METABOLIC ENGINEERING FOR PRODUCTION OF LIPOIC ACID
20230123431 · 2023-04-20
Assignee
Inventors
- Matthew Wook Chang (Singapore, SG)
- Binbin CHEN (Singapore, SG)
- Jee Loon Foo (Singapore, SG)
- Hua Ling (Singapore, SG)
Cpc classification
C12P7/40
CHEMISTRY; METALLURGY
C12P11/00
CHEMISTRY; METALLURGY
Y02A50/30
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
International classification
C12P11/00
CHEMISTRY; METALLURGY
Abstract
The present invention provides for a method to increase the free lipoic acid production in an isolated genetically engineered bacteria or yeast cell. The method involves culturing in a cysteine supplemented culture medium the engineered bacteria or yeast that is transformed with a recombinant expression vector encoding polynucleotide molecules that results in the overexpression of the following genes that are linked to at least one promoter: (1) substrate protein (e.g. Gcv3p); (2) octanoyltransferase or lipoyl synthase; (3) cofactor S-adenosyl methionine synthase; and (4) lipoamidase. The invention also relates to the engineered bacteria or yeast cell thereof.
Claims
1. An isolated genetically engineered bacteria or yeast cell, wherein the cell has been transformed by at least one polynucleotide molecule; the at least one polynucleotide molecule comprising lipoic acid pathway genes which encode an octanoyltransferase, a lipoyl synthase, a protein substrate that is lipoylated, a lipoamidase and/or an S-adenosylmethionine synthase, operably linked to at least one promoter, wherein at least one lipoic acid pathway gene is heterologous and said genetically engineered bacteria or yeast cell is capable of increased production of free lipoic acid compared to a non-transformed cell.
2. The isolated genetically engineered bacteria or yeast cell of claim 1, wherein the protein substrate that is lipoylated is selected from a group comprising Gcv3p (H protein of the glycine cleavage system), Lat1p and Kgd2p.
3. The isolated genetically engineered bacteria or yeast cell of claim 1, wherein the S-adenosylmethionine synthase is from a cell selected from a group comprising Kluyveromyces, Candida, Pichia, Yarrowia, Debaryomyces, Saccharomyces spp., and Schizosaccharomycespombe.
4. The isolated genetically engineered bacteria or yeast cell of claim 1, wherein the lipoic acid pathway genes comprise at least one gene selected from the group consisting of: LIP2 (octanoyltransferase), LIP5 (lipoyl synthase), GCV3 (H protein of the glycine cleavage system), LPA (lipoamidase), SAM1 and/or SAM2.
5. The isolated genetically engineered bacteria or yeast cell of claim 1, wherein the lipoic acid pathway genes are expressed in mitochondria.
6. The isolated genetically engineered bacteria or yeast of claim 2, wherein the lipoic acid pathway genes are expressed in the mitochondria by virtue of a mitochondrial targeting peptide (MTP).
7. The isolated genetically engineered bacteria or yeast of claim 6, wherein the mitochondrial targeting peptide (MTP) for LPA, Sam1 and/or Sam2 is from yeast cytochrome c oxidase subunit IV (COX4).
8. The isolated genetically engineered yeast of claim 1, wherein the yeast is selected from a group comprising Kluyveromyces, Candida, Pichia, Yarrowia, Debaryomyces, Saccharomyces spp., and Schizosaccharomyces pombe.
9. The isolated genetically engineered bacteria or yeast of claim 1, wherein said at least one promoter is a constitutive promoter.
10. The isolated genetically engineered bacteria or yeast of claim 1, wherein said lipoic acid pathway genes are expressed from one or more plasmids.
11. The isolated genetically engineered bacteria or yeast of claim 1, wherein at least one of said lipoic acid pathway genes is integrated into the bacteria or yeast genome.
12. The isolated genetically engineered bacteria or yeast of claim 1, wherein the lipoamidase is from Enterococcus faecalis (EfLPA).
13. The isolated genetically engineered bacteria or yeast of claim 4, wherein the LIP2, LIP5, GCV3, LPA, SAM1 and/or SAM2 genes respectively encode an amino acid sequence comprising SEQ ID NO: 1, SEQ ID NO: 3, SEQ ID NO: 5, SEQ ID NO: 7, SEQ ID NO: 9 and/or SEQ ID NO: 11.
14. The isolated genetically engineered bacteria or yeast of claim 4, wherein the LIP2, LIP5, GCV3, LPA, SAM1 and/or SAM2 genes respectively comprises a polynucleotide sequence having at least 70% sequence identity, at least 80% sequence identity, at least 90% sequence identity or 100% sequence identity to SEQ ID NO: 2, SEQ ID NO: 4, SEQ ID NO: 6, SEQ ID NO: 8, SEQ ID NO: 10 and/or SEQ ID NO: 12.
15. A recombinant expression vector comprising one or more heterologous lipoic acid pathway genes defined in claim 1, operably linked to a promoter, wherein an expressed protein from said pathway genes is located to the mitochondria.
16. The recombinant vector of claim 15, wherein said promoter is a constitutive promoter.
17. A method of producing free lipoic acid in a genetically engineered cell, comprising the steps: a) culturing a plurality of genetically engineered cells of claim 1 in medium under conditions for lipoic acid biosynthesis, and b) supplementing the medium with cysteine, wherein said genetically engineered cell is capable of increased production of free lipoic acid compared to a non-transformed cell.
