CN109971817B - Preparation of Boldenone by Sequential Transformation of Arthrobacter simplex and Genetically Engineered Yeast Strains - Google Patents
Preparation of Boldenone by Sequential Transformation of Arthrobacter simplex and Genetically Engineered Yeast Strains Download PDFInfo
- Publication number
- CN109971817B CN109971817B CN201910264964.XA CN201910264964A CN109971817B CN 109971817 B CN109971817 B CN 109971817B CN 201910264964 A CN201910264964 A CN 201910264964A CN 109971817 B CN109971817 B CN 109971817B
- Authority
- CN
- China
- Prior art keywords
- genetically engineered
- pichia pastoris
- boldenone
- arthrobacter simplex
- fermentation
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- RSIHSRDYCUFFLA-DYKIIFRCSA-N boldenone Chemical compound O=C1C=C[C@]2(C)[C@H]3CC[C@](C)([C@H](CC4)O)[C@@H]4[C@@H]3CCC2=C1 RSIHSRDYCUFFLA-DYKIIFRCSA-N 0.000 title claims abstract description 52
- 229950007271 boldenone Drugs 0.000 title claims abstract description 52
- RSIHSRDYCUFFLA-UHFFFAOYSA-N dehydrotestosterone Natural products O=C1C=CC2(C)C3CCC(C)(C(CC4)O)C4C3CCC2=C1 RSIHSRDYCUFFLA-UHFFFAOYSA-N 0.000 title claims abstract description 52
- 241000203720 Pimelobacter simplex Species 0.000 title claims abstract description 32
- 230000009466 transformation Effects 0.000 title claims description 22
- 240000004808 Saccharomyces cerevisiae Species 0.000 title abstract description 7
- 238000002360 preparation method Methods 0.000 title description 5
- 241000235058 Komagataella pastoris Species 0.000 claims abstract description 42
- 238000006243 chemical reaction Methods 0.000 claims abstract description 33
- 238000000855 fermentation Methods 0.000 claims abstract description 33
- 230000004151 fermentation Effects 0.000 claims abstract description 32
- 238000000034 method Methods 0.000 claims abstract description 25
- 150000001875 compounds Chemical class 0.000 claims abstract description 24
- 241000235648 Pichia Species 0.000 claims abstract description 19
- 108010031132 Alcohol Oxidoreductases Proteins 0.000 claims abstract description 12
- 102000005751 Alcohol Oxidoreductases Human genes 0.000 claims abstract description 10
- 244000005700 microbiome Species 0.000 claims abstract description 5
- 230000001131 transforming effect Effects 0.000 claims abstract description 5
- BTTWKVFKBPAFDK-UHFFFAOYSA-N (9beta,10alpha)-Androst-4-ene-3,17-dione Natural products OC1CCC2(C)C3CCC(C)(C(CC4)O)C4C3CCC2=C1 BTTWKVFKBPAFDK-UHFFFAOYSA-N 0.000 claims description 30
- AEMFNILZOJDQLW-QAGGRKNESA-N androst-4-ene-3,17-dione Chemical compound O=C1CC[C@]2(C)[C@H]3CC[C@](C)(C(CC4)=O)[C@@H]4[C@@H]3CCC2=C1 AEMFNILZOJDQLW-QAGGRKNESA-N 0.000 claims description 30
- AEMFNILZOJDQLW-UHFFFAOYSA-N androstenedione Natural products O=C1CCC2(C)C3CCC(C)(C(CC4)=O)C4C3CCC2=C1 AEMFNILZOJDQLW-UHFFFAOYSA-N 0.000 claims description 30
- 239000000758 substrate Substances 0.000 claims description 28
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 claims description 11
- 239000008103 glucose Substances 0.000 claims description 11
- 108090000623 proteins and genes Proteins 0.000 claims description 10
- ODLHGICHYURWBS-LKONHMLTSA-N trappsol cyclo Chemical compound CC(O)COC[C@H]([C@H]([C@@H]([C@H]1O)O)O[C@H]2O[C@@H]([C@@H](O[C@H]3O[C@H](COCC(C)O)[C@H]([C@@H]([C@H]3O)O)O[C@H]3O[C@H](COCC(C)O)[C@H]([C@@H]([C@H]3O)O)O[C@H]3O[C@H](COCC(C)O)[C@H]([C@@H]([C@H]3O)O)O[C@H]3O[C@H](COCC(C)O)[C@H]([C@@H]([C@H]3O)O)O3)[C@H](O)[C@H]2O)COCC(O)C)O[C@@H]1O[C@H]1[C@H](O)[C@@H](O)[C@@H]3O[C@@H]1COCC(C)O ODLHGICHYURWBS-LKONHMLTSA-N 0.000 claims description 10
- 230000036983 biotransformation Effects 0.000 claims description 8
- 238000006356 dehydrogenation reaction Methods 0.000 claims description 6
- 101150102504 ayr1 gene Proteins 0.000 claims description 5
- 239000002028 Biomass Substances 0.000 claims description 4
- 239000013067 intermediate product Substances 0.000 claims description 4
- 239000006184 cosolvent Substances 0.000 claims description 3
- 238000010353 genetic engineering Methods 0.000 claims description 3
- OSVMTWJCGUFAOD-KZQROQTASA-N formestane Chemical compound O=C1CC[C@]2(C)[C@H]3CC[C@](C)(C(CC4)=O)[C@@H]4[C@@H]3CCC2=C1O OSVMTWJCGUFAOD-KZQROQTASA-N 0.000 claims 1
- 241000894006 Bacteria Species 0.000 abstract description 10
- 238000004519 manufacturing process Methods 0.000 abstract description 9
- 230000003637 steroidlike Effects 0.000 abstract description 4
- 229940079593 drug Drugs 0.000 abstract description 2
- 239000003814 drug Substances 0.000 abstract description 2
- 210000004027 cell Anatomy 0.000 description 23
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 description 15
- 239000000047 product Substances 0.000 description 11
- 230000000694 effects Effects 0.000 description 10
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 9
- 239000002609 medium Substances 0.000 description 7
- 230000008569 process Effects 0.000 description 7
- 239000007853 buffer solution Substances 0.000 description 6
- 125000002915 carbonyl group Chemical group [*:2]C([*:1])=O 0.000 description 6
- 230000002779 inactivation Effects 0.000 description 6
- 230000000813 microbial effect Effects 0.000 description 6
- 230000009467 reduction Effects 0.000 description 6
- 238000003786 synthesis reaction Methods 0.000 description 6
- 235000014680 Saccharomyces cerevisiae Nutrition 0.000 description 5
- 230000001580 bacterial effect Effects 0.000 description 5
- 230000015572 biosynthetic process Effects 0.000 description 5
- 230000003197 catalytic effect Effects 0.000 description 5
- 238000004128 high performance liquid chromatography Methods 0.000 description 5
- 239000013612 plasmid Substances 0.000 description 5
- 241001506991 Komagataella phaffii GS115 Species 0.000 description 4
- MUMGGOZAMZWBJJ-DYKIIFRCSA-N Testostosterone Chemical compound O=C1CC[C@]2(C)[C@H]3CC[C@](C)([C@H](CC4)O)[C@@H]4[C@@H]3CCC2=C1 MUMGGOZAMZWBJJ-DYKIIFRCSA-N 0.000 description 4
- 229940041514 candida albicans extract Drugs 0.000 description 4
- 239000007788 liquid Substances 0.000 description 4
- 239000006228 supernatant Substances 0.000 description 4
- 239000012138 yeast extract Substances 0.000 description 4
- 241000186063 Arthrobacter Species 0.000 description 3
- FBPFZTCFMRRESA-FSIIMWSLSA-N D-Glucitol Natural products OC[C@H](O)[C@H](O)[C@@H](O)[C@H](O)CO FBPFZTCFMRRESA-FSIIMWSLSA-N 0.000 description 3
- 101100437170 Schizosaccharomyces pombe (strain 972 / ATCC 24843) ayr1 gene Proteins 0.000 description 3
- 239000000872 buffer Substances 0.000 description 3
