(en)A recombinant microorganism having the ability to produce glycerol 3-HP, or acrylic acid, in which glycerol is produced from dihydroxyacetone phosphate (DHAP) via dihydroxyacetone (DHA) in a biosynthetic pathway, and a method of producing glycerol, 3-hydroxypropioninc acid (3-HP), or acrylic acid by using the recombinant microorganism.

1.ApplicationNumber: US-201414508809-A
1.PublishNumber: US-9476070-B2
2.Date Publish: 20161025
3.Inventor: JUNG WONSEOK
KIM EUNYOUNG
KANG JINHO
KIM NAGJONG

4.Inventor Harmonized: JUNG WONSEOK(KR)
KIM EUNYOUNG(KR)
KANG JINHO(KR)
KIM NAGJONG(KR)

5.Country: US
6.Claims:
(en)A recombinant microorganism having the ability to produce glycerol 3-HP, or acrylic acid, in which glycerol is produced from dihydroxyacetone phosphate (DHAP) via dihydroxyacetone (DHA) in a biosynthetic pathway, and a method of producing glycerol, 3-hydroxypropioninc acid (3-HP), or acrylic acid by using the recombinant microorganism.

7.Description:
(en)RELATED APPLICATION
This application claims the benefit of Korean Patent Application No. 10-2014-0034131, filed on Mar. 24, 2014, in the Korean Intellectual Property Office, the entire disclosure of which hereby incorporated by reference.
INCORPORATION-BY-REFERENCE OF MATERIAL ELECTRONICALLY SUBMITTED
Incorporated by reference in its entirety herein is a computer-readable nucleotide/amino acid sequence listing submitted herewith and identified as follows: One 76,853 Byte ASCII (Text) file named “718161_ST25-Revised.TXT” created Dec. 16, 2014.
BACKGROUND
1. Field
The present disclosure relates to recombinant microorganisms that produce glycerol, 3-hydroxypropionic acid (HP), or acrylic acid, and methods of producing glycerol, 3-HP, or acrylic acid using the recombinant microorganisms.
2. Description of the Related Art
Carbon emission reduction and instability caused by the surge in oil prices have been recently considered global issues, and accordingly, efforts have been made to produce fuels or chemicals via carbon-neutral biological processes in place of the existing fuels or chemicals that were produced via chemical processes using oil as a raw material.
Glycerol is a compound that is necessary for cosmetics, liquid soaps, medicines, lubricants, anti-coagulate solutions, and many different industrial applications. Microorganisms that are capable of producing glycerol in various physiological conditions are demanded in a variety of industries. Thus, microorganisms that are capable of producing glycerol in physiological conditions by which glycerol itself is used as a substrate in vivo in a part of a further complicated catabolic or biosynthesis pathway are demanded.
With regard to metabolic pathways of synthesizing glycerol, dihydroxyacetone phosphate (DHAP) produced from glucose is converted into glycerol-3-phosphate (G3P), and G3P is converted into glycerol. Dehydrogenase (G3PDH) may be involved in the conversion of DHAP into G3P, and G3P phosphatase may be involved in the conversion of G3P into glycerol.
There remains a need for alternative microorganisms with the ability to produce glycerol and methods of producing glycerol by using the alternative microorganisms.
SUMMARY
Provided is a recombinant microorganism having an increased ability to produce glycerol 3-HP, and 3-acrylic acid compared to an unmodified microorganism of the same type.
In one embodiment, provided is a recombinant microorganism comprising: a polynucleotide encoding dihydroxyacetone phosphate phosphatase (DHAPP) that catalyzes the conversion of dihydroxyacetone phosphate (DHAP) into dihydroxyacetone (DHA); and a polynucleotide encoding glycerol dehydrogenase (GLDH) that catalyzes the conversion of DHA into glycerol.
In another embodiment, the recombinant microorganism further comprises a polynucleotide encoding glycerol dehydratase (GDH) that catalyzes the conversion of glycerol into 3-hydroxypropionaldehyde (3-HPA); and a polynucleotide encoding an aldehyde dehydrogenase (ALD) that catalyzes the conversion of 3-HPA into 3-hydroxypropionic acid (3-HP).
In an additional embodiment, the recombinant microorganism further comprises: an enzyme that converts 3-HP into 3-HP-CoA; and an enzyme that converts 3-HP-CoA into acryloyl-CoA.
Also provided is a method of efficiently producing glycerol using a recombinant microorganism according to the invention.
According to another aspect of the present invention, provided is a method of efficiently producing 3-HP using a recombinant microorganism according to the invention.
According to another aspect of the present invention, provided is a method of efficiently producing acrylic acid using a recombinant microorganism according to the invention.



BRIEF DESCRIPTION OF THE DRAWINGS
These and/or other aspects will become apparent and more readily appreciated from the following description of the embodiments, taken in conjunction with the accompanying drawings in which:
FIG. 1 is a diagram displaying a biosynthesis pathway of producing glycerol from glucose;
FIG. 2 is a cleavage map of a pACYCDuet_hdpA_gldA vector;
FIG. 3 is a cleavage map of a pETDuet/dhaB_gdrAB_gabD vector; and
FIG. 4 is a cleavage map of a pRSF/pct_yciA_hpd vector.



