WO2019010971A1 - Preparation method for dehydroepiandrosterone, and enzyme for preparation thereof - Google Patents

Preparation method for dehydroepiandrosterone, and enzyme for preparation thereof Download PDF

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WO2019010971A1
WO2019010971A1 PCT/CN2018/075822 CN2018075822W WO2019010971A1 WO 2019010971 A1 WO2019010971 A1 WO 2019010971A1 CN 2018075822 W CN2018075822 W CN 2018075822W WO 2019010971 A1 WO2019010971 A1 WO 2019010971A1
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ketoreductase
seq
glucose dehydrogenase
coding sequence
gene coding
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PCT/CN2018/075822
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French (fr)
Chinese (zh)
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傅荣昭
刘立辉
陈小春
曹磊
刘滔滔
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邦泰生物工程(深圳)有限公司
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Priority to CN201880001977.1A priority Critical patent/CN109312382A/en
Priority to PCT/CN2018/075822 priority patent/WO2019010971A1/en
Publication of WO2019010971A1 publication Critical patent/WO2019010971A1/en

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    • C12P33/00Preparation of steroids
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    • C07ORGANIC CHEMISTRY
    • C07KPEPTIDES
    • C07K14/00Peptides having more than 20 amino acids; Gastrins; Somatostatins; Melanotropins; Derivatives thereof
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    • C12N1/00Microorganisms, e.g. protozoa; Compositions thereof; Processes of propagating, maintaining or preserving microorganisms or compositions thereof; Processes of preparing or isolating a composition containing a microorganism; Culture media therefor
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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
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    • C12N9/00Enzymes; Proenzymes; Compositions thereof; Processes for preparing, activating, inhibiting, separating or purifying enzymes
    • C12N9/0004Oxidoreductases (1.)
    • C12N9/0006Oxidoreductases (1.) acting on CH-OH groups as donors (1.1)
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    • C12P7/00Preparation of oxygen-containing organic compounds
    • C12P7/02Preparation of oxygen-containing organic compounds containing a hydroxy group
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    • C12R2001/00Microorganisms ; Processes using microorganisms
    • C12R2001/01Bacteria or Actinomycetales ; using bacteria or Actinomycetales
    • C12R2001/185Escherichia
    • C12R2001/19Escherichia coli

Definitions

  • the invention relates to the technical field of biomedicine, in particular to a preparation method of dehydroepiandrosterone and an enzyme for preparation thereof.
  • DHEA Dehypoepiandrosterone
  • DHEA is a C19 steroid carrier compound with the chemical name 3 ⁇ -hydroxyandrost-5-en-17-one, the molecular formula C 19 H 28 O 2 .
  • DHEA is a large number of adrenal steroidal compounds coexisting in human plasma. It has anti-inflammatory, anti-proliferative and anti-depressant activities. Its derivatives can promote the immune response of animals in experiments and have a good neuroprotective effect.
  • DHEA is an important intermediate for the synthesis of steroids. In recent years, DHEA has gradually developed into one of the most popular research objects due to its important research value.
  • the synthesis of traditional DHEA is mostly carried out by chemical methods, for example, using pregnane dienolone or gestational dienolone acetate as a raw material, and after deuteration, rearrangement and hydrolysis, a product is obtained.
  • the synthesis method is completed in three or more chemical reactions, the raw material price is high, and the solvent used in the process such as benzene, alkyl halide or pyridine is harmful to the environment.
  • the products in the traditional process have low purity, low efficiency, and complicated purification operations in the later stage.
  • the present invention provides a preparation method of dehydroepiandrosterone and an enzyme for preparation thereof, and the preparation method of the dehydroepiandrosterone involves a two-step reaction, which greatly reduces the preparation process of the traditional method.
  • the synthesis process of the present invention provides the synthesis process of the dehydroepiandrosterone with high yield, low cost and green environmental protection.
  • the present invention provides a method for preparing dehydroepiandrosterone, comprising:
  • the process comprises a two-step reaction, the first step is a chemical method, the second step is a biological enzymatic method, and the 4-androstenenedione (4-Androstene-3, 17-dione, 4-AD) is as As shown in the formula (I), the 5-androstenone (5-Androstene-3, 17-dione, 5-AD) is represented by the formula (II), and the dehydroepiandrosterone is as defined in the formula (III). ) shown.
  • the protective atmosphere refers to the environment filled with nitrogen or an inert gas.
  • the inert gas includes one or more of helium (He), neon (Ne), argon (Ar), krypton (Kr), and xenon (Xe).
  • the specific preparation process of the mixture comprises: adding potassium t-butoxide to t-butanol at room temperature, then raising the temperature to 55-65 ° C, and stirring for 0.3-0.8 hours. After the potassium t-butoxide was completely dissolved, the temperature was maintained at 25 to 30 ° C, and 4-androstenedione was added thereto for stirring for 0.3 to 0.8 hours, followed by cooling to obtain the mixture.
  • the temperature is controlled at 55-65 ° C, the dissolution time of potassium t-butoxide can be greatly shortened, and the dissolution time of the conventional 3 hours or more can be shortened to about 0.5 hour; Maintaining at 25-30 ° C can promote the efficient forward reaction of the 4-androstenedione. If the temperature is too high, it is easy to reversely react to form 4-androstenedione. If the temperature is too low, the reaction takes a long time. , production efficiency is low.
  • the reaction mixture is added to an acetic acid solution containing sodium ascorbate to obtain a 5-androstenedione, and the reaction temperature is 25-30 ° C, and the reaction is carried out.
  • the time is 0.3-0.8 hours.
  • the reaction temperature may be 26 to 30 ° C, and the reaction time is 0.5 to 0.8 hours.
  • the reaction temperature is 30 °C.
  • the molar ratio of the 4-androstenedione and the potassium t-butoxide is 1: (0.75-1.2). Further optionally, the molar ratio of the 4-androstenedione and the potassium t-butoxide is 1: (0.8-1.2).
  • the organic solvent comprises a hydrophobic solvent.
  • the organic solvent comprises ethyl acetate.
  • the preferred ethyl acetate solvent in step (2) of the present invention is effective to increase the yield of said dehydroepiandrosterone.
  • the molar ratio of the 4-androstenedione, the acetic acid and the sodium ascorbate is 1: (0.5-1): (0.04-0.4). Further optionally, the molar ratio of the 4-androstenedione, the acetic acid and the sodium ascorbate is 1: (0.6-1): (0.05-0.2).
  • the ketoreductase, glucose dehydrogenase, glucose and redox coenzyme are an aqueous solution or a buffer solution.
  • the buffer solution comprises a phosphate buffer, a Tris-HCl buffer or other buffer solution having a pH of 6.0-7.0.
  • the buffer solution is a sodium phosphate buffer.
  • the buffer solution has a concentration of 50-120 mmol/L.
  • the buffer solution has a concentration of 60-100 mmol/L.
  • the buffer solution has a concentration of 80-120 mmol/L.
  • the concentration of the buffer solution is 60 mmol/L, or 70 mmol/L, or 90 mmol/L, or 100 mmol/L, or 120 mmol/L.
  • the four components of the ketoreductase, glucose dehydrogenase, glucose, and redox coenzyme may be added after mixing four kinds of ketoreductase, glucose dehydrogenase, glucose, and redox coenzyme. Adding simultaneously; or separately adding the ketoreductase, glucose dehydrogenase, glucose, and redox coenzyme, wherein, when added alone, the ketoreductase, glucose dehydrogenase, glucose, and redox coenzyme are sequentially added in order. And the order of addition is not limited.
  • the ketoreductase, glucose dehydrogenase, glucose, and redox coenzyme may be added in the form of one or more of the ketoreductase, glucose dehydrogenase, glucose, and redox coenzyme, and The remaining components of the ketoreductase, glucose dehydrogenase, glucose, and redox coenzyme are mixed and added to the organic solvent containing 5-androstenedione.
  • the ketoreductase in the ketoreductase, glucose dehydrogenase, glucose, and redox coenzyme and the glucose dehydrogenase are first mixed together, and then in a mixed group of ketoreductase and glucose dehydrogenase.
  • the concentration of the glucose is 0.04-0.12 mg/mL. Further optionally, the concentration of the glucose is from 0.08 to 0.1 mg/mL. For example, the concentration of the glucose in the buffer solution is 0.1 mg/mL, or 0.12 mg/mL.
  • the microbial strain comprises one or both of Rosetta (DE3) E. coli and BL21 (DE3) E. coli. Further optionally, the microbial strain comprises Rosetta (DE3) E. coli.
  • the specific process of co-expressing the microbial strain to produce the ketoreductase and the glucose dehydrogenase comprises: constructing a recombinant expression plasmid, transfecting the recombinant expression plasmid After the microorganism strain is introduced, the microorganism strain containing the recombinant expression plasmid is induced to express the ketoreductase and the glucose dehydrogenase in a microorganism culture solution, wherein the recombinant expression plasmid includes the ketoreductase and The gene coding sequence of the glucose dehydrogenase.
  • the ketoreductase and the glucose dehydrogenase may be produced intracellularly in the microbial strain, or may be released from the microbial culture solution after intracellular production of the microbial strain.
  • the crude enzyme solution is obtained by collecting, washing, and granulating the microorganism strain capable of expressing a ketoreductase and a glucose dehydrogenase, and the crude enzyme solution contains the ketoreductase and the glucose Dehydrogenase.
  • the ketoreductase and the glucose dehydrogenase are two independent protein molecules, and are obtained by the above-mentioned co-expression, so that the operation can save production cost and simplify the experimental process.
  • the recombinant expression plasmid may simultaneously contain the gene coding sequence of the ketoreductase and the glucose dehydrogenase, and simultaneously express the ketoreductase and the glucose dehydrogenase protein molecules.
  • the reaction in the step (2) is carried out in the form of a crude enzyme solution, for example, the crude enzyme solution may be an expression of the ketoreductase and the glucose dehydrogenase induced by Escherichia coli Rosetta (DE3).
  • the Escherichia coli Rosetta (DE3) is collected by centrifugation and washing, after the cells are suspended in a buffer solution and subjected to ultrasonic disruption, the ketoreductase and the glucose dehydrogenase are released to a buffer solution.
  • the crude enzyme solution is obtained.
  • the invention adopts the co-expression form to obtain the ketoreductase and the glucose dehydrogenase crude enzyme solution to participate in the preparation of DHEA, not only streamlining the preparation process, but also improving the yield, saving cost and being green. Further, the present invention can also purify the ketoreductase and glucose dehydrogenase and participate in the synthesis reaction.
  • the gene coding sequence of the ketoreductase includes any one of the nucleotide sequences shown in SEQ ID NO: 1, SEQ ID NO: 2, and SEQ ID NO: 3.
  • the gene coding sequence of the glucose dehydrogenase comprises the nucleotide sequence as shown in SEQ ID NO: 4.
  • the present invention preferably has the above ketoreductase comprising any one of the nucleotide sequences shown as SEQ ID NO: 1, SEQ ID NO: 2 and SEQ ID NO: 3, which can be efficiently expressed in the microorganism strain
  • the crude enzyme solution has a higher concentration of the ketoreductase.
  • the molar ratio of the ketoreductase, the glucose dehydrogenase, and the 4-androstenedione is (0.015-0.04): (0.01-0.04):1. .
  • the redox coenzyme includes one or more of NAD + , NADP + , NADH, and NADPH. Further optionally, in the step (2), the redox coenzyme comprises NAD + .
  • the concentration of the redox coenzyme is 0.04-0.4 mg/mL. Further optionally, the concentration of the redox coenzyme is from 0.08 to 0.2 mg/mL. For example, the concentration of the redox coenzyme in the buffer solution is 0.1 mg/mL, or 0.15 mg/mL, or 0.2 mg/mL.
  • the NAD + is Nicotinamide adenine dinucleotide (NAD + ), also known as oxidized coenzyme I;
  • NADH is a reduced state of nicotinamide adenine dinucleotide, also called Is a reduced coenzyme I;
  • NADP + is nicotinamide adenine dinucleotide phosphate (NADP + ), also known as oxidized coenzyme II;
  • the NADPH is nicotinamide adenine dinucleotide The reduced state of phosphoric acid, also known as reduced coenzyme II.
  • a redox coenzyme, glucose dehydrogenase and glucose form a coenzyme regeneration system, which is an electronic cycle system, which can effectively make 5 under the action of ketoreductase - androstenedione is reduced to form dehydroepiandrosterone, which increases the yield of dehydroepiandrosterone.
  • DHEA has very high yields can only use the NAD +, NADP +, NADH and NADPH in NAD + can be implemented with cycles and the.
  • the process of separating and purifying in the step (2) comprises a sequential filtration, washing and extraction process. Further optionally, the step (2) further comprises recrystallizing the dehydroepiandrosterone.
  • the specific process of separating and purifying in the step (2) comprises: adding the reaction liquid to diatomaceous earth to obtain a filtrate and a filter cake, and washing the filter cake with ethyl acetate to obtain a washing liquid, and collecting And mixing the washing liquid and the filtrate to obtain an aqueous phase and an organic phase, and extracting the aqueous phase with ethyl acetate for two or three times to obtain an extract, and mixing the extract with the organic phase and concentrating Dehydroepiandrosterone is obtained by filtration, washing, washing and drying.
  • the method for preparing dehydroepiandrosterone provided by the first aspect of the present invention is simple, time-saving, high-efficiency, low-cost, green and environmentally friendly, and the preparation method is applicable to large-scale industrial production;
  • the resulting dehydroepiandrosterone has an extremely high yield.
  • the present invention provides a ketoreductase comprising ketoreductase KRED3 (abbreviated as KRED3), ketoreductase KRED4 (abbreviated as KRED4) and ketoreductase KRED5 (abbreviated as KRED5)
  • KRED3 ketoreductase KRED3
  • KRED4 ketoreductase KRED4
  • KRED5 ketoreductase KRED5
  • One or more of the gene coding sequences of the ketoreductase KRED3 include the nucleotide sequence set forth in SEQ ID NO: 1
  • the gene coding sequence of the ketoreductase KRED4 includes as set forth in SEQ ID NO:
  • the nucleotide sequence shown, the gene coding sequence of the ketoreductase KRED5 includes the nucleotide sequence shown in SEQ ID NO: 3.
  • the gene coding sequence of KRED3 further comprises a nucleotide sequence of at least 95% homology of the nucleotide sequence shown in SEQ ID NO: 1
  • the gene coding sequence of KRED4 further comprises SEQ ID NO: a nucleotide sequence of at least 95% homology of the nucleotide sequence shown by 2
  • the gene coding sequence of KRED5 further comprising at least 95% homology of the nucleotide sequence as shown in SEQ ID NO: Nucleotide sequence.
  • amino acid sequence of KRED3 comprises the amino acid sequence set forth in SEQ ID NO: 5
  • amino acid sequence of KRED4 comprises the amino acid sequence set forth in SEQ ID NO: 6
  • amino acid sequence of KRED5 comprises SEQ ID NO: NO: The amino acid sequence shown in 7.