- 239000003550 marker Substances 0.000 description 3
- 210000001087 myotubule Anatomy 0.000 description 3
- 238000003259 recombinant expression Methods 0.000 description 3
- 238000011160 research Methods 0.000 description 3
- 239000000600 sorbitol Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 239000012137 tryptone Substances 0.000 description 3
- 238000012795 verification Methods 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- YBJHBAHKTGYVGT-ZKWXMUAHSA-N (+)-Biotin Chemical compound N1C(=O)N[C@@H]2[C@H](CCCCC(=O)O)SC[C@@H]21 YBJHBAHKTGYVGT-ZKWXMUAHSA-N 0.000 description 2
- 229920001817 Agar Polymers 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 description 2
- 101710088194 Dehydrogenase Proteins 0.000 description 2
- 239000001888 Peptone Substances 0.000 description 2
- 108010080698 Peptones Proteins 0.000 description 2
- 240000008042 Zea mays Species 0.000 description 2
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 description 2
- 235000002017 Zea mays subsp mays Nutrition 0.000 description 2
- 239000008272 agar Substances 0.000 description 2
- 238000005119 centrifugation Methods 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 235000005822 corn Nutrition 0.000 description 2
- 238000001976 enzyme digestion Methods 0.000 description 2
- 239000013604 expression vector Substances 0.000 description 2
- 230000014509 gene expression Effects 0.000 description 2
- 230000006698 induction Effects 0.000 description 2
- 238000009776 industrial production Methods 0.000 description 2
- 229910000402 monopotassium phosphate Inorganic materials 0.000 description 2
- 235000019796 monopotassium phosphate Nutrition 0.000 description 2
- 235000019319 peptone Nutrition 0.000 description 2
- PJNZPQUBCPKICU-UHFFFAOYSA-N phosphoric acid;potassium Chemical compound [K].OP(O)(O)=O PJNZPQUBCPKICU-UHFFFAOYSA-N 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 102000004169 proteins and genes Human genes 0.000 description 2
- 238000012163 sequencing technique Methods 0.000 description 2
- 150000003431 steroids Chemical class 0.000 description 2
- 229960003604 testosterone Drugs 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- LWIHDJKSTIGBAC-UHFFFAOYSA-K tripotassium phosphate Chemical compound [K+].[K+].[K+].[O-]P([O-])([O-])=O LWIHDJKSTIGBAC-UHFFFAOYSA-K 0.000 description 2
- YLZOPXRUQYQQID-UHFFFAOYSA-N 3-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)-1-[4-[2-[[3-(trifluoromethoxy)phenyl]methylamino]pyrimidin-5-yl]piperazin-1-yl]propan-1-one Chemical compound N1N=NC=2CN(CCC=21)CCC(=O)N1CCN(CC1)C=1C=NC(=NC=1)NCC1=CC(=CC=C1)OC(F)(F)F YLZOPXRUQYQQID-UHFFFAOYSA-N 0.000 description 1
- DEXFNLNNUZKHNO-UHFFFAOYSA-N 6-[3-[4-[2-(2,3-dihydro-1H-inden-2-ylamino)pyrimidin-5-yl]piperidin-1-yl]-3-oxopropyl]-3H-1,3-benzoxazol-2-one Chemical compound C1C(CC2=CC=CC=C12)NC1=NC=C(C=N1)C1CCN(CC1)C(CCC1=CC2=C(NC(O2)=O)C=C1)=O DEXFNLNNUZKHNO-UHFFFAOYSA-N 0.000 description 1
- FRXSZNDVFUDTIR-UHFFFAOYSA-N 6-methoxy-1,2,3,4-tetrahydroquinoline Chemical compound N1CCCC2=CC(OC)=CC=C21 FRXSZNDVFUDTIR-UHFFFAOYSA-N 0.000 description 1
- 241000192652 Desmonostoc muscorum Species 0.000 description 1
- 241000588724 Escherichia coli Species 0.000 description 1
- 241000235526 Mucor racemosus Species 0.000 description 1
- 102000004316 Oxidoreductases Human genes 0.000 description 1
- 108090000854 Oxidoreductases Proteins 0.000 description 1
- 238000010222 PCR analysis Methods 0.000 description 1
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 1
- 244000302274 Saccharomyces cerevisiae W303 Species 0.000 description 1
- 235000011859 Saccharomyces cerevisiae W303 Nutrition 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- LUJVUUWNAPIQQI-QAGGRKNESA-N androsta-1,4-diene-3,17-dione Chemical compound O=C1C=C[C@]2(C)[C@H]3CC[C@](C)(C(CC4)=O)[C@@H]4[C@@H]3CCC2=C1 LUJVUUWNAPIQQI-QAGGRKNESA-N 0.000 description 1
- 230000010310 bacterial transformation Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000001851 biosynthetic effect Effects 0.000 description 1
- 230000006696 biosynthetic metabolic pathway Effects 0.000 description 1
- 229960002685 biotin Drugs 0.000 description 1
- 235000020958 biotin Nutrition 0.000 description 1
- 239000011616 biotin Substances 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 239000005515 coenzyme Substances 0.000 description 1
- 238000012258 culturing Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 230000029087 digestion Effects 0.000 description 1
- 238000004520 electroporation Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000012869 ethanol precipitation Methods 0.000 description 1
- 239000013613 expression plasmid Substances 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 239000012634 fragment Substances 0.000 description 1
- 239000012737 fresh medium Substances 0.000 description 1
- 230000002538 fungal effect Effects 0.000 description 1
- 229940088597 hormone Drugs 0.000 description 1
- 239000005556 hormone Substances 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 238000005805 hydroxylation reaction Methods 0.000 description 1
- 239000002054 inoculum Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 210000003205 muscle Anatomy 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 230000002018 overexpression Effects 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 229910000160 potassium phosphate Inorganic materials 0.000 description 1
- 235000011009 potassium phosphates Nutrition 0.000 description 1
- 239000002243 precursor Substances 0.000 description 1
- 238000001243 protein synthesis Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000005070 sampling Methods 0.000 description 1
- 238000012216 screening Methods 0.000 description 1
- 238000011218 seed culture Methods 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 239000008223 sterile water Substances 0.000 description 1
- 238000012414 sterilization procedure Methods 0.000 description 1
- 238000005728 strengthening Methods 0.000 description 1
- 150000003515 testosterones Chemical class 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 230000014616 translation Effects 0.000 description 1
- 238000002137 ultrasound extraction Methods 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
- 239000013598 vector Substances 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
- C12N9/00—Enzymes; Proenzymes; Compositions thereof; Processes for preparing, activating, inhibiting, separating or purifying enzymes
- C12N9/0004—Oxidoreductases (1.)
