WO2023108505A1 - Method for improving sam cofactor supply of saccharomyces cerevisiae, engineered yeast and use thereof - Google Patents

Method for improving sam cofactor supply of saccharomyces cerevisiae, engineered yeast and use thereof Download PDF

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WO2023108505A1
WO2023108505A1 PCT/CN2021/138511 CN2021138511W WO2023108505A1 WO 2023108505 A1 WO2023108505 A1 WO 2023108505A1 CN 2021138511 W CN2021138511 W CN 2021138511W WO 2023108505 A1 WO2023108505 A1 WO 2023108505A1
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gene
nucleotide sequence
opt1
site
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周雍进
张磊
陈瑞兵
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中国科学院大连化学物理研究所
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    • C12N15/00Mutation or genetic engineering; DNA or RNA concerning genetic engineering, vectors, e.g. plasmids, or their isolation, preparation or purification; Use of hosts therefor
    • C12N15/09Recombinant DNA-technology
    • C12N15/63Introduction of foreign genetic material using vectors; Vectors; Use of hosts therefor; Regulation of expression
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    • C12N15/00Mutation or genetic engineering; DNA or RNA concerning genetic engineering, vectors, e.g. plasmids, or their isolation, preparation or purification; Use of hosts therefor
    • C12N15/09Recombinant DNA-technology
    • C12N15/63Introduction of foreign genetic material using vectors; Vectors; Use of hosts therefor; Regulation of expression
    • C12N15/79Vectors or expression systems specially adapted for eukaryotic hosts
    • C12N15/80Vectors or expression systems specially adapted for eukaryotic hosts for fungi
    • C12N15/81Vectors or expression systems specially adapted for eukaryotic hosts for fungi for yeasts
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    • C12R2001/645Fungi ; Processes using fungi
    • C12R2001/85Saccharomyces
    • C12R2001/865Saccharomyces cerevisiae

Definitions

  • the invention belongs to the application field of microbial genetic engineering and metabolic engineering, and in particular relates to an engineering strain and its preparation method and application.
  • Ferulic acid is a plant-derived phenolic acid compound, which has good pharmacological effects and biological activities such as anti-oxidation, anti-radiation and antibacterial, so it has high application value in medicine, health care products, cosmetic raw materials and food additives. .
  • As a precursor raw material it can be used to synthesize complex active natural medicines such as rosmarinic acid, salvianolic acid B and silybin.
  • the content of free ferulic acid in plants is low, and the Saccharomyces cerevisiae cell factory provides a new idea for obtaining a large amount of free ferulic acid, which is a more environmentally friendly, green and efficient way.
  • the conventional strategy of constructing Saccharomyces cerevisiae cell factory is to design the synthetic pathway and find the elements needed for the pathway according to the design-build-test-learn (DBTL) cycle; then construct the synthetic pathway through the pathway modularization strategy to obtain engineering strains; The strains are cultivated and the product is tested to verify the synthesis efficiency of the target compound; finally, the conclusion is analyzed and studied, suggestions for improvement are put forward, and then enters the next DBTL cycle.
  • maximization of precursor supply and redirection of metabolic flux distribution through element screening and pathway optimization are considered as core engineering strategies to improve yield.
  • the synthesis process of many compounds requires the participation of multiple cofactors. When the target compound is synthesized efficiently, the contradiction of insufficient cofactors is gradually highlighted, which may become the rate-limiting step that limits the synthesis efficiency of cell factories. At present, the supply of cofactors in the synthesis process of natural products is often be ignored.
  • SAM cofactor adenosylmethionine
  • a method for increasing the supply of SAM cofactors in Saccharomyces cerevisiae is provided, which can overcome the difficulty of insufficient supply of endogenous cofactors during the synthesis of methylated products such as ferulic acid, thereby improving their synthesis efficiency.
  • a method of increasing the supply of SAM cofactors to Saccharomyces cerevisiae comprising:
  • MET6 gene, cMTFHR gene, LiMETK1 gene, SAH1 gene and ADO1 gene were introduced into Saccharomyces cerevisiae.
  • the method includes:
  • a DNA fragment containing T HSP26 -MET6-P GAL10/1 -cMTFHR-T PDC6 -P GAL7 -liMetK1-Sc OPT1 -T UBX6 was integrated into the HO site of Saccharomyces cerevisiae;
  • a DNA fragment containing T PRM9 -ADO1-P GAL10/1 -SAH1-T PYK1 was integrated into the V3 locus of S. cerevisiae.
  • nucleotide sequence of the MET6 gene is shown in SEQ ID NO: 2;
  • the nucleotide sequence of the cMTFHR gene is shown in SEQ ID NO: 3;
  • the nucleotide sequence of the LiMETK1 gene is shown in SEQ ID NO: 4;
  • the nucleotide sequence of the ADO1 gene is shown in SEQ ID NO: 5;
  • the nucleotide sequence of the SAH1 gene is shown in SEQ ID NO:6.
  • Saccharomyces cerevisiae is a ferulic acid producing strain
  • the ferulic acid producing strain is obtained by introducing the NtCOMT1 gene into the caffeic acid producing strain.
  • nucleotide sequence of the NtCOMT1 gene is shown in SEQ ID NO:1.
  • the NtCOMT1 gene is introduced into the caffeic acid-producing strain as T CSP1 -NtCOMT1-Sc OPT1 -P GAL10/1 -NtCOMT1-T HIS5 and integrated into the XII5 site of the caffeic acid producing strain.
  • the caffeic acid producing strain is obtained by introducing genes related to the phenolic acid synthesis pathway into the starting strain of Saccharomyces cerevisiae:
  • the phenolic acid synthesis pathway-related genes include at least one of Aro4 K229L , Aro7 G141S , EcAROL, ARO1, ARO2, ARO3, PHA2, MtPDH1, FjTAL, SbPAL1 H123F , AtCPR1, PtrC4H1, PtrC4H2, PtrC3H, PaHPAB, SeHPAC.
  • the phenolic acid synthesis pathway-related genes include Aro4 K229L having the nucleotide sequence shown in SEQ ID NO: 44, Aro7 G141S having the nucleotide sequence shown in SEQ ID NO: 45, Aro7 G141S having the nucleotide sequence shown in SEQ ID NO: 46 EcAROL with the nucleotide sequence shown, ARO1 with the nucleotide sequence shown in SEQ ID NO: 47, ARO2 with the nucleotide sequence shown in SEQ ID NO: 48, ARO2 with the nucleotide sequence shown in SEQ ID NO: 49 ARO3 having a nucleotide sequence, PHA2 having a nucleotide sequence shown in SEQ ID NO: 50, MtPDH1 having a nucleotide sequence shown in SEQ ID NO: 51, having a nucleotide sequence shown in SEQ ID NO: 52 FjTAL of the acid sequence, SbPAL1 H123F having the nucleotide sequence shown in SEQ
  • the introduction site of ARO7 G141S , ARO4 K229L and EcAROL is ARO10.
  • the import site of FjTAL, SbPAL1 H123F and AtCPR1 is PDC5;
  • ARO1, ARO2, and ARO3 The import site of ARO1, ARO2, and ARO3 is XII1;
  • the import site of PahpaB and SehpaC is X2;
  • the import site of PHA2 and MtPDH1 is XI8.
  • a DNA fragment containing THIS3 -ARO7 G141S -P GAL10/1 -ARO4 K229L -T ENO2 -P GAL7 -EcAROL-T ADH1 is integrated into the ARO10 site of the starting strain;
  • a DNA fragment containing T CPS1 -PHA2-P GAL10/1 -MtPDH1-Sc OPT1 -T HIS5 was integrated into the XI8 site of the starting strain.
  • the LmXFPK gene, CkPTA gene, TAL1 gene and TKL1 gene were also introduced into the starting strain of Saccharomyces cerevisiae.
  • nucleotide sequence of the TKL1 gene is shown in SEQ ID NO: 40;
  • the nucleotide sequence of the TAL1 gene is shown in SEQ ID NO: 41;
  • the nucleotide sequence of the LmXFPK gene is shown in SEQ ID NO: 42;
  • the nucleotide sequence of the CkPTA gene is shown in SEQ ID NO: 43.
  • the GAL80 gene of the starting strain of S. cerevisiae was also knocked out.
  • the engineering bacteria obtained by the method is provided.
  • the engineering bacteria obtained by the method and the application of the above-mentioned engineering bacteria in the preparation of SAM-dependent methylation products are provided.
  • the SAM-dependent methylation product includes ferulic acid.
  • the present application discloses the construction of a SAM-supplying yeast strain and its application to increase the yield of ferulic acid, which belongs to the application field of microbial genetic engineering and metabolic engineering.
  • the construction method described in this application uses the strain RB197 as the starting chassis cell, overexpresses the caffeic acid oxymethyltransferase gene NtCOMT1, and obtains the strain RB202.
  • the present invention uses the SAM yeast strain to make the ferulic acid yield reach 184.2mg/L, and the conversion efficiency of the substrate caffeic acid to synthesize ferulic acid is increased from 46% to 64%, and at the same time, the batch-type fed-batch fermentation reaches the highest yield so far of 3.8g/L , proving the application potential of this cell line in the industrialization of cell factories.
  • the purpose of this application is to provide the construction of yeast strains that supply SAM, so as to solve the difficulty of insufficient supply of endogenous SAM during the synthesis of methylated products such as ferulic acid, thereby improving the synthesis efficiency of yeast cell factories.
  • it fills the technical gap in this field, and on the other hand, it explores the application potential and prospect of SAM cofactor engineering as the target of cell factory engineering.
  • the present application provides a construction method of strain RB202.
  • the construction method uses the previously constructed high-caffeic acid-producing strain RB197 as a starting chassis cell, and overexpresses the caffeic acid oxymethyltransferase gene NtCOMT1 to obtain strain RB202. , to realize the synthesis of ferulic acid from caffeic acid.
  • nucleotide sequence of the oxygen methyltransferase gene NtCOMT1 is shown in SEQ ID NO:1.
  • the present application provides the strain RB202 constructed by the method for constructing the strain RB202.
  • the present application provides a construction method of recombinant yeast RB210, the construction method comprising: overexpressing MET6, cMTFHR and LiMETK1 in Saccharomyces cerevisiae strain RB197 to obtain strain RB210, thereby increasing the metabolic flux of SAM in the engineering strain and synthetic levels.
  • nucleotide sequence of the MET6 is shown in SEQ ID NO: 2
  • nucleotide sequence of the cMTFHR is shown in SEQ ID NO: 3
  • nucleotide sequence of the LiMETK1 is shown in SEQ ID NO :4.
  • the present application provides the strain RB210 constructed by the method for constructing the recombinant yeast RB210.
  • the present application provides a construction method of recombinant yeast RB218, the construction method comprising: expressing Saccharomyces cerevisiae-derived genes ADO1 and SAH1 in RB210 to obtain recombinant yeast RB218.
  • nucleotide sequence of the ADO1 is shown in SEQ ID NO: 5
  • nucleotide sequence of the SAH11 is shown in SEQ ID NO: 6.
  • the present application provides the strain RB218 constructed by the method for constructing the recombinant yeast RB218.
  • the present application provides the use of protected yeast in the production of natural products.
  • the natural product is ferulic acid.
  • the present application provides an adenosylmethionine (SAM) cofactor engineering strategy and a method for improving the synthesis efficiency of yeast ferulic acid, belonging to the field of microbial technology.
  • SAM often participates in cell life activities as a methyl donor, and plays an important role in the synthesis of various natural products such as ferulic acid. Therefore, the present invention designs a SAM cofactor metabolic engineering strategy, which can accelerate the methyl cycle in Saccharomyces cerevisiae cells, continuously supply the cofactor SAM, and improve the synthesis efficiency of the target product.
  • This strategy can avoid the exogenous addition of expensive, low transmembrane efficiency and photolabile cofactors or their precursors, while significantly improving the synthesis efficiency of ferulic acid.
  • the SAM cofactor engineering used in the present invention makes the ferulic acid output increase 39% in the shake flask fermentation, reaches 184.2mg/L, and the transformation efficiency of substrate caffeic acid synthetic ferulic acid is improved to 64% by 46%, simultaneously batch formula replenishes Feed fermentation reached the highest yield so far of 3.8g/L.
  • This strategy has the characteristics of high transformation efficiency, low production cost, and broad prospects for industrial application, which proves that SAM cofactor engineering has important potential and application value in the synthesis of ferulic acid and other SAM-dependent natural products in Saccharomyces cerevisiae.
  • the present application provides a method for improving yeast ferulic acid synthesis efficiency through a SAM cofactor engineering strategy, which is characterized in that it mainly includes the following steps:
  • the NtCOMT1 gene after codon optimization has the nucleotide sequence shown in SEQ ID NO: 1
  • the MET6 gene after codon optimization has the nucleotide sequence shown in SEQ ID NO: 2
  • the codon The optimized cMTFHR gene has the nucleotide sequence shown in SEQ ID NO: 3
  • the codon-optimized LiMETK1 gene has the nucleotide sequence shown in SEQ ID NO: 4
  • the ADO1 gene has the nucleotide sequence shown in SEQ ID NO: The nucleotide sequence shown in 5
  • SAH1 gene has the nucleotide sequence shown in SEQ ID NO: 6.
  • the method also includes step (4) using 20g/L glucose as a substrate in a basal salt medium to inoculate engineered yeast strains for fermentation, the initial inoculation OD600 is 0.1, and the fermentation condition is a liquid loading capacity of 20 /100mL, 30°C, 220rpm, fermentation time is 96h.
  • the expressed gene for enhanced cofactor supply may come from the coding gene of isozyme of other species or its codon-optimized gene.
  • the invention belongs to the application field of microbial genetic engineering and metabolic engineering, and specifically relates to a yeast SAM cofactor regulation strategy for improving the synthesis of ferulic acid and other SAM-dependent methylation products.
  • the purpose of the present invention is to provide a cofactor SAM engineering strategy to solve the difficulty of insufficient supply of endogenous SAM during the synthesis of ferulic acid and other methylated products, thereby improving the synthesis efficiency of yeast cell factories.
  • the method for constructing a Saccharomyces cerevisiae strain producing ferulic acid provided by the application.
  • the high caffeic acid-producing strain RB197 constructed earlier was used as the starting chassis cell, and the caffeic acid oxymethyltransferase gene NtCOMT1 (optimized nucleotide sequence shown in SEQ ID NO: 1) was overexpressed to obtain strain RB202. Acid synthesis of ferulic acid.
  • the present application provides a SAM cofactor engineering strategy, which can significantly increase the yield of ferulic acid.
  • the method of the above technical solution is to overexpress three key enzyme genes of the SAM synthesis pathway in Saccharomyces cerevisiae strain RB197 to obtain strain RB210, thereby improving the metabolic flow and synthesis level of SAM in the engineering strain.