18. The method of claim 17, wherein the medium is supplemented with cysteine at a concentration of at least 0.05 mg/ml, at least 0.1 mg/ml, at least 0.2 mg/ml, at least 0.5 mg/ml or in the range from 0.05 mg/ml to 0.7 mg/ml, preferably in the range 0.1 mg/ml to 0.4 mg/ml.
19. The method of claim 17, further comprising isolating said free lipoic acid.
20. The method of claim 17, wherein the engineered cell is a yeast cell.
21. The method of claim 20, wherein the engineered cell is Saccharomyces cerevisiae.
Description
BRIEF DESCRIPTION OF THE FIGURES
[0029]
[0030]
[0031]
[0032]
[0033]
[0034]
[0035]
DETAILED DESCRIPTION OF THE INVENTION
[0036] Bibliographic references mentioned in the present specification are for convenience listed in the form of a list of references and added at the end of the examples. The whole content of such bibliographic references is herein incorporated by reference. Any discussion about prior art is not an admission that the prior art is part of the common general knowledge in the field of the invention.
Definitions
[0037] Certain terms employed in the specification, examples and appended claims are collected here for convenience.
[0038] It must be noted that as used herein and in the appended claims, the singular forms “a”, “an”, and “the” include plural reference unless the context clearly dictates otherwise.
[0039] As used herein, the term “comprising” or “including” is to be interpreted as specifying the presence of the stated features, integers, steps or components as referred to, but does not preclude the presence or addition of one or more features, integers, steps or components, or groups thereof. However, in context with the present disclosure, the term “comprising” or “including” also includes “consisting of”. The variations of the word “comprising”, such as “comprise” and “comprises”, and “including”, such as “include” and “includes”, have correspondingly varied meanings.
[0040] The terms “nucleotide”, “nucleic acid” or “nucleic acid sequence”, as used herein, refer to an oligonucleotide, polynucleotide, or any fragment thereof, to DNA or RNA of genomic or synthetic origin which may be single-stranded or double-stranded and may represent the sense or the antisense strand, to peptide nucleic acid (PNA), or to any DNA-like or RNA-like material.
[0041] As used herein, the term “operably linked” means that the components to which the term is applied are in a relationship that allows them to carry out their inherent functions under suitable conditions. For example, a control sequence which is “operably linked” to a protein coding sequence is ligated thereto, so that expression of the protein coding sequence is achieved under conditions compatible with the transcriptional activity of the control sequences. By way of an example, a first nucleic acid sequence is operably linked with a second nucleic acid sequence when the first nucleic acid sequence is placed in a functional relationship with the second nucleic acid sequence. For instance, a promoter is operably linked to a coding sequence if the promoter affects the transcription or expression of the coding sequence. Generally, operably linked DNA sequences are contiguous and, where necessary to join two protein-coding regions, in the same reading frame.
[0042] The terms “amino acid” or “amino acid sequence,” as used herein, refer to an oligopeptide, peptide, polypeptide, or protein sequence, or a fragment of any of these, and to naturally occurring or synthetic molecules. Where “amino acid sequence” is recited herein to refer to an amino acid sequence of a naturally occurring protein molecule, “amino acid sequence” and like terms are not meant to limit the amino acid sequence to the complete native amino acid sequence associated with the recited protein molecule.
[0043] As used herein, the terms “polypeptide”, “peptide” or “protein” refer to one or more chains of amino acids, wherein each chain comprises amino acids covalently linked by peptide bonds, and wherein said polypeptide or peptide can comprise a plurality of chains noncovalently and/or covalently linked together by peptide bonds, having the sequence of native proteins, that is, proteins produced by naturally-occurring and specifically non-recombinant cells, or genetically-engineered or recombinant cells, and comprise molecules having the amino acid sequence of the native protein, or molecules having deletions from, additions to, and/or substitutions of one or more amino acids of the native sequence. A “polypeptide”, “peptide” or “protein” can comprise one (termed “a monomer”) or a plurality (termed “a multimer”) of amino acid chains.
[0044] Media suitable for lipoic acid biosynthesis include LB broth, YPD, 2YT, and any other suitable culture media. The culture medium may include antibiotics such as ampicillin, kanamycin, chloramphenicol, Isopropyl p-D-1-galactopyranoside (IPTG), and L-arabinose. A person skilled in the art would know appropriate concentrations for each component.
[0045] A vector can include one or more catalytic enzyme nucleic acid(s) in a form suitable for expression of the nucleic acid(s) in a host cell. Preferably the recombinant expression vector includes one or more regulatory sequences operatively linked to the nucleic acid sequence(s) to be expressed. The term “regulatory sequence” includes promoters, enhancers, ribosome binding sites and/or IRES elements, and other expression control elements (e.g., polyadenylation signals). 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 protein desired, and the like. The expression vectors of the invention can be introduced into host cells to thereby produce proteins or polypeptides, including fusion proteins or polypeptides, encoded by nucleic acids as described herein (e.g., catalytic enzyme proteins).
[0046] The recombinant expression vectors of the invention can be designed for expression of catalytic enzyme proteins in prokaryotic or eukaryotic cells, more particularly prokaryotic cells. For example, polypeptides of the invention can be expressed in bacteria (e.g., cyanobacteria) or yeast cells. Suitable host cells are discussed further in Goeddel, (1990) Gene Expression Technology: Methods in Enzymology 185, Academic Press, San Diego, Calif.Having now generally described the invention, the same will be more readily understood through reference to the following examples which are provided by way of illustration, and are not intended to be limiting of the present invention.
