CN102732579A - Method for preparing (3S)-3-(tertbutyloxycarbonyl)amino-1-chlorin-4-phenyl-(2R)-butanol by microbial transformation - Google Patents
Method for preparing (3S)-3-(tertbutyloxycarbonyl)amino-1-chlorin-4-phenyl-(2R)-butanol by microbial transformation Download PDFInfo
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Abstract
本发明提供了一种微生物转化制备(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-(2R)-丁醇的方法:以(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-2-丁酮为底物、以酿酒酵母(Saccharomycescerevisiae)CGMCCNo.2266发酵获得的含酶菌体细胞为生物催化剂,进行转化反应得到所述产物。本发明生产的菌株安全无毒,微生物菌体易于大规模培养,比化学催化剂和催化酶成本低廉;而且反应条件温和,环境友好,摩尔转化率高,易于实现大规模工业化生产,是工业化生产(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-(2R)-丁醇的绿色工艺。The present invention provides a method for the preparation of (3S)-3-(tert-butoxycarbonyl)amino-1-chloro-4-phenyl-(2R)-butanol by microbial conversion: (3S)-3-(tert- butoxycarbonyl)amino-1-chloro-4-phenyl-2-butanone as a substrate, using enzyme-containing bacterial cells obtained from Saccharomycescerevisiae CGMCC No.2266 fermentation as a biocatalyst, and performing a conversion reaction to obtain the product. The bacterial strain produced by the present invention is safe and non-toxic, and the microbial thalline is easy to cultivate on a large scale, and the cost is lower than chemical catalysts and catalytic enzymes; and the reaction conditions are mild, the environment is friendly, the molar conversion rate is high, and it is easy to realize large-scale industrial production, which is industrial production ( A green process for 3S)-3-(tert-butoxycarbonyl)amino-1-chloro-4-phenyl-(2R)-butanol.
Description
技术领域 technical field
本发明涉及微生物转化方法领域,具体涉及一种生物催化制备(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-(2R)-丁醇的方法。 The invention relates to the field of microbial transformation methods, in particular to a method for biocatalytically preparing (3S)-3-(tert-butoxycarbonyl)amino-1-chloro-4-phenyl-(2R)-butanol.
背景技术 Background technique
(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-(2R)-丁醇,英文名:((3S)-3-(tert-Butoxycarbonyl)amino-1-chloro-4-phenyl-(2R)-butanol),CAS号:162536-40-5,分子式C15H22NClO3,分子量299.79。(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-(2R)-丁醇是制备抗艾滋病药物阿扎那韦的关键中间体。阿扎那韦是一新型氮杂肽类蛋白酶抑制剂(PI),是根据酶-氮杂肽复合物的X射线衍射研究设计而成的,具有C-2对称的化学结构。它是HIV-1蛋白酶的高选择性和高效的抑制剂,通过阻断病毒gap和gap-pol前体多聚蛋白的裂解,从而抑制病毒结构蛋白、逆转录酶、整合酶和蛋白酶的生成,使HIV-1感染的细胞释放出非感染性的不成熟的病毒颗粒。本品对多株HIV-1病毒具有比其他PI更强的抑制活性,在体外培养基中半数有效浓度(EC50)为2.6~5.3 nmol/L,90%有效浓度(EC90)为9~15 nmol/L。 (3S)-3-(tert-Butoxycarbonyl)amino-1-chloro-4-phenyl-(2R)-butanol, English name: ((3S)-3-(tert-Butoxycarbonyl)amino-1-chloro -4-phenyl-(2R)-butanol), CAS number: 162536-40-5, molecular formula C 15 H 22 NClO 3 , molecular weight 299.79. (3S)-3-(tert-butoxycarbonyl)amino-1-chloro-4-phenyl-(2R)-butanol is a key intermediate in the preparation of the anti-AIDS drug atazanavir. Atazanavir is a new type of azapeptide protease inhibitor (PI), which is designed according to the X-ray diffraction study of the enzyme-azapeptide complex and has a C-2 symmetrical chemical structure. It is a highly selective and efficient inhibitor of HIV-1 protease. It inhibits the production of viral structural proteins, reverse transcriptase, integrase and protease by blocking the cleavage of viral gap and gap-pol precursor polyproteins, HIV-1-infected cells release non-infectious immature virus particles. This product has stronger inhibitory activity against multiple strains of HIV-1 virus than other PIs. The half effective concentration (EC50) in the in vitro medium is 2.6-5.3 nmol/L, and the 90% effective concentration (EC90) is 9-15 nmol. /L.
拆分外消旋体(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-丁醇,可以获得(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-(2R)-丁醇,但是拆分效率最大只有50%,生产效率不高。以(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-2-丁酮为底物采用化学法和微生物法不对称还原底物中的羰基均可以得到(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-(2R)-丁醇。而化学法不对称还原需要制备手性化学催化剂,价格昂贵,制备过程繁琐,且通常环境污染较大。 The racemate (3S)-3-(tert-butoxycarbonyl)amino-1-chloro-4-phenyl-butanol can be resolved to obtain (3S)-3-(tert-butoxycarbonyl)amino-1- Chloro-4-phenyl-(2R)-butanol, but the maximum resolution efficiency is only 50%, and the production efficiency is not high. With (3S)-3-(tert-butoxycarbonyl)amino-1-chloro-4-phenyl-2-butanone as the substrate, the carbonyl group in the substrate can be asymmetrically reduced by chemical and microbial methods to obtain (3S )-3-(tert-butoxycarbonyl)amino-1-chloro-4-phenyl-(2R)-butanol. However, the chemical asymmetric reduction requires the preparation of a chiral chemical catalyst, which is expensive, cumbersome in the preparation process, and usually causes greater environmental pollution.
发明内容 Contents of the invention
本发明目的是提供一种微生物转化制备(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-(2R)-丁醇的方法,该方法反应条件温和,操作简便,环境友好,产物转化率高,易于工业化生产。 The object of the present invention is to provide a method for the preparation of (3S)-3-(tert-butoxycarbonyl)amino-1-chloro-4-phenyl-(2R)-butanol by microbial transformation, the method has mild reaction conditions and is easy to operate , environment-friendly, high product conversion rate, easy industrial production.