  • overexpressing MET6 the optimized nucleotide sequence is shown in SEQ ID NO: 2
  • cMTFHR the optimized nucleotide sequence is shown in SEQ ID NO: 3
  • LiMETK1 the optimized nucleotide sequence is shown in SEQ ID NO: 3
  • LiMETK1 the optimized nucleotide sequence is shown in SEQ ID NO: 4
  • Saccharomyces cerevisiae endogenous genes ADO1 (nucleotide sequence shown in SEQ ID NO: 5) and SAH1 (nucleotide sequence shown in SEQ ID NO: 6)
  • recombinant yeast RB218 was obtained to achieve efficient Methyl cycle and SAM turnover, supporting high-level synthesis of ferulic acid.
  • RB218 yeast strain was inoculated to carry out ferulic acid synthesis fermentation.
  • shake flask fermentation is carried out in a basal salt medium with 20g/L glucose as the substrate, the initial inoculation OD600 is 0.1, the fermentation conditions are liquid volume 20/100mL, 30°C, 220rpm, and the fermentation time is 96h .
  • batch fed-batch fermentation was carried out in a 1L fermenter, and the fermentation was started on a basal salt medium with 20g/L glucose as the substrate, with an initial inoculum volume of 0.25L and an OD600 of 0.2. Dissolved oxygen is controlled to be 40% by the stirring paddle speed (800-1200rpm), and the fermentation temperature is 30°C. The pH was maintained at 5.6 using 4M KOH and 2M HCl. During the fed-batch phase, additional 200 g/L glucose solution was added, and the feed rate was coupled to growth and increased exponentially (set ⁇ to 0.05 h-1) to maintain a constant biomass-to-glucose consumption rate.
  • the present invention provides a SAM cofactor engineering strategy to solve the difficulty of insufficient supply of endogenous cofactors during the synthesis of ferulic acid and other methylated products, thereby improving their synthesis efficiency.
  • the cofactor regulation method of the present invention involves SAM synthesis and SAM cycle, which can realize high-speed turnover and high-level supply of endogenous cofactor SAM, avoid the addition of expensive and unstable cofactor or its prerequisites from exogenous sources, and reduce cost consumption.
  • the invention uses SAM cofactor engineering to make the ferulic acid output reach 184.2mg/L, the conversion efficiency of the substrate caffeic acid to synthesize ferulic acid is increased from 46% to 64%, and at the same time, the batch-type fed-batch fermentation reaches the highest yield so far of 3.8g/L L, demonstrating the potential of this cofactor engineering strategy for the industrialization of cell factories.
  • Figure 1 shows a schematic diagram of the pgRNA plasmid construction process in the Saccharomyces cerevisiae CRISPR/Cas9 system. .
  • Figure 2 shows the yield of ferulic acid synthesized by SAM cofactor engineered yeast in shake flasks.
  • Figure 3 shows a schematic diagram of the SAM cofactor engineering strategy.
  • Figure 4 shows the yield of ferulic acid produced by SAM cofactor engineered yeast in bacterial batch fed-batch fermentation.
  • the Saccharomyces cerevisiae strain that synthesizes ferulic acid can use any yeast strain that produces caffeic acid as the starting strain, and the caffeic acid-producing strain RB197 is used in the examples of the present application.
  • a recombinant Saccharomyces cerevisiae CEN.PK113-11C-CAS (genotype MATa, SUC2, MAL2-8c, his3 ⁇ , ura3 ⁇ , XI5::(P TEF1 -CAS9-T CYC1 )) integrating the CAS9 gene was constructed and used as a host The strains were constructed for cofactor engineering yeast strains.
  • CEN.PK113-11C-CAS the construction method of CEN.PK113-11C-CAS is as follows: First, directly chemically synthesize CAS9 and the resistance gene KanMX expression cassette T AgTEF -KanMX-P AgTEF -P TEF1 -CAS9-T CYC1 , and combine the expression cassette with XI5 by fusion PCR
  • the upstream and downstream 500bp fusions obtained the donor DNA fragment XI5up-T AgTEF -KanMX-P AgTEF -P TEF1 -CAS9-T CYC1 -XI5dw, transformed Saccharomyces cerevisiae CEN.PK113-11C (available from Euroscarf, Germany), and homologous Recombination was integrated into the XI5 site, and positive strains were screened by geneticin G418 to obtain strain CEN.PK113-11C-CAS+KanMX.
  • pgRNA-KanMX was transformed with the donor DNA fragment XI5up- PTEF1 obtained by fusion PCR.
  • chemical transformation method about 500ng of pgRNA-KanMX and donor DNA were simultaneously transformed into the yeast strain integrated with the Cas9 protein, and cultured statically at 30°C for 2 days on the SD plate with histidine added; the transformant was added with After cultured in the liquid SD medium of histidine, it was verified correctly by PCR, and spread on the solid medium containing 5-fluoroorotic acid for plasmid loss. After the plasmid loss, the strain CEN.PK113-11C-CAS was obtained, and the strain was preserved for future use. .
  • the sgRNA expression vector construction process of each gene in the caffeic acid production strain RB197 is the same as that in Example 1, and the sgRNA expression vector involved includes pgRNA-GAL80 (target gene GAL80), pgRNA-GPP1 (target gene GPP1), pgRNA-XI7 (target gene To site XI7), pgRNA-XI6 (target site XI6), pgRNA-ARO10 (target gene ARO10), pgRNA-PDC5 (target gene PDC5), pgRNA-XII4 (target site XII4), pgRNA- XII1 (targeting site XII1), pgRNA-X2 (targeting site X2), pgRNA-XI8 (targeting site XI8), and the targeting sequences are shown in Table 1.
  • the donor DNA respectively amplify about 500 bp downstream of the target site of the pgRNA vector as homology arms, and then assemble each fragment to be inserted by conventional fusion PCR to obtain a complete donor DNA molecule, and The pgRNAs of the corresponding sites were transformed into yeast together for gene editing and strain transformation.
  • the information of each gene is shown in Table 2.
  • pgRNA-KanMX SEQ ID NO: 37; GGTTCTAGAAGTGCCCTTTG SEQ ID NO: 38; ATTCTACCGATTTATCATGC
  • Sc OPT1 indicates that the gene is codon-optimized according to S. cerevisiae preference.
  • YPD medium 20g/L glucose, 20g/L peptone, 10g/L yeast powder;
  • SD medium 20g/L glucose, 6.7g/L YNB, add histidine 0.02g/L when used;
  • Fermentation medium (basic component medium): (NH 4 ) 2 SO 4 2.5g/L, KH 2 PO 4 14.4g/L, MgSO 4 7H 2 O 0.5g/L, add about 900mL ddH 2 O, adjust The pH is 5.6, the volume is adjusted to 950mL, and sterilized at 115°C for 30min. After sterilization, add 1mL vitamin solution (see Table 4 for recipe) and 2mL trace metal solution (see Table 3 for recipe), and add histidine and uracil (40mg/L) as needed. Glucose was added to the fermentation medium to 20g/L for phenolic acid fermentation.
  • Ferulic acid is converted from caffeic acid by caffeic acid oxymethyltransferase, which is a one-step methylation reaction. Therefore, NtCOMT1 was overexpressed in the caffeic acid producing strain RB197 constructed above, and it was found that it can synthesize ferulic acid more efficiently.
  • the promoter P GAL10/1 was used to express the exogenous pathway to realize the synthesis of ferulic acid under the condition of sugar restriction and reduce the impact on cell growth.
  • the exogenous gene NtCOMT1 was integrated into the yeast genome by transformation chemical transformation method and CRISPR technology to obtain strain RB202.
  • the specific method is: pick a single clone of the strain and put it in 3 mL of YPD medium, culture it overnight at 220 rpm at 30°C for 16 hours; inoculate it into 20 mL of YPD medium (100 mL shake flask), ensure that the initial OD600 is 0.1, and cultivate for about After 6 hours, the OD600 reached 0.6-1.0; centrifuged at 2000g for 5min at room temperature to collect the cells, added 1mL of 0.1M LiAc solution to resuspend the cells, and transferred to a 2mL sterile centrifuge tube; centrifuged at 2000g for 2min to collect the cells, and resuspended in 200uL of 0.1M LiAc, placed on ice to obtain competent cells; add 120 ⁇ L of PEG3350 solution (50%),
  • sgRNA expression vectors used in the present invention are identical except for the 20bp targeting sequence. Briefly, the vector backbone S1 was first amplified from pgRNA (SEQ ID NO: 7) using primer 6005 (SEQ ID NO: 8, GATCATTTATTCTTTCACTGCGGAGAAG); then, sgRNA-1 and sgRNA-2 were amplified for targeting yeast Genomic loci were edited and exogenous gene inserted, wherein sgRNA-1 used primers p1 (SEQ ID NO: 9, GCGGTTAGCTCCTTCGGTCCTCCGATCGTTGTCAGAAGTAAGTTGGCCGCAGTGTTATC) and pX1 (AAACTTCTCCGCAGTGAAAGATAAATGATC( M20 )GTTTTGAGCTAGAAATAG, where M20 is an alternative 20bp targeting sequence), sgRNA -2 Use primers p2 (SEQ ID NO: 10, GATAACACTGCGGCC
  • the replacement sequences of M20 and N20 in pX1 and pX2 in Examples 1-2 and the corresponding sequence names after replacement are shown in Table 5.
  • the sgRNA expression vectors involved in Examples 1-2 of the present invention include pgRNA-XII5 (targeting site XII5), pgRNA-HO (targeting site HO), pgRNA-V3 (targeting gene V3).
  • pgRNA-XII5 targeting site XII5
  • pgRNA-HO targeting site HO
  • pgRNA-V3 targeting gene V3
  • For the donor DNA respectively amplify about 500 bp downstream of the target site of the pgRNA vector as homology arms, and then assemble each fragment to be inserted by conventional fusion PCR to obtain a complete donor DNA molecule, and The pgRNAs of the corresponding sites are transformed into yeast together for gene editing and strain transformation. The information of each gene is shown in Table 6.
  • Sc OPT1 indicates that the gene is codon-optimized according to S. cerevisiae preference.
  • the fermentation experiment of ferulic acid was carried out under the condition of the basal medium containing 20g/L glucose, the initial inoculation OD600 was 0.1, the fermentation condition was 20/100mL, 30°C, 220rpm, and the fermentation time was 96h.
  • Ferulic acid was then extracted and detected. Take 50 ⁇ L fermentation sample, add 450 ⁇ L sterile water, then add 500 ⁇ L ethanol, vortex and mix well; centrifuge at 13,000 g for 5 min, take 500 ⁇ L supernatant and pass through a 0.22 ⁇ m aqueous microporous membrane to obtain the phenolic acid sample. Samples were detected using Shimadzu HPLC, the chromatographic column was 3 ⁇ 100mm 2.7um Poroshell 120 EC-C18 (Agilent), the flow rate was 0.8mL/min, the mobile phase A was H 2 O+0.05%HCOOH, and the mobile phase B was ACN+0.05 %HCOOH, the detection wavelength of the ultraviolet detector is 280nm or 330nm. The specific mobile phase gradient is 95%-A (0min), 90%-A (3min), 88%-A (4-5min), 85%-A (6-7min), 40%-A (10min), 95 %-A (12-14min).
  • Sah1 catalyzes a reversible reaction, and the reaction proceeds in the direction of synthesizing adenosylhomocysteine from homocysteine under natural conditions, which is not conducive to the synthesis of ferulic acid. Therefore, by overexpressing S-adenosylhomocysteine hydrolase SAH1 and adenosine kinase ADO1, it is possible to consume the by-product adenosine and change the kinetic direction of the reaction to synthesize homocysteine from adenosylhomocysteine. in the direction of cystine.
  • RB218 was subjected to fed-batch fermentation.
  • start fermentation with basal salt medium with 20g/L glucose as the substrate, the initial inoculum volume is 0.25L, and the OD600 is 0.2.
  • Dissolved oxygen is controlled to be 40% by the stirring paddle speed (800-1200rpm), and the fermentation temperature is 30°C.
  • the pH was maintained at 5.6 using 4M KOH and 2M HCl.
  • 500 g/L glucose solution was added every 24 hours until the glucose concentration reached 20 g/L.
  • the highest ferulic acid yield so far was 3.8g/L (Fig. 4). This result confirmed the potential and important application value of S. cerevisiae NADPH and FADH 2 cofactor engineering in phenolic acid synthesis.

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Abstract

Provided in the present application are a method for improving the SAM cofactor supply of Saccharomyces cerevisiae, an engineered yeast and the use thereof. The method comprises: introducing an MET6 gene, a cMTFHR gene, a LiMETK1 gene, an SAH1 gene and an ADO1 gene into Saccharomyces cerevisiae. The method can solve the problem of the insufficient supply of endogenous auxiliary factors in the synthesis process of methylation products such as ferulic acid, thereby increasing the synthesis efficiency thereof.

Description

一种提高酿酒酵母SAM辅因子供应的方法、工程菌及其应用A method for improving the supply of SAM cofactor of Saccharomyces cerevisiae, engineering bacteria and its application 技术领域technical field
本发明属于微生物基因工程与代谢工程应用领域,具体涉及一种工程菌株及其制备方法与应用。The invention belongs to the application field of microbial genetic engineering and metabolic engineering, and in particular relates to an engineering strain and its preparation method and application.
背景技术Background technique
阿魏酸是一种植物来源的酚酸化合物,具有抗氧化、抗辐射和抗菌等良好的药理作用和生物活性,因而在医药、保健品、化妆品原料和食品添加剂等方面具有较高的应用价值。作为前体原料,可用于合成迷迭香酸、丹参酚酸B和水飞蓟宾等复杂的活性天然药物。植物中游离阿魏酸含量较低,酿酒酵母细胞工厂为游离阿魏酸的大量获取提供了新思路,是一种更加环保、绿色和高效的方式。Ferulic acid is a plant-derived phenolic acid compound, which has good pharmacological effects and biological activities such as anti-oxidation, anti-radiation and antibacterial, so it has high application value in medicine, health care products, cosmetic raw materials and food additives. . As a precursor raw material, it can be used to synthesize complex active natural medicines such as rosmarinic acid, salvianolic acid B and silybin. The content of free ferulic acid in plants is low, and the Saccharomyces cerevisiae cell factory provides a new idea for obtaining a large amount of free ferulic acid, which is a more environmentally friendly, green and efficient way.