[0047] A person skilled in the art will appreciate that the present invention may be practiced without undue experimentation according to the methods given herein. The methods, techniques and chemicals are as described in the references given or from protocols in standard biotechnology and molecular biology textbooks.
EXAMPLES
Example 1
Materials and Methods
Strains and Media
[0048] E. coli TOP10 (Invitrogen) and Luria-Bertani (Becton, Dickinson and Company) were used for cloning experiments unless otherwise stated. 100 mg/L ampicillin was used for selection of positive colonies where applicable. The yeast strain S. cerevisiae BY4741 (ATCC) was used for genetic engineering for lipoic acid production.
[0049] S. cerevisiae BY4741 wild-type and mutant strains were cultured in rich medium YPD/YPGR (1% yeast extract, 2% peptone, and 2% D-glucose or 2% galactose with 1% raffinose), synthetic minimal medium lacking uracil SC-U (0.67% yeast nitrogen base, 0.192% uracil dropout and 2% D-glucose), medium lacking lysine SC-L (0.67% yeast nitrogen base, 0.18% lysine dropout and 2% D-glucose), medium lacking leucine SC-LE (0.67% yeast nitrogen base, 0.16% leucine dropout and 2% D-glucose), or medium lacking both leucine and uracil SC-LU (0.67% yeast nitrogen base, 0.154% leucine and uracil dropout, and 2% D-glucose). 2% agar was supplemented for making solid media. Yeast growth media components were purchased from Sigma-Aldrich, MP Biomedicals and BD (Becton, Dickinson and Company). 5-Fluoroorotic acid (5-FOA, Fermentas) or geneticin (G418, PAA Laboratories) was used for selection. Cysteine (0.2 mg/mL) and ferrous sulfate (0.2 mg/mL) (Sigma-Aldrich) were supplemented into growth culture where necessary. Yeast cells were cultivated at 30° C. in flasks and shaken at 225 rpm.
Plasmid Construction and Gene Integration
[0050] EfLPA gene (GenBank Accession No. AY735444) was codon-optimized for S. cerevisiae and synthesized by Integrated DNA Technologies. EfLPA genes with and without mitochondrial targeting peptide (MTP) sequence were ligated between P.sub.GAL1 promoter and T.sub.CYC1 terminator, which were amplified from the S. cerevisiae genomic DNA. EfLPA expression cassettes with and without MTP were inserted to the vector pRS41K (Euroscarf), resulting in plasmids pRS41K-P.sub.GAL1-mEfLPA-T.sub.CYC1 and pRS41K-P.sub.GAL1-EfLPA-T.sub.CYC1, respectively. The plasmids pRS41K-P.sub.GAL1-mEGFP-T.sub.CYC1 and pRS41K-P.sub.GAL1-EGFP-T.sub.CYC1 were similarly constructed for EGFP with and without MTP, respectively. The constructed recombinant plasmids are listed in Table 1. The list of primers used was shown in Table 2.
TABLE-US-00001 TABLE 1 Strains and plasmids used in this study Strains or plasmids Description Source Strains E. coli Top10 F.sup.− mcrA Δ(mrr-hsdRMS-mcrBC) φ80lacZΔM15 1 ΔlacX74 recA1 araD139 Δ(ara-leu)7697 galU galK rpsL(Str.sup.R) endA1 nupG S. cerevisiae BY4741 MATa his3Δ1 leu2Δ0 met15Δ0 ura3Δ0 2 BY4741-GCV3 BY4741 with P.sub.TEF1-GCV3-T.sub.CYC1 (lys2 site) 3 BY4741-LAT1 BY4741 with P.sub.TEF1-LAT1-T.sub.ADH1 (lys2 site) 3 BY4741-KGD2 BY4741 with P.sub.TEF1-KGD2-T.sub.KGD2 (lys2 site) 3 BY4741-control BY4741 with plasmid pRS41K 3 BY4741-EfLPA BY4741 with plasmid pRS41K-P.sub.GAL1-EfLPA-T.sub.CYC1 3 BY4741-mEfLPA BY4741 with plasmid pRS41K-P.sub.GAL1-mEfLPA-T.sub.CYC1 3 BY4741-EGFP BY4741 with plasmid pRS41K-P.sub.GAL1-EGFP-T.sub.CYC1 3 BY4741-mEGFP BY4741 with plasmid pRS41K-P.sub.GAL1-mEGFP-T.sub.CYC1 3 BY4741-GCV3- BY4741 with P.sub.TEF1-GCV3-T.sub.CYC1 (lys2 site) and plasmid 3 mEfLPA pRS41K--P.sub.GAL1-mEfLPA-T.sub.CYC1 BY4741-GCV3- BY4741 with P.sub.TEF1-GCV3-T.sub.CYC1 (lys2 site), P.sub.TEF1-LIP2- 3 LIP2-LIP5--mEfLPA T.sub.LIP2 (CS6 site), P.sub.PGI1-LIP5-T.sub.LIP5 (CS6 site) and plasmid pRS41K-P.sub.GAL1-mEfLPA-T.sub.CYC1 BY4741-GCV3- BY4741 with P.sub.TEF1-GCV3-T.sub.CYC1 (lys2 