CN115960862B - Cutinase mutant and application thereof in synthesis of 1, 4-diacetylpiperazine - Google Patents
Cutinase mutant and application thereof in synthesis of 1, 4-diacetylpiperazine Download PDFInfo
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Abstract
Description
技术领域Technical Field
本发明属于酶工程技术领域,具体涉及一种角质酶突变体及其在合成1,4-二乙酰哌嗪中的应用。The invention belongs to the technical field of enzyme engineering, and particularly relates to a cutinase mutant and application thereof in synthesizing 1,4-diacetylpiperazine.
背景技术Background technique
哌嗪是一种重要的医药中间体,可合成磷酸哌嗪、胍哌、依诺沙星等几十种药物,还可用于生产湿润剂、乳化剂、分散剂、抗氧化剂、防腐剂、稳定剂、塑料加工和橡胶助剂等。哌嗪修饰的药物及功能试剂,主要通过酰化反应实现哌嗪分子的引入。哌嗪具有两个仲胺结构,通过乙酰化修饰、脱乙酰化反应,可实现两个仲胺分别连接不同的官能团,能够极大丰富药物结构种类,并显著影响该类化合物的药代动力学性质。因此,哌嗪的乙酰化反应,尤其是1,4-二乙酰哌嗪类化合物的构建对上述药物及功能试剂具有重要意义。目前1,4-二乙酰哌嗪的制备主要是利用传统化学法,该过程需要偶联试剂对羧酸活化,形成酰氯、酸酐、酰基叠氮化物等活性中间体,活性中间体进一步与胺进行亲核取代从而形成酰胺。但这种方法转化率很低,且要用到许多腐蚀性和毒性很大的试剂,导致原子经济性差。在绿色化学的要求下,迫切需要一种新的方法合成1,4-二乙酰哌嗪类化合物。Piperazine is an important pharmaceutical intermediate. It can be used to synthesize dozens of drugs such as piperazine phosphate, guanidine piperazine, and enoxacin. It can also be used to produce wetting agents, emulsifiers, dispersants, antioxidants, preservatives, stabilizers, plastic processing, and rubber additives. Piperazine-modified drugs and functional reagents mainly introduce piperazine molecules through acylation reactions. Piperazine has two secondary amine structures. Through acetylation modification and deacetylation reactions, the two secondary amines can be connected to different functional groups, which can greatly enrich the types of drug structures and significantly affect the pharmacokinetic properties of such compounds. Therefore, the acetylation reaction of piperazine, especially the construction of 1,4-diacetylpiperazine compounds, is of great significance to the above-mentioned drugs and functional reagents. At present, the preparation of 1,4-diacetylpiperazine mainly uses traditional chemical methods. This process requires coupling reagents to activate carboxylic acids to form active intermediates such as acyl chlorides, anhydrides, and acyl azides. The active intermediates further undergo nucleophilic substitution with amines to form amides. However, this method has a very low conversion rate and requires the use of many corrosive and highly toxic reagents, resulting in poor atom economy. Under the requirements of green chemistry, a new method for synthesizing 1,4-diacetylpiperazine compounds is urgently needed.
近年来,生物催化(酶催化)作为一种可持续的技术得到了普及,不需要任何保护或脱保护步骤,通常具有很高的对映选择性,可以在温和的条件下进行。本发明所使用的角质酶,属于α/β水解酶,具有角质酶特征性的甘氨酸(Gly)-酪氨酸(Tyr)-丝氨酸(Ser)谷氨酰胺(Gln)-甘氨酸(Gly)氨基酸序列以及丝氨酸(Ser)-组氨酸(His)-天冬氨酸(Asp)催化三联体,能够高效的催化脱水/水解反应。相对于脂肪酶,绝大多数角质酶没有脂肪酶结构中的“盖子”,因此角质酶的催化关键氨基酸丝氨酸暴露于溶剂;另外,角质酶催化三联体一般位于由疏水氨基酸包围的表面沟槽中,有利于容纳底物。这就为角质酶带来了较广的底物范围,如聚酯的聚合及降解,同时这一特性也为1,4-二乙酰哌嗪的生物催化制备提供了更多可能。In recent years, biocatalysis (enzyme catalysis) has been popularized as a sustainable technology, does not require any protection or deprotection steps, usually has high enantioselectivity, and can be carried out under mild conditions. The cutinase used in the present invention belongs to α/β hydrolase, has the characteristic glycine (Gly)-tyrosine (Tyr)-serine (Ser) glutamine (Gln)-glycine (Gly) amino acid sequence and serine (Ser)-histidine (His)-aspartic acid (Asp) catalytic triad of cutinase, and can efficiently catalyze dehydration/hydrolysis reaction. Relative to lipase, most cutinases do not have the "lid" in the lipase structure, so the catalytic key amino acid serine of cutinase is exposed to the solvent; in addition, the cutinase catalytic triad is generally located in the surface groove surrounded by hydrophobic amino acids, which is conducive to accommodating substrates. This brings a wider substrate range to cutinase, such as the polymerization and degradation of polyesters, and this characteristic also provides more possibilities for the biocatalytic preparation of 1,4-diacetylpiperazine.
然而,由于酶催化具有温和性,该特点限制了酶在工业化中的应用。为获得更理想的催化活性或更广泛的反应条件,还需要在野生型的基础上,通过化学修饰改造、针对酶分子结构的非理性和理性设计等方法对现有的酶进行修饰改造。However, the mildness of enzyme catalysis limits the application of enzymes in industrialization. In order to obtain more ideal catalytic activity or a wider range of reaction conditions, it is necessary to modify the existing enzymes based on the wild type through chemical modification, irrational and rational design of enzyme molecular structure, etc.