构建酿酒酵母细胞工厂的常规策略是依据设计-构建-测试-学习(DBTL)循环,设计合成途径并寻找途径所需的元件;然后通过途径模块化策略构建合成通路,获得工程菌株;进一步对工程菌株进行培养和产物检测,验证目标化合物的合成效率;最后对结论进行分析和学习,提出改良意见,再进入下一次DBTL循环。在这个过程中,通过元件筛选和途径优化,实现前体供应最大化和代谢流分布重定向被认为是提高产量的核心工程策略。很多化合物合成过程效多种辅因子参与,当目标化合物高效合成时,辅因子不足的矛盾逐渐凸显,可能成为限制细胞工厂合成效率的限速步骤,目前,天然产物合成过程中辅因子的供应往往被忽略。The conventional strategy of constructing Saccharomyces cerevisiae cell factory is to design the synthetic pathway and find the elements needed for the pathway according to the design-build-test-learn (DBTL) cycle; then construct the synthetic pathway through the pathway modularization strategy to obtain engineering strains; The strains are cultivated and the product is tested to verify the synthesis efficiency of the target compound; finally, the conclusion is analyzed and studied, suggestions for improvement are put forward, and then enters the next DBTL cycle. In this process, maximization of precursor supply and redirection of metabolic flux distribution through element screening and pathway optimization are considered as core engineering strategies to improve yield. The synthesis process of many compounds requires the participation of multiple cofactors. When the target compound is synthesized efficiently, the contradiction of insufficient cofactors is gradually highlighted, which may become the rate-limiting step that limits the synthesis efficiency of cell factories. At present, the supply of cofactors in the synthesis process of natural products is often be ignored.
阿魏酸合成途径的最后一步反应由咖啡酸氧甲基转移酶催化完成,需要辅因子腺苷甲硫氨酸(SAM)作为甲基供体参与反应。SAM辅因子具有显著的时空分布特征和严格的动态调控机制,在酵母中设计精准的SAM工程策略并用于提高生物合成效率极具挑战。The last step of the ferulic acid synthesis pathway is catalyzed by caffeic acid oxymethyltransferase, which requires the cofactor adenosylmethionine (SAM) as a methyl donor to participate in the reaction. SAM cofactors have significant spatiotemporal distribution characteristics and strict dynamic regulation mechanism, and it is extremely challenging to design precise SAM engineering strategies in yeast and use them to improve biosynthetic efficiency.
发明内容Contents of the invention
根据本申请的一个方面,提供一种提高酿酒酵母SAM辅因子供应的方法,可以阿魏酸等甲基化产物合成过程中内源辅因子供应不足的困难,从而提高其合成效率。According to one aspect of the present application, a method for increasing the supply of SAM cofactors in Saccharomyces cerevisiae is provided, which can overcome the difficulty of insufficient supply of endogenous cofactors during the synthesis of methylated products such as ferulic acid, thereby improving their synthesis efficiency.
一种提高酿酒酵母SAM辅因子供应的方法,所述方法包括:A method of increasing the supply of SAM cofactors to Saccharomyces cerevisiae, said method comprising:
在酿酒酵母中导入MET6基因、cMTFHR基因、LiMETK1基因、SAH1基因和ADO1基因。MET6 gene, cMTFHR gene, LiMETK1 gene, SAH1 gene and ADO1 gene were introduced into Saccharomyces cerevisiae.
可选地,所述方法包括:Optionally, the method includes:
将含有T HSP26-MET6-P GAL10/1-cMTFHR-T PDC6-P GAL7-liMetK1-Sc OPT1-T UBX6的DNA片段整合到酿酒酵母的HO位点; A DNA fragment containing T HSP26 -MET6-P GAL10/1 -cMTFHR-T PDC6 -P GAL7 -liMetK1-Sc OPT1 -T UBX6 was integrated into the HO site of Saccharomyces cerevisiae;
将含有T PRM9-ADO1-P GAL10/1-SAH1-T PYK1的DNA片段整合到酿酒酵母的V3位点。 A DNA fragment containing T PRM9 -ADO1-P GAL10/1 -SAH1-T PYK1 was integrated into the V3 locus of S. cerevisiae.
可选地,MET6基因的核苷酸序列如SEQ ID NO:2所示;Optionally, the nucleotide sequence of the MET6 gene is shown in SEQ ID NO: 2;
cMTFHR基因的核苷酸序列如SEQ ID NO:3所示;The nucleotide sequence of the cMTFHR gene is shown in SEQ ID NO: 3;
LiMETK1基因的核苷酸序列如SEQ ID NO:4所示;The nucleotide sequence of the LiMETK1 gene is shown in SEQ ID NO: 4;
ADO1基因的核苷酸序列如SEQ ID NO:5所示;The nucleotide sequence of the ADO1 gene is shown in SEQ ID NO: 5;
SAH1基因的核苷酸序列如SEQ ID NO:6所示。The nucleotide sequence of the SAH1 gene is shown in SEQ ID NO:6.
可选地,所述酿酒酵母为阿魏酸生产菌株;Optionally, the Saccharomyces cerevisiae is a ferulic acid producing strain;
所述阿魏酸生产菌株通过在产咖啡酸菌株中导入NtCOMT1基因得到。The ferulic acid producing strain is obtained by introducing the NtCOMT1 gene into the caffeic acid producing strain.
可选地,所述NtCOMT1基因的核苷酸序列如SEQ ID NO:1所示。Optionally, the nucleotide sequence of the NtCOMT1 gene is shown in SEQ ID NO:1.
可选地,在产咖啡酸菌株中导入NtCOMT1基因为T CSP1-NtCOMT1-Sc OPT1-P GAL10/1-NtCOMT1-T HIS5整合到产咖啡酸菌株的XII5位点。 Optionally, the NtCOMT1 gene is introduced into the caffeic acid-producing strain as T CSP1 -NtCOMT1-Sc OPT1 -P GAL10/1 -NtCOMT1-T HIS5 and integrated into the XII5 site of the caffeic acid producing strain.
可选地,所述产咖啡酸菌株通过在酿酒酵母出发菌株中导入酚酸合成途径相关基因得到:Optionally, the caffeic acid producing strain is obtained by introducing genes related to the phenolic acid synthesis pathway into the starting strain of Saccharomyces cerevisiae:
所述酚酸合成途径相关基因包括Aro4 K229L、Aro7 G141S、EcAROL、ARO1、ARO2、ARO3、PHA2、MtPDH1、FjTAL、SbPAL1 H123F、AtCPR1、PtrC4H1、PtrC4H2、PtrC3H、PaHPAB、SeHPAC中的至少一种。 The phenolic acid synthesis pathway-related genes include at least one of Aro4 K229L , Aro7 G141S , EcAROL, ARO1, ARO2, ARO3, PHA2, MtPDH1, FjTAL, SbPAL1 H123F , AtCPR1, PtrC4H1, PtrC4H2, PtrC3H, PaHPAB, SeHPAC.
所述酚酸合成途径相关基因包括具有如SEQ ID NO:44所示核苷酸序列的Aro4 K229L、具有如SEQ ID NO:45所示核苷酸序列的Aro7 G141S、具有如SEQ ID NO:46所示核苷酸序列的EcAROL、具有如SEQ ID NO:47所示的核苷酸序列的ARO1、具有SEQ ID NO:48所示核苷酸序列的ARO2、具有如SEQ ID NO:49所示核苷酸序列的ARO3、具有如SEQ ID NO:50所示核苷酸序列的PHA2、具有如SEQ ID NO:51所示核苷酸序列的MtPDH1、具有如SEQ ID NO:52所示核苷酸序列的FjTAL,具有如SEQ ID NO:53所示核苷酸序列的SbPAL1 H123F、具有如SEQ ID NO:54所示核苷酸序列的AtCPR1、具有如SEQ ID NO:55所示核苷酸序列的PtrC4H1、具有如SEQ ID NO:56所示核苷酸序列的PtrC4H2、具有如SEQ ID NO:57所示核苷酸序列的PtrC3H、具有如SEQ ID NO:58所示核苷酸序列的PaHPAB、具有如SEQ ID NO:59所示核苷酸序列的SeHPAC中的至少一种; The phenolic acid synthesis pathway-related genes include Aro4 K229L having the nucleotide sequence shown in SEQ ID NO: 44, Aro7 G141S having the nucleotide sequence shown in SEQ ID NO: 45, Aro7 G141S having the nucleotide sequence shown in SEQ ID NO: 46 EcAROL with the nucleotide sequence shown, ARO1 with the nucleotide sequence shown in SEQ ID NO: 47, ARO2 with the nucleotide sequence shown in SEQ ID NO: 48, ARO2 with the nucleotide sequence shown in SEQ ID NO: 49 ARO3 having a nucleotide sequence, PHA2 having a nucleotide sequence shown in SEQ ID NO: 50, MtPDH1 having a nucleotide sequence shown in SEQ ID NO: 51, having a nucleotide sequence shown in SEQ ID NO: 52 FjTAL of the acid sequence, SbPAL1 H123F having the nucleotide sequence shown in SEQ ID NO: 53, AtCPR1 having the nucleotide sequence shown in SEQ ID NO: 54, having the nucleotide sequence shown in SEQ ID NO: 55 PtrC4H1 of sequence, PtrC4H2 having the nucleotide sequence shown in SEQ ID NO: 56, PtrC3H having the nucleotide sequence shown in SEQ ID NO: 57, PtrC3H having the nucleotide sequence shown in SEQ ID NO: 58 At least one of PaHPAB and SeHPAC having the nucleotide sequence shown in SEQ ID NO: 59;
可选地,ARO7 G141S、ARO4 K229L、EcAROL的导入位点为ARO10。 Optionally, the introduction site of ARO7 G141S , ARO4 K229L and EcAROL is ARO10.
FjTAL、SbPAL1 H123F、AtCPR1的导入位点为PDC5; The import site of FjTAL, SbPAL1 H123F and AtCPR1 is PDC5;
PtrC4H2、PtrC4H1、PtrC3H的导入位点为XII4;The import site of PtrC4H2, PtrC4H1 and PtrC3H is XII4;
ARO1、ARO2、ARO3的导入位点为XII1;The import site of ARO1, ARO2, and ARO3 is XII1;
PahpaB、SehpaC的导入位点为X2;The import site of PahpaB and SehpaC is X2;
PHA2、MtPDH1的导入位点为XI8。The import site of PHA2 and MtPDH1 is XI8.
可选地,将含有T HIS3-ARO7 G141S-P GAL10/1-ARO4 K229L-T ENO2-P GAL7-EcAROL-T ADH1的DNA片段整合到出发菌株的ARO10位点; Alternatively, a DNA fragment containing THIS3 -ARO7 G141S -P GAL10/1 -ARO4 K229L -T ENO2 -P GAL7 -EcAROL-T ADH1 is integrated into the ARO10 site of the starting strain;
将含有T CYC1-FjTAL-Sc OPT1-P GAL10/1-SbPAL1 H123F-Sc OPT1-T TDH2-T FBA1-AtCPR1-Sc OPT1-P GAL7的DNA片段整合到出发菌株的PDC5位点; Integrate the DNA fragment containing T CYC1 -FjTAL-Sc OPT1 -P GAL10/1 -SbPAL1 H123F -Sc OPT1 -T TDH2 -T FBA1 -AtCPR1-Sc OPT1 -P GAL7 into the PDC5 site of the starting strain;
将含有T PRM9t-PtrC4H2-Sc OPT1-P GAL10/1-PtrC4H1-Sc OPT1-T PYK1-P GAL7-PtrC3H-Sc OPT1-T DIT1的DNA片段整合到出发菌株的XII4位点;、 Integrate the DNA fragment containing T PRM9t -PtrC4H2-Sc OPT1 -P GAL10/1 -PtrC4H1-Sc OPT1 -T PYK1 -P GAL7 -PtrC3H-Sc OPT1 -T DIT1 into the XII4 site of the starting strain;
将含有P GAL7-ARO1-T ENO2-T CPS1-ARO2-P GAL10/1-ARO3-T HIS5的DNA片段整合到出发菌株的XII1位点; Integrate the DNA fragment containing P GAL7 -ARO1-T ENO2 -T CPS1 -ARO2-P GAL10/1 -ARO3-T HIS5 into the XII1 site of the starting strain;
将含有T PRM9-PahpaB-Sc OPT1-P GAL10/1-SehpaC-Sc OPT1-T HIS3的DNA片段整合到出发菌株的X2位点; Integrate the DNA fragment containing T PRM9 -PahpaB-Sc OPT1 -P GAL10/1 -SehpaC-Sc OPT1 -T HIS3 into the X2 site of the starting strain;
将含有T CPS1-PHA2-P GAL10/1-MtPDH1-Sc OPT1-T HIS5的DNA片段整合到出发菌株的XI8位点。 A DNA fragment containing T CPS1 -PHA2-P GAL10/1 -MtPDH1-Sc OPT1 -T HIS5 was integrated into the XI8 site of the starting strain.
可选地,还在酿酒酵母出发菌株中导入LmXFPK基因、CkPTA基因、TAL1基因和TKL1基因。Optionally, the LmXFPK gene, CkPTA gene, TAL1 gene and TKL1 gene were also introduced into the starting strain of Saccharomyces cerevisiae.
可选地,TKL1基因的核苷酸序列如SEQ ID NO:40所示;Optionally, the nucleotide sequence of the TKL1 gene is shown in SEQ ID NO: 40;
TAL1基因的核苷酸序列如SEQ ID NO:41所示;The nucleotide sequence of the TAL1 gene is shown in SEQ ID NO: 41;
LmXFPK基因的核苷酸序列如SEQ ID NO:42所示;The nucleotide sequence of the LmXFPK gene is shown in SEQ ID NO: 42;
CkPTA基因的核苷酸序列如SEQ ID NO:43所示。The nucleotide sequence of the CkPTA gene is shown in SEQ ID NO: 43.
可选地,还敲除酿酒酵母出发菌株的GAL80基因。Optionally, the GAL80 gene of the starting strain of S. cerevisiae was also knocked out.
根据本申请的一个方面,提供所述的方法得到的工程菌。According to one aspect of the present application, the engineering bacteria obtained by the method is provided.
根据本申请的一个方面,提供所述的方法得到的工程菌、上述所述的工程菌在制备SAM依赖的甲基化产物中的应用。According to one aspect of the present application, the engineering bacteria obtained by the method and the application of the above-mentioned engineering bacteria in the preparation of SAM-dependent methylation products are provided.
可选地,所述SAM依赖的甲基化产物包括阿魏酸。Optionally, the SAM-dependent methylation product includes ferulic acid.
作为一种实施方案,本申请公开了一种供应SAM酵母菌株的构建及其提高阿魏酸产量的应用,属于微生物基因工程与代谢工程应用领域。本申请所述构建方法以菌株RB197为起始底盘细胞,过表达咖啡酸氧甲基转移酶基因NtCOMT1,获得菌株RB202。本发明应用SAM酵母菌株使得阿魏酸产量达到184.2mg/L,底物咖啡酸合成阿魏酸的转化效率由46%提高到64%,同时批式补料发酵达到迄今最高产量3.8g/L,证明了该细胞株在细胞工厂工业化的应用潜力。As an embodiment, the present application discloses the construction of a SAM-supplying yeast strain and its application to increase the yield of ferulic acid, which belongs to the application field of microbial genetic engineering and metabolic engineering. The construction method described in this application uses the strain RB197 as the starting chassis cell, overexpresses the caffeic acid oxymethyltransferase gene NtCOMT1, and obtains the strain RB202. The present invention uses the SAM yeast strain to make the ferulic acid yield reach 184.2mg/L, and the conversion efficiency of the substrate caffeic acid to synthesize ferulic acid is increased from 46% to 64%, and at the same time, the batch-type fed-batch fermentation reaches the highest yield so far of 3.8g/L , proving the application potential of this cell line in the industrialization of cell factories.