本发明采用的技术方案是: The technical scheme adopted in the present invention is:
一种微生物转化制备(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-(2R)-丁醇的方法,所述方法是以(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-2-丁酮为底物,以酿酒酵母(Saccharomyces cerevisiae)CGMCC No. 2266发酵获得的含酶菌体细胞为生物催化剂,进行转化反应制得所述(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-(2R)-丁醇。 A method for preparing (3S)-3-(tert-butoxycarbonyl)amino-1-chloro-4-phenyl-(2R)-butanol by microbial transformation, the method is based on (3S)-3-(tert- butoxycarbonyl)amino-1-chloro-4-phenyl-2-butanone as the substrate, and the enzyme-containing bacterial cells obtained from the fermentation of Saccharomyces cerevisiae ( Saccharomyces cerevisiae ) CGMCC No. 2266 as the biocatalyst, and the conversion reaction The (3S)-3-(tert-butoxycarbonyl)amino-1-chloro-4-phenyl-(2R)-butanol was obtained.
所述酿酒酵母CGMCC No.2266,已在先前授权专利200810059686中作为新菌株予以保护,保藏于中国微生物菌种保藏管理委员会普通微生物保藏中心,位于北京市朝阳区大屯路中国科学院微生物研究所内,保藏号CGMCC No.2266,保藏日期2007年11月26 日。 The Saccharomyces cerevisiae CGMCC No.2266 has been protected as a new strain in the previously authorized patent 200810059686, and is preserved in the General Microorganism Collection Center of the China Microbial Culture Collection Management Committee, located in the Institute of Microbiology, Chinese Academy of Sciences, Datun Road, Chaoyang District, Beijing, The deposit number is CGMCC No.2266, and the deposit date is November 26, 2007. the
所述酿酒酵母CGMCC No.2266的菌落特征:在琼脂培养基上呈现出乳白色、有光泽、平坦、边缘整齐、湿润、表面光滑,质地均匀的菌落形态。 The colony characteristics of the Saccharomyces cerevisiae CGMCC No.2266: on the agar medium, it presents a milky white, shiny, flat, neat edge, moist, smooth surface, and uniform colony morphology.
进一步地,本发明所述的微生物转化制备(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-(2R)-丁醇的方法为:以pH 5.0~8.0的磷酸盐缓冲液为反应溶剂,以(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-2-丁酮为底物、以酿酒酵母(Saccharomyces cerevisiae)CGMCC No. 2266发酵获得的含酶菌体细胞为生物催化剂,于25~45℃下转化反应12~72小时,反应结束后,转化液经分离纯化得到所述(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-(2R)-丁醇。 Further, the method for preparing (3S)-3-(tert-butoxycarbonyl)amino-1-chloro-4-phenyl-(2R)-butanol by microbial transformation of the present invention is as follows: Phosphate buffer was used as the reaction solvent, (3S)-3-(tert-butoxycarbonyl)amino-1-chloro-4-phenyl-2-butanone was used as the substrate, and Saccharomyces cerevisiae CGMCC No. The enzyme-containing bacterial cells obtained by 2266 fermentation are used as biocatalysts, and the transformation reaction is carried out at 25~45°C for 12~72 hours. After the reaction, the transformation liquid is separated and purified to obtain the (3S)-3-(tert-butoxycarbonyl) Amino-1-chloro-4-phenyl-(2R)-butanol.
所述的(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-2-丁酮在磷酸盐缓冲液中的初始终浓度为0.1~1 mmol/L。 The initial concentration of the (3S)-3-(tert-butoxycarbonyl)amino-1-chloro-4-phenyl-2-butanone in the phosphate buffer is 0.1-1 mmol/L.
进一步地,本发明所述的反应体系中还可以添加有终浓度为5~20%的乙醇作为辅助底物。微生物细胞中含有大量的乙醇脱氢酶,乙醇脱氢酶转化乙醇生成乙醛,同时将氢传递给烟酰胺腺嘌呤二核苷酸(NAD)生成烟酰胺腺嘌呤二核苷酸的还原态(还原型辅酶Ⅰ,NADH),乙醇的加入有利于实现辅酶NADH的原位再生,为反应过程提供大量的供氢体,从而提高反应的转化率。同时,乙醇的加入可以适当增强细胞的通透性,促使更多的底物进入微生物细胞内进行生物转化,提高转化率。 Further, ethanol with a final concentration of 5-20% can also be added as an auxiliary substrate in the reaction system of the present invention. Microbial cells contain a large amount of alcohol dehydrogenase, which converts ethanol to acetaldehyde, and at the same time transfers hydrogen to nicotinamide adenine dinucleotide (NAD) to form the reduced state of nicotinamide adenine dinucleotide ( Reduced coenzyme Ⅰ, NADH), the addition of ethanol is conducive to the in situ regeneration of coenzyme NADH, providing a large amount of hydrogen donors for the reaction process, thereby increasing the conversion rate of the reaction. At the same time, the addition of ethanol can appropriately enhance the permeability of the cells, promote more substrates to enter the microbial cells for biotransformation, and increase the conversion rate.
所述的含酶菌体细胞用量以细胞干重计为1~20 g/g底物,这里所述的底物的量即(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-2-丁酮的质量。 Described enzyme-containing bacterium cell dosage is 1~20 g/g substrate by cell dry weight, and the amount of substrate described here is (3S)-3-(tert-butoxycarbonyl) amino-1-chloro - The mass of 4-phenyl-2-butanone. the
所述含酶菌体细胞干重是指将发酵液离心分离,弃去上清液,将所得湿细胞在120 ℃烘干48小时至恒重后,所得干细胞的重量。定量细胞干重所需的所述含酶菌体细胞发酵液用量的确定方法是:取部分发酵液中离心分离,弃去上清液,将湿细胞在120 ℃烘干48小时至恒重,测定所得细胞干重,计算出单位含酶菌体细胞发酵液中干细胞比率,再以这个比率计算定量细胞干重所需含有含酶菌体细胞发酵液用量。 The dry weight of the enzyme-containing bacterial cells refers to the weight of the obtained dry cells after centrifuging the fermentation broth, discarding the supernatant, and drying the obtained wet cells at 120° C. for 48 hours to constant weight. The method for determining the amount of fermented liquid containing enzyme-containing bacterial cells required for quantifying the dry weight of cells is: take part of the fermented liquid and centrifuge, discard the supernatant, dry the wet cells at 120°C for 48 hours to constant weight, Measure the dry weight of the obtained cells, calculate the ratio of dry cells in the fermented broth of the unit enzyme-containing bacterium cells, and then calculate the amount of fermented liquid containing the enzyme-containing bacterium cells required for the quantitative dry weight of the cells.