发明内容Summary of the invention
本发明针对针对野生型角质酶对哌嗪类氮杂环底物识别性差、催化活性低的问题,在原有角质酶序列(原有角质酶来源于米曲酶(Aspergillusoryzae),氨基酸序列如SEQIDNO.5所示)基础上进行突变,提供了一种具有更高催化效率的角质酶突变体。Aiming at the problem that the wild-type cutinase has poor recognition of piperazine nitrogen heterocyclic substrates and low catalytic activity, the present invention performs mutation on the basis of the original cutinase sequence (the original cutinase is derived from Aspergillus oryzae, and the amino acid sequence is shown in SEQ ID NO.5), thereby providing a cutinase mutant with higher catalytic efficiency.
本发明的具体技术方案如下:The specific technical solutions of the present invention are as follows:
本发明的第一个目的是提供一种提高1,4-二乙酰哌嗪产率的角质酶突变体,所述角质酶突变体为下述突变体中的任意一种:The first object of the present invention is to provide a cutinase mutant having improved 1,4-diacetylpiperazine productivity, wherein the cutinase mutant is any one of the following mutants:
突变体cuitinaseM1,氨基酸序列如SEQ ID NO.1所示;Mutant cuitinaseM1, the amino acid sequence of which is shown in SEQ ID NO.1;
突变体cuitinaseM2,氨基酸序列如SEQ ID NO.2所示。The mutant cuitinaseM2, the amino acid sequence is shown in SEQ ID NO.2.
本发明的第二个目的是提供上述角质酶突变体的编码序列:The second object of the present invention is to provide the coding sequence of the above-mentioned Cutinase mutant:
所述突变体cuitinaseM1的编码序列如SEQ ID NO.3所示;The coding sequence of the mutant cuitinaseM1 is shown in SEQ ID NO.3;
所述突变体cuitinaseM2的编码序列如SEQ ID NO.4所示。The coding sequence of the mutant cuitinaseM2 is shown in SEQ ID NO.4.
本发明的第三个目的是提供含有上述编码序列的重组载体。The third object of the present invention is to provide a recombinant vector containing the above coding sequence.
本发明的第四个目的是提供含有上述重组载体的重组菌。The fourth object of the present invention is to provide a recombinant bacterium containing the above recombinant vector.
本发明的第五个目的是提供上述角质酶突变体、编码序列、重组载体或重组菌在合成1,4-二乙酰哌嗪中的应用。The fifth object of the present invention is to provide the use of the above-mentioned cutinase mutant, coding sequence, recombinant vector or recombinant bacteria in the synthesis of 1,4-diacetylpiperazine.
本发明的第六个目的是提供一种合成1,4-二乙酰哌嗪的方法,所述方法是将哌嗪和乙酰基供体溶于溶剂中,加入上述的角质酶突变体,催化获得1,4-二乙酰哌嗪。The sixth object of the present invention is to provide a method for synthesizing 1,4-diacetylpiperazine, wherein piperazine and an acetyl donor are dissolved in a solvent, the above-mentioned cutinase mutant is added, and 1,4-diacetylpiperazine is obtained by catalysis.
在本发明的一种实施方式中,所述哌嗪浓度为0.1~5g/L;所述乙酰基供体为乙烯乙酸酯;所述乙烯乙酸酯与哌嗪的物质的量之比为2.2~3:1;所述角质酶的浓度为0.1~10mg/L。In one embodiment of the present invention, the piperazine concentration is 0.1-5 g/L; the acetyl donor is vinyl acetate; the molar ratio of vinyl acetate to piperazine is 2.2-3:1; and the cutinase concentration is 0.1-10 mg/L.
在本发明的一种实施方式中,所述溶剂为N,N-二甲基甲酰胺、乙腈、二甲亚砜、四氢呋喃、正己烷、乙酸乙酯和水中的任意一种或两种以上的混合物。In one embodiment of the present invention, the solvent is any one or a mixture of two or more of N,N-dimethylformamide, acetonitrile, dimethyl sulfoxide, tetrahydrofuran, n-hexane, ethyl acetate and water.
在本发明的一种实施方式中,所述催化的反应温度为20~50℃,反应时间为0.5~24h。In one embodiment of the present invention, the catalytic reaction temperature is 20-50° C., and the reaction time is 0.5-24 h.
本发明的第七个目的是提供一种制备上述角质酶突变体的方法,包括如下步骤:The seventh object of the present invention is to provide a method for preparing the above-mentioned Cutinase mutant, comprising the following steps:
(1)构建含编码所述角质酶突变体的基因的质粒载体;(1) constructing a plasmid vector containing a gene encoding the cutinase mutant;
(2)将突变体质粒导入大肠杆菌BL21中;(2) Introducing the mutant plasmid into Escherichia coli BL21;
(3)挑选阳性克隆进行发酵培养,离心收集细胞,细胞破壁上清即为角质酶突变体的粗酶液;(3) selecting positive clones for fermentation culture, collecting cells by centrifugation, and the supernatant of cell wall disruption is the crude enzyme solution of the cutinase mutant;
(4)利用镍柱对粗酶液进行蛋白纯化,得到目的蛋白,再使用超滤管进行浓缩,得到纯化酶。(4) Purify the crude enzyme solution using a nickel column to obtain the target protein, and then concentrate it using an ultrafiltration tube to obtain the purified enzyme.
在本发明的一种实施方式中,步骤(2)所述突变体质粒为pET-28a-cutinaseM1或pET-28a-cutinaseM2。In one embodiment of the present invention, the mutant plasmid in step (2) is pET-28a-cutinaseM1 or pET-28a-cutinaseM2.