DETAILED DESCRIPTION
Reference will now be made in detail to embodiments, examples of which are illustrated in the accompanying drawings, wherein like reference numerals refer to like elements throughout. In this regard, the present embodiments may have different forms and should not be construed as being limited to the descriptions set forth herein. Accordingly, the embodiments are merely described below, by referring to the figures, to explain aspects of the present description. As used herein, the term “and/or” includes any and all combinations of one or more of the associated listed items. Expressions such as “at least one of,” when preceding a list of elements, modify the entire list of elements and do not modify the individual elements of the list.
A “sequence identity” of nucleic acid or polypeptide according to an embodiment of the present invention refers to the extent of identity between bases or amino acid residues after aligning the sequences such that they maximally match in certain comparative regions. The sequence identity is a value calculated by optimally aligning two sequences at certain comparative regions, wherein portions of the sequences at the certain comparative regions may be added or deleted, compared to reference sequences. A percentage of the sequence identity may be calculated by, for example, comparing two optimally aligned sequences in the entire comparative region, determining the number of locations in which the same amino acids or nucleic acids appear to obtain the number of matched locations, dividing the number of matched locations by the total number of locations in the comparative regions (that is, the size of the range), and multiplying by 100 to calculate the percentage of the sequence identity. The percentage of the sequence identity may be calculated by using a known sequence comparison program, and examples of the program include BLASTN (NCBI), CLC Main Workbench (CLC bio), and MegAlign™ (DNASTAR Inc).
Various levels of sequence identity may be used to identify various types of polypeptides or polynucleotides having the same or similar functions. For example, a sequence identity of about 50% or more, about 55% or more, about 60% or more, about 65% or more, about 70% or more, about 75% or more, about 80% or more, about 85% or more, about 90% or more, about 95% or more, about 96% or more, about 97% or more, about 98% or more, about 99% or more, or 100% may be used.
According to an aspect of the present invention, provided is a recombinant microorganism including a polynucleotide encoding dihydroxyacetone phosphate phosphatase (DHAPP) that catalyzes the conversion of dihydroxyacetone phosphate (DHAP) into dihydroxyacetone (DHA); and a polynucleotide encoding glycerol dehydrogenase (GLDH) that catalyzes the conversion of DHA into glycerol. The recombinant microorganism may produce an increased amount of glycerol compared to an unmodified organism of the same type.
As used herein, the term “DHAPP” refers to any enzyme that catalyzes the conversion of DHAP into DHA. The DHAPP may belong to the haloacid dehydrogease superfamily (HAD family). The HAD family may have phosphatase activity of P-type ATPase. The HAD family may not exhibit any phosphatase activity, or have almost no phosphatase activity, with respect to nucleoside monophosphates (i.e., AMP, CMP, GMP, or UMP), for example, when the nucleotide monophosphates are at a concentration of 5 to 10 mM in a solution and or cell culture medium with a member of the HAD family. The DHAPP may be HAD superfamily phosphatase A (HdpA) derived from C. glutamicum . The HdpA may have an amino acid sequence of SEQ ID NO: 1. The polynucleotide encoding the HdpA may have a nucleotide sequence encoding an amino acid sequence of SEQ ID NO: 1, for example, a nucleotide sequence of SEQ ID NO: 2. The DHAPP may include an amino acid sequence having a sequence identity of about 65% or more, for example, about 70% or more, about 80% or more, about 85% or more, about 90% or more, about 91% or more, about 92% or more, about 93% or more, about 94% or more, about 95% or more, about 96% or more, about 97% or more, about 98% or more, about 99% or more, or about 100% to SEQ ID NO: 1. The DHAPP may be phospholipid-translocating ATPase categorized as EC 3.6.3.1, 3-deoxy-D-manno-octulosonate (KDO) 8-phosphate phosphatase categorized as EC 3.1.3.45, mannosyl-3-phosphoglycerate phosphatase categorized as EC 3.1.3.70, or phosphoglycolate phosphatase categorized as EC 3.1.3.18. The DHAPP may be a polypeptide belonging to the HAD superfamily that has NCBI IDs listed in Table 1. The polynucleotide encoding DHAPP may be heterologous to the recombinant microorganism.






TABLE 1



NCBI ID
Microorganism



gi|25028706
Corynebacterium efficiens YS.314

gi|334564111
Corynebacterium bovis DSM20582

gi|38234264
Corynebacterium diphtheriae NCTC13129

gi|337291210
Corynebacterium ulcerans BR.AD22

gi|300858925
Corynebacterium pseudotuberculosis FRC41

gi|255324876
Corynebacterium tuberculostearicum SK141

gi|227833577
Corynebacterium aurimucosum ATCC700975

gi|227503202
Corynebacterium accolens ATCC49725

gi|296119783
Corynebacterium ammoniagenes DSM20306

gi|227504606
Corynebacterium striatum ATCC6940

gi|358445640
Corynebacterium casei UCMA3821

gi|237785884
Corynebacterium kroppenstedtii DSM44385

gi|54027323
Nocardia farcinica IFM10152

gi|300790316
Amycolatopsis mediterranei U32

gi|375102711
Saccharomonospora cyanea NA.134

gi|72162161
Thermobifida fusca YX

gi|357413254
Streptomyces favogriseus ATCC33331

gi|297561702
Nocardiopsis dassonvillei subsp. dassonvillei DSM43111

gi|262200628
Gordonia bronchialis DSM43247

gi|134097184
Saccharopolyspora erythraea NRRL2338

gi|358457856
Frankia sp. CN3

gi|312141254
Rhodococcus equi 103S

gi|324997972
Pseudonocardia sp. P1

gi|377575652
Mobilicoccus pelagius NBRC104925

gi|357389721
Kitasatospora setae KM.6054

gi|325961988
Arthrobacter phenanthrenivorans Sphe3

gi|326331131
Nocardioidaceae bacterium Broad.1

gi|258654845
Nakamurella multipartita DSM44233

gi|302868690
Micromonospora aurantiaca ATCC27029

gi|330469082
Verrucosispora maris AB.18.032

gi|296138280
Tsukamurella paurometabola DSM20162

gi|152968106
Kineococcus radiotolerans SRS30216

gi|118470582
Mycobacterium smegmatis MC2.155

gi|159038790
Salinispora arenicola CMS.205

gi|148271663
Clavibacter michiganensis subsp.