作为一种实施方案,本申请目的是提供供应SAM酵母菌株的构建,以解决阿魏酸等甲基化产物合成过程中内源SAM供应不足的困难,从而提高酵母细胞工厂的合成效率。一方面填补本领域技术空白,另一方面探索SAM辅因子工程作为细胞工厂工程靶点的应用潜力与前景。As an embodiment, the purpose of this application is to provide the construction of yeast strains that supply SAM, so as to solve the difficulty of insufficient supply of endogenous SAM during the synthesis of methylated products such as ferulic acid, thereby improving the synthesis efficiency of yeast cell factories. On the one hand, it fills the technical gap in this field, and on the other hand, it explores the application potential and prospect of SAM cofactor engineering as the target of cell factory engineering.
作为一种实施方案,本申请提供菌株RB202的构建方法,所述构建方法以前期构建的高产咖啡酸的菌株RB197为起始底盘细胞,过表达咖啡酸氧甲基转移酶基因NtCOMT1,获得菌株RB202,实现从咖啡酸合成阿魏酸。As an embodiment, the present application provides a construction method of strain RB202. The construction method uses the previously constructed high-caffeic acid-producing strain RB197 as a starting chassis cell, and overexpresses the caffeic acid oxymethyltransferase gene NtCOMT1 to obtain strain RB202. , to realize the synthesis of ferulic acid from caffeic acid.
可选地,所述氧甲基转移酶基因NtCOMT1核苷酸序列如SEQ ID NO:1所示。Optionally, the nucleotide sequence of the oxygen methyltransferase gene NtCOMT1 is shown in SEQ ID NO:1.
作为一种实施方案,本申请提供所述菌株RB202的构建方法所构建的菌株RB202。As an embodiment, the present application provides the strain RB202 constructed by the method for constructing the strain RB202.
作为一种实施方案,本申请提供重组酵母菌RB210的构建方法,所述构建方法包括:在酿酒酵母菌株RB197中过表达MET6,cMTFHR和LiMETK1,获得菌株RB210,从而提高工程菌株中SAM的代谢流和合成水平。As an embodiment, the present application provides a construction method of recombinant yeast RB210, the construction method comprising: overexpressing MET6, cMTFHR and LiMETK1 in Saccharomyces cerevisiae strain RB197 to obtain strain RB210, thereby increasing the metabolic flux of SAM in the engineering strain and synthetic levels.
可选地,所述MET6的核苷酸序列如SEQ ID NO:2所示,所述cMTFHR的核苷酸序列如SEQ ID NO:3所示,所述LiMETK1的核苷酸序列如SEQ ID NO:4所示。Optionally, the nucleotide sequence of the MET6 is shown in SEQ ID NO: 2, the nucleotide sequence of the cMTFHR is shown in SEQ ID NO: 3, and the nucleotide sequence of the LiMETK1 is shown in SEQ ID NO :4.
作为一种实施方案,本申请提供所述重组酵母菌RB210的构建方法所构建的菌株RB210。As an embodiment, the present application provides the strain RB210 constructed by the method for constructing the recombinant yeast RB210.
作为一种实施方案,本申请提供重组酵母菌RB218的构建方法,所述构建方法包括:RB210中表达酿酒酵母来源基因ADO1和SAH1,得到重组酵母菌RB218。As an embodiment, the present application provides a construction method of recombinant yeast RB218, the construction method comprising: expressing Saccharomyces cerevisiae-derived genes ADO1 and SAH1 in RB210 to obtain recombinant yeast RB218.
可选地,所述ADO1的核苷酸序列如SEQ ID NO:5所示,所述SAH11的核苷酸序列如SEQ ID NO:6所示。Optionally, the nucleotide sequence of the ADO1 is shown in SEQ ID NO: 5, and the nucleotide sequence of the SAH11 is shown in SEQ ID NO: 6.
作为一种实施方案,本申请提供所述重组酵母菌RB218的构建方法所构建的菌株RB218。As an embodiment, the present application provides the strain RB218 constructed by the method for constructing the recombinant yeast RB218.
作为一种实施方案,本申请提供保护酵母菌在生产天然产物中的应用。As an embodiment, the present application provides the use of protected yeast in the production of natural products.
可选地,所述天然产物为阿魏酸。Optionally, the natural product is ferulic acid.
作为一种实施方案,本申请提供了一种腺苷甲硫氨酸(SAM)辅因子工程策略并用于提高酵母阿魏酸合成效率的方法,属于微生物技术领域。SAM常作为甲基供体参与细胞生命活动,在多种天然产物如阿魏酸合成过程中具有重要作用。因此,本发明设计了一种SAM辅因子代谢工程策略,能够在酿酒酵母细胞中加速甲基循环,持续供应辅因子SAM,提高目标产物合成效率。该策略能够避免外源添加价格昂贵、跨膜效率低和光不稳定的辅因子或其前体,同时显著提高阿魏酸的合成效率。本发明使用的SAM辅因子工程使得摇瓶发酵中阿魏酸产量提高39%,达到184.2mg/L,底物咖啡酸合成阿魏酸的转化效率由46%提高到64%,同时批式补料发酵达到迄今最高产量3.8g/L。这一策略具有转化效率高、生产成本低、工业化应用前景广等特点,证实SAM辅因子工程在酿酒酵母合成阿魏酸等 SAM依赖的天然产物中具有重要的潜力和应用价值。As an embodiment, the present application provides an adenosylmethionine (SAM) cofactor engineering strategy and a method for improving the synthesis efficiency of yeast ferulic acid, belonging to the field of microbial technology. SAM often participates in cell life activities as a methyl donor, and plays an important role in the synthesis of various natural products such as ferulic acid. Therefore, the present invention designs a SAM cofactor metabolic engineering strategy, which can accelerate the methyl cycle in Saccharomyces cerevisiae cells, continuously supply the cofactor SAM, and improve the synthesis efficiency of the target product. This strategy can avoid the exogenous addition of expensive, low transmembrane efficiency and photolabile cofactors or their precursors, while significantly improving the synthesis efficiency of ferulic acid. The SAM cofactor engineering used in the present invention makes the ferulic acid output increase 39% in the shake flask fermentation, reaches 184.2mg/L, and the transformation efficiency of substrate caffeic acid synthetic ferulic acid is improved to 64% by 46%, simultaneously batch formula replenishes Feed fermentation reached the highest yield so far of 3.8g/L. This strategy has the characteristics of high transformation efficiency, low production cost, and broad prospects for industrial application, which proves that SAM cofactor engineering has important potential and application value in the synthesis of ferulic acid and other SAM-dependent natural products in Saccharomyces cerevisiae.
作为一种实施方案,本申请提供一种SAM辅因子工程策略提高酵母阿魏酸合成效率的方法,其特征在于,主要包括以下步骤:As an embodiment, the present application provides a method for improving yeast ferulic acid synthesis efficiency through a SAM cofactor engineering strategy, which is characterized in that it mainly includes the following steps:
(1)在前期构建的咖啡酸酵母底盘细胞中表达烟草(Nicotiana tabacum)来源的咖啡酸氧甲基转移酶NtCOMT1,获得合成阿魏酸的酿酒酵母菌株RB202;(1) Express the caffeic acid oxymethyltransferase NtCOMT1 derived from tobacco (Nicotiana tabacum) in the previously constructed caffeic acid yeast chassis cells, and obtain the ferulic acid-synthesizing Saccharomyces cerevisiae strain RB202;
(2)表达SAM合成途径的三个关键基因,包括酿酒酵母内源的MET6,人工改造的cMTFHR和来自细菌Leishmania infantum的LiMETK1,得到重组酵母菌RB210,实现SAM合成水平的提高,实现阿魏酸合成;(2) Express three key genes in the SAM synthesis pathway, including Saccharomyces cerevisiae endogenous MET6, artificially modified cMTFHR and LiMETK1 from the bacterium Leishmania infantum, to obtain recombinant yeast RB210, which can improve the synthesis level of SAM and realize ferulic acid synthesis;
(3)进一步,通过表达酿酒酵母来源基因ADO1和SAH1,得到重组酵母菌RB218,提高SAM的周转速率,实现甲基高效循环,强化阿魏酸合成。(3) Further, by expressing the Saccharomyces cerevisiae-derived genes ADO1 and SAH1, the recombinant yeast RB218 was obtained, which increased the turnover rate of SAM, realized the efficient cycle of methyl groups, and enhanced the synthesis of ferulic acid.
可选地,密码子优化后的NtCOMT1基因具有如SEQ ID NO:1所示的核苷酸序列,密码子优化后的MET6基因具有如SEQ ID NO:2所示的核苷酸序列,密码子优化后的cMTFHR基因具有如SEQ ID NO:3所示的核苷酸序列,密码子优化后的LiMETK1基因具有如SEQ ID NO:4所示的核苷酸序列,ADO1基因具有如SEQ ID NO:5所示的核苷酸序列;SAH1基因具有如SEQ ID NO:6所示的核苷酸序列。Optionally, the NtCOMT1 gene after codon optimization has the nucleotide sequence shown in SEQ ID NO: 1, the MET6 gene after codon optimization has the nucleotide sequence shown in SEQ ID NO: 2, the codon The optimized cMTFHR gene has the nucleotide sequence shown in SEQ ID NO: 3, the codon-optimized LiMETK1 gene has the nucleotide sequence shown in SEQ ID NO: 4, and the ADO1 gene has the nucleotide sequence shown in SEQ ID NO: The nucleotide sequence shown in 5; SAH1 gene has the nucleotide sequence shown in SEQ ID NO: 6.
可选地,所述方法还包括步骤(4)以20g/L葡萄糖为底物的基础盐培养基中,接种工程酵母菌株,进行发酵,初始接种OD 600为0.1,发酵条件是装液量20/100mL,30℃,220rpm,发酵时间为96h。 Optionally, the method also includes step (4) using 20g/L glucose as a substrate in a basal salt medium to inoculate engineered yeast strains for fermentation, the initial inoculation OD600 is 0.1, and the fermentation condition is a liquid loading capacity of 20 /100mL, 30°C, 220rpm, fermentation time is 96h.
所述增强辅因子供应所表达的基因可以来自于其他物种同工酶的编码基因或其密码子优化基因。The expressed gene for enhanced cofactor supply may come from the coding gene of isozyme of other species or its codon-optimized gene.
上述所述任一工程酵母菌在生产阿魏酸或类似依赖SAM依赖的甲基化产物产品中的应用。Application of any of the above-mentioned engineered yeasts in the production of ferulic acid or similar SAM-dependent methylation products.
本发明属于微生物基因工程与代谢工程应用领域,具体涉及一种酵母SAM辅因子调控策略并用于提高合成阿魏酸及其它SAM依赖的甲基化产物。The invention belongs to the application field of microbial genetic engineering and metabolic engineering, and specifically relates to a yeast SAM cofactor regulation strategy for improving the synthesis of ferulic acid and other SAM-dependent methylation products.
本发明的目的是提供一种辅因子SAM的工程策略,以解决阿魏酸等甲基化产物合成过程中内源SAM供应不足的困难,从而提高酵母细胞工厂的合成效率。The purpose of the present invention is to provide a cofactor SAM engineering strategy to solve the difficulty of insufficient supply of endogenous SAM during the synthesis of ferulic acid and other methylated products, thereby improving the synthesis efficiency of yeast cell factories.
本申请所提供的生产阿魏酸的酿酒酵母菌株构建方法。以前期构建的高产咖啡酸的菌株RB197为起始底盘细胞,过表达咖啡酸氧甲基转移酶基因NtCOMT1(优化的核苷酸序列如SEQ ID NO:1所示)获得菌株RB202,实现从咖啡酸合成阿魏酸。The method for constructing a Saccharomyces cerevisiae strain producing ferulic acid provided by the application. The high caffeic acid-producing strain RB197 constructed earlier was used as the starting chassis cell, and the caffeic acid oxymethyltransferase gene NtCOMT1 (optimized nucleotide sequence shown in SEQ ID NO: 1) was overexpressed to obtain strain RB202. Acid synthesis of ferulic acid.
本申请所提供的提供一种SAM辅因子工程策略,能够显著提高阿魏酸的产量。The present application provides a SAM cofactor engineering strategy, which can significantly increase the yield of ferulic acid.
上述技术方案的方法是在酿酒酵母菌株RB197中过表达SAM合成途径的三个关键酶基因,获得菌株RB210,从而提高工程菌株中SAM的代谢流和合成水平。具体包括过表达MET6(优化的核苷酸序列如SEQ ID NO:2所示),cMTFHR(优化的核苷酸序列如SEQ ID NO:3所示)和LiMETK1(优化的核苷酸序列如SEQ ID NO:4所示)。The method of the above technical solution is to overexpress three key enzyme genes of the SAM synthesis pathway in Saccharomyces cerevisiae strain RB197 to obtain strain RB210, thereby improving the metabolic flow and synthesis level of SAM in the engineering strain. Specifically include overexpressing MET6 (the optimized nucleotide sequence is shown in SEQ ID NO: 2), cMTFHR (the optimized nucleotide sequence is shown in SEQ ID NO: 3) and LiMETK1 (the optimized nucleotide sequence is shown in SEQ ID NO: 3) and LiMETK1 (the optimized nucleotide sequence is shown in SEQ ID NO: 3) ID NO: 4).
进一步,通过表达酿酒酵母内源基因ADO1(核苷酸序列如SEQ ID NO:5所示)和SAH1(核苷酸序列如SEQ ID NO:6所示),得到重组酵母菌RB218,实现高效的甲基循环和SAM周转,支持阿魏酸的高水平合成。Further, by expressing Saccharomyces cerevisiae endogenous genes ADO1 (nucleotide sequence shown in SEQ ID NO: 5) and SAH1 (nucleotide sequence shown in SEQ ID NO: 6), recombinant yeast RB218 was obtained to achieve efficient Methyl cycle and SAM turnover, supporting high-level synthesis of ferulic acid.
进一步地,接种RB218酵母菌株,进行阿魏酸合成发酵。Further, RB218 yeast strain was inoculated to carry out ferulic acid synthesis fermentation.
可选地,在以20g/L葡萄糖为底物的基础盐培养基中进行摇瓶发酵,初始接种OD 600为0.1,发酵条件是装液量20/100mL,30℃,220rpm,发酵时间为96h。 Alternatively, shake flask fermentation is carried out in a basal salt medium with 20g/L glucose as the substrate, the initial inoculation OD600 is 0.1, the fermentation conditions are liquid volume 20/100mL, 30°C, 220rpm, and the fermentation time is 96h .