在本发明的一种实施方式中,步骤(3)所述发酵培养是指使用LB-kana液体培养基于37℃条件下培养重组大肠杆菌至OD600于0.6至0.8之间,进行诱导得发酵液。In one embodiment of the present invention, the fermentation culture in step (3) refers to culturing the recombinant Escherichia coli at 37° C. to an OD 600 between 0.6 and 0.8 using LB-kana liquid culture medium, and inducing to obtain a fermentation broth.
在本发明的一种实施方式中,所述诱导的条件为加入终浓度0.5mM的IPTG,于16℃温度下诱导16h。In one embodiment of the present invention, the induction condition is to add IPTG with a final concentration of 0.5 mM and induce at a temperature of 16° C. for 16 h.
在本发明的一种实施方式中,步骤(3)所述细胞破壁上清的获得方法是将发酵液离心,舍上清液,菌体使用PBS缓冲液重悬,并重复离心步骤两次,得到重组大肠杆菌悬浮液,使用高压细胞破碎仪将菌体破碎,并于一定条件下离心,舍弃沉淀,即得细胞破壁上清。In one embodiment of the present invention, the method for obtaining the cell wall-breaking supernatant in step (3) is to centrifuge the fermentation broth, discard the supernatant, resuspend the bacteria using PBS buffer, and repeat the centrifugation step twice to obtain a recombinant Escherichia coli suspension, use a high-pressure cell disruptor to disrupt the bacteria, and centrifuge under certain conditions, discard the precipitate, and obtain the cell wall-breaking supernatant.
在本发明的一种实施方式中,所述离心条件为4℃、8000rpm条件下离心5min。In one embodiment of the present invention, the centrifugation condition is 4° C. and 8000 rpm for 5 min.
在本发明的一种实施方式中,步骤(4)所述蛋白纯化过程需要配置纯化蛋白所需溶剂,所需溶剂配置方法如下:准确称量8.95gNa2HPO4·12H2O、8.766gNaCl、0.3404g咪唑于500mLUP水中得到BindingBuffer;准确称量8.95gNa2HPO4·12H2O、8.766gNaCl、1.5318g咪唑于500mLUP水中得到WashingBuffer;准确称量8.95gNa2HPO4·12H2O、8.766gNaCl、17.02g咪唑于500mLUP水中得到ElutionBuffer。In one embodiment of the present invention, the protein purification process in step (4) requires the preparation of solvents required for protein purification, and the required solvent preparation method is as follows: accurately weigh 8.95g Na2HPO4 · 12H2O , 8.766g NaCl, and 0.3404g imidazole in 500mL UP water to obtain BindingBuffer; accurately weigh 8.95g Na2HPO4 ·12H2O, 8.766g NaCl, and 1.5318g imidazole in 500mL UP water to obtain WashingBuffer; accurately weigh 8.95g Na2HPO4 · 12H2O , 8.766g NaCl , and 17.02g imidazole in 500mL UP water to obtain ElutionBuffer.
在本发明的一种实施方式中,步骤(4)中所述蛋白纯化步骤为:先使用5个柱体积的BindingBuffer平衡柱子,粗酶液反复上样三次,使用5个柱体积的WashingBuffer冲洗杂蛋白,使用3个柱体积的ElutionBuffer收集目标蛋白。In one embodiment of the present invention, the protein purification step in step (4) is: first use 5 column volumes of Binding Buffer to balance the column, repeatedly load the crude enzyme solution three times, use 5 column volumes of Washing Buffer to wash away impurities, and use 3 column volumes of Elution Buffer to collect the target protein.
在本发明的一种实施方式中,所述气相检测条件为:气相色谱采用Agilent8890GC系统,气相检测条件为:30m×250μm×250μmHP-INNOWAX色谱柱,加热器220℃,空气流量400mL/min,氢气燃气流量30mL/min,尾气(N2)流量25mL/min。柱温箱温度最高270℃,柱温箱温度梯度设置为:初始温度80℃,15℃/min升温至200℃后保持5min,20℃/min升温至240℃,保持5min。In one embodiment of the present invention, the gas phase detection conditions are: the gas chromatograph uses an Agilent 8890GC system, the gas phase detection conditions are: 30m×250μm×250μm HP-INNOWAX chromatographic column, heater 220°C, air flow 400mL/min, hydrogen fuel gas flow 30mL/min, tail gas (N 2 ) flow 25mL/min. The column oven temperature is up to 270°C, and the column oven temperature gradient is set as: initial temperature 80°C, 15°C/min heating to 200°C and then maintained for 5min, 20°C/min heating to 240°C and maintained for 5min.
本发明的有益效果:Beneficial effects of the present invention:
本发明通过对来源于微生物Aspergillusoryzae的角质酶进行理性突变获得对哌嗪的识别与结合能力更强的突变型角质酶cuitinaseM1和cuitinaseM2,上述突变型角质酶能够有效结合哌嗪并连续催化两步乙酰化反应,可利用低活性的乙酸为乙酰基供体,直接将哌嗪酰化为1,4-二乙酰哌嗪,为哌嗪类氮杂环化合物的酰化反应提供了新的生物催化工具,具有如下优点:The present invention obtains mutant cutinases, cuitinaseM1 and cuitinaseM2, with stronger recognition and binding ability to piperazine by rationally mutating cutinases derived from the microorganism Aspergillus oryzae. The mutant cutinases can effectively bind to piperazine and continuously catalyze two-step acetylation reactions, and can use low-activity acetic acid as an acetyl donor to directly acylate piperazine into 1,4-diacetylpiperazine, thereby providing a new biocatalytic tool for the acylation reaction of piperazine-type nitrogen heterocyclic compounds, and has the following advantages:
(1)相比于野生型Aspergillusoryzae的角质酶,突变型角质酶cuitinaseM1、cuitinase M2对哌嗪的识别与结合能力更强,通过丝氨酸(Ser)-组氨酸(His)-天冬氨酸(Asp)催化三联体高效脱除水分子,在催化哌嗪为1-乙酰哌嗪后,可结合1-乙酰哌嗪进一步催化第二步乙酰化反应,生成1,4-二乙酰哌嗪,产率相比于野生型角质酶分别提升6.1倍、7.4倍。(1) Compared with the wild-type Aspergillus oryzae cutinase, the mutant cutinases cuitinase M1 and cuitinase M2 have stronger recognition and binding abilities for piperazine. They can efficiently remove water molecules through the serine (Ser)-histidine (His)-aspartic acid (Asp) catalytic triad. After catalyzing piperazine to 1-acetylpiperazine, they can further catalyze the second step acetylation reaction by combining with 1-acetylpiperazine to generate 1,4-diacetylpiperazine. The yields are increased by 6.1 and 7.4 times, respectively, compared with the wild-type cutinase.