  • amino acid sequence of the glucose dehydrogenase comprises the amino acid sequence set forth in SEQ ID NO: 8.
  • the gene of the ketoreductase KRED3 of the present invention is derived from Burkholderia territorii
  • the gene of the ketoreductase KRED4 is derived from Rhodococcus
  • the gene for KRED5 is derived from Sphingomonas sp.
  • the gene for the glucose dehydrogenase is derived from Bacillus megaterium.
  • the ketoreductase of the present invention has strong chemical selectivity and regioselectivity, and under certain conditions, the 5-androstenedione can be efficiently converted into the dehydroepiandrosterone.
  • the gene fragment of any one of the ketoreductases KRED3, KRED4 and KRED5 further includes a His tag.
  • the gene fragment of any one of the ketoreductases KRED3, KRED4 and KRED5 further comprises an 8 ⁇ His tag.
  • the gene fragment of the glucose dehydrogenase further includes a 6 x His tag. As the number of His tags of the His tag increases, the binding efficiency of the protein increases, and the purification yield increases; the present invention can connect different numbers of His on the ketoreductase and the glucose dehydrogenase.
  • the His tag is separately purified.
  • the ketoreductases KRED3, KRED4 and KRED5 provided by the second aspect of the present invention are one of the enzymes for preparing the method for preparing dehydroepiandrosterone according to the first aspect of the present invention, and a His tag is added to the gene fragment (group)
  • the nucleotide sequence of the amino acid tag enables the expressed protein to be tagged with His tag.
  • the His tag facilitates the isolation and purification of the expressed protein, and is analyzed and traced in experiments, such as analysis for immunoblot experiments. .
  • the present invention also provides a use of a ketoreductase for catalyzing the conversion of a ketone or an aldehyde to a chiral alcohol, the gene coding sequence of the ketoreductase comprising SEQ ID NO: 1, SEQ ID NO: 2 And any one of the nucleotide sequences shown in SEQ ID NO: 3. That is, the ketoreductase of the present invention can efficiently and selectively catalyze the reduction of a carbonyl group on an aldehyde or a ketone to a chiral hydroxyl group.
  • the use of the catalytic ketone or aldehyde to convert to a chiral alcohol includes the use of catalyzing the conversion of 5-androstenedione to dehydroepiandrosterone.
  • the ketoreductase of the present invention has strong chemical selectivity and regioselectivity, and under certain conditions, the 5-androstenedione can be efficiently and selectively converted to the dehydroepiandrosterone. .
  • the present invention also provides a recombinant plasmid comprising a gene coding sequence of a ketoreductase, wherein the gene coding sequence of the ketoreductase comprises a gene coding sequence of KRED3, a gene coding sequence of KRED4, and KRED5
  • the gene coding sequence of the ketoreductase comprises a gene coding sequence of KRED3, a gene coding sequence of KRED4, and KRED5
  • the gene coding sequence of KRED3 comprising the nucleotide sequence shown in SEQ ID NO: 1
  • the gene coding sequence of KRED4 comprising as shown in SEQ ID NO:
  • the nucleotide sequence of the KRED5 gene coding sequence includes the nucleotide sequence shown in SEQ ID NO: 3.
  • the recombinant plasmid further comprises a gene coding sequence of glucose dehydrogenase, and an RBS sequence is inserted between the gene coding sequence of the glucose dehydrogenase and the gene coding sequence of the ketoreductase, and the glucose is removed.
  • the gene coding sequence of the hydrogenase includes a nucleotide sequence as shown in SEQ ID NO: 4, and the RBS sequence includes the nucleotide sequence as shown in SEQ ID NO: 17.
  • the recombinant plasmid includes a gene coding sequence for a ketoreductase ligated from the 5' end to the 3' end, a RBS sequence, and a gene coding sequence for glucose dehydrogenase.
  • the RBS sequence of the present invention is a ribosome binding site (RBS) sequence, which can effectively promote the independent transcription and translation of two homologous genes (the ketoreductase gene and the glucose dehydrogenase gene).
  • the recombinant plasmid of the fourth aspect of the invention can be used for co-expressing ketone reductase and glucose dehydrogenase, and the ketoreductase and glucose dehydrogenase have excellent activity and can be widely used in the fields of biopharmaceuticals, protein production and the like.
  • the present invention also provides a method for preparing a recombinant plasmid, comprising:
  • the coding sequence includes any one of the nucleotide sequences set forth in SEQ ID NO: 1, SEQ ID NO: 2, and SEQ ID NO: 3, and the genetic coding sequence of the glucose dehydrogenase includes SEQ ID NO: a nucleotide sequence as shown in 4;
  • the gene for the ketoreductase is inserted between the Nde I and EcoR I cleavage sites in the pET22b(+) vector plasmid.
  • the gene of the ketoreductase is inserted into the pET22b(+) vector plasmid, the 3' end of the gene coding sequence of the ketoreductase can be added to the stop codon (such as TAA) and the pET22b (+) vector plasmid in the EcoRI digestion. The sites are connected.
  • the gene for the glucose dehydrogenase was inserted between the EcoR I and Xho I restriction sites in the pET22b(+) vector plasmid.
  • the 3' end of the gene coding sequence of the glucose dehydrogenase may be added to a stop codon (such as TAA) and a pET22b (+) vector plasmid. I cleavage sites are linked.
  • the RBS sequence between the ketoreductase and the glucose dehydrogenase gene coding sequence comprising the nucleotide sequence set forth in SEQ ID NO: 17
  • the gene coding sequence of the ketoreductase includes any one of the nucleotide sequences shown in SEQ ID NO: 1, SEQ ID NO: 2, and SEQ ID NO: 3, and the gene coding sequence of the glucose dehydrogenase includes A nucleotide sequence as shown in SEQ ID NO: 4.
  • the sequence of the ketoreductase and the glucose dehydrogenase gene coding sequence in the pET22b(+) vector plasmid may be that the 3' end of the ketoreductase gene is located 5' of the glucose dehydrogenase gene Before the end, or the 5' end of the ketoreductase gene is located after the 3' end of the glucose dehydrogenase gene.
  • the RBS sequence is inserted before the 5' end of the glucose dehydrogenase gene sequence.
  • a linker may be disposed between the 3' end of the RBS sequence and the 5' end of the glucose dehydrogenase gene sequence to facilitate translation recognition of the glucose dehydrogenase, which is beneficial to ketoreductase and glucose dehydrogenase. Translational expression can be performed separately in the same vector.
  • the sequence of the linker may be "ATATACAT".
  • the cleavage sites used for the pET22b(+) vector plasmid include Nde I endonuclease and Xho I endonuclease.
  • the preparation method can prepare a recombinant plasmid containing only a ketoreductase or a glucose dehydrogenase, and can also prepare a recombinant plasmid containing both a ketoreductase and a glucose dehydrogenase.
  • one or both of the ketoreductase and glucose dehydrogenase of the present invention can be obtained by transfecting the recombinant plasmid into a microbial strain to induce expression.
  • the preparation method of dehydroepiandrosterone according to the present invention comprises a two-step reaction, using 4-androstenedione as a starting material, and adopting a biological enzyme such as ketoreductase, which has low production cost, simple process and time saving. High efficiency, mild reaction conditions, greatly improving the yield of the product;
  • the preparation method of dehydroepiandrosterone according to the invention is green and environmentally friendly, avoids environmental pollution problems from the root causes, further reduces costs, and can be widely applied to industrial scale production;
  • Dehydroepiandrosterone prepared by the method of the present invention has high purity and can be widely used in the pharmaceutical field or biomedical field.
  • 1 is a plasmid map of a recombinant plasmid pET22b-KRED3-GDH according to an embodiment of the present invention
  • FIG. 2 is a plasmid map of a recombinant plasmid pET22b-KRED4-GDH according to an embodiment of the present invention
  • FIG. 3 is a plasmid map of a recombinant plasmid pET22b-KRED5-GDH according to an embodiment of the present invention
  • FIG. 4 is a gel electrophoresis diagram of a KRED3-GDH crude enzyme solution according to an embodiment of the present invention
  • FIG. 5 is a gel electrophoresis diagram of a KRED4-GDH crude enzyme solution according to an embodiment of the present invention.
  • FIG. 6 is a gel electrophoresis diagram of a KRED5-GDH crude enzyme solution according to an embodiment of the present invention.
  • Figure 10 is a high performance liquid chromatogram of a crude product of dehydroepiandrosterone according to an embodiment of the present invention.
  • the present invention provides a preparation method of a ketoreductase and a glucose dehydrogenase, wherein the ketoreductase and the glucose dehydrogenase are enzymes for preparation in the preparation method of the dehydroepiandrosterone, and the specific experiment
  • the steps include:
  • ketoreductase KRED3, ketoreductase KRED4, ketoreductase KRED5 and glucose dehydrogenase were obtained by PCR amplification experiments.
  • the gene coding sequence of the ketoreductase KRED3 is as shown in SEQ ID NO: 1
  • the gene coding sequence of the ketoreductase KRED4 is as shown in SEQ ID NO: 2
  • the coding sequence of the ketoreductase KRED5 is encoded.
  • SEQ ID NO: 3 the gene coding sequence of the glucose dehydrogenase is shown in SEQ ID NO: 4.
  • the base sequence of the upstream primer corresponding to the ketoreductase KRED3 is shown in SEQ ID NO: 9, and the base sequence of the downstream primer is shown in SEQ ID NO: 10.
  • the base sequence of the upstream primer corresponding to the gene of the ketoreductase KRED3 is shown in SEQ ID NO: 9, and the base sequence of the downstream primer is shown in SEQ ID NO: 10.
  • the base sequence of the upstream primer corresponding to the gene of the ketoreductase KRED4 is shown in SEQ ID NO: 11, and the base sequence of the downstream primer is shown in SEQ ID NO: 12.
  • the base sequence of the upstream primer corresponding to the gene of the ketoreductase KRED5 is shown in SEQ ID NO: 13, and the base sequence of the downstream primer is shown in SEQ ID NO: 14.
  • the base sequence of the upstream primer corresponding to the gene of the glucose dehydrogenase is shown in SEQ ID NO: 15, and the base sequence of the downstream primer is shown in SEQ ID NO: 16.
  • the RBS sequence is inserted before the 5' end of the gene of the glucose dehydrogenase, and can be inserted into the plasmid pET22b(+) by the upstream and downstream primers as shown in SEQ ID NO: 17.
  • the PCR amplification system was carried out by the corresponding upstream primer and downstream primer, respectively, and the amplification system was configured as follows:
  • the PCR amplification procedure was: predenaturation at 98 ° C for 2 min; denaturation at 98 ° C for 10 s; annealing at 60 ° C for 30 s; extension at 72 ° C for 1 min; after 30 cycles, extension at 72 ° C for 10 min.
  • the PCR products were purified by gel recovery kit and digested with restriction endonucleases Nde I and EcoR I, EcoR I and Xho I respectively. After digestion, they were ligated with T4 ligase and digested with Nde I and Xho I. Plasmid pET22b(+). The ligation product was transferred into E.
  • coli DH5 ⁇ and after screening with ampicillin resistance (Amp + ), the colony was picked and sequenced. After successful sequencing, the recombinant plasmid pET22b-KRED3/4/5 co-expressed by ketoreductase and glucose dehydrogenase was obtained.
  • - GDH including pET22b-KRED3-GDH, pET22b-KRED4-GDH or pET22b-KRED5-GDH).
  • the plasmid map of the recombinant plasmid pET22b-KRED3-GDH is shown in Figure 1; the plasmid map of the recombinant plasmid pET22b-KRED4-GDH is shown in Figure 2; the plasmid map of the recombinant plasmid pET22b-KRED5-GDH is shown in Figure 3 is shown.
  • the DNA templates described in the present embodiment are plasmids pET22b-KRED3, pET22b-KRED4, pET22b-KRED5, and pET22b-GDH, respectively.
  • Escherichia coli containing the recombinant plasmid pET22b-KRED3-GDH, pET22b-KRED4-GDH or pET22b-KRED5-GDH was inoculated to a 50 mL containing 10 mL of LB medium (100 ⁇ g/mL ampicillin (Amp)) at a 1% inoculation amount.
  • LB medium 100 ⁇ g/mL ampicillin (Amp)
  • a triangular flask maintain a constant shaking temperature of 37 ° C and 200 rpm. After overnight culture, transfer the bacterial solution to a 2 L flask containing 1 L of LB medium (100 ⁇ g/mL Amp) at 1% inoculation.
  • the OD600 value of the medium cultured at 37 ° C was adjusted to about 0.6, and isopropyl- ⁇ -D-thiogalactoside (IPTG) inducer (systemic concentration: 0.5 mM) was added, and cultured at 37 ° C for 8 hours.
  • IPTG isopropyl- ⁇ -D-thiogalactoside
  • the KRED3-GDH crude enzyme solution contains a ketoreductase KRED3 and a glucose dehydrogenase.
  • the KRED4-GDH crude enzyme solution contains a ketoreductase KRED4 and a glucose dehydrogenase.
  • the KRED5-GDH crude enzyme solution contains a ketoreductase KRED5 and a glucose dehydrogenase.
  • FIG. 4 is a gel electrophoresis diagram of the KRED3-GDH crude enzyme solution, wherein the lane M is the protein Marker (Thermo Scientific PageRuler), the lane 1 is the total protein after the cell disruption, and the lane 2 is the supernatant after the cell disruption.
  • Figure 5 is a gel electrophoresis diagram of the KRED4-GDH crude enzyme solution, wherein the lane M is the protein Marker (Thermo Scientific PageRuler), the lane 1 is the supernatant after the cell disruption, and the lane 2 is the total cell after the cell is broken.
  • the protein wherein KRED4 has a molecular weight of 29 kDa and the GDH has a molecular weight of 26 kDa.
  • Figure 6 is a gel electrophoresis diagram of the KRED5-GDH crude enzyme solution, wherein the lane M is the protein Marker (Thermo Scientific PageRuler), the lane 1 is the supernatant after the cell disruption, and the lane 2 is the total cell after the cell is broken.
  • KRED5 has a molecular weight of 28 kDa and the GDH has a molecular weight of 26 kDa.
  • the ketoreductases KRED3, KRED4 and KRED5, as well as the molecules of GDH, are similar in theoretical calculations for the corresponding proteins.
  • a method for preparing dehydroepiandrosterone comprises the following steps:
  • the mixture was slowly added dropwise to the acetic acid solution containing sodium ascorbate at 30 ° C for 30 min, maintained at a temperature of 30 ° C for 0.5 h, and cooled at room temperature to obtain a reaction containing 5-AD. liquid.
  • the washing liquid and the filtrate were mixed, the aqueous phase and the organic phase were separated, and the aqueous phase was extracted twice with ethyl acetate.
  • the liquid was mixed with the organic phase, and the organic phase was concentrated under reduced pressure. 600 g of water was added, and the mixture was thoroughly stirred and then filtered.