所述的含酶菌体细胞按照以下方法制备:将酿酒酵母CGMCC No. 2266接种至发酵培养基中,摇床转速为150~200 r/min,26~35 ℃下培养18~30 h,将发酵液离心,制得含酶菌体细胞。 The enzyme-containing bacterial cells are prepared according to the following method: Saccharomyces cerevisiae CGMCC No. 2266 is inoculated into the fermentation medium, the shaker speed is 150-200 r/min, and cultured at 26-35°C for 18-30 h, the The fermented liquid is centrifuged to obtain enzyme-containing bacterial cells. the
进一步地,(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-(2R)-丁醇纯品的获得方法如下:反应结束后,将转化液4000 r/min离心20分钟,弃去菌体沉淀,将上清液用等体积乙酸乙酯连续萃取3次,合并乙酸乙酯萃取液,在乙酸乙酯萃取液中加入无水硫酸钠除去水分,抽滤,取滤液蒸馏除去乙酸乙酯,即得所述(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-(2R)-丁醇。 Further, the method for obtaining the pure product of (3S)-3-(tert-butoxycarbonyl)amino-1-chloro-4-phenyl-(2R)-butanol is as follows: Centrifuge for 20 minutes, discard the precipitated bacteria, extract the supernatant with an equal volume of ethyl acetate for 3 times, combine the ethyl acetate extracts, add anhydrous sodium sulfate to the ethyl acetate extracts to remove water, filter with suction, Take the filtrate and distill off the ethyl acetate to obtain the (3S)-3-(tert-butoxycarbonyl)amino-1-chloro-4-phenyl-(2R)-butanol.
本发明所述的(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-(2R)-丁醇制备方法推荐按照以下步骤进行: The preparation method of (3S)-3-(tert-butoxycarbonyl)amino-1-chloro-4-phenyl-(2R)-butanol of the present invention is recommended to be carried out according to the following steps:
(1)斜面培养:将酿酒酵母CGMCC No. 2266接种到斜面培养基,26~35 ℃培养4~6天得菌体斜面;所述的斜面培养基终浓度组成为:麦芽汁5~15 g/L,酵母粉2~4 g/L,蛋白胨4~6 g/L,葡萄糖7~12 g/L,琼脂15~25 g/L,自然pH值,溶剂为水; (1) Slant culture: Inoculate Saccharomyces cerevisiae CGMCC No. 2266 into the slant medium, and culture it at 26-35°C for 4-6 days to obtain the slant; the final concentration of the slant medium is composed of: wort juice 5-15 g /L, yeast powder 2~4 g/L, peptone 4~6 g/L, glucose 7~12 g/L, agar 15~25 g/L, natural pH value, solvent is water;
(2)种子培养:从菌体斜面取一接种环菌体转接到种子培养基,摇床转速为150~200 r/min,26~35℃培养18~26 h得种子液;所述的种子培养基终浓度组成为:葡萄糖26~32 g/L,酵母粉2~4 g/L,硫酸铵3~6 g/L,无水MgSO4 0. 2~0. 4 g/L,K2HPO4·3H2O 0. 5~1.5 g/L,KH2PO4 0. 6~1.5 g/L,用NaOH或HCl溶液调整液体培养基的pH值为7.0,溶剂为水; (2) Seed culture: take an inoculation loop from the slant of the bacterium and transfer it to the seed medium, the rotation speed of the shaker is 150-200 r/min, and cultivate at 26-35°C for 18-26 hours to obtain the seed liquid; The final concentration of the seed medium is composed of: glucose 26~32 g/L, yeast powder 2~4 g/L, ammonium sulfate 3~6 g/L, anhydrous MgSO 4 0.2~0.4 g/L, K 2 HPO 4 3H 2 O 0. 5~1.5 g/L, KH 2 PO 4 0. 6~1.5 g/L, use NaOH or HCl solution to adjust the pH of the liquid medium to 7.0, and the solvent is water;
(3)发酵培养:取种子液,以体积分数10~20%的接种量接种于发酵培养基中,摇床转速为150~200 r/min,26~35℃培养18~30 h,将发酵液离心分离得到所述含酶菌体细胞;所述发酵培养基终浓度组成为:葡萄糖26~32 g/L,酵母粉2~4 g/L,硫酸铵3~6 g/L,无水MgSO4 0. 2~0. 4 g/L,K2HPO4·3H2O 0. 5~1.5 g/L,KH2PO4 0.6~1.5 g/L,用NaOH或HCl溶液调整液体培养基的pH值为7.0,溶剂为水; (3) Fermentation culture: Take the seed liquid, inoculate it into the fermentation medium with an inoculum volume fraction of 10-20%, and incubate at 26-35°C for 18-30 h at a shaker speed of 150-200 r/min. The enzyme-containing bacterial cells were obtained by centrifugation of liquid; the final concentration of the fermentation medium was composed of: glucose 26-32 g/L, yeast powder 2-4 g/L, ammonium sulfate 3-6 g/L, anhydrous MgSO 4 0.2~0.4 g/L, K 2 HPO 4 3H 2 O 0.5~1.5 g/L, KH 2 PO 4 0.6~1.5 g/L, adjust liquid medium with NaOH or HCl solution The pH value is 7.0, and the solvent is water;
(4)生物转化:在pH 5.0~8.0的磷酸盐缓冲液中,添加终浓度为5~20%的乙醇作为辅助底物,加入终浓度为0.1~1 mmol/L的(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-2-丁酮,以及相当于细胞干重质量为(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-2-丁酮1~20倍的含酶菌体细胞,25~45 ℃下转化反应12~72小时,得转化液; (4) Biotransformation: Add ethanol at a final concentration of 5 to 20% as an auxiliary substrate in a phosphate buffer solution with a pH of 5.0 to 8.0, and add (3S)-3- at a final concentration of 0.1 to 1 mmol/L (tert-butoxycarbonyl)amino-1-chloro-4-phenyl-2-butanone, and (3S)-3-(tert-butoxycarbonyl)amino-1-chloro-4- Phenyl-2-butanone 1~20 times of enzyme-containing bacterial cells, transformation reaction at 25~45°C for 12~72 hours, to obtain transformation solution;
(5)反应结束后获得(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-(2R)-丁醇纯品的方法如下:反应结束后,将转化液于4000 r/min离心20分钟,弃去菌体沉淀,将上清液用等体积乙酸乙酯连续萃取3次,合并乙酸乙酯萃取液,在乙酸乙酯萃取液中加入无水硫酸钠除去水分,抽滤,取滤液蒸馏除去乙酸乙酯,即得所述(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-(2R)-丁醇。 (5) The method to obtain the pure product of (3S)-3-(tert-butoxycarbonyl)amino-1-chloro-4-phenyl-(2R)-butanol after the reaction is finished is as follows: Centrifuge at 4000 r/min for 20 minutes, discard the bacterial precipitate, extract the supernatant with an equal volume of ethyl acetate for 3 times, combine the ethyl acetate extract, add anhydrous sodium sulfate to the ethyl acetate extract to remove water , filtered with suction, and the filtrate was distilled to remove ethyl acetate to obtain the (3S)-3-(tert-butoxycarbonyl)amino-1-chloro-4-phenyl-(2R)-butanol.