site), P.sub.TEF1-LIP2-T.sub.LIP2 3 LIP2-LIP5--mSAM1- (CS6 site), P.sub.PGI1-LIP5-T.sub.LIP5 (CS6 site), P.sub.ADH1-mSAM1-T.sub.SAM1 mEfLPA (CS8) and plasmid pRS41K--P.sub.GAL1-mEfLPA-T.sub.CYC1 BY4741-GCV3- BY4741 with P.sub.TEF1-GCV3-T.sub.CYC1 (lys2 site), P.sub.TEF1-LIP2- 3 LIP2-LIP5--mSAM2- T.sub.LIP2 (CS6 site), P.sub.PGI1-LIP5-T.sub.LIP5 (CS6 site), P.sub.ADH1- mEfLPA mSAM2-T.sub.SAM2 (CS8) and plasmid pRS41K-P.sub.GAL1- mEfLPA-T.sub.CYC1 Plasmids pIS385 AmpR, URA3 4 pRS41K ARS/CEN origin, kanMX 4 pRS41K-P.sub.GAL1- pRS41K carrying EfLPA under P.sub.GAL1 control 3 EfLPA-T.sub.CYC1 pRS41K-P.sub.GAL1- pRS41K carrying MTP-EfLPA under P.sub.GAL1 control 3 mEfLPA-T.sub.CYC1 pRS41K-P.sub.GAL1- pRS41K carrying EGFP under P.sub.GAL1 control 3 EGFP-T.sub.CYC1 pRS41K-P.sub.GAL1- pRS41K carrying MTP-EGFP under P.sub.GAL1 control 3 mEGFP-T.sub.CYC1 1. Invitrogen; 2. ATCC; 3. This study; 4. Euroscarf
TABLE-US-00002 TABLE 2 Primers used in this study. Restriction sites are in bold. SEQ Primers Primer Sequence 5’-3’ ID NO P.sub.GAL1-F AAACGAGCTCAGTACGGATTAGAAGCC 13 P.sub.GAL1-R TTTTTAGGGTTTTTTCTCCTTGACGTT 14 T.sub.CYC1-F ATCCGCTCTAACCGAAAAGG 15 T.sub.CYC1-R AAACGAGCTCCTTCGAGCGTCCCAAAACC 16 EfLPA-F CGTCAAGGAGAAAAAACCCTAAAAAATGCTAGCCCAAGAA 17 mEfLPA- CGTCAAGGAGAAAAAACCCTAAAAAATGCTTTCACTACGTCAATCT 18 F ATAAGATTTTTCAAGCCAGCCACAAGAACTTTGTGTAGCTCTAGAT ATCTGCTTCAGCAAAAACCCATGCTAGCCCAAGAA EfLPA-R CTAACTCCTTCCTTTTCGGTTAGAGCGGATTCATTAATGGTGATGG 19 TGATGATGCTTACGGGTCTTTCTAATGTAGA EGFP-F CGTCAAGGAGAAAAAACCCTAAAAAATGTCTAAAGGTGAA 20 mEGFP- CGTCAAGGAGAAAAAACCCTAAAAAATGCTTTCACTACGTCAATCT 21 F ATAAGATTTTTCAAGCCAGCCACAAGAACTTTGTGTAGCTCTAGAT ATCTGCTTCAGCAAAAACCCATGTCTAAAGGTGAA EGFP-R CTAACTCCTTCCTTTTCGGTTAGAGCGGATTCATTAATGGTGATGG 22 TGATGATGTTTGTACAATTCATC P.sub.TEF1-F ACCGCTCGAGCATAGCTTCAAAATGTTTCTACTCCTTT 23 P.sub.TEF1-R TTGTAATTAAAACTTAGATTAGATTGC 24 GCV3-F GCAATCTAATCTAAGTTTTAATTACAAATGTTACGCACTACTAGACT 25 ATGG GCV3-R CTAACTCCTTCCTTTTCGGTTAGAGCGGATTCATTAATGGTGATGG 26 TGATGATGGTCATCATGAACCAGTGT KGD2-F GCAATCTAATCTAAGTTTTAATTACAAATGCTTTCCAGAGCGACG 27 KGD2-R ATCAGATTGGTATGGGCTGCAAATTTCAAATCATTAATGGTGATGG 28 TGATGATGCCATAACAACATTTTTCTAG T.sub.KGD2-F TTTGAAATTTGCAGCCCATAC 29 T.sub.KGD2-R ATTCGAGCTCATGTGGAAATCAAAAGAATATTAGTTGAT 30 LAT1-F GCAATCTAATCTAAGTTTTAATTACAAATGTCTGCCTTTGTCAGGGT 31 G LAT1-R TAATAAAAATCATAAATCATAAGAAATTCGTCATTAATGGTGATGGT 32 GATGATGCAATAGCATTTCCAAAGGAT T.sub.ADH1-F CGAATTTCTTATGATTTATGATTTTTA 33 T.sub.ADH1-R ACGCGGATCCGAGCGACCTCATGCTATACCT 34 LIP2- AACCTCGAGGAGAAGTTTTTTTACCCCTCTCCACAGATCCTCGAGC 35 LIP5- ATAGCTTCAAAATGTTTCTAC CS6-F LIP2- TAATTAGGTAGACCGGGTAGATTTTTCCGTAACCTTGGTGTCGAGC 36 LIP5- TCACGCATTTTTTTCTTTTGC CS6-R SAM1/2- CAAAATTACCTACGGTAATTAGTGAAAGGCCAAAATCTAATGTTAC 37 CS8-F AATAGTATACTAGAAGAATGAGCCAAG SAM1- GACCGTTCCCTTGTGTTGTACCAGTGGTAGGGTTCTTCTCGGTAG 38 CS8-R CTTCTATAAGATAAAGTTTGGTTTGTTGATC SAM2- GACCGTTCCCTTGTGTTGTACCAGTGGTAGGGTTCTTCTCGGTAG 39 CS8-R CTTCTCCTCAAAGACATTCTATATTTCAACC
[0051] Chromosomal integration of the expression cassettes P.sub.TEF1-GCV3-T.sub.CYC1, P.sub.TEF1-KGD2-T.sub.KGD2 and P.sub.TEF1-LAT1-T.sub.ADH1 into the LYS2 site were conducted based on the method previously described by Sadowski et al. (Sadowski et al., Yeast 24: 447-455 (2007)), where the integrative vector pIS385 (Euroscarf) containing URA3 selectable marker was used for integration. In addition, the cassettes P.sub.TEF1-LIP2-T.sub.LIP2 and P.sub.PGI1-LIP5-T.sub.LIP5 were integrated into intergenic site CS6 while P.sub.ADH1-mSAM1-T.sub.SAM1 and P.sub.ADH1-mSAM2-T.sub.SAM2 were integrated into intergenic site CS8 (Xia et al., ACS Synthetic Biology 6: 276-283 (2017)) based on Clustered Regularly Interspaced Short Palindromic Repeats (CRISPR) and CRISPR-associated (Cas) system previously established (DiCarlo et al., Nucleic Acids Research 41: 4336-4343 (2013)). To clone GCV3, LAT1, KGD2, LIP2, LIP5, SAM1 and SAM2, genomic DNA of S. cerevisiae was used as the PCR template. All proteins abovementioned were located to the mitochondria through its native MTP (for Gcv3p, Lat1p and Kgd2p) or MTP from yeast cytochrome c oxidase subunit IV (COX4) (for mEfLPA, mSam1p and mSam2p) (Maarse et al., The EMBO Journal 3: 2831-2837 (1984)). Hexa-histidine tag was added to either the C- or N-terminus of these proteins for expression analysis. Oligonucleotide primers used are listed in Table 2.