  • the filter cake was washed twice with 120 g of water, and the washed cake was vacuum dried to obtain a crude DHEA product.
  • the crude DHEA product was transferred to a clean container, and 234 g of acetone was added to dissolve, and then 200 g of water was added, and the above operation was repeated to carry out recrystallization to obtain 78.02 g of DHEA final product.
  • the yield of DHEA was 78.02%.
  • the two-step reaction was sampled and tested.
  • the detection conditions were: Ferenbach Phenyl-Hexyl 250 ⁇ 4.6 mm column, wavelength UV210 nm, mobile phase 50% acetonitrile aqueous solution, flow rate 1.0 mL/min, temperature 25 °C.
  • 4-AD can be efficiently converted to produce 5-AD
  • DHEA The liquid chromatogram of the crude product ( Figure 10) is compared to the liquid chromatogram of the DHEA standard (see Figure 9), which contains the higher purity DHEA.
  • a method for preparing dehydroepiandrosterone comprises the following steps:
  • the mixture was slowly added dropwise to the acetic acid solution containing sodium ascorbate at 30 ° C for 30 min, maintained at a temperature of 30 ° C for 0.5 h, and cooled at room temperature to obtain a reaction containing 5-AD. liquid.
  • the washing liquid and the filtrate were mixed, the aqueous phase and the organic phase were separated, and the aqueous phase was extracted twice with ethyl acetate.
  • the liquid was mixed with the organic phase, and the organic phase was concentrated under reduced pressure. 600 g of water was added, and the mixture was thoroughly stirred and then filtered.
  • the filter cake was washed twice with 120 g of water, and the washed cake was vacuum dried to obtain a crude DHEA product.
  • the crude DHEA product was transferred to a clean container, and 234 g of acetone was added to dissolve, and then 200 g of water was added.
  • the above operation was repeated for recrystallization to obtain 75.16 g of DHEA final product.
  • the yield of DHEA was 75.16%.
  • a method for preparing dehydroepiandrosterone comprises the following steps:
  • the mixture was slowly added dropwise to the acetic acid solution containing sodium ascorbate at 30 ° C for 30 min, maintained at a temperature of 28 ° C for 0.5 h, and cooled at room temperature to obtain a reaction containing 5-AD. liquid.
  • the filter cake was washed twice with 120 g of water, and the washed cake was vacuum dried to obtain a crude DHEA product.
  • the crude DHEA product was transferred to a clean container, and after adding 250 g of acetone to dissolve, 200 g of water was added, and the above operation was repeated to carry out recrystallization to obtain 77.53 g of DHEA final product.
  • the yield of DHEA was 77.53%.

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Abstract

A preparation method for dehydroepiandrosterone, comprising: in a protective atmosphere, adding potassium tert-butoxide to tert-butanol, stirring evenly, adding 4-androstenedione to obtain a mixture, and adding the mixture dropwise to a sodium ascorbate-containing acetic acid solution for a reaction to obtain 5-androstenedione; dissolving the 5-androstenedione in an organic solvent, adding a ketone reductase, a glucose dehydrogenase, glucose and a redox coenzyme to obtain a mixture, controlling the pH of the mixture to be 6.0-6.3, stirring and reacting for 1-6 hours at 22-26°C to obtain a reaction solution, and performing separation and purification on the reaction solution to obtain dehydroepiandrosterone, the ketone reductase and the glucose dehydrogenase being coexpressed by a microbial strain and added in the form of a crude enzyme solution. The synthesis process of the preparation method has few steps, simple operations, high yields and low costs, and may be widely applied to industrial scale production. Also provided is an enzyme for preparation.

Description

一种去氢表雄酮的制备方法及其制备用酶Preparation method of dehydroepiandrosterone and preparation enzyme thereof 技术领域Technical field
本发明涉及生物医药技术领域,特别涉及一种去氢表雄酮的制备方法及其制备用酶。The invention relates to the technical field of biomedicine, in particular to a preparation method of dehydroepiandrosterone and an enzyme for preparation thereof.
背景技术Background technique
去氢表雄酮(脱氢表雄酮)(dehyroepiandrosterone,DHEA)是一种C19类固醇载体化合物,化学名称为3β-羟基雄甾-5-烯-17-酮,分子式C 19H 28O 2。DHEA是人血浆中大量共存在的肾上腺甾体化合物,具有抗炎、抗增殖及抗抑郁等活性,其衍生物在实验中能促进动物免疫应答,而且具有很好的神经保护作用。此外,DHEA还是合成甾体药物的重要中间体。近几年来,DHEA凭借其重要研究价值,已逐渐发展成为最具热门的研究对象之一。 Dehypoepiandrosterone (DHEA) is a C19 steroid carrier compound with the chemical name 3β-hydroxyandrost-5-en-17-one, the molecular formula C 19 H 28 O 2 . DHEA is a large number of adrenal steroidal compounds coexisting in human plasma. It has anti-inflammatory, anti-proliferative and anti-depressant activities. Its derivatives can promote the immune response of animals in experiments and have a good neuroprotective effect. In addition, DHEA is an important intermediate for the synthesis of steroids. In recent years, DHEA has gradually developed into one of the most popular research objects due to its important research value.
传统的DHEA的合成大多采用化学方法,例如以孕甾双烯醇酮或醋酸妊娠双烯醇酮为原料,经过肟化、重排与水解后得到产物。然而所述合成方法分3步以上化学反应完成,原料价格高昂,并且工艺中使用苯、卤代烷或吡啶等溶剂,对环境伤害较大。此外,传统工艺中的产品纯度低、效率低,后期提纯操作繁琐。The synthesis of traditional DHEA is mostly carried out by chemical methods, for example, using pregnane dienolone or gestational dienolone acetate as a raw material, and after deuteration, rearrangement and hydrolysis, a product is obtained. However, the synthesis method is completed in three or more chemical reactions, the raw material price is high, and the solvent used in the process such as benzene, alkyl halide or pyridine is harmful to the environment. In addition, the products in the traditional process have low purity, low efficiency, and complicated purification operations in the later stage.
因此,开发一种步骤少、成本低、产率高且绿色环保的DHEA合成方法具有重要意义。Therefore, it is of great significance to develop a DHEA synthesis method with few steps, low cost, high yield and green environmental protection.
发明内容Summary of the invention
为了解决上述技术问题,本发明提供了一种去氢表雄酮的制备方法及其制备用酶,所述去氢表雄酮的制备方法共涉及二步反应,大大缩少了传统方法制备过程中繁多的合成步骤,同时本发明提供的制备用酶使所述去氢表雄酮的合成工艺具备高收率、低成本且绿色环保的特点。In order to solve the above technical problems, the present invention provides a preparation method of dehydroepiandrosterone and an enzyme for preparation thereof, and the preparation method of the dehydroepiandrosterone involves a two-step reaction, which greatly reduces the preparation process of the traditional method. The synthesis process of the present invention provides the synthesis process of the dehydroepiandrosterone with high yield, low cost and green environmental protection.
第一方面,本发明提供了一种去氢表雄酮的制备方法,包括:In a first aspect, the present invention provides a method for preparing dehydroepiandrosterone, comprising:
(1)在保护气氛下,向叔丁醇中加入叔丁醇钾,搅拌均匀后加入4-雄烯二酮得到混合料,将所述混合料滴加至含有抗坏血酸钠的乙酸溶液中反应得到5-雄烯二酮;(1) Adding potassium t-butoxide to t-butanol under a protective atmosphere, stirring uniformly, adding 4-androstenedione to obtain a mixture, and adding the mixture to an acetic acid solution containing sodium ascorbate to obtain a mixture 5-androstenedione;
(2)将步骤(1)中所述5-雄烯二酮溶于有机溶剂中,并添加酮还原酶、葡萄糖脱氢酶、葡萄糖和氧化还原辅酶得到混合液,控制所述混合液的pH为6.0-6.3,于22-26℃下搅拌反应1-6小时,得到反应液,将所述反应液分离提纯后得到去氢表雄酮,所述酮还原酶和所述葡萄糖脱氢酶由微生物菌株共表达产生并以粗酶液形式添加,所述酮还原酶的来源于领地伯克霍尔德菌属、红球菌属和鞘氨醇单胞菌属中的一种或多种。(2) dissolving the 5-androstenedione in the step (1) in an organic solvent, adding a ketoreductase, glucose dehydrogenase, glucose, and redox coenzyme to obtain a mixture, and controlling the pH of the mixture. For 6.0-6.3, the reaction is stirred at 22-26 ° C for 1-6 hours to obtain a reaction solution, and the reaction solution is separated and purified to obtain dehydroepiandrosterone, and the ketoreductase and the glucose dehydrogenase are The microbial strain is co-expressed and added as a crude enzyme solution derived from one or more of the genus Burkholderia, Rhodococcus and Sphingomonas.
本发明中,所述去氢表雄酮的制备方法的具体工艺路线如下所示:In the present invention, the specific process route of the preparation method of the dehydroepiandrosterone is as follows:
Figure PCTCN2018075822-appb-000001
Figure PCTCN2018075822-appb-000001
其中,所述工艺中共包括两步反应,第一步为化学法,第二步为生物酶法,所述4-雄烯二酮(4-Androstene-3,17-dione,4-AD)如所式(Ⅰ)所示,所述5-雄烯二酮(5-Androstene-3,17-dione,5-AD)如式(Ⅱ)所示,所述去氢表雄酮如式(Ⅲ)所示。Wherein, the process comprises a two-step reaction, the first step is a chemical method, the second step is a biological enzymatic method, and the 4-androstenenedione (4-Androstene-3, 17-dione, 4-AD) is as As shown in the formula (I), the 5-androstenone (5-Androstene-3, 17-dione, 5-AD) is represented by the formula (II), and the dehydroepiandrosterone is as defined in the formula (III). ) shown.
可选地,所述步骤(1)中,所述保护气氛是指所述充满氮气或惰性气体的环境下。所述惰性气体包括氦(He)、氖(Ne)、氩(Ar)、氪(Kr)和氙(Xe)中的一种或多种。Optionally, in the step (1), the protective atmosphere refers to the environment filled with nitrogen or an inert gas. The inert gas includes one or more of helium (He), neon (Ne), argon (Ar), krypton (Kr), and xenon (Xe).
可选地,所述步骤(1)中,所述混合料的具体制备过程包括:在室温下向叔丁醇中加入叔丁醇钾,然后升温至55-65℃,搅拌0.3-0.8小时至所述叔丁醇钾完全溶解后,将温度维持在25-30℃下,加入4-雄烯二酮搅拌0.3-0.8小时后,冷却得到所述混合料。本发明中,在加入叔丁醇钾后,将温度控制在55-65℃,可以大大缩短叔丁醇钾的溶解时间,可以将传统3小时以上的溶解时间缩短至0.5小时左右;随后将温度维持在25-30℃下,可以促进所述4-雄烯二酮高效地正向反应,若温度过高容易逆反应生成4-雄烯二酮,若温度过低则该反应过程耗时较长,生产效率低。Optionally, in the step (1), the specific preparation process of the mixture comprises: adding potassium t-butoxide to t-butanol at room temperature, then raising the temperature to 55-65 ° C, and stirring for 0.3-0.8 hours. After the potassium t-butoxide was completely dissolved, the temperature was maintained at 25 to 30 ° C, and 4-androstenedione was added thereto for stirring for 0.3 to 0.8 hours, followed by cooling to obtain the mixture. In the present invention, after the addition of potassium t-butoxide, the temperature is controlled at 55-65 ° C, the dissolution time of potassium t-butoxide can be greatly shortened, and the dissolution time of the conventional 3 hours or more can be shortened to about 0.5 hour; Maintaining at 25-30 ° C can promote the efficient forward reaction of the 4-androstenedione. If the temperature is too high, it is easy to reversely react to form 4-androstenedione. If the temperature is too low, the reaction takes a long time. , production efficiency is low.
可选地,所述步骤(1)中,所述将所述混合料滴加至含有抗坏血酸钠的乙酸溶液中反应得到5-雄烯二酮的过程中,反应温度为25-30℃,反应时间为0.3-0.8小时。进一步优选地,所述反应温度可以为26-30℃,反应时间为0.5-0.8小时。例如,所述反应温度为30℃。Optionally, in the step (1), the reaction mixture is added to an acetic acid solution containing sodium ascorbate to obtain a 5-androstenedione, and the reaction temperature is 25-30 ° C, and the reaction is carried out. The time is 0.3-0.8 hours. Further preferably, the reaction temperature may be 26 to 30 ° C, and the reaction time is 0.5 to 0.8 hours. For example, the reaction temperature is 30 °C.
可选地,步骤(1)中,所述4-雄烯二酮和所述叔丁醇钾的摩尔比为1:(0.75-1.2)。进一步可选地,所述4-雄烯二酮和所述叔丁醇钾的摩尔比为1:(0.8-1.2)。Optionally, in the step (1), the molar ratio of the 4-androstenedione and the potassium t-butoxide is 1: (0.75-1.2). Further optionally, the molar ratio of the 4-androstenedione and the potassium t-butoxide is 1: (0.8-1.2).
可选地,所述步骤(2)中,所述有机溶剂包括疏水性溶剂。进一步可选地,所述有机溶剂包括乙酸乙酯。本发明步骤(2)中优选的乙酸乙酯溶剂可以有效提高所述去氢表雄酮的产量。Optionally, in the step (2), the organic solvent comprises a hydrophobic solvent. Further optionally, the organic solvent comprises ethyl acetate. The preferred ethyl acetate solvent in step (2) of the present invention is effective to increase the yield of said dehydroepiandrosterone.
可选地,步骤(1)中,所述4-雄烯二酮、所述乙酸和所述抗坏血酸钠的摩尔比为1:(0.5-1):(0.04-0.4)。进一步可选地,所述4-雄烯二酮、所述乙酸和所述抗坏血酸钠的摩尔比为1:(0.6-1):(0.05-0.2)。Optionally, in the step (1), the molar ratio of the 4-androstenedione, the acetic acid and the sodium ascorbate is 1: (0.5-1): (0.04-0.4). Further optionally, the molar ratio of the 4-androstenedione, the acetic acid and the sodium ascorbate is 1: (0.6-1): (0.05-0.2).