(2)相对于传统化学法,该方法绿色环保,对环境污染小。(2) Compared with traditional chemical methods, this method is green and environmentally friendly, with less pollution to the environment.
附图说明BRIEF DESCRIPTION OF THE DRAWINGS
图1为实施例3中角质酶突变体cutinaseM1催化哌嗪气相检测结果;其中,图1中7.117min为1-乙酰哌嗪的气相出峰结果,14.928min为1,4-二乙酰哌嗪的气相出峰结果;FIG. 1 is a gas phase detection result of piperazine catalyzed by the cutinase mutant cutinaseM1 in Example 3; wherein, in FIG. 1 , 7.117 min is the gas phase peak result of 1-acetylpiperazine, and 14.928 min is the gas phase peak result of 1,4-diacetylpiperazine;
图2为实施例4中角质酶突变体cutinaseM2催化哌嗪气相检测结果;其中,图2中7.117min为1-乙酰哌嗪的气相出峰结果,14.928min为1,4-二乙酰哌嗪的气相出峰结果。FIG2 is the gas phase detection result of piperazine catalyzed by the cutinase mutant cutinaseM2 in Example 4; wherein, 7.117 min in FIG2 is the gas phase peak result of 1-acetylpiperazine, and 14.928 min is the gas phase peak result of 1,4-diacetylpiperazine.
具体实施方式Detailed ways
本发明旨在提供一种角质酶突变体及其在1,4-二乙酰哌嗪合成中的应用。本领域技术人员可以借鉴本文内容,适当改进工艺参数实现。特别需要指出的是,所有类似的替换和改动对本领域技术人员来说是显而易见的,它们都被视为包括在本发明当中。本发明的方法及应用已经通过较佳实施例进行了描述,相关人员明显能在不脱离本发明内容和范围内对本文所述的方法和应用进行改动或适当变更与组合,来实现和应用本发明技术。The present invention aims to provide a cutinase mutant and its application in the synthesis of 1,4-diacetylpiperazine. Those skilled in the art can refer to the content of this article and appropriately improve the process parameters to achieve it. It is particularly important to point out that all similar substitutions and modifications are obvious to those skilled in the art and are considered to be included in the present invention. The method and application of the present invention have been described through preferred embodiments, and relevant personnel can obviously modify or appropriately change and combine the methods and applications described herein without departing from the content and scope of the present invention to implement and apply the technology of the present invention.
为了使本领域技术人员能够更好的理解本发明,下面结合具体实施方式对本发明作进一步的详细说明。In order to enable those skilled in the art to better understand the present invention, the present invention is further described in detail below in conjunction with specific implementation methods.
本发明用到的LB-kana液体培养基的配制如下:胰化蛋白胨(10g),酵母提取物(5g),氯化钠(5g),1mL1mol/L的氢氧化钠水溶液调pH=7.4,加入卡那抗生素至终浓度50ug/mL,以去离子水定容至1L,高压下蒸汽灭菌20min。The LB-kana liquid culture medium used in the present invention is prepared as follows: tryptone (10 g), yeast extract (5 g), sodium chloride (5 g), 1 mL of 1 mol/L sodium hydroxide aqueous solution to adjust the pH to 7.4, add kanamycin to a final concentration of 50 ug/mL, dilute to 1 L with deionized water, and steam sterilize under high pressure for 20 min.
本发明涉及的气相检测条件为:气相色谱采用Agilent8890GC系统,气相检测条件为:30m×250μm×250μmHP-INNOWAX色谱柱,加热器220℃,空气流量400mL/min,氢气燃气流量30mL/min,尾气(N2)流量25mL/min。柱温箱温度最高270℃,柱温箱温度梯度设置为:初始温度80℃,15℃/min升温至200℃后保持5min,20℃/min升温至240℃,保持5min。The gas phase detection conditions involved in the present invention are: the gas chromatograph adopts the Agilent 8890GC system, the gas phase detection conditions are: 30m×250μm×250μm HP-INNOWAX chromatographic column, heater 220°C, air flow 400mL/min, hydrogen fuel gas flow 30mL/min, tail gas (N 2 ) flow 25mL/min. The column oven temperature is up to 270°C, and the column oven temperature gradient is set as follows: initial temperature 80°C, 15°C/min heating to 200°C and then maintained for 5min, 20°C/min heating to 240°C and maintained for 5min.
实施例1:一种提高1,4-二乙酰哌嗪产率的角质酶突变体及其编码序列与相关重组载体Example 1: A cutinase mutant with improved 1,4-diacetylpiperazine yield and its coding sequence and related recombinant vector
本实施例提供了一种对哌嗪的识别与结合能力更强的的角质酶的突变体,所述突变体选自突变体(1)~(2)中的任意一种:This example provides a mutant of cutinase with stronger recognition and binding ability to piperazine, wherein the mutant is selected from any one of mutants (1) to (2):
(1)突变体cuitinaseM1,氨基酸序列如SEQ ID NO.1所示:(1) Mutant cuitinaseM1, the amino acid sequence of which is shown in SEQ ID NO.1:
MHLAIKSLFVSLLGASVLASPLPSNALVERNAPLNEFLSALLSHLPAIDGTIDAVSGVITDFDQLLADLTGARTTQNGYIGVCTDYTVLFARGTSEPGNVGVLVGPPLSEAFEQAVGAKALSFQGVNGYNADVAGILAGSDAAGSKSMASLASEVLSKCPDTKLVMSGYSQGCQIVHNAVEQLPAADASKISSVLLFGDPYAGKAFPNVDASRVHTVCHAGDTICNNSVVWLPPHLTYAVDVTNAVQFAVAAAN;MHLAIKSLFVSLLGASVLASPLPSNALVERNAPLNEFLSALLSHLPAIDGTIDAVSGVITDFDQLLADLTGARTTQNGYIGVCTDYTVLFARGTSEPGNVGVLVGPPLSEAFEQAVGAKALSFQGVNGYNADVAGILAGSDAAGSKSMASLASEVLSKCPDTKLVMSGYSQGCQIVHNAVEQLPAADASKISSVLLFGDPYAGKAFPNVDASRVHTVCHAGDTICNNSVVWLPPHLTYAVDVTNAVQFAVAAAN;
(2)突变体cuitinaseM2,氨基酸序列如SEQ ID NO.2所示:(2) Mutant cuitinaseM2, the amino acid sequence of which is shown in SEQ ID NO.2:
MHLAIKSLFVSLLGASVLASPLPSNALVERNAPLNEFLSALLSHLPAIDGTIDAVSGVITDFDQLLADLTGSRTTQNGYIGVCTDYTVLFARGTSEPGNVGVLVGPPLSEAFELAVGAKALSFQGVNGYNADVAGYLAGSDAAGSKSMASLASEVLSKCPDTKLVMSGYSQGCQIVHNAVEQLPAADASKISSVLLFGDPYAAKAFPNVDASRVHTVCHAGDTICNNSVVILPPHLTYAVDVTNAVQFAVAAAN。MHLAIKSLFVSLLGASVLASPLPSNALVERNAPLNEFLSALLSHLPAIDGTIDAVSGVITDFDQLLADLTGSRTTQNGYIGVCTDYTVLFARGTSEPGNVGVLVGPPLSEAFELAVGAKALSFQGVNGYNADVAGYLAGSDAAGSKSMASLASEVLSKCPDTKLVMSGYSQGCQIVHNAVEQLPAADASKISSVLLFGDPYAAKAFPNVDASRVHTVCHAGDTICNNSVVILPPHLTYAVDVTNAVQFAVAAAN.
上述突变体是在野生型角质酶的基础上进行理性突变而得到。所述突变是指:在来源于米曲酶(Aspergillusoryzae)的野生型角质酶的氨基酸序列(如SEQ ID NO.5所示)基础上,将第136位的酪氨酸突变为异亮氨酸,将第231位的异亮氨酸突变为色氨酸获得突变体cuitinaseM1,或在来源于米曲酶(Aspergillusoryzae)的野生型角质酶的氨基酸序列(如SEQ ID NO.5所示)基础上,将第72位的丙氨酸突变为丝氨酸,将第114位的谷氨酰胺突变为亮氨酸,将第203位的甘氨酸突变为丙氨酸获得突变体cuitinaseM2。The above mutants are obtained by rational mutation on the basis of wild-type cutinase. The mutation refers to: on the basis of the amino acid sequence of wild-type cutinase derived from Aspergillus oryzae (as shown in SEQ ID NO.5), tyrosine at position 136 is mutated to isoleucine, isoleucine at position 231 is mutated to tryptophan to obtain mutant cuitinaseM1, or on the basis of the amino acid sequence of wild-type cutinase derived from Aspergillus oryzae (as shown in SEQ ID NO.5), alanine at position 72 is mutated to serine, glutamine at position 114 is mutated to leucine, and glycine at position 203 is mutated to alanine to obtain mutant cuitinaseM2.
SEQ ID NO.5:SEQ ID NO.5:
MHLAIKSLFVSLLGASVLASPLPSNALVERNAPLNEFLSALLSHLPAIDGTIDAVSGVITDFDQLLADLTGARTTQNGYIGVCTDYTVLFARGTSEPGNVGVLVGPPLSEAFEQAVGAKALSFQGVNGYNADVAGYLAGSDAAGSKSMASLASEVLSKCPDTKLVMSGYSQGCQIVHNAVEQLPAADASKISSVLLFGDPYAGKAFPNVDASRVHTVCHAGDTICNNSVVILPPHLTYAVDVTNAVQFAVAAANMHLAIKSLFVSLLGASVLASPLPSNALVERNAPLNEFLSALLSHLPAIDGTIDAVSGVITDFDQLLADLTGARTTQNGYIGVCTDYTVLFARGTSEPGNVGVLVGPPLSEAFEQAVGAKALSFQGVNGYNADVAGYLAGSDAAGSKSMASLASEVLSKCPDTKLVMSGYSQGCQIVHNAVEQLPAADASKISSVLLFGDPYAGKAFPNVDASRVHTVCHAGDTICNNSVVILPPHLTYAVDVTNAVQFAVAAAN
本实施例通过将野生型角质酶进行突变,提高了野生型角质酶对哌嗪的识别与结合能力,进而提高了野生型角质酶的催化活性,加强了该酶合成1,4-二乙酰哌嗪的能力。In this example, by mutating the wild-type cutinase, the recognition and binding ability of the wild-type cutinase to piperazine is improved, thereby improving the catalytic activity of the wild-type cutinase and enhancing the ability of the enzyme to synthesize 1,4-diacetylpiperazine.
本实施例还提供了上述角质酶突变体的编码序列,所述突变体cuitinaseM1的编码序列如SEQ ID NO.3所示;所述突变体cuitinaseM2的编码序列如SEQ ID NO.4所示。This example also provides the coding sequence of the above-mentioned cutinase mutants. The coding sequence of the mutant cuitinaseM1 is shown in SEQ ID NO.3; the coding sequence of the mutant cuitinaseM2 is shown in SEQ ID NO.4.
SEQ ID NO.3:SEQ ID NO.3:
ATGCACCTGGCCATCAAGAGCCTGTTCGTGAGCCTGCTGGGCGCCAGCGTGCTGGCCAGCCCCCTGCCCAGCAACGCCCTGGTGGAGAGGAACGCCCCCCTGAACGAGTTCCTGAGCGCCCTGCTGAGCCACCTGCCCGCCATCGACGGCACCATCGACGCCGTGAGCGGCGTGATCACCGACTTCGACCAGCTGCTGGCCGACCTGACCGGCGCCAGGACCACCCAGAACGGCTACATCGGCGTGTGCACCGACTACACCGTGCTGTTCGCCAGGGGCACCAGCGAGCCCGGCAACGTGGGCGTGCTGGTGGGCCCCCCCCTGAGCGAGGCCTTCGAGCAGGCCGTGGGCGCCAAGGCCCTGAGCTTCCAGGGCGTGAACGGCTACAACGCCGACGTGGCCGGCATCCTGGCCGGCAGCGACGCCGCCGGCAGCAAGAGCATGGCCAGCCTGGCCAGCGAGGTGCTGAGCAAGTGCCCCGACACCAAGCTGGTGATGAGCGGCTACAGCCAGGGCTGCCAGATCGTGCACAACGCCGTGGAGCAGCTGCCCGCCGCCGACGCCAGCAAGATCAGCAGCGTGCTGCTGTTCGGCGACCCCTACGCCGGCAAGGCCTTCCCCAACGTGGACGCCAGCAGGGTGCACACCGTGTGCCACGCCGGCGACACCATCTGCAACAACAGCGTGGTGTGGCTGCCCCCCCACCTGACCTACGCCGTGGACGTGACCAACGCCGTGCAGTTCGCCGTGGCCGCCGCCAACATGCACCTGGCCATCAAGAGCCTGTTCGTGAGCCTGCTGGGCGCCAGCGTGCTGGCCAGCCCCCTGCCCAGCAACGCCCTGGTGGAGAGGAACGCCCCCCTGAACGAGTTCCTGAGCGCCCTGCTGAGCCACCTGCCCGCCATCGACGGCACCATCGACGCCGTGAGCGGCGTGATCACCGACTTCGACCAGCTGCTGGCCGACCTGACCGGCGCCAGGACCACCCAGAACGGCTACATCGGCGTGTGCACCGACTACACCGTGCTGTTCGCCAGGGGCACCAGCGAGCCCGGCAACGTGGGCGTGCTGGTGGGCCCCCCCCTGAGCGAGGCCTTCGAGCAGGCCGTGGGCGCCAAGGCCCTGAGCTTCCAGGGCGTGAAC GGCTACAACGCCGACGTGGCCGGCATCCTGGCCGGCAGCGACGCCGCCGGCAGCAAGAGCATGGCCAGCCTGGCCAGCGAGGTGCTGAGCAAGTGCCCCGACACCAAGCTGGTGATGAGCGGCTACAGCCAGGGCTGCCAGATCGTGCACAACGCCGTGGAGCAGCTGCCCGCCGCCGACGCCAGCAAGATCAGCAGCGTGCTGCTGTTCGGCGACCCCTACGCCGGCAAGGCCTTCCCCAACGTGGACGCCAGCAGGGTGCACACCGTGTGCCACGCCGGCGACACCATCTGCAACAACAGCGTGGTGTGGCTGCCCCCCCACCTGACCTACGCCGTGGACGTGACCAACGCCGTGCAGTTCGCCGTGGCCGCCGCCAAC
SEQ ID NO.4:SEQ ID NO.4:
ATGCACCTGGCCATCAAGAGCCTGTTCGTGAGCCTGCTGGGCGCCAGCGTGCTGGCCAGCCCCCTGCCCAGCAACGCCCTGGTGGAGAGGAACGCCCCCCTGAACGAGTTCCTGAGCGCCCTGCTGAGCCACCTGCCCGCCATCGACGGCACCATCGACGCCGTGAGCGGCGTGATCACCGACTTCGACCAGCTGCTGGCCGACCTGACCGGCAGCAGGACCACCCAGAACGGCTACATCGGCGTGTGCACCGACTACACCGTGCTGTTCGCCAGGGGCACCAGCGAGCCCGGCAACGTGGGCGTGCTGGTGGGCCCCCCCCTGAGCGAGGCCTTCGAGCTGGCCGTGGGCGCCAAGGCCCTGAGCTTCCAGGGCGTGAACGGCTACAACGCCGACGTGGCCGGCTACCTGGCCGGCAGCGACGCCGCCGGCAGCAAGAGCATGGCCAGCCTGGCCAGCGAGGTGCTGAGCAAGTGCCCCGACACCAAGCTGGTGATGAGCGGCTACAGCCAGGGCTGCCAGATCGTGCACAACGCCGTGGAGCAGCTGCCCGCCGCCGACGCCAGCAAGATCAGCAGCGTGCTGCTGTTCGGCGACCCCTACGCCGCCAAGGCCTTCCCCAACGTGGACGCCAGCAGGGTGCACACCGTGTGCCACGCCGGCGACACCATCTGCAACAACAGCGTGGTGATCCTGCCCCCCCACCTGACCTACGCCGTGGACGTGACCAACGCCGTGCAGTTCGCCGTGGCCGCCGCCAACATGCACCTGGCCATCAAGAGCCTGTTCGTGAGCCTGCTGGGCGCCAGCGTGCTGGCCAGCCCCCTGCCCAGCAACGCCCTGGTGGAGAGGAACGCCCCCCTGAACGAGTTCCTGAGCGCCCTGCTGAGCCACCTGCCCGCCATCGACGGCACCATCGACGCCGTGAGCGGCGTGATCACCGACTTCGACCAGCTGCTGGCCGACCTGACCGGCAGCAGGACCACCCAGAACGGCTACATCGGCGTGTGCACCGACTACACCGTGCTGTTCGCCAGGGGCACCAGCGAGCCCGGCAACGTGGGCGTGCTGGTGGGCCCCCCCCTGAGCGAGGCCTTCGAGCTGGCCGTGGGCGCCAAGGCCCTGAGCTTCCAGGGCGTGAAC GGCTACAACGCCGACGTGGCCGGCTACCTGGCCGGCAGCGACGCCGCCGGCAGCAAGAGCATGGCCAGCCTGGCCAGCGAGGTGCTGAGCAAGTGCCCCGACACCAAGCTGGTGATGAGCGGCTACAGCCAGGGCTGCCAGATCGTGCACAACGCCGTGGAGCAGCTGCCCGCCGCCGACGCCAGCAAGATCAGCAGCGTGCTGCTGTTCGGCGACCCCTACGCCGCCAAGGCCTTCCCCAACGTGGACGCCAGCAGGGTGCACACCGTGTGCCACGCCGGCGACACCATCTGCAACAACAGCGTGGTGATCCTGCCCCCCCACCTGACCTACGCCGTGGACGTGACCAACGCCGTGCAGTTCGCCGTGGCCGCCGCCAAC
本实施例还提供了包括上述突变体编码序列的重组载体。所述重组载体优选地以pET-28a作为原始表达载体;本发明对构建重组载体的方法没有特殊限制,采用本领域常规方法即可。This embodiment also provides a recombinant vector comprising the mutant coding sequence. The recombinant vector preferably uses pET-28a as the original expression vector; the present invention has no particular limitation on the method for constructing the recombinant vector, and conventional methods in the art can be used.
本实施例还提供了一种包括上述重组载体的重组菌株。所述重组菌优选地以大肠杆菌作为宿主菌;所述大肠杆菌优选地为E.coliBL21(DE3)。本发明对所述重组菌株的构建方法没有特殊限制,采用本领域常规方法即可。This embodiment also provides a recombinant strain comprising the above recombinant vector. The recombinant bacteria preferably uses Escherichia coli as a host bacteria; the Escherichia coli is preferably E. coli BL21 (DE3). The present invention has no special restrictions on the construction method of the recombinant strain, and conventional methods in the art can be used.
实施例2:一种制备实施例1所述角质酶突变体的方法Example 2: A method for preparing the cutinase mutant described in Example 1
方法一:method one:
步骤1:将cuitinaseM1修饰的质粒pET-28a-cutinaseM1导入大肠杆菌BL21中,LB-kana液体培养基于37℃条件下培养至OD600于0.6至0.8之间,加入终浓度0.5mM的IPTG,于16℃温度下诱导16h;离心获得菌体,离心条件为:4℃、8000rpm条件下离心5min;使用PBS离心洗涤菌体,重悬,得到重组大肠杆菌悬浮液。Step 1: Introduce the cutinaseM1-modified plasmid pET-28a-cutinaseM1 into Escherichia coli BL21, culture in LB-kana liquid medium at 37°C until OD600 is between 0.6 and 0.8, add IPTG with a final concentration of 0.5mM, and induce at 16°C for 16h; obtain the cells by centrifugation, the centrifugation conditions are: 4°C, 8000rpm for 5min; wash the cells by centrifugation with PBS, resuspend them, and obtain a recombinant Escherichia coli suspension.
步骤2:使用高压细胞破碎仪将菌体破碎,并于4℃、13500rpm条件下离心30min,舍弃沉淀,得到粗酶液。Step 2: Use a high-pressure cell disruptor to disrupt the bacteria and centrifuge at 4°C and 13,500 rpm for 30 min. Discard the precipitate to obtain a crude enzyme solution.
步骤3:使用5个柱体积的BindingBuffer平衡镍柱,粗酶液反复上样三次,使用5个柱体积的WashingBuffer冲洗杂蛋白,使用3个柱体积的ElutionBuffer收集目标蛋白,最终得到纯化酶cutinaseM1,使用Bradford法测量蛋白浓度。Step 3: Use 5 column volumes of Binding Buffer to equilibrate the nickel column, repeatedly load the crude enzyme solution three times, use 5 column volumes of Washing Buffer to wash away the impurities, use 3 column volumes of Elution Buffer to collect the target protein, and finally obtain the purified enzyme cutinase M1, and measure the protein concentration using the Bradford method.