- C12N9/0006—Oxidoreductases (1.) acting on CH-OH groups as donors (1.1)
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
- C12P33/00—Preparation of steroids
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12Y—ENZYMES
- C12Y101/00—Oxidoreductases acting on the CH-OH group of donors (1.1)
- C12Y101/01—Oxidoreductases acting on the CH-OH group of donors (1.1) with NAD+ or NADP+ as acceptor (1.1.1)
- C12Y101/01184—Carbonyl reductase (NADPH) (1.1.1.184)
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Health & Medical Sciences (AREA)
- Engineering & Computer Science (AREA)
- Zoology (AREA)
- Wood Science & Technology (AREA)
- Genetics & Genomics (AREA)
- Bioinformatics & Cheminformatics (AREA)
- General Health & Medical Sciences (AREA)
- Biochemistry (AREA)
- General Engineering & Computer Science (AREA)
- Microbiology (AREA)
- Biotechnology (AREA)
- Biomedical Technology (AREA)
- Molecular Biology (AREA)
- Medicinal Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Micro-Organisms Or Cultivation Processes Thereof (AREA)
- Preparation Of Compounds By Using Micro-Organisms (AREA)
Abstract
本发明涉及一种甾体类药物的生产方法,具体涉及利用简单节杆菌与基因工程酵母菌株顺序发酵制备宝丹酮甾体化合物的方法。本发明首先提供一株能高效表达17β羰基还原酶的毕赤酵母基因工程菌株,其次利用上述毕赤酵母基因工程菌,提供一种微生物顺序转化发酵化合物AD制备化合物BD的方法,该方法是将AD先经简单节杆菌发酵后,将反应体系灭活,再经毕赤酵母基因工程菌株顺序发酵制备化合物宝丹酮。The invention relates to a production method of steroidal drugs, in particular to a method for sequentially fermenting and preparing boldenone steroidal compounds using Arthrobacter simplex and genetically engineered yeast strains. The present invention firstly provides a Pichia genetically engineered strain capable of efficiently expressing 17β carbonyl reductase, and secondly utilizes the above-mentioned Pichia genetically engineered bacteria to provide a method for sequentially transforming fermentation compound AD to prepare compound BD by microorganisms. After AD is first fermented by Arthrobacter simplex, the reaction system is inactivated, and then the compound Boldenone is prepared by sequential fermentation with Pichia pastoris genetically engineered strains.
Description
技术领域:Technical field:
本发明涉及一种甾体类药物的生产方法,具体涉及利用简单节杆菌与基因工程酵母菌株顺序发酵制备宝丹酮甾体化合物的方法。The invention relates to a production method of steroidal drugs, in particular to a method for sequentially fermenting and preparing boldenone steroidal compounds using Arthrobacter simplex and genetically engineered yeast strains.
背景技术:Background technique:
宝丹酮(BD)又名勃地酮,是一种白色或类白色结晶性粉末,其分子式为C19H26O2。宝丹酮是睾酮的衍生物,因此继承了睾酮的大部分性质,具有雄性激素能力和蛋白质合成能力。宝丹酮能使肌纤维细胞的氮平衡状态随时保持趋于正向,使肌纤维细胞加速合成蛋白质,肌纤维细胞因此而扩张膨胀,对体能锻炼者增强肌肉和耐力有很大功效。长期以来,宝丹酮的原料生产企业在国内并不多,且多为化学法合成。化学法因其生产步骤繁琐、涉及有毒有害试剂的使用、高污染等问题,不利于工业大规模生产。因此,如何通过生物合成途径来替代化学合成方法,并建立高效的生物合成策略,是目前亟待解决的关键性问题。Boldenone (BD), also known as Boldenone, is a white or off-white crystalline powder with a molecular formula of C 19 H 26 O 2 . Boldenone is a derivative of testosterone, so it inherits most of the properties of testosterone, and has male hormone ability and protein synthesis ability. Boldenone can keep the nitrogen balance of muscle fiber cells positive at any time, accelerate the synthesis of protein in muscle fiber cells, and expand the muscle fiber cells, which has a great effect on strengthening muscles and endurance of physical exercisers. For a long time, there are not many raw material manufacturers of Boldenone in China, and most of them are synthesized by chemical methods. The chemical method is not conducive to large-scale industrial production because of its cumbersome production steps, the use of toxic and harmful reagents, and high pollution. Therefore, how to replace chemical synthesis methods with biosynthetic pathways and establish efficient biosynthetic strategies are key issues to be solved urgently.
近年来,研究者在通过微生物转化法合成宝丹酮的相关研究多集中于利用单一菌株进行催化,且其催化过程依然存在底物投料浓度低、转化效率不足等问题。虽然Mucorracemosus,Nostocmuscorum,Arihrobacteroxydans等微生物,都能够以雄甾-1,4-二烯-3,17-二酮(ADD)为底物,通过17β羰基还原作用生产BD,但是它们中很少有微生物能够直接以价格相对低廉的雄甾-4-烯-3,17-二酮(AD)为底物合成BD。AD是合成ADD的前体物质,AD经3-甾酮-△1-脱氢酶(KsdD)的C1,2位脱氢作用可以合成ADD,ADD再经17β羰基还原作用生成目的产物BD。虽然已有研究将真菌来源的KsdD蛋白于毕赤酵母中外源表达可以获得产物BD,但由于毕赤酵母自身的17β羰基还原作用不够强,因此其底物投料量及BD产量并不高。In recent years, most of the researchers' research on the synthesis of boldenone by microbial transformation has focused on the use of a single bacterial strain for catalysis, and the catalytic process still has problems such as low substrate concentration and insufficient conversion efficiency. Although Mucorracemosus, Nostocmuscorum, Arihrobacteroxydans and other microorganisms can use androst-1,4-diene-3,17-dione (ADD) as a substrate to produce BD through 17β carbonyl reduction, few of them BD can be synthesized directly using relatively cheap androst-4-ene-3,17-dione (AD) as a substrate. AD is the precursor substance for the synthesis of ADD. AD can be synthesized by the dehydrogenation of C1 and 2 positions of 3-sterone-△1-dehydrogenase (KsdD), and ADD can be converted into the target product BD by 17β carbonyl reduction. Although exogenous expression of fungal-derived KsdD protein in Pichia pastoris has been studied to obtain the product BD, but the 17β carbonyl reduction effect of Pichia pastoris itself is not strong enough, so its substrate dosage and BD production are not high.
目前为止,还未发现有微生物同时具有较强的C1,2位脱氢作用及较强的17β羰基还原作用。简单节杆菌(Arthrobacter simplex)因为转化效率高、反应速率快等优点,已成为工业生产中广泛使用的甾体C1,2脱氢反应菌株;而酵母来源的17β羰基还原酶具有较强的17β羰基还原作用。目前,尚未有利用简单节杆菌和酵母菌株进行联合发酵生产BD的相关研究。So far, no microorganism has been found to have strong C1,2 dehydrogenation and strong 17β carbonyl reduction at the same time. Arthrobacter simplex has become a steroid C1,2 dehydrogenation reaction strain widely used in industrial production because of its high transformation efficiency and fast reaction rate; and the 17β carbonyl reductase derived from yeast has a strong 17β carbonyl Reduction. At present, there is no related research on the joint fermentation of BD produced by Arthrobacter simplex and yeast strains.
发明内容:Invention content:
为解决上述问题,节约成本并提高产品收率,本发明首先提供一株能高效表达17β羰基还原酶的毕赤酵母基因工程菌株,其次利用上述毕赤酵母基因工程菌,提供一种微生物顺序转化化合物AD制备化合物BD的方法,该方法是将AD先经简单节杆菌发酵后,将反应体系灭活,再经毕赤酵母基因工程菌株顺序发酵制备化合物宝丹酮。In order to solve the above problems, save costs and improve product yield, the present invention firstly provides a Pichia genetically engineered strain capable of efficiently expressing 17β carbonyl reductase, and secondly uses the above-mentioned Pichia genetically engineered bacteria to provide a microbial sequence transformation A method for preparing compound BD from compound AD, the method is to firstly ferment AD with Arthrobacter simplex, inactivate the reaction system, and then sequentially ferment the compound Boldenone through Pichia pastoris genetically engineered strains.