可选地,所述步骤(2)中,所述酮还原酶、葡萄糖脱氢酶、葡萄糖和氧化还原辅酶为水溶液或缓冲溶液。进一步可选地,所述缓冲溶液包括磷酸盐缓冲液、Tris-HCl缓冲液或其他缓冲溶液,所述缓冲溶液的pH为6.0-7.0。例如所述缓冲溶液为磷酸钠缓冲液。可选地,所述缓 冲溶液的浓度为50-120mmol/L。进一步可选地,所述缓冲溶液的浓度为60-100mmol/L。优选的,所述缓冲溶液的浓度为80-120mmol/L。例如,所述缓冲溶液的浓度为60mmol/L,或为70mmol/L,或为90mmol/L,或为100mmol/L,或为120mmol/L。Optionally, in the step (2), the ketoreductase, glucose dehydrogenase, glucose and redox coenzyme are an aqueous solution or a buffer solution. Further optionally, the buffer solution comprises a phosphate buffer, a Tris-HCl buffer or other buffer solution having a pH of 6.0-7.0. For example, the buffer solution is a sodium phosphate buffer. Optionally, the buffer solution has a concentration of 50-120 mmol/L. Further optionally, the buffer solution has a concentration of 60-100 mmol/L. Preferably, the buffer solution has a concentration of 80-120 mmol/L. For example, the concentration of the buffer solution is 60 mmol/L, or 70 mmol/L, or 90 mmol/L, or 100 mmol/L, or 120 mmol/L.
可选地,所述酮还原酶、葡萄糖脱氢酶、葡萄糖和氧化还原辅酶这四种组分的添加形式可以是将酮还原酶、葡萄糖脱氢酶、葡萄糖和氧化还原辅酶这四种混合后同时添加;或单独添加所述酮还原酶、葡萄糖脱氢酶、葡萄糖和氧化还原辅酶,其中,当单独添加时,所述酮还原酶、葡萄糖脱氢酶、葡萄糖和氧化还原辅酶按顺序依次加入且添加顺序不做限定。所述酮还原酶、葡萄糖脱氢酶、葡萄糖和氧化还原辅酶的添加形式还可以为:取所述酮还原酶、葡萄糖脱氢酶、葡萄糖和氧化还原辅酶中的一种或多种,并与所述酮还原酶、葡萄糖脱氢酶、葡萄糖和氧化还原辅酶中剩下的组分混合后进行添加至所述含有5-雄烯二酮的有机溶剂中。例如,所述酮还原酶、葡萄糖脱氢酶、葡萄糖和氧化还原辅酶中的所述酮还原酶和所述葡萄糖脱氢酶先混合在一起,然后在酮还原酶和葡萄糖脱氢酶的混合组分中再添加剩下的葡萄糖和氧化还原辅酶这两种组分,得到了含有酮还原酶、葡萄糖脱氢酶、葡萄糖和氧化还原辅酶的混合组分,并将其添加至所述含有5-雄烯二酮的有机溶剂中得到混合液。Alternatively, the four components of the ketoreductase, glucose dehydrogenase, glucose, and redox coenzyme may be added after mixing four kinds of ketoreductase, glucose dehydrogenase, glucose, and redox coenzyme. Adding simultaneously; or separately adding the ketoreductase, glucose dehydrogenase, glucose, and redox coenzyme, wherein, when added alone, the ketoreductase, glucose dehydrogenase, glucose, and redox coenzyme are sequentially added in order. And the order of addition is not limited. The ketoreductase, glucose dehydrogenase, glucose, and redox coenzyme may be added in the form of one or more of the ketoreductase, glucose dehydrogenase, glucose, and redox coenzyme, and The remaining components of the ketoreductase, glucose dehydrogenase, glucose, and redox coenzyme are mixed and added to the organic solvent containing 5-androstenedione. For example, the ketoreductase in the ketoreductase, glucose dehydrogenase, glucose, and redox coenzyme and the glucose dehydrogenase are first mixed together, and then in a mixed group of ketoreductase and glucose dehydrogenase. Adding the remaining components of glucose and redox coenzyme to the fraction, and obtaining a mixed component containing ketoreductase, glucose dehydrogenase, glucose and redox coenzyme, and adding it to the 5-containing A mixed solution is obtained in an organic solvent of androstenedione.
可选地,所述步骤(2)中,所述葡萄糖的浓度为0.04-0.12mg/mL。进一步可选地,所述葡萄糖的浓度为0.08-0.1mg/mL。例如,所述葡萄糖在所述缓冲溶液中的浓度为0.1mg/mL,或为0.12mg/mL。Optionally, in the step (2), the concentration of the glucose is 0.04-0.12 mg/mL. Further optionally, the concentration of the glucose is from 0.08 to 0.1 mg/mL. For example, the concentration of the glucose in the buffer solution is 0.1 mg/mL, or 0.12 mg/mL.
可选地,所述步骤(2)中,所述微生物菌株包括Rosetta(DE3)大肠杆菌和BL21(DE3)大肠杆菌中的一种或两种。进一步可选地,所述微生物菌株包括Rosetta(DE3)大肠杆菌。Optionally, in the step (2), the microbial strain comprises one or both of Rosetta (DE3) E. coli and BL21 (DE3) E. coli. Further optionally, the microbial strain comprises Rosetta (DE3) E. coli.
可选地,所述步骤(2)中,所述微生物菌株共表达产生所述酮还原酶和所述葡萄糖脱氢酶的具体过程包括:构建一重组表达质粒,将所述重组表达质粒转染至所述微生物菌株内后,在微生物培养液中诱导含有所述重组表达质粒的微生物菌株表达所述酮还原酶和所述葡萄糖脱氢酶,其中所述重组表达质粒包括所述酮还原酶和所述葡萄糖脱氢酶的基因编码序列。所述酮还原酶和所述葡萄糖脱氢酶可以在所述微生物菌株的胞内生成,也可以由所述微生物菌株的胞内生成后在释放在所述微生物培养液中。通过对所述能够表达酮还原酶和葡萄糖脱氢酶的微生物菌株进行收集、清洗、破胞后收集得到所述粗酶液,所述粗酶液中包含有所述酮还原酶和所述葡萄糖脱氢酶。Optionally, in the step (2), the specific process of co-expressing the microbial strain to produce the ketoreductase and the glucose dehydrogenase comprises: constructing a recombinant expression plasmid, transfecting the recombinant expression plasmid After the microorganism strain is introduced, the microorganism strain containing the recombinant expression plasmid is induced to express the ketoreductase and the glucose dehydrogenase in a microorganism culture solution, wherein the recombinant expression plasmid includes the ketoreductase and The gene coding sequence of the glucose dehydrogenase. The ketoreductase and the glucose dehydrogenase may be produced intracellularly in the microbial strain, or may be released from the microbial culture solution after intracellular production of the microbial strain. The crude enzyme solution is obtained by collecting, washing, and granulating the microorganism strain capable of expressing a ketoreductase and a glucose dehydrogenase, and the crude enzyme solution contains the ketoreductase and the glucose Dehydrogenase.
本发明中,所述酮还原酶和所述葡萄糖脱氢酶是两个独立的蛋白分子,并通过上述共表达的方式得到,这样操作既可以节省生产成本,又能简化实验过程。所述重组表达质粒可以同时含有所述酮还原酶和所述葡萄糖脱氢酶的基因编码序列,并能够同时表达所述酮还原酶和所述葡萄糖脱氢酶两个蛋白分子。本发明中,以粗酶液的形式参与所述步骤(2)中的反应, 例如所述粗酶液可以是由大肠杆菌Rosetta(DE3)诱导表达所述酮还原酶和所述葡萄糖脱氢酶后,对所述大肠杆菌Rosetta(DE3)进行离心收集、清洗后,将菌体悬浮于缓冲溶液中并进行超声破胞后,所述酮还原酶和所述葡萄糖脱氢酶被释放至缓冲溶液中,得到所述粗酶液。本发明通过采用共表达形式得到酮还原酶和葡萄糖脱氢酶粗酶液参与DHEA的制备,不仅精简制备工艺,而且还提高产量,节约成本,绿色环保。进一步地,本发明还可以对所述酮还原酶和葡萄糖脱氢酶提纯并参与合成反应。In the present invention, the ketoreductase and the glucose dehydrogenase are two independent protein molecules, and are obtained by the above-mentioned co-expression, so that the operation can save production cost and simplify the experimental process. The recombinant expression plasmid may simultaneously contain the gene coding sequence of the ketoreductase and the glucose dehydrogenase, and simultaneously express the ketoreductase and the glucose dehydrogenase protein molecules. In the present invention, the reaction in the step (2) is carried out in the form of a crude enzyme solution, for example, the crude enzyme solution may be an expression of the ketoreductase and the glucose dehydrogenase induced by Escherichia coli Rosetta (DE3). After the Escherichia coli Rosetta (DE3) is collected by centrifugation and washing, after the cells are suspended in a buffer solution and subjected to ultrasonic disruption, the ketoreductase and the glucose dehydrogenase are released to a buffer solution. The crude enzyme solution is obtained. The invention adopts the co-expression form to obtain the ketoreductase and the glucose dehydrogenase crude enzyme solution to participate in the preparation of DHEA, not only streamlining the preparation process, but also improving the yield, saving cost and being green. Further, the present invention can also purify the ketoreductase and glucose dehydrogenase and participate in the synthesis reaction.
可选地,所述酮还原酶的基因编码序列包括如SEQ ID NO:1、SEQ ID NO:2和SEQ ID NO:3所示的核苷酸序列中的任意一种。可选地,所述葡萄糖脱氢酶的基因编码序列包括如SEQ ID NO:4所示的核苷酸序列。本发明优选地具有上述包括如SEQ ID NO:1、SEQ ID NO:2和SEQ ID NO:3所示的核苷酸序列中的任意一种的酮还原酶可以在所述微生物菌株中高效表达,所述粗酶液具有较高浓度的所述酮还原酶。Alternatively, the gene coding sequence of the ketoreductase includes any one of the nucleotide sequences shown in SEQ ID NO: 1, SEQ ID NO: 2, and SEQ ID NO: 3. Alternatively, the gene coding sequence of the glucose dehydrogenase comprises the nucleotide sequence as shown in SEQ ID NO: 4. The present invention preferably has the above ketoreductase comprising any one of the nucleotide sequences shown as SEQ ID NO: 1, SEQ ID NO: 2 and SEQ ID NO: 3, which can be efficiently expressed in the microorganism strain The crude enzyme solution has a higher concentration of the ketoreductase.
可选地,所述步骤(2)中,所述酮还原酶、所述葡萄糖脱氢酶和所述4-雄烯二酮的摩尔比为(0.015-0.04):(0.01-0.04):1。Optionally, in the step (2), the molar ratio of the ketoreductase, the glucose dehydrogenase, and the 4-androstenedione is (0.015-0.04): (0.01-0.04):1. .
所述步骤(2)中,所述氧化还原辅酶包括NAD +、NADP +、NADH和NADPH中的一种或多种。进一步可选地,所述步骤(2)中,所述氧化还原辅酶包括NAD +。可选地,所述步骤(2)中,所述氧化还原辅酶的浓度为0.04-0.4mg/mL。进一步可选地,所述氧化还原辅酶的浓度为0.08-0.2mg/mL。例如,所述氧化还原辅酶在所述缓冲溶液中的浓度为0.1mg/mL,或为0.15mg/mL,或为0.2mg/mL。 In the step (2), the redox coenzyme includes one or more of NAD + , NADP + , NADH, and NADPH. Further optionally, in the step (2), the redox coenzyme comprises NAD + . Optionally, in the step (2), the concentration of the redox coenzyme is 0.04-0.4 mg/mL. Further optionally, the concentration of the redox coenzyme is from 0.08 to 0.2 mg/mL. For example, the concentration of the redox coenzyme in the buffer solution is 0.1 mg/mL, or 0.15 mg/mL, or 0.2 mg/mL.
其中,所述NAD +为烟酰胺腺嘌呤二核苷酸(Nicotinamide adenine dinucleotide,NAD +),也称为氧化型辅酶Ⅰ;所述NADH为烟酰胺腺嘌呤二核苷酸的还原态,也称为还原型辅酶Ⅰ;所述NADP +为烟酰胺腺嘌呤二核苷酸磷酸(Nicotinamide adenine dinucleotide phosphate,NADP +),也称为氧化型辅酶Ⅱ;所述NADPH为烟酰胺腺嘌呤二核苷酸磷酸的还原态,也称为还原型辅酶Ⅱ。在存在氧气(O 2)的条件下,所述氧化还原辅酶,葡萄糖脱氢酶以及葡萄糖之间形成一个辅酶再生体系,该体系是一电子循环体系,在酮还原酶作用下,可以有效使5-雄烯二酮还原生成去氢表雄酮,提高去氢表雄酮的产量。本发明体系中,可以仅仅使用所述NAD +、NADP +、NADH和NADPH中的NAD +就能具有实现循环,且所述去氢表雄酮的具有很高产率。 Wherein, the NAD + is Nicotinamide adenine dinucleotide (NAD + ), also known as oxidized coenzyme I; the NADH is a reduced state of nicotinamide adenine dinucleotide, also called Is a reduced coenzyme I; the NADP + is nicotinamide adenine dinucleotide phosphate (NADP + ), also known as oxidized coenzyme II; the NADPH is nicotinamide adenine dinucleotide The reduced state of phosphoric acid, also known as reduced coenzyme II. In the presence of oxygen (O 2 ), a redox coenzyme, glucose dehydrogenase and glucose form a coenzyme regeneration system, which is an electronic cycle system, which can effectively make 5 under the action of ketoreductase - androstenedione is reduced to form dehydroepiandrosterone, which increases the yield of dehydroepiandrosterone. System of the present invention, DHEA has very high yields can only use the NAD +, NADP +, NADH and NADPH in NAD + can be implemented with cycles and the.
可选地,所述步骤(2)中分离提纯的过程包括依次进行的过滤、清洗和萃取过程。进一步可选地,所述步骤(2)之后还包括对所述去氢表雄酮进行重结晶。Optionally, the process of separating and purifying in the step (2) comprises a sequential filtration, washing and extraction process. Further optionally, the step (2) further comprises recrystallizing the dehydroepiandrosterone.
可选地,所述步骤(2)中分离提纯的具体过程包括:将所述反应液加至硅藻土中过滤得到滤液和滤饼,将滤饼用乙酸乙酯洗涤后得到洗涤液,收集并混合所述洗涤液和所述滤液, 得到水相和有机相,对所述水相用乙酸乙酯萃取两或三次后得到萃取液,将所述萃取液与所述有机相混合并经浓缩、过滤、清洗、洗涤干燥后得到去氢表雄酮。Optionally, the specific process of separating and purifying in the step (2) comprises: adding the reaction liquid to diatomaceous earth to obtain a filtrate and a filter cake, and washing the filter cake with ethyl acetate to obtain a washing liquid, and collecting And mixing the washing liquid and the filtrate to obtain an aqueous phase and an organic phase, and extracting the aqueous phase with ethyl acetate for two or three times to obtain an extract, and mixing the extract with the organic phase and concentrating Dehydroepiandrosterone is obtained by filtration, washing, washing and drying.
本方面第一方面所提供的去氢表雄酮的制备方法,所述制备方法工艺简单,省时高效、成本低廉、绿色环保,该制备方法可适用于大规模工业化生产;由所述制备方法制得的去氢表雄酮具有极高的产率。The method for preparing dehydroepiandrosterone provided by the first aspect of the present invention, the preparation method is simple, time-saving, high-efficiency, low-cost, green and environmentally friendly, and the preparation method is applicable to large-scale industrial production; The resulting dehydroepiandrosterone has an extremely high yield.