Detection of Lipoylated and Octanoylated Proteins
[0052] Cells were pre-cultured in 5 ml yeast extract peptone dextrose (YPD) medium overnight and then diluted in 100 ml YPD medium using 500 ml flask to achieve an initial OD.sub.600 of 0.4. After growth for 18 h, cells were harvested by centrifugation. Cell pellets were re-suspended in 25 ml lysis buffer (0.3 M NaCl, 50 mM sodium phosphate, pH 6.5). Cells were lysed with a high-pressure homogenizer (EmulsiFlex-C3, AVESTIN, Inc.) at 25000 psi. The soluble cell lysate was collected by centrifugation and mixed an equal volume of 8 M Guanidine hydrochloride. 300 μl final products were injected into Agilent 1260 Infinity binary HPLC (Agilent). The proteins were resolved with an mRP-C18 High-Recovery Protein column (Agilent) at a solvent flow rate of 1.5 ml/min and column temperature of 80° C. The mobile phases A and B were 0.1% trifluoroacetic acid/water and 0.1% trifluoroacetic acid/acetonitrile respectively. The proteins were eluted with the following gradient: 0-1 min (10%-30% B), 1-12 min (30%-50% B), 12-13 min (50%-80% B), 13-14 min (80% B), 14-15 min (80%-10% B) and 15-17 min (10% B). Protein collection started from 1 min and 12 successive 1-min fractions were collected. The proteins were dried overnight in a Speedvac concentrator (Thermo Fisher Scientific). Each fraction of proteins was re-suspended with 50 μl 0.5 M triethylammonium bicarbonate with 1 μg Glu-C(Promega). The mixture was incubated overnight.
[0053] 7 μl digested peptides was loaded into Agilent 1260 infinity HPLC-Chip/MS System (Agilent) equipped with a PortID-Chip-43 (II) column (Agilent). A linear gradient of acetonitrile was used to elute the peptides from the HPLC-Chip system at a consistent flow rate of 0.35 μl/min. For LC separation, 0.2% formic acid/water (mobile phase A) and 0.2% formic acid/acetonitrile (mobile phase B) were used. The samples were eluted with the following gradient through a nano pump: 0-1 min (7%-10% B), 1-35 min (10%-30% B), 35-37 min (30%-80% B), 37-38 min (80% B), 38-40 min (80%-7% B) and 40-43 min (7% B). The eluted samples were directly infused into a mass spectrometer for detection. The mass spectra were scanned in the range of 100-1600 m/z with a scan rate of 3 spectra per second. The MS/MS scan range is 80-2000 m/z with a scan rate of 4 spectra per second. Mass data was collected in positive ion mode at a fragmentor voltage of 175 V and skimmer voltage of 65 V.
Peptide Post-Translational Modification (PTM) Analysis
[0054] The SPIDER feature of PEAKS 8 software (Bioinformatics Solutions Inc., Waterloo, Canada) (Zhang et al., Molecular & Cellular Proteomics: MCP 11: M111.010587 (2012)) was used to identify the peptides with PTMs based on mass difference. The yeast peptides were searched with the following search parameters. The precursor mass error tolerance was 100 ppm (part-per-million) while the fragment mass error tolerance was 0.1 Da. The fixed PTM was carbamidomethylation(C) (+57.02) and variable PTMs were lipoyl (K) (+188.03), octanoyl (TS) (+126.10), oxidation (M) (+15.99) and oxidation (HW) (+15.99). The peptide and protein identification reliability score (−10lgP, where P is the probability of identification) was set at a threshold of 15 and 20 respectively, corresponding to confident identifications.
The Database Used was UniProtKB/Swiss-Prot.