所述毕赤酵母基因工程菌株,是在毕赤酵母宿主细胞中过表达17β羰基还原酶编码基因所述的;The Pichia genetically engineered strain is described in the overexpression of the gene encoding 17β carbonyl reductase in the Pichia host cell;
优选地,所述毕赤酵母宿主细胞为毕赤酵母GS115;Preferably, the Pichia host cell is Pichia GS115;
优选地,所述17β羰基还原酶(GenBank编号为:KZV10489.1)编码基因为ayr1基因,Gene ID:854682;Preferably, the 17β carbonyl reductase (GenBank number: KZV10489.1) encoding gene is ayr1 gene, Gene ID: 854682;
优选地,所述毕赤酵母基因工程菌株为毕赤酵母(P.pastoris)GS115AYR1S.c,是通过在毕赤酵母GS115中通过质粒pPIC3.5K表达Gene ID:854682所示的ayr1基因所得;Preferably, the Pichia genetically engineered strain is Pichia pastoris (P.pastoris) GS115AYR1 Sc , obtained by expressing the ayr1 gene shown in Gene ID: 854682 in Pichia pastoris GS115 through plasmid pPIC3.5K;
所述微生物顺序转化发酵化合物AD制备化合物BD的方法具体如下:The method for the preparation of compound BD by the sequential conversion of the microorganisms from the fermented compound AD is as follows:
在含有底物AD浓度为3g/L-10g/L的生物转化体系中,投加生物量为4-6g/L(湿重)的具有C1,2脱氢能力的简单节杆菌,待中间产物ADD的量达到最高后,将反应体系灭活,再经25-200g/L(湿重)的毕赤酵母基因工程菌株(Pichia pastoris)GS115AYR1S.c顺序发酵制备化合物宝丹酮;In the biotransformation system containing the substrate AD concentration of 3g/L-10g/L, add Arthrobacter simplex with C1,2 dehydrogenation ability with a biomass of 4-6g/L (wet weight), and the intermediate product After the amount of ADD reached the highest level, the reaction system was inactivated, and the compound Boldenone was prepared by sequential fermentation with 25-200g/L (wet weight) Pichia pastoris genetically engineered strain (Pichia pastoris) GS115AYR1 Sc ;
进一步地,所述生物转化体系为50mM PBS缓冲溶液(pH 7.2);Further, the biotransformation system is 50mM PBS buffer solution (pH 7.2);
进一步地,简单节杆菌的发酵时间为25-50h,发酵条件为:20-40℃,150-250r/min;Further, the fermentation time of Arthrobacter simplex is 25-50h, and the fermentation conditions are: 20-40°C, 150-250r/min;
进一步地,反应体系灭活条件为:121℃,20min;Further, the inactivation condition of the reaction system is: 121°C, 20min;
进一步地,添加毕赤酵母同时,在体系中加入终浓度0-100g/L的葡萄糖;Further, while adding Pichia pastoris, add glucose at a final concentration of 0-100g/L to the system;
优选地,葡萄糖浓度为75g/L;Preferably, the glucose concentration is 75g/L;
进一步地,毕赤酵母基因工程菌株的发酵时间为2-4h,发酵条件为:20-40℃,150-250r/min;Further, the fermentation time of the genetically engineered strain of Pichia pastoris is 2-4 hours, and the fermentation conditions are: 20-40°C, 150-250r/min;
优选地,所述简单节杆菌为简单节杆菌(Arthrobacter simplex)TCCC 11037;Preferably, the Arthrobacter simplex is Arthrobacter simplex TCCC 11037;
优选地,生物转化体系中采用羟丙基-β-环糊精(HP-β-CD)作为底物助溶剂,其与底物AD的摩尔比为0-2:1;Preferably, hydroxypropyl-β-cyclodextrin (HP-β-CD) is used as a substrate co-solvent in the biotransformation system, and its molar ratio to the substrate AD is 0-2:1;
优选地,HP-β-CD作为底物助溶剂,其与底物AD的摩尔比为1:1;Preferably, HP-β-CD is used as a substrate co-solvent, and its molar ratio to the substrate AD is 1:1;
上述反应结束后,发酵体系中的BD的产量可以达到1.68-7.7g/L,产率达到56%-83%。After the above reaction is completed, the yield of BD in the fermentation system can reach 1.68-7.7g/L, and the yield can reach 56%-83%.
有益效果:Beneficial effect:
(1)本发明首次实现了利用微生物联合发酵转化AD制备化合物BD的方法,并且使BD的最终产率达到83%,达到了提高化合物BD产率的目的,具有良好的应用价值和推广前景。(1) The present invention realizes for the first time the method for preparing compound BD by transforming AD with microbial co-fermentation, and makes the final yield of BD reach 83%, which achieves the purpose of improving the yield of compound BD, and has good application value and promotion prospect.
(2)本发明可以提高反应体系中的辅酶利用率,降低体系中的氧化作用,提高BD最终转化率。(2) The present invention can improve the coenzyme utilization rate in the reaction system, reduce the oxidation in the system, and improve the final conversion rate of BD.
(3)本发明所述的微生物联合发酵简单便捷,便于实现,效果显著。(3) The microbial joint fermentation described in the present invention is simple and convenient, easy to realize, and has remarkable effect.
附图说明:Description of drawings:
图1重组质粒pPIC3.5K-ayr1的PCR分析Figure 1 PCR analysis of recombinant plasmid pPIC3.5K-ayr1
其中,M:DL5000DNA Marker;1,2:pPIC3.5K-ayr1S.cPCR产物;Wherein, M: DL5000DNA Marker; 1, 2: pPIC3.5K-ayr1 Sc PCR product;
图2重组质粒pPIC3.5K-ayr1经BamHⅠ和EcoRⅠ的双酶切分析Figure 2 Analysis of recombinant plasmid pPIC3.5K-ayr1 by BamHI and EcoRI double enzyme digestion
其中M:1kbDNA Marker;1,2:pPIC3.5K-ayr1S.c双酶切产物;Among them, M: 1kbDNA Marker; 1, 2: pPIC3.5K-ayr1 Sc double digestion product;
图3含有重组表达载体pPIC3.5K-ayr1的P.pastoris GS115基因工程菌株的PCR验证Figure 3 PCR verification of the P. pastoris GS115 genetically engineered strain containing the recombinant expression vector pPIC3.5K-ayr1
其中,M:DL5000DNA Marker;1,2:pPIC3.5K-ayr1S.c重组P.pastoris GS115基因组PCR产物;Among them, M: DL5000 DNA Marker; 1, 2: pPIC3.5K-ayr1 Sc recombinant P. pastoris GS115 genome PCR product;
图4简单节杆菌和重组毕赤酵母双菌同时转化AD;Figure 4 Simultaneous transformation of AD by Arthrobacter simplex and recombinant Pichia pastoris;
图5重组毕赤酵母对AD及ADD的转化;Figure 5 Transformation of recombinant Pichia pastoris to AD and ADD;
图6失活简单节杆菌对BD生产的影响。Figure 6 Effect of inactivation of Arthrobacter simplex on BD production.
具体实施方式:Detailed ways:
下面将通过实施例对本发明做进一步描述,以下实施例只是描述性的,不是限定性的,不能以此限定本发明的保护范围。The following examples will further describe the present invention, the following examples are only descriptive, not limiting, and can not limit the protection scope of the present invention.