第二方面,本发明提供了一种酮还原酶,所述酮还原酶包括酮还原酶KRED3(简写成KRED3)、酮还原酶KRED4(简写成KRED4)和酮还原酶KRED5(简写成KRED5)中的一种或多种,所述酮还原酶KRED3的基因编码序列包括如SEQ ID NO:1所示的核苷酸序列,所述酮还原酶KRED4的基因编码序列包括如SEQ ID NO:2所示的核苷酸序列,所述酮还原酶KRED5的基因编码序列包括如SEQ ID NO:3所示的核苷酸序列。In a second aspect, the present invention provides a ketoreductase comprising ketoreductase KRED3 (abbreviated as KRED3), ketoreductase KRED4 (abbreviated as KRED4) and ketoreductase KRED5 (abbreviated as KRED5) One or more of the gene coding sequences of the ketoreductase KRED3 include the nucleotide sequence set forth in SEQ ID NO: 1, and the gene coding sequence of the ketoreductase KRED4 includes as set forth in SEQ ID NO: The nucleotide sequence shown, the gene coding sequence of the ketoreductase KRED5 includes the nucleotide sequence shown in SEQ ID NO: 3.
可选地,所述KRED3的基因编码序列还包括如SEQ ID NO:1所示的核苷酸序列至少95%同源性的核苷酸序列,所述KRED4的基因编码序列还包括如SEQ ID NO:2所示的核苷酸序列至少95%同源性的核苷酸序列,所述KRED5的基因编码序列还包括如SEQ ID NO:3所示的核苷酸序列至少95%同源性的核苷酸序列。Optionally, the gene coding sequence of KRED3 further comprises a nucleotide sequence of at least 95% homology of the nucleotide sequence shown in SEQ ID NO: 1, and the gene coding sequence of KRED4 further comprises SEQ ID NO: a nucleotide sequence of at least 95% homology of the nucleotide sequence shown by 2, the gene coding sequence of KRED5 further comprising at least 95% homology of the nucleotide sequence as shown in SEQ ID NO: Nucleotide sequence.
其中,所述KRED3的氨基酸序列包括如SEQ ID NO:5所示的氨基酸序列,所述KRED4的氨基酸序列包括如SEQ ID NO:6所示的氨基酸序列,所述KRED5的氨基酸序列包括如SEQ ID NO:7所示的氨基酸序列。可选地,所述葡萄糖脱氢酶的氨基酸序列包括如SEQ ID NO:8所示的氨基酸序列。Wherein the amino acid sequence of KRED3 comprises the amino acid sequence set forth in SEQ ID NO: 5, the amino acid sequence of KRED4 comprises the amino acid sequence set forth in SEQ ID NO: 6, and the amino acid sequence of KRED5 comprises SEQ ID NO: NO: The amino acid sequence shown in 7. Alternatively, the amino acid sequence of the glucose dehydrogenase comprises the amino acid sequence set forth in SEQ ID NO: 8.
可选地,本发明所述酮还原酶KRED3的基因来源于领地伯克霍尔德菌(Burkholderia territorii),所述酮还原酶KRED4的基因来源于红球菌属(Rhodococcus),所述酮还原酶KRED5的基因来源于鞘氨醇单胞菌属(Sphingomonas sp.)。所述葡萄糖脱氢酶的基因来源于巨大芽孢杆菌(Bacillus megaterium)。本发明优选地酮还原酶具有很强的化学选择性和区域选择性,在一定条件下,可以高效地将所述5-雄烯二酮转化为所述去氢表雄酮。Alternatively, the gene of the ketoreductase KRED3 of the present invention is derived from Burkholderia territorii, the gene of the ketoreductase KRED4 is derived from Rhodococcus, the ketoreductase The gene for KRED5 is derived from Sphingomonas sp. The gene for the glucose dehydrogenase is derived from Bacillus megaterium. Preferably, the ketoreductase of the present invention has strong chemical selectivity and regioselectivity, and under certain conditions, the 5-androstenedione can be efficiently converted into the dehydroepiandrosterone.
可选地,所述酮还原酶KRED3、KRED4和KRED5中的任意一个蛋白酶的基因片段上还包括His标签。进一步可选地,所述酮还原酶KRED3、KRED4和KRED5中的任意一个蛋白酶的基因片段上还包括8×His标签。所述葡萄糖脱氢酶的基因片段上还包括6×His标签。随着所述His标签的His数目的增加,所述蛋白的结合效率,纯化收率增加;本发明可以通过对所述所述酮还原酶和所述葡萄糖脱氢酶上连接不同His个数的His标签来分别提纯。Alternatively, the gene fragment of any one of the ketoreductases KRED3, KRED4 and KRED5 further includes a His tag. Further optionally, the gene fragment of any one of the ketoreductases KRED3, KRED4 and KRED5 further comprises an 8×His tag. The gene fragment of the glucose dehydrogenase further includes a 6 x His tag. As the number of His tags of the His tag increases, the binding efficiency of the protein increases, and the purification yield increases; the present invention can connect different numbers of His on the ketoreductase and the glucose dehydrogenase. The His tag is separately purified.
本发明第二方面提供的酮还原酶KRED3、KRED4和KRED5为本发明第一方面所述去氢表雄酮的制备方法的制备用酶之一,在所述基因片段的上增设His标签(组氨酸标签)的核苷酸序列,能使表达后的蛋白带上His标签,His标签有利于表达后蛋白的分离纯化,及在 实验中的分析和追踪,比如用于免疫印迹实验时的分析。The ketoreductases KRED3, KRED4 and KRED5 provided by the second aspect of the present invention are one of the enzymes for preparing the method for preparing dehydroepiandrosterone according to the first aspect of the present invention, and a His tag is added to the gene fragment (group) The nucleotide sequence of the amino acid tag enables the expressed protein to be tagged with His tag. The His tag facilitates the isolation and purification of the expressed protein, and is analyzed and traced in experiments, such as analysis for immunoblot experiments. .
第三方面,本方面还提供了一种酮还原酶在催化酮或醛转化为手性醇中的应用,所述酮还原酶的基因编码序列包括如SEQ ID NO:1、SEQ ID NO:2和SEQ ID NO:3所示的核苷酸序列中的任意一种。即本发明所述酮还原酶可以高效、有选择性地将醛或酮上的羰基催化还原为手性羟基。In a third aspect, the present invention also provides a use of a ketoreductase for catalyzing the conversion of a ketone or an aldehyde to a chiral alcohol, the gene coding sequence of the ketoreductase comprising SEQ ID NO: 1, SEQ ID NO: 2 And any one of the nucleotide sequences shown in SEQ ID NO: 3. That is, the ketoreductase of the present invention can efficiently and selectively catalyze the reduction of a carbonyl group on an aldehyde or a ketone to a chiral hydroxyl group.
可选地,所述催化酮或醛转化为手性醇中的应用包括催化5-雄烯二酮转化为去氢表雄酮中的应用。本发明优选地酮还原酶具有很强的化学选择性和区域选择性,在一定条件下,可以高效地、有选择性地将所述5-雄烯二酮转化为所述去氢表雄酮。Alternatively, the use of the catalytic ketone or aldehyde to convert to a chiral alcohol includes the use of catalyzing the conversion of 5-androstenedione to dehydroepiandrosterone. Preferably, the ketoreductase of the present invention has strong chemical selectivity and regioselectivity, and under certain conditions, the 5-androstenedione can be efficiently and selectively converted to the dehydroepiandrosterone. .
第四方面,本方面还提供了一种重组质粒,所述重组质粒包括酮还原酶的基因编码序列,所述酮还原酶的基因编码序列包括KRED3的基因编码序列、KRED4的基因编码序列和KRED5的基因编码序列中的一种或多种,所述KRED3的基因编码序列包括如SEQ ID NO:1所示的核苷酸序列,所述KRED4的基因编码序列包括如SEQ ID NO:2所示的核苷酸序列,所述KRED5的基因编码序列包括如SEQ ID NO:3所示的核苷酸序列。In a fourth aspect, the present invention also provides a recombinant plasmid comprising a gene coding sequence of a ketoreductase, wherein the gene coding sequence of the ketoreductase comprises a gene coding sequence of KRED3, a gene coding sequence of KRED4, and KRED5 One or more of the gene coding sequences, the gene coding sequence of KRED3 comprising the nucleotide sequence shown in SEQ ID NO: 1, the gene coding sequence of KRED4 comprising as shown in SEQ ID NO: The nucleotide sequence of the KRED5 gene coding sequence includes the nucleotide sequence shown in SEQ ID NO: 3.
可选地,所述重组质粒还包括葡萄糖脱氢酶的基因编码序列,所述葡萄糖脱氢酶的基因编码序列与所酮还原酶的基因编码序列之间还插入有RBS序列,所述葡萄糖脱氢酶的基因编码序列包括如SEQ ID NO:4所示的核苷酸序列,所述RBS序列包括如SEQ ID NO:17所示的核苷酸序列。可选地,所述重组质粒包括从5’端到3’端顺次连接的酮还原酶的基因编码序列、RBS序列和葡萄糖脱氢酶的基因编码序列。本发明所述RBS序列为核糖体结合位点(ribosome binding site,RBS)序列,可以有效促进两个同源基因(酮还原酶基因和葡萄糖脱氢酶基因)进行独立的转录及翻译。Optionally, the recombinant plasmid further comprises a gene coding sequence of glucose dehydrogenase, and an RBS sequence is inserted between the gene coding sequence of the glucose dehydrogenase and the gene coding sequence of the ketoreductase, and the glucose is removed. The gene coding sequence of the hydrogenase includes a nucleotide sequence as shown in SEQ ID NO: 4, and the RBS sequence includes the nucleotide sequence as shown in SEQ ID NO: 17. Alternatively, the recombinant plasmid includes a gene coding sequence for a ketoreductase ligated from the 5' end to the 3' end, a RBS sequence, and a gene coding sequence for glucose dehydrogenase. The RBS sequence of the present invention is a ribosome binding site (RBS) sequence, which can effectively promote the independent transcription and translation of two homologous genes (the ketoreductase gene and the glucose dehydrogenase gene).
本发明第四方面所述重组质粒可用于共表达酮还原酶和葡萄糖脱氢酶,该酮还原酶和葡萄糖脱氢酶具有很好的活性,可广泛应用于生物制药、蛋白生产等领域。The recombinant plasmid of the fourth aspect of the invention can be used for co-expressing ketone reductase and glucose dehydrogenase, and the ketoreductase and glucose dehydrogenase have excellent activity and can be widely used in the fields of biopharmaceuticals, protein production and the like.
第五方面,本发明还提供了一种重组质粒的制备方法,包括:In a fifth aspect, the present invention also provides a method for preparing a recombinant plasmid, comprising:
(1)提供或制备包含酮还原酶和葡萄糖脱氢酶的基因模板;(1) providing or preparing a gene template comprising a ketoreductase and a glucose dehydrogenase;
(2)制备所述酮还原酶和所述葡萄糖脱氢酶的基因的上游引物和下游引物,扩增所述酮还原酶和所述葡萄糖脱氢酶的基因片段,所述酮还原酶的基因编码序列包括如SEQ ID NO:1、SEQ ID NO:2和SEQ ID NO:3所示的核苷酸序列中的任意一种,所述葡萄糖脱氢酶的基因编码序列包括如SEQ ID NO:4所示的核苷酸序列;(2) preparing an upstream primer and a downstream primer of the ketoreductase and the gene of the glucose dehydrogenase, and amplifying the ketoreductase and the gene fragment of the glucose dehydrogenase, the gene of the ketoreductase The coding sequence includes any one of the nucleotide sequences set forth in SEQ ID NO: 1, SEQ ID NO: 2, and SEQ ID NO: 3, and the genetic coding sequence of the glucose dehydrogenase includes SEQ ID NO: a nucleotide sequence as shown in 4;
(3)取pET22b(+)载体质粒,将步骤(2)扩增得到的所述酮还原酶和所述葡萄糖脱氢酶基因片段插入至所述pET22b(+)载体质粒,纯化回收后进行连接,得到所述重组质粒。(3) taking the pET22b(+) vector plasmid, inserting the ketoreductase and the glucose dehydrogenase gene fragment amplified by the step (2) into the pET22b(+) vector plasmid, and purifying and recycling The recombinant plasmid was obtained.
可选地,所述酮还原酶的基因插入到pET22b(+)载体质粒中Nde I和EcoR I酶切位点之间。 所述酮还原酶的基因插入到pET22b(+)载体质粒时,所述酮还原酶的基因编码序列的3’端可加入终止密码子(如TAA)与pET22b(+)载体质粒中EcoRⅠ酶切位点相连。Alternatively, the gene for the ketoreductase is inserted between the Nde I and EcoR I cleavage sites in the pET22b(+) vector plasmid. When the gene of the ketoreductase is inserted into the pET22b(+) vector plasmid, the 3' end of the gene coding sequence of the ketoreductase can be added to the stop codon (such as TAA) and the pET22b (+) vector plasmid in the EcoRI digestion. The sites are connected.
所述葡萄糖脱氢酶的基因插入到pET22b(+)载体质粒中EcoR I和Xho I酶切位点之间。所述葡萄糖脱氢酶的基因插入到pET22b(+)载体质粒时,所述葡萄糖脱氢酶的基因编码序列的3’端可加入终止密码子(如TAA)与pET22b(+)载体质粒中Xho I酶切位点相连。The gene for the glucose dehydrogenase was inserted between the EcoR I and Xho I restriction sites in the pET22b(+) vector plasmid. When the gene of the glucose dehydrogenase is inserted into the pET22b(+) vector plasmid, the 3' end of the gene coding sequence of the glucose dehydrogenase may be added to a stop codon (such as TAA) and a pET22b (+) vector plasmid. I cleavage sites are linked.
可选地,在所述酮还原酶和所述葡萄糖脱氢酶基因编码序列之间插入RBS序列,所述RBS序列包括如SEQ ID NO:17所示的核苷酸序列可选地,所述酮还原酶的基因编码序列包括如SEQ ID NO:1、SEQ ID NO:2和SEQ ID NO:3所示的核苷酸序列中的任意一种,所述葡萄糖脱氢酶的基因编码序列包括如SEQ ID NO:4所示的核苷酸序列。所述酮还原酶和所述葡萄糖脱氢酶基因编码序列在所述pET22b(+)载体质粒的先后顺序可以是所述酮还原酶基因的3’端位于所述葡萄糖脱氢酶基因的5’端之前,或所述酮还原酶基因的5’端位于所述葡萄糖脱氢酶基因的3’端之后。Optionally, inserting an RBS sequence between the ketoreductase and the glucose dehydrogenase gene coding sequence, the RBS sequence comprising the nucleotide sequence set forth in SEQ ID NO: 17 optionally The gene coding sequence of the ketoreductase includes any one of the nucleotide sequences shown in SEQ ID NO: 1, SEQ ID NO: 2, and SEQ ID NO: 3, and the gene coding sequence of the glucose dehydrogenase includes A nucleotide sequence as shown in SEQ ID NO: 4. The sequence of the ketoreductase and the glucose dehydrogenase gene coding sequence in the pET22b(+) vector plasmid may be that the 3' end of the ketoreductase gene is located 5' of the glucose dehydrogenase gene Before the end, or the 5' end of the ketoreductase gene is located after the 3' end of the glucose dehydrogenase gene.