本发明所述的(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-(2R)-丁醇的对映体过剩值(ee%)及底物转化率的确定:反应进行过程中,每间隔1~11 h取样5 mL,样品4000 r/min离心20分钟,弃去沉淀,将上清液用5 mL乙酸乙酯萃取,吸取乙酸乙酯萃取液5 μL打入液相色谱进行分析。液相色谱型号为安捷伦1200, 色谱柱为手性柱CHIRACEL OD-H(4.6 mm×250 mm,5 um), 缓冲液成分为正己烷-叔丁基甲基甲醚-三氟乙酸(800:200:2),流动相由上述缓冲液和乙醇按照体积比99:1进行配制,流动相流速为0.5 mL/min,进样量为5 ul。在该分析条件下能够将底物(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-2-丁酮、(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-(2R)-丁醇和(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-(2S)-丁醇完全分开,从而进一步计算出底物的摩尔转化率和产物(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-(2R)-丁醇的对映体过剩值。 (3S)-3-(tert-butoxycarbonyl)amino-1-chloro-4-phenyl-(2R)-butanol of the present invention is enantiomeric excess value (ee%) and substrate conversion rate Confirmation: during the reaction process, 5 mL of sample was taken every 1-11 h, the sample was centrifuged at 4000 r/min for 20 minutes, the precipitate was discarded, the supernatant was extracted with 5 mL of ethyl acetate, and 5 μL of the ethyl acetate extract was absorbed into liquid chromatography for analysis. The liquid chromatography model is Agilent 1200, the chromatographic column is chiral column CHIRACEL OD-H (4.6 mm×250 mm, 5 um), and the buffer solution is n-hexane-tert-butyl methyl ether-trifluoroacetic acid (800:200: 2), the mobile phase was prepared from the above buffer solution and ethanol at a volume ratio of 99:1, the flow rate of the mobile phase was 0.5 mL/min, and the injection volume was 5 ul. Under the analytical conditions, the substrate (3S)-3-(tert-butoxycarbonyl)amino-1-chloro-4-phenyl-2-butanone, (3S)-3-(tert-butoxycarbonyl)amino -1-chloro-4-phenyl-(2R)-butanol and (3S)-3-(tert-butoxycarbonyl)amino-1-chloro-4-phenyl-(2S)-butanol are completely separated, thereby further The molar conversion of the substrate and the enantiomeric excess of the product (3S)-3-(tert-butoxycarbonyl)amino-1-chloro-4-phenyl-(2R)-butanol were calculated.
制得的(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-(2R)-丁醇纯品可用液相色谱-质谱联用仪检测,确定产物的纯度和分子量。 The (3S)-3-(tert-butoxycarbonyl) amino-1-chloro-4-phenyl-(2R)-butanol pure product can be detected by liquid chromatography-mass spectrometry to determine the purity and molecular weight.
本发明中采用微生物细胞不对称还原(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-2-丁酮制备(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-(2R)-丁醇,可以获得高对映体过剩值的产品,添加5~20%的乙醇作为辅助底物有利于提高底物的摩尔转化率。 In the present invention, microbial cells are used to asymmetrically reduce (3S)-3-(tert-butoxycarbonyl)amino-1-chloro-4-phenyl-2-butanone to prepare (3S)-3-(tert-butoxycarbonyl)amino -1-Chloro-4-phenyl-(2R)-butanol can obtain products with high enantiomeric excess value, and adding 5-20% ethanol as an auxiliary substrate is beneficial to improve the molar conversion rate of the substrate.
本发明采用微生物转化法制备(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-(2R)-丁醇,与化学合成法、酶催化法相比具有以下优点:(1)生产菌株安全无毒,微生物菌体易于大规模培养,可以获得大量的生物催化剂,比化学催化剂和催化酶成本低廉;(2)反应条件温和,环境友好,摩尔转化率高,易于实现大规模工业化生产,是工业化生产(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-(2R)-丁醇的绿色工艺。 The present invention adopts microbial conversion method to prepare (3S)-3-(tert-butoxycarbonyl)amino-1-chloro-4-phenyl-(2R)-butanol, which has the following advantages compared with chemical synthesis method and enzyme catalysis method: (1) The production strain is safe and non-toxic, and the microbial cells are easy to cultivate on a large scale, and a large amount of biocatalysts can be obtained, which is cheaper than chemical catalysts and catalytic enzymes; (2) The reaction conditions are mild, environmentally friendly, and the molar conversion rate is high, which is easy to realize Large-scale industrial production is a green process for the industrial production of (3S)-3-(tert-butoxycarbonyl)amino-1-chloro-4-phenyl-(2R)-butanol.
(一) 具体实施方式 (1) Specific implementation methods
下面结合具体实施例对本发明进行进一步描述,但本发明的范围并不仅限于此。 The present invention will be further described below in conjunction with specific examples, but the scope of the present invention is not limited thereto.
斜面培养基配制:麦芽汁10 g/L,酵母粉3 g/L,蛋白胨5 g/L,葡萄糖10 g/L,琼脂20 g/L,自然pH值,溶剂为水;121 ℃灭菌20 min,灭菌后冷却制成斜面。 Slant medium preparation: wort juice 10 g/L, yeast powder 3 g/L, peptone 5 g/L, glucose 10 g/L, agar 20 g/L, natural pH value, solvent is water; sterilized at 121 ℃ for 20 min, sterilized and cooled to make a slope.
种子和发酵培养基配制:葡萄糖30 g/L,酵母粉3 g/L,硫酸铵5 g/L,无水MgSO4 0.25 g/L,K2HPO4·3H2O 1 g/L,KH2PO4 1 g/L,溶剂为水,用NaOH或HCl溶液调整液体培养基的pH值为7.0,121 ℃灭菌20 min。 Preparation of seeds and fermentation medium: glucose 30 g/L, yeast powder 3 g/L, ammonium sulfate 5 g/L, anhydrous MgSO 4 0.25 g/L, K 2 HPO 4 3H 2 O 1 g/L, KH 2 PO 4 1 g/L, the solvent is water, the pH of the liquid medium is adjusted to 7.0 with NaOH or HCl solution, and sterilized at 121 °C for 20 min.