本发明的简单节杆菌(Arthrobacter simplex)TCCC 11037和毕赤酵母基因工程菌株(P.pastoris)GS115AYR1S.c通过常规的斜面培养、种子培养以发酵培养,得到生物转化用湿菌体,本发明以下实施例如未特别说明则所用湿菌体获得方法如下:Arthrobacter simplex (Arthrobacter simplex) TCCC 11037 of the present invention and Pichia pastoris genetically engineered bacterial strain (P.pastoris) GS115AYR1 Sc are cultivated by conventional slant culture, seed culture and fermentation culture, obtain the wet thallus for biotransformation, the present invention is implemented as follows For example, if there is no special description, the method for obtaining the wet bacteria used is as follows:
简单节杆菌(Arthrobacter simplex)TCCC 11037:Arthrobacter simplex TCCC 11037:
(1)斜面培养:(1) Incline cultivation:
斜面培养基:1%葡萄糖,1%酵母膏,2%琼脂,调pH至7.2;Incline medium: 1% glucose, 1% yeast extract, 2% agar, adjust the pH to 7.2;
培养条件:32℃,3-5天;Culture conditions: 32°C, 3-5 days;
(2)种子培养:(2) Seed cultivation:
种子培养基:1%葡萄糖,1%玉米浆(上清),0.5%蛋白胨,0.25%磷酸二氢钾,调pH至7.2;Seed medium: 1% glucose, 1% corn steep liquor (supernatant), 0.5% peptone, 0.25% potassium dihydrogen phosphate, adjust the pH to 7.2;
培养条件:32℃,160r/min,18小时;Culture conditions: 32°C, 160r/min, 18 hours;
(3)发酵培养:(3) Fermentation culture:
发酵培养基:1%葡萄糖,1%玉米浆(上清),0.5%蛋白胨,0.25%磷酸二氢钾,调pH至7.2的接种量将种子液接入发酵培养基中,32℃,200r/min,16小时时加入乙醇溶解的底物AD,使发酵液的底物终浓度为0.1%,诱导简单节杆菌细胞产生脱氢酶,继续培养8h后,发酵结束。Fermentation medium: 1% glucose, 1% corn steep liquor (supernatant), 0.5% peptone, 0.25% potassium dihydrogen phosphate, adjust the inoculum size to 7.2, insert the seed liquid into the fermentation medium, 32°C, 200r/ At 16 hours, add ethanol-dissolved substrate AD to make the final concentration of the substrate in the fermentation broth 0.1%, induce Arthrobacter simplex cells to produce dehydrogenase, continue culturing for 8 hours, and the fermentation ends.
发酵培养结束后,将发酵培养液于4℃,5000×g下离心10min,弃去上清液,用0.05mol/L的PBS缓冲液(pH 7.2)将离心得到的菌体洗涤2次,5000×g离心10min,收集细胞得湿菌体。After the fermentation culture was finished, the fermentation culture liquid was centrifuged at 4°C at 5000×g for 10 min, the supernatant was discarded, and the centrifuged bacterial cells were washed twice with 0.05 mol/L PBS buffer (pH 7.2), 5000 Centrifuge at × g for 10 min, and collect the cells to obtain wet cells.
毕赤酵母基因工程菌株(P.pastoris)GS115AYR1S.c:Pichia genetic engineering strain (P.pastoris) GS115AYR1 Sc :
(1)斜面培养:(1) Incline cultivation:
斜面培养基:1%酵母提取物,2%胰蛋白胨,2%葡萄糖,2%琼脂粉;Slant medium: 1% yeast extract, 2% tryptone, 2% glucose, 2% agar powder;
培养条件:30℃,3-5天;Culture conditions: 30°C, 3-5 days;
(2)种子培养:(2) Seed cultivation:
种子培养基:1%酵母提取物,2%胰蛋白胨,2%葡萄糖;Seed medium: 1% yeast extract, 2% tryptone, 2% glucose;
培养条件:30℃,200r/min,20小时;Culture conditions: 30°C, 200r/min, 20 hours;
(3)发酵培养(3) Fermentation culture
发酵培养基:1%酵母提取物,2%胰蛋白胨,100mmol/L磷酸钾(pH 6.0),1.34%YNB(过滤除菌),4×10-5生物素(过滤除菌),0.5%甲醇(过滤除菌);Fermentation medium: 1% yeast extract, 2% tryptone, 100mmol/L potassium phosphate (pH 6.0), 1.34% YNB (filter sterilized), 4×10 -5 biotin (filter sterilized), 0.5% methanol (sterilized by filtration);
培养条件:30℃,200r/min,培养4天,每24h补加0.5%甲醇,诱导毕赤酵母产生羰基还原酶。发酵培养完成后,将发酵培养液于4℃,6000r/min下离心10min,弃去上清液,用0.05mol/L的PBS缓冲液(pH 7.2)将离心得到的菌体洗涤2次,离心10min,收集细胞得湿菌体。Culture conditions: 30°C, 200r/min, culture for 4 days, add 0.5% methanol every 24h, induce Pichia pastoris to produce carbonyl reductase. After the fermentation culture was completed, the fermentation culture liquid was centrifuged at 4°C and 6000r/min for 10min, the supernatant was discarded, and the bacteria cells obtained by centrifugation were washed twice with 0.05mol/L PBS buffer (pH 7.2), centrifuged After 10 min, the cells were collected to obtain wet cells.
实验室前期研究表明,简单节杆菌中含有作用较强的17位羟基脱氢酶,会严重影响终产物BD的生成。因此,联合转化的技术难点和关键点就在于如何确定合适的催化顺序和催化方式,以获得产物BD的最大产率。相对于单独或同时使用上述两种菌株进行脱氢和羟化反应,本发明通过两菌株的顺序发酵制备甾体化合物BD,使产物的总收率大幅度提高,减少了能耗和生产周期,降低了生产成本和劳动力,符合科学生产的要求。Preliminary research in the laboratory has shown that Arthrobacter simplex contains a powerful 17-hydroxy dehydrogenase, which will seriously affect the production of the final product BD. Therefore, the technical difficulty and key point of combined conversion lies in how to determine the appropriate catalytic sequence and catalytic method to obtain the maximum yield of the product BD. Compared with the dehydrogenation and hydroxylation reactions using the above two strains alone or at the same time, the present invention prepares the steroid compound BD through the sequential fermentation of the two strains, which greatly increases the total yield of the product, reduces energy consumption and production cycle, The production cost and labor force are reduced, and the requirements of scientific production are met.
以下将通过具体实施方式对本发明做进一步的解释说明。The present invention will be further explained through specific embodiments below.
实施例1 17β羰基还原酶基因的获取以及毕赤酵母基因工程菌株的构建Example 1 Acquisition of 17β carbonyl reductase gene and construction of Pichia pastoris genetic engineering strain
(1)17β羰基还原酶基因ayr1的获取(1) Acquisition of 17β carbonyl reductase gene ayr1
以酿酒酵母W303基因组为模板,扩增17β羰基还原酶(GenBank编号为:KZV10489.1)编码基因ayr1(GeneID:854682),设计引物对如下所示,PCR产物用GelExtraction Kit(Omega,USA)回收,回收片段连接于载体pPIC3.5K上,构建重组质粒pPIC3.5K-ayr1,并转化E.coli JM109,获得含有目标基因的基因工程菌株。经菌液PCR验证及双酶切验证,表明重组质粒pPIC3.5K-ayr1构建成功(如图1及图2所示)。通过对上述克隆子进行测序,并与已获得的ayr1序列进行比对,测序结果与目标基因序列完全符合。Using the Saccharomyces cerevisiae W303 genome as a template, amplify the 17β carbonyl reductase (GenBank number: KZV10489.1) encoding gene ayr1 (GeneID: 854682), design the primer pair as follows, and recover the PCR product with GelExtraction Kit (Omega, USA) , the recovered fragment was connected to the vector pPIC3.5K, the recombinant plasmid pPIC3.5K-ayr1 was constructed, and transformed into E.coli JM109 to obtain a genetically engineered strain containing the target gene. The bacterial liquid PCR verification and double enzyme digestion verification showed that the recombinant plasmid pPIC3.5K-ayr1 was successfully constructed (as shown in Figure 1 and Figure 2). By sequencing the above clones and comparing them with the obtained ayr1 sequence, the sequencing results were completely consistent with the target gene sequence.