进一步可选地,所述RBS序列插入至所述葡萄糖脱氢酶基因序列的5’端前。所述RBS序列的3’端与所述葡萄糖脱氢酶基因序列的5’端之间还可以设置一段linker,便于所述葡萄糖脱氢酶的翻译识别,有利于酮还原酶和葡萄糖脱氢酶能够在同一载体中分别进行翻译表达。优选地,所述linker的序列可以为“ATATACAT”。Further optionally, the RBS sequence is inserted before the 5' end of the glucose dehydrogenase gene sequence. A linker may be disposed between the 3' end of the RBS sequence and the 5' end of the glucose dehydrogenase gene sequence to facilitate translation recognition of the glucose dehydrogenase, which is beneficial to ketoreductase and glucose dehydrogenase. Translational expression can be performed separately in the same vector. Preferably, the sequence of the linker may be "ATATACAT".
可选地,所述步骤(3)中,所示pET22b(+)载体质粒采用的酶切位点包括Nde I内切酶和Xho I内切酶。Alternatively, in the step (3), the cleavage sites used for the pET22b(+) vector plasmid include Nde I endonuclease and Xho I endonuclease.
本发明中,所述制备方法可以制备仅含有酮还原酶或葡萄糖脱氢酶的重组质粒,也可以制备同时含有酮还原酶和葡萄糖脱氢酶的重组质粒。可选地,将所述重组质粒转染至微生物菌株中诱导表达可以获得本发明所述酮还原酶和葡萄糖脱氢酶中的一种或两种。In the present invention, the preparation method can prepare a recombinant plasmid containing only a ketoreductase or a glucose dehydrogenase, and can also prepare a recombinant plasmid containing both a ketoreductase and a glucose dehydrogenase. Alternatively, one or both of the ketoreductase and glucose dehydrogenase of the present invention can be obtained by transfecting the recombinant plasmid into a microbial strain to induce expression.
本发明的有益效果包括以下几个方面:The beneficial effects of the present invention include the following aspects:
1、本发明所述去氢表雄酮的制备方法,共包括两步反应,以4-雄烯二酮为初始原料,并采用酮还原酶等生物酶,生产成本低廉,工艺简单,省时高效,反应条件温和,大大提高了产品的收率;1. The preparation method of dehydroepiandrosterone according to the present invention comprises a two-step reaction, using 4-androstenedione as a starting material, and adopting a biological enzyme such as ketoreductase, which has low production cost, simple process and time saving. High efficiency, mild reaction conditions, greatly improving the yield of the product;
2、本发明所述去氢表雄酮的制备方法,绿色环保,从根源上避免了环境污染问题,进一步降低成本,可以广泛适用于工业化规模生产;2. The preparation method of dehydroepiandrosterone according to the invention is green and environmentally friendly, avoids environmental pollution problems from the root causes, further reduces costs, and can be widely applied to industrial scale production;
3、由本发明所述的方法制备的去氢表雄酮,纯度高,可在制药领域或生物医学领域中有广泛的应用。3. Dehydroepiandrosterone prepared by the method of the present invention has high purity and can be widely used in the pharmaceutical field or biomedical field.
附图说明DRAWINGS
图1为本发明一实施例提供的pET22b-KRED3-GDH重组质粒的质粒图谱;1 is a plasmid map of a recombinant plasmid pET22b-KRED3-GDH according to an embodiment of the present invention;
图2为本发明一实施例提供的pET22b-KRED4-GDH重组质粒的质粒图谱;2 is a plasmid map of a recombinant plasmid pET22b-KRED4-GDH according to an embodiment of the present invention;
图3为本发明一实施例提供的pET22b-KRED5-GDH重组质粒的质粒图谱;3 is a plasmid map of a recombinant plasmid pET22b-KRED5-GDH according to an embodiment of the present invention;
图4为本发明一实施例提供的KRED3-GDH粗酶液的凝胶电泳图;4 is a gel electrophoresis diagram of a KRED3-GDH crude enzyme solution according to an embodiment of the present invention;
图5为本发明一实施例提供的KRED4-GDH粗酶液的凝胶电泳图;5 is a gel electrophoresis diagram of a KRED4-GDH crude enzyme solution according to an embodiment of the present invention;
图6为本发明一实施例提供的KRED5-GDH粗酶液的凝胶电泳图;6 is a gel electrophoresis diagram of a KRED5-GDH crude enzyme solution according to an embodiment of the present invention;
图7为本发明一实施例提供的4-雄烯二酮的高效液相色谱图;7 is a high performance liquid chromatogram of 4-androstenedione according to an embodiment of the present invention;
图8为本发明一实施例提供的5-雄烯二酮的高效液相色谱图;8 is a high performance liquid chromatogram of 5-androstenedione according to an embodiment of the present invention;
图9为本发明一实施例提供的去氢表雄酮标准品的高效液相色谱图;9 is a high performance liquid chromatogram of a dehydroepiandrosterone standard according to an embodiment of the present invention;
图10为本发明一实施例提供的去氢表雄酮粗产品的高效液相色谱图。Figure 10 is a high performance liquid chromatogram of a crude product of dehydroepiandrosterone according to an embodiment of the present invention.
具体实施方式Detailed ways
以下所述是本发明实施例的优选实施方式,应当指出,对于本技术领域的普通技术人员来说,在不脱离本发明实施例原理的前提下,还可以做出若干改进和润饰,这些改进和润饰也视为本发明实施例的保护范围。The following are the preferred embodiments of the embodiments of the present invention, and it should be noted that those skilled in the art can make some improvements and refinements without departing from the principles of the embodiments of the present invention. And retouching is also considered to be the scope of protection of the embodiments of the present invention.
若无特别说明,本发明实施例所采用的原料及其它化学试剂皆为市售商品。Unless otherwise stated, the raw materials and other chemical reagents used in the examples of the present invention are all commercially available.
本发明实施例提供了一种酮还原酶和葡萄糖脱氢酶的制备方法,所述酮还原酶和葡萄糖脱氢酶为所述去氢表雄酮的制备方法中的制备用酶,具体的实验步骤包括:The present invention provides a preparation method of a ketoreductase and a glucose dehydrogenase, wherein the ketoreductase and the glucose dehydrogenase are enzymes for preparation in the preparation method of the dehydroepiandrosterone, and the specific experiment The steps include:
(1)构建pET22b-KRED3/4/5-GDH重组质粒(1) Construction of pET22b-KRED3/4/5-GDH recombinant plasmid
提供上游引物和下游引物,采用PCR扩增实验得到酮还原酶KRED3、酮还原酶KRED4、酮还原酶KRED5和葡萄糖脱氢酶的基因编码序列。其中,所述酮还原酶KRED3的基因编码序列如SEQ ID NO:1所示,所述酮还原酶KRED4的基因编码序列如SEQ ID NO:2所示,所述酮还原酶KRED5的基因编码序列如SEQ ID NO:3所示,所述葡萄糖脱氢酶的基因编码序列如SEQ ID NO:4所示。所述酮还原酶KRED3对应的上游引物的碱基序列如SEQ ID NO:9所示,下游引物的碱基序列如SEQ ID NO:10所示。所述酮还原酶KRED3的基因对应的上游引物的碱基序列如SEQ ID NO:9所示,下游引物的碱基序列如SEQ ID NO:10所示。所述酮还原酶KRED4的基因对应的上游引物的碱基序列如SEQ ID NO:11所示,下游引物的碱基序列如SEQ ID NO:12所示。所述酮还原酶KRED5的基因对应的上游引物的碱基序列如SEQ ID NO:13所示,下游引物的碱基序列如SEQ ID NO:14所示。所述葡萄糖脱氢酶的基因对应的上游引物的碱基序列如SEQ ID NO:15所示,下游引物的碱基序列如SEQ ID NO:16所示。在所述葡萄糖脱氢酶的基因的5’端前插入RBS序列,并可通过上下游引物进行将其与插入至质粒pET22b(+)中,所述RBS序列如SEQ ID NO:17所示。The upstream primer and the downstream primer were provided, and the gene coding sequences of ketoreductase KRED3, ketoreductase KRED4, ketoreductase KRED5 and glucose dehydrogenase were obtained by PCR amplification experiments. Wherein the gene coding sequence of the ketoreductase KRED3 is as shown in SEQ ID NO: 1, the gene coding sequence of the ketoreductase KRED4 is as shown in SEQ ID NO: 2, and the coding sequence of the ketoreductase KRED5 is encoded. As shown in SEQ ID NO: 3, the gene coding sequence of the glucose dehydrogenase is shown in SEQ ID NO: 4. The base sequence of the upstream primer corresponding to the ketoreductase KRED3 is shown in SEQ ID NO: 9, and the base sequence of the downstream primer is shown in SEQ ID NO: 10. The base sequence of the upstream primer corresponding to the gene of the ketoreductase KRED3 is shown in SEQ ID NO: 9, and the base sequence of the downstream primer is shown in SEQ ID NO: 10. The base sequence of the upstream primer corresponding to the gene of the ketoreductase KRED4 is shown in SEQ ID NO: 11, and the base sequence of the downstream primer is shown in SEQ ID NO: 12. The base sequence of the upstream primer corresponding to the gene of the ketoreductase KRED5 is shown in SEQ ID NO: 13, and the base sequence of the downstream primer is shown in SEQ ID NO: 14. The base sequence of the upstream primer corresponding to the gene of the glucose dehydrogenase is shown in SEQ ID NO: 15, and the base sequence of the downstream primer is shown in SEQ ID NO: 16. The RBS sequence is inserted before the 5' end of the gene of the glucose dehydrogenase, and can be inserted into the plasmid pET22b(+) by the upstream and downstream primers as shown in SEQ ID NO: 17.
通过对应的上游引物和下游引物分别进行PCR扩增体系,配置扩增体系如下:The PCR amplification system was carried out by the corresponding upstream primer and downstream primer, respectively, and the amplification system was configured as follows:
Figure PCTCN2018075822-appb-000002
Figure PCTCN2018075822-appb-000002
PCR扩增程序为:98℃预变性2min;98℃变性10s;60℃退火30s;72℃延伸1min;30个循环后,72℃延伸10min。PCR产物经胶回收试剂盒纯化后,分别利用限制性内切酶Nde I和EcoR I、EcoR I和Xho I进行酶切,酶切后用T4连接酶连接已用Nde I和Xho I酶切处理的质粒pET22b(+)。连接产物转入大肠杆菌DH5α,经过氨苄抗性(Amp +)的筛选后挑取菌落送测序,测序成功后即得到酮还原酶和葡萄糖脱氢酶共表达的重组质粒pET22b-KRED3/4/5-GDH(包括pET22b-KRED3-GDH、pET22b-KRED4-GDH或pET22b-KRED5-GDH)。所述重组质粒pET22b-KRED3-GDH的质粒图谱如图1所示;所述重组质粒pET22b-KRED4-GDH的质粒图谱如图2所示;所述重组质粒pET22b-KRED5-GDH的质粒图谱如图3所示。本实施方式中所述DNA模板分别为质粒pET22b-KRED3、pET22b-KRED4、pET22b-KRED5和pET22b-GDH。 The PCR amplification procedure was: predenaturation at 98 ° C for 2 min; denaturation at 98 ° C for 10 s; annealing at 60 ° C for 30 s; extension at 72 ° C for 1 min; after 30 cycles, extension at 72 ° C for 10 min. The PCR products were purified by gel recovery kit and digested with restriction endonucleases Nde I and EcoR I, EcoR I and Xho I respectively. After digestion, they were ligated with T4 ligase and digested with Nde I and Xho I. Plasmid pET22b(+). The ligation product was transferred into E. coli DH5α, and after screening with ampicillin resistance (Amp + ), the colony was picked and sequenced. After successful sequencing, the recombinant plasmid pET22b-KRED3/4/5 co-expressed by ketoreductase and glucose dehydrogenase was obtained. - GDH (including pET22b-KRED3-GDH, pET22b-KRED4-GDH or pET22b-KRED5-GDH). The plasmid map of the recombinant plasmid pET22b-KRED3-GDH is shown in Figure 1; the plasmid map of the recombinant plasmid pET22b-KRED4-GDH is shown in Figure 2; the plasmid map of the recombinant plasmid pET22b-KRED5-GDH is shown in Figure 3 is shown. The DNA templates described in the present embodiment are plasmids pET22b-KRED3, pET22b-KRED4, pET22b-KRED5, and pET22b-GDH, respectively.
(2)表达酮还原酶和葡萄糖脱氢酶(2) expression of ketoreductase and glucose dehydrogenase
将构建的重组质粒pET22b-KRED3-GDH、pET22b-KRED4-GDH和pET22b-KRED5-GDH中的一种或多种转入大肠杆菌Rosetta(DE3)中,得到能够表达酮还原酶和葡萄糖脱氢酶的大肠杆菌Rosetta(DE3)。将含有重组质粒pET22b-KRED3-GDH、pET22b-KRED4-GDH或pET22b-KRED5-GDH的大肠杆菌以1%的接种量接种至含有10mL的LB培养基(100μg/mL氨苄青霉素(Amp))的50mL三角瓶中,维持恒定的37℃,200rpm的摇晃速率,过夜培养后,将菌液以1%的接种量转接到含有1L的LB培养基(100μg/mL Amp)的2L三角瓶中,继续37℃恒温培养至培养基中的OD600值达到0.6左右,加入异丙基-β-D-硫代半乳糖苷(IPTG)诱导剂(体系终浓度0.5mM),在37℃条件培养8小时后离心收集菌体。将菌体分别用4倍质量的100mM的磷酸钾缓冲液(pH=6.5)进行重悬并超声破碎20min,得到KRED3-GDH粗酶液、KRED4-GDH粗酶液或KRED5-GDH粗酶液。所述KRED3-GDH粗酶液中含有酮还原酶KRED3和葡萄糖脱氢酶。所述KRED4-GDH粗酶液中含有酮还原酶 KRED4和葡萄糖脱氢酶。所述KRED5-GDH粗酶液中含有酮还原酶KRED5和葡萄糖脱氢酶。Transfer one or more of the constructed recombinant plasmids pET22b-KRED3-GDH, pET22b-KRED4-GDH and pET22b-KRED5-GDH into E. coli Rosetta (DE3) to obtain ketone reductase and glucose dehydrogenase E. Rosetta (DE3). Escherichia coli containing the recombinant plasmid pET22b-KRED3-GDH, pET22b-KRED4-GDH or pET22b-KRED5-GDH was inoculated to a 50 mL containing 10 mL of LB medium (100 μg/mL ampicillin (Amp)) at a 1% inoculation amount. In a triangular flask, maintain a constant shaking temperature of 37 ° C and 200 rpm. After overnight culture, transfer the bacterial solution to a 2 L flask containing 1 L of LB medium (100 μg/mL Amp) at 1% inoculation. The OD600 value of the medium cultured at 37 ° C was adjusted to about 0.6, and isopropyl-β-D-thiogalactoside (IPTG) inducer (systemic concentration: 0.5 mM) was added, and cultured at 37 ° C for 8 hours. The cells were collected by centrifugation. The cells were resuspended in 4 times the mass of 100 mM potassium phosphate buffer (pH=6.5) and sonicated for 20 min to obtain KRED3-GDH crude enzyme solution, KRED4-GDH crude enzyme solution or KRED5-GDH crude enzyme solution. The KRED3-GDH crude enzyme solution contains a ketoreductase KRED3 and a glucose dehydrogenase. The KRED4-GDH crude enzyme solution contains a ketoreductase KRED4 and a glucose dehydrogenase. The KRED5-GDH crude enzyme solution contains a ketoreductase KRED5 and a glucose dehydrogenase.