可选地,在1L发酵罐中进行批式补料发酵,以20g/L葡萄糖为底物的基础盐培养基开始发酵,起始接种体积为0.25L,OD 600为0.2。通过搅拌桨速度(800-1200rpm)控制溶氧为40%,发酵温度为30℃。使用4M的KOH和2M的HCl控制pH维持在5.6。在补料批次阶段,补加200g/L葡萄糖溶液,补料速率与生长偶联,呈指数增加(将μ设置为0.05h-1),以保持恒定的生物量比葡萄糖消耗速率。 Alternatively, batch fed-batch fermentation was carried out in a 1L fermenter, and the fermentation was started on a basal salt medium with 20g/L glucose as the substrate, with an initial inoculum volume of 0.25L and an OD600 of 0.2. Dissolved oxygen is controlled to be 40% by the stirring paddle speed (800-1200rpm), and the fermentation temperature is 30°C. The pH was maintained at 5.6 using 4M KOH and 2M HCl. During the fed-batch phase, additional 200 g/L glucose solution was added, and the feed rate was coupled to growth and increased exponentially (set μ to 0.05 h-1) to maintain a constant biomass-to-glucose consumption rate.
进一步地,对发酵产物进行提取和检测。结果证明SAM辅因子工程策略能够显著增加阿魏酸的产量。Further, the fermentation product is extracted and detected. The results demonstrate that the SAM cofactor engineering strategy can significantly increase the production of ferulic acid.
有益效果:Beneficial effect:
本发明提供了一种SAM辅因子工程策略,以解决阿魏酸等甲基化产物合成过程中内源辅因子供应不足的困难,从而提高其合成效率。The present invention provides a SAM cofactor engineering strategy to solve the difficulty of insufficient supply of endogenous cofactors during the synthesis of ferulic acid and other methylated products, thereby improving their synthesis efficiency.
本发明的辅因子调控方法涉及SAM合成和SAM循环,可以实现内源辅因子SAM的高速周转和高水平供应,避免外源添加昂贵且不稳定的辅因子或其前提,降低成本消耗。The cofactor regulation method of the present invention involves SAM synthesis and SAM cycle, which can realize high-speed turnover and high-level supply of endogenous cofactor SAM, avoid the addition of expensive and unstable cofactor or its prerequisites from exogenous sources, and reduce cost consumption.
本发明应用SAM辅因子工程使得阿魏酸产量达到184.2mg/L,底物咖啡酸合成阿魏酸的转化效率由46%提高到64%,同时批式补料发酵达到迄今最高产量3.8g/L,证明了该辅因子工程策略在细胞工厂工业化的应用潜力。The invention uses SAM cofactor engineering to make the ferulic acid output reach 184.2mg/L, the conversion efficiency of the substrate caffeic acid to synthesize ferulic acid is increased from 46% to 64%, and at the same time, the batch-type fed-batch fermentation reaches the highest yield so far of 3.8g/L L, demonstrating the potential of this cofactor engineering strategy for the industrialization of cell factories.
附图说明Description of drawings
图1示出了酿酒酵母CRISPR/Cas9系统中pgRNA质粒构建过程示意图。。Figure 1 shows a schematic diagram of the pgRNA plasmid construction process in the Saccharomyces cerevisiae CRISPR/Cas9 system. .
图2示出了SAM辅因子工程酵母菌在摇瓶中合成阿魏酸的产量。Figure 2 shows the yield of ferulic acid synthesized by SAM cofactor engineered yeast in shake flasks.
图3示出了SAM辅因子工程策略示意图。Figure 3 shows a schematic diagram of the SAM cofactor engineering strategy.
图4示出了SAM辅因子工程酵母菌在菌批式补料发酵中生产阿魏酸的产量。Figure 4 shows the yield of ferulic acid produced by SAM cofactor engineered yeast in bacterial batch fed-batch fermentation.
具体实施方式Detailed ways
下述非限制性实施例可以使本领域的普通技术人员更全面地理解本发明,但不以任何方式限制本发明。下述实施例中,如无特殊说明,所使用的实验方法均为常规方法,所用材料、试剂等均可从生物或化学公司购买,使用的所有技术和科学术语具有与本申请所属技术领域的普通技术人员通常理解的相同含义。The following non-limiting examples can enable those skilled in the art to understand the present invention more fully, but do not limit the present invention in any way. In the following examples, unless otherwise specified, the experimental methods used are conventional methods, and the materials used, reagents, etc. can be purchased from biological or chemical companies, and all technical and scientific terms used are consistent with those of the technical field of the application. The same meaning as commonly understood by those of ordinary skill.
合成阿魏酸的酿酒酵母菌株可以使用任意生产咖啡酸的酵母菌株作为出发菌株,本申请实施例中使用的是咖啡酸生产菌株RB197。The Saccharomyces cerevisiae strain that synthesizes ferulic acid can use any yeast strain that produces caffeic acid as the starting strain, and the caffeic acid-producing strain RB197 is used in the examples of the present application.
咖啡酸生产菌株RB197的构建:Construction of caffeic acid producing strain RB197:
构建了整合CAS9基因的重组酿酒酵母CEN.PK113-11C-CAS(基因型MATa,SUC2,MAL2-8c,his3Δ,ura3Δ,XI5::(P TEF1-CAS9-T CYC1)),并以此为宿主菌株进行辅因子工程酵母菌株的构建。其中,CEN.PK113-11C-CAS构建方法如下:首先,直接化学合成CAS9和抗性基因KanMX表达盒T AgTEF-KanMX-P AgTEF-P TEF1-CAS9-T CYC1,将表达盒通过融合PCR与XI5上下游500bp融合获得供体DNA片段XI5up-T AgTEF-KanMX-P AgTEF-P TEF1-CAS9-T CYC1-XI5dw,转化酿酒酵母CEN.PK113-11C(可从德国Euroscarf公司购买得到),以同源重组方式整合到XI5位点,通过遗传霉素G418进行阳性菌株筛选,获得菌株CEN.PK113-11C-CAS+KanMX。为了从基因组中去除KanMX抗性基因标签,使用pgRNA-KanMX与融合PCR获得的供体DNA片段XI5up-P TEF1进行转化。使用化学转化法将约500ng的pgRNA-KanMX和供体DNA同时转化进入整合有Cas9蛋白的酵母菌株,在加有组氨酸的SD平板上于30℃静置培养2天;转化子经加有组氨酸的液体SD培养基培养后,通过PCR验证正确,涂布于含有5-氟乳清酸的固体培养基进行质粒丢失,质粒丢失后获得菌株CEN.PK113-11C-CAS,菌株保存备用。进一步转化pgRNA-GAL80和供体DNA片段GAL80up-GAL80dw完成GAL80敲除,获得菌株A0(MATa,SUC2,MAL2-8c,his3Δ,ura3Δ,gal80Δ,XI5::(P TEF1-CAS9-T CYC1)),可实现P GAL7和P GAL10/1表达的途径基因在限糖条件下高效表达。 A recombinant Saccharomyces cerevisiae CEN.PK113-11C-CAS (genotype MATa, SUC2, MAL2-8c, his3Δ, ura3Δ, XI5::(P TEF1 -CAS9-T CYC1 )) integrating the CAS9 gene was constructed and used as a host The strains were constructed for cofactor engineering yeast strains. Among them, the construction method of CEN.PK113-11C-CAS is as follows: First, directly chemically synthesize CAS9 and the resistance gene KanMX expression cassette T AgTEF -KanMX-P AgTEF -P TEF1 -CAS9-T CYC1 , and combine the expression cassette with XI5 by fusion PCR The upstream and downstream 500bp fusions obtained the donor DNA fragment XI5up-T AgTEF -KanMX-P AgTEF -P TEF1 -CAS9-T CYC1 -XI5dw, transformed Saccharomyces cerevisiae CEN.PK113-11C (available from Euroscarf, Germany), and homologous Recombination was integrated into the XI5 site, and positive strains were screened by geneticin G418 to obtain strain CEN.PK113-11C-CAS+KanMX. To remove the KanMX resistance gene tag from the genome, pgRNA-KanMX was transformed with the donor DNA fragment XI5up- PTEF1 obtained by fusion PCR. Using the chemical transformation method, about 500ng of pgRNA-KanMX and donor DNA were simultaneously transformed into the yeast strain integrated with the Cas9 protein, and cultured statically at 30°C for 2 days on the SD plate with histidine added; the transformant was added with After cultured in the liquid SD medium of histidine, it was verified correctly by PCR, and spread on the solid medium containing 5-fluoroorotic acid for plasmid loss. After the plasmid loss, the strain CEN.PK113-11C-CAS was obtained, and the strain was preserved for future use. . Further transform pgRNA-GAL80 and donor DNA fragment GAL80up-GAL80dw to complete GAL80 knockout, and obtain strain A0 (MATa, SUC2, MAL2-8c, his3Δ, ura3Δ, gal80Δ, XI5::( PTEF1 -CAS9-T CYC1 )), The pathway genes that can realize the expression of PGAL7 and PGAL10/1 were highly expressed under the condition of glucose restriction.
利用上述构建的基因编辑菌株A0,通过转化pgRNA-GPP1和GPP1up-T ENO2-CkPTA-P GAL10/1-LmXFPK-T ADH1-GPP1dw敲除GPP1的同时表达CkPTA和LmXFPK,进一步转化pgRNA-XI7和XI7up-T PRM9-P GAL10/1-TAL1-T PYK1-XI7dw表达TAL1,然后转化pgRNA-XI6和XI6up-P GAL7-TKL1-T ENO2-XI6dw表达TKL1,获得辅因子NADPH工程酵母菌株A1。 Using the gene editing strain A0 constructed above, by transforming pgRNA-GPP1 and GPP1up-T ENO2 -CkPTA-P GAL10/1 -LmXFPK-T ADH1 -GPP1dw to knock out GPP1 while expressing CkPTA and LmXFPK, and further transforming pgRNA-XI7 and XI7up -T PRM9 -P GAL10/1 -TAL1-T PYK1 -XI7dw to express TAL1, then transform pgRNA-XI6 and XI6up-P GAL7 -TKL1-T ENO2 -XI6dw to express TKL1, and obtain cofactor NADPH engineering yeast strain A1.
在A1基础上构建酚酸途径。分别依次转化pgRNA-ARO10和ARO10up-T HIS3-ARO7 G141S-P GAL10/1-ARO4 K229L-T ENO2-P GAL7-EcAROL-T ADH1-ARO10dw;pgRNA-PDC5和PDC5up-T CYC1-FjTAL-Sc OPT1-P GAL10/1-SbPAL1 H123F-Sc OPT1-T TDH2-T FBA1-AtCPR1-Sc OPT1-P GAL7-PDC5dw;pgRNA-XII4和XII4up-T PRM9t-PtrC4H2-Sc OPT1-P GAL10/1-PtrC4H1-Sc OPT1-T PYK1-P GAL7-PtrC3H3-Sc OPT1-T DIT1-XII4dw;pgRNA-XII1和XII1up-P GAL7-ARO1-T ENO2-T CPS1-ARO2-P GAL10/1-ARO3-T HIS5-XII1dw;pgRNA-X2和X2up-T PRM9-PahpaB-Sc OPT1-P GAL10/1-SehpaC-Sc OPT1-T HIS3-X2dw;pgRNA-XI8和XI8up-T CPS1-PHA2-P GAL10/1-MtPDH1-Sc OPT1-T HIS5-XI8dw,完成酚酸途径的构建和增强,获得菌株RB197。 Construction of the phenolic acid pathway on the basis of A1. Sequentially transform pgRNA-ARO10 and ARO10up-T HIS3 -ARO7 G141S -P GAL10/1 -ARO4 K229L -T ENO2 -P GAL7 -EcAROL-T ADH1 -ARO10dw; pgRNA-PDC5 and PDC5up-T CYC1 -FjTAL-Sc OPT1 - P GAL10/1 -SbPAL1 H123F -Sc OPT1 -T TDH2 -T FBA1 -AtCPR1-Sc OPT1 -P GAL7 -PDC5dw; pgRNA-XII4 and XII4up-T PRM9t -PtrC4H2-Sc OPT1 -P GAL10/1 -PtrC4H1-Sc OPT1 -T PYK1 -P GAL7 -PtrC3H3-Sc OPT1 -T DIT1 -XII4dw; pgRNA-XII1 and XII1up-P GAL7 -ARO1-T ENO2 -T CPS1 -ARO2-P GAL10/1 -ARO3-T HIS5 -XII1dw; pgRNA- pgRNA-XI8 and XI8up-T CPS1 -PHA2 - P GAL10/1 -MtPDH1 - Sc OPT1 -T HIS5 -XI8dw, completed the construction and enhancement of the phenolic acid pathway, and obtained strain RB197.
咖啡酸生产菌株RB197中各基因的sgRNA表达载体构建过程同实施例1,涉及的sgRNA表达载体包括pgRNA-GAL80(靶向基因GAL80),pgRNA-GPP1(靶向基因GPP1),pgRNA-XI7(靶向位点XI7),pgRNA-XI6(靶向位点XI6),pgRNA-ARO10(靶向基因ARO10),pgRNA-PDC5(靶向基因PDC5),pgRNA-XII4(靶向位点XII4),pgRNA-XII1(靶向位点XII1),pgRNA-X2(靶向位点X2),pgRNA-XI8(靶向位点XI8),靶向序列见表1。对于供体DNA,分别扩增pgRNA载体靶向位点的下游各约500bp序列作为同源臂,之后通过常规融合PCR的方式将需要插入的各个片段进行组装,获得完整的供体DNA分子,与对应位点的pgRNA一起转化酵母,用于基因编辑和菌株改造,各基因信息见表2。The sgRNA expression vector construction process of each gene in the caffeic acid production strain RB197 is the same as that in Example 1, and the sgRNA expression vector involved includes pgRNA-GAL80 (target gene GAL80), pgRNA-GPP1 (target gene GPP1), pgRNA-XI7 (target gene To site XI7), pgRNA-XI6 (target site XI6), pgRNA-ARO10 (target gene ARO10), pgRNA-PDC5 (target gene PDC5), pgRNA-XII4 (target site XII4), pgRNA- XII1 (targeting site XII1), pgRNA-X2 (targeting site X2), pgRNA-XI8 (targeting site XI8), and the targeting sequences are shown in Table 1. For the donor DNA, respectively amplify about 500 bp downstream of the target site of the pgRNA vector as homology arms, and then assemble each fragment to be inserted by conventional fusion PCR to obtain a complete donor DNA molecule, and The pgRNAs of the corresponding sites were transformed into yeast together for gene editing and strain transformation. The information of each gene is shown in Table 2.