实施例1 Example 1
将酿酒酵母CGMCC No. 2266菌种接种至斜面培养基,30 ℃培养6天制得菌体斜面。用接种针从菌体斜面取一接种环菌体接种在含有100 mL液体培养基的250 mL三角瓶中,于30℃、180 r/min的条件下培养24 h获得种子液。将10mL种子液(接种量用量为液体培养基体积10%)接种于含有100 mL液体培养基的250 mL三角瓶中,于30℃、180 r/min的条件下培养24 h获得发酵液,发酵液离心,得含酶菌体细胞。 Saccharomyces cerevisiae CGMCC No. 2266 was inoculated into the slant medium, and cultured at 30°C for 6 days to prepare the slant. Use an inoculation needle to take an inoculation loop from the slant of the bacterium and inoculate it into a 250 mL Erlenmeyer flask containing 100 mL of liquid medium, and cultivate it at 30 °C and 180 r/min for 24 h to obtain a seed solution. Inoculate 10 mL of seed solution (the inoculation amount is 10% of the volume of the liquid medium) into a 250 mL Erlenmeyer flask containing 100 mL of liquid medium, and culture it at 30°C and 180 r/min for 24 hours to obtain a fermentation broth. The solution was centrifuged to obtain enzyme-containing bacterial cells.
经测定,本实施例的每升发酵液中含有含酶菌体细胞的干重为50克。 After determination, the dry weight of enzyme-containing bacterium cells contained in each liter of fermented liquid of the present embodiment is 50 grams.
在十份含有100 mL pH7.0磷酸盐缓冲液的三角瓶中分别加入上述所得发酵液200 mL,其中含有含酶菌体细胞的干重为10 g,分别加入(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-2-丁酮,使(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-2-丁酮的终浓度分别为0.1 mmol/L、0.2 mmol/L、0.3 mmol/L、0.4 mmol/L、0.5 mmol/L、0.6 mmol/L、0.7 mmol/L、0.8 mmol/L、0.9 mmol/L、1.0 mmol/L,均置于30 ℃,180 r/min的摇床中反应36 h。反应结束后将转化液于4000 r/min离心20分钟,弃去菌体沉淀,将上清液用等体积乙酸乙酯连续萃取3次,合并乙酸乙酯萃取液,在乙酸乙酯萃取液中加入无水硫酸钠除去少量水分,抽滤,滤液蒸馏除去乙酸乙酯,即得所述(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-(2R)-丁醇,底物初始浓度对摩尔转化率及(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-(2R)-丁醇的对应体过剩值(ee%)的影响见表1。 Add 200 mL of the fermented liquid obtained above to ten portions of Erlenmeyer flasks containing 100 mL of pH7.0 phosphate buffer solution, which contains 10 g of the dry weight of enzyme-containing bacterial cells, and add (3S)-3-(tert- Butoxycarbonyl) amino-1-chloro-4-phenyl-2-butanone, so that the terminal of (3S)-3-(tert-butoxycarbonyl)amino-1-chloro-4-phenyl-2-butanone Concentrations are 0.1 mmol/L, 0.2 mmol/L, 0.3 mmol/L, 0.4 mmol/L, 0.5 mmol/L, 0.6 mmol/L, 0.7 mmol/L, 0.8 mmol/L, 0.9 mmol/L, 1.0 mmol /L, were placed in a shaker at 30 °C and 180 r/min for 36 h. After the reaction, the transformation solution was centrifuged at 4000 r/min for 20 minutes, the bacterial precipitate was discarded, and the supernatant was continuously extracted 3 times with an equal volume of ethyl acetate, and the ethyl acetate extract was combined, and added to the ethyl acetate extract. Add anhydrous sodium sulfate to remove a small amount of water, filter with suction, and distill the filtrate to remove ethyl acetate to obtain the (3S)-3-(tert-butoxycarbonyl)amino-1-chloro-4-phenyl-(2R)- Butanol, initial substrate concentration versus molar conversion and (3S)-3-(tert-butoxycarbonyl)amino-1-chloro-4-phenyl-(2R)-butanol (ee%) The impact can be seen in Table 1.
表1 底物初始浓度对转化率及(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-(2R)-丁醇对映体过剩值的影响 Table 1 Effect of initial substrate concentration on conversion and enantiomeric excess of (3S)-3-(tert-butoxycarbonyl)amino-1-chloro-4-phenyl-(2R)-butanol
表1可以看出:随着底物浓度的提高转化率逐渐降低。当底物浓度为0.1 mmol/L时转化率为100%。底物浓度对产物(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-(2R)-丁醇的对映体过剩值有较大的影响, (3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-(2R)-丁醇的对映体过剩值随着底物浓度的提高而降低。底物浓度低于0.3mmol/L时,产物(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-(2R)-丁醇的对映体过剩值为100%。 It can be seen from Table 1 that the conversion rate gradually decreases with the increase of the substrate concentration. The conversion rate was 100% when the substrate concentration was 0.1 mmol/L. The substrate concentration has a greater impact on the enantiomeric excess of the product (3S)-3-(tert-butoxycarbonyl)amino-1-chloro-4-phenyl-(2R)-butanol, (3S)- The enantiomeric excess of 3-(tert-butoxycarbonyl)amino-1-chloro-4-phenyl-(2R)-butanol decreases with increasing substrate concentration. The enantiomeric excess of the product (3S)-3-(tert-butoxycarbonyl)amino-1-chloro-4-phenyl-(2R)-butanol is 100% at substrate concentrations below 0.3 mmol/L .