将表达获得的KRED3-GDH粗酶液、KRED4-GDH粗酶液或KRED5-GDH粗酶液分别进行SDS-聚丙烯酰胺凝胶电泳(SDS-PAGE)鉴定。图4为所述KRED3-GDH粗酶液的凝胶电泳图,其中泳道M为蛋白Marker(Thermo Scientific PageRuler),泳道1为菌体破胞后总蛋白,泳道2为菌体破胞后上清液,其中KRED3的分子量约为28kDa,GDH的分子量为26kDa。图5为所述KRED4-GDH粗酶液的凝胶电泳图,其中泳道M为蛋白Marker(Thermo Scientific PageRuler),泳道1为菌体破胞后上清液,泳道2为菌体破胞后总蛋白,其中KRED4的分子量为29kDa,GDH的分子量为26kDa。图6为所述KRED5-GDH粗酶液的凝胶电泳图,其中泳道M为蛋白Marker(Thermo Scientific PageRuler),泳道1为菌体破胞后上清液,泳道2为菌体破胞后总蛋白,其中KRED5的分子量为28kDa,GDH的分子量为26kDa。所述酮还原酶KRED3、KRED4和KRED5,以及GDH的分子均于相应蛋白的理论计算值相近。The obtained KRED3-GDH crude enzyme solution, KRED4-GDH crude enzyme solution or KRED5-GDH crude enzyme solution was identified by SDS-polyacrylamide gel electrophoresis (SDS-PAGE). Figure 4 is a gel electrophoresis diagram of the KRED3-GDH crude enzyme solution, wherein the lane M is the protein Marker (Thermo Scientific PageRuler), the lane 1 is the total protein after the cell disruption, and the lane 2 is the supernatant after the cell disruption. The solution wherein KRED3 has a molecular weight of about 28 kDa and GDH has a molecular weight of 26 kDa. Figure 5 is a gel electrophoresis diagram of the KRED4-GDH crude enzyme solution, wherein the lane M is the protein Marker (Thermo Scientific PageRuler), the lane 1 is the supernatant after the cell disruption, and the lane 2 is the total cell after the cell is broken. The protein, wherein KRED4 has a molecular weight of 29 kDa and the GDH has a molecular weight of 26 kDa. Figure 6 is a gel electrophoresis diagram of the KRED5-GDH crude enzyme solution, wherein the lane M is the protein Marker (Thermo Scientific PageRuler), the lane 1 is the supernatant after the cell disruption, and the lane 2 is the total cell after the cell is broken. The protein, wherein KRED5 has a molecular weight of 28 kDa and the GDH has a molecular weight of 26 kDa. The ketoreductases KRED3, KRED4 and KRED5, as well as the molecules of GDH, are similar in theoretical calculations for the corresponding proteins.
实施例一 Embodiment 1
一种去氢表雄酮的制备方法,包括以下步骤:A method for preparing dehydroepiandrosterone comprises the following steps:
(1)在氮气保护下,在388mL的叔丁醇中加入82.5g叔丁醇钾,然后升温到60℃,搅拌0.5h至叔丁醇钾完全溶解,降温至30℃,持续氮气保护中加入100g的4-AD,持续搅拌0.5h后,冷却至室温得到混合料。在氮气保护下,在205.3g的26.8%的乙酸水溶液中,加入6.0g抗坏血酸钠,得到含有抗坏血酸钠的乙酸溶液。在氮气保护下,30℃下,将所述混合料在30min内缓慢滴加到含有抗坏血酸钠的乙酸溶液中,维持在温度30℃下续搅拌0.5h,室温冷却,得到含有5-AD的反应液。(1) Under nitrogen protection, add 82.5g of potassium t-butoxide to 388mL of tert-butanol, then raise the temperature to 60 ° C, stir for 0.5h to completely dissolve potassium t-butoxide, cool down to 30 ° C, continue to add nitrogen protection 100 g of 4-AD was continuously stirred for 0.5 h and then cooled to room temperature to obtain a mixture. Under a nitrogen atmosphere, 6.0 g of sodium ascorbate was added to 205.3 g of a 26.8% aqueous acetic acid solution to obtain an acetic acid solution containing sodium ascorbate. Under nitrogen protection, the mixture was slowly added dropwise to the acetic acid solution containing sodium ascorbate at 30 ° C for 30 min, maintained at a temperature of 30 ° C for 0.5 h, and cooled at room temperature to obtain a reaction containing 5-AD. liquid.
(2)将500mL乙酸乙酯加入所述5-AD的反应液中,搅拌均匀,加入400mL 1.8g/L KRED3和GDH的粗酶液,300mL 100mmol/L磷酸钠缓冲液(pH6.5),100g葡萄糖,200mg NAD +,于25℃搅拌至完全溶解,加入含有5-AD的反应液,控制pH为6.3,温度26℃,以200rpm的速率搅拌3h,得到酶反应液;将酶反应液加入至硅藻土中搅拌、过滤后收集滤饼,并用乙酸乙酯对滤饼洗涤两次,并将洗涤液和滤液混合,分开水相和有机相,水相用乙酸乙酯萃取两次,萃取液与有机相混合,将有机相减压浓缩后,加入600g水并充分搅拌后过滤,滤饼用120g水洗涤两次,将洗涤后的滤饼真空干燥得DHEA粗产品。将DHEA粗产品转入至干净的容器中,加入234g丙酮溶解后再加200g水,重复上述操作进行重结晶,得到78.02g DHEA最终产物,本实施例中,DHEA的收率为78.02%。 (2) 500 mL of ethyl acetate was added to the reaction solution of the 5-AD, and the mixture was stirred uniformly, and 400 mL of a 1.8 g/L KRED3 and GDH crude enzyme solution, 300 mL of 100 mmol/L sodium phosphate buffer (pH 6.5) was added. 100 g of glucose, 200 mg of NAD + , stirred at 25 ° C until completely dissolved, adding a reaction solution containing 5-AD, controlling pH to 6.3, temperature 26 ° C, stirring at 200 rpm for 3 h to obtain an enzyme reaction solution; adding the enzyme reaction solution After stirring to diatomaceous earth, the filter cake was collected, and the filter cake was washed twice with ethyl acetate. The washing liquid and the filtrate were mixed, the aqueous phase and the organic phase were separated, and the aqueous phase was extracted twice with ethyl acetate. The liquid was mixed with the organic phase, and the organic phase was concentrated under reduced pressure. 600 g of water was added, and the mixture was thoroughly stirred and then filtered. The filter cake was washed twice with 120 g of water, and the washed cake was vacuum dried to obtain a crude DHEA product. The crude DHEA product was transferred to a clean container, and 234 g of acetone was added to dissolve, and then 200 g of water was added, and the above operation was repeated to carry out recrystallization to obtain 78.02 g of DHEA final product. In the present example, the yield of DHEA was 78.02%.
分别对两步反应进行取样检测,检测条件:费罗门Phenyl-Hexyl 250×4.6mm色谱柱,波长UV210nm,流动相为50%乙腈水溶液,流速1.0mL/min,温度25℃。其中,从4-AD的液相色谱图(见图7)和5-AD合成过程中的液相色谱图(见图8)对比发现,4-AD可以高效地转化 生产5-AD;将DHEA粗产品的液相色谱图(将图10)与DHEA标准品液相色谱图(见图9)进行比对,粗产品中含有纯度较高的DHEA。The two-step reaction was sampled and tested. The detection conditions were: Ferenbach Phenyl-Hexyl 250×4.6 mm column, wavelength UV210 nm, mobile phase 50% acetonitrile aqueous solution, flow rate 1.0 mL/min, temperature 25 °C. Among them, from the liquid chromatogram of 4-AD (see Figure 7) and the liquid chromatogram of 5-AD synthesis (see Figure 8), it was found that 4-AD can be efficiently converted to produce 5-AD; DHEA The liquid chromatogram of the crude product (Figure 10) is compared to the liquid chromatogram of the DHEA standard (see Figure 9), which contains the higher purity DHEA.
实施例二 Embodiment 2
一种去氢表雄酮的制备方法,包括以下步骤:A method for preparing dehydroepiandrosterone comprises the following steps:
(1)在氮气保护下,在388mL的叔丁醇中加入80.0g叔丁醇钾,然后升温到55℃,搅拌0.8h至叔丁醇钾完全溶解,降温至30℃,持续氮气保护中加入100g的4-AD,持续搅拌0.6h后,冷却至室温得到混合料。在氮气保护下,在200.0g的26.8%的乙酸水溶液中,加入6.0g抗坏血酸钠,得到含有抗坏血酸钠的乙酸溶液。在氮气保护下,30℃下,将所述混合料在30min内缓慢滴加到含有抗坏血酸钠的乙酸溶液中,维持在温度30℃下续搅拌0.5h,室温冷却,得到含有5-AD的反应液。(1) Under nitrogen protection, add 80.0 g of potassium t-butoxide to 388 mL of tert-butanol, then raise the temperature to 55 ° C, stir for 0.8 h until the potassium tert-butoxide is completely dissolved, cool to 30 ° C, and continue to add nitrogen gas. 100 g of 4-AD was stirred for 0.6 h and then cooled to room temperature to obtain a mixture. Under a nitrogen atmosphere, 6.0 g of sodium ascorbate was added to 200.0 g of a 26.8% aqueous acetic acid solution to obtain an acetic acid solution containing sodium ascorbate. Under nitrogen protection, the mixture was slowly added dropwise to the acetic acid solution containing sodium ascorbate at 30 ° C for 30 min, maintained at a temperature of 30 ° C for 0.5 h, and cooled at room temperature to obtain a reaction containing 5-AD. liquid.
(2)将500mL乙酸乙酯加入所述5-AD的反应液中,搅拌均匀,加入400mL 1.5g/L KRED4和GDH的粗酶液,300mL 80mmol/L磷酸钠缓冲液(pH6.0),100g葡萄糖,200mg NAD +,于25℃搅拌至完全溶解,加入含有5-AD的反应液,控制pH为6.1,温度22℃,以180rpm的速率搅拌5h,得到酶反应液;将酶反应液加入至硅藻土中搅拌、过滤后收集滤饼,并用乙酸乙酯对滤饼洗涤两次,并将洗涤液和滤液混合,分开水相和有机相,水相用乙酸乙酯萃取两次,萃取液与有机相混合,将有机相减压浓缩后,加入600g水并充分搅拌后过滤,滤饼用120g水洗涤两次,将洗涤后的滤饼真空干燥得DHEA粗产品。将DHEA粗产品转入至干净的容器中,加入234g丙酮溶解后再加200g水,重复上述操作进行重结晶,得到75.16g DHEA最终产物,本实施例中,DHEA的收率为75.16%。 (2) 500 mL of ethyl acetate was added to the reaction solution of the 5-AD, and the mixture was stirred uniformly. 400 mL of a crude enzyme solution of 1.5 g/L of KRED4 and GDH, 300 mL of 80 mmol/L sodium phosphate buffer (pH 6.0) was added. 100 g of glucose, 200 mg of NAD + , stirred at 25 ° C until completely dissolved, adding a reaction solution containing 5-AD, controlling pH to 6.1, temperature 22 ° C, stirring at 180 rpm for 5 h to obtain an enzyme reaction solution; adding the enzyme reaction solution After stirring to diatomaceous earth, the filter cake was collected, and the filter cake was washed twice with ethyl acetate. The washing liquid and the filtrate were mixed, the aqueous phase and the organic phase were separated, and the aqueous phase was extracted twice with ethyl acetate. The liquid was mixed with the organic phase, and the organic phase was concentrated under reduced pressure. 600 g of water was added, and the mixture was thoroughly stirred and then filtered. The filter cake was washed twice with 120 g of water, and the washed cake was vacuum dried to obtain a crude DHEA product. The crude DHEA product was transferred to a clean container, and 234 g of acetone was added to dissolve, and then 200 g of water was added. The above operation was repeated for recrystallization to obtain 75.16 g of DHEA final product. In the present example, the yield of DHEA was 75.16%.
实施例三Embodiment 3
一种去氢表雄酮的制备方法,包括以下步骤:A method for preparing dehydroepiandrosterone comprises the following steps:
(1)在氮气保护下,在400mL的叔丁醇中加入90.0g叔丁醇钾,然后升温到65℃,搅拌0.3h至叔丁醇钾完全溶解,降温至30℃,持续氮气保护中加入100g的4-AD,持续搅拌0.5h后,冷却至室温得到混合料。在氮气保护下,在230g的25%的乙酸水溶液中,加入6.5g抗坏血酸钠,得到含有抗坏血酸钠的乙酸溶液。在氮气保护下,30℃下,将所述混合料在30min内缓慢滴加到含有抗坏血酸钠的乙酸溶液中,维持在温度28℃下续搅拌0.5h,室温冷却,得到含有5-AD的反应液。(1) Under nitrogen protection, add 90.0g of potassium t-butoxide to 400mL of tert-butanol, then raise the temperature to 65 ° C, stir for 0.3h to completely dissolve potassium t-butoxide, cool down to 30 ° C, continue to add nitrogen protection 100 g of 4-AD was continuously stirred for 0.5 h and then cooled to room temperature to obtain a mixture. Under a nitrogen atmosphere, 6.5 g of sodium ascorbate was added to 230 g of a 25% aqueous acetic acid solution to obtain an acetic acid solution containing sodium ascorbate. Under nitrogen protection, the mixture was slowly added dropwise to the acetic acid solution containing sodium ascorbate at 30 ° C for 30 min, maintained at a temperature of 28 ° C for 0.5 h, and cooled at room temperature to obtain a reaction containing 5-AD. liquid.