上游引物:CGCGGATCCATGTCGGAGTTACAGTCACAACCTAA;Upstream primer: CGCGGATCCATGTCGGAGTTACAGTCACAACCTAA;
下游引物:CCGGAATTCCTAATCGTCCTTATTCTTCTGTTTCG。Downstream primer: CCGGAATTCCTAATCGTCCTTATTTCTTCTGTTTCG.
(2)17β羰基还原酶毕赤酵母基因工程菌株的构建和筛选(2) Construction and screening of genetically engineered strains of 17β carbonyl reductase Pichia pastoris
(1)毕赤酵母感受态细胞的制备:(1) Preparation of Pichia Competent Cells:
①在含5mL YPD的50mL离心管中,培养毕赤酵母GS115,30℃过夜;① Cultivate Pichia pastoris GS115 in a 50mL centrifuge tube containing 5mL YPD overnight at 30°C;
②取0.1-0.5mL过夜培养物,接种含500mL新鲜培养基的2L摇瓶,过夜生长至OD600=1.3-1.5;②Take 0.1-0.5mL overnight culture, inoculate a 2L shake flask containing 500mL fresh medium, and grow overnight until OD600=1.3-1.5;
③在4℃,1500g离心5min收集细胞,用500mL预冷的灭菌水悬浮细胞;③Collect the cells by centrifugation at 1500g for 5min at 4°C, and suspend the cells with 500mL pre-cooled sterilized water;
④如上离心,用250mL预冷的灭菌水悬浮细胞;④ Centrifuge as above, suspend the cells with 250mL pre-cooled sterile water;
⑤如上离心,用20mL预冷的1mol/L山梨醇悬浮细胞;⑤ Centrifuge as above, and suspend the cells with 20 mL of pre-cooled 1mol/L sorbitol;
⑥如上离心,用1mL预冷的1mol/L山梨醇悬浮细胞,至终体积约1.5mL。⑥ Centrifuge as above, and suspend the cells with 1 mL of pre-cooled 1 mol/L sorbitol to a final volume of about 1.5 mL.
(2)电转化毕赤酵母感受态细胞:(2) Electrotransformation of Pichia pastoris competent cells:
将提取的重组表达质粒pPIC3.5K-ayr1经SacⅠ进行线性化后,通过酚:氯仿抽提及乙醇沉淀,提纯线性化产物。After the extracted recombinant expression plasmid pPIC3.5K-ayr1 was linearized by SacI, the linearized product was purified by phenol:chloroform extraction and ethanol precipitation.
①取80μL上述细胞与5-20μg线性化DNA混合,转入预冷的0.2cm电转杯中;① Mix 80 μL of the above cells with 5-20 μg of linearized DNA, and transfer to a pre-cooled 0.2 cm electroporation cuvette;
②在冰上放置5min;② Place on ice for 5 minutes;
③根据所使用装置推荐的酿酒酵母参数进行电击;③Electric shock is performed according to the parameters of Saccharomyces cerevisiae recommended by the device used;
④立即加入1mL预冷的1mol/L山梨醇至杯中,将内容物转移至灭菌离心管中;④ Immediately add 1 mL of pre-cooled 1mol/L sorbitol to the cup, and transfer the contents to a sterilized centrifuge tube;
⑤分成200-600μL等份,涂于MD平板上;⑤ Divide into 200-600μL aliquots and apply on the MD plate;
⑥在30℃孵育平板至克隆产生。⑥Incubate the plate at 30°C until clones are produced.
通过对含有重组表达载体pPIC3.5K-ayr1的毕赤酵母进行基因组PCR鉴定,确定构建了表达ayr1基因的毕赤酵母基因工程菌株(P.pastoris)GS115AYR1S.c。(如图3所示)Through genomic PCR identification of Pichia pastoris containing the recombinant expression vector pPIC3.5K-ayr1, it was confirmed that a Pichia pastoris genetically engineered strain (P. pastoris) GS115AYR1 Sc expressing the ayr1 gene had been constructed. (As shown in Figure 3)
实施例2双菌顺序催化体系的建立The establishment of
在下面的实施例中分别考察了毕赤酵母基因工程菌株对AD或ADD的作用,简单节杆菌和毕赤酵母基因工程菌株同时转化和顺序转化对BD合成的影响,及简单节杆菌反应体系的失活对BD合成的影响。In the following examples, the effects of Pichia genetically engineered strains on AD or ADD, the simultaneous transformation and sequential transformation of Arthrobacter simplex and Pichia genetically engineered strains on the synthesis of BD, and the effects of simple Arthrobacter reaction systems were investigated respectively in the following examples. Effect of inactivation on BD synthesis.
实施例2-1Example 2-1
挑取毕赤酵母基因工程菌株P.pastoris GS115AYR1S.c单克隆,接种至30mL BMGY中,30℃,200r/min,摇至OD600=5-6;室温1500g-3000g离心5min,收集细胞,去除上清,用30mL BMMY重悬细胞,进行诱导表达;每24h,加甲醇至终浓度为0.5%以继续诱导4d;于诱导4d后的发酵液中分别投加5g/L的底物AD(或ADD)及与底物摩尔比1:1的HP-β-CD,30℃,200r/min继续转化4d,取样1mL,等体积乙酸乙酯超声萃取,HPLC分析。如图5所示,毕赤酵母基因工程菌株P.pastoris GS115AYR1S.c生长细胞对底物AD及ADD进行转化后,其对应产物TS(睾酮)和BD的产率分别为59%和69%。这表明,ADD更适合于用作重组毕赤酵母17β羰基还原作用的底物。Pick a single clone of P. pastoris GS115AYR1 Sc , a genetically engineered strain of Pichia pastoris, inoculate it into 30 mL of BMGY, shake at 30°C and 200 r/min until OD 600 = 5-6; 30mL BMMY was used to resuspend the cells to induce expression; every 24h, add methanol to a final concentration of 0.5% to continue induction for 4d; add 5g/L substrate AD (or ADD) to the fermentation broth after induction 4d ) and HP-β-CD with a molar ratio of 1:1 to the substrate, 30°C, 200r/min to continue the transformation for 4 days, sample 1mL, ultrasonically extract an equal volume of ethyl acetate, and analyze by HPLC. As shown in FIG. 5 , after the Pichia genetically engineered strain P. pastoris GS115AYR1 Sc growth cells transformed the substrates AD and ADD, the yields of the corresponding products TS (testosterone) and BD were 59% and 69%, respectively. This indicated that ADD was more suitable as a substrate for the reduction of 17β carbonyl in recombinant Pichia pastoris.