实施例2 Example 2
将酿酒酵母CGMCC No. 2266菌种接种至斜面培养基,30 ℃培养6天得菌体斜面。用接种针从菌体斜面取一接种环菌体接种在含有100 mL液体培养基的250 mL三角瓶中,于30 ℃、180 r/min的条件下培养24 h获得种子液。将10 mL种子液(接种量用量为液体培养基体积10%)接种于含有100 mL液体培养基的250 mL三角瓶中,于30 ℃、180 r/min的条件下培养24 h获得发酵液,发酵液离心,得含酶菌体细胞,每升发酵液中含有含酶菌体细胞的干重为50克。 Saccharomyces cerevisiae CGMCC No. 2266 was inoculated into the slant medium and cultured at 30°C for 6 days to obtain the slant. Use an inoculation needle to take an inoculation loop from the slant of the bacterium and inoculate it into a 250 mL Erlenmeyer flask containing 100 mL of liquid medium, and cultivate it at 30 °C and 180 r/min for 24 h to obtain a seed solution. Inoculate 10 mL of seed solution (the inoculation amount is 10% of the volume of the liquid medium) into a 250 mL Erlenmeyer flask containing 100 mL of liquid medium, and culture it at 30 °C and 180 r/min for 24 h to obtain a fermentation broth. The fermented liquid is centrifuged to obtain enzyme-containing bacterium cells, and the dry weight of the enzyme-containing bacterium cells in every liter of fermented liquid is 50 grams.
在七份含有100 mL pH7.0磷酸盐缓冲液的三角瓶中分别加入上述所得发酵液200 mL,其中含有含酶菌体细胞的干重为10 g,分别加入(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-2-丁酮使(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-2-丁酮终浓度为0.3 mmol/L,各自加入辅助底物乙醇使乙醇体积用量占反应体系的体积百分比(v/v)分别为0%、5%、10%、15%、20%、25%和30%,置于30℃,180 r/min的摇床中反应36 h,反应结束后将转化液于4000 r/min离心20分钟,弃去菌体沉淀,将上清液用等体积乙酸乙酯连续萃取3次,合并乙酸乙酯萃取液,在乙酸乙酯萃取液中加入无水硫酸钠除去少量水分,抽滤,将滤液蒸馏除去乙酸乙酯,即得所述(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-(2R)-丁醇,辅助底物乙醇浓度对摩尔转化率及(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-(2R)-丁醇的对应体过剩值(ee%)的影响见表2。 In seven Erlenmeyer flasks containing 100 mL of pH7.0 phosphate buffer solution, 200 mL of the above-mentioned fermented liquid was added, in which the dry weight of enzyme-containing bacterial cells was 10 g, and (3S)-3-(tert- Butoxycarbonyl) amino-1-chloro-4-phenyl-2-butanone makes (3S)-3-(tert-butoxycarbonyl) amino-1-chloro-4-phenyl-2-butanone final concentration of 0.3 mmol/L, respectively add auxiliary substrate ethanol so that the volume percentage of ethanol in the reaction system (v/v) is 0%, 5%, 10%, 15%, 20%, 25% and 30%, respectively, set React in a shaker at 30°C and 180 r/min for 36 h. After the reaction, centrifuge the transformation liquid at 4000 r/min for 20 minutes, discard the precipitated bacteria, and extract the supernatant continuously with an equal volume of ethyl acetate for 3 Next, combine the ethyl acetate extracts, add anhydrous sodium sulfate to the ethyl acetate extracts to remove a small amount of water, filter with suction, and distill the filtrate to remove ethyl acetate to obtain the (3S)-3-(tert-butoxy Carbonyl) amino-1-chloro-4-phenyl-(2R)-butanol, auxiliary substrate ethanol concentration versus molar conversion and (3S)-3-(tert-butoxycarbonyl)amino-1-chloro-4- The effect of the enantiomer excess (ee%) of phenyl-(2R)-butanol is shown in Table 2.
表2:添加乙醇对转化率及(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-(2R)-丁醇对映体过剩值的影响 Table 2: Effect of ethanol addition on conversion and enantiomeric excess of (3S)-3-(tert-butoxycarbonyl)amino-1-chloro-4-phenyl-(2R)-butanol
表2可以看出:适量乙醇的加入有利于提高底物摩尔转化率,乙醇添加量为10%~15%时,效果较好,乙醇浓度更高于反而会降低微生物的生物转化能力,转化率会逐渐降低。(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-(2R)-丁醇的对映体过剩值不随乙醇添加量的改变而改变,均保持在100%。 It can be seen from Table 2 that the addition of an appropriate amount of ethanol is conducive to improving the molar conversion rate of the substrate. When the amount of ethanol added is 10% to 15%, the effect is better, and the higher concentration of ethanol will reduce the biotransformation ability of microorganisms. will gradually decrease. The enantiomeric excess of (3S)-3-(tert-butoxycarbonyl)amino-1-chloro-4-phenyl-(2R)-butanol did not change with the amount of ethanol added and remained at 100%.
实施例3 Example 3
将酿酒酵母CGMCC No. 2266菌种接种至斜面培养基,30 ℃培养6天得菌体斜面。用接种针从菌体斜面取一接种环菌体接种在含有100 mL液体培养基的250 mL三角瓶中,于30℃、180 r/min的条件下培养24 h获得种子液。将种子液以10%的接种量接种于含有100 mL液体培养基的250 mL三角瓶中,于30 ℃、180 r/min的条件下培养24 h获得发酵液,发酵液离心,得含酶菌体细胞,每升发酵液中含有含酶菌体细胞的干重为50克。 Saccharomyces cerevisiae CGMCC No. 2266 was inoculated into the slant medium and cultured at 30°C for 6 days to obtain the slant. Use an inoculation needle to take an inoculation loop from the slant of the bacterium and inoculate it into a 250 mL Erlenmeyer flask containing 100 mL of liquid medium, and cultivate it at 30 °C and 180 r/min for 24 h to obtain a seed solution. The seed liquid was inoculated into a 250 mL Erlenmeyer flask containing 100 mL of liquid medium at an inoculation amount of 10%, and cultured at 30°C and 180 r/min for 24 hours to obtain a fermentation liquid, and the fermentation liquid was centrifuged to obtain enzyme-containing bacteria For somatic cells, the dry weight of enzyme-containing bacterial somatic cells per liter of fermentation broth is 50 grams.