[0055] Protein modeling for structure visualization SWISS-MODEL (Waterhouse et al., Nucleic Acids Research 46: W296-W303 (2018)) was used to build the 3D structure models of Gcv3p, Kgd2p and Lat1p proteins from their amino acid sequences using homology modelling techniques. The structures were predicted based on templates available in the SWISS-MODEL template library (SMTL) which aggregates information of experimental structures from Protein Data Bank (PDB). PyMOL Molecular Graphics System (Schrödinger, Inc., New York, USA) (Schrödinger, “The PyMOL Molecular Graphics System, Version 1.8” (2015)) was used to observe the structures.
[0056] Template homologue proteins with 41%, 37% and 48% sequence identity were used for modelling of Gcv3p, Kgd2p and Lat1p, respectively. The template protein for Gcv3p is glycine cleavage system protein H from Mycobacterium tuberculosis (PDB chain id: 3hgb.1.A), while for Kgd2p and Lat1p, only the N-termini (lipoyl domains) were modelled due to the lack of templates with crystal structure of full length. The template for the N-terminus (lipoyl domain) of Kgd2p is the lipoyl domain of E2 component of 2-oxoglutarate dehydrogenase complex in Azotobacter vinelandii (PDB chain id: 1ghj.1.A). The N-terminus of Lat1p (lipoyl domain) was modelled using the dihydrolipoyllysine-residue acetyltransferase component of the pyruvate dehydrogenase complex in Homo sapiens (PDB chain id: 1y8n.1.B).
Protein Overexpression and Purification
[0057] Cells were pre-cultured in 5 ml medium overnight and then diluted in 50 ml induction medium using 200 ml flask to achieve an initial OD.sub.600 of 0.4. After overnight cell growth, the yeast cells were harvested by centrifugation. The cell pellets were re-suspended in lysis buffer (0.5 M NaCl, 20 mM sodium phosphate, 20 mM imidazole, pH 6.8) and lysed with a high-pressure homogenizer (EmulsiFlex-C3, AVESTIN, Inc.) at 25000 psi. After centrifugation, the insoluble protein and cell debris were separated from the soluble protein. To check protein expression, the soluble protein was boiled with Laemmli sample buffer (Bio-Rad) and separated on an SDS-polyacrylamide gel. The proteins in the gels were transferred onto western blotting membrane and using HRP conjugated anti-6x His-tag antibody (ThermoFisher Scientific) as described previously (Chen et al., Biotechnology for Biofuels 6: 21 (2013)). To detect protein expressed in the mitochondria, mitochondrial proteins were extracted using yeast mitochondria isolation kit (Biovision). The extracted proteins will be boiled with Laemmli sample buffer and detected through western blotting as described.
[0058] To purify the proteins, the soluble proteins were incubated with Nickel-IMAC resin (GE Healthcare) overnight for protein binding. After protein binding and washing, the His-tagged proteins were eluted with elution buffer (0.5 M NaCl, 20 mM sodium phosphate, 300 mM imidazole, pH 6.8). Protein concentrator (Thermo Scientific) was used to exchange the elution buffer with PBS buffer for downstream protein activity test.
Free Lipoic Acid Detection
[0059] The extraction and detection of free lipoic acid using the LC-MS/MS method developed by Chng et al. (Chng et al., Journal of Pharmaceutical and Biomedical Analysis 51: 754-757 (2010)) with modifications. Equal volume of acetonitrile was added to the supernatant of cell culture or lysate. The mixture was vortex-mixed for 2 min. After cooling at −30° C. for 30 min, the upper phase containing lipoic acid was transferred to a clean tube for evaporation to dryness. The residue was reconstituted with 200 μl of 50% acetonitrile in water. The extracted lipoic acid sample was injected into an LC-MS/MS system (Agilent 1290 liquid chromatograph and Agilent 6550 iFunnel Q-TOF) in negative mode. Chromatographic separation was achieved with an Agilent Eclipse Plus C18 column (2.1×100 mm, 1.8 μm, Agilent) at a flow rate of 0.7 ml/min by gradient solution at 0-5.8 min (80%-68% A), 5.8-6.5 min (68%-15% A) and 6.5-7 min (15%-95% A). Mobile phase A is 0.1% acetic acid (pH 4 adjusted with ammonia hydroxide solution) and mobile phase B is acetonitrile. Nebulizer was set at 40 psig, while sheath gas flow rate is 11 l/min. The optimized collision energy for lipoic acid is 8 eV. Quantification was achieved by using 2-propylvaleric Acid (Tokyo Chemical Industry Co., Ltd.) as an internal standard.
[0060] Gas chromatography-mass spectrometry (GC-MS) was also used to confirm the identity of lipoic acid. Briefly, HPLC grade ethyl acetate (Sigma) was added to either the supernatant of the cell culture or lysate to extract lipoic acid. The mixture was separated into two phases by centrifugation. The upper phase containing lipoic acid was mixed with N,O-bis(trimethylsilyl)trifluoroacetamide (BSTFA) containing 1% trimethylchlorosilane at a ratio 4:1. The derivatized lipoic acid was analyzed using GC-MS under the following conditions. An HP-5 ms column (30 m by 0.25 mm; 0.25 μm film; Agilent) was used with a helium flow rate set to 1 ml/min. Injections of 1 μl were carried out under splitless injection condition with the inlet set to 250° C. The GC temperature profile was as follows: an initial temperature of 45° C. was maintained for 2 min, followed by ramping to 280° C. at a rate of 10° C./min, where the temperature was held for 3.5 min. The mass spectrometer detector was scanned from 30 to 800 amu in the electron ionization (EI) mode. To aid peak identification, authentic lipoic acid (Sigma) standard was used as reference.
