USPatent applicationPatented

Method for producing medium chain diol

Granted 17 Aug 2021 · 2 office actions

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Abstract

The present invention relates to a method for producing medium chain diol and, more particularly to recombinant microorganisms in which fatty alcohol dehydrogenase and/or fatty alcohol oxidase genes on a ω-oxidative metabolism pathway are deleted, the fatty aldehyde dehydrogenase genes are optionally deleted, and β-oxidative metabolism pathway-related genes are deleted, and to a method for producing medium chain diol from fatty acid-derived alcohol or alkane by culturing the recombinant microorganisms. The recombinant microorganisms of the present invention can produce a high yield of medium chain diol by preventing further oxidation and β-oxidative metabolism of fatty alcohols.

Description

12 parts
›This application is a National Stage Application of…

This application is a National Stage Application of PCT/KR2016/012170, filed 27 Oct. 2016, which claims benefit of Serial No. 10-2016-0141017, filed 27 Oct. 2016 in Korea and Serial No. 10-2015-0149251, filed 27 Oct. 2015 in Korea and which applications are incorporated herein by reference. To the extent appropriate, a claim of priority is made to each of the above disclosed applications.

›TECHNICAL FIELD

The present invention relates to a method for producing a medium chain diol, and more particularly, to a method for producing a medium chain diol from a fatty acid-derived alcohol or alkane by culturing a recombinant microorganism from which fatty alcohol dehydrogenase and/or fatty alcohol oxidase genes in an ω-oxidative metabolism pathway are deleted, a fatty aldehyde dehydrogenase gene is optionally deleted, and β-oxidative metabolism pathway-related genes are also deleted.

›BACKGROUND ART

Bioplatform compounds are produced through biological or chemical conversion on the basis of biomass-derived raw materials, and have been used for synthesis of polymeric monomers, new materials, and the like.

Among the bioplatform compounds, a medium chain diol is a material used as a monomer for polyesters. In this case, the polyesters have been used for various applications including fibers, films, and combinations thereof due to their excellent properties. For example, the polyethylene terephthalate obtained through the polycondensation of terephthalic acid with ethylene glycol has been used for many applications due to excellent physical properties such as mechanical strength, chemical properties, and the like, and has been mass-produced as a synthetic fiber most suitable for clothing all over the world. Also, the market for polytrimethylene terephthalate prepared using 1,3-propanediol and terephthalic acid as raw materials tends to increase with the recent development of inexpensive methods of synthesizing 1,3-propanediol. Thus, the polytrimethylene terephthalate is expected to be employed for clothing applications requiring the soft texture because it has polymeric characteristics such as excellent elastic recovery percentage of elongation and low Young's modulus. In addition, the biomass resource-derived polyesters have come into the spotlight for fear of the rising price and depletion of petroleum resources.

Production of medium chain diols may be carried out using biological methods through chemical synthesis or microbial fermentation. In this case, the use of such biological methods requires the development of novel strains and the optimization of fermentation processes using metabolic engineering technology.

In the prior art, a microorganism which harbors a β-oxidative metabolism pathway as well as an ω-oxidative metabolism pathway may be used as the strain capable of producing a medium chain diol. For example, it is known that the strains such as Klebsiella oxytoca, Klebsiella pneumoniae, Aerobacter aerogenes , recombinant Saccharomyces cerevisiae , and the like may produce 2,3-butanediol with high yield and high productivity (Korean Patent Publication Nos. 10-2012-0107021, 10-2012-0128776, and 10-2015-0068581). However, because some of these microorganisms are classified into pathogenic microorganisms, they have limitations in terms of safety and industrialization. Also, because the medium chain diols correspond to intermediate products in the ω-oxidative metabolism pathway, the medium chain diols have a problem in that the medium chain diols may not be produced with high yield when they are produced using the microorganisms.

›DISCLOSURE

Technical Problem

Therefore, it is an object of the present invention to provide a recombinant microorganism from which fatty alcohol dehydrogenase and/or fatty alcohol oxidase-related genes in an ω-oxidative metabolism pathway are deleted, a fatty aldehyde dehydrogenase gene is optionally deleted, and β-oxidative metabolism pathway-related genes are also deleted, and a method of producing a medium chain diol from a fatty acid-derived alcohol or alkane by culturing the recombinant microorganism.

Technical Solution

To solve the above problems, according to an aspect of the present invention, there is provided a recombinant microorganism from which one or more genes selected from the group consisting of fatty alcohol dehydrogenase and fatty alcohol oxidase genes in an ω-oxidative metabolism pathway are deleted, a fatty aldehyde dehydrogenase gene is optionally deleted, and β-oxidative metabolism pathway-related genes are also deleted.

According to an embodiment of the present invention, the fatty alcohol dehydrogenase gene, the fatty alcohol oxidase gene, the fatty aldehyde dehydrogenase gene, and the β-oxidative metabolism pathway-related genes may be deleted from all homologous genes present in the microorganism, but the present invention is not limited thereto. According to another embodiment of the present invention, the fatty alcohol dehydrogenase gene, the fatty alcohol oxidase gene, the fatty aldehyde dehydrogenase gene, and the β-oxidative metabolism pathway-related genes may be deleted from some of the homologous genes present in the corresponding microorganism, but the present invention is not limited thereto.

According to an embodiment of the present invention, the fatty alcohol dehydrogenase gene may be selected from the group consisting of ADH1, ADH2, ADH3, ADH4, ADH5, ADH6, ADH7, ADH8, and FADH genes, but the present invention is not limited thereto. According to another embodiment of the present invention, the fatty alcohol oxidase gene may be an FAO gene, but the present invention is not limited thereto. According to still another embodiment of the present invention, the fatty aldehyde dehydrogenase gene may be a gene selected from the group consisting of FALDH1, FALDH2, FALDH3, and FALDH4 genes, but the present invention is not limited thereto.

According to an embodiment of the present invention, the β-oxidative metabolism pathway-related genes may be an acyl-CoA oxidase gene, but the present invention is not limited thereto. According to preferred embodiments of the present invention, the acyl-CoA oxidase gene may be selected from the group consisting of ACO1, ACO2, ACO3, ACO4, ACO5, and ACO6 genes, but the present invention is not limited thereto.

According to an embodiment of the present invention, the microorganism may be a yeast or Escherichia coli , but the present invention is not limited thereto. According to preferred embodiments of the present invention, the yeast may be selected from the group of the yeast consisting of Yarrowia sp., Saccharomyces sp., Pichia sp., and Candida sp., but the present invention is not limited thereto. According to other preferred embodiments of the present invention, the Yarrowia sp. yeast may be Yarrowia lipolytica , but the present invention is not limited thereto.

According to another aspect of the present invention, there is provided a method for producing a medium chain diol, which comprises (1) preparing a recombinant microorganism from which one or more genes selected from the group consisting of fatty alcohol dehydrogenase and fatty alcohol oxidase genes in an ω-oxidative metabolism pathway are deleted, a fatty aldehyde dehydrogenase gene is optionally deleted, and β-oxidative metabolism pathway-related genes are also deleted; and (2) treating the recombinant microorganism with a substrate to culture the recombinant microorganism.

According to an embodiment of the present invention, the substrate may be selected from the group consisting of a fatty acid-derived alcohol and alkane, but the present invention is not limited thereto. According to preferred embodiments of the present invention, each of the fatty acid-derived alcohol and alkane and the medium chain diol may have 5 to 30 carbon atoms, preferably 6 to 20 carbon atoms, and more preferably 8 to 16 carbon atoms, but the present invention is not limited thereto. According to other preferred embodiments of the present invention, the alkane may be dodecane, but the present invention is not limited thereto. According to still other preferred embodiments of the present invention, the medium chain diol may be 1,12-dodecanediol, but the present invention is not limited thereto.

Advantageous Effects

Because fatty alcohol dehydrogenase and/or fatty alcohol oxidase genes in an ω-oxidative metabolism pathway are deleted, a fatty aldehyde dehydrogenase gene is optionally deleted, and β-oxidative metabolism pathway-related genes are also deleted from a recombinant microorganism according to the present invention, the recombinant microorganism can produce medium chain diols with high yield by preventing further oxidation and β-oxidative metabolism of fatty alcohols.

›DESCRIPTION OF DRAWINGS

FIG. 1 is a diagram showing types of products and related enzymes associated with ω-oxidative and β-oxidative metabolism reactions.

FIG. 2 is a diagram schematically showing a process of preparing a recombinant microorganism of the present invention from which fatty alcohol dehydrogenase, fatty alcohol oxidase and fatty aldehyde dehydrogenase genes associated with ω-oxidation and an acyl-CoA oxidase gene associated with β-oxidation are deleted.

FIG. 3 is a diagram schematically showing a vector containing an ura3 gene to be used as a selective marker for gene knockout to modify a strain, and a pop-out region for deleting the ura3 gene after insertion of a knock-out cassette.

FIG. 4 is a schematic diagram showing a process of constructing a knock-out cassette used to prepare a transformant microorganism according to the present invention.

FIG. 5 is a graph illustrating types of knock-out genes in the transformant microorganism according to the present invention.

FIG. 6 is a graph illustrating an amount of a medium chain diol produced from the alkane substrate, using the transformant microorganism according to the present invention.

FIG. 7 is a graph illustrating an amount of the medium chain diol produced from the alkane substrate, when an Y4-20 strain of the present invention is cultured in a flask.

FIG. 8 shows the GC/MS data showing that the medium chain diol is produced the alkane substrate in the Y4-20 strain according to the present invention.

›BEST MODE · 1 of 2

The present invention provides a recombinant microorganism from which one or more genes selected from the group consisting of fatty alcohol dehydrogenase and fatty alcohol oxidase genes in an ω-oxidative metabolism pathway are deleted, a fatty aldehyde dehydrogenase gene is optionally deleted, and β-oxidative metabolism pathway-related genes are also deleted.

In the present invention, the term “ω-oxidation” refers to a metabolic process in which the terminal methyl group of a fatty acid is oxidized to form dicarboxylic acid, and the term “β-oxidation” refers to a metabolic process in which a carbon atom at the β-position in a carboxyl group is oxidized to release acetyl-CoA, whereby fatty acids are gradually decomposed to form fatty acids whose number of carbon atoms is reduced by two. The concept of the ω- and β-oxidations and the enzymes involved in such metabolic processes are widely known to persons having ordinary skill in the field of biochemistry. For example, when a fatty acid is used as the substrate for ω-oxidation, an ω-hydroxy fatty acid is first produced by means of an action of cytochrome P450 and an NADPH-cytochrome P450 reductase. Then, the ω-hydroxy fatty acid is converted into ω-aldehyde fatty acid by an action of a fatty alcohol dehydrogenase and a fatty alcohol oxidase, and the ω-aldehyde fatty acid is converted into dicarboxylic acid by an action of a fatty aldehyde dehydrogenase. Also, for the β-oxidation, a fatty acid whose number of carbon atoms is reduced by two is produced by an acyl-CoA oxidase (see FIG. 1 ).

According to an embodiment of the present invention, the fatty alcohol dehydrogenase and fatty alcohol oxidase genes and the fatty aldehyde dehydrogenase gene that may be optionally deleted are preferably deleted from all homologous genes present in the corresponding microorganism, but a recombinant microorganism from which some of these genes are deleted may also be applied to the present invention, when necessary.

According to an embodiment of the present invention, the fatty alcohol dehydrogenase gene may be selected from the group consisting of ADH1, ADH2, ADH3, ADH4, ADH5, ADH6, ADH7, ADH8, and FADH genes, but the present invention is not limited thereto. According to preferred embodiments of the present invention, the ADH1, ADH2, ADH3, ADH4, ADH5, ADH6, ADH7, ADH8, and FADH genes may comprise base sequences set forth in SEQ ID NOs: 1 to 9, respectively, but the present invention is not limited thereto.

According to another embodiment of the present invention, the fatty alcohol oxidase gene may be an FAO gene, but the present invention is not limited thereto. According to preferred embodiments of the present invention, the FAO gene may comprise a base sequence set forth in SEQ ID NO: 10, but the present invention is not limited thereto.

According to still another embodiment of the present invention, the fatty aldehyde dehydrogenase gene may be selected from the group consisting of FALDH1, FALDH2, FALDH3, and FALDH4 genes, but the present invention is not limited thereto. The FALDH1, FALDH2, FALDH3, and FALDH4 genes may comprise base sequences set forth in SEQ ID NOs: 11 to 14, respectively, but the present invention is not limited thereto.

According to an embodiment of the present invention, the β-oxidative metabolism pathway-related genes are preferably deleted from all homologous genes present in the corresponding microorganism, but a recombinant microorganism from which some of these genes are deleted may also be applied to the present invention, when necessary. The β-oxidative metabolism pathway-related genes preferably includes an acyl-CoA oxidase gene, and the acyl-CoA oxidase gene may be selected from the group consisting of ACO1, ACO2, ACO3, ACO4, ACO5, and ACO6 genes, but the present invention is not limited thereto (see FIG. 2 ). According to other preferred embodiments of the present invention, the ACO1, ACO2, ACO3, ACO4, ACO5, and ACO6 genes may comprise base sequences set forth in SEQ ID NOs: 15 to 20, respectively, but the present invention is not limited thereto.

In the present invention, the recombinant microorganism from which the genes selected from the fatty alcohol dehydrogenase gene, the fatty alcohol oxidase gene, the fatty aldehyde dehydrogenase gene, and the acyl-CoA oxidase gene are deleted may be prepared using conventional genetic recombinant technology known in the related art. In the present invention, the term “deletion” is used as a meaning generally encompassing a physical deletion of part or all of the corresponding gene, and also encompassing a situation in which a protein is not expressed from mRNA transcribed from the corresponding gene and a situation in which a protein expressed from the corresponding gene does not function. Examples of the genetic recombinant technology that may be used herein may include methods such as transformation, transduction, transfection, microinjection, electroporation, and the like, but the present invention is not limited thereto.

In the present invention, any microorganisms having both ω-oxidative and β-oxidative metabolism processes may be used without limitation. For example, eukaryotes including a yeast and prokaryotes including Escherichia coli may be used. According to an embodiment of the present invention, the yeast is preferably used as the microorganism. In this case, yeasts such as Yarrowia sp., Saccharomyces sp., Pichia sp., Candida sp., and the like may be used as the yeast without limitation. Among theses, Yarrowia hpolytica, Candida tropicalis, Candida infanticola, Saccharomyces cerevisiae, Pichia alcoholophia , or Candida mycoderma is preferably used. Yarrowia lipolytica is more preferably used.

As described above, in the case of the microorganism from which the fatty alcohol dehydrogenase and fatty alcohol oxidase genes and the β-oxidative metabolism pathway-related genes are deleted and the fatty aldehyde dehydrogenase gene is optionally deleted, when the alkane is supplied as the substrate, one of both terminals of the alkane is oxidized by an action of cytochrome P450 and an NADPH-cytochrome P450 reductase to form a primary alcohol. However, because the fatty alcohol dehydrogenase gene and the fatty alcohol oxidase gene are deleted, no further oxidation occurs anymore. Also, the primary alcohol thus formed is again used as a substrate so that the other terminal of the primary alcohol is oxidized by an action of the cytochrome P450 and the NADPH-cytochrome P450 reductase to form a diol as a secondary alcohol. When the alkane is used as the substrate as described above, the diol is formed through a two-step oxidation reaction, whereas the diol is formed through a one-step oxidation reaction when the alcohol other than the alkane is used as the substrate.

›BEST MODE · 2 of 2

Also, the present invention provides a method for producing a medium chain diol, which comprises:

(1) preparing a recombinant microorganism from which one or more genes selected from the group consisting of fatty alcohol dehydrogenase and fatty alcohol oxidase genes in an ω-oxidative metabolism pathway are deleted, a fatty aldehyde dehydrogenase gene is optionally deleted, and β-oxidative metabolism pathway-related genes are also deleted; and

(2) treating the recombinant microorganism with a substrate to culture the recombinant microorganism.

In the present invention, the recombinant microorganism, from which the fatty alcohol dehydrogenase and/or fatty alcohol oxidase genes in the ω-oxidative metabolism pathway are deleted, the fatty aldehyde dehydrogenase gene is optionally deleted, and the β-oxidative metabolism pathway-related genes are also deleted, may be used to produce medium chain diols with high yield by preventing additional oxidation and β-oxidative metabolism of fatty alcohols. The fatty alcohol dehydrogenase gene, the fatty alcohol oxidase gene, the fatty aldehyde dehydrogenase gene, and the β-oxidative metabolism pathway-related genes are preferably deleted from all homologous genes present in the corresponding microorganism, but a recombinant microorganism from which some of these genes are deleted may also be applied to the present invention, when necessary.

In the present invention, any microorganisms having both ω-oxidative and β-oxidative metabolism processes may be used without limitation. For example, eukaryotes including a yeast and prokaryotes including Escherichia coli may be used. According to an embodiment of the present invention, the yeast is preferably used as the microorganism. In this case, yeasts such as Yarrowia sp., Saccharomyces sp., Pichia sp., Candida sp., and the like may be used as the yeast without limitation. Among theses, Yarrowia lipolytica, Saccharomyces cerevisiae, Candida tropicalis, Candida infanticola, Pichia alcoholophia , or Candida mycoderma is preferably used. Yarrowia lipolytica is more preferably used.

In the present invention, the recombinant microorganism from which the genes selected from the fatty alcohol dehydrogenase gene, the fatty alcohol oxidase gene, the fatty aldehyde dehydrogenase gene, and the acyl-CoA oxidase gene are deleted may be prepared using conventional genetic recombinant technology known in the related art. In the present invention, the term “deletion” is used as a meaning generally encompassing a physical deletion of part or all of the corresponding gene, and also encompassing a situation in which a protein is not expressed from mRNA transcribed from the corresponding gene and a situation in which a protein expressed from the corresponding gene does not function.

In the present invention, the term “diol” generally refers to a compound that contains two hydroxyl groups (—OH groups), and the term “medium chain diol” is used as a meaning encompassing all diol compounds having 5 to 30 carbon atoms, preferably 6 to 20 carbon atoms, and more preferably 8 to 16 carbon atoms.

In the present invention, the substrate of step (2) may be selected from the group consisting of a fatty acid-derived alcohol and alkane, but the present invention is not limited thereto. According to an embodiment of the present invention, alcohols having 5 to 30 carbon atoms, preferably 6 to 20 carbon atoms, and more preferably 8 to 16 carbon atoms may be used as the fatty acid-derived alcohol, but the present invention is not limited thereto. According to another embodiment of the present invention, alkanes having 5 to 30 carbon atoms, preferably 6 to 20 carbon atoms, and more preferably 8 to 16 carbon atoms may be used as the alkane, but the present invention is not limited thereto. According to preferred embodiments of the present invention, the alkane may be dodecane, but the present invention is not limited thereto. According to other preferred embodiments of the present invention, the medium chain diol may be 1,12-dodecanediol, but the present invention is not limited thereto.

›MODE FOR INVENTION

Hereinafter, the present invention will be described in further detail with reference to examples thereof.

However, it should be understood that the following examples are just preferred examples for the purpose of illustration only and is not intended to limit or define the scope of the invention.

›Examples4
›Example 1: Construction of Knock-Out Cassette

A vector containing an ura3 gene to be used as a selective marker for gene knockout to modify a strain, and a pop-out region for deleting the ura3 gene after insertion of a knock-out cassette was constructed ( FIG. 3 ). A Yarrowia -derived gene was used as the ura3 gene, and the pop-out region used to modify a strain had a total of four sequences, and was referenced from two genes. Here, a Bacillus -derived glutamate-producing gene was used as one of the genes, and a gene associated with a Salmonella - or cloning vector pHUKH-derived His operon was used as the other one. The primers used to construct the pop-out vectors, and sequences thereof are listed in the following Table 1.

A knock-out cassette was constructed as shown in FIG. 4 . First, PCR of a homologous region (HR) to be knocked out from the genomic DNA of Yarrowia sp., and PCR of two 5′- and 3′-terminal fragments from a pop-out vector were carried out. Thereafter, each of the 5′ HR and 3′ HR was subjected to alignment PCR (2 nd PCR) with a PO-ura3 region to construct a knock-out cassette. The primers used to amplify the respective homologous regions, and sequences thereof are listed in Table 2.

The primers used to PCR-amplify the pop-out region and ura3 as two fragments are listed in Table 3.

The gene sequences used to modify the recombinant microorganism strain according to the present invention are listed in the sequence listing, and summarized in Table 4.

›Example 2: Construction of Knock-Out Strain

The knock-out cassette constructed in Example 1 was used to prepare a total of six knock-out strains from which some or all of fatty alcohol dehydrogenase, fatty alcohol oxidase and fatty aldehyde dehydrogenase genes and β-oxidative metabolism pathway-related genes present in a wild-type Yarrowia strain were deleted ( FIG. 5 ). Specifically, a strain to be knocked out was plated on an YPD plate, and cultured at 30° C. for 16 to 24 hours. The cultured cells were scraped with a loop, put into 100 μL of a one-step buffer (45% PEG4000, 100 mM DTT, 0.1 L LiAc, 25 μg of single-strand carrier DNA), and vortexed. Thereafter, the knock-out cassette (1 ng or more) was added thereto, and the resulting mixture was vortexed again, and cultured at 39° C. for an hour. The cultured sample was loaded onto a selective medium (6.7 g/L of YNB without amino acids, and 20 g/L of glucose), and then cultured at 30° C. for 48 hours to screen a strain into which the constructed cassette was inserted. To check whether the cassettes were correctly inserted onto the genome of the screened strain, PCR was then performed using the primers included in the gene deletions listed in Table 2.

To insert another cassette, a pop-out process was performed on the strain into which the cassette was inserted. The strain screened from a selective medium was inoculated in 2 mL of an YPD medium, and cultured at 30° C. for 16 hours, and 200 μL of the culture broth was spread on a 5′ FOA medium (6.7 g/L of YNB without amino acids, 20 g/L of glucose, 0.8 g/L of 5′ FOA, 0.1 g/L of uracil, and 0.1 g/L of uridine), and then cultured at 30° C. for 48 hours. The strains grown on the 5′ FOA medium were picked, and plated on an YPD plate and a UD plate. Then, the strains grown on the YPD plate were screened, and a PCR process was again performed using the primers listed in Table 2 to check whether the ura3 gene was deleted from the strains. A knock-out process was performed on other genes of the Ura3-deleted strains.

The aforementioned processes were repeatedly performed to prepare the recombinant microorganism strain of the present invention (Chen D C, Beckerich J M, Gaillardin C (1997) Appl Microbiol Biotechnol 48: 232-235).

›Example 3: Culturing of Knock-Out Strain

A day earlier, the strain to be cultured and tested was inoculated in 2 mL of an YPD medium (Bacto Laboratories, 10 g/L of Yeast extract, 20 g/L of peptone, and 20 g/L of glucose), and grown at 30° C. and 200 rpm for a day. 2 mL of a growth medium (pH 6.0) having the compositions listed in Table 5 was put into a 24-well plate, and a pre-cultured culture broth was inoculated at 1%. Thereafter, the strains were cultured at 30° C. and 450 rpm for a day in a plate stirrer. The strains cultured for a day were inoculated at a volume of 900 μL in a new plate containing 900 μL of a conversion medium (pH 7.6) listed in Table 6, and 200 μL of a substrate was added thereto at the same time. The resulting mixture was cultured at 30° C. and 450 rpm for a day. In this case, 10 g/L of dodecane dissolved in DMSO was used as the substrate.

As a result, it was revealed that the Y1-28 and Y1-36 strains in which only the β-oxidative metabolism pathway-related genes and the fatty aldehyde dehydrogenase gene were knocked out did not produce 1,12-dodecanediol from dodecane serving as the substrate, but all the Y1-36 strain in which the fatty alcohol oxidase gene was further knocked out, and the Y4-2, Y4-20 and Y4-30 strains in which the fatty alcohol oxidase gene and the fatty alcohol dehydrogenase gene were further knocked out exhibited an excellent ability to synthesize 1,12-dodecanediol ( FIG. 6 ). Also, it was revealed that the Y4-20 strain exhibited an ability to synthesize approximately 18 mg/L of 1,12-dodecanediol when cultured in the flask ( FIG. 7 ). In the following experiment, a sample analysis test was performed using the Y4-20 strain.

›Example 4: Sample Analysis

1 mL of 1 N sodium hydroxide and 10 mL of chloroform were added to 10 mL of a culture broth of the Y4-20 strain which had been proven to have the most excellent ability to synthesize 1,12-dodecanediol in Example 3. Thereafter, the resulting mixture was thoroughly vortexed, extracted, and then centrifuged at 10,000 rpm for 10 minutes. Then, only a chloroform layer was separated, concentrated 10-fold, and then subjected to a GC/MS assay under the following analytical conditions.

Analytical Conditions

{circle around (1)} Equipment: Agilent 5975 MSD® {circle around (2)} Column: HP-5MS {circle around (3)} Temperature: Oven (150° C. to 230° C.) {circle around (4)} Carrier gas: He {circle around (5)} Flow rate: 1 mL/min.

As a result, it was confirmed that the recombinant Y4-20 strain of the present invention was able to synthesize 1,12-dodecanediol from dodecane serving as a substrate ( FIG. 8 ).

›Tables in the description — 6
TABLE 1 — Pop-out Vectors SEQ ID
NamesBase SequencesNOs
HisG1BglII Faattgggcccagatctcagaccggttcagacaggat22
EcoRI Rtctctgggcggaattcggaggtgcggatatgaggta23
NotI FtgTTTCTCGgcggccgccagaccggttcagacaggat24
BamHI RTCCAACGCGTGGATCCggaggtgcggatatgaggta25
HisG2BglII Faattgggcccagatctaacgctacctcgaccagaaa26
EcoRI Rtctctgggcggaattctcttctcgatcggcagtacc27
NotI FtgTTTCTCGgcggccgcaacgctacctcgaccagaaa28
BamHI RTCCAACGCGTGGATCCtcttctcgatcggcagtacc29
glt2BglII FaattgggcccagatctTCAGAACTTGCGCCGATAAA30
EcoRI RtctctgggcggaattcCTTTGCCAGCTAGACCATAGAG31
NotI FtgTTTCTCGgcggccgcTCAGAACTTGCGCCGATAAA32
BamHI RTCCAACGCGTGGATCCCTTTGCCAGCTAGACCATA33
GAG
glt3BglII FaattgggcccagatctATTGGCGGGTTCGTTACTT34
EcoRI RtctctgggcggaattcCCTGGAAGAAGGCCGTATTATC35
NotI FtgTTTCTCGgcggccgcATTGGCGGGTTCGTTACTT36
BamHI RTCCAACGCGTGGATCCCCTGGAAGAAGGCCGTAT37
TATC
TABLE 2 — Gene Deletions SEQ ID
NamesBase SequencesNOs
ACO1F1TTCCTCAATGGTGGAGAAGA38
R1TCTTTATCCTGTCTGAACCGGTCTG39
GTACCATAGTCCTTGCCATGC
F2ATCGCTACCTCATATCCGCACCTCC40
CTTCTGTCCCCCGAGTTTCT
R2AAGAAGGGCTTGAGAGTCG41
ACO2F1CCCAACAACACTGGCAC42
R1TCTTTATCCTGTCTGAACCGGTCTG43
CTCCTCATCGTAGATGGC
F2ATCGCTACCTCATATCCGCACCTCC44
gacaagacccgacaggc
R2AGACCAGAGTCCTCTTCG45
ACO3F1Accttcacagagccaccca46
R1ATGGCTCTCTGGGCGgtgttgggggtgttgatgatg47
F2TTGTTGTGTTTCTCGcaaggttctcatcgaggcctg48
R2Aggaaaggtcgaagagtgctct49
ACO4F1Actgcgagagcgatctg50
R1TCTTTATCCTGTCTGAACCGGTCTG51
TTCATGAGCATGTAGTTTCG
F2ATCGCTACCTCATATCCGCACCTCC52
gaggacgacaaagccggag
R2AGAGCAGAGTCCTCCTCAA53
ACO5F1AACTTCCTCACAGGCAGCGAGC54
R1ATGGCTCTCTGGGCG55
GAGTAGAGAGTGGGAGTTGAGGTC
F2ttgttgtgtttctcg ccccgtcaaggacgctgag56
R2ACAGTAAGGTGGGGCTTGACTC57
ACO6F1AGTCCCTCAACACGTTTACCG58
R1TCTTTATCCTGTCTGAACCGGTCTG59
CCATTTAGTGGCAGCAACGTT
F2ATCGCTACCTCATATCCGCACCTCC60
GAGCTCTGATCAACCGAACC
R2AGGAAGGGTCTAATGACAGA61
FALDH1F1AATCACTCCTCCTACGC62
R1TCTTTATCCTGTCTGAACCGGTCTG63
TGGTCTCGGGGACACCTC
F2ATCGCTACCTCATATCCGCACCTCC64
CCATCATCAAGCCCCGAA
R2ACCGACATAATCTGAGCAAT65
FALDH2F1Accactaggtgagatcgag66
R1TCTTTATCCTGTCTGAACCGGTCTG67
CTCCGACACTACCGGAACGC
F2ATCGCTACCTCATATCCGCACCTCC68
CTTGCTCCCACAGTTGTT
R2GATCACCCAGAACCATAGC69
FALDH3F1GTGACCCCCACCACGTCAC70
R1TCTTTATCCTGTCTGAACCGGTCTG71
TTCTGACATTTTCAGCGCCAC
F2ATCGCTACCTCATATCCGCACCTCC72
CCATTACGAGCGTTTGACGG
R2CAGGGCTGGGGACCACC73
FALDH4F1TACCGACTGGACCAGATTC74
R1TCTTTATCCTGTCTGAACCGGTCTG75
CGGCAGTGGCAATGATCTTAC
F2ATCGCTACCTCATATCCGCACCTCC76
GACTCGATTCATCGCTCCTAC
R2CAAATCTTTCGGAAGATTCGG77
FAO1F1atcattgtcggtggaggaac78
R1ACGCCTTTCTGGTCGAGGTAGCGTTgcgtagtcgt79
aaggctggac
F2attctggtactgccgatcgagaaga80
ccgtcatcggtgagattctt
R2attcgaggtcggagatcctt81
ADH1F1cccagaaggctgtcattttc82
R1ACGCCTTTCTGGTCGAGGTAGCGTTtcgcagttct83
tggggatatg
F2attctggtactgccgatcgagaaga84
gccgacaaggagaagatgtg
R2caatcttgccctcctccat85
ADH2F1ccagaagggtgtcatcttcg86
R1ACGCCTTTCTGGTCGAGGTAGCGTTatcgcagttc87
ttgggaatgt
F2attctggtactgccgatcgagaaga88
ccgacaaggagaagatgtgc
R2caatcttgccctcctccata89
ADH3F1agaaagccgtcatcttcgag90
R1ttgcacaagtaacgaacccgccaat91
tcacagttcttggggatgtg
F2ggagataatacggccttcttccagg92
gctgacaaggagaagatgtgc
R2acttggagcagtccagaacg93
ADH4F1gtcaaaacgtcgacgaacct94
R1AGGTATTTATCGGCGCAAGTTCTGA95
ggcttgaggtcaatgtcgat
F2ctcctctatggtctagctggcaaag96
gacatggaggcccactctaa
R2agtactcccaagcgtcctca97
ADH5F1gagagccgctttcaccac98
R1AGGTATTTATCGGCGCAAGTTCTGA99
agagcctggtaggcagtgag
F2ctcctctatggtctagctggcaaag100
ttccaggacgtgatcaagga
R2taaggatgatcttgccggtag101
ADH6F1gacccagaaagccattgtgt102
R1AGGTATTTATCGGCGCAAGTTCTGA103
agccacctgagaaaggtctg
F2ctcctctatggtctagctggcaaag104
caccgaggagaaggagaaga
R2tccctcctccatcaaggtaa105
ADH7F1gacgttcccaagacacaaaag106
R1AGGTATTTATCGGCGCAAGTTCTGA107
aggcgtactgctggaaagag
F2ctcctctatggtctagctggcaaag108
acccacaccaaggagctg
R2caacgacacgaccaacaatc109
ADH8F1atcgcgccaacttgtttaat110
R1AGGTATTTATCGGCGCAAGTTCTGA111
caccttctctcgtgggatgt
F2ctcctctatggtctagctggcaaag112
tgtgttgagtctggcaaagc
R2tcaagtccatggcatcaaac113
FADHF1ccgaaggaaagaccatcact114
R1ttgcacaagtaacgaacccgccaat115
agaaggaagagcagcccata
F2ggagataatacggccttcttccagg116
gcttgggcttacaagtttgg
R2tcggtgaaggcagagttgat117
TABLE 3 — Pop-out Cassettes SEQ ID
NamesBase SequencesNOs
HISG1Fcagaccggttcagacaggat118
Rggaggtgcggatatgaggta119
HISG2Faacgctacctcgaccagaaa120
Rtcttctcgatcggcagtacc121
glt2FTCAGAACTTGCGCCGATAAA122
RCTTTGCCAGCTAGACCATAGAG123
glt3FATTGGCGGGTTCGTTACTT124
RCCTGGAAGAAGGCCGTATTATC125
BipartiteUlura3 cs 2Batgccctcctacgaagctcgagc126
Ylura3Fctcccaacgagaagctggcc127
TABLE 4
GenesSEQ ID NOs
ADH11
ADH22
ADH33
ADH44
ADH55
ADH66
ADH77
ADH88
FADH9
FAO110
FALDH111
FALDH212
FALDH313
FALDH414
ACO115
ACO216
ACO317
ACO418
ACO519
ACO620
Ura321
TABLE 5 — Growth Medium (pH 6.0)
ComponentsConcentration (g/L)
Glucose50
YNB w/o amino acids6.7
Yeast extract10
(NH 4 ) 2 SO 45
Uracil0.05
0.1M phosphate buffer
Preparation of 0.1M potassium phosphate buffer at 25° C.
pHVolume (mL) of 1M K 2 HPO 4Volume (mL) of 1M KH 2 PO 4
6.013.286.8
TABLE 6 — Conversion Medium (pH 7.6)
ComponentsConcentration (g/L)
Glucose30
YNB w/o amino acids6.7
Yeast extract3
(NH 4 ) 2 SO 415
Uracil0.05
L-alanine10
0.1M phosphate buffer
Preparation of 0.1M potassium phosphate buffer at 25° C.
pHVolume (mL) of 1M K 2 HPO 4Volume (mL) of 1M KH 2 PO 4
7.686.613.4
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9 codes
IPC · International Patent Classification
Section C — Chemistry; metallurgy
  • C12N15/00
  • C12N9/06
  • C12N9/02
  • C07H21/04
  • C12N9/04
  • C12N15/81
  • C12N1/18
  • C12N1/14
  • C12P7/18

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Yong D Pak
art unit 1652 · TC 1600
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