表1Table 1
序列名称sequence name M 20 M20 N 20 N 20
pgRNA-GAL80pgRNA-GAL80 SEQ ID NO:17;TTCCAAGGCACATTGTTAAASEQ ID NO: 17; TTCCAAGGCACATTGTTAAA SEQ ID NO:18;CACAATTTGTAATGCAAGGTSEQ ID NO: 18; CACAATTTGTAATGCAAGGT
pgRNA-GPP1pgRNA-GPP1 SEQ ID NO:19;GTCTGGAGCGAACTTGGCAASEQ ID NO: 19; GTCTGGAGCGAACTTGGCAA SEQ ID NO:20;GAATACGTTAACAAGCTAGASEQ ID NO: 20; GAATACGTTAACAAGCTAGA
pgRNA-XI7pgRNA-XI7 SEQ ID NO:21;GTCAGTAACAGTGATTGCTGSEQ ID NO: 21; GTCAGTAACAGTGATTGCTG SEQ ID NO:22;TATGTAGGTTCCGATTAAAGSEQ ID NO: 22; TATGTAGGTTCCGATTAAAG
pgRNA-XI6pgRNA-XI6 SEQ ID NO:23;CGCTACAATTCGGTAAGTTTSEQ ID NO: 23; CGCTACAATTCGGTAAGTTT SEQ ID NO:24;TAGTAAATACAACTATTGGASEQ ID NO: 24; TAGTAAATACAACTATTGGA
pgRNA-ARO10pgRNA-ARO10 SEQ ID NO:25;GAAAACTGATTTCGTATCGASEQ ID NO: 25; GAAAACTGATTTCGTATCGA SEQ ID NO:26;AATATACGAACGAAACAATGSEQ ID NO: 26; AATATACGAACGAAACAATG
pgRNA-PDC5pgRNA-PDC5 SEQ ID NO:27;GATAAGCTTTATGAAGTCAASEQ ID NO: 27; GATAAGCTTTATGAAGTCAA SEQ ID NO:28;ATTTGCCTTGCAAAAATTGTSEQ ID NO: 28; ATTTGCCTTGCAAAAATTGT
pgRNA-XII4pgRNA-XII4 SEQ ID NO:29;TAATGGGGAATTGTACAAATSEQ ID NO: 29; TAATGGGGAATTGTACAAAT SEQ ID NO:30;GTTACCCGCGCTATTTCACASEQ ID NO: 30; GTTACCCGCGCTATTTCACA
pgRNA-XII1pgRNA-XII1 SEQ ID NO:31;CCACTTCTCATGACATATATSEQ ID NO: 31; CCACTTCTCATGACATATAT SEQ ID NO:32;CAATACTAATTAGTCTTTGCSEQ ID NO: 32; CAATACTAATTAGTCTTTGC
pgRNA-X2pgRNA-X2 SEQ ID NO:33;CGGGTCTAGGCCTGCATAATSEQ ID NO: 33; CGGGTCTAGGCCTGCATAAT SEQ ID NO:34;GCTCGTTTCTTTTTTCAGTGSEQ ID NO: 34; GCTCGTTTCTTTTTTTCAGTG
pgRNA-XI8pgRNA-XI8 SEQ ID NO:35;GATGAAATAGCCTCAGTTACSEQ ID NO: 35; GATGAAATAGCCTCAGTTAC SEQ ID NO:36;TTGTCGTGTTACTGATAGTASEQ ID NO: 36; TTGTCGTGTTACTGATAGTA
pgRNA-KanMXpgRNA-KanMX SEQ ID NO:37;GGTTCTAGAAGTGCCCTTTGSEQ ID NO: 37; GGTTCTAGAAGTGCCCTTTG SEQ ID NO:38;ATTCTACCGATTTATCATGCSEQ ID NO: 38; ATTCTACCGATTTATCATGC
表2基因名称及序列编号Table 2 Gene name and sequence number
编号serial number 基因名称gene name 来源source 序列编号 serial number
11 GAL80GAL80 Saccharomyces cerevisiaeSaccharomyces cerevisiae SEQ ID NO:39SEQ ID NO: 39
22 TKL1TKL1 Saccharomyces cerevisiaeSaccharomyces cerevisiae SEQ ID NO:40SEQ ID NO: 40
33 TAL1TAL1 Saccharomyces cerevisiaeSaccharomyces cerevisiae SEQ ID NO:41SEQ ID NO: 41
55 LmXFPK-Sc OPT1 LmXFPK-Sc OPT1 Leuconostoc mesenteroidesLeuconostoc mesenteroides SEQ ID NO:42SEQ ID NO: 42
66 CkPTA-Sc OPT1 CkPTA-Sc OPT1 Clostridium kluyveriClostridium kluyveri SEQ ID NO:43SEQ ID NO: 43
77 ARO4 K229L ARO4 K229L Saccharomyces cerevisiaeSaccharomyces cerevisiae SEQ ID NO:44SEQ ID NO: 44
88 ARO7 G141S ARO7 G141S Saccharomyces cerevisiaeSaccharomyces cerevisiae SEQ ID NO:45SEQ ID NO: 45
99 EcAROLECAROL Escherichia coliEscherichia coli SEQ ID NO:46SEQ ID NO: 46
1010 ARO1ARO1 Saccharomyces cerevisiaeSaccharomyces cerevisiae SEQ ID NO:47SEQ ID NO: 47
1111 ARO2ARO2 Saccharomyces cerevisiaeSaccharomyces cerevisiae SEQ ID NO:48SEQ ID NO: 48
1212 ARO3ARO3 Saccharomyces cerevisiaeSaccharomyces cerevisiae SEQ ID NO:49SEQ ID NO: 49
1313 PHA2PHA2 Saccharomyces cerevisiaeSaccharomyces cerevisiae SEQ ID NO:50SEQ ID NO: 50
1414 MtPDH1-Sc OPT1 MtPDH1-Sc- OPT1 Medicago truncatulaMedicago truncatula SEQ ID NO:51SEQ ID NO: 51
1515 FjTAL-Sc OPT1 FjTAL-Sc OPT1 Flavobacterium johnsoniaeFlavobacterium johnsoniae SEQ ID NO:52SEQ ID NO: 52
1616 SbPAL1 H123F-Sc OPT1 SbPAL1 H123F -Sc OPT1 Sorghum bicolorSorghum bicolor SEQ ID NO:53SEQ ID NO: 53
1717 AtCPR1-Sc OPT1 AtCPR1-Sc OPT1 Arabidopsis thalianaArabidopsis thaliana SEQ ID NO:54SEQ ID NO: 54
1818 PtrC4H1-Sc OPT1 PtrC4H1-Sc OPT1 Populus trichocarpaPopulus trichocarpa SEQ ID NO:55SEQ ID NO: 55
1919 PtrC4H2-Sc OPT1 PtrC4H2-Sc OPT1 Populus trichocarpaPopulus trichocarpa SEQ ID NO:56SEQ ID NO: 56
2020 PtrC3H-Sc OPT1 PtrC3H-Sc OPT1 Populus trichocarpaPopulus trichocarpa SEQ ID NO:57SEQ ID NO: 57
21twenty one PaHPAB-Sc OPT1 PaHPAB-Sc OPT1 Pseudomonas aeruginosaPseudomonas aeruginosa SEQ ID NO:58SEQ ID NO: 58
22twenty two SeHPAC-Sc OPT1 SeHPAC-Sc OPT1 Sulfobacillus acidophilusSulfobacillus acidophilus SEQ ID NO:59SEQ ID NO: 59
注:Sc OPT1表明将基因按照酿酒酵母偏好性进行密码子优化。 Note: Sc OPT1 indicates that the gene is codon-optimized according to S. cerevisiae preference.
实施例中所用培养基如下:The medium used in the embodiment is as follows:
YPD培养基:20g/L葡萄糖,20g/L蛋白胨,10g/L酵母粉;YPD medium: 20g/L glucose, 20g/L peptone, 10g/L yeast powder;
SD培养基:20g/L葡萄糖,6.7g/L YNB,使用时添加组氨酸0.02g/L;SD medium: 20g/L glucose, 6.7g/L YNB, add histidine 0.02g/L when used;
发酵培养基(基础成分培养基):(NH 4) 2SO 4 2.5g/L,KH 2PO 4 14.4g/L,MgSO 4·7H 2O 0.5g/L,加入约900mL ddH 2O,调节pH为5.6,定容至950mL,115℃灭菌30min。灭菌后,补加1mL维生素溶液(配方见表4)和2mL微量金属溶液(配方见表3),根据需要添加组氨酸和尿嘧啶(40mg/L)。向发酵培养基中添加葡糖糖到20g/L,用于酚酸发酵。 Fermentation medium (basic component medium): (NH 4 ) 2 SO 4 2.5g/L, KH 2 PO 4 14.4g/L, MgSO 4 7H 2 O 0.5g/L, add about 900mL ddH 2 O, adjust The pH is 5.6, the volume is adjusted to 950mL, and sterilized at 115°C for 30min. After sterilization, add 1mL vitamin solution (see Table 4 for recipe) and 2mL trace metal solution (see Table 3 for recipe), and add histidine and uracil (40mg/L) as needed. Glucose was added to the fermentation medium to 20g/L for phenolic acid fermentation.
表3微量金属溶液配置方法(1L溶液):Table 3 Trace metal solution configuration method (1L solution):
编号serial number 试剂Reagent 重量[g]Weight [g]
11 FeSO 4·7H 2O FeSO 4 7H 2 O 3.03.0
22 ZnSO 4·7H 2O ZnSO 4 7H 2 O 4.54.5
33 CaCl 2·2H 2O CaCl 2 2H 2 O 4.54.5
44 MnCl 2·4H 2O MnCl 2 4H 2 O 1.031.03
55 CoCl 2·6H 2O CoCl 2 6H 2 O 0.30.3
66 CuSO 4·5H 2O CuSO 4 5H 2 O 0.30.3
77 Na 2MoO 4·2H 2O Na 2 MoO 4 2H 2 O 0.40.4
88 H 3BO 3 H 3 BO 3 1.01.0
99 KIKI 0.10.1
1010 Na 2EDTA·2H 20 Na 2 EDTA·2H 2 0 19.019.0
表4维生素溶液配置方法(1L溶液):Table 4 Vitamin solution configuration method (1L solution):
编号serial number 名称name 重量[g]Weight [g]
11 D-生物素D-biotin 0.050.05
22 D-泛酸钙Calcium D-pantothenate 1.01.0
33 硫胺Thiamine 1.01.0
44 吡哆醇Pyridoxine 1.01.0
55 烟酸niacin 1.01.0
66 对氨基苯甲酸p-aminobenzoic acid 0.20.2
77 肌醇Inositol 25.025.0
实施例1Example 1
构建合成阿魏酸的酿酒酵母菌株Construction of a Saccharomyces cerevisiae strain that synthesizes ferulic acid
阿魏酸是通过咖啡酸氧甲基转移酶转化咖啡酸而来,是一步甲基化反应。因此,在上述构建的咖啡酸生产菌株RB197,过表达NtCOMT1,发现其能够较为高效地合成阿魏酸。Ferulic acid is converted from caffeic acid by caffeic acid oxymethyltransferase, which is a one-step methylation reaction. Therefore, NtCOMT1 was overexpressed in the caffeic acid producing strain RB197 constructed above, and it was found that it can synthesize ferulic acid more efficiently.
(1)过表达包括NtCOMT1在内的氧甲基转移酶(1) Overexpression of oxygen methyltransferases including NtCOMT1
使用启动子P GAL10/1表达外源途径,实现在限糖条件下合成阿魏酸,减少对细胞生长的影响。 The promoter P GAL10/1 was used to express the exogenous pathway to realize the synthesis of ferulic acid under the condition of sugar restriction and reduce the impact on cell growth.
利用起始菌株RB197,通过转化化学转化法和CRISPR技术将外源基因NtCOMT1整合在酵母基因组中获得菌株RB202。具体做法是:挑取菌株单克隆到3mL的YPD培养基中,以220rpm,30℃恒温过夜培养16h;接种到20mL的YPD培养基(100mL摇瓶)中,保证初始OD 600为0.1,培养约6小时,使得OD 600达到0.6-1.0;以2000g,室温离心5min收集细胞,加入1mL 0.1M的LiAc溶液重悬细胞,并转移至2mL无菌离心管中;2000g离心2min收集细胞,重悬于200uL的0.1M的LiAc中,置于冰上获得感受态细胞;在1.5mL的离心管中加入120μL的PEG3350溶液(50%)、18μL的1.0M的LiAc溶液、5μL的10mg/mL的单链保护ssDNA,混匀后分别加入500ng含有目标基因NtCOMT1表达框的供体DNA(XII5up-T CSP1-NtCOMT1-Sc OPT1-P GAL10/1-NtCOMT1-T HIS5-XII5dw)和gRNA表达质粒,再加入25μL的感受态细胞后充分混匀;将转化体系置于30℃水浴锅温浴30min;然后转移到42℃水浴锅热激15min;立即置于冰上2min;2000g离心2min收集细胞,500μL灭菌水洗1次,200ul灭菌水重悬后涂SD平板筛选;30℃培养3天后挑选平板单菌落进行基因鉴定。 Using the starting strain RB197, the exogenous gene NtCOMT1 was integrated into the yeast genome by transformation chemical transformation method and CRISPR technology to obtain strain RB202. The specific method is: pick a single clone of the strain and put it in 3 mL of YPD medium, culture it overnight at 220 rpm at 30°C for 16 hours; inoculate it into 20 mL of YPD medium (100 mL shake flask), ensure that the initial OD600 is 0.1, and cultivate for about After 6 hours, the OD600 reached 0.6-1.0; centrifuged at 2000g for 5min at room temperature to collect the cells, added 1mL of 0.1M LiAc solution to resuspend the cells, and transferred to a 2mL sterile centrifuge tube; centrifuged at 2000g for 2min to collect the cells, and resuspended in 200uL of 0.1M LiAc, placed on ice to obtain competent cells; add 120μL of PEG3350 solution (50%), 18μL of 1.0M LiAc solution, 5μL of 10mg/mL single-chain Protect ssDNA, add 500ng of donor DNA (XII5up-T CSP1 -NtCOMT1-Sc OPT1 -P GAL10/1 -NtCOMT1-T HIS5 -XII5dw) and gRNA expression plasmid containing target gene NtCOMT1 expression cassette after mixing, then add 25μL After mixing the competent cells thoroughly; place the transformation system in a 30°C water bath for 30 minutes; then transfer to a 42°C water bath for heat shock for 15 minutes; immediately place it on ice for 2 minutes; Second, resuspend in 200ul sterilized water and apply SD plate for screening; after culturing at 30°C for 3 days, select a single colony on the plate for gene identification.