在五份含有100 mL pH7.0磷酸盐缓冲液的三角瓶中分别加入上述所得发酵液200 mL,其中含有含酶菌体细胞的干重为10 g,各自加入(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-2-丁酮使(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-2-丁酮终浓度0.3 mmol/L,加入辅助底物乙醇,使乙醇终浓度为10%,在180 r/min的摇床中分别于25 ℃、30 ℃、35 ℃、40 ℃、45 ℃下转化反应36 h。反应结束后将转化液于4000 r/min离心20分钟,弃去菌体沉淀,将上清液用等体积乙酸乙酯连续萃取3次,合并乙酸乙酯萃取液,在乙酸乙酯萃取液中加入无水硫酸钠除去少量水分,抽滤,滤液蒸馏除去乙酸乙酯,即得所述(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-(2R)-丁醇,反应温度对底物摩尔转化率及(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-(2R)-丁醇的对应体过剩值(ee%)的影响见表3。 Add 200 mL of the fermented liquid obtained above to five parts of Erlenmeyer flasks containing 100 mL of pH7.0 phosphate buffer solution, which contains 10 g of enzyme-containing bacterium cells in dry weight, and add (3S)-3-(tert- Butoxycarbonyl)amino-1-chloro-4-phenyl-2-butanone to make the final concentration of (3S)-3-(tert-butoxycarbonyl)amino-1-chloro-4-phenyl-2-butanone 0.3 mmol/L, the auxiliary substrate ethanol was added to make the final concentration of ethanol 10%, and the conversion reaction was carried out at 25°C, 30°C, 35°C, 40°C, and 45°C for 36 h in a shaker at 180 r/min. After the reaction, the transformation solution was centrifuged at 4000 r/min for 20 minutes, the bacterial precipitate was discarded, and the supernatant was continuously extracted 3 times with an equal volume of ethyl acetate, and the ethyl acetate extract was combined, and added to the ethyl acetate extract. Add anhydrous sodium sulfate to remove a small amount of water, filter with suction, and distill the filtrate to remove ethyl acetate to obtain the (3S)-3-(tert-butoxycarbonyl)amino-1-chloro-4-phenyl-(2R)- Butanol, reaction temperature versus substrate molar conversion and (3S)-3-(tert-butoxycarbonyl)amino-1-chloro-4-phenyl-(2R)-butanol (ee%) The impact can be seen in Table 3.
表3 反应温度对转化率及(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-(2R)-丁醇对映体过剩值的影响 Table 3 Effect of reaction temperature on conversion and enantiomeric excess of (3S)-3-(tert-butoxycarbonyl)amino-1-chloro-4-phenyl-(2R)-butanol
表3可以看出:反应温度对转化率有较大影响。反应温度过高可以导致酶的部分失活,因而转化率降低。较佳的转化温度为30 ℃左右,(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-(2R)-丁醇的对映体过剩值不随转化温度的改变而改变,均保持在100%。 It can be seen from Table 3 that the reaction temperature has a great influence on the conversion rate. Excessively high reaction temperature can lead to partial inactivation of the enzyme, thus lowering the conversion rate. The preferred conversion temperature is about 30 °C, and the enantiomeric excess value of (3S)-3-(tert-butoxycarbonyl)amino-1-chloro-4-phenyl-(2R)-butanol does not change with the conversion temperature While changing, all remain at 100%.
实施例4: Example 4:
将酿酒酵母CGMCC No. 2266菌种接种至斜面培养基,30 ℃培养6天得菌体斜面。用接种针从菌体斜面取一接种环菌体接种在含有100 mL液体培养基的250 mL三角瓶中,于30 ℃、180 r/min的条件下培养24 h获得种子液。将种子液以10%的接种量接种于含有100 mL液体培养基的250 mL三角瓶中,于30 ℃、180 r/min的条件下培养24 h获得发酵液,发酵液离心,得含酶菌体细胞,每升发酵液中含有含酶菌体细胞的干重为50克。 Saccharomyces cerevisiae CGMCC No. 2266 was inoculated into the slant medium and cultured at 30°C for 6 days to obtain the slant. Use an inoculation needle to take an inoculation loop from the slant of the bacterium and inoculate it into a 250 mL Erlenmeyer flask containing 100 mL of liquid medium, and cultivate it at 30 °C and 180 r/min for 24 h to obtain a seed solution. The seed liquid was inoculated into a 250 mL Erlenmeyer flask containing 100 mL of liquid medium at an inoculation amount of 10%, and cultured at 30°C and 180 r/min for 24 hours to obtain a fermentation liquid, and the fermentation liquid was centrifuged to obtain enzyme-containing bacteria For somatic cells, the dry weight of enzyme-containing bacterial somatic cells per liter of fermentation broth is 50 grams.
在五份含有100 mL pH7.0磷酸盐缓冲液的三角瓶中分别加入上述所得发酵液200 mL,其中含有含酶菌体细胞的干重为10 g,加入(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-2-丁酮,使(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-2-丁酮终浓度为0.3 mmol/L,加入辅助底物乙醇,使乙醇终浓度为10%,置于30 ℃,180 r/min的摇床中分别反应12 h、24 h、36 h、48 h、72 h。反应结束后将转化液于4000 r/min离心20分钟,弃去菌体沉淀,将上清液用等体积乙酸乙酯连续萃取3次,合并乙酸乙酯萃取液,在乙酸乙酯萃取液中加入无水硫酸钠除去少量水分,抽滤,滤液馏除去乙酸乙酯,即得所述(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-(2R)-丁醇,反应时间对底物摩尔转化率及(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-(2R)-丁醇的对应体过剩值(ee%)的影响见表4。 Add 200 mL of the above-mentioned fermented liquid to five Erlenmeyer flasks containing 100 mL of pH7.0 phosphate buffer solution, which contains 10 g of enzyme-containing bacterium cells in dry weight, and add (3S)-3-(tert-butyl Oxycarbonyl) amino-1-chloro-4-phenyl-2-butanone, so that the final concentration of (3S)-3-(tert-butoxycarbonyl) amino-1-chloro-4-phenyl-2-butanone is 0.3 mmol/L, the auxiliary substrate ethanol was added to make the final ethanol concentration 10%, and placed in a shaker at 30 °C and 180 r/min to react for 12 h, 24 h, 36 h, 48 h, and 72 h, respectively. After the reaction, the transformation solution was centrifuged at 4000 r/min for 20 minutes, the bacterial precipitate was discarded, and the supernatant was continuously extracted 3 times with an equal volume of ethyl acetate, and the ethyl acetate extract was combined, and added to the ethyl acetate extract. Add anhydrous sodium sulfate to remove a small amount of water, filter with suction, remove ethyl acetate by distillation from the filtrate, and obtain the (3S)-3-(tert-butoxycarbonyl)amino-1-chloro-4-phenyl-(2R)- Butanol, reaction time versus substrate molar conversion and (3S)-3-(tert-butoxycarbonyl)amino-1-chloro-4-phenyl-(2R)-butanol (ee%) The impact can be seen in Table 4.