Fluorescence Microscopy
[0061] S. cerevisiae BY4741 cells carrying the plasmids pRS41K-P.sub.GAL1-EGFP-T.sub.CYC1 and pRS41K-P.sub.GAL1-mEGFP-T.sub.CYC1 were grown to early logarithmic phase in induction medium (YPGR with 200 mg/L G418). The cells were harvested and mounted on a poly-L-lysine-coated glass slide. EGFP fluorescence was visualized with a fluorescent microscope (Leica DMi8).
Example 2
[0062] Proteomic analysis and characterization of lipoylated proteins as substrates for free lipoic acid biosynthesis
[0063] To engineer the yeast for free lipoic acid biosynthesis, we first aimed to evaluate the availability of the various forms of lipoate-bound proteins and understand their formation process. We hypothesized that this would facilitate our selection of a suitable lipoylated protein as substrate for subsequent enzymatically cleavage by EfLPA at the amide linkage to release free lipoic acid. Lipoic acid exists covalently bound to proteins via an amide linkage in S. cerevisiae. It was hypothesized that its biosynthesis begins with the transfer of an octanoyl moiety from octanoyl-ACP to the apo form of lipoate-dependent proteins, followed by modification of the octanoyl moiety by insertion of two sulfur atoms (Schonauer et al., Journal of Biological Chemistry 284: 23234-23242 (2009)). As lipoic acid is mainly bound to three proteins, namely Gcv3p, Lat1p and Kgd2p, we sought to focus our analysis on these proteins through LC-MS/MS to better our understanding of the protein lipoylation mechanism.
[0064] To investigate the lipoylation of Gcv3p, Lat1p and Kgd2p, we extracted the total protein from S. cerevisiae and separated the proteins into 12 fractions by HPLC with reverse phase column to reduce the complexity of our protein samples. Instead of using trypsin and chymotrypsin reported previously to generate long peptide fragments (Gey et al., PLoS one 9:e103956 (2014)), in this study, each protein sample was digested with Glu-C leading to shorter peptides which gives better precision. The digested peptide mixtures were analyzed by LC-MS/MS. In total, 2,713 peptides were identified based on their m/z value and MS/MS spectra. As shown in
[0065] In addition to lipoylated peptides, we also observed octanoylated peptides in Gcv3p that likely originated from precursors of lipoate-proteins. Detection of two singly charged peptides with m/z 833.4583 and 833.4628 indicates single octanoyl modification of the Gcv3p fragment at the S.sup.100 (serine.sup.100) (.sup.100SVKSASE.sup.106; SEQ ID NO: 43) or S.sup.103 position (.sup.100SVKSASE.sup.106; SEQ ID NO: 44), respectively (
[0066] To elucidate the protein structural characteristics and visualize the locations of the octanoylation and lipolylation sites, we predicted the structures of Gcv3p, Kgd2p and Lat1p by homology modeling (
Example 3
In Vitro Characterization of EfLPA for Free Lipoic Acid Biosynthesis
[0067] Free lipoic acid is produced by enzymatic cleavage of the amide bond linking the lipoyl moiety to the lysine of lipoate-dependent proteins with a lipoamidase. EfLPA from E. faecalis was previously shown to release lipoic acid from lipoate-modified proteins in E. coli (Spalding and Prigge, PLoS one 4: e7392 (2009)). Lipoic acid is mainly bound to three proteins, namely Gcv3p, Lat1p and Kgd2p in yeast as demonstrated in
[0068] To test the catalytic activity of EfLPA towards lipoylated proteins from yeast, EfLPA with hexa-histidine tag was expressed under the strong galactose-inducible P.sub.GAL1 promoter from a low copy-number plasmid. Lipoate-bound proteins (i.e. Gcv3p, Kgd2p and Lat1p) fused with a hexa-histidine tag were expressed individually under the strong constitutive promoter P.sub.TEF1 from the genome. As shown in
[0069] To determine whether EfLPA possesses broad-range lipoamidase activity towards lipoylated proteins from yeast, purified Gcv3p, Kgd2p and Lat1p proteins were incubated with purified EfLPA individually at 37° C. for 2 h. The extracted products from the enzymatic reaction mixtures were analyzed by LC-MS/MS. No lipoic acid was detected in the control reaction mixture containing EfLPA, Gcv3p, Kgd2p or Lat1p only. Interestingly, no lipoic acid was observed in the reaction mixtures containing EfLPA with Kgd2p or Lat1p individually. Only the reaction of EfLPA with Gcv3p resulted in a peak with m/z 205.0360 (
[0070] Taken together, the in vitro results show that Gcv3p, being a better substrate for EfLPA compared to Lat1p and Kgd2p, is the most suitable protein substrate out of the three candidates for subsequent pathway engineering to optimize free lipoic acid biosynthesis. Moreover, Gcv3p is a smaller protein than Kgd2p and Lat1p (19 kDa, 50 KDa and 52 kDa, respectively), and thus its overexpression utilizes less resource than the latter proteins. Furthermore, unlike the formation of lipoate-Gcv3p, lipoylation of Kgd2p and Lat1p requires an additional enzyme, i.e. Lip3p, which might reduce the efficiency of lipoylation and increase metabolic burden if LIP3 overexpression is additionally required. In summary, we established that EfLPA is functionally expressed in S. cerevisiae and has activity on Gcv3p, which we therefore selected as the preferred lipoylated protein substrate. These enzymes were employed for subsequent engineering of S. cerevisiae to overproduce free lipoic acid in vivo.
Example 4
Overexpression of EfLPA in the Mitochondria LED to Lipoic Acid Biosynthesis In Vivo
[0071] As mentioned, lipoic acid synthesis occurs in the mitochondria of yeast. To enable lipoic acid biosynthesis in vivo, EfLPA must be translocated to the mitochondria where it hydrolyzes lipoic acid from lipoylated protein substrates. To this end, a 29-amino-acid mitochondrial targeting peptide (MTP) from the yeast cytochrome c oxidase subunit IV (COX4) (Maarse et al., The EMBO Journal 3: 2831-2837 (1984)) was explored for translocating proteins to the mitochondria. As shown in
[0072] We evaluated the in vivo activity of the EfLPA in mitochondria by quantifying the lipoic acid concentrations in cell cultures grown for 3 d. We found that the wild-type BY4741 with empty plasmid and BY4741 expressing EfLPA without MTP produced no detectable lipoic acid, whilst the BY4741-mEfLPA strain expressing EfLPA in the mitochondria produced free lipoic acid at 10.1 μg/L (
Example 5
Expression of Pathway Enzymes and Regeneration of Cofactor Improved Lipoic Acid Production
[0073] The overall genetic engineering for lipoic acid production in vivo is shown in
[0074] The catalytic enzyme Lip2p, an octanoyltransferase, has been demonstrated to convert apo-Gcv3p to octanoyl-Gcv3p while another catalytic enzyme Lip5p, a lipoyl synthase, catalyzes the conversion of octanoyl-Gcv3p to lipoyl-Gcv3p (Hermes and Cronan, Yeast 30: 415-427 (2013)) (
[0075] Another possible rate-limiting factor for lipoic acid production in yeast is the availability of cofactors, particularly S-adenosylmethionine (SAM), which is required for sulfurization of the octanoyl moiety. Homologous lipoyl synthase from E. coli uses radical SAM chemistry to perform the insertion of two sulfurs into the octanoyl moiety, a process that requires both the cofactor SAM and the iron-sulfur clusters in the lipoyl synthase (Cicchillo et al., Biochemistry 43: 6378-6386 (2004)). Radical intermediates are generated from SAM to abstract hydrogen atoms from C-6 and C-8 of the octanoyl moiety, allowing for subsequent sulfur insertion by a mechanism involving carbon-centered radicals. Iron-sulfur cluster in the lipoyl synthase provides an electron during the cleavage of SAM for radical generation and also may act as the source for sulfur atoms during lipoylation (Cicchillo and Booker, Journal of the American Chemical Society 127: 2860-2861 (2005)). Therefore, increasing the availability of SAM and functional iron-sulfur clusters may drive the formation of lipoyl moiety. In S. cerevisiae, SAM can be generated from methionine and ATP by the lipoyl synthases Sam1p and Sam2p (Marobbio et al., The EMBO Journal 22: 5975-5982 (2003); Dato et al., Microbial Cell Factories 13: 147 (2014)). To increase SAM availability by regeneration from methionine and ATP, SAM1 and SAM2 were fused with MTP for mitochondria translocation and overexpressed under the weak P.sub.ADH1 promoter. Overexpression of the mitochondrial mSAM1 or mSAM2 increased lipoic acid production to 14.8 μg/L and 17.0 μg/L, respectively (
[0076] While we have identified a few rate-limiting steps in the lipoic acid production pathway, there is still much space for improvement to enhance lipoic acid production. To further boost the titer of lipoic acid, ion-sulfur cluster biogenesis and SAM availability, which are limiting factors of lipoic acid bio-production, can further be engineered in the future. In addition, to generate a molecule of lipoic acid, a molar equivalent of the precursor octanoyl-ACP is required (
SUMMARY
[0077] In this study, we aimed to develop a bio-based method for environmentally friendly lipoic acid production by metabolic engineering of S. cerevisiae. To achieve this goal, we sought to (i) understand the lipoylation process in S. cerevisiae, (ii) characterize the function of EfLPA towards lipoylated proteins from yeast, (iii) employ EfLPA to enable S. cerevisiae to produce free lipoic acid in vivo and (iv) improve lipoic acid production using metabolic engineering strategies. We first confirmed the presence of protein-bound lipoate through LC-MS/MS. Using homology modelling techniques, the protein structure of Gcv3p, Kgd2p and Lat1p were predicted and the residues for modification were found to be solvent-exposed, and hence accessible to enzymes acting on these residues. Through in vitro activity analysis, EfLPA was validated to release lipoic acid from yeast lipoyl-Gcv3p, hence demonstrating the first reported functional expression of EfLPA in yeast for releasing lipoic acid from lipoate-bound yeast protein. Subsequently, overexpression of EfLPA in the mitochondria led to lipoic acid production in vivo, thus accomplishing unprecedented free lipoic acid biosynthesis in the yeast S. cerevisiae. To enhance lipoic acid production, metabolic engineering approaches, including overexpression of pathway enzymes and regeneration of cofactors, were employed and the titer of lipoic acid production in S. cerevisiae was boosted by nearly 2.9-fold to 29.2 μg/L. Collectively, the protein analysis, enzyme characterization, structure modeling and combinatorial metabolic engineering approaches in this study provided a better understanding of the lipoic acid production pathway and revealed strategies to improve it. We envisage that the knowledge gained from this study will provide insights on lipoic acid biosynthesis in S. cerevisiae and spearhead future efforts in lipoic acid production in yeast.
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