(2)将500mL乙酸乙酯加入所述5-AD的反应液中,搅拌均匀,加入400mL 2.0g/L KRED5和GDH的粗酶液,300mL 100mmol/L磷酸钠缓冲液(pH7.0),100g葡萄糖,180mg NADH,于25℃搅拌至完全溶解,加入含有5-AD的反应液,控制pH为6.2,温度26℃,以220rpm的速率搅拌2h,得到酶反应液;将酶反应液加入至硅藻土中搅拌、过滤后收集滤饼,并用乙酸乙 酯对滤饼洗涤两次,并将洗涤液和滤液混合,分开水相和有机相,水相用乙酸乙酯萃取两次,萃取液与有机相混合,将有机相减压浓缩后,加入600g水并充分搅拌后过滤,滤饼用120g水洗涤两次,将洗涤后的滤饼真空干燥得DHEA粗产品。将DHEA粗产品转入至干净的容器中,加入250g丙酮溶解后再加200g水,重复上述操作进行重结晶,得到77.53g DHEA最终产物,本实施例中,DHEA的收率为77.53%。(2) 500 mL of ethyl acetate was added to the reaction solution of the 5-AD, and the mixture was stirred uniformly, and 400 mL of a 2.0 g/L KRED5 and GDH crude enzyme solution, 300 mL of 100 mmol/L sodium phosphate buffer (pH 7.0) was added. 100 g of glucose, 180 mg of NADH, stirred at 25 ° C until completely dissolved, adding a reaction solution containing 5-AD, controlling pH to 6.2, temperature 26 ° C, stirring at 220 rpm for 2 h to obtain an enzyme reaction solution; adding the enzyme reaction solution to After stirring and filtering in celite, the cake was collected, and the filter cake was washed twice with ethyl acetate, and the washing liquid and the filtrate were mixed, the aqueous phase and the organic phase were separated, and the aqueous phase was extracted twice with ethyl acetate. After mixing with the organic phase, the organic phase was concentrated under reduced pressure, 600 g of water was added, and the mixture was thoroughly stirred and filtered. The filter cake was washed twice with 120 g of water, and the washed cake was vacuum dried to obtain a crude DHEA product. The crude DHEA product was transferred to a clean container, and after adding 250 g of acetone to dissolve, 200 g of water was added, and the above operation was repeated to carry out recrystallization to obtain 77.53 g of DHEA final product. In the present example, the yield of DHEA was 77.53%.
以上所述实施例仅表达了本发明的几种实施方式,其描述较为具体和详细,但并不能因此而理解为对本发明专利范围的限制。应当指出的是,对于本领域的普通技术人员来说,在不脱离本发明构思的前提下,还可以做出若干变形和改进,这些都属于本发明的保护范围。因此,本发明专利的保护范围应以所附权利要求为准。The above-mentioned embodiments are merely illustrative of several embodiments of the present invention, and the description thereof is more specific and detailed, but is not to be construed as limiting the scope of the invention. It should be noted that a number of variations and modifications may be made by those skilled in the art without departing from the spirit and scope of the invention. Therefore, the scope of the invention should be determined by the appended claims.

Claims (14)

  1. 一种去氢表雄酮的制备方法,其中,包括:A method for preparing dehydroepiandrosterone, which comprises:
    (1)在保护气氛下,向叔丁醇中加入叔丁醇钾,搅拌均匀后加入4-雄烯二酮得到混合料,将所述混合料滴加至含有抗坏血酸钠的乙酸溶液中反应得到5-雄烯二酮;(1) Adding potassium t-butoxide to t-butanol under a protective atmosphere, stirring uniformly, adding 4-androstenedione to obtain a mixture, and adding the mixture to an acetic acid solution containing sodium ascorbate to obtain a mixture 5-androstenedione;
    (2)将步骤(1)中所述5-雄烯二酮溶于有机溶剂中,并添加酮还原酶、葡萄糖脱氢酶、葡萄糖和氧化还原辅酶得到混合液,控制所述混合液的pH为6.0-6.3,于22-26℃下搅拌反应1-6小时,得到反应液,将所述反应液分离提纯后得到去氢表雄酮,所述酮还原酶和所述葡萄糖脱氢酶由微生物菌株共表达产生并以粗酶液形式添加,所述酮还原酶的来源于领地伯克霍尔德菌属、红球菌属和鞘氨醇单胞菌属中的一种或多种。(2) dissolving the 5-androstenedione in the step (1) in an organic solvent, adding a ketoreductase, glucose dehydrogenase, glucose, and redox coenzyme to obtain a mixture, and controlling the pH of the mixture. For 6.0-6.3, the reaction is stirred at 22-26 ° C for 1-6 hours to obtain a reaction solution, and the reaction solution is separated and purified to obtain dehydroepiandrosterone, and the ketoreductase and the glucose dehydrogenase are The microbial strain is co-expressed and added as a crude enzyme solution derived from one or more of the genus Burkholderia, Rhodococcus and Sphingomonas.
  2. 如权利要求1所述的去氢表雄酮的制备方法,其中,所述步骤(1)中,所述混合料的具体制备过程包括:在室温下向叔丁醇中加入叔丁醇钾,然后升温至55-65℃,搅拌0.3-0.8小时至所述叔丁醇钾完全溶解后,将温度维持在25-30℃下,加入4-雄烯二酮搅拌0.3-0.8小时后,冷却得到所述混合料。The method for preparing dehydroepiandrosterone according to claim 1, wherein in the step (1), the specific preparation process of the mixture comprises: adding potassium t-butoxide to t-butanol at room temperature, Then, the temperature is raised to 55-65 ° C, stirred for 0.3-0.8 hours until the potassium t-butoxide is completely dissolved, the temperature is maintained at 25-30 ° C, 4-androstenedione is added for stirring for 0.3-0.8 hours, and then cooled. The mixture.
  3. 如权利要求1所述的去氢表雄酮的制备方法,其中,所述步骤(1)中,所述将所述混合料滴加至含有抗坏血酸钠的乙酸溶液中反应得到5-雄烯二酮的过程中,反应温度为25-30℃,反应时间为0.3-0.8小时。The method for preparing dehydroepiandrosterone according to claim 1, wherein in the step (1), the mixture is added dropwise to an acetic acid solution containing sodium ascorbate to obtain 5-androstene. In the course of the ketone, the reaction temperature is 25-30 ° C and the reaction time is 0.3-0.8 hours.
  4. 如权利要求1所述的去氢表雄酮的制备方法,其中,所述步骤(2)中,所述微生物菌株包括Rosetta大肠杆菌和BL21大肠杆菌中的一种或两种。The method for producing dehydroepiandrosterone according to claim 1, wherein in the step (2), the microorganism strain comprises one or both of Rosetta E. coli and BL21 E. coli.
  5. 如权利要求1所述的去氢表雄酮的制备方法,其中,所述步骤(2)中,所述微生物菌株共表达产生所述酮还原酶和所述葡萄糖脱氢酶的具体过程包括:构建一重组表达质粒,将所述重组表达质粒转染至所述微生物菌株内后,在微生物培养液中诱导含有所述重组表达质粒的微生物菌株表达所述酮还原酶和所述葡萄糖脱氢酶,其中所述重组表达质粒包括所述酮还原酶和所述葡萄糖脱氢酶的基因编码序列。The method for producing dehydroepiandrosterone according to claim 1, wherein in the step (2), the specific process of co-expressing the microbial strain to produce the ketoreductase and the glucose dehydrogenase comprises: Constructing a recombinant expression plasmid, transfecting the recombinant expression plasmid into the microbial strain, and inducing the microbial strain containing the recombinant expression plasmid to express the ketoreductase and the glucose dehydrogenase in a microbial culture solution Wherein the recombinant expression plasmid comprises the ketoreductase and the gene coding sequence of the glucose dehydrogenase.
  6. 如权利要求1或5所述的去氢表雄酮的制备方法,其中,所述酮还原酶的基因编码序列包括如SEQ ID NO:1、SEQ ID NO:2和SEQ ID NO:3所示的核苷酸序列中的任意一种;所述葡萄糖脱氢酶的基因编码序列包括如SEQ ID NO:4所示的核苷酸序列。The method for producing dehydroepiandrosterone according to claim 1 or 5, wherein the gene coding sequence of the ketoreductase comprises as shown in SEQ ID NO: 1, SEQ ID NO: 2, and SEQ ID NO: 3. Any one of the nucleotide sequences; the gene coding sequence of the glucose dehydrogenase comprises the nucleotide sequence set forth in SEQ ID NO: 4.
  7. 如权利要求1所述的去氢表雄酮的制备方法,其中,所述步骤(2)中,所述氧化还原辅酶包括NAD +、NADP +、NADH和NADPH中的一种或多种。 The method for producing dehydroepiandrosterone according to claim 1, wherein in the step (2), the redox coenzyme comprises one or more of NAD + , NADP + , NADH and NADPH.
  8. 一种酮还原酶,其中,所述酮还原酶包括酮还原酶KRED3、酮还原酶KRED4和酮还 原酶KRED5中的一种或多种,所述酮还原酶KRED3的基因编码序列包括如SEQ ID NO:1所示的核苷酸序列,所述酮还原酶KRED4的基因编码序列包括如SEQ ID NO:2所示的核苷酸序列,所述酮还原酶KRED5的基因编码序列包括如SEQ ID NO:3所示的核苷酸序列。A ketoreductase, wherein the ketoreductase comprises one or more of a ketoreductase KRED3, a ketoreductase KRED4 and a ketoreductase KRED5, and the gene coding sequence of the ketoreductase KRED3 comprises as SEQ ID a nucleotide sequence represented by NO: 1, the gene coding sequence of the ketoreductase KRED4 includes the nucleotide sequence shown in SEQ ID NO: 2, and the gene coding sequence of the ketoreductase KRED5 includes SEQ ID NO: NO: The nucleotide sequence shown by 3.
  9. 一种酮还原酶在催化酮或醛转化为手性醇中的应用,其中,所述酮还原酶的基因编码序列包括如SEQ ID NO:1、SEQ ID NO:2和SEQ ID NO:3所示的核苷酸序列中的任意一种。A ketoreductase for use in catalyzing the conversion of a ketone or an aldehyde to a chiral alcohol, wherein the gene coding sequence of the ketoreductase comprises as set forth in SEQ ID NO: 1, SEQ ID NO: 2, and SEQ ID NO: Any of the nucleotide sequences shown.
  10. 如权利要求9所述的应用,其中,所述催化酮或醛转化为手性醇中的应用包括催化5-雄烯二酮转化为去氢表雄酮中的应用。The use according to claim 9, wherein the conversion of the catalytic ketone or aldehyde to a chiral alcohol comprises the use of catalyzing the conversion of 5-androstenedione to dehydroepiandrosterone.
  11. 一种重组质粒,其中,所述重组质粒包括酮还原酶的基因编码序列,所述酮还原酶的基因编码序列包括酮还原酶KRED3的基因编码序列、酮还原酶KRED4的基因编码序列和酮还原酶KRED5的基因编码序列中的一种或多种,所述酮还原酶KRED3的基因编码序列包括如SEQ ID NO:1所示的核苷酸序列,所述酮还原酶KRED4的基因编码序列包括如SEQ ID NO:2所示的核苷酸序列,所述酮还原酶KRED5的基因编码序列包括如SEQ ID NO:3所示的核苷酸序列。A recombinant plasmid, wherein the recombinant plasmid comprises a gene coding sequence of a ketoreductase, and the gene coding sequence of the ketoreductase comprises a gene coding sequence of a ketoreductase KRED3, a gene coding sequence of a ketoreductase KRED4, and a ketone reduction One or more of the gene coding sequences of the enzyme KRED5, the gene coding sequence of the ketoreductase KRED3 includes the nucleotide sequence shown in SEQ ID NO: 1, and the gene coding sequence of the ketoreductase KRED4 includes As the nucleotide sequence shown in SEQ ID NO: 2, the gene coding sequence of the ketoreductase KRED5 includes the nucleotide sequence shown in SEQ ID NO: 3.
  12. 如权利要求11所述的重组质粒,其中,所述重组质粒还包括葡萄糖脱氢酶的基因编码序列,所述葡萄糖脱氢酶的基因编码序列与所酮还原酶的基因编码序列之间还插入有RBS序列,所述葡萄糖脱氢酶的基因编码序列包括如SEQ ID NO:4所示的核苷酸序列,所述RBS序列包括如SEQ ID NO:17所示的核苷酸序列。The recombinant plasmid according to claim 11, wherein the recombinant plasmid further comprises a gene coding sequence of glucose dehydrogenase, and a gene coding sequence of the glucose dehydrogenase and a gene coding sequence of the ketoreductase are further inserted. There is an RBS sequence, the gene coding sequence of the glucose dehydrogenase comprises a nucleotide sequence as shown in SEQ ID NO: 4, and the RBS sequence comprises the nucleotide sequence shown in SEQ ID NO: 17.
  13. 一种重组质粒的制备方法,其中,包括:A method for preparing a recombinant plasmid, comprising:
    (1)提供或制备包含酮还原酶和葡萄糖脱氢酶的基因模板;(1) providing or preparing a gene template comprising a ketoreductase and a glucose dehydrogenase;
    (2)制备所述酮还原酶和所述葡萄糖脱氢酶的基因的上游引物和下游引物,扩增所述酮还原酶和所述葡萄糖脱氢酶的基因片段,所述酮还原酶的基因编码序列包括如SEQ ID NO:1、SEQ ID NO:2和SEQ ID NO:3所示的核苷酸序列中的任意一种,所述葡萄糖脱氢酶的基因编码序列包括如SEQ ID NO:4所示的核苷酸序列;(2) preparing an upstream primer and a downstream primer of the ketoreductase and the gene of the glucose dehydrogenase, and amplifying the ketoreductase and the gene fragment of the glucose dehydrogenase, the gene of the ketoreductase The coding sequence includes any one of the nucleotide sequences set forth in SEQ ID NO: 1, SEQ ID NO: 2, and SEQ ID NO: 3, and the genetic coding sequence of the glucose dehydrogenase includes SEQ ID NO: a nucleotide sequence as shown in 4;
    (3)取pET22b(+)载体质粒,将步骤(2)扩增得到的所述酮还原酶和所述葡萄糖脱氢酶基因片段插入至所述pET22b(+)载体质粒,纯化回收后进行连接,得到所述重组质粒。(3) taking the pET22b(+) vector plasmid, inserting the ketoreductase and the glucose dehydrogenase gene fragment amplified by the step (2) into the pET22b(+) vector plasmid, and purifying and recycling The recombinant plasmid was obtained.
  14. 如权利要求13所述的重组质粒的制备方法,其中,所述步骤(3)中,在所述酮还原酶和所述葡萄糖脱氢酶基因编码序列之间插入RBS序列,所述RBS序列包括如SEQ ID NO:17所示的核苷酸序列。The method for producing a recombinant plasmid according to claim 13, wherein in the step (3), an RBS sequence is inserted between the ketoreductase and the glucose dehydrogenase gene coding sequence, and the RBS sequence includes A nucleotide sequence as shown in SEQ ID NO: 17.
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