michiganensis NCPPB382

gi|333922006
Amycolicicoccus subflavus DQS3.9A1

gi|334335848
Isoptericola variabilis 225

gi|379737345
Blastococcus saxobsidens DD2

gi|359834376
Actinoplanes sp. SE50/110

gi|296130804
Cellulomonas flavigena DSM20109

gi|256374626
Actinosynnema mirum DSM43827

gi|271964711
Streptosporangium roseum DSM43021

gi|309811927
Dermacoccus sp. Ellin185

gi|284992561
Geodermatophilus obscurus DSM43160





























































As used herein, the term “GLDH” may be any material as long as it catalyzes the conversion of DHA into glycerol. The GLDH may be a polypeptide that catalyzes the conversion of DHA into glycerol. The GLDH may be an enzyme categorized as EC 1.1.1.6. The GLDH may also be DHA reductase. The GLDH may be dependent on NAD categorized as EC 1.1.1.6, NADP categorized as EC 1.1.1.72, or other cofactors categorized as, for example, EC 1.1.99.22. An example of the NAD-dependent GLDH is gldA (GenBank U000006) having an amino acid sequence of SEQ ID NO: 3. In addition, the polynucleotide encoding the GLDH may have a nucleotide sequence encoding an amino acid sequence of SEQ ID NO: 3, for example, a nucleotide sequence of SEQ ID NO: 4. The GLDH may include an amino acid sequence having a sequence identity of about 65% or more, for example, about 70% or more, about 80% or more, about 85% or more, about 90% or more, about 91% or more, about 92% or more, about 93% or more, about 94% or more, about 95% or more, about 96% or more, about 97% or more, about 98% or more, about 99% or more, or about 100% to SEQ ID NO: 3. The polynucleotide encoding GLDH may be heterologous to the recombinant microorganism.
The DHAPP-coding polynucleotide and/or the GLDH-coding polynucleotide may be expressed at higher levels in the recombinant microorganism than those in a microorganism that is not genetically manipulated. The expression level may refer to the expression of mRNA or protein encoded by the mRNA. The expression at the protein level may be based on amount of protein expressed or the activity of the expressed protein. The expression level may be increased by about 5% or more, about 10% or more, about 15% or more, about 20% or more, about 30% or more, about 50% or more, about 60% or more, about 70% or more, about 100% or more, about 200% or more, or about 300% or more than that in a microorganism that is not genetically manipulated. The term “microorganism that is not genetically manipulated” as used herein may be a parent cell or microorganism that is not genetically manipulated or genetically engineered, for example, a parent microorganism that does not contain the DHAPP-coding polynucleotide and/or the GLDH-coding polynucleotide, or that contains fewer copies of the DHAPP-coding polynucleotide and/or GLDH-coding polynucleotide.
The recombinant microorganism may have the ability to produce glycerol. The recombinant microorganism may produce glycerol at higher levels than a parent microorganism that is not genetically manipulated. The production of glycerol may include production in a cell, secretion of glycerol from the cell (e.g., in a cell culture medium) after being produced in a cell, or a combination thereof. Glycerol produced in a cell may be converted from metabolites such as 3-HP or acrylic acid. The production of glycerol may be increased by about 5% or more, about 10% or more, about 15% or more, about 20% or more, about 30% or more, about 50% or more, about 60% or more, about 70% or more, about 100% or more, about 200% or more, or about 300% or more than that in a microorganism that is not genetically manipulated.
The increase in the expression level of polynucleotides, proteins, or enzymes used in embodiments of the present invention may occur by introducing a polynucleotide encoding a polypeptide (i.e., enzyme) into a cell, increasing a copy number of the polynucleotide in the cell, or mutating a regulatory region of the polynucleotide. A polynucleotide that is introduced from the outside or present in an increased copy number may be an endogenous gene or an exogenous gene. The endogenous gene refers to a gene that exists in a genetic material included in a microorganism. The exogenous gene refers to a gene that is introduced into a host cell, such as a gene that is integrated into a host cell genome, wherein the introduced gene may be homologous or heterologous with respect to the host cell genome.
The expression “increased copy number” as used herein may include a copy number increase by an introduction or amplification of the gene and a genetic manipulation of a cell that does not have a gene so as to have the gene in the cell. The introduction of the gene may occur by using a vehicle such as a vector. The vector may be delivered to the microorganism using a variety of techniques e.g., incubation in a solution containing divalent cations followed by heat shock and electroporation, or other suitable transformation techniques known in the art. The introduction may be a transient introduction, in which the gene is not integrated into the genome, or an integration into the genome. The introduction may, for example, occur by introducing a vector inserted with a polynucleotide encoding a desired polypeptide into the genome of the cell and then replicating the vector in the cell or integrating the polynucleotide into the genome.
The term “gene” as used herein refers to a nucleic acid fragment expressing a specific protein, and may include a regulatory sequence such as 5′-non coding sequence and 3′-non coding sequence in addition to a coding region.
The term “heterologous” as used herein refers to foreign matter that is not native to the cell.
The term “secretion” as used herein refers to a movement of a material from cell interior to a periplasmic space or an extracellular environment.
The recombinant microorganism may be a prokaryote. The recombinant microorganism may be a bacterium, and examples thereof include Escherichia such as Escherichia coli, Clostritidia such as Clostritidium ljungdahlii, Clostritidium autoethanogenum or Clostritidium kluyveri, Corynebacteria such as Corynebacterium glutamicum, Cupriavidus such as Cupriavidus necator or Cupriavidus metallidurans, Pseudomonas such as Pseudomonas fluorescens, Pseudomonas putida or Pseudomonas oleavorans, Delftia such as Delftia acidovorans, Bacillus such as Bacillus subtilis, Lactobacillus such as Lactobacillus delbrueckii , or Lactococcus genus including Lactococcus lactis. Corynebacteria genus may include C. callunae, C. efficiens, C. ulcerans, C. halotolerans, C. pseudotuberculosis, C. durum , or C. striatum . These bacteria may act as a host cell for the recombinant microorganism.
The recombinant microorganism may be a eukaryote, and the eukaryote may be fungi such as yeasts. The eukaryote may be Aspergillus genus including A. niger, Saccharomyces genus including S. cerevisiae, Pichia genus including P. pastoris, Yarrowia genus including Y. lipolytica, Issatchenkia genus including I. orientalis, Debaryomyces genus including D. hansenii, Arxula genus including A. adenoinivorans, Kluyveromyces genus including K. lactis , or Hypocrea genus including H. americana . These microorganisms may act as a host cell for the recombinant microorganism. The Saccharomyces genus may not include S. pombe.
The recombinant microorganism is genetically manipulated, as compared to a parent microorganism. Such manipulation may include introducing a polynucleotide encoding a polypeptide into a cell (e.g., a non-native polynucleotide), increasing a copy number of the polynucleotide in the cell (e.g., a native polynucleotide), or mutating a regulatory region of a polynucleotide (e.g., of a native polynucleotide). A polynucleotide that is introduced from the outside or present in an increased copy number may be an endogenous gene or an exogenous gene. The endogenous gene refers to a gene that exists in a genetic material natively included in a microorganism. The exogenous gene refers to a gene that is introduced into a host cell, such as a gene that is integrated into a host cell genome, wherein the introduced gene may be homologous or heterologous with respect to the host cell genome. The recombinant microorganism may be manipulated, as compared to the polypeptide or the gene used in the present specification.
The recombinant microorganism may further include a polynucleotide encoding glycerol dehydratase (GDH) that catalyzes the conversion of glycerol into 3-hydroxypropionaldehyde (3-HPA); and a polynucleotide encoding aldehyde dehydrogenase (ALD) that catalyzes the conversion of 3-HPA into 3-hydroxypropionic acid (3-HP). The polynucleotide encoding GDH may be heterologous to the microorganism. The recombinant microorganism may produce an increased amount of 3-HP compared to an unmodified microorganism of the same type (e.g., a parent microorganism).
The term “GDH” as used herein may include any enzyme as long as it is catalyzes the conversion of glycerol into 3-HPA. The GDH may be categorized as EC 4.2.1.30 or may be a diol dehydratase categorized as EC 4.2.1.28. The GDH and a nucleotide encoding GDH may be derived from Ilyobacter polytropus, Klebsiella pneumoniae, Citrobacter freundii, Clostritidium pasteurianum, Salmonella typhimurium , or Klebsiella oxytoca . In each case of these genra, the GDH may be composed of three subunits: a large or “α” subunit, a medium or “β” subunit, and a small or “γ” subunit. A gene encoding the large or “α” subunit of the GDH may include dhaB1, gldA, and dhaB. A gene encoding the medium or “β” subunit of the GDH may include dhaB2, gldB, and dhaC. A gene encoding the small or “γ” subunit of the GDH may include dhaB3, gldC, and dhaE. A gene encoding a large or “α” subunit of the diol dehydratase may include pduC and pddA. A gene encoding a medium or “β” subunit of the diol dehydratase may include pduD and pddB. A gene encoding a small or “γ” subunit of the diol dehydratase may include pduE and pddC. Tables 2 and 3 shows a comparison of gene names regarding GDH and functions related to the GDH and GenBank references. The GDH may include dhaB1, dhaB2, and dhaB derived from Ilyobacter polytropus . DhaB1, DhaB2, and DhaB3 derived from Ilyobacter polytropus may each include an amino acid sequence of SEQ ID NO: 45, 46, and 47. The dhaB1, dhaB2, and dhaB3 genes may each encode an amino acid sequence of SEQ ID NO: 45, 46, and 47. The dhaB1, dhaB2, and dhaB3 genes derived from Ilyobacter polytropus may each have a sequence of SEQ ID NO: 5, 6, and 7.






TABLE 2



Individual
Gene function







(GenBank
Regulation
Unknown
Reactivation
Unknown











reference

Base

Base

Base

Base

number)
Gene
pair
Gene
pair
Gene
pair
Gene
pair




K. pneumoniae



orf2c
7116-
orf2b
6762-
orf2a
5125-

(U30903)



7646

7115

5556


K. pneumoniae





GdrB

(U60992)


C. freundii

dhaR
3746-
orfW
5649-
orfX
6180-
orfY
7736-

(U09771)

5671

6179

6533

8164


C.



pasteurianum


(AF051373)


C.



orfW
210-
orfX
1-
orfY
746-


pasteurianum




731

196

1177

(AF026270)


S. typhimurium





pduH
8274-

(AF026270)





8645


K. oxytoca





DdrB
2063-

(AF017781)





2440


K. oxytoca


(AF051373)

















































TABLE 3



Individual
Gene function







(GenBank
Dehydratase, α
Dehydratase, α
Dehydratase, α
Reactivation











reference

Base

Base

Base

Base

number)
Gene
pair
Gene
pair
Gene
pair
Gene
pair




K. pneumoniae

dhaB1
3047-
dhaB2
2450-
dhaB3
2022-
orf2a
186-

(U30903)

4714

2890

2447

2009


K. pneumoniae

gldA
121-
gldB
1801-
gldB
2388-
gdrA

(U60992)

1788

2382

2813


C. freundii

dhaB
8556-
dhaC
10235-
dhaC
10822-
orfY
11261-

(U09771)

10223

10819

11250

13072


C. pasteurianum

dhaB
84-
dhaC
1779-
dhaC
2333-

2790-

(AF051373)

1748

2318

2773

4598


C. pasteurianum







orfY

(AF026270)


S. typhimurium

pduC
3557-
pduD
5232-
pduD
5921-

6452-

(AF026270)

5221

5906

6442

8284


K. oxytoca








241-

(AF017781)







2073


K. oxytoca

pddA
121-
pddB
1796-
pddB
2485-

(AF051373)

1785

2470

3006









































The GDH may include an amino acid sequence derived from Ilyobacter polytropus , the amino acid sequence having a sequence identity of about 65% or more, for example, about 70% or more, about 80% or more, about 85% or more, about 90% or more, about 91% or more, about 92% or more, about 93% or more, about 94% or more, about 95% or more, about 96% or more, about 97% or more, about 98% or more, about 99% or more, or about 100% to each sequence of dhaB1, dhaB2, and dhaB3.
The term “ALD” as used herein may include any protein as long as it is capable of catalyzing the conversion of 3-HPA into 3-HP. The ALD may use redox cofactors, such as NAD, NADP, FAD, or PQQ. The ALD may be categorized as EC 1.2.1.3 (NAD-dependent ALD), EC 1.2.1.4 (NADP-dependent ALD), EC 1.2.99.3 (PQQ-dependent ALD), or EC 1.2.99.7 (FAD-dependent ALD). An example of the NADP-dependent ALD includes AldB encoded by aldB gene of E. coli . An example of the NAD-dependent ALD includes AldA encoded by aldA gene of E. coli or AldH encoded by aldH gene of E. coli . The ALD may be succinate semialdehyde dehydrogenase (SSADH). The SSADH may be categorized as EC 1.2.1.24 or EC 1.2.1.16. The SSADH may be dependent on NAD+, NADP+, or both NAD+ and NADP+. The SSADH may be CoA-independent enzyme. The SSADH may be, for example, derived from Corynebacterium sp., Rhodococcus sp., Gordonia sp., Mycobacterium sp., Enterobacter sp., or Aserica sp. The SSADH may be gabD1, gabD2, or gabD3 derived from E. coli . A gene encoding the SSADH may be, for example, a polynucleotide encoding an amino acid sequence of SEQ ID NO: 8, 9, and 10. The SSADH may be gabD (a nucleotide sequence of SEQ ID NO: 36 and an amino acid sequence of SEQ ID NO: 48) derived from Cupriavidus necator . A gene encoding the SSADH may be, for example, a polynucleotide encoding an amino acid sequence of SEQ ID NO: 8, 9, 10, and 36. A gene encoding the SSADH may include, for example, a nucleotide sequence of SEQ ID NO: 11, 12, 13, and 36. The SSADH may include an amino acid sequence having a sequence identity of about 65% or more, for example, about 70% or more, about 80% or more, about 85% or more, about 90% or more, about 91% or more, about 92% or more, about 93% or more, about 94% or more, about 95% or more, about 96% or more, about 97% or more, about 98% or more, about 99% or more, or about 100% to amino acid sequences of SEQ ID NO: 8, 9, 10, and 48.
The recombinant microorganism may further include a polynucleotide encoding glycerol dehydratase reactivase (GDR). Glycerol and diol dehydratases may be subjected to metabolism-based suicide inactivation by glycerol and some other substrates (see e.g., Daniel et al., FEMS Microbiol. Rev. 22, 553(1999)). The term “glycerol dehydratase reactivase (GDR)” as used herein refers to proteins responsible for reactivating the dehydratase activity. The term “dehydratase reactivating activity” as used herein refers to the phenomenon of converting a dehydratase that is unable to catalyze a substrate into a dehydratase capable of catalyzing a substrate, or to the phenomenon of inhibiting the degradation of a dehydratase, or the phenomenon of extending the half-life of the dehydratase enzyme in vivo. The GDR may be at least one of dhaB, gdrA, pduG, and ddrA. In addition, the GDR may be at least one of orfX, orf2b, gdrB, pduH, and ddrB.
The GDR, as gdrA and gdrB derived from K. pneumonia (U60992), may each have amino acid sequences of SEQ ID NO: 18 and 19. Alternatively, the GDR, as gdrA and gdrB derived from I. polytropus , may each have amino acid sequences of SEQ ID NO: 14 and 15. The GDR may have an amino acid sequence having a sequence identity of about 65% or more, for example, about 70% or more, about 80% or more, about 85% or more, about 90% or more, about 91% or more, about 92% or more, about 93% or more, about 94% or more, about 95% or more, about 96% or more, about 97% or more, about 98% or more, about 99% or more, or about 100% to each amino acid sequence of SEQ ID NO: 14, 15, 18, and 19. Genes encoding GdrA and GdrB may have sequences coding each amino acid sequence of SEQ ID NO: 14, 15, 18, and 19, and for example, may have each nucleotide sequence of SEQ ID NO: 16, 17, 20, and 21.
In the recombinant microorganism, at least one polynucleotide selected from the group consisting of a polynucleotide encoding the GDH, a polynucleotide encoding the ALD, and a polynucleotide encoding the GDR may be expressed at higher levels than in a microorganism that is not genetically manipulated (e.g., parent microorganism). The expression level may be an expression at an mRNA or protein level. The expression at the protein level is based on amounts or activities of the expressed proteins. The expression level may be increased by about 5% or more, about 10% or more, about 15% or more, about 20% or more, about 30% or more, about 50% or more, about 60% or more, about 70% or more, about 100% or more, about 200% or more, or about 300% or more than that in a microorganism that is not genetically manipulated, for example, a parent cell.
In some embodiments, the recombinant microorganism may produce 3-HP. In this regard, the increase in the expression level may refer to production of 3-HP at higher levels than that in a microorganism that is not genetically manipulated (e.g., parent microorganism). The production of 3-HP may include production in a cell, secretion to the outside after being produced in a cell, or a combination thereof. 3-HP produced in a cell may be converted from other metabolites such as acrylic acid. The production of 3-HP may be increased by about 5% or more, about 10% or more, about 15% or more, about 20% or more, about 30% or more, about 50% or more, about 60% or more, about 70% or more, about 100% or more, about 200% or more, or about 300% or more than that in a microorganism that is not genetically manipulated, for example, a parent cell.
The increase in the expression level may be due to any mode of genetic manipulation as described, above (e.g., introducing a new polynucleotide, increasing the copy number of an existing polynucleotide, or mutating a regulatory region). The recombinant microorganism may further include a polynucleotide encoding an enzyme that catalyzes the conversion 3-HP into 3-HP-CoA; and another polynucleotide encoding an enzyme that catalyzes the conversion of 3-HP-CoA into acryloyl-CoA and/or acrylate. The recombinant microorganism may further include a polynucleotide encoding an enzyme (e.g., acryloyl-CoA hydrolase) that catalyzes the conversion acryloyl-CoA into acrylate.
The enzyme that catalyzes the conversion of 3-HP into 3-HP-CoA may be a polypeptide having CoA transferase activity, a polypeptide having 3-HP CoA hydrolase activity, or a polypeptide having 3-hydroxyisobutyryl-CoA hydrolase activity. The polypeptide having CoA transferase activity may be categorized as EC 2.8.3.1. The polypeptide having CoA transferase activity or a polynucleotide encoding the same may be derived from Megasphaera elsdenii, Clostritidium propionicum, Clostritidium kluyveri , and Escherichia coli . The polypeptide having CoA transferase activity may be Pct (SEQ ID NO: 22) derived from M. elsdenii ATCC17753 CoA transferase, and the gene encoding the same may be pct (SEQ ID NO: 23). The polypeptide having 3-HP CoA hydrolase activity may be categorized as EC 3.1.2.-. The enzyme categorized as EC 3.1.2.- may be a gene product, such as YciA, tesB, or Acot13. The polypeptide having 3-hydroxypropionly-CoA hydrolase activity and a polynucleotide encoding the same may be a yciA gene product (SEQ ID NO: 24) of E. coli K-12 W3110 and the gene of the same (SEQ ID NO: 25). The polypeptide having 3-hydroxyisobutyryl-CoA hydrolase activity may be categorized as EC 3.1.2.4.
The enzyme that catalyzes the conversion of 3-HP-CoA into acryloyl-CoA or acrylate may be a polypeptide having activity of 3-hydroxypropionyl-CoA dehydratase. The conversion of acrylate of acryloyl-CoA into acrylic acid may be achieved by intracellular CoA ligase. The bacterial cells may be capable of expressing CoA ligase, and may have genes encoding CoA ligase. The polypeptide having activity of 3-hydroxypropionyl-CoA dehydratase may be categorized as EC 4.2.1.-. The polypeptide having activity of 3-hydroxypropionyl-CoA dehydratase or a polynucleotide encoding the same may be derived from Chloroflexus aurantiacus, Candida rugosa, Rhodospirillum rubrum , or Rhodobacter capsulates . The polypeptide having activity of 3-hydroxypropionyl-CoA dehydratase or the polynucleotide encoding the same, i.e., HPD and hpd derived from C. aurantiacus , may each have an amino acid sequence of SEQ ID NO: 26 and a nucleotide sequence of SEQ ID NO: 27.
In the recombinant microorganism, at least one polynucleotide selected from the group consisting of a polynucleotide encoding an enzyme that converts 3-HP into 3-HP-CoA and a polynucleotide encoding an enzyme that converts 3-HP-CoA into acryloyl-CoA and/or acrylate may be expressed at higher levels than in a microorganism that is not genetically manipulated. The expression level may be an expression at an mRNA or protein level. The expression at the protein level is based on amounts or activities of the expressed proteins. The expression level may be increased by about 5% or more, about 10% or more, about 15% or more, about 20% or more, about 30% or more, about 50% or more, about 60% or more, about 70% or more, about 100% or more, about 200% or more, or about 300% or more than that in a microorganism that is not genetically manipulated.
In additional embodiments, the recombinant microorganism may have the ability to produce acrylic acid and/or acrylate. In this regard, the increase in the expression level may refer to production of acrylic acid and/or acrylate at higher levels than that in a microorganism that is not genetically manipulated. The production of acrylic acid and/or acrylate may include production in a cell, secretion to the outside after being produced in a cell, or a combination thereof. 3-HP produced in a cell may be converted from other metabolites such as acrylic acid. The production of acrylic acid and/or acrylate may be increased by about 5% or more, about 10% or more, about 15% or more, about 20% or more, about 30% or more, about 50% or more, about 60% or more, about 70% or more, about 100% or more, about 200% or more, or about 300% or more than that in a microorganism that is not genetically manipulated.
The increase in the expression level may be due to any mode of genetic manipulation as described, above (e.g., introducing a new polynucleotide, increasing the copy number of an existing polynucleotide, or mutating a regulatory region). Another aspect of the present invention provides a method of producing glycerol comprising culturing the recombinant microorganism in a cell culture medium, whereby the microorganism produces glycerol; and recovering glycerol from the culture.
Another aspect of the present invention provides a method of producing 3-HP comprising culturing the recombinant microorganism; and recovering 3-HP from the culture.
Another aspect of the present invention provides a method of producing acrylic acid comprising culturing the recombinant microorganism in a cell culture medium, whereby the microorganism produces acrylic acid; and recovering acrylic acid from the culture.
Another aspect of the present invention provides a method of producing 3-hydroxypropionic acid (3-HP), the method comprising:
culturing the recombinant microorganism of claim 7 in a cell culture medium, whereby the microorganism produces 3-HP; and recovering 3-HP from the culture.
The culturing may be performed in a suitable medium under suitable culturing conditions known in the art. For example, the medium may be aqueous solution containing glucose 40 g/l, MgSO 4 .7H 2 O 1.4 g/l, K 2 HP 4 17.4 g/l, KH 2 PO 4 3.0 g/l, (NH 4 ) 2 HPO 4 4.0 g/l, citric acid 1.7 g/l, ZnCl 2 0.014 g/l, FeCl 2 .4H 2 O 0.041 g/l, MnCl 2 0.015 g/l, CuCl 2 0.0015 g/l, H 3 BO 3 0.003 g/l, and Na 2 MoO 4 0.0025 g/l. One of ordinary skill in the art may suitably change a culture medium and culturing conditions according to the microorganism selected. Culturing methods may include batch culturing, continuous culturing, fed-batch culturing, or a combination thereof.
The culture medium may include various carbon sources, nitrogen sources, and trace elements.
The carbon source may include assimilable sugars, which may be hexose or pentose sugars. The carbon source may be, for example, carbohydrate such as glucose, sucrose, lactose, fructose, maltose, starch, or cellulose; fat such as soybean oil, sunflower oil, castor oil, or coconut oil; fatty acid such as palmitic acid, stearic acid, linoleic acid; alcohol such as glycerol or ethanol; organic acid such as acetic acid, or a combination thereof. The culturing may be performed by having glucose as the carbon source. The nitrogen source may be an organic nitrogen source such as peptone, yeast extract, beef stock, malt extract, corn steep liquor (CSL), or soybean flour, or an inorganic nitrogen source such as urea, ammonium sulfate, ammonium chloride, ammonium phosphate, ammonium carbonate, and ammonium nitrate, or a combination thereof. The culture medium is a supply source of phosphorus and may include, for example, potassium dihydrogen phosphate, dipotassium phosphate, and corresponding sodium-containing salt thereof, and a metal salt such as magnesium sulfate or iron sulfate. Also, amino acid, vitamin, a suitable precursor, or the like may be included in the culture medium. The culture medium or an individual component may be added to a culture medium solution in a batch, fed-batch, or continuous manner.
Also, the pH of the culture medium solution may not be adjusted or may be adjusted by adding a compound such as ammonium hydroxide, potassium hydroxide, ammonia, phosphoric acid, and sulfuric acid to the culture medium solution by using a suitable method during the culturing process. Also, an antifoaming agent such as fatty acid polyglycol ester may be used during the culturing process to inhibit the generation of bubbles.
The culturing process may be performed under anaerobic or a microaerobic condition. As used herein, the term “anaerobic conditions” refers to an environment devoid of oxygen. As used herein, the term “microaerobic conditions” when used in reference to a culture or growth condition is intended to mean that the dissolved oxygen concentration in the medium remains larger than 0% and less than 10% of saturation for dissolved oxygen in liquid media. Microaerobic conditions also include growing or resting cells in liquid medium or on solid agar inside a sealed chamber maintained with an atmosphere of less than 1% oxygen. The percent of oxygen can be maintained by, for example, sparging the culture with an N 2 /CO 2 mixture or other suitable non-oxygen gas or gases. The oxygen conditions may include a dissolved oxygen (DO) concentration of 0% to 10%, for example, 0%, 0 to 8%, 0 to 6%, 0 to 4%, 0 to 2%, 1 to 10%, 1 to 8%, 1 to 6%, 1 to 4%, or 1 to 2%, 2 to 10%, 2 to 8%, 2 to 6%, 2 to 4%, 3 to 10%, 3 to 8%, 3 to 6%, 4 to 10%, 4 to 8%, or 4 to 6%.
Glycerol, 3-HP, or acrylic acid produced by the recombinant microorganism may be secreted from the cell, and then recovered from the culture medium. Additionally, glycerol, 3-HP, or acrylic acid may be separated from the culture medium. The separation of glycerol, 3-HP, or acrylic acid from the culture medium may be performed by using separation and purification methods known in the art. The recovering may be performed by centrifugation, chromatography, extraction, filtration, sedimentation, or a combination thereof.
The chemical conversion of glycerol, 3-HP, or acrylic acid produced by the methods above may achieve synthesis of substrates that are structurally related thereto.
Hereinafter, the present invention is described in greater detail with reference to embodiments. However, the embodiments are for illustrative purposes only and do not limit the scope of the present invention.
EXAMPLE 1
Manufacture of Microorganisms Introduced by DHAPP and GLDH Genes and Evaluation of Ability to Produce Glycerol in the Microorganisms
(1) Manufacture of a Vector to be Introduced into hdpA and gldA Genes.
Genes (e.g., hdpA of SEQ ID NO: 2) encoding DHAPP derived from Corynebacterium glutamicum ATCC 13032 were obtained by PCR amplification using a primer set of hdpA_F (SEQ ID NO: 28) and hdpA_R (SEQ ID NO: 29). The PCR amplification was performed in 30 cycles by repeating the processes of denaturing at a temperature of 95° C. for 30 seconds, annealing at a temperature of 50° C. for 30 seconds, and elongation at a temperature of 72° C. for 1 minute. The amplification products obtained therefrom were processed with restriction enzymes, i.e., NcoI and BamHI, and then cloned in a pACYCDuet™-1 vector (Novagen).
In addition, genes (gldA of SEQ ID NO: 4) encoding GLDH derived from E. coli (e.g., E. coli K strains) used were obtained by PCR amplification using a primer set of gldA_F (SEQ ID NO: 30) and gldA_R (SEQ ID NO: 31). The PCR amplification was performed in 30 cycles by repeating the processes of denaturing at a temperature of 95° C. for 30 seconds, annealing at a temperature of 50° C. for 30 seconds, and elongation at a temperature of 72° C. for 1 minute. The amplification products obtained therefrom were processed with restriction enzymes, i.e., NdeI and XhoI, and then cloned to the vector above, thereby obtaining a pACYC/hdpA_gldA vector. FIG. 2 is a cleavage map of the pACYCDuet_hdpA_gldA vector.
(2) Evaluation of Glycerol Productivity
The pACYC/hdpA_gldA vector manufactured in step (1) was transformed into E. coli K (DE3) strains. The E. coli to which the vector was introduced was cultured in an M9 minimal medium (0.4 g/L of MgSO 4 H 2 O, 17.4 g/L of K 2 HPO 4 , 3 g/L of KH 2 PO 4 , 4 g/L of (NH 4 ) 2 HPO 4 , 1.7 g/L of citric acid, 0.014 g/L of ZnCl 2 , 0.041 g/L of FeCl 2 H 2 O, 0.015 g/L of MnCl 2 , 0.0015 g/L of CuCl 2 , 0.003 g/L of H 3 BO 3 , 0.0025 g/L of Na 2 MoO 4 , 200 mg/L of nitriloacetic acid, 30 μg/L of sodium selenite, and 40 g/L of glycerol) at a temperature of 30° C. until OB 600 achieved 0.6. of 0.02 mM of IPTG was added thereto, and the medium was cultured again at a temperature of 30° C. for 24 hours. Then, the concentration of glycerol produced in the culture medium was measured. The culturing may be performed by shaking the medium in a 250 mL flask, and then the concentration of acrylic acid was calculated using HPLC.
After culturing the culture medium for 24 hours, portions of the culture medium were extracted for measuring optical density and pH, thereby identifying production of 3-HP by using HPLC (Waters). Once every 24 hours, the pH of the culture medium was corrected to pH 7.0 by using 4N NaOH. In HPLC analysis, an Aminex HPX-87H (300 mm×7.8 mm) column was used, and 0.5 mM of an aqueous solution of sulfuric acid containing 9% acetonitrile was used in a mobile phase. Here, HPLC had a flow rate of 0.4 ml/min and a temperature of 35° C. in the column. A detector device used a dual mode of RI and UV/VIS (210 nm). Glycerol was detected in 16.2 minutes out of 35 minutes in total.
Table 4 below shows produced amounts of glycerol according to consumed amounts of glucose of the E. coli . The recombinant strain consumed 20.15 g/L of glucose in 24 hours while it produced 0.85 g/L of glycerol.









TABLE 4





Produced amount
Consumed amount



of glycerol (g/L)
of glucose (g/L)
OD











pACYC/hdpA_gldA
0.85
20.15
6.13

Control group
0
22.51
6.81























EXAMPLE 2
Manufacture of Microorganism having Ability to Produce 3-HP and Evaluation on Ability of Producing 3-HP in the Microorganism
(1) Manufacture of an ET_BAB_Dc5 Vector
In order to manufacture a microorganism capable of producing 3-hydroxypropionic acid (3-HP) from glycerol, an ET_BAB_Dc5 vector was manufactured.
Genes (i.e., dhaB1, dhaB2, and dhaB3 of SEQ ID NO: 5, 6, and 7, respectively) encoding GDH from genome DNA of Ilyobacter polytropus and genes (i.e., gdrA and gdrB of SEQ ID NO: 16 and 17, respectively) encoding GDR were used. The dhaB1, dhaB2, and dhaB3 genes used genome DNA of I. polytropus as a template, and dhaB123 was obtained as an amplification product by PCR amplification using a primer set of dhaB123_F (SEQ ID NO: 32) and dhaB123_R (SEQ ID NO: 33). The gdrA and gdrB genes used genomic DNA of I. polytropus as a template, and gdrAB was obtained as an amplification product by PCR amplification using a primer set of gdrAB_F (SEQ ID NO: 34) and gdrAB_R (SEQ ID NO: 35). The amplification products obtained therefrom were processed with restriction enzymes, i.e., BamHI and SacI, and then cloned in a pETDuet™-1 vector (Novagen).
In addition, genes (i.e., gabD of SEQ ID NO: 35) encoding SSADH from genomic DNA of Cupriavidus necator were obtained by PCR amplification using a primer set of gabD_F (SEQ ID NO: 37) and gabD_R (SEQ ID NO: 38). The amplification products obtained therefrom were processed with restriction enzymes, i.e., NdeI and KpnI, and then cloned in the vector above. As a result, a pETDuet-1/dhaB_gdrAB_gabD vector was obtained. FIG. 3 is a cleavage map of the pETDuet/dhaB_gdrAB_gabD vector.
(2) Evaluation on Ability to Produce 3-HP
The pETDuet/dhaB_gdrAB_gabD vector manufactured in step (1) of Example 2 was transformed into E. coli K(DE3) pACYC/hdpA_gldA strains capable of producing glycerol from glucose.
The strain was cultured using a 250 ml flask in a 50 ml medium (1.4 g/L of MgSO 4 H 2 O, 17.4 g/L of K 2 HPO 4 , 3 g/L of KH 2 PO 4 , 4 g/L of (NH 4 ) 2 HPO 4 , 1.7 g/L of citric acid, 0.014 g/L of ZnCl 2 , 0.041 g/L of FeCl 2 H 2 O, 0.015 g/L of MnCl 2 , 0.0015 g/L of CuCl 2 , 0.003 g/L of H 3 BO 3 , 0.0025 g/L of Na 2 MoO 4 , 200 mg/L of nitriloacetic acid, 30 μg/L of sodium selenite, and 40 g/L of glycerol) at a temperature of 33° C. and at a rate of 250 rpm. In the beginning of the culture, the expression of 0.05 mM IPTG was induced when OD achieved 0.8 at a wavelength of 600 nm, and then 50 μM of Vitamin B12 was added thereto.
After culturing the culture medium for 24 hours, portions of the culture medium were harvested for measuring OD and pH, thereby identifying production of 3-HP by using HPLC (Waters). Once every 24 hours, the pH of the culture medium was corrected to pH 7.0 by using 4N NaOH. In HPLC analysis, an Aminex HPX-87H (300 mm×7.8 mm) column was used, and 0.5 mM of an aqueous solution of sulfuric acid containing 9% acetonitrile was used in a mobile phase. Here, HPLC had a flow rate of 0.4 ml/min and a temperature of 35° C. in the column. A detector device used a dual mode of RI and UV/VIS (210 nm). Glycerol was detected in 17.5 minutes out of 35 minutes in total.
Table 5 below shows produced amounts of 3-HP according to consumed amounts of glucose of E. coli . The recombinant strain consumed 22.84 g/L of glucose in 24 hours while it produced 0.51 g/L of 3-HP.