以上sgRNA表达载体构建过程如图1所示,本发明中使用的所有sgRNA表达载体除20bp靶向序列不同以外,其余部分完全相同。简单来说,首先使用引物6005(SEQ ID NO:8,GATCATTTATCTTTCACTGCGGAGAAG)从pgRNA(SEQ ID NO:7)中扩增载体骨架S1;接着,分别扩增sgRNA-1和sgRNA-2用于靶向酵母基因组位点进行编辑和外源基因插入,其中sgRNA-1使用引物p1(SEQ ID NO:9,GCGGTTAGCTCCTTCGGTCCTCCGATCGTTGTCAGAAGTAAGTTGGCCGCAGTGTTATC)和pX1(AAACTTCTCCGCAGTGAAAGATAAATGATC(M 20)GTTTTAGAGCTAGAAATAG,其中M 20为可替换20bp靶向序列),sgRNA-2使用引物p2(SEQ ID NO:10,GATAACACTGCGGCCAACTTACTTCTGACAACGATCGGAGGACCGAAGGAGCTAACCGC)和pX2(AAACTTCTCCGCAGTGAAAGATAAATGATC(N 20)GTTTTAGAGCTAGAAATAG,其中N(N 20)为可替换的另外20bp靶向序列);最后,sgRNA片段和载体骨架片段使用Gibson Assembly的方法进行克隆连接,获得的重组载体测序后进行应用。实施例1~2中pX1和pX2中M 20和N 20的替换序列及替换后对应的序列名称详见表5,本发明实施例1~2中涉及的sgRNA表达载体包括pgRNA-XII5(靶向位点XII5),pgRNA-HO(靶向位点HO),pgRNA-V3(靶向基因V3)。对于供体DNA,分别扩增pgRNA载体靶向位点的下游各约500bp序列作为同源臂,之后通过常规融合PCR的方式将需要插入的各个片段进行组装,获得完整的供体DNA分子,与对应位点的pgRNA一起转化酵母,用于基因编辑和菌株改造。各基因信息见表6。 The construction process of the above sgRNA expression vectors is shown in Figure 1. All the sgRNA expression vectors used in the present invention are identical except for the 20bp targeting sequence. Briefly, the vector backbone S1 was first amplified from pgRNA (SEQ ID NO: 7) using primer 6005 (SEQ ID NO: 8, GATCATTTATTCTTTCACTGCGGAGAAG); then, sgRNA-1 and sgRNA-2 were amplified for targeting yeast Genomic loci were edited and exogenous gene inserted, wherein sgRNA-1 used primers p1 (SEQ ID NO: 9, GCGGTTAGCTCCTTCGGTCCTCCGATCGTTGTCAGAAGTAAGTTGGCCGCAGTGTTATC) and pX1 (AAACTTCTCCGCAGTGAAAGATAAATGATC( M20 )GTTTTGAGCTAGAAATAG, where M20 is an alternative 20bp targeting sequence), sgRNA -2 Use primers p2 (SEQ ID NO: 10, GATAACACTGCGGCCAACTTACTTCTGACAACGATCGGAGGACCGAAGGAGCTAACCGC) and pX2 (AAACTTCTCCGCAGTGAAAGATAAATGATC(N 20 )GTTTTAGAGCTAGAAATAG, where N(N 20 ) is an alternative 20bp targeting sequence); finally, sgRNA fragment and vector backbone fragment use The Gibson Assembly method was used for cloning and connection, and the obtained recombinant vector was sequenced and applied. The replacement sequences of M20 and N20 in pX1 and pX2 in Examples 1-2 and the corresponding sequence names after replacement are shown in Table 5. The sgRNA expression vectors involved in Examples 1-2 of the present invention include pgRNA-XII5 (targeting site XII5), pgRNA-HO (targeting site HO), pgRNA-V3 (targeting gene V3). For the donor DNA, respectively amplify about 500 bp downstream of the target site of the pgRNA vector as homology arms, and then assemble each fragment to be inserted by conventional fusion PCR to obtain a complete donor DNA molecule, and The pgRNAs of the corresponding sites are transformed into yeast together for gene editing and strain transformation. The information of each gene is shown in Table 6.
表5table 5
序列名称sequence name MMMMMM NNNNNN
pgRNA-XII5pgRNA-XII5 SEQ ID NO:11,CTTATCGATATTTTGTATATSEQ ID NO: 11, CTTATCGATATTTTGTATAT SEQ ID NO:12,TGGTACTACTGTCCTGATGTSEQ ID NO: 12, TGGTACTACTGTCCTGATGT
pgRNA-HOpgRNA-HO SEQ ID NO:13,GTTCGTGAAGCATTCTTAGCSEQ ID NO: 13, GTTCGTGAAGCATTCTTAGC SEQ ID NO:14,GCTCGCCGTACATAAATTCASEQ ID NO: 14, GCTCGCCGTACATAAATTCA
pgRNA-V3pgRNA-V3 SEQ ID NO:15,GTGCTCTTAAGTCGTAATGASEQ ID NO: 15, GTGCTCTTAAGTCGTAATGA SEQ ID NO:16,CGTCTAGAAGAACAGCACATSEQ ID NO: 16, CGTCTAGAAGAACAGCACAT
表6Table 6
编号serial number 序列名称sequence name 来源source 序列编号 serial number
11 NtCOMT1-Sc OPT1 NtCOMT1-Sc OPT1 Nicotiana tabacumNicotiana tabacum SEQ ID NO:1SEQ ID NO:1
22 MET6-Sc OPT1 MET6-Sc OPT1 Saccharomyces cerevisiaeSaccharomyces cerevisiae SEQ ID NO:2SEQ ID NO:2
33 cMTFHR-Sc OPT1 cMTFHR-Sc OPT1 人工设计artificial design SEQ ID NO:3SEQ ID NO:3
44 LiMETK1-Sc OPT1 LiMETK1-Sc OPT1 Leishmania infantumLeishmania infantum SEQ ID NO:4SEQ ID NO:4
55 ADO1-Sc OPT1 ADO1-Sc OPT1 Saccharomyces cerevisiaeSaccharomyces cerevisiae SEQ ID NO:5SEQ ID NO:5
66 SAH1-Sc OPT1 SAH1-Sc- OPT1 Saccharomyces cerevisiaeSaccharomyces cerevisiae SEQ ID NO:6SEQ ID NO:6
77 pgRNApgRNA // SEQ ID NO:7SEQ ID NO:7
注:Sc OPT1表明将基因按照酿酒酵母偏好性进行密码子优化。 Note: Sc OPT1 indicates that the gene is codon-optimized according to S. cerevisiae preference.
(2)发酵菌株合成阿魏酸(2) Fermentation strains synthesize ferulic acid
选择3个阳性克隆进行发酵。在含20g/L葡萄糖的基础培养基条件下进行阿魏酸的发酵实验,初始接种OD 600为0.1,发酵条件是装液量20/100mL,30℃,220rpm,发酵时间为96h。 Three positive clones were selected for fermentation. The fermentation experiment of ferulic acid was carried out under the condition of the basal medium containing 20g/L glucose, the initial inoculation OD600 was 0.1, the fermentation condition was 20/100mL, 30℃, 220rpm, and the fermentation time was 96h.
然后提取和检测阿魏酸。取50μL发酵样品,加入450μL无菌水,再加入500μL乙醇后充分涡旋混匀;13000g离心5min,取500μL上清过0.22μm水相微孔滤膜后获得酚酸样品。样品检测使用岛津HPLC,色谱柱为3×100mm 2.7um Poroshell 120 EC-C18(Agilent),流速为0.8mL/min,流动相A为H 2O+0.05%HCOOH,流动相B为ACN+0.05%HCOOH,紫外检测器检测波长为280nm或330nm。具体流动相梯度为95%-A(0min),90%-A(3min),88%-A(4-5min),85%-A(6-7min),40%-A(10min),95%-A(12-14min)。 Ferulic acid was then extracted and detected. Take 50 μL fermentation sample, add 450 μL sterile water, then add 500 μL ethanol, vortex and mix well; centrifuge at 13,000 g for 5 min, take 500 μL supernatant and pass through a 0.22 μm aqueous microporous membrane to obtain the phenolic acid sample. Samples were detected using Shimadzu HPLC, the chromatographic column was 3×100mm 2.7um Poroshell 120 EC-C18 (Agilent), the flow rate was 0.8mL/min, the mobile phase A was H 2 O+0.05%HCOOH, and the mobile phase B was ACN+0.05 %HCOOH, the detection wavelength of the ultraviolet detector is 280nm or 330nm. The specific mobile phase gradient is 95%-A (0min), 90%-A (3min), 88%-A (4-5min), 85%-A (6-7min), 40%-A (10min), 95 %-A (12-14min).
结果发现在工程菌中过表达NtCOMT1能够相对高效地合成阿魏酸,结果如图2中RB202所示,摇瓶发酵阿魏酸达到132.1mg/L。It was found that overexpression of NtCOMT1 in engineering bacteria can synthesize ferulic acid relatively efficiently. As shown in Figure 2 RB202, ferulic acid reached 132.1 mg/L in shake flask fermentation.
实施例2Example 2
SAM辅因子工程提高阿魏酸的产量SAM cofactor engineering enhances ferulic acid production
阿魏酸的合成需要大量SAM辅因子作为甲基供体参与反应,因此在强化SAM合成途径的基础上进一步提高甲基循环和SAM再生速度,可以为阿魏酸高效合成提供充足的辅因子,显著提高酵母合成阿魏酸的产量(图3)。The synthesis of ferulic acid requires a large number of SAM cofactors as methyl donors to participate in the reaction. Therefore, on the basis of strengthening the SAM synthesis pathway, further improving the methyl cycle and SAM regeneration speed can provide sufficient cofactors for the efficient synthesis of ferulic acid. Significantly increased the yield of ferulic acid synthesized by yeast (Figure 3).
(1)强化SAM合成途径(1) Strengthen the SAM synthesis pathway
仍然设计使用GAL系统启动子(P GAL10/1或P GAL7)表达外源途径,实现在限糖条件下表达外源基因,减少对细胞生长的影响。以阿魏酸生产菌株RB202起始,通过上述相同方法进行基因编辑,使用pgRNA-HO和供体DNA分子HOup-T HSP26-MET6-P GAL10/1-cMTFHR-T PDC6-P GAL7-liMetK1-Sc OPT1-T UBX6-HOdw表达SAM合成途径基因,MET6(优化的核苷酸序列如SEQ ID NO:2所示),cMTFHR(优化的核苷酸序列如SEQ ID NO:3所示)和LiMETK1(优化的核苷酸序列如SEQ ID NO:4所示)。分子鉴定后获得阳性菌株RB210。 It is still designed to use the GAL system promoter ( PGAL10/1 or PGAL7 ) to express the exogenous pathway, so as to realize the expression of exogenous genes under the condition of sugar restriction and reduce the impact on cell growth. Starting with the ferulic acid producing strain RB202, gene editing was performed by the same method as above, using pgRNA-HO and the donor DNA molecule HOup-T HSP26 -MET6-P GAL10/1 -cMTFHR-T PDC6 -P GAL7 -liMetK1-Sc OPT1 -T UBX6 -HOdw expresses SAM synthesis pathway genes, MET6 (the optimized nucleotide sequence is shown in SEQ ID NO: 2), cMTFHR (the optimized nucleotide sequence is shown in SEQ ID NO: 3) and LiMETK1 ( The optimized nucleotide sequence is shown in SEQ ID NO: 4). The positive strain RB210 was obtained after molecular identification.
(2)加速甲基循环和SAM再生(2) Accelerate methyl cycle and SAM regeneration
Sah1催化可逆反应,自然条件下由同型半胱氨酸合成腺苷同型半胱氨酸方向进行反应,不利于合成阿魏酸。因此,通过过表达S-腺苷同型半胱氨酸水解酶SAH1和腺苷激酶ADO1可以实现消耗副产物腺苷的同时,改变反应的动力学方向,由腺苷同型半胱氨酸合成同型半胱氨酸方向进行。Sah1 catalyzes a reversible reaction, and the reaction proceeds in the direction of synthesizing adenosylhomocysteine from homocysteine under natural conditions, which is not conducive to the synthesis of ferulic acid. Therefore, by overexpressing S-adenosylhomocysteine hydrolase SAH1 and adenosine kinase ADO1, it is possible to consume the by-product adenosine and change the kinetic direction of the reaction to synthesize homocysteine from adenosylhomocysteine. in the direction of cystine.
仍然设计使用GAL系统启动子(P GAL10/1或P GAL7)表达外源基因SAH1和ADO1,使其在限糖条件下表达。以阿魏酸生产菌株RB210起始,通过上述相同方法进行基因编辑,使用pgRNA-V3和供体DNA分子V3up-T PRM9-ADO1-P GAL10/1-SAH1-T PYK1-V3dw表达ADO1(核苷酸序列如SEQ ID NO:5所示)和SAH1(核苷酸序列如SEQ ID NO:6所示),得到重组酵母菌RB218,实现高效的甲基循环和SAM周转,支持阿魏酸的高水平合成。 It is still designed to use the GAL system promoter ( PGAL10/1 or PGAL7 ) to express the exogenous genes SAH1 and ADO1, so that they can be expressed under the condition of sugar restriction. Starting with the ferulic acid producing strain RB210, gene editing was carried out by the same method as above, using pgRNA-V3 and the donor DNA molecule V3up-T PRM9 -ADO1-P GAL10/1 -SAH1-T PYK1 -V3dw to express ADO1 (nucleoside Acid sequence as shown in SEQ ID NO: 5) and SAH1 (nucleotide sequence as shown in SEQ ID NO: 6), to obtain recombinant yeast RB218, to achieve efficient methyl cycle and SAM turnover, support the high ferulic acid horizontal compositing.
(3)发酵菌株合成阿魏酸(3) Fermentation strains synthesize ferulic acid
选择菌株RB210和RB218的3个阳性克隆,通过上述方法进行发酵和化合物提取。样品检测使用岛津HPLC进行,检测方法与上述一致。结果发现在工程菌RB210中阿魏酸产量达到143.7mg/L,相对于对照菌株RB202提高9%(图2)。工程菌RB218的阿魏酸产量进一步提高28%,达到184.2mg/L。通过计算咖啡酸的转化率(咖啡酸转化率%=100%×[阿魏酸产量/(咖啡酸产量+阿魏酸产量)])。特别是咖啡酸转化为阿魏酸的效率由46%提高到64%,显著提高了阿魏酸的合成效率。Three positive clones of strains RB210 and RB218 were selected, and fermented and compound extracted by the above method. Sample detection was carried out by Shimadzu HPLC, and the detection method was consistent with the above. As a result, it was found that the yield of ferulic acid in the engineered strain RB210 reached 143.7 mg/L, which was 9% higher than that of the control strain RB202 (Fig. 2). The ferulic acid production of engineering strain RB218 was further increased by 28%, reaching 184.2mg/L. By calculating the conversion rate of caffeic acid (caffeic acid conversion rate%=100%×[ferulic acid production/(caffeic acid production+ferulic acid production)]). In particular, the conversion efficiency of caffeic acid into ferulic acid was increased from 46% to 64%, which significantly improved the synthesis efficiency of ferulic acid.