实施例2-2Example 2-2
将简单节杆菌和毕赤酵母基因工程菌株P.pastoris GS115AYR1S.c的湿菌体同时加入50mM PBS缓冲溶液(pH 7.2)反应体系中,使得简单节杆菌的终浓度为5g/L(湿重)、毕赤酵母基因工程菌株终浓度为175g/L(湿重),并向反应体系中投加终浓度5g/L的底物AD及与底物摩尔比1:1的HP-β-CD,30℃,200r/min连续转化30h。转化过程中每6h取样,等体积乙酸乙酯超声萃取,HPLC分析,如图4所示,BD产率可达36%。但生成的BD并不能稳定地存在于体系中,随后BD的生成率又明显下降;而相反,ADD的积累量却持续上升至约占总体系的80%以上。分析原因,这可能是由该双菌催化体系的简单节杆菌内存在的内源的17β羟基氧化酶的作用,于是新生成的BD又继续被氧化成了ADD。Add the wet thallus of Arthrobacter simplex and Pichia genetically engineered strain P.pastoris GS115AYR1 Sc to the 50mM PBS buffer solution (pH 7.2) reaction system simultaneously, so that the final concentration of Arthrobacter simplex is 5g/L (wet weight), The final concentration of Pichia pastoris genetically engineered strains was 175g/L (wet weight), and substrate AD with a final concentration of 5g/L and HP-β-CD with a molar ratio of 1:1 to the substrate were added to the reaction system, 30 °C, 200r/min continuous conversion for 30h. Samples were taken every 6 hours during the conversion process, ultrasonically extracted with an equal volume of ethyl acetate, and analyzed by HPLC. As shown in Figure 4, the yield of BD can reach 36%. But the formed BD could not exist in the system stably, and then the generation rate of BD decreased obviously; on the contrary, the accumulation of ADD continued to rise to more than 80% of the total system. Analyzing the reason, this may be due to the action of the endogenous 17β hydroxyl oxidase in Arthrobacter simplex in the dual-bacteria catalytic system, so the newly formed BD is further oxidized into ADD.
实施例2-3Example 2-3
以30mL 50mM PBS(pH7.2)缓冲液将制得的简单节杆菌湿菌体重悬至浓度5g/L,同时投加5g/L的底物AD及摩尔比1:1的HP-β-CD,于34℃,200r/min转化30h后,直接向该反应体系中加入终浓度175g/L的毕赤酵母基因工程菌株GS115AYR1S.c湿菌体,于30℃,200r/min继续转化12h。转化过程中定时取样,等体积乙酸乙酯超声萃取,HPLC分析,BD产率可达62.4%。Resuspend the prepared Arthrobacter simplex wet bacteria with 30mL 50mM PBS (pH7.2) buffer solution to a concentration of 5g/L, and add 5g/L of substrate AD and HP-β-CD at a molar ratio of 1:1 , after transforming at 34°C and 200r/min for 30h, directly add Pichia pastoris genetically engineered strain GS115AYR1 Sc wet cells at a final concentration of 175g/L to the reaction system, and continue transforming at 30°C and 200r/min for 12h. Sampling was performed regularly during the conversion process, ultrasonic extraction with equal volume of ethyl acetate, and HPLC analysis showed that the yield of BD could reach 62.4%.
实施例2-4Example 2-4
以30mL PBS(pH7.2)缓冲液将制得的简单节杆菌湿菌体重悬至浓度5g/L,同时投加5g/L的底物AD及摩尔比1:1的HP-β-CD,于34℃,200r/min转化30h后,将该转化体系通过121℃,20min进行失活处理。然后向该失活后的反应体系中加入终浓度175g/L的毕赤酵母基因工程菌株GS115AYR1S.c湿菌体,于30℃,200r/min继续转化12h。转化过程中定时取样,等体积乙酸乙酯超声萃取,HPLC分析,BD产率可达73%。Resuspend the prepared Arthrobacter simplex wet bacteria with 30mL PBS (pH7.2) buffer solution to a concentration of 5g/L, and add 5g/L of substrate AD and HP-β-CD at a molar ratio of 1:1 at the same time, After transformation at 34°C and 200r/min for 30h, the transformation system was deactivated at 121°C for 20min. Then, wet cells of Pichia genetically engineered strain GS115AYR1 Sc at a final concentration of 175 g/L were added to the inactivated reaction system, and the transformation was continued at 30° C. and 200 r/min for 12 hours. During the conversion process, samples were taken regularly, an equal volume of ethyl acetate was ultrasonically extracted, and HPLC analysis showed that the yield of BD could reach 73%.
图6中“对照”为实施例2-3的转化过程,“失活”为实施例2-4的转化过程。对比可见,失活简单节杆菌有助于提高BD产率。In Fig. 6, "control" is the transformation process of Example 2-3, and "inactivation" is the transformation process of Example 2-4. It can be seen from the comparison that the inactivation of Arthrobacter simplex helps to increase the yield of BD.
实施例2-5Example 2-5
以30mL PBS(pH7.2)缓冲液将制得的简单节杆菌湿菌体重悬至浓度5g/L,同时投加5g/L的底物AD及与底物摩尔比1:1的HP-β-CD,于34℃,200r/min转化30h后,将该转化体系通过121℃,20min进行失活处理。然后向该失活后的反应体系中加入终浓度175g/L(湿重)的毕赤酵母基因工程菌株GS115AYR1S.c湿菌体及75g/L葡萄糖,于30℃,200r/min继续转化12h。转化过程中定时取样,等体积乙酸乙酯超声萃取,HPLC分析,BD产率可达83%。Resuspend the prepared Arthrobacter simplex wet bacteria with 30mL PBS (pH7.2) buffer to a concentration of 5g/L, and add 5g/L of substrate AD and HP-β with a molar ratio of 1:1 to the substrate at the same time -CD, after transformation at 34°C and 200r/min for 30h, the transformation system was deactivated at 121°C for 20min. Then, Pichia pastoris genetically engineered strain GS115AYR1 Sc wet thallus and 75 g/L glucose were added to the inactivated reaction system at a final concentration of 175 g/L (wet weight), and the transformation was continued at 30° C. and 200 r/min for 12 h. During the conversion process, samples were taken regularly, an equal volume of ethyl acetate was ultrasonically extracted, and HPLC analysis showed that the yield of BD could reach 83%.
实施例2说明简单节杆菌和毕赤酵母基因工程菌株顺序转化合成BD的效果优于双菌同时转化及单菌转化;顺序转化时,简单节杆菌完成转化后增加灭菌程序效果优于不灭菌直接进行毕赤酵母转化;反应体系中添加葡萄糖效果优于不添加。Example 2 illustrates that the effect of sequential transformation of Arthrobacter simplex and Pichia genetically engineered strains to synthesize BD is better than simultaneous transformation of double bacteria and single bacterial transformation; during sequential transformation, the effect of increasing the sterilization procedure after completion of transformation of Arthrobacter simplex is better than indestructible Bacteria were directly transformed into Pichia pastoris; the effect of adding glucose in the reaction system was better than that without adding it.
实施例3微生物顺序转化发酵化合物AD制备化合物BD的方法Example 3 Microbial Sequential Conversion of Fermentation Compound AD to the Method for Preparation of Compound BD
在含有底物AD浓度为3g/L的50mM PBS缓冲溶液(pH 7.2)生物转化体系中,添加与底物摩尔比1:1的HP-β-CD,投加生物量为5g/L的简单节杆菌TCCC 11037湿菌体,20℃,150r/min反应30h中间产物ADD的量达到最高后,将反应体系121℃,20min灭活,再经湿重为25g/L的毕赤酵母基因工程菌株(Pichia pastoris)GS115AYR1S.c在25℃,150r/min条件下,顺序发酵2h制备化合物宝丹酮;In the biotransformation system containing 50mM PBS buffer solution (pH 7.2) with a substrate AD concentration of 3g/L, HP-β-CD was added with a molar ratio of 1:1 to the substrate, and a simple biomass of 5g/L was added. Arthrobacter TCCC 11037 wet cells, 20°C, 150r/min reaction for 30h, after the intermediate product ADD reached the highest amount, the reaction system was inactivated at 121°C for 20min, and then passed through the genetically engineered strain of Pichia pastoris with a wet weight of 25g/L (Pichia pastoris) GS115AYR1 Sc was sequentially fermented for 2 hours at 25°C and 150r/min to prepare compound Boldenone;
上述反应结束后,发酵体系中的BD的产量可以达到1.68g/L,产率达到56%。After the above reaction, the yield of BD in the fermentation system can reach 1.68g/L, and the yield can reach 56%.