表4:反应时间对转化率及(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-(2R)-丁醇对映体过剩值的影响 Table 4: Effect of reaction time on conversion and enantiomeric excess of (3S)-3-(tert-butoxycarbonyl)amino-1-chloro-4-phenyl-(2R)-butanol
表4可以看出:随着转化时间的延长转化率逐渐提高。当反应36小时以后转化率基本上都可以达到100%,因此最佳的转化时间为36小时。(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-(2R)-丁醇的对映体过剩值不随转化时间的改变而改变,均保持在100%。 It can be seen from Table 4 that the conversion rate gradually increases with the prolongation of the conversion time. After 36 hours of reaction, the conversion rate can basically reach 100%, so the optimum conversion time is 36 hours. The enantiomeric excess of (3S)-3-(tert-butoxycarbonyl)amino-1-chloro-4-phenyl-(2R)-butanol remained at 100% without changing with the conversion time.
实施例5: Example 5:
将酿酒酵母CGMCC No. 2266菌种接种至斜面培养基,30℃培养6天得菌体斜面。用接种针从菌体斜面取一环菌体接种在含有100 mL液体培养基的250 mL三角瓶中,于30 ℃、180 r/min的条件下培养24 h获得种子液。将种子液以10%的接种量接种于含有100 mL液体培养基的250 mL三角瓶中,于30℃、180 r/min的条件下培养24 h获得发酵液,发酵液离心,得含酶菌体细胞,每升发酵液中含有含酶菌体细胞的干重为50克。 Saccharomyces cerevisiae CGMCC No. 2266 was inoculated into the slant medium, and cultured at 30°C for 6 days to obtain the slant. A ring of bacteria was taken from the slant of the bacteria with an inoculation needle and inoculated into a 250 mL Erlenmeyer flask containing 100 mL of liquid medium, and cultured at 30 °C and 180 r/min for 24 h to obtain a seed liquid. The seed solution was inoculated into a 250 mL Erlenmeyer flask containing 100 mL of liquid medium at an inoculum amount of 10%, cultured at 30°C and 180 r/min for 24 hours to obtain a fermentation liquid, and the fermentation liquid was centrifuged to obtain enzyme-containing bacteria For somatic cells, the dry weight of enzyme-containing bacterial somatic cells per liter of fermentation broth is 50 grams.
在五份含有100 mLpH7.0磷酸盐缓冲液的三角瓶中分别加入上述所得发酵液40毫升、100毫升、200毫升、300毫升和400毫升的,其中含有含酶菌体细胞的干重分别为2 g、5 g、10 g、15 g和20 g。在上述五只三角瓶中分别加入(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-2-丁酮,使(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-2-丁酮终浓度为0.3 mmol/L,再各自加入辅助底物乙醇使乙醇终浓度为10%,置于30℃,180 r/min的摇床中反应36 h。反应结束后将转化液于4000 r/min离心20分钟,弃去菌体沉淀,将上清液用等体积乙酸乙酯连续萃取3次,合并乙酸乙酯萃取液,在乙酸乙酯萃取液中加入无水硫酸钠除去少量水分,抽滤,滤液蒸馏除去乙酸乙酯,即得所述(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-(2R)-丁醇,菌体细胞量对底物摩尔转化率及(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-(2R)-丁醇的对应体过剩值(ee%)的影响见表5。 Add respectively 40 milliliters, 100 milliliters, 200 milliliters, 300 milliliters and 400 milliliters of the above-mentioned gained fermentation broth in five parts of Erlenmeyer flasks containing 100 mLpH7. 2g, 5g, 10g, 15g and 20g. Add (3S)-3-(tert-butoxycarbonyl)amino-1-chloro-4-phenyl-2-butanone to the above five conical flasks to make (3S)-3-(tert-butoxycarbonyl) The final concentration of amino-1-chloro-4-phenyl-2-butanone is 0.3 mmol/L, and then the auxiliary substrate ethanol is added to make the final concentration of ethanol 10%, and placed in a shaking table at 30°C and 180 r/min React in medium for 36 h. After the reaction, the transformation solution was centrifuged at 4000 r/min for 20 minutes, the bacterial precipitate was discarded, and the supernatant was continuously extracted 3 times with an equal volume of ethyl acetate, and the ethyl acetate extract was combined, and added to the ethyl acetate extract. Add anhydrous sodium sulfate to remove a small amount of water, filter with suction, and distill the filtrate to remove ethyl acetate to obtain the (3S)-3-(tert-butoxycarbonyl)amino-1-chloro-4-phenyl-(2R)- Butanol, bacterial cell mass to substrate molar conversion rate and (3S)-3-(tert-butoxycarbonyl)amino-1-chloro-4-phenyl-(2R)-butanol corresponding excess value (ee %) can be seen in Table 5.
表5 菌体量对转化率及(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-(2R)-丁醇对映体过剩值的影响 Table 5 Effects of bacterial mass on conversion rate and enantiomeric excess of (3S)-3-(tert-butoxycarbonyl)amino-1-chloro-4-phenyl-(2R)-butanol
表5 菌体量对转化率及(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-(2R)-丁醇对映体过剩值的影响 Table 5 Effect of bacterial mass on conversion rate and enantiomeric excess of (3S)-3-(tert-butoxycarbonyl)amino-1-chloro-4-phenyl-(2R)-butanol
表5可以看出: 随着菌体用量的增加转化率逐渐增加。菌体用量增加不仅提高了酶的用量,同时提高了辅酶NADH的用量,因此有利于提高反应转化率。(3S)-3-(叔丁氧羰基)氨基-1-氯-4-苯基-(2R)-丁醇的对映体过剩值不随菌体加入量的改变而改变,均保持在100%。 It can be seen from Table 5 that the conversion rate gradually increases with the increase of the bacterial cell dosage. The increase in the amount of bacteria not only increases the amount of enzyme, but also increases the amount of coenzyme NADH, so it is beneficial to improve the conversion rate of the reaction. The enantiomeric excess value of (3S)-3-(tert-butoxycarbonyl)amino-1-chloro-4-phenyl-(2R)-butanol does not change with the amount of bacteria added, and remains at 100% .
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CN109897872A (en) * | 2017-12-11 | 2019-06-18 | 湖州颐辉生物科技有限公司 | Enzyme process prepares (2S, 3S)-N- tertbutyloxycarbonyl -3- amino -1- chlorine-2-hydroxyl -4- phenyl butane |
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CN109897872A (en) * | 2017-12-11 | 2019-06-18 | 湖州颐辉生物科技有限公司 | Enzyme process prepares (2S, 3S)-N- tertbutyloxycarbonyl -3- amino -1- chlorine-2-hydroxyl -4- phenyl butane |
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