TABLE 5





Produced
Produced
Consumed



amounts of
amounts of
amounts of


3-HP
glycerol
glucose


(g/L)
(g/L)
(g/L)
OD












pACYC/hdpA_gldA +
0.51
0
22.84
5.32

pETDuet/

dhaB_gdrAB_gabD4

Control group
0
0
23.03
7.02



























EXAMPLE 3
Evaluation on Manufacture of Microorganisms Introduced with CoA Transferase, 3-HP CoA Dehydratase, and Acyl-CoA Thioester Hydrolase, and on Ability of the Microorganisms to Produce Acrylic Acid
(1) Manufacture of a Vector for Introduction
Genes (i.e., pct of SEQ ID NO: 23) encoding CoA transferase derived from Megasphaera elsdenii ATCC17753 used genome DNA of Megasphaera elsdenii ATCC17753 as a template, and were obtained by PCR amplification using a primer set of pct_F (SEQ ID NO: 39) and pct_R (SEQ ID NO: 40). PCR was performed in 25 cycles, each of which consists of a temperature of 95° C. for 30 seconds, at a temperature of 50° C. for 30 seconds, and a temperature of 72° C. for 3 minutes. The amplification products obtained therefrom were processed with restriction enzymes, i.e., BamHI and SacI, followed by being cloned into a pRSFDuet™-1 vector (Novagen).
In addition, genes (i.e., yciA of SEQ ID NO: 25) encoding acyl-CoA thioester hydrolase derived from E. coli (e.g., E. coli K strains) used genome DNA of the E. coli K strains as a template and were obtained by PCR amplification using a primer set of yciA_F (SEQ ID NO: 41) and yciA_R (SEQ ID NO: 42). PCR was performed in 28 cycles, each of which consists of a temperature of 95° C. for 30 seconds, at a temperature of 50° C. for 30 seconds, and a temperature of 72° C. for 30 minutes. The obtained PCR products were then processed with restriction enzymes such as SacI and HindIII, followed by being cloned into a vector. As a result, a pRSFDuet/pct_yciA vector was obtained.
Genes (i.e., hpd of SEQ ID NO: 27) encoding 3-hydroxypropionyl-CoA derived from Chloroflexus aurantiacus ATCC29365 were obtained by PCR amplification using a primer set of hpdF (SEQ ID NO: 43) and hdpR (SEQ ID NO: 44). PCR was performed in 28 cycles, each of which consists of a temperature of 95° C. for 30 seconds, at a temperature of 54° C. for 30 seconds, and a temperature of 72° C. for 6 minutes. The obtained PCR products were then processed with restriction enzymes such as NdeI and XhoI, followed by being cloned into a vector. As a result, a pRSFDuet/pct_yciA_hpd vector was obtained.
(2) Evaluation on Ability to Produce Acrylic Acid
The pACYC/pct_yciA_hpd vector manufactured in step (1) was transformed into E. coli K (DE3) (pETDuet_dhaB_gdrAB_gabD and pACYC_hdpA_gldA), which is a strain producing 3-HP.
The E. coli to which the vector was introduced was cultured in an M9 minimal medium (1.4 g/L of MgSO 4 H 2 O, 17.4 g/L of K 2 HPO 4 , 3 g/L of KH 2 PO 4 , 4 g/L of (NH 4 ) 2 HPO 4 , 1.7 g/L of citric acid, 0.014 g/L of ZnCl 2 , 0.041 g/L of FeCl 2 H 2 O, 0.015 g/L of MnCl 2 , 0.0015 g/L of CuCl 2 , 0.003 g/L of H 3 BO 3 , 0.0025 g/L of Na 2 MoO 4 , 200 mg/L of nitriloacetic acid, 30 μg/L of sodium selenite, and 40 g/L of glycerol) at a temperature of 30° C. until OB 600 achieved 0.6. 0.02 mM of IPTG was added thereto, and the medium was cultured again at a temperature of 30° C. for 24 hours. Then, the concentration of glycerol produced in the culture medium was measured. The culturing may be performed by shaking the medium in a 250 mL flask, and then the concentration of acrylic acid was calculated using high performance liquid chromatography (HPLC).
After culturing the culture medium for 24 hours, portions of the culture medium were extracted for measuring optical density and pH, thereby identifying production of 3-HP by using HPLC (Waters). Once every 24 hours, the pH of the culture medium was corrected to pH 7.0 by using 4N NaOH. In HPLC analysis, an Aminex HPX-87H (300 mm×7.8 mm) column was used, and 0.5 mM of an aqueous solution of sulfuric acid containing 9% acetonitrile was used in a mobile phase. Here, HPLC had a flow rate of 0.4 ml/min and a temperature of 35° C. in the column. A detector device used a dual mode of RI and UV/VIS (210 nm). Glycerol was detected in 18.2 minutes out of 35 minutes in total.
Table 6 below shows produced amounts of acrylic acid according to consumed amounts of glucose of the E. coli . The recombinant strain consumed 21.84 g/L of glucose in 24 hours while it produced 0.31 g/L of acrylic acid.











TABLE 6





Produced






amount of
Produced
Produced
Consumed


acrylic acid
amount of 3-
amount of
amount of


(g/L)
HP (g/L)
glycerol (g/L)
glucose (g/L)
OD













pACYC/hdpA_gldA +
0.31
0
0
21.84
5.21

pETDuet/

dhaB_gdrAB_gabD +

pRSF/pct_yciA_hdp

Control group
0
0
0
23.03
6.02




























It should be understood that the exemplary embodiments described therein should be considered in a descriptive sense only and not for purposes of limitation. Descriptions of features or aspects within each embodiment should typically be considered as available for other similar features or aspects in other embodiments.
While one or more embodiments of the present invention have been described with reference to the figures, it will be understood by those of ordinary skill in the art that various changes in form and details may be made therein without departing from the spirit and scope of the present invention as defined by the following claims.
All references, including publications, patent applications, and patents, cited herein are hereby incorporated by reference to the same extent as if each reference were individually and specifically indicated to be incorporated by reference and were set forth in its entirety herein.
The use of the terms “a” and “an” and “the” and “at least one” and similar referents in the context of describing the invention (especially in the context of the following claims) are to be construed to cover both the singular and the plural, unless otherwise indicated herein or clearly contradicted by context. The use of the term “at least one” followed by a list of one or more items (for example, “at least one of A and B”) is to be construed to mean one item selected from the listed items (A or B) or any combination of two or more of the listed items (A and B), unless otherwise indicated herein or 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. 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.
Preferred embodiments of this invention are described herein, including the best mode known to the inventors for carrying out the invention. 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.