实施例4微生物顺序转化发酵化合物AD制备化合物BD的方法Example 4 Microbial Sequential Conversion of Fermentation Compound AD to the Method for Preparation of Compound BD
在含有底物AD浓度为10g/L的50mM PBS缓冲溶液(pH 7.2)生物转化体系中,添加与底物摩尔比1:1的HP-β-CD,投加生物量为5g/L的简单节杆菌TCCC 11037湿菌体,35℃,250r/min反应50h中间产物ADD的量达到最高后,将反应体系121℃,20min灭活,再添加终浓度200g/L的毕赤酵母基因工程菌株(Pichia pastoris)GS115AYR1S.c湿菌体在37℃,250r/min条件下,顺序发酵4h制备化合物宝丹酮,添加酵母的同时,加入体系终浓度100g/L的葡萄糖;In the biotransformation system containing 50mM PBS buffer solution (pH 7.2) with a substrate AD concentration of 10g/L, HP-β-CD was added with a molar ratio of 1:1 to the substrate, and a simple biomass of 5g/L was added. Arthrobacter TCCC 11037 wet thalline, 35 ℃, 250r/min reaction 50h after the amount of intermediate product ADD reaches the highest, with reaction system 121 ℃, 20min inactivation, then add the Pichia genetically engineered bacterial strain of final concentration 200g/L ( Pichia pastoris) GS115AYR1 Sc wet cells were sequentially fermented for 4 hours at 37°C and 250r/min to prepare the compound Boldenone, and at the same time adding yeast, glucose with a final concentration of 100g/L was added to the system;
上述反应结束后,发酵体系中的BD的产量可以达到7.7g/L,产率达到77%。After the above reaction, the yield of BD in the fermentation system can reach 7.7g/L, and the yield can reach 77%.
Claims (1)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201910163656 | 2019-03-05 | ||
CN2019101636568 | 2019-03-05 |
Publications (2)
Publication Number | Publication Date |
---|---|
CN109971817A CN109971817A (en) | 2019-07-05 |
CN109971817B true CN109971817B (en) | 2023-06-16 |
Family
ID=67082642
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201910264964.XA Active CN109971817B (en) | 2019-03-05 | 2019-04-03 | Preparation of Boldenone by Sequential Transformation of Arthrobacter simplex and Genetically Engineered Yeast Strains |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN109971817B (en) |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1639354A (en) * | 2002-02-01 | 2005-07-13 | 阿克佐诺贝尔公司 | Process for fermentation of phytosterols to androstadienedione |
CN102168099A (en) * | 2011-01-21 | 2011-08-31 | 华东理工大学 | 3-ketosteroid -delta 1-dehydrogenase, engineering bacterium and application thereof |
-
2019
- 2019-04-03 CN CN201910264964.XA patent/CN109971817B/en active Active
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1639354A (en) * | 2002-02-01 | 2005-07-13 | 阿克佐诺贝尔公司 | Process for fermentation of phytosterols to androstadienedione |
CN102168099A (en) * | 2011-01-21 | 2011-08-31 | 华东理工大学 | 3-ketosteroid -delta 1-dehydrogenase, engineering bacterium and application thereof |
Non-Patent Citations (4)
Title |
---|
Characterization and application of fusidane antibiotic biosynethsis enzyme 3-ketosteroid-Δ1-dehydrogenase in steroid transformation;Miao-Miao Chen,et al;《Appl Microbiol Biotechnol》;20120111;第96卷;第138页第1栏第2段,第139页第2栏第2段,第139页图3d,第141页第2栏第2段 * |
Highly efficient synthesis of boldenone from androst-4-ene-3,17-dione by Arthrobacter simplex and Pichia pastoris ordered biotransformation;Rui Tang,et al;《Bioprocess and Biosystems Engineering》;20190308;第2页第2栏第1段,第3页第1栏第2-3段,第2栏倒数第1段,第6页第2页 * |
环糊精介质中甾体结构对包结作用及C1,2脱氢反应的影响;王芳;《中国知网》;20170715(第7期);摘要,第9页第1.3.4节,第12页第2.1.2节,第32页图3-5,第36页图3-9 * |
简单节杆菌3-甾酮-△1-脱氢酶基因的克隆表达及定点突变研究;李婕等;《现代生物医学进展》;20170930;第17卷(第25期);第4801页摘要,第4803页第2.3节 * |
Also Published As
Publication number | Publication date |
---|---|
CN109971817A (en) | 2019-07-05 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN108913643A (en) | A method of it improving mycobacteria regenerating coenzyme and androstenedione is promoted to produce simultaneously | |
CN112813129A (en) | Method for increasing 7-dehydrocholesterol yield in yeast by compartmentalization | |
CN113430127B (en) | Recombinant bacterium for producing L-lactic acid and application thereof | |
CN112725212A (en) | Recombinant yeast chassis cell transformation for efficiently converting chenodeoxycholic acid, recombinant strain construction and application | |
CN101475914B (en) | Method for producing oligo-galactose by cyclic utilization of recombinant Saccharomyces cerevisiae | |
CN104531746B (en) | A method for transforming AD into ADD by utilizing recombinant Corynebacterium crenatum whole cells | |
CN109706107B (en) | Method for producing steroid precursor by high-efficiency fermentation | |
CN116064435A (en) | Curcumin reductase CfcurA, coding gene and its application | |
CN114874941A (en) | A strain of Paenibacillus phyllodes with the ability to hydrolyze raw starch and its application | |
CN115161208A (en) | Saccharomyces cerevisiae genetically engineered bacteria and its application in the production of cucurbitacin intermediates | |
CN107779423A (en) | Cofactor regeneration mycobacteria and its application in the fermentation of profit Two Liquid Phases | |
CN112941119A (en) | Method for increasing yield of fatty acid ethyl ester of saccharomyces cerevisiae engineering bacteria | |
CN111484962B (en) | A kind of highly efficient genetically engineered bacteria producing 5α-androstanedione and its application | |
CN111454871B (en) | A kind of recombinant mycobacterium with high androstenedione production and construction method and application | |
CN109971817B (en) | Preparation of Boldenone by Sequential Transformation of Arthrobacter simplex and Genetically Engineered Yeast Strains | |
CN102559518B (en) | High-yield fumaric acid Rhizopus delemar and application thereof | |
CN118147027A (en) | Method, strain and application for improving steroid precursor production by enhancing intracellular ATP metabolism | |
CN103255095A (en) | Genetically engineered bacterium and leavening agent for dehydrogenation of steroid A ring 1,2 positions | |
CN116262903A (en) | Aspergillus oryzae engineering bacteria, construction method and application | |
CN115838679A (en) | A kind of genetically engineered bacteria with high yield of steroid drug precursor and its application | |
CN116555062B (en) | Methods for improving L-lactic acid production by Saccharomyces cerevisiae based on regulation of ethanol metabolic flow | |
CN104988162B (en) | Application of cofactor regeneration module in enhancing synthesis of secondary metabolites in microorganisms | |
CN114395494B (en) | Saberlin Dener yeast T52 and application thereof | |
CN112877229B (en) | A Saccharomyces cerevisiae genetically engineered strain knocking out Sok2 and its construction method and application | |
CN115747240B (en) | A recombinant Escherichia coli engineering strain for producing equol and its application |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant |