., 279(12): 1163-1169 (2004)). U.S. Provisional Application No. 61/470,989 describes improved methods of producing fatty acid derivatives in a host cell which is genetically engineered to have an altered level of expression of a FadR polypeptide as compared to the level of expression of the FadR polypeptide in a corresponding wild-type host cell.
There are conflicting reports in the literature as to factors that can limit fatty acid biosynthesis in host cells, such as E. coli. One suggestion is that a limitation of the main precursors for fatty acid biosynthesis, for example, acetyl-CoA and malonyl-CoA can result in decreased synthesis of fatty acid derivatives. One approach to increasing the flux through fatty acid biosynthesis is to manipulate various enzymes in the pathway (
The supply of acyl-ACPs from acetyl-CoA via the acetyl-CoA carboxylase (acc) complex and fatty acid biosynthetic (fab) pathway is another step that may limit the rate of fatty acid derivative production (
In yet another approach, mutations in the rph and ilvG genes in the E. coli host cell were shown to result in higher free fatty acid (FFA) production, which translated into higher production of fatty alcohol. See Example 4.
In still another approach, transposon mutagenesis and high-throughput screening was carried out to find beneficial mutations that increase the titer or yield. Example 5 describes studies where it was observed that a transposon insertion in the yijP gene can improve the fatty alcohol yield in shake flask and fed-batch fermentations.
Generation of Fatty Acid Derivative by Recombinant Host CellsThis disclosure provides numerous examples of polypeptides (i.e., enzymes) having activities suitable for use in the fatty acid biosynthetic pathways described herein. Such polypeptides are collectively referred to herein as “fatty acid biosynthetic polypeptides” or “fatty acid biosynthetic enzymes”. Non-limiting examples of fatty acid pathway polypeptides suitable for use in recombinant host cells of the invention are provided herein.
In some embodiments, the invention includes a recombinant host cell comprising a polynucleotide sequence (also referred to herein as a “fatty acid biosynthetic polynucleotide” sequence) which encodes a fatty acid biosynthetic polypeptide.
The polynucleotide sequence, which comprises an open reading frame encoding a fatty acid biosynthetic polypeptide and operably-linked regulatory sequences, can be integrated into a chromosome of the recombinant host cells, incorporated in one or more plasmid expression systems resident in the recombinant host cell, or both. In the Examples, both plasmid expression systems and integration into the host genome are used to illustrate different embodiments of the present invention.
In some embodiments, a fatty acid biosynthetic polynucleotide sequence encodes a polypeptide which is endogenous to the parental host cell of the recombinant cell being engineered. Some such endogenous polypeptides are overexpressed in the recombinant host cell. An “endogenous polypeptide”, as used herein, refers to a polypeptide which is encoded by the genome of the parental (e.g., wild-type) cell that is engineered to produce the recombinant host cell.
In some embodiments, the fatty acid biosynthetic polynucleotide sequence encodes an exogenous or heterologous polypeptide. In other words, the polypeptide encoded by the polynucleotide is exogenous to the parental host cell. An “exogenous” (or “heterologous”) polypeptide, as used herein, refers to a polypeptide not encoded by the genome of the parental (e.g., wild-type) host cell that is being engineered to produce the recombinant host cell. Such a polypeptide can also be referred to as a “non-native” polypeptide. A variant (that is, a mutant) polypeptide is an example of a heterologous polypeptide.
In certain embodiments, the genetically modified host cell overexpresses a gene encoding a polypeptide (protein) that increases the rate at which the host cell produces the substrate of a fatty acid biosynthetic enzyme, i.e., a fatty acyl-thioester substrate. In certain embodiments, the enzyme encoded by the over expressed gene is directly involved in fatty acid biosynthesis.
Such recombinant host cells may be further engineered to comprise a polynucleotide sequence encoding one or more “fatty acid biosynthetic polypeptides”, (enzymes involved in fatty acid biosynthesis), for example, a polypeptide:
(1) having thioesterase activity, wherein the recombinant host cell synthesizes fatty acids;
(2) having thioesterase activity and carboxylic acid reductase (“CAR”) activity, wherein the recombinant host cell synthesizes fatty aldehydes and fatty alcohols;
(3) having thioesterase activity, carboxylic acid reductase activity and alcohol dehydrogenase activity wherein the recombinant host cell synthesizes fatty alcohols;
(4) having acyl-CoA reductase (“AAR”) activity wherein the recombinant host cell synthesizes fatty aldehydes and fatty alcohols;
(5) having acyl-CoA reductase (“AAR”) activity and alcohol dehydrogenase activity wherein the recombinant host cell synthesizes fatty alcohols;
(6) having fatty alcohol forming acyl-CoA reductase (“FAR”) activity, wherein the recombinant host cell synthesizes fatty alcohols;
(7) having thioesterase activity, carboxylic acid reductase activity and aldehyde decarbonylase activity, wherein the recombinant host cell synthesizes alkanes;
(8) having acyl-CoA reductase activity and aldehyde decarbonylase activity, wherein the recombinant host cell synthesizes alkanes
(9) having ester synthase activity wherein the recombinant host cell synthesizes fatty esters (“one enzyme system”;
(10) having thioesterase activity, acyl-CoA synthase activity and ester synthase activity wherein the recombinant host cell synthesizes fatty esters (“three enzyme system”;
(11) having OleA activity, wherein the recombinant host cell synthesizes aliphatic ketones;
(12) having OleABCD activity, wherein the recombinant host cell synthesizes internal olefins, or
(13) having thioesterase activity and decarboxylase activity, wherein the recombinant host cell synthesizes terminal olefins.
In some embodiments, at least one polypeptide encoded by a fatty acid biosynthetic polynucleotide is an exogenous (or heterologous) polypeptide (for example, a polypeptide originating from an organism other than the parental host cell, or, a variant of a polypeptide native to the parental microbial cell) or an endogenous polypeptide (that is, a polypeptide native to the parental host cell) wherein the endogenous polypeptide is overexpressed in the recombinant host cell.
Table 1 provides a listing of exemplary proteins which can be expressed in recombinant host cells to facilitate production of particular fatty acid derivatives.
The recombinant host cells may comprise one or more polynucleotide sequences that comprise an open reading frame encoding a thioesterase, e.g., having an Enzyme Commission number of EC 3.1.1.5 or EC 3.1.2.—(for example, EC 3.1.2.14), together with operably-linked regulatory sequences that facilitate expression of the protein in the recombinant host cells. In the recombinant host cells, the open reading frame coding sequences and/or the regulatory sequences are modified relative to the corresponding wild-type gene encoding the thioesterase. The activity of the thioesterase in the recombinant host cell is modified relative to the activity of the thioesterase expressed from the corresponding wild-type gene in a corresponding host cell. In some embodiments, a fatty acid derivative composition comprising fatty acids is produced by culturing a recombinant cell in the presence of a carbon source under conditions effective to express the thioesterase.
In related embodiments, the recombinant host cell comprises a polynucleotide encoding a polypeptide having thioesterase activity, and one or more additional polynucleotides encoding polypeptides having other fatty acid biosynthetic enzyme activities. In some such instances, the fatty acid produced by the action of the thioesterase is converted by one or more enzymes having a different fatty acid biosynthetic enzyme activity to another fatty acid derivative, such as, for example, a fatty ester, fatty aldehyde, fatty alcohol, or a hydrocarbon.
The chain length of a fatty acid, or a fatty acid derivative made therefrom, can be selected for by modifying the expression of particular thioesterases. The thioesterase will influence the chain length of fatty acid derivatives produced. The chain length of a fatty acid derivative substrate can be selected for by modifying the expression of selected thioesterases (EC 3.1.2.14 or LC 3, 1.1.5). Hence, host cells can be engineered to express, overexpress, have attenuated expression, or not express one or more selected thioesterases to increase the production of a preferred fatty acid derivative substrate. For example, C10 fatty acids can be produced by expressing a thioesterase that has a preference for producing C10 fatty acids and attenuating thioesterases that have a preference for producing fatty acids other than C10 fatty acids (e.g., a thioesterase which prefers to produce C14 fatty acids). This would result in a relatively homogeneous population of fatty acids that have a carbon chain length of 10. In other instances, C14 fatty acids can be produced by attenuating endogenous thioesterases that produce non-C14 fatty acids and expressing the thioesterases that use C14-ACP. In some situations, C12 fatty acids can be produced by expressing thioesterases that use C12-ACP and attenuating thioesterases that produce non-C12 fatty acids. For example, C12 fatty acids can be produced by expressing a thioesterase that has a preference for producing C12 fatty acids and attenuating thioesterases that have a preference for producing fatty acids other than C12 fatty acids. This would result in a relatively homogeneous population of fatty acids that have a carbon chain length of 12. The fatty acid derivatives are recovered from the culture medium with substantially all of the fatty acid derivatives produced extracellularly. The fatty acid derivative composition produced by a recombinant host cell can be analyzed using methods known in the art, for example, GC-FID, in order to determine the distribution of particular fatty acid derivatives as well as chain lengths and degree of saturation of the components of the fatty acid derivative composition. Acetyl-CoA, malonyl-CoA, and fatty acid overproduction can be verified using methods known in the art, for example, by using radioactive precursors, HPLC, or GC-MS subsequent to cell lysis.
Additional non-limiting examples of thioesterases and polynucleotides encoding them for use in the fatty acid pathway are provided in PCT Publication No. WO 2010/075483, expressly incorporated by reference herein.
Production of Fatty AldehydesIn one embodiment, the recombinant host cell produces a fatty aldehyde. In some embodiments, a fatty acid produced by the recombinant host cell is converted into a fatty aldehyde. In some embodiments, the fatty aldehyde produced by the recombinant host cell is then converted into a fatty alcohol or a hydrocarbon.
In some embodiments, native (endogenous) fatty aldehyde biosynthetic polypeptides, such as aldehyde reductases, are present in the host cell (e.g., E. coli) and are effective to convert fatty aldehydes to fatty alcohols. In other embodiments, a native (endogenous) fatty aldehyde biosynthetic polypeptide is overexpressed. In still other embodiments, an exogenous fatty aldehyde biosynthetic polypeptide is introduced into a recombinant host cell and expressed or overexpressed.
A native or recombinant host cell may comprise a polynucleotide encoding an enzyme having fatty aldehyde biosynthesis activity (also referred to herein as a “fatty aldehyde biosynthetic polypeptide” or a “fatty aldehyde biosynthetic polypeptide” or enzyme). A fatty aldehyde is produced when the fatty aldehyde biosynthetic enzyme is expressed or overexpressed in the host cell.
A recombinant host cell engineered to produce a fatty aldehyde will typically convert some of the fatty aldehyde to a fatty alcohol.
In some embodiments, a fatty aldehyde is produced by expressing or overexpressing in the recombinant host cell a polynucleotide encoding a polypeptide having fatty aldehyde biosynthetic activity such as carboxylic acid reductase (CAR) activity.
The terms “carboxylic acid reductase,” and “CAR,” are used interchangeably herein with respect to a “fatty aldehyde biosynthetic polypeptide”. CarB, is an exemplary carboxylic acid reductase. In practicing the invention, a gene encoding a carboxylic acid reductase polypeptide may be expressed or overexpressed in the host cell. In some embodiments, the CarB polypeptide has the amino acid sequence of SEQ ID NO: 7. In other embodiments, the CarB polypeptide is a variant or mutant of SEQ ID NO: 7.
Examples of carboxylic acid reductase (CAR) polypeptides and polynucleotides encoding them include, but are not limited to FadD9 (EC 6.2.1.-, UniProtKB Q50631, GenBank NP—217106, SEQ ID NO: 34), CarA (GenBank ABK75684), CarB (GenBank YP889972; SEQ ID NO: 33) and related polypeptides described in PCT Publication No. WO 2010/042664 and U.S. Pat. No. 8,097,439, each of which is expressly incorporated by reference herein. In some embodiments the recombinant host cell further comprises a polynucleotide encoding a thioesterase.
In some embodiments, the fatty aldehyde is produced by expressing or overexpressing in the recombinant host cell a polynucleotide encoding a fatty aldehyde biosynthetic polypeptide, such as a polypeptide having acyl-ACP reductase (AAR) activity. Expression of acyl-ACP reductase in a recombinant host cell results in the production of fatty aldehydes and fatty alcohols. (See
A composition comprising fatty aldehydes (“a fatty aldehyde composition”) is produced by culturing a host cell in the presence of a carbon source under conditions effective to express the fatty aldehyde biosynthetic enzyme. In some embodiments, the fatty aldehyde composition comprises fatty aldehydes and fatty alcohols. Typically, the fatty aldehyde composition is recovered from the extracellular environment of the recombinant host cell, i.e., the cell culture medium.
Production of Fatty AlcoholsIn some embodiments, the recombinant host cell comprises a polynucleotide encoding a polypeptide (an enzyme) having fatty alcohol biosynthetic activity (also referred to herein as a “fatty alcohol biosynthetic polypeptide” or a “fatty alcohol biosynthetic enzyme”), and a fatty alcohol is produced by the recombinant host cell. A composition comprising fatty alcohols (“a fatty alcohol composition”) may be produced by culturing the recombinant host cell in the presence of a carbon source under conditions effective to express a fatty alcohol biosynthetic enzyme. In some embodiments, the fatty alcohol composition comprises fatty alcohols, however, a fatty alcohol composition may comprise other fatty acid derivatives. Typically, the fatty alcohol composition is recovered from the extracellular environment of the recombinant host cell, i.e., the cell culture medium.
In one approach, recombinant host cells have been engineered to produce fatty alcohols by expressing a thioesterase, which catalyzes the conversion of acyl-ACPs into free fatty acids (FFAs) and a carboxylic acid reductase (CAR), which converts free fatty acids into fatty aldehydes. Native (endogenous) aldehyde reductases present in the host cell (e.g., E. coli) can convert the fatty aldehydes into fatty alcohols.
In some embodiments, native (endogenous) fatty aldehyde biosynthetic polypeptides, such as aldehyde reductases present in the host cell, may be sufficient to convert fatty aldehydes to fatty alcohols. However, in other embodiments, a native (endogenous) fatty aldehyde biosynthetic polypeptide is overexpressed and in still other embodiments, an exogenous fatty aldehyde biosynthetic polypeptide is introduced into a recombinant host cell and expressed or overexpressed.
In some embodiments, the fatty alcohol is produced by expressing or overexpressing in the recombinant host cell a polynucleotide encoding a polypeptide having fatty alcohol biosynthetic activity which converts a fatty aldehyde to a fatty alcohol. For example, an “alcohol dehydrogenase” (also referred to herein as an “aldehyde reductase”, e.g., EC 1.1.1.1), may be used in practicing the invention. As used herein, the term “alcohol dehydrogenase” refers to a polypeptide capable of catalyzing the conversion of a fatty aldehyde to an alcohol (e.g., a fatty alcohol). One of ordinary skill in the art will appreciate that certain alcohol dehydrogenases are capable of catalyzing other reactions as well, and these non-specific alcohol dehydrogenases also are encompassed by the term “alcohol dehydrogenase.” Examples of alcohol dehydrogenase polypeptides useful in accordance with the invention include, but are not limited to A1rA of Acinetobacter sp. M-1 (SEQ ID NO: 3) or A1rA homologs such as AlrAadpl (SEQ ID NO: 4) and endogenous E. coli alcohol dehydrogenases such as YjgB, (AAC77226) (SEQ ID NO: 5), DkgA (NP—417485), DkgB (NP—414743), YdjL (AAC74846), YdjJ (NP—416288), AdhP (NP—415995), YhdH (NP—417719), YahK (NP—414859), YphC (AAC75598), YqhD (446856) and YbbO [AAC73595.1]. Additional examples are described in International Patent Application Publication Nos. WO 2007/136762, WO2008/119082 and WO 2010/062480, each of which is expressly incorporated by reference herein. In certain embodiments, the fatty alcohol biosynthetic polypeptide has aldehyde reductase or alcohol dehydrogenase activity (EC 1.1.1.1).
In another approach, recombinant host cells have been engineered to produce fatty alcohols by expressing fatty alcohol forming acyl-CoA reductases or fatty acyl reductases (“FARs”) which convert fatty acyl-thioester substrates (e.g., fatty acyl-CoA or fatty acyl-ACP) to fatty alcohols. In some embodiments, the fatty alcohol is produced by expressing or overexpressing a polynucleotide encoding a polypeptide having fatty alcohol forming acyl-CoA reductase (FAR) activity in a recombinant host cell. Examples of FAR polypeptides useful in accordance with this embodiment are described in PCT Publication No. WO 2010/062480 which is expressly incorporated by reference herein.
Fatty alcohol may be produced via an acyl-CoA dependent pathway utilizing fatty acyl-ACP and fatty acyl-CoA intermediates and an acyl-CoA independent pathway utilizing fatty acyl-ACP intermediates but not a fatty acyl-CoA intermediate. In particular embodiments, the enzyme encoded by the over expressed gene is selected from a fatty acid synthase, an acyl-ACP thioesterase, a fatty acyl-CoA synthase and an acetyl-CoA carboxylase. In some embodiments, the protein encoded by the over expressed gene is endogenous to the host cell. In other embodiments, the protein encoded by the overexpressed gene is heterologous to the host cell.
Fatty alcohols are also made in nature by enzymes that are able to reduce various acyl-ACP or acyl-CoA molecules to the corresponding primary alcohols. See also, U.S. Patent Publication Nos. 20100105963, and 20110206630 and U.S. Pat. No. 8,097,439, expressly incorporated by reference herein.
Strategies to increase production of fatty alcohols by recombinant host cells include increased flux through the fatty acid biosynthetic pathway by overexpression of native fatty acid biosynthetic genes and/or expression of exogenous fatty acid biosynthetic genes from different organisms in the production host such that fatty alcohol biosynthesis is increased.
Production of EstersAs used herein, the term “fatty ester” may be used with reference to an ester. A fatty ester as referred to herein can be any ester made from a fatty acid, for example a fatty acid ester. In some embodiments, a fatty ester contains an A side and a B side. As used herein, an “A side” of an ester refers to the carbon chain attached to the carboxylate oxygen of the ester. As used herein, a “B side” of an ester refers to the carbon chain comprising the parent carboxylate of the ester. In embodiments where the fatty ester is derived from the fatty acid biosynthetic pathway, the A side is contributed by an alcohol, and the B side is contributed by a fatty acid.
Any alcohol can be used to form the A side of the fatty esters. For example, the alcohol can be derived from the fatty acid biosynthetic pathway. Alternatively, the alcohol can be produced through non-fatty acid biosynthetic pathways. Moreover, the alcohol can be provided exogenously. For example, the alcohol can be supplied in the fermentation broth in instances where the fatty ester is produced by an organism. Alternatively, a carboxylic acid, such as a fatty acid or acetic acid, can be supplied exogenously in instances where the fatty ester is produced by an organism that can also produce alcohol.
The carbon chains comprising the A side or B side can be of any length. In one embodiment, the A side of the ester is at least about 1, 2, 3, 4, 5, 6, 7, 8, 10, 12, 14, 16, or 18 carbons in length. When the fatty ester is a fatty acid methyl ester, the A side of the ester is 1 carbon in length. When the fatty ester is a fatty acid ethyl ester, the A side of the ester is 2 carbons in length. The B side of the ester can be at least about 4, 6, 8, 10, 12, 14, 16, 18, 20, 22, 24, or 26 carbons in length. The A side and/or the B side can be straight or branched chain. The branched chains can have one or more points of branching. In addition, the branched chains can include cyclic branches. Furthermore, the A side and/or B side can be saturated or unsaturated. If unsaturated, the A side and/or B side can have one or more points of unsaturation.
In one embodiment, the fatty ester is produced biosynthetically. In this embodiment, first the fatty acid is “activated.” Non-limiting examples of “activated” fatty acids are acyl-CoA, acyl ACP, and acyl phosphate. Acyl-CoA can be a direct product of fatty acid biosynthesis or degradation. In addition, acyl-CoA can be synthesized from a free fatty acid, a CoA, and an adenosine nucleotide triphosphate (ATP). An example of an enzyme which produces acyl-CoA is acyl-CoA synthase.
In some embodiments, the recombinant host cell comprises a polynucleotide encoding a polypeptide, e.g., an enzyme having ester synthase activity, (also referred to herein as an “ester synthase polypeptide” or an “ester synthase”). A fatty ester is produced by a reaction catalyzed by the ester synthase polypeptide expressed or overexpressed in the recombinant host cell. In some embodiments, a composition comprising fatty esters (also referred to herein as a “fatty ester composition”) comprising fatty esters is produced by culturing the recombinant cell in the presence of a carbon source under conditions effective to express an ester synthase. In some embodiments, the fatty ester composition is recovered from the cell culture.
Ester synthase polypeptides include, for example, an ester synthase polypeptide classified as EC 2.3.1.75, or any other polypeptide which catalyzes the conversion of an acyl-thioester to a fatty ester, including, without limitation, a thioesterase, an ester synthase, an acyl-CoA:alcohol transacylase, an acyltransferase, or a fatty acyl-CoA:fatty alcohol acyltransferase. For example, the polynucleotide may encode wax/dgat, a bifunctional ester synthase/acyl-CoA:diacylglycerol acyltransferase from Simmondsia chinensis, Acinetobacter sp. Strain ADP, Alcanivorax borkumensis, Pseudomonas aeruginosa, Fundibacter jadensis, Arabidopsis thaliana, or Alkaligenes eutrophus. In a particular embodiment, the ester synthase polypeptide is an Acinetobacter sp. diacylglycerol O-acyltransferase (wax-dgaT; UniProtKB Q8GGG1, GenBank AA017391) or Simmondsia chinensis wax synthase (UniProtKB Q9XGY6, GenBank AAD38041. In another embodiment, the ester synthase polypeptide is for example ES9 (a wax ester synthase from Marinobacter hydrocarbonoclasticus DSM 8798, UniProtKB A3RE51 (SEQ ID NO: 6); ES8 of Marinobacter hydrocarbonoclasticus DSM8789 (GenBank Accession No. AB021021; SEQ ID NO:7); GenBank AB021021, encoded by the ws2 gene; or ES376 (another wax ester synthase derived from Marinobacter hydrocarbonoclasticus DSM 8798, UniProtKB A3RE50, GenBank AB021020, encoded by the ws1 gene. In a particular embodiment, the polynucleotide encoding the ester synthase polypeptide is overexpressed in the recombinant host cell.
In some embodiments, a fatty acid ester is produced by a recombinant host cell engineered to express three fatty acid biosynthetic enzymes: a thioesterase enzyme, an acyl-CoA synthetase (fadD) enzyme and an ester synthase enzyme (“three enzyme system”;
In other embodiments, a fatty acid ester is produced by a recombinant host cell engineered to express one fatty acid biosynthetic enzyme, an ester synthase enzyme (“one enzyme system”;
Non-limiting examples of ester synthase polypeptides and polynucleotides encoding them suitable for use in these embodiments include those described in PCT Publication Nos. WO 2007/136762 and WO2008/119082, and WO/2011/038134 (“three enzyme system”) and WO/2011/038132 (“one enzyme system”), each of which is expressly incorporated by reference herein.
The recombinant host cell may produce a fatty ester, such as a fatty acid methyl ester, a fatty acid ethyl ester or a wax ester in the extracellular environment of the host cells.
Production of HydrocarbonsThis aspect of the invention is based, at least in part, on the discovery that altering the level of expression of a fatty aldehyde biosynthetic polypeptide, for example, an acyl-ACP reductase polypeptide (EC 6.4.1.2) and a hydrocarbon biosynthetic polypeptide, e.g., a decarbonylase in a recombinant host cell facilitates enhanced production of hydrocarbons by the recombinant host cell.
In one embodiment, the recombinant host cell produces a hydrocarbon, such as an alkane or an alkene (e.g., a terminal olefin or an internal olefin) or a ketone. In some embodiments, a fatty aldehyde produced by a recombinant host cell is converted by decarboxylation, removing a carbon atom to form a hydrocarbon. In other embodiments, a fatty acid produced by a recombinant host cell is converted by decarboxylation, removing a carbon atom to form a terminal olefin. In some embodiments, an acyl-ACP intermediate is converted by decarboxylation, removing a carbon atom to form an internal olefin or a ketone. See,
In some embodiments, the recombinant host cell comprises a polynucleotide encoding a polypeptide (an enzyme) having hydrocarbon biosynthetic activity (also referred to herein as a “hydrocarbon biosynthetic polypeptide” or a “hydrocarbon biosynthetic enzyme”), and the hydrocarbon is produced by expression or overexpression of the hydrocarbon biosynthetic enzyme in a recombinant host cell.
An alkane biosynthetic pathway from cyanobacteria consisting of an acyl-acyl carrier protein reductase (AAR) and an aldehyde decarbonylase (ADC), which together convert intermediates of fatty acid metabolism to alkanes and alkenes has been used to engineer recombinant host cells for the production of hydrocarbons (
In some embodiments, the hydrocarbon is produced by expressing or overexpressing in the recombinant host cell a polynucleotide encoding a polypeptide having hydrocarbon biosynthetic activity such as an aldehyde decarbonylase (ADC) activity (e.g., EC 4.1.99.5). exemplary polynucleotides encoding an aldehyde decarbonylase useful in accordance with this embodiment include, but are not limited to, those described in PCT Publication Nos. WO 2008/119082 and WO 2009/140695 which are expressly incorporated by reference herein and those sequences presented in Table 2, below. In some embodiments the recombinant host cell further comprises a polynucleotide encoding a fatty aldehyde biosynthesis polypeptide. In some embodiments the recombinant host cell further comprises a polynucleotide encoding an acyl-ACP reductase. See, for example Table 2, below.
In some embodiments, a composition comprising hydrocarbons (also referred to herein as a “hydrocarbon composition”) is produced by culturing the recombinant cell in the presence of a carbon source under conditions effective to express the Acyl-CoA reductase and decarbonylase polynucleotides. In some embodiments, the hydrocarbon composition comprises saturated and unsaturated hydrocarbons, however, a hydrocarbon composition may comprise other fatty acid derivatives. Typically, the hydrocarbon composition is recovered from the extracellular environment of the recombinant host cell, i.e., the cell culture medium.
As used herein, the term “alkane” means saturated hydrocarbons or compounds that consist only of carbon (C) and hydrogen (H), wherein these atoms are linked together by single bonds (i.e., they are saturated compounds).
The terms “olefin” and “alkene” are used interchangeably herein, and refer to hydrocarbons containing at least one carbon-to-carbon double bond (i.e., they are unsaturated compounds).
The terms “terminal olefin,” “α-olefin”, “terminal alkene” and “1-alkene” are used interchangeably herein with reference to α-olefins or alkenes with a chemical formula CxH2x, distinguished from other olefins with a similar molecular formula by linearity of the hydrocarbon chain and the position of the double bond at the primary or alpha position.
In some embodiments, a terminal olefin is produced by expressing or overexpressing in the recombinant host cell a polynucleotide encoding a hydrocarbon biosynthetic polypeptide, such as a polypeptide having decarboxylase activity as described, for example, in PCT Publication No. WO 2009/085278 which is expressly incorporated by reference herein. In some embodiments the recombinant host cell further comprises a polynucleotide encoding a thioesterase.
In other embodiments, a ketone is produced by expressing or overexpressing in the recombinant host cell a polynucleotide encoding a hydrocarbon biosynthetic polypeptide, such as a polypeptide having OleA activity as described, for example, in PCT Publication No. WO 2008/147781, which is expressly incorporated by reference herein.
In related embodiments, an internal olefin is produced by expressing or overexpressing in the recombinant host cell a polynucleotide encoding a hydrocarbon biosynthetic polypeptide, such as a polypeptide having OleCD or OleBCD activity together with a polypeptide having OleA activity as described, for example, in PCT Publication No. WO 2008/147781, expressly incorporated by reference herein.
Recombinant Host Cells and Cell CulturesStrategies to increase production of fatty acid derivatives by recombinant host cells include increased flux through the fatty acid biosynthetic pathway by overexpression of native fatty acid biosynthetic genes and expression of exogenous fatty acid biosynthetic genes from different organisms in the production host.
As used herein, the term “recombinant host cell” or “engineered host cell” refers to a host cell whose genetic makeup has been altered relative to the corresponding wild-type host cell, for example, by deliberate introduction of new genetic elements and/or deliberate modification of genetic elements naturally present in the host cell. The offspring of such recombinant host cells also contain these new and/or modified genetic elements. In any of the aspects of the invention described herein, the host cell can be selected from the group consisting of a plant cell, insect cell, fungus cell (e.g., a filamentous fungus, such as Candida sp., or a budding yeast, such as Saccharomyces sp.), an algal cell and a bacterial cell. In one preferred embodiment, recombinant host cells are “recombinant microorganisms.”
Examples of host cells that are microorganisms, include but are not limited to cells from the genus Escherichia, Bacillus, Lactobacillus, Zymomonas, Rhodococcus, Pseudomonas, Aspergillus, Trichoderma, Neurospora, Fusarium, Humicola, Rhizomucor, Kluyveromyces, Pichia, Mucor, Myceliophtora, Penicillium, Phanerochaete, Pleurotus, Trametes, Chrysosporium, Saccharomyces, Stenotrophamonas, Schizosaccharomyces, Yarrowia, or Streptomyces. In some embodiments, the host cell is a Gram-positive bacterial cell. In other embodiments, the host cell is a Gram-negative bacterial cell.
In some embodiments, the host cell is an E. coli cell.
In other embodiments, the host cell is a Bacillus lentus cell, a Bacillus brevis cell, a Bacillus stearothermophilus cell, a Bacillus lichenoformis cell, a Bacillus alkalophilus cell, a Bacillus coagulans cell, a Bacillus circulans cell, a Bacillus pumilis cell, a Bacillus thuringiensis cell, a Bacillus clausii cell, a Bacillus megaterium cell, a Bacillus subtilis cell, or a Bacillus amyloliquefaciens cell.
In other embodiments, the host cell is a Trichoderma koningii cell, a Trichoderma viride cell, a Trichoderma reesei cell, a Trichoderma longibrachiatum cell, an Aspergillus awamori cell, an Aspergillus fumigates cell, an Aspergillus foetidus cell, an Aspergillus nidulans cell, an Aspergillus niger cell, an Aspergillus oryzae cell, a Humicola insolens cell, a Humicola lanuginose cell, a Rhodococcus opacus cell, a Rhizomucor miehei cell, or a Mucor michei cell.
In yet other embodiments, the host cell is a Streptomyces lividans cell or a Streptomyces murinus cell.
In yet other embodiments, the host cell is an Actinomycetes cell.
In some embodiments, the host cell is a Saccharomyces cerevisiae cell.
In other embodiments, the host cell is a cell from a eukaryotic plant, algae, cyanobacterium, green-sulfur bacterium, green non-sulfur bacterium, purple sulfur bacterium, purple non-sulfur bacterium, extremophile, yeast, fungus, an engineered organism thereof, or a synthetic organism. In some embodiments, the host cell is light-dependent or fixes carbon. In some embodiments, the host cell has autotrophic activity. In some embodiments, the host cell has photoautotrophic activity, such as in the presence of light. In some embodiments, the host cell is heterotrophic or mixotrophic in the absence of light. In certain embodiments, the host cell is a cell from Arabidopsis thaliana, Panicum virgatum, Miscanthus giganteus, Zea mays, Botryococcuse braunii, Chlamydomonas reinhardtii, Dunaliela sauna, Synechococcus Sp. PCC 7002, Synechococcus Sp. PCC 7942, Synechocystis Sp. PCC 6803, Thermosynechococcus elongates BP-1, Chlorobium tepidum, Chlorojlexus auranticus, Chromatiumm vinosum, Rhodospirillum rubrum, Rhodobacter capsulatus, Rhodopseudomonas palusris, Clostridium ljungdahlii, Clostridiuthermocellum, Penicillium chrysogenum, Pichia pastoris, Saccharomyces cerevisiae, Schizosaccharomyces pombe, Pseudomonas fluorescens, or Zymomonas mobilis.
Production of Fatty Acid Derivative Compositions by Recombinant Host CellsA large variety of fatty acid derivatives can be produced by recombinant host cells comprising strain improvements as described herein, including, but not limited to, fatty acids, acyl-CoA, fatty aldehydes, short and long chain alcohols, hydrocarbons (e.g., alkanes, alkenes or olefins, such as terminal or internal olefins), fatty alcohols, esters (e.g., wax esters, fatty acid esters (e.g., methyl or ethyl esters)), and ketones.
In some embodiments of the present invention, the higher titer of fatty acid derivatives in a particular composition is a higher titer of a particular type of fatty acid derivative (e.g., fatty alcohols, fatty acid esters, or hydrocarbons) produced by a recombinant host cell culture relative to the titer of the same fatty acid derivatives produced by a control culture of a corresponding wild-type host cell. In such cases, the fatty acid derivative compositions may comprise, for example, a mixture of the fatty alcohols with a variety of chain lengths and saturation or branching characteristics.
In other embodiments of the present invention, the higher titer of fatty acid derivatives in a particular compositions is a higher titer of a combination of different fatty acid derivatives (for example, fatty aldehydes and alcohols, or fatty acids and esters) relative to the titer of the same fatty acid derivative produced by a control culture of a corresponding wild-type host cell.
Engineering Host CellsIn some embodiments, a polynucleotide (or gene) sequence is provided to the host cell by way of a recombinant vector, which comprises a promoter operably linked to the polynucleotide sequence. In certain embodiments, the promoter is a developmentally-regulated, an organelle-specific, a tissue-specific, an inducible, a constitutive, or a cell-specific promoter.
In some embodiments, the recombinant vector comprises at least one sequence selected from the group consisting of (a) an expression control sequence operatively coupled to the polynucleotide sequence; (b) a selection marker operatively coupled to the polynucleotide sequence; (c) a marker sequence operatively coupled to the polynucleotide sequence; (d) a purification moiety operatively coupled to the polynucleotide sequence; (e) a secretion sequence operatively coupled to the polynucleotide sequence; and (f) a targeting sequence operatively coupled to the polynucleotide sequence.
The expression vectors described herein include a polynucleotide sequence described herein in a form suitable for expression of the polynucleotide sequence in a host cell. It will be appreciated by those skilled in the art that the design of the expression vector can depend on such factors as the choice of the host cell to be transformed, the level of expression of polypeptide desired, etc. The expression vectors described herein can be introduced into host cells to produce polypeptides, including fusion polypeptides, encoded by the polynucleotide sequences as described herein.
Expression of genes encoding polypeptides in prokaryotes, for example, E. coli, is most often carried out with vectors containing constitutive or inducible promoters directing the expression of either fusion or non-fusion polypeptides. Fusion vectors add a number of amino acids to a polypeptide encoded therein, usually to the amino- or carboxy-terminus of the recombinant polypeptide. Such fusion vectors typically serve one or more of the following three purposes: (1) to increase expression of the recombinant polypeptide; (2) to increase the solubility of the recombinant polypeptide; and (3) to aid in the purification of the recombinant polypeptide by acting as a ligand in affinity purification. Often, in fusion expression vectors, a proteolytic cleavage site is introduced at the junction of the fusion moiety and the recombinant polypeptide. This enables separation of the recombinant polypeptide from the fusion moiety after purification of the fusion polypeptide. Examples of such enzymes, and their cognate recognition sequences, include Factor Xa, thrombin, and enterokinase. Exemplary fusion expression vectors include pGEX (Pharmacia Biotech, Inc., Piscataway, N.J.; Smith et al., Gene, 67: 31-40 (1988)), pMAL (New England Biolabs, Beverly, Mass.), and pRITS (Pharmacia Biotech, Inc., Piscataway, N.J.), which fuse glutathione S-transferase (GST), maltose E binding protein, or protein A, respectively, to the target recombinant polypeptide.
Examples of inducible, non-fusion E. coli expression vectors include pTrc (Amann et al., Gene (1988) 69:301-315) and pET 11d (Studier et al., Gene Expression Technology: Methods in Enzymology 185, Academic Press, San Diego, Calif. (1990) 60-89). Target gene expression from the pTrc vector relies on host RNA polymerase transcription from a hybrid trp-lac fusion promoter. Target gene expression from the pET 11d vector relies on transcription from a T7 gn10-lac fusion promoter mediated by a coexpressed viral RNA polymerase (T7 gni). This viral polymerase is supplied by host strains BL21(DE3) or HMS174(DE3) from a resident 2 prophage harboring a T7 gni gene under the transcriptional control of the lacUV 5 promoter.
Suitable expression systems for both prokaryotic and eukaryotic cells are well known in the art; see, e.g., Sambrook et al., “Molecular Cloning: A Laboratory Manual,” second edition, Cold Spring Harbor Laboratory, (1989). Examples of inducible, non-fusion E. coli expression vectors include pTrc (Amann et al., Gene, 69: 301-315 (1988)) and PET 11 d (Studier et al., Gene Expression Technology: Methods in Enzymology 185, Academic Press, San Diego, Calif., pp. 60-89 (1990)). In certain embodiments, a polynucleotide sequence of the invention is operably linked to a promoter derived from bacteriophage T5.
In one embodiment, the host cell is a yeast cell. In this embodiment, the expression vector is a yeast expression vector.
Vectors can be introduced into prokaryotic or eukaryotic cells via a variety of art-recognized techniques for introducing foreign nucleic acid (e.g., DNA) into a host cell. Suitable methods for transforming or transfecting host cells can be found in, for example, Sambrook et al. (supra).
For stable transformation of bacterial cells, it is known that, depending upon the expression vector and transformation technique used, only a small fraction of cells will take-up and replicate the expression vector. In order to identify and select these transformants, a gene that encodes a selectable marker (e.g., resistance to an antibiotic) can be introduced into the host cells along with the gene of interest. Selectable markers include those that confer resistance to drugs such as, but not limited to, ampicillin, kanamycin, chloramphenicol, or tetracycline. Nucleic acids encoding a selectable marker can be introduced into a host cell on the same vector as that encoding a polypeptide described herein or can be introduced on a separate vector. Cells stably transformed with the introduced nucleic acid can be identified by growth in the presence of an appropriate selection drug.
Host CellsAs used herein, an engineered or recombinant “host cell” is a cell used to produce a fatty acid derivative composition as further described herein.
A host cell is referred to as an “engineered host cell” or a “recombinant host cell” if the expression of one or more polynucleotides or polypeptides in the host cell are altered or modified as compared to their expression in a corresponding wild-type (or “native”) host cell under the same conditions.
In any of the aspects of the invention described herein, the host cell can be selected from the group consisting of a eukaryotic plant, algae, cyanobacterium, green-sulfur bacterium, green non-sulfur bacterium, purple sulfur bacterium, purple non-sulfur bacterium, extremophile, yeast, fungus, engineered organisms thereof, or a synthetic organism. In some embodiments, the host cell is light dependent or fixes carbon. In some embodiments, the host cell has autotrophic activity.
Various host cells can be used to produce fatty acid derivatives, as described herein.
Mutants or VariantsIn some embodiments, the polypeptide is a mutant or a variant of any of the polypeptides described herein. The terms “mutant” and “variant” as used herein refer to a polypeptide having an amino acid sequence that differs from a wild-type polypeptide by at least one amino acid. For example, the mutant can comprise one or more of the following conservative amino acid substitutions: replacement of an aliphatic amino acid, such as alanine, valine, leucine, and isoleucine, with another aliphatic amino acid; replacement of a serine with a threonine; replacement of a threonine with a serine; replacement of an acidic residue, such as aspartic acid and glutamic acid, with another acidic residue; replacement of a residue bearing an amide group, such as asparagine and glutamine, with another residue bearing an amide group; exchange of a basic residue, such as lysine and arginine, with another basic residue; and replacement of an aromatic residue, such as phenylalanine and tyrosine, with another aromatic residue. In some embodiments, the mutant polypeptide has about 1, 2, 3, 4, 5, 6, 7, 8, 9, 10, 15, 20, 30, 40, 50, 60, 70, 80, 90, 100, or more amino acid substitutions, additions, insertions, or deletions.
Preferred fragments or mutants of a polypeptide retain some or all of the biological function (e.g., enzymatic activity) of the corresponding wild-type polypeptide. In some embodiments, the fragment or mutant retains at least 75%, at least 80%, at least 90%, at least 95%, or at least 98% or more of the biological function of the corresponding wild-type polypeptide. In other embodiments, the fragment or mutant retains about 100% of the biological function of the corresponding wild-type polypeptide. Guidance in determining which amino acid residues may be substituted, inserted, or deleted without affecting biological activity may be found using computer programs well known in the art, for example, LASERGENE™ software (DNASTAR, Inc., Madison, Wis.).
In yet other embodiments, a fragment or mutant exhibits increased biological function as compared to a corresponding wild-type polypeptide. For example, a fragment or mutant may display at least a 10%, at least a 25%, at least a 50%, at least a 75%, or at least a 90% improvement in enzymatic activity as compared to the corresponding wild-type polypeptide. In other embodiments, the fragment or mutant displays at least 100% (e.g., at least 200%, or at least 500%) improvement in enzymatic activity as compared to the corresponding wild-type polypeptide.
It is understood that the polypeptides described herein may have additional conservative or non-essential amino acid substitutions, which do not have a substantial effect on the polypeptide function. Whether or not a particular substitution will be tolerated (i.e., will not adversely affect desired biological function, such as carboxylic acid reductase activity) can be determined as described in Bowie et al. (Science, 247: 1306-1310 (1990)). A “conservative amino acid substitution” is one in which the amino acid residue is replaced with an amino acid residue having a similar side chain. Families of amino acid residues having similar side chains have been defined in the art. These families include amino acids with basic side chains (e.g., lysine, arginine, histidine), acidic side chains (e.g., aspartic acid, glutamic acid), uncharged polar side chains (e.g., glycine, asparagine, glutamine, serine, threonine, tyrosine, cysteine), nonpolar side chains (e.g., alanine, valine, leucine, isoleucine, proline, phenylalanine, methionine, tryptophan), beta-branched side chains (e.g., threonine, valine, isoleucine), and aromatic side chains (e.g., tyrosine, phenylalanine, tryptophan, histidine).
Variants can be naturally occurring or created in vitro. In particular, such variants can be created using genetic engineering techniques, such as site directed mutagenesis, random chemical mutagenesis, Exonuclease III deletion procedures, or standard cloning techniques. Alternatively, such variants, fragments, analogs, or derivatives can be created using chemical synthesis or modification procedures.
Methods of making variants are well known in the art. These include procedures in which nucleic acid sequences obtained from natural isolates are modified to generate nucleic acids that encode polypeptides having characteristics that enhance their value in industrial or laboratory applications. In such procedures, a large number of variant sequences having one or more nucleotide differences with respect to the sequence obtained from the natural isolate are generated and characterized. Typically, these nucleotide differences result in amino acid changes with respect to the polypeptides encoded by the nucleic acids from the natural isolates.
For example, variants can be prepared by using random and site-directed mutagenesis. Random and site-directed mutagenesis are described in, for example, Arnold, Curr. Opin. Biotech., 4: 450-455 (1993).
Random mutagenesis can be achieved using error prone PCR (see, e.g., Leung et al., Technique, 1: 11-15 (1989); and Caldwell et al., PCR Methods Applic., 2: 28-33 (1992)). In error prone PCR, PCR is performed under conditions where the copying fidelity of the DNA polymerase is low, such that a high rate of point mutations is obtained along the entire length of the PCR product. Briefly, in such procedures, nucleic acids to be mutagenized (e.g., a polynucleotide sequence encoding a carboxylic reductase enzyme) are mixed with PCR primers, reaction buffer, MgCl2, MnCl2, Taq polymerase, and an appropriate concentration of dNTPs for achieving a high rate of point mutation along the entire length of the PCR product. For example, the reaction can be performed using 20 fmoles of nucleic acid to be mutagenized, 30 pmole of each PCR primer, a reaction buffer comprising 50 mM KCl, 10 mM Tris HCl (pH 8.3), 0.01% gelatin, 7 mM MgCl2, 0.5 mM MnCl2, 5 units of Taq polymerase, 0.2 mM dGTP, 0.2 mM dATP, 1 mM dCTP, and 1 mM dTTP. PCR can be performed for 30 cycles of 94° C. for 1 min, 45° C. for 1 min, and 72° C. for 1 min. However, it will be appreciated that these parameters can be varied as appropriate. The mutagenized nucleic acids are then cloned into an appropriate vector, and the activities of the polypeptides encoded by the mutagenized nucleic acids are evaluated.
Site-directed mutagenesis can be achieved using oligonucleotide-directed mutagenesis to generate site-specific mutations in any cloned DNA of interest. Oligonucleotide mutagenesis is described in, for example, Reidhaar-Olson et al., Science, 241: 53-57 (1988). Briefly, in such procedures a plurality of double stranded oligonucleotides bearing one or more mutations to be introduced into the cloned DNA are synthesized and inserted into the cloned DNA to be mutagenized (e.g., a polynucleotide sequence encoding a CAR polypeptide). Clones containing the mutagenized DNA are recovered, and the activities of the polypeptides they encode are assessed.
Another method for generating variants is assembly PCR. Assembly PCR involves the assembly of a PCR product from a mixture of small DNA fragments. A large number of different PCR reactions occur in parallel in the same vial, with the products of one reaction priming the products of another reaction. Assembly PCR is described in, for example, U.S. Pat. No. 5,965,408.
Still another method of generating variants is sexual PCR mutagenesis. In sexual PCR mutagenesis, forced homologous recombination occurs between DNA molecules of different, but highly related, DNA sequences in vitro as a result of random fragmentation of the DNA molecule based on sequence homology. This is followed by fixation of the crossover by primer extension in a PCR reaction. Sexual PCR mutagenesis is described in, for example, Stemmer, Proc. Natl. Acad. Sci., U.S.A., 91: 10747-10751 (1994).
Variants can also be created by in vivo mutagenesis. In some embodiments, random mutations in a nucleic acid sequence are generated by propagating the sequence in a bacterial strain, such as an E. coli strain, which carries mutations in one or more of the DNA repair pathways. Such “mutator” strains have a higher random mutation rate than that of a wild-type strain. Propagating a DNA sequence (e.g., a polynucleotide sequence encoding a CAR polypeptide) in one of these strains will eventually generate random mutations within the DNA. Mutator strains suitable for use for in vivo mutagenesis are described in, for example, International Patent Application Publication No. WO 1991/016427.
Variants can also be generated using cassette mutagenesis. In cassette mutagenesis, a small region of a double-stranded DNA molecule is replaced with a synthetic oligonucleotide “cassette” that differs from the native sequence. The oligonucleotide often contains a completely and/or partially randomized native sequence.
Recursive ensemble mutagenesis can also be used to generate variants. Recursive ensemble mutagenesis is an algorithm for protein engineering (i.e., protein mutagenesis) developed to produce diverse populations of phenotypically related mutants whose members differ in amino acid sequence. This method uses a feedback mechanism to control successive rounds of combinatorial cassette mutagenesis. Recursive ensemble mutagenesis is described in, for example, Arkin et al., Proc. Natl. Acad. Sci., U.S.A., 89: 7811-7815 (1992).
In some embodiments, variants are created using exponential ensemble mutagenesis. Exponential ensemble mutagenesis is a process for generating combinatorial libraries with a high percentage of unique and functional mutants, wherein small groups of residues are randomized in parallel to identify, at each altered position, amino acids which lead to functional proteins. Exponential ensemble mutagenesis is described in, for example, Delegrave et al., Biotech. Res, 11: 1548-1552 (1993).
In some embodiments, variants are created using shuffling procedures wherein portions of a plurality of nucleic acids that encode distinct polypeptides are fused together to create chimeric nucleic acid sequences that encode chimeric polypeptides as described in, for example, U.S. Pat. Nos. 5,965,408 and 5,939,250.
Insertional mutagenesis is mutagenesis of DNA by the insertion of one or more bases. Insertional mutations can occur naturally, mediated by virus or transposon, or can be artificially created for research purposes in the lab, e.g., by transposon mutagenesis. When exogenous DNA is integrated into that of the host, the severity of any ensuing mutation depends entirely on the location within the host's genome wherein the DNA is inserted. For example, significant effects may be evident if a transposon inserts in the middle of an essential gene, in a promoter region, or into a repressor or an enhancer region. Transposon mutagenesis and high-throughput screening was done to find beneficial mutations that increase the titer or yield of a fatty acid derivative or derivatives.
Culture Recombinant Host Cells and Cell Cultures/FermentationAs used herein, the term “fermentation” broadly refers to the conversion of organic materials into target substances by host cells, for example, the conversion of a carbon source by recombinant host cells into fatty acids or derivatives thereof by propagating a culture of the recombinant host cells in a media comprising the carbon source.
As used herein, the term “conditions permissive for the production” means any conditions that allow a host cell to produce a desired product, such as a fatty acid or a fatty acid derivative. Similarly, the term “conditions in which the polynucleotide sequence of a vector is expressed” means any conditions that allow a host cell to synthesize a polypeptide. Suitable conditions include, for example, fermentation conditions. Fermentation conditions can comprise many parameters, including but not limited to temperature ranges, levels of aeration, feed rates and media composition. Each of these conditions, individually and in combination, allows the host cell to grow. Fermentation can be aerobic, anaerobic, or variations thereof (such as micro-aerobic). Exemplary culture media include broths or gels. Generally, the medium includes a carbon source that can be metabolized by a host cell directly. In addition, enzymes can be used in the medium to facilitate the mobilization (e.g., the depolymerization of starch or cellulose to fermentable sugars) and subsequent metabolism of the carbon source.
For small scale production, the engineered host cells can be grown in batches of, for example, about 100 mL, 500 mL, 1 L, 2 L, 5 L, or 10 L; fermented; and induced to express a desired polynucleotide sequence, such as a polynucleotide sequence encoding a CAR polypeptide. For large scale production, the engineered host cells can be grown in batches of about 10 L, 100 L, 1000 L, 10,000 L, 100,000 L, and 1,000,000 L or larger; fermented; and induced to express a desired polynucleotide sequence. Alternatively, large scale fed-batch fermentation may be carried out.
The fatty acid derivative compositions described herein are found in the extracellular environment of the recombinant host cell culture and can be readily isolated from the culture medium. A fatty acid derivative may be secreted by the recombinant host cell, transported into the extracellular environment or passively transferred into the extracellular environment of the recombinant host cell culture. The fatty acid derivative is isolated from a recombinant host cell culture using routine methods known in the art.
Products Derived from Recombinant Host Cells
As used herein, “fraction of modem carbon” or fM has the same meaning as defined by National Institute of Standards and Technology (NIST) Standard Reference Materials (SRMs4990B and 4990C, known as oxalic acids standards HOxI and HOxII, respectively. The fundamental definition relates to 0.95 times the 14C/12C isotope ratio HOxI (referenced to AD 1950). This is roughly equivalent to decay-corrected pre-Industrial Revolution wood. For the current living biosphere (plant material), fM is approximately 1.1.
Bioproducts (e.g., the fatty acid derivatives produced in accordance with the present disclosure) comprising biologically produced organic compounds, and in particular, the fatty acid derivatives produced using the fatty acid biosynthetic pathway herein, have not been produced from renewable sources and, as such, are new compositions of matter. These new bioproducts can be distinguished from organic compounds derived from petrochemical carbon on the basis of dual carbon-isotopic fingerprinting or 14C dating. Additionally, the specific source of biosourced carbon (e.g., glucose vs. glycerol) can be determined by dual carbon-isotopic fingerprinting (see, e.g., U.S. Pat. No. 7,169,588, which is herein incorporated by reference).
The ability to distinguish bioproducts from petroleum based organic compounds is beneficial in tracking these materials in commerce. For example, organic compounds or chemicals comprising both biologically based and petroleum based carbon isotope profiles may be distinguished from organic compounds and chemicals made only of petroleum based materials. Hence, the bioproducts herein can be followed or tracked in commerce on the basis of their unique carbon isotope profile.
Bioproducts can be distinguished from petroleum based organic compounds by comparing the stable carbon isotope ratio (13C/12C) in each sample. The 13C/12C ratio in a given bioproduct is a consequence of the 13C/12C ratio in atmospheric carbon dioxide at the time the carbon dioxide is fixed.
It also reflects the precise metabolic pathway. Regional variations also occur. Petroleum, C3 plants (the broadleaf), C4 plants (the grasses), and marine carbonates all show significant differences in 13C/12C and the corresponding δ13C values. Furthermore, lipid matter of C3 and C4 plants analyze differently than materials derived from the carbohydrate components of the same plants as a consequence of the metabolic pathway. Within the precision of measurement, 13C shows large variations due to isotopic fractionation effects, the most significant of which for bioproducts is the photosynthetic mechanism. The major cause of differences in the carbon isotope ratio in plants is closely associated with differences in the pathway of photosynthetic carbon metabolism in the plants, particularly the reaction occurring during the primary carboxylation (i.e., the initial fixation of atmospheric CO2). Two large classes of vegetation are those that incorporate the “C3” (or Calvin-Benson) photosynthetic cycle and those that incorporate the “C4” (or Hatch-Slack) photosynthetic cycle.
In C3 plants, the primary CO2 fixation or carboxylation reaction involves the enzyme ribulose-1,5-diphosphate carboxylase, and the first stable product is a 3-carbon compound. C3 plants, such as hardwoods and conifers, are dominant in the temperate climate zones.
In C4 plants, an additional carboxylation reaction involving another enzyme, phosphoenolpyruvate carboxylase, is the primary carboxylation reaction. The first stable carbon compound is a 4-carbon acid that is subsequently decarboxylated. The CO2 thus released is refixed by the C3 cycle. Examples of C4 plants are tropical grasses, corn, and sugar cane.
Both C4 and C3 plants exhibit a range of 13C/12C isotopic ratios, but typical values are about −7 to about −13 per mil for C4 plants and about −19 to about −27 per mil for C3 plants (see, e.g., Stuiver et al., Radiocarbon 19:355 (1977)). Coal and petroleum fall generally in this latter range. The 13C measurement scale was originally defined by a zero set by Pee Dee Belemnite (PDB) limestone, where values are given in parts per thousand deviations from this material. The “613C” values are expressed in parts per thousand (per mil), abbreviated, % o, and are calculated as follows:
δ13C(%)=[(13C/12C)sample−(13C/12C)standard]/(13C/12C) standard×1000
Since the PDB reference material (RM) has been exhausted, a series of alternative RMs have been developed in cooperation with the IAEA, USGS, NIST, and other selected international isotope laboratories. Notations for the per mil deviations from PDB is δ13C. Measurements are made on CO2 by high precision stable ratio mass spectrometry (IRMS) on molecular ions of masses 44, 45, and 46.
The compositions described herein include bioproducts produced by any of the methods described herein, including, for example, fatty aldehyde and alcohol products. Specifically, the bioproduct can have a δ13C of about −28 or greater, about −27 or greater, −20 or greater, −18 or greater, −15 or greater, −13 or greater, −10 or greater, or −8 or greater. For example, the bioproduct can have a δ13C of about −30 to about −15, about −27 to about −19, about −25 to about −21, about −15 to about −5, about −13 to about −7, or about −13 to about −10. In other instances, the bioproduct can have a δ13C of about −10, −11, −12, or −12.3.
Bioproducts produced in accordance with the disclosure herein, can also be distinguished from petroleum based organic compounds by comparing the amount of 14C in each compound. Because 14C has a nuclear half-life of 5730 years, petroleum based fuels containing “older” carbon can be distinguished from bioproducts which contain “newer” carbon (see, e.g., Currie, “Source Apportionment of Atmospheric Particles”, Characterization of Environmental Particles, J. Buffle and H. P. van Leeuwen, Eds., 1 of Vol. I of the IUPAC Environmental Analytical Chemistry Series (Lewis Publishers, Inc.) 3-74, (1992)).
The basic assumption in radiocarbon dating is that the constancy of 14C concentration in the atmosphere leads to the constancy of 14C in living organisms. However, because of atmospheric nuclear testing since 1950 and the burning of fossil fuel since 1850, 14C has acquired a second, geochemical time characteristic. Its concentration in atmospheric CO2, and hence in the living biosphere, approximately doubled at the peak of nuclear testing, in the mid-1960s. It has since been gradually returning to the steady-state cosmogenic (atmospheric) baseline isotope rate (14C/12C) of about 1.2×10-12, with an approximate relaxation “half-life” of 7-10 years. (This latter half-life must not be taken literally; rather, one must use the detailed atmospheric nuclear input/decay function to trace the variation of atmospheric and biospheric 14C since the onset of the nuclear age.)
It is this latter biospheric 14C time characteristic that holds out the promise of annual dating of recent biospheric carbon. 14C can be measured by accelerator mass spectrometry (AMS), with results given in units of “fraction of modern carbon” (fM). fM is defined by National Institute of Standards and Technology (NIST) Standard Reference Materials (SRMs) 4990B and 4990C. As used herein, “fraction of modern carbon” or “fM” has the same meaning as defined by National Institute of Standards and Technology (NIST) Standard Reference Materials (SRMs) 4990B and 4990C, known as oxalic acids standards HOxI and HOxII, respectively. The fundamental definition relates to 0.95 times the 14C/12C isotope ratio HOxI (referenced to AD 1950). This is roughly equivalent to decay-corrected pre-Industrial Revolution wood. For the current living biosphere (plant material), fM is approximately 1.1.
The compositions described herein include bioproducts that can have an fM 14C of at least about 1. For example, the bioproduct of the invention can have an fM 14C of at least about 1.01, an fM 14C of about 1 to about 1.5, an fM 14C of about 1.04 to about 1.18, or an fM 14C of about 1.111 to about 1.124.
Another measurement of 14C is known as the percent of modern carbon (pMC). For an archaeologist or geologist using 14C dates, AD 1950 equals “zero years old”. This also represents 100 pMC. “Bomb carbon” in the atmosphere reached almost twice the normal level in 1963 at the peak of thermo-nuclear weapons. Its distribution within the atmosphere has been approximated since its appearance, showing values that are greater than 100 pMC for plants and animals living since AD 1950. It has gradually decreased over time with today's value being near 107.5 pMC. This means that a fresh biomass material, such as corn, would give a 14C signature near 107.5 pMC. Petroleum based compounds will have a pMC value of zero. Combining fossil carbon with present day carbon will result in a dilution of the present day pMC content. By presuming 107.5 pMC represents the 14C content of present day biomass materials and 0 pMC represents the 14C content of petroleum based products, the measured pMC value for that material will reflect the proportions of the two component types. For example, a material derived 100% from present day soybeans would give a radiocarbon signature near 107.5 pMC. If that material was diluted 50% with petroleum based products, it would give a radiocarbon signature of approximately 54 pMC.
A biologically based carbon content is derived by assigning “100%” equal to 107.5 pMC and “0%” equal to 0 pMC. For example, a sample measuring 99 pMC will give an equivalent biologically based carbon content of 93%. This value is referred to as the mean biologically based carbon result and assumes all the components within the analyzed material originated either from present day biological material or petroleum based material.
A bioproduct comprising one or more fatty acid derivatives as described herein can have a pMC of at least about 50, 60, 70, 75, 80, 85, 90, 95, 96, 97, 98, 99, or 100. In other instances, a fatty acid derivative described herein can have a pMC of between about 50 and about 100; about 60 and about 100; about 70 and about 100; about 80 and about 100; about 85 and about 100; about 87 and about 98; or about 90 and about 95. In yet other instances, a fatty acid derivative described herein can have a pMC of about 90, 91, 92, 93, 94, or 94.2.
Screening Fatty Acid Derivative Compositions Produced by Recombinant Host CellsTo determine if conditions are sufficient to allow expression, a host cell can be cultured, for example, for about 4, 8, 12, 24, 36, or 48 hours. During and/or after culturing, samples can be obtained and analyzed to determine if the conditions allow expression. For example, the host cells in the sample or the medium in which the host cells were grown can be tested for the presence of a desired product. When testing for the presence of a product, assays, such as, but not limited to, TLC, HPLC, GC/FID, GC/MS, LC/MS, MS, can be used. Recombinant host cell cultures are screened at the 96 well plate level, 1 liter and 5 liter tank level and in a 1000 L pilot plant using a GC/FID assay for “total fatty species”.
Utility of Fatty Acid Derivative CompositionsA fatty acid is a carboxylic acid with a long aliphatic tail (chain), which is either saturated or unsaturated. Most naturally occurring fatty acids have a chain of an even number of carbon atoms, from 4 to 28. Fatty acids are usually derived from triglycerides. When they are not attached to other molecules, they are known as “free” fatty acids. Fatty acids are usually produced industrially by the hydrolysis of triglycerides, with the removal of glycerol.
Palm, soybean, rapeseed, coconut oil and sunflower oil are currently the most common sources of fatty acids. The majority of fatty acids derived from such sources are used in human food products. Coconut oil and palm kernel oil (consist mainly of 12 and 14 carbon fatty acids). These are particularly suitable for further processing to surfactants for washing and cleansing agents as well as cosmetics. Palm, soybean, rapeseed, and sunflower oil, as well as animal fats such as tallow, contain mainly long-chain fatty acids (e.g., C18, saturated and unsaturated) which are used as raw materials for polymer applications and lubricants. Ecological and toxicological studies suggest that fatty acid-derived products based on renewable resources have more favorable properties than petrochemical-based substances.
Fatty aldehydes are used to produce many specialty chemicals. For example, aldehydes are used to produce polymers, resins (e.g., Bakelite), dyes, flavorings, plasticizers, perfumes, pharmaceuticals, and other chemicals, some of which may be used as solvents, preservatives, or disinfectants. In addition, certain natural and synthetic compounds, such as vitamins and hormones, are aldehydes, and many sugars contain aldehyde groups. Fatty aldehydes can be converted to fatty alcohols by chemical or enzymatic reduction.
Fatty alcohols have many commercial uses. Worldwide annual sales of fatty alcohols and their derivatives are in excess of U.S. $1 billion. The shorter chain fatty alcohols are used in the cosmetic and food industries as emulsifiers, emollients, and thickeners. Due to their amphiphilic nature, fatty alcohols behave as nonionic surfactants, which are useful in personal care and household products, such as, for example, detergents. In addition, fatty alcohols are used in waxes, gums, resins, pharmaceutical salves and lotions, lubricating oil additives, textile antistatic and finishing agents, plasticizers, cosmetics, industrial solvents, and solvents for fats.
The invention also provides a surfactant composition or a detergent composition comprising a fatty alcohol produced by any of the methods described herein. One of ordinary skill in the art will appreciate that, depending upon the intended purpose of the surfactant or detergent composition, different fatty alcohols can be produced and used. For example, when the fatty alcohols described herein are used as a feedstock for surfactant or detergent production, one of ordinary skill in the art will appreciate that the characteristics of the fatty alcohol feedstock will affect the characteristics of the surfactant or detergent composition produced. Hence, the characteristics of the surfactant or detergent composition can be selected for by producing particular fatty alcohols for use as a feedstock.
A fatty alcohol-based surfactant and/or detergent composition described herein can be mixed with other surfactants and/or detergents well known in the art. In some embodiments, the mixture can include at least about 10%, at least about 15%, at least about 20%, at least about 30%, at least about 40%, at least about 50%, at least about 60%, or a range bounded by any two of the foregoing values, by weight of the fatty alcohol. In other examples, a surfactant or detergent composition can be made that includes at least about 5%, at least about 10%, at least about 20%, at least about 30%, at least about 40%, at least about 50%, at least about 60%, at least about 70%, at least about 80%, at least about 85%, at least about 90%, at least about 95%, or a range bounded by any two of the foregoing values, by weight of a fatty alcohol that includes a carbon chain that is 8, 9, 10, 11, 12, 13, 14, 15, 16, 17, 18, 19, 20, 21, or 22 carbons in length. Such surfactant or detergent compositions also can include at least one additive, such as a microemulsion or a surfactant or detergent from non-microbial sources such as plant oils or petroleum, which can be present in the amount of at least about 5%, at least about 10%, at least about 15%, at least about 20%, at least about 30%, at least about 40%, at least about 50%, at least about 60%, at least about 70%, at least about 80%, at least about 85%, at least about 90%, at least about 95%, or a range bounded by any two of the foregoing values, by weight of the fatty alcohol.
Esters have many commercial uses. For example, biodiesel, an alternative fuel, is comprised of esters (e.g., fatty acid methyl esters, fatty acid ethyl esters, etc.). Some low molecular weight esters are volatile with a pleasant odor, which makes them useful as fragrances or flavoring agents. In addition, esters are used as solvents for lacquers, paints, and varnishes. Furthermore, some naturally occurring substances, such as waxes, fats, and oils are comprised of esters. Esters are also used as softening agents in resins and plasticizers, flame retardants, and additives in gasoline and oil. In addition, esters can be used in the manufacture of polymers, films, textiles, dyes, and pharmaceuticals.
Hydrocarbons have many commercial uses. For example, shorter chain alkanes are used as fuels. Longer chain alkanes (e.g., from five to sixteen carbons) are used as transportation fuels (e.g., gasoline, diesel, or aviation fuel). Alkanes having more than sixteen carbon atoms are important components of fuel oils and lubricating oils. Even longer alkanes, which are solid at room temperature, can be used, for example, as a paraffin wax. In addition, longer chain alkanes can be cracked to produce commercially valuable shorter chain hydrocarbons.
Like short chain alkanes, short chain alkenes are used in transportation fuels. Longer chain alkenes are used in plastics, lubricants, and synthetic lubricants. In addition, alkenes are used as a feedstock to produce alcohols, esters, plasticizers, surfactants, tertiary amines, enhanced oil recovery agents, fatty acids, thiols, alkenylsuccinic anhydrides, epoxides, chlorinated alkanes, chlorinated alkenes, waxes, fuel additives, and drag flow reducers.
Ketones are used commercially as solvents. For example, acetone is frequently used as a solvent, but it is also a raw material for making polymers. Ketones are also used in lacquers, paints, explosives, perfumes, and textile processing. In addition, ketones are used to produce alcohols, alkenes, alkanes, imines, and enamines.
Lubricants are typically composed of olefins, particularly polyolefins and alpha-olefins. Lubricants can either be refined from crude petroleum or manufactured using raw materials refined from crude petroleum. Obtaining these specialty chemicals from crude petroleum requires a significant financial investment as well as a great deal of energy. It is also an inefficient process because frequently the long chain hydrocarbons in crude petroleum are cracked to produce smaller monomers. These monomers are then used as the raw material to manufacture the more complex specialty chemicals.
The invention is further illustrated by the following examples. The examples are provided for illustrative purposes only. They are not to be construed as limiting the scope or content of the invention in any way.
EXAMPLES Example 1 Production Host Modifications—Attenuation of Acyl-CoA DehydrogenaseThis example describes the construction of a genetically engineered host cell wherein the expression of a fatty acid degradation enzyme is attenuated.
The fadE gene of E. coli MG1655 (an E. coli K strain) was deleted using the Lambda Red (also known as the Red-Driven Integration) system described by Datsenko et al., Proc. Natl. Acad. Sci. USA 97: 6640-6645 (2000), with the following modifications:
The following two primers were used to create the deletion of fadE:
The Del-fadE-F and Del-fadE-R primers were used to amplify the kanamycin resistance (KmR) cassette from plasmid pKD13 (described by Datsenko et al., supra) by PCR. The PCR product was then used to transform electrocompetent E. coli MG1655 cells containing pKD46 (described in Datsenko et al., supra) that had been previously induced with arabinose for 3-4 hours. Following a 3-hour outgrowth in a super optimal broth with catabolite repression (SOC) medium at 37° C., the cells were plated on Luria agar plates containing 50 μg/mL of Kanamycin. Resistant colonies were identified and isolated after an overnight incubation at 37° C. Disruption of the fadE gene was confirmed by PCR amplification using primers fadE-L2 and fadE-R1, which were designed to flank the E. coli fadE gene.
The fadE deletion confirmation primers were:
After the fadE deletion was confirmed, a single colony was used to remove the KmR marker using the pCP20 plasmid as described by Datsenko et al., supra. The resulting MG1655 E. coli strain with the fadE gene deleted and the KmR marker removed was named E. coli MG1655 AfadE, or E. coli MG 1655 D1.
Fatty acid derivative (“total fatty species”) production by the MG1655 E. coli strain with the fadE gene deleted was compared to fatty acid derivative production by E. coli MG1655. The data presented in
A number of exemplary host cell strains are described herein, examples of which are described below in Table 3.
The main precursors for fatty acid biosynthesis are malonyl-CoA and acetyl-CoA (
In one approach, in order to increase malonyl-CoA levels, an acetyl-CoA carboxylase enzyme complex from Corynebacterium glutamicum (“C. glutamicum”) was overexpressed. Acetyl-CoA carboxylase (“acc”) consists of four discrete subunits, accA, accB, accC and accD (
The synthetic operons of the C. glutamicum acc genes were cloned in the following way in OP80: Ptrc1-accDACB, Ptrc3-accDACB, Ptrc1-accCBDA and Ptrc3-CBDA. Ptrc1 and Ptrc3 are derivatives of the commonly used Ptrc promoter, which allow attenuated transcription of target genes. Note that the native sequences were amplified from the chromosomal DNA as they showed favorable codon usage (only the codon for Arg6 in accCB was changed). The C. glutamicum birA gene was codon optimized and obtained by gene synthesis. It was cloned then downstream of the acc genes in all four operon constructs. Below we refer to the operon configuration accDACB as accD- and the operon configuration accDACB+birA as accD+.
The resulting plasmids were transformed into E. coli DAM1_i377, which contains integrated copies (i) of leaderless thioesterease 'tesA and acyl-CoA synthetase fadD from E. coli and Ester synthase 9 (ES9) from Marinobacter hydrocarbonoclasticus. All genes are controlled by Ptrc promoters. The strains were grown in 5NBT media in shake flasks and were analyzed for malonyl-CoA using the method described above.
In order to test the effect of combining panK and acc-birA overexpression, the optimized panK gene was cloned downstream of birA in ptrc1/3_accDACB-birA. Pantothenate kinase panK (or CoaA) catalyzes the first step in the biosynthesis of coenzyme A, an essential cofactor that is involved in many reactions, e.g. the formation of acetyl-CoA, the substrate for acetyl-CoA carboxylase. The resulting plasmids were transformed into DAM1_i377, grown in 5NBT (+TVS1) media in shake flasks, and the strains were analyzed for short-chain-CoAs using the method described above.
As shown in
The impact of coexpressing an acetyl-CoA carboxylase enzyme complex on fatty ester production was evaluated by expressing ester synthase 9 (SEQ ID NO:6) with and without acc genes in another E. coli production host. More specifically, plasmids OP80 (vector control), pDS57 (with ES9), pDS57-accD- (with ES9 and accDACB) or pDS57-accD+(with ES9 and accDACB-birA; SEQ ID NO:63) were transformed into E. coli strain DV2 and the corresponding transformants were selected on LB plates supplemented with 100 mg/L of spectinomycin.
Two transformants of each plasmid were independently inoculated into LB medium supplemented with 100 mg/L of spectinomycin and grown for 5-8 hours at 32C. The cultures were diluted 30-fold into a minimal medium with the following composition: 0.5 g/L NaCl, 1 mM MgSO4×7H2O, 0.1 mM CaCl2, 2 g/L NH4C1, 3 g/L KH2PO4, 6 g/L Na2HPO4, 1 mg/L thiamine, 1× trace metal solution, 10 mg/L ferric citrate, 100 mM Bis-Tris (pH7.0), 30 g/L glucose and 100 mg/L spectinomycin. After over-night growth at 32 C, the cultures were diluted 10-fold in quadruplicate into minimal medium of the same composition except that the media contained 1 g/L instead of 2 g/L NH4Cl and was supplemented with 1 mM IPTG and 2% (v/v) methanol. The resulting cultures were then grown at 32° C. in a shaker.
The production of fatty acid methyl esters (FAMEs) was analyzed by gas chromatography with flame ionization detector (GC-FID). The samples were extracted with butyl acetate in a ratio of 1:1 vol/vol. After strong vortexing, the samples were centrifuged, and the organic phase was analyzed by gas chromatography (GC). The analysis conditions were as follows: instrument: Trace GC Ultra, Thermo Electron Corporation with Flame ionization detector (FID) detector; column: DB-1 (1% diphenyl siloxane; 99% dimethyl siloxane) CO1 UFM 1/0.1/5 01 DET from Thermo Electron Corporation, phase pH 5, FT: 0.4 μm, length 5 m, id: 0.1 mm; inlet conditions: 250° C. splitless, 3.8 m 1/25 split method used depending upon sample concentration with split flow of 75 mL/m; carrier gas, flow rate: Helium, 3.0 mL/m; block temperature: 330° C.; oven temperature: 0.5 m hold at 50° C., 100° C./m to 330° C., 0.5 m hold at 330° C.; detector temperature: 300° C.; injection volume: 2 μL; run time/flow rate: 6.3 m/3.0 mL/m (splitless method), 3.8 m/1.5 mL/m (split 1/25 method), 3.04 m/1.2 mL/m (split 1/50 method).
FAMEs produced are shown in
The impact of coexpressing an acetyl-CoA carboxylase enzyme complex on Fatty alcohol production was evaluated by expressing the Acyl-ACP reductase (AAR) from Synechococcus elongatus with and without acc genes in E. coli DV2. The accD+operon configuration was selected as it gave the best results when coexpressed with ester synthase (see previous example).
The accDABC-birA operon was cloned downstream from the aar gene in pLS9185, a pCL1920 derivative) using Infusion technology, the resulting plasmid was transformed into E. coli DV2 and the corresponding transformants were selected on LB plates supplemented with 100 mg/L of spectinomycin.
Fatty alcohols produced are shown in
In addition, Example 3 describes co-expression of acc genes together with entire fab operons.
Example 3 Increased Flux Through the Fatty Acid Synthesis Pathway—iFABs A. Fatty Acid Derivative ProductionStrategies to increase the flux through the fatty acid synthesis pathway in recombinant host cells include both overexpression of native E. coli fatty acid biosynthesis genes and expression of exogenous fatty acid biosynthesis genes from different organisms in E. coli.
In this study, exogenous fatty acid biosynthesis genes from different organisms were combined in the genome of E. coli DV2. E. coli DV2 has the following genetic characterization: F-, λ-, ilvG-, rfb-50, rph-1, ΔfhuA::FRT, ΔfadE::FRT.
Sixteen strains containing iFABs 130-145 were evaluated. The detailed structure of iFABs 130-145 is presented in iFABs Table 4, below.
Each “iFAB” comprises various components in the following order: BS_fabI, BS_FabL, Vc_FabV, or Ec_FabI. All constructs contain St_H, St_D, and St_G, yet half of them have a synthetic RBS in front of St_H. All constructs contain either St_fabA or St_fabZ.
All constructs include Cac_fabF. See Table 4, below for the specific composition of iFABs 130-145.
The plasmid pCL-WT TRC WT TesA was transformed into each of the strains shown above and a fermentation was run in FA2 media with 20 hours from induction to harvest at both 32° C. and 37° C. Data for production of “Total Fatty Species” from duplicate plate screens is shown in
From this screen the best construct was determined to be DV2 with iFAB138. The iFAB138 construct was transferred into strain D178 to make strain EG149. This strain was used for further engineering. The sequence of iFAB138 in the genome of EG149 is presented as SEQ ID NO:19. (LOCUS integrated_pDS138 8029 bp ds-DNA linear15-JUL-2010).
B. Fatty Ester ProductionA full synthetic fab operon was integrated into the E. coli chromosome and evaluated for increased FAME production by expression in E. coli DAM1 pDS57. In addition, four synthetic acc operons from Corynebaterium glutamicum were coexpressed and evaluated for improved FAME productivity. Several strains were obtained that produced FAMEs at a faster rate and higher titers.
Sixteen different fab operons were constructed (either assembled in vitro or as plasmid-based intermediates) as summarized in Table 5. The fab operons were put under the control of the lacUV5 promoter and integrated into the IS5-11 site of E. coli DAM1. These strains were named ifab130 to 145. They were transformed either with pDS57 (containing ester synthase 377) or pDS57 coexpressing different versions of acc operons, see above) for evaluation of FAME production. Exemplary plasmids are described in Table 5.
The DAM1 ifab strains were analyzed in 96-well plates (4NBT medium), shake flasks (5NBT medium) and in fermenters at 32° C. The best results were obtained in 96-well plates and in shake flasks, where several DAM1 ifab strains with pDS57-acc-birA plasmids showed higher FAME titers. In particular, DAM1 ifab131, ifab135, ifab137, ifab138 and ifab143 with pDS57-accDACB-birA showed 20-40% improved titers indicating that in these strains a higher flux through the fatty acid pathway was achieved, which apparently resulted in a better product formation rate (these results were reproducible in several independent experiments).
It was also observed that the FAMEs produced by some of the outperforming DAM1 ifab/acc strains showed a shift towards higher chain length. In particular, DAM1 ifab138 pDS57-accDACB-birA showed a significantly higher C16 and C18 to C8-C14 FAME ratio than the control. These results suggest that a stronger pull by tesA/fadD/WS377 may further improve FAME production.
C. Effect of Overexpressing fabH and fabI on Fatty Acid Methyl Ester (FAME) Production
Strategies to increase the flux through the fatty acid synthesis pathway in recombinant host cells include both overexpression of native fatty acid biosynthesis genes and expression of heterologous fatty acid biosynthesis genes. FabH and fabI are two fatty acid biosynthetic enzymes that have been shown to be feedback inhibited. A study was conducted to determine if FabH and FabI might be limiting the rate of FAME production.
FabH and fabI homologues (from E. coli, B. subtilis, Acinetobacter baylyi ADP1, Marinobacter aquaeoli VT8, and Rhodococcus opacus) were overexpressed as a synthetic operon and evaluated in E. coli DAM1 pDS57 (a strain observed to be a good FAME producer).
In one approach, fabHfabI operons were constructed from organisms that accumulate waxes (A. baylyi, M. aquaeoli) or triacylglycerides (R. opacus) and integrated into the chromosome of E. coli DAM1 pDS57. In a related approach, a synthetic acc operons from C. glutamicum were co-expressed (as described in Example 2, above).
Eleven different fabHI operons were constructed (assembled in vitro) as summarized in Table 7. The fabHI operons were put under the control of IPTG inducible lacUV5 promoter and integrated into the IS5-11 site of E. coli DAM1. These strains were named as shown in the table below. They were transformed either with pDS57 (containing ester synthase 377) or pDS57 coexpressing different versions of acc operons for evaluation of FAME production.
The DAM1 ifabHI strains were analyzed in 96-well plates (4NBT medium), shake flasks (5NBT medium) and in fermenters at 32° C.
In shake flask, a number of the ifabHI strains carrying pDS57 plasmid performed better than the control DAM1 pDS57strain, reaching 10 to 15% higher FAME titers (
Some of the ifabHI strains were also run in fermenters, where an increase in FAME titers, specific productivity and yield were also observed (
The lacUV5 promoter of FAB138 was replaced by a T5 promoter leading to higher levels of expression of FAB138, as confirmed by mRNA analysis. The expression of FAB138 from the T5 promoter resulted in a higher titer, yield and productivity of fatty esters.
Strain BD64 is DV2 ifab138 iT5_fadR. Strain shu.002 is isogenic to strain BD64 except that it contains the T5 promoter controlling expression of the FAB138 operon.
Primers DG405 and DG406 were used to amplify a cat-loxP and T5 promoter cassette adding 50 bp homology to each end of the PCR product, such that it could be integrated into any strain replacing the lacUV5 promoter regulating expression of the FAB138 operon. The cat-loxP-T5 promoter was transformed into BD64/pKD46 strain. Transformants were recovered on LB+chloramphenicol plates at 37° C. overnight, patched to a fresh LB+chloramphenicol plate, and verified by colony PCR using primers DG422 and DG423. Plasmid pJW168 was transformed into strain BD64 i-cat-loxP-T5—138 and selected on LB+carbenicillin plates at 32° C. In order to remove the cat marker, expression of the cre-recombinase was induced by IPTG. The plasmid pHW168 was removed by growing cultures at 42° C. Colonies were patched on LB+chloramphenicol and LB+carbenicillin to verify loss of pJW168 and removal of cat marker, respectively. The colony was also patched into LB as a positive control, all patched plates were incubated at 32° C. The removal of the cat marker was confirmed by colony PCR using primers DG422 and DG423. The resulting PCR product was verified by sequencing with primers EG744, EG749 and oTREE047, the strain was called shu.002.
The sequence of the cat-loxP-T5 promoter integrated in front of FAB138 with 50 base pair of homology shown in each side of cat-loxP-T5 promoter region is presented as SEQ ID NO:1 and the sequence of the iT5—138 promoter region with 50 base pair homology in each side is presented as SEQ ID NO:2.
There are a number of conditions that can lead to increased fatty acid flux. In this example increased fatty acid flux was achieved by altering the promoter strength of operon FAB138. The expression of FAB138 from the T5 promoter was beneficial, however, when this promoter change was combined with the insertion of yijP::Tn5 cassette further improvements were observed in titer, yield and productivity of fatty acid esters and other fatty acid derivatives. (See Example 5).
Example 4 Increasing the Amount of Free Fatty Acid (FFA) Product by Repairing the Rph and ilvG MutationsThe ilvG and rph mutations were corrected in this strain resulting in higher production of FFA. Strains EG149 (D178 is 5-11::iFAB138) and V668 (EG149 rph+ilvG+) were transformed with pCL-tesA obtained from D191. Fermentation was run at 32° C. in FA2 media for 40 hours to compare the FFA production of strains D178, EG149, and V668 with pCL-tesA. Fermentation and extraction was run according to a standard FALC fermentation protocol exemplified by the following.
A frozen cell bank vial of the selected E. coli strain was used to inoculate 20 mL of LB broth in a 125 mL baffled shake flask containing spectinomycin antibiotic at a concentration of 115 μg/mL. This shake flask was incubated in an orbital shaker at 32° C. for approximately six hours, then 1.25 mL of the broth was transferred into 125 mL of low P FA2 seed media (2 g/L NH4C1, 0.5 g/L NaCl, 3 g/L KH2PO4, 0.25 g/L MgSO4-7H2O, 0.015 g/L mM CaCl2-2H2O, 30 g/L glucose, 1 mL/L of a trace minerals solution (2 g/L of ZnCl2. 4H2O, 2 g/L of CaCl2. 6H2O, 2 g/L of Na2MoO4. 2H2O, 1.9 g/L of CuSO4.5H2O, 0.5 g/L of H3BO3, and 10 mL/L of concentrated HCl), 10 mg/L of ferric citrate, 100 mM of Bis-Tris buffer (pH 7.0), and 115 μg/mL of spectinomycin), in a 500 mL baffled Erlenmeyer shake flask, and incubated on a shaker overnight at 32° C.
100 mL of this low P FA2 seed culture was used to inoculate a 5 L Biostat Aplus bioreactor (Sartorius BBI), initially containing 1.9 L of sterilized F1 bioreactor fermentation medium. This medium is initially composed of 3.5 g/L of KH2PO4, 0.5 g/L of (NH4)2SO4, 0.5 g/L of MgSO4 heptahydrate, 10 g/L of sterile filtered glucose, 80 mg/L ferric citrate, 5 g/L Casamino acids, 10 mL/L of the sterile filtered trace minerals solution, 1.25 mL/L of a sterile filtered vitamin solution (0.42 g/L of riboflavin, 5.4 g/L of pantothenic acid, 6 g/L of niacin, 1.4 g/L of pyridoxine, 0.06 g/L of biotin, and 0.04 g/L of folic acid), and the spectinomycin at the same concentration as utilized in the seed media. The pH of the culture was maintained at 6.9 using 28% w/v ammonia water, the temperature at 33° C., the aeration rate at 1 lpm (0.5 v/v/m), and the dissolved oxygen tension at 30% of saturation, utilizing the agitation loop cascaded to the DO controller and oxygen supplementation. Foaming was controlled by the automated addition of a silicone emulsion based antifoam (Dow Corning 1410).
A nutrient feed composed of 3.9 g/L MgSO4 heptahydrate and 600 g/L glucose was started when the glucose in the initial medium was almost depleted (approximately 4-6 hours following inoculation) under an exponential feed rate of 0.3 hr-1 to a constant maximal glucose feed rate of 10-12 g/L/hr, based on the nominal fermentation volume of 2 L. Production of fatty alcohol in the bioreactor was induced when the culture attained an OD of 5 AU (approximately 3-4 hours following inoculation) by the addition of a 1M IPTG stock solution to a final concentration of 1 mM. The bioreactor was sampled twice per day thereafter, and harvested approximately 72 hours following inoculation.
A 0.5 mL sample of the well-mixed fermentation broth was transferred into a 15 mL conical tube (VWR), and thoroughly mixed with 5 mL of butyl acetate. The tube was inverted several times to mix, then vortexed vigorously for approximately two minutes. The tube was then centrifuged for five minutes to separate the organic and aqueous layers, and a portion of the organic layer transferred into a glass vial for gas chromatographic analysis.
Correcting the rph and ilvG mutations resulted in a 116% increase in the FFA production of the base strain with pCL-tesA. As seen in
It has been demonstrated that expression of many genes, not limited to, fabA, B, Z, G, H, D, and fadR can lead to increased fatty acid production. Further strain improvements are likely to result in higher titers, yields and productivity of fatty acid derivatives such as FALC by recombinant host cells.
Example 5 Increased Production of Fatty Acid Derivatives by Transposon Mutagenesis—yijP A. Fatty Alcohol ProductionTo improve the titer, yield, productivity of fatty alcohol production by E. coli, transposon mutagenesis and high-throughput screening was carried out and beneficial mutations were sequenced. A transposon insertion in the yijP strain was shown to improve the strain's fatty alcohol yield in both shake flask and fed-batch fermentations.
The SL313 strain produces fatty alcohols. The genotype of this strain is provided in Table **.
The genotype of this strain is MG1655 (ΔfadE::FRT ΔfhuA::FRT fabBA329V ΔentD::T5-entD ΔinsH-11:: PlacUV5 fab138 rph+lacI::PA1_tesA) containing the plasmid pDG109 (pCL1920_PTRC_carBopt—12H08_alrAadp1_fabB[A329G]_fadR).
Briefly, transposon mutagenesis was carried out by preparation of transposon DNA was prepared by cloning a DNA fragment into the plasmid EZ-Tn5™ pMOD™<R6K ori/MCS> (Epicentre Biotechnologies). The DNA fragment contains a T5 promoter and the cat gene flanked by loxP sites. The resulting plasmid was named p100.38 and the sequence is listed in Appendix I. This plasmid was digested with PshAI restriction enzyme, incubated with EZ-Tn5™ Transposase enzyme (Epicentre Biotechnologies), and electroporated into electrocompetent SL313 cells as per the manufacturer's instructions. The resulting colonies contained the transposon DNA inserted randomly into the chromosome of SL313.
Transposon clones were then subjected to high-throughput screening to measure production of fatty alcohols. Briefly, colonies were picked into deep-well plates containing LB, grown overnight, inoculated into fresh LB and grown for 3 hours, inoculated into fresh FA-2.1 media, grown for 16 hours, then extracted using butyl acetate. The crude extract was derivatized with BSTFA (N,O-bis[Trimethylsilyl]trifluoroacetamide) and analyzed using GC/FID. Spectinomycin (100 ug/mL) was included in all media to maintain selection of the pDG109 plasmid.
Hits were selected by choosing clones that produced a similar total fatty species as the control strain SL313, but that had a higher percent of fatty alcohol species and a lower percent of free fatty acids than the control. Strain 68F11 was identified as a hit and was validated in a shake flask fermentation, according to the shake flask fermentation method described below. A comparison of transposon hit 68F11 to control strain SL313 indicated that 68F11 produces a higher percentage of fatty alcohol species than the control, while both strains produce similar titers of total fatty species.
A single colony of hit 68F11, named LC535, was sequenced to identify the location of the transposon insertion. Sequencing was performed according to previous transposon IDFs. Briefly, genomic DNA was purified from a 10 mL overnight LB culture using the kit ZR Fungal/Bacterial DNA MiniPrep™ (Zymo Research) according to the manufacturer's instructions. The purified genomic DNA was sequenced outward from the transposon using primers internal to the transposon:
Strain LC535 was determined to have a transposon insertion in the yijP gene (
Strain LC535 was evaluated in a fed-batch fermentation on two different dates. Both fermentations demonstrated that LC535 produced fatty alcohols with a higher yield than control SL313, and the improvement was 1.3-1.9% absolute yield based on carbon input.
The yijP transposon cassette was further evaluated in a different strain V940, which produces fatty alcohol at a higher yield than strain SL313. The yijP::Tn5-cat cassette was amplified from strain LC535 using primers:
This linear DNA was electroporated into strain SL571 and integrated into the chromosome using the lambda red recombination system. Colonies were screened using primers outside the transposon region:
A colony with the correct yijP transposon cassette was transformed with the production plasmid pV171.1 to produce strain D851. D851 (V940 yijP::Tn5-cat) was tested in a shake-flask fermentation against isogenic strain V940 that does not contain the yijP transposon cassette. The result of this fermentation showed that the yijP transposon cassette confers production of a higher percent of fatty alcohol by the D851 strain relative to the V940 strain and produces similar titers of total fatty species as the V940 control strain.
Strain D851 was evaluated in a fed-batch fermentation on two different dates. Data from these fermentations is shown in Table 9 which illustrates that in 5-liter fed-batch fermentations, strains with the yijP::Tn5-cat transposon insertion had an increased total fatty species (“FAS”) yield and an increase in percent fatty alcohol (“FALC”).
The terms “total fatty species” and “total fatty acid product” may be used interchangeably herein with reference to the amount of fatty alcohols, fatty aldehydes and free fatty acids, as evaluated by GC-FID as described in International Patent Application Publication WO 2008/119082. The same terms may be used to mean fatty esters and free fatty acids when referring to a fatty ester analysis. As used herein, the term “fatty esters” includes beta hydroxy esters.
To assess production of fatty acid esters in tank a glycerol vial of desired strain was used to inoculate 20 mL LB+spectinomycin in shake flask and incubated at 32° C. for approximately six hours. 4 mL of LB culture was used to inoculate 125 mL Low PFA Seed Media (below), which was then incubated at 32° C. shaker overnight. 50 mL of the overnight culture was used to inoculate 1 L of Tank Media. Tanks were run at pH 7.2 and 30.5° C. under pH stat conditions with a maximum feed rate of 16 g/L/hr (glucose or methanol).
Further studies suggest that the improved titer and yield of FAS and FALC in strains with the yijP transposon insertion is due to reduction in the activity of phosphoenolpyruvate carboxylase (ppc). A ppc enzyme assay was carried out in-vitro in the following strains to evaluate this hypothesis.
-
- 1) Δppc=DG14 (LC942 Δppc::cat-sacB/pLC56)
- 2) wt-ppc=DG16 (LC942/pLC56)
- 3) yijP::Tn5=DG18 (LC942 yijP::Tn5-cat/pCL56)
Ppc activity was measured in cells grown in a shake flask fermentation (as detailed above) and harvested 12-16 hours after induction. Approximately 5 mL of cells were centrifuged and the cell paste was suspended in BugBuster Protein Extraction Reagent (Novagen) with a protease inhibitor cocktail solution. The cell suspension was incubated with gentle shaking on a shaker for 20 min. Insoluble cell debris was removed by centrifugation at 16,000×g for 20 min at 4° C. followed by transferring the supernatant to a new tube. Ppc activity in the cell lysate was determined by a coupling reaction with citrate synthase using following reaction mixture: 0.4 mM acetyl-CoA, 10 mM phosphoenolpyruvate, 0.5 mM monobromobimane, 5 mM MgCl2, 10 mM NaHCO3, and 10 units citrate synthase from porcine heart in 100 mM Tris-HCl (pH 8.0). The formation of CoA in the reaction with citrate synthase using oxaloacetate and acetyl-CoA was monitored photometrically using fluorescent derivatization of CoA with monobromobimane.
The Ppc assay results showed that the yijP::Tn5-cat transposon cassette decreased the Ppc activity in the cell. The results also indicate that the highest yield of fatty alcohol production requires a level of Ppc expression lower than the wild-type level.
Proteomics data was also collected to assess the abundance of the Ppc protein in two strains with and without the yijP::Tn5-cat transposon cassette. Protein samples were collected from strains V940 and D851 grown in bioreactors under standard fatty alcohol production conditions. Samples were taken at three different time points: 32, 48, 56 hours and prepared for analysis.
Sample collection and protein isolation was carried out as follows:
-
- 1. 20 ml of fermentation broth were collected from each bioreactor at each time point. Samples were quenched with ice-cold PBS and harvested by centrifugation (4500 rpm/10 min) at 4° C. Cell pellet was washed with ice-cold PBS and centrifuged one more time and stored at −80° C. for further processing.
- 2. Total protein extraction was performed using a French press protocol. Briefly, cell pellets were resuspended in 7 ml of ice-cold PBS and French pressed at 2000 psi twice to ensure complete lysing of the bacteria. Samples were centrifuged for 20 min at 10000 rpm at 4° C. to separate non-lysed cells and cell debris from the protein fraction. Total protein concentration of clear lysate was determined using BCA Protein Assay Reagent. Samples were diluted to 2 mg proteins/ml concentration and frozen at −80° C.
- 3. Samples were resuspended in the appropriate buffer and trypsinized overnight at 37° C. and lyophilized. Fragmented protein samples were labeled with isotopically enriched methylpiperazine acetic acid at room temperature for 30 min. Labeled samples were separated using cation exchange liquid chromatography and subjected to mass spectroscopy analysis using an ion trap mass spectrometer. Raw data was normalized using background subtraction and bias correction.
Proteomics data showed a significant reduction in the relative abundance of Ppc protein in D851 strain when compared to V940 at 36 hours and 48 hours). These data show that the yijP::Tn5-cat transposon cassette results in a significant reduction in Ppc abundance in the cell. This suggests that the observed benefits to fatty alcohol production by strains harboring the yijP::Tn5-cat transposon hit is due to reducing the amount of Ppc protein.
These results suggest that altering ppc activity can improve the yield of fatty acid derivatives. There are a number of ways to alter the expression of the ppc gene, and the yijP transposon insertion is one way to accomplish this. While the mechanism is not part of the invention, if the effect of reducing phosphoenolpyruvate carboxylase activity is to limit the flow of carbon through the TCA cycle, one could achieve similar results by decreasing the activity of citrate synthase (gltA) or slowing the TCA cycle by decreasing the activity of any of the enzymes involved in the TCA cycle.
B. Fatty Ester ProductionAdditional strains with a transposon insertion in yijP were evaluated for production of fatty acid esters. Strains containing a transposon insertion in yijP were shown to produce higher yields of fatty acid esters and maintain the glucose utilization rate for a longer time in tanks.
A strain designated, “shu.010” was developed which is isogenic to strain BD64 except that it contains the yijP::Tn5-cat transposon cassette. The cassette containing the yijP::(Tn5) transposon DNA was amplified from strain DG851 using primers DG408 and DG407 (Table 12). The cassette was transformed into BD64/pKD46. Transformants were recovered on LB+chloramphenicol plates at 37° C. overnight, patched to a fresh LB+chloramphenicol plate, and verified by colony PCR using primers DG131, DG407, and DG408.
Plasmid pKEV022 was transformed into shu.010. After selection in LB+spectinomycin plates, one colony was selected and called shu.015. Strain shu.015 was grown in tanks using standard conditions (see Appendix I for media and tank conditions). The tank performance of shu.015 was compared to strains KEV006.1 (BD64 pKEV018) and KEV075 (BD64 pKEV022) for Total Fatty Acid Product, Total Product Yield and glucose utilization rate.
The yield of total fatty acid products for all strains was similar, however, shu.015 was able to sustain higher glucose utilization rates for a longer time than either KEV006.1 or KEV075, suggesting that yijP::Tn5 was responsible for the improvement.
Example 6 Increased Flux Through the Fatty Acid Synthesis Pathway—Acyl Carrier Protein (ACP) Mediated Fatty Alcohol ProductionWhen terminal pathway enzymes from sources other than E. coli are expressed in E. coli as the heterologous host to convert fatty acyl-ACPs to products, limitations may exist in the recognition, affinity and/or turnover of the recombinant pathway enzyme towards the E. coli fatty acyl-ACPs. Note that although ACP proteins are conserved to some extent in all organisms, their primary sequence can differ significantly.
To test this hypothesis the acp genes from several cyanobacteria were cloned downstream from the Synechococcus elongatus PCC7942 acyl-ACP reductase (AAR) present in pLS9-185, which is a pCL1920 derivative (3-5 copies/cell). In addition, the sfp gene (Accession no. X63158; SEQ ID NO:53) from Bacillus subtilis, encoding a phosphopantetheinyl transferase with broad substrate specificity, was cloned downstream of the respective acp genes. This enzyme is involved in conversion of the inactive apo-ACP to the active holo-ACP. The plasmids constructed are described in Table 13.
All the acp genes were cloned with a synthetic RBS into the EcoRI site immediately downstream of the aar gene in pLS9-185 using InFusion technology. The EcoRI site was reconstructed downstream of the acp gene. Similarly, the B. subtilis sfp gene was InFusion cloned into this EcoRI site along with a synthetic RBS. All plasmids were transformed into E. coli MG1655 DV2. The control for these experiments was the expression of AAR alone (pLS9-185).
The results from standard shake flask fermentation experiments are shown in
In order to evaluate if the overexpression of an ACP can also increase free fatty acid production, one cyanobacterial ACP gene with sfp was amplified from pDS171s (Table 13) and cloned downstream from 'tesA into a pCL vector. The resulting operon was under the control of the Ptrc3 promoter, which provides slightly lower transcription levels than the Ptrc wildtype promoter. The construct was cloned into E. coli DV2 and evaluated for fatty acid production. The control strain contained the identical plasmid but without cyanobacterial ACP and B. subtilis sfp.
The results from a standard microtiter plate fermentation experiment are shown in
All methods described herein can be performed in any suitable order unless otherwise indicated herein or otherwise clearly contradicted by context. The use of any and all examples, or exemplary language (e.g., “such as”) provided herein, is intended merely to better illuminate the invention and does not pose a limitation on the scope of the invention unless otherwise claimed. No language in the specification should be construed as indicating any non-claimed element as essential to the practice of the invention. It is to be understood that the terminology used herein is for the purpose of describing particular embodiments only, and is not intended to be limiting. Preferred embodiments of this invention are described herein. Variations of those preferred embodiments may become apparent to those of ordinary skill in the art upon reading the foregoing description. The inventors expect skilled artisans to employ such variations as appropriate, and the inventors intend for the invention to be practiced otherwise than as specifically described herein. Accordingly, this invention includes all modifications and equivalents of the subject matter recited in the claims appended hereto as permitted by applicable law. Moreover, any combination of the above-described elements in all possible variations thereof is encompassed by the invention unless otherwise indicated herein or otherwise clearly contradicted by context.
The terms “comprising,” “having,” “including,” and “containing” are to be construed as open-ended terms (i.e., meaning “including, but not limited to,”) unless otherwise noted. Recitation of ranges of values herein are merely intended to serve as a shorthand method of referring individually to each separate value falling within the range, unless otherwise indicated herein, and each separate value is incorporated into the specification as if it were individually recited herein.
Claims
1. A cultured genetically engineered host cell comprising:
- (a) a polynucleotide sequence encoding one or more of: (i) an acetyl-CoA carboxylase (EC 6.4.1.2) polypeptide, (ii) a FadR polypeptide, (iii) a heterologous iFAB polypeptide, (iv) a sequence having a transposon insertion in the yijP gene, and (v) a heterologous ACP protein; and
- (b) a polynucleotide sequence encoding a fatty acid derivative biosynthetic polypeptide, wherein the genetically engineered host cell produces a fatty acid derivative composition at a higher titer, yield or productivity when cultured in medium containing a carbon source under conditions effective to overexpress the polynucleotide(s) relative to a corresponding wild type host cell propagated under the same conditions as the genetically engineered host cell.
2. The genetically engineered host cell of claim 1, wherein the fatty acid derivative composition comprises a fatty acid derivative selected from the group consisting of a fatty acid, a fatty aldehyde, a fatty alcohol, a fatty ester, an alkane, a terminal olefin, an internal olefin and a ketone.
3. The genetically engineered host cell of claim 1 or 2, wherein the fatty acid derivative composition is produced at a titer that is at least 3 times greater, at least 5 times greater, at least 8 times greater, or at least 10 times greater than the titer of a fatty acid derivative composition produced by a corresponding wild type host cell cultured under the same conditions as the genetically engineered host cell.
4. The genetically engineered host cell of claim 1 or 2, wherein the fatty acid derivative composition is produced at a titer of at least 100 mg/L.
5. The genetically engineered host cell of claim 1 or 2, wherein the fatty acid derivative composition is produced at a titer of from 30 g/L to 250 g/L.
6. The genetically engineered host cell of claim 1 or 2, wherein the fatty acid derivative composition is produced at a yield that is at least 3 times greater, at least 5 times greater, at least 8 times greater, or at least 10 times greater than the yield of a fatty acid derivative composition produced by a corresponding wild type host cell cultured under the same conditions as the genetically engineered host cell.
7. The genetically engineered host cell of claim 1 or 2, wherein the fatty acid derivative composition has a yield of from 10% to 40%.
8. The genetically engineered host cell of claim 1 or 2, wherein the fatty acid derivative composition is produced at a productivity that is at least 3 times greater, at least 5 times greater, at least 8 times greater, or at least 10 times greater than the productivity of a fatty acid derivative composition produced by a corresponding wild type host cell cultured under the same conditions as the genetically engineered host cell.
9. The genetically engineered host cell of claim 1 or 2, wherein the fatty acid derivative composition is produced at a productivity of from 0.7 mg/L/hr to 3 g/L/hr.
10. The genetically engineered host cell of claim 1 or 2, wherein the acetyl-CoA carboxylase (EC 6.4.1.2) polypeptide is overexpressed.
11. The genetically engineered host cell of claim 10, wherein the acetyl-CoA carboxylase (EC 6.4.1.2) polypeptide is accD+.
12. The genetically engineered host cell of any one of claims 1 to 11, wherein the FadR polypeptide is overexpressed.
13. The genetically engineered host cell of any one of claims 1 to 12, wherein the heterologous iFAB polypeptide is overexpressed.
14. The genetically engineered host cell of claim 13, wherein the heterologous iFAB polypeptide is iFAB 138.
15. The genetically engineered host cell of any one of claims 1 to 14, wherein the host cell comprises a transposon insertion in the yijP gene.
16. The genetically engineered host cell of any one of claims 1 to 15, wherein the host cell comprises a heterologous acp sequence.
17. The genetically engineered host cell of claim 16, further comprising an sfp gene.
18. The genetically engineered host cell of any one of claims 1 to 17, wherein the polynucleotide sequence encoding a fatty acid derivative biosynthetic polypeptide is selected from the group consisting of a polypeptide:
- (a) having thioesterase activity, wherein the recombinant host cell synthesizes fatty acids;
- (b) having thioesterase activity and carboxylic acid reductase (“CAR”) activity, wherein the recombinant host cell synthesizes fatty aldehydes and fatty alcohols;
- (c) having thioesterase activity, carboxylic acid reductase activity and alcohol dehydrogenase activity wherein the recombinant host cell synthesizes fatty alcohols;
- (d) having acyl-CoA reductase (“AAR”) activity wherein the recombinant host cell synthesizes fatty aldehydes and fatty alcohols;
- (e) having acyl-CoA reductase (“AAR”) activity and alcohol dehydrogenase activity wherein the recombinant host cell synthesizes fatty alcohols;
- (f) having fatty alcohol forming acyl-CoA reductase (“FAR”) activity, wherein the recombinant host cell synthesizes fatty alcohols;
- (g) having thioesterase activity, carboxylic acid reductase activity and aldehyde decarbonylase activity, wherein the recombinant host cell synthesizes alkanes;
- (h) having acyl-CoA reductase (“AAR”) activity and aldehyde decarbonylase activity, wherein the recombinant host cell synthesizes alkanes;
- (i) having ester synthase activity wherein the recombinant host cell synthesizes fatty esters;
- (j) having thioesterase activity, acyl-CoA synthase activity and ester synthase activity wherein the recombinant host cell synthesizes fatty esters;
- (k) having OleA activity, wherein the recombinant host cell synthesizes aliphatic ketones;
- (l) having OleABCD activity, wherein the recombinant host cell synthesizes internal olefins; and
- (m) having thioesterase activity and decarboxylase activity, wherein the recombinant host cell synthesizes terminal olefins.
19. The genetically engineered host cell of any one of claims 1 to 16, wherein the fatty acid derivative composition is produced extracellularly.
20. A cell culture comprising the genetically engineered host cell of any one of claims 1 to 19.
21. The cell culture of claim 20, wherein the culture medium comprises a fatty acid derivative composition.
22. The cell culture of claim 20, wherein the fatty acid derivative composition comprises at least one fatty acid derivative selected from the group consisting of a fatty acid, a fatty aldehyde, a fatty alcohol, a fatty ester, an alkane, a terminal olefin, an internal olefin and a ketone.
23. The cell culture of claim 20, wherein the fatty acid derivative is a C6, C8, C10, C12, C13, C14, C15, C16, C17, or C18 fatty acid derivative.
24. The cell culture of claim 20, wherein the fatty acid derivative is a C10:1, C12:1, C14:1, C16:1, or C18:1 unsaturated fatty acid derivative.
25. The cell culture of claim 20, wherein the fatty acid derivative composition comprises one or more of C8, C10, C12, C14, C16, and C18 fatty acid derivatives.
26. The cell culture of claim 22, wherein the fatty acid derivative composition comprises fatty acids.
27. The cell culture of claim 22, wherein the fatty acid derivative composition comprises fatty aldehydes.
28. The cell culture of claim 22, wherein the fatty acid derivative composition comprises fatty alcohols.
29. The cell culture of claim 22, wherein the fatty acid derivative composition comprises fatty esters.
30. The cell culture of claim 22, wherein the fatty acid derivative composition comprises an alkane.
31. The cell culture of claim 22, wherein the fatty acid derivative composition comprises a terminal olefin.
32. The cell culture of claim 22, wherein the fatty acid derivative composition comprises an internal olefin.
33. The cell culture of claim 22, wherein the fatty acid derivative composition comprises a ketone.
34. The cell culture of claim 20, wherein the fatty acid derivative composition comprises a fatty acid derivative having a double bond at position 7 in the carbon chain (between C7 and C8) from the reduced end of the fatty alcohol.
35. The cell culture of claim 20, wherein the fatty acid derivative composition comprises unsaturated fatty acid derivatives.
36. The cell culture of claim 20, wherein the fatty acid derivative composition comprises saturated fatty acid derivatives.
37. The cell culture of claim 20, wherein the fatty acid derivative composition comprises branched chain fatty acid derivatives.
38. The cell culture of claim 20, wherein the fatty acid derivative has a fraction of modern carbon of about 1.003 to about 1.5.
39. The cell culture of claim 20, wherein the fatty acid derivative has a δ13C of from about −10.9 to about −15.4.
40. A cultured recombinant host cell, engineered to increase the production of malonyl CoA, comprising:
- a polynucleotide sequence encoding one or more of: (i) an acetyl-CoA carboxylase (EC 6.4.1.2) polypeptide, (ii) a FadR polypeptide, (iii) a heterologous iFAB polypeptide, or (iv) a sequence having a transposon insertion in the yijP gene, wherein the engineered host cells produces a fatty acid derivative composition at a higher titer, yield or productivity when cultured in medium containing a carbon source under conditions effective to overexpress the polynucleotide(s) relative to a corresponding wild type host cell propagated under the same conditions as the genetically engineered host cell.
41. The cultured recombinant host cell of claim 40, wherein the host cell further comprises a polynucleotide sequence encoding a fatty acid derivative biosynthetic polypeptide.
42. The cultured recombinant host cell of claim 40, wherein the fatty acid derivative composition produced by the cultured genetically engineered host cell has a titer that is at least 3 times greater, at least 5 times greater, at least 8 times greater, or at least 10 times greater than the titer of a fatty acid derivative composition produced by a corresponding wild type host cell cultured under the same conditions as the genetically engineered host cell.
43. The cultured recombinant host cell of claim 40, wherein the host cell has a titer of at least 100 mg/L.
44. The cultured recombinant host cell of claim 40, wherein the fatty acid derivative composition produced by the cultured genetically engineered host cell has a titer of from 30 g/L to 250 g/L.
45. The cultured recombinant host cell of claim 40, wherein the fatty acid derivative composition produced by a cultured genetically engineered host cell has a yield that is at least 3 times greater, at least 5 times greater, at least 8 times greater, or at least 10 times greater than the yield of a fatty acid derivative composition produced by a corresponding wild type host cell cultured under the same conditions as the genetically engineered host cell.
46. The cultured recombinant host cell of claim 40, wherein the fatty acid derivative composition produced by the cultured genetically engineered host cell has a yield of from 10% to 40%.
47. The cultured recombinant host cell of claim 40, wherein the fatty acid derivative composition produced by a cultured genetically engineered host cell has a productivity that is at least 3 times greater, at least 5 times greater, at least 8 times greater, or at least 10 times greater than the productivity of a fatty acid derivative composition produced by a corresponding wild type host cell cultured under the same conditions as the genetically engineered host cell.
48. The cultured recombinant host cell of claim 40, wherein the fatty acid derivative composition produced by a cultured genetically engineered host cell has a productivity of from 0.7 mg/L/hr to 3 g/L/hr.
49. The cultured recombinant host cell of any one of claims 40 to 49, wherein the acetyl-CoA carboxylase (EC 6.4.1.2) polypeptide is overexpressed.
50. The cultured recombinant host cell of claim 49, wherein the acetyl-CoA carboxylase (EC 6.4.1.2) polypeptide is accD+.
51. The cultured recombinant host cell of any one of claims 40 to 50, wherein the FadR polypeptide is overexpressed.
52. The cultured recombinant host cell of any one of claims 40 to 51, wherein the heterologous iFAB polypeptide is overexpressed.
53. The cultured recombinant host cell of claim 52 wherein the heterologous iFAB polypeptide is iFAB 138.
54. The cultured recombinant host cell of any one of claims 40 to 53, wherein the host cell comprises a transposon insertion in the yijP gene.
55. A cell culture comprising the cultured recombinant host cell of any one of claims 40 to 54
56. A method of making a fatty acid derivative composition, comprising the steps of:
- (a) engineering a parental host cell to obtain a recombinant host cell which comprises an acetyl-CoA carboxylase (EC 6.4.1.2) polypeptide, (ii) a FadR polypeptide, (iii) a heterologous iFAB polypeptide, and (iv) a sequence having a transposon insertion in the yijP gene;
- (b) further engineering the cell to comprise polynucleotide sequence encoding a fatty acid derivative biosynthetic polypeptide;
- (c) culturing the recombinant host cell in the presence of a carbon source under conditions effective to result in a yield, titer or productivity of the fatty acid derivative composition that is at least 3 times the yield, titer or productivity of fatty acid derivative composition produced by the parental microbial cell cultured under the same conditions; and
- (d) optionally isolating the fatty acid derivative composition.
57. The method of claim 56, wherein the host cell is further engineered to comprise a polynucleotide sequence encoding a heterologous acp protein.
58. The method of claim 57, wherein the host cell is further engineered to comprise an sfp gene.
59. The method of claim 56, wherein the fatty acid derivative biosynthetic polypeptide is selected from the group consisting of a polypeptide:
- (a) having thioesterase activity, wherein the recombinant host cell synthesizes fatty acids;
- (b) having thioesterase activity and carboxylic acid reductase (“CAR”) activity, wherein the recombinant host cell synthesizes fatty aldehydes and fatty alcohols;
- (c) having thioesterase activity, carboxylic acid reductase activity and alcohol dehydrogenase activity wherein the recombinant host cell synthesizes fatty alcohols;
- (d) having acyl-CoA reductase (“AAR”) activity wherein the recombinant host cell synthesizes fatty aldehydes and fatty alcohols;
- (e) having acyl-CoA reductase (“AAR”) activity and alcohol dehydrogenase activity wherein the recombinant host cell synthesizes fatty alcohols;
- (f) having fatty alcohol forming acyl-CoA reductase (“FAR”) activity, wherein the recombinant host cell synthesizes fatty alcohols;
- (g) having thioesterase activity, carboxylic acid reductase activity and aldehyde decarbonylase activity, wherein the recombinant host cell synthesizes alkanes;
- (h) having acyl-CoA reductase (“AAR”) activity and aldehyde decarbonylase activity, wherein the recombinant host cell synthesizes alkanes;
- (i) having ester synthase activity wherein the recombinant host cell synthesizes fatty esters;
- (j) having thioesterase activity, acyl-CoA synthase activity and ester synthase activity wherein the recombinant host cell synthesizes fatty esters;
- (k) having OleA activity, wherein the recombinant host cell synthesizes aliphatic ketones;
- (l) having OleABCD activity, wherein the recombinant host cell synthesizes internal olefins; and
- (m) having thioesterase activity and decarboxylase activity, wherein the recombinant host cell synthesizes terminal olefins.
60. The method of claim 56, where in the fatty acid derivative is selected from the group consisting of a fatty acid, a fatty alcohol, a fatty aldehyde, a fatty acid ester, a hydrocarbon, a ketone, and an olefin.
61. The method of claim 56, where in the fatty acid derivative is a C6, C8, C10, C12, C13, C14, C15, C16, C17, or C18 fatty acid derivative.
62. The method of claim 56, where in the fatty acid derivative is a C10:1, C12:1, C14:1, C16:1, or C18:1 unsaturated fatty acid derivative.
63. A method of making a fatty acid derivative composition with a higher titer, yield or productivity of fatty acid derivatives than produced by a parental host cell, the method comprising:
- (a) engineering a parental host cell to obtain a recombinant host cell which comprises one or more of: (i) a polynucleotide encoding an acetyl-CoA carboxylase (EC 6.4.1.2) polypeptide, (ii) a polynucleotide encoding a FadR polypeptide, (iii) a polynucleotide encoding a heterologous iFAB polypeptide, (iv) a sequence having a transposon insertion in the yijP gene, and (v) a polynucleotide encoding a heterologous ACP protein;
- (b) further engineering the cell to comprise a polynucleotide sequence encoding a fatty acid derivative biosynthetic polypeptide;
- (c) culturing the recombinant host cell in the presence of a carbon source under conditions effective to result in a yield, titer or productivity of fatty acid derivatives that is at least 3 times the yield, titer or productivity of fatty acid derivatives produced by the parental microbial cell cultured under the same conditions; and
- (d) optionally isolating the fatty acid derivative composition.
Type: Application
Filed: Apr 2, 2013
Publication Date: Mar 5, 2015
Applicant: REG LIFE SCIENCES, LLC (South San Francisco, CA)
Inventors: Derek L. Greenfield (South San Francisco, CA), Andreas W. Schirmer (South San Francisco, CA), Elizabeth J. Clarke (South San Francisco, CA), Eli S. Groban (South San Francisco, CA), Bernardo M. Da Costa (South San Francisco, CA), Zhihao Hu (South San Francisco, CA)
Application Number: 14/390,378
International Classification: C12N 15/70 (20060101); C12P 7/64 (20060101);