(4)批式补料发酵合成阿魏酸(4) Synthesis of ferulic acid by batch fed-batch fermentation
为了验证SAM辅因子工程合成阿魏酸的潜力,对RB218进行批式补料发酵。在1L发酵罐中,以20g/L葡萄糖为底物的基础盐培养基开始发酵,起始接种体积为0.25L,OD600为0.2。通过搅拌桨速度(800-1200rpm)控制溶氧为40%,发酵温度为30℃。使用4M的KOH和2M的HCl控制pH维持在5.6。在补料批次阶段,每24小时补加500g/L葡萄糖溶液至葡萄糖浓度到20g/L。最终发酵86h达到迄今为止最高的阿魏酸产量3.8g/L(图4)。这一结果证实了酿酒酵母NADPH和FADH 2辅因子工程在酚酸合成中的潜力和重要应用价值。 To verify the potential of SAM cofactor engineering to synthesize ferulic acid, RB218 was subjected to fed-batch fermentation. In a 1L fermenter, start fermentation with basal salt medium with 20g/L glucose as the substrate, the initial inoculum volume is 0.25L, and the OD600 is 0.2. Dissolved oxygen is controlled to be 40% by the stirring paddle speed (800-1200rpm), and the fermentation temperature is 30°C. The pH was maintained at 5.6 using 4M KOH and 2M HCl. During the fed batch phase, 500 g/L glucose solution was added every 24 hours until the glucose concentration reached 20 g/L. After 86 hours of final fermentation, the highest ferulic acid yield so far was 3.8g/L (Fig. 4). This result confirmed the potential and important application value of S. cerevisiae NADPH and FADH 2 cofactor engineering in phenolic acid synthesis.
以上所述,仅是本申请的几个实施例,并非对本申请做任何形式的限制,虽然本申请以较佳实施例揭示如上,然而并非用以限制本申请,任何熟悉本专业的技术人员,在不脱离本申请技术方案的范围内,利用上述揭示的技术内容做出些许的变动或修饰均等同于等效实施案例,均属于技术方案范围内。The above are only a few embodiments of the application, and do not limit the application in any form. Although the application is disclosed as above with preferred embodiments, it is not intended to limit the application. Any skilled person familiar with this field, Without departing from the scope of the technical solution of the present application, any changes or modifications made using the technical content disclosed above are equivalent to equivalent implementation cases, and all belong to the scope of the technical solution.

Claims (16)

  1. 一种提高酿酒酵母SAM辅因子供应的方法,其特征在于,所述方法包括:A method for improving the supply of saccharomyces cerevisiae SAM cofactor, characterized in that the method comprises:
    在酿酒酵母中导入MET6基因、cMTFHR基因、LiMETK1基因、SAH1基因和ADO1基因。MET6 gene, cMTFHR gene, LiMETK1 gene, SAH1 gene and ADO1 gene were introduced into Saccharomyces cerevisiae.
  2. 根据权利要求1所述的方法,其特征在于,所述方法包括:The method according to claim 1, characterized in that the method comprises:
    将含有T HSP26-MET6-P GAL10/1-cMTFHR-T PDC6-P GAL7-liMetK1-Sc OPT1-T UBX6的DNA片段整合到酿酒酵母的HO位点; A DNA fragment containing T HSP26 -MET6-P GAL10/1 -cMTFHR-T PDC6 -P GAL7 -liMetK1-Sc OPT1 -T UBX6 was integrated into the HO site of Saccharomyces cerevisiae;
    将含有T PRM9-ADO1-P GAL10/1-SAH1-T PYK1的DNA片段整合到酿酒酵母的V3位点。 A DNA fragment containing T PRM9 -ADO1-P GAL10/1 -SAH1-T PYK1 was integrated into the V3 locus of S. cerevisiae.
  3. 根据权利要求1所述的方法,其特征在于,MET6基因的核苷酸序列如SEQ ID NO:2所示;method according to claim 1, is characterized in that, the nucleotide sequence of MET6 gene is as shown in SEQ ID NO:2;
    cMTFHR基因的核苷酸序列如SEQ ID NO:3所示;The nucleotide sequence of the cMTFHR gene is shown in SEQ ID NO: 3;
    LiMETK1基因的核苷酸序列如SEQ ID NO:4所示;The nucleotide sequence of the LiMETK1 gene is shown in SEQ ID NO: 4;
    ADO1基因的核苷酸序列如SEQ ID NO:5所示;The nucleotide sequence of the ADO1 gene is shown in SEQ ID NO: 5;
    SAH1基因的核苷酸序列如SEQ ID NO:6所示。The nucleotide sequence of the SAH1 gene is shown in SEQ ID NO:6.
  4. 根据权利要求1所述的方法,其特征在于,所述酿酒酵母为阿魏酸生产菌株;The method according to claim 1, wherein said Saccharomyces cerevisiae is a ferulic acid production strain;
    所述阿魏酸生产菌株通过在产咖啡酸菌株中导入NtCOMT1基因得到。The ferulic acid producing strain is obtained by introducing the NtCOMT1 gene into the caffeic acid producing strain.
  5. 根据权利要求4所述的方法,其特征在于,所述NtCOMT1基因的核苷酸序列如SEQ ID NO:1所示。The method according to claim 4, wherein the nucleotide sequence of the NtCOMT1 gene is as shown in SEQ ID NO: 1.
  6. 根据权利要求4所述的方法,其特征在于,在产咖啡酸菌株中导入NtCOMT1基因为T CSP1-NtCOMT1-Sc OPT1-P GAL10/1-NtCOMT1-T HIS5整合到产咖啡酸菌株的XII5位点。 The method according to claim 4, wherein the NtCOMT1 gene is introduced into the caffeic acid-producing bacterial strain as T CSP1 -NtCOMT1-Sc OPT1 -P GAL10/1 -NtCOMT1-T HIS5 integrated into the XII5 site of the caffeic acid-producing bacterial strain .
  7. 根据权利要求4所述的方法,其特征在于,所述产咖啡酸菌株通过在酿酒酵母出发菌株中导入酚酸合成途径相关基因得到:The method according to claim 4, wherein the caffeic acid producing strain is obtained by introducing genes related to the phenolic acid synthesis pathway into the starting strain of Saccharomyces cerevisiae:
    所述酚酸合成途径相关基因包括Aro4 K229L、Aro7 G141S、EcAROL、ARO1、ARO2、ARO3、PHA2、MtPDH1、FjTAL、SbPAL1 H123F、AtCPR1、PtrC4H1、PtrC4H2、PtrC3H、PaHPAB、SeHPAC中的至少一种。 The phenolic acid synthesis pathway-related genes include at least one of Aro4 K229L , Aro7 G141S , EcAROL, ARO1, ARO2, ARO3, PHA2, MtPDH1, FjTAL, SbPAL1 H123F , AtCPR1, PtrC4H1, PtrC4H2, PtrC3H, PaHPAB, SeHPAC.
  8. 根据权利要求7所述的方法,其特征在于,所述酚酸合成途径相关基因包括具有如SEQ ID NO:44所示核苷酸序列的Aro4 K229L、具有如SEQ ID NO:45所示核苷酸序列的Aro7 G141S、具有如SEQ ID NO:46所示核苷酸序列的EcAROL、具有如SEQ ID NO:47所示的核苷酸序列的ARO1、具有SEQ ID NO:48所示核苷酸序列的ARO2、具有如SEQ ID NO:49所示核苷酸序列的ARO3、具有如SEQ ID NO:50所示核苷酸序列的PHA2、具有如SEQ ID NO:51所示核苷酸序列的MtPDH1、具有如SEQ ID NO:52所示核苷酸序列的FjTAL,具有如SEQ ID NO:53所示核苷酸序列的SbPAL1 H123F、具有如SEQ ID NO:54所示核苷酸序列的AtCPR1、具有如SEQ ID NO:55所示核苷酸序列的PtrC4H1、具有如SEQ ID NO:56所示核苷酸序列的PtrC4H2、具有如SEQ ID NO:57所示核苷酸序列的PtrC3H、具有如SEQ ID NO:58所示核苷酸序列的PaHPAB、具有如SEQ ID NO:59所示核苷酸序列的SeHPAC中的至少一种。 The method according to claim 7, wherein the phenolic acid synthesis pathway-related genes include Aro4 K229L having a nucleotide sequence as shown in SEQ ID NO: 44, Aro4 K229L having a nucleotide sequence as shown in SEQ ID NO: 45 Aro7 G141S of the acid sequence, EcAROL having the nucleotide sequence shown in SEQ ID NO: 46, ARO1 having the nucleotide sequence shown in SEQ ID NO: 47, having the nucleotide shown in SEQ ID NO: 48 ARO2 of the sequence, ARO3 having the nucleotide sequence shown in SEQ ID NO: 49, PHA2 having the nucleotide sequence shown in SEQ ID NO: 50, and PHA having the nucleotide sequence shown in SEQ ID NO: 51 MtPDH1, FjTAL having the nucleotide sequence shown in SEQ ID NO: 52, SbPAL1 H123F having the nucleotide sequence shown in SEQ ID NO: 53, AtCPR1 having the nucleotide sequence shown in SEQ ID NO: 54 , PtrC4H1 having the nucleotide sequence shown in SEQ ID NO: 55, PtrC4H2 having the nucleotide sequence shown in SEQ ID NO: 56, PtrC3H having the nucleotide sequence shown in SEQ ID NO: 57, having At least one of PaHPAB having the nucleotide sequence shown in SEQ ID NO:58 and SeHPAC having the nucleotide sequence shown in SEQ ID NO:59.
  9. 根据权利要求7所述的方法,其特征在于,ARO7 G141S、ARO4 K229L、EcAROL的导入位点为ARO10; The method according to claim 7, wherein the introduction site of ARO7 G141S , ARO4 K229L , and EcAROL is ARO10;
    FjTAL、SbPAL1 H123F、AtCPR1的导入位点为PDC5; The import site of FjTAL, SbPAL1 H123F and AtCPR1 is PDC5;
    PtrC4H2、PtrC4H1、PtrC3H的导入位点为XII4;The import site of PtrC4H2, PtrC4H1 and PtrC3H is XII4;
    ARO1、ARO2、ARO3的导入位点为XII1;The import site of ARO1, ARO2, and ARO3 is XII1;
    PahpaB、SehpaC的导入位点为X2;The import site of PahpaB and SehpaC is X2;
    PHA2、MtPDH1的导入位点为XI8。The import site of PHA2 and MtPDH1 is XI8.
  10. 根据权利要求7所述的方法,其特征在于,将含有T HIS3-ARO7 G141S-P GAL10/1-ARO4 K229L-T ENO2-P GAL7-EcAROL-T ADH1的DNA片段整合到出发菌株的ARO10位点; The method according to claim 7, wherein the DNA fragment containing THIS3 -ARO7 G141S -P GAL10/1 -ARO4 K229L -T ENO2 -P GAL7- EcAROL-T ADH1 is integrated into the ARO10 site of the starting strain ;
    将含有T CYC1-FjTAL-Sc OPT1-P GAL10/1-SbPAL1 H123F-Sc OPT1-T TDH2-T FBA1-AtCPR1-Sc OPT1-P GAL7的DNA片段整合到出发菌株的PDC5位点; Integrate the DNA fragment containing T CYC1 -FjTAL-Sc OPT1 -P GAL10/1 -SbPAL1 H123F -Sc OPT1 -T TDH2 -T FBA1 -AtCPR1-Sc OPT1 -P GAL7 into the PDC5 site of the starting strain;
    将含有T PRM9t-PtrC4H2-Sc OPT1-P GAL10/1-PtrC4H1-Sc OPT1-T PYK1-P GAL7-PtrC3H-Sc OPT1-T DIT1的DNA片段整合到出发菌株的XII4位点;、 Integrate the DNA fragment containing T PRM9t -PtrC4H2-Sc OPT1 -P GAL10/1 -PtrC4H1-Sc OPT1 -T PYK1 -P GAL7 -PtrC3H-Sc OPT1 -T DIT1 into the XII4 site of the starting strain;
    将含有P GAL7-ARO1-T ENO2-T CPS1-ARO2-P GAL10/1-ARO3-T HIS5的DNA片段整合到出发菌株的XII1位点; Integrate the DNA fragment containing P GAL7 -ARO1-T ENO2 -T CPS1 -ARO2-P GAL10/1 -ARO3-T HIS5 into the XII1 site of the starting strain;
    将含有T PRM9-PahpaB-Sc OPT1-P GAL10/1-SehpaC-Sc OPT1-T HIS3的DNA片段整合到出发菌株的X2位点; Integrate the DNA fragment containing T PRM9 -PahpaB-Sc OPT1 -P GAL10/1 -SehpaC-Sc OPT1 -T HIS3 into the X2 site of the starting strain;
    将含有T CPS1-PHA2-P GAL10/1-MtPDH1-Sc OPT1-T HIS5的DNA片段整合到出发菌株的XI8位点; Integrate the DNA fragment containing T CPS1 -PHA2-P GAL10/1 -MtPDH1-Sc OPT1 -T HIS5 into the XI8 site of the starting strain;
  11. 根据权利要求7所述的方法,其特征在于,还在酿酒酵母出发菌株中导入LmXFPK基因、CkPTA基因、TAL1基因和TKL1基因。The method according to claim 7, characterized in that, the LmXFPK gene, the CkPTA gene, the TAL1 gene and the TKL1 gene are also introduced into the starting strain of Saccharomyces cerevisiae.
  12. 根据权利要求11所述的方法,其特征在于,TKL1基因的核苷酸序列如SEQ ID NO:40所示;The method according to claim 11, wherein the nucleotide sequence of the TKL1 gene is as shown in SEQ ID NO: 40;
    TAL1基因的核苷酸序列如SEQ ID NO:41所示;The nucleotide sequence of the TAL1 gene is shown in SEQ ID NO: 41;
    LmXFPK基因的核苷酸序列如SEQ ID NO:42所示;The nucleotide sequence of the LmXFPK gene is shown in SEQ ID NO: 42;
    CkPTA基因的核苷酸序列如SEQ ID NO:43所示。The nucleotide sequence of the CkPTA gene is shown in SEQ ID NO: 43.
  13. 根据权利要求7所述的方法,其特征在于,还敲除酿酒酵母出发菌株的GAL80基因。The method according to claim 7, characterized in that the GAL80 gene of the starting strain of Saccharomyces cerevisiae is also knocked out.
  14. 权利要求1~3任一项所述的方法得到的工程菌。The engineering bacterium obtained by the method described in any one of claims 1 to 3.
  15. 权利要求1~3任一项所述的方法得到的工程菌、权利要求14所述的工程菌在制备SAM依赖的甲基化产物中的应用。Application of the engineering bacteria obtained by the method according to any one of claims 1 to 3 and the engineering bacteria according to claim 14 in the preparation of SAM-dependent methylation products.
  16. 根据权利要求15所述的应用,其特征在于,所述SAM依赖的甲基化产物包括阿魏酸。The use according to claim 15, characterized in that the SAM-dependent methylation product comprises ferulic acid.
PCT/CN2021/138511 2021-12-15 2021-12-15 Method for improving sam cofactor supply of saccharomyces cerevisiae, engineered yeast and use thereof WO2023108505A1 (en)

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