方法二:Method Two:
步骤1:将cuitinaseM2修饰的质粒pET-28a-cutinaseM2导入大肠杆菌BL21中,LB-kana液体培养基于37℃条件下培养至OD600于0.6至0.8之间,加入终浓度0.5mM的IPTG,于16℃温度下诱导16h;离心获得菌体,离心条件为:4℃、8000rpm条件下离心5min;使用PBS离心洗涤菌体,重悬,得到重组大肠杆菌悬浮液。Step 1: Introduce the cutinaseM2-modified plasmid pET-28a-cutinaseM2 into Escherichia coli BL21, culture in LB-kana liquid medium at 37°C until OD600 is between 0.6 and 0.8, add IPTG with a final concentration of 0.5mM, and induce at 16°C for 16h; obtain the cells by centrifugation, the centrifugation conditions are: 4°C, 8000rpm for 5min; wash the cells by centrifugation with PBS, resuspend them, and obtain a recombinant Escherichia coli suspension.
步骤2:使用高压细胞破碎仪将菌体破碎,并于4℃、13500rpm条件下离心30min,舍弃沉淀,得到粗酶液。Step 2: Use a high-pressure cell disruptor to disrupt the bacteria and centrifuge at 4°C and 13,500 rpm for 30 min. Discard the precipitate to obtain a crude enzyme solution.
步骤3:使用5个柱体积的BindingBuffer平衡镍柱,粗酶液反复上样三次,使用5个柱体积的WashingBuffer冲洗杂蛋白,使用3个柱体积的ElutionBuffer收集目标蛋白,最终得到纯化酶cutinaseM2,使用Bradford法测量蛋白浓度。Step 3: Use 5 column volumes of Binding Buffer to equilibrate the nickel column, repeatedly load the crude enzyme solution three times, use 5 column volumes of Washing Buffer to wash away the impurities, use 3 column volumes of Elution Buffer to collect the target protein, and finally obtain the purified enzyme cutinase M2, and measure the protein concentration using the Bradford method.
上述方法中所需溶剂配置方法如下:准确称量8.95gNa2HPO4·12H2O、8.766gNaCl、0.3404g咪唑于500mLUP水中得到BindingBuffer;准确称量8.95gNa2HPO4·12H2O、8.766gNaCl、1.5318g咪唑于500mLUP水中得到WashingBuffer;准确称量8.95gNa2HPO4·12H2O、8.766gNaCl、17.02g咪唑于500mLUP水中得到ElutionBuffer。The solvent preparation method required in the above method is as follows: accurately weigh 8.95gNa2HPO4 · 12H2O , 8.766gNaCl, and 0.3404g imidazole in 500mLUP water to obtain BindingBuffer; accurately weigh 8.95gNa2HPO4 · 12H2O , 8.766gNaCl, and 1.5318g imidazole in 500mLUP water to obtain WashingBuffer; accurately weigh 8.95gNa2HPO4 · 12H2O , 8.766gNaCl, and 17.02g imidazole in 500mLUP water to obtain ElutionBuffer.
实施例3:角质酶突变体cutinaseM1在合成1,4二乙酰哌嗪中的应用Example 3: Application of cutinase mutant cutinaseM1 in the synthesis of 1,4-diacetylpiperazine
按照实施例2中的方法一获得纯化酶cutinaseM1,使用Bradford法测量蛋白浓度为5.5mg/mL。将底物哌嗪(11.6μmol,2g/L)、乙酸乙烯酯(34.8μmol)加入到N,N-二甲基甲酰胺中,加入45.5μL的cuitinaseM1重组角质酶溶液,酶终浓度为0.5mg/mL;催化体系终体积为500μL;于30℃催化反应12h,通过Agilent8890GC气相仪测定1-乙酰哌嗪产率为53.47%,1,4-二乙酰哌嗪产率为11.86%(气相检测结果图见图1)。1-乙酰哌嗪是1,4-二乙酰哌嗪的合成前体,哌嗪先发生第一步乙酰化,生成1-乙酰哌嗪,再发生第二步乙酰化,生成1,4-二乙酰哌嗪。Purified enzyme cutinaseM1 was obtained according to method 1 in Example 2, and the protein concentration was measured by Bradford method to be 5.5 mg/mL. Substrate piperazine (11.6 μmol, 2 g/L) and vinyl acetate (34.8 μmol) were added to N, N-dimethylformamide, and 45.5 μL of cutinaseM1 recombinant cutinase solution was added, and the final enzyme concentration was 0.5 mg/mL; the final volume of the catalytic system was 500 μL; the catalytic reaction was carried out at 30°C for 12 hours, and the yield of 1-acetylpiperazine was 53.47% and the yield of 1,4-diacetylpiperazine was 11.86% (see Figure 1 for gas phase detection results). 1-Acetylpiperazine is a synthetic precursor of 1,4-diacetylpiperazine. Piperazine first undergoes the first step of acetylation to generate 1-acetylpiperazine, and then undergoes the second step of acetylation to generate 1,4-diacetylpiperazine.
产率计算公式如下:The yield calculation formula is as follows:
1-乙酰哌嗪产率=(1-乙酰哌嗪产量/1-乙酰哌嗪物质的量)/底物哌嗪的物质的量×100%1-Acetylpiperazine yield = (1-Acetylpiperazine yield / 1-Acetylpiperazine amount of substance) / amount of substrate piperazine × 100%
1,4-二乙酰哌嗪产率=(1,4-二乙酰哌嗪产量/1,4-二乙酰哌嗪物质的量)/底物哌嗪的物质的量×100%1,4-diacetylpiperazine yield = (1,4-diacetylpiperazine yield / 1,4-diacetylpiperazine amount of substance) / amount of substrate piperazine × 100%
实施例4:角质酶突变体cutinaseM2在合成1,4二乙酰哌嗪中的应用Example 4: Application of cutinase mutant cutinase M2 in the synthesis of 1,4-diacetylpiperazine
按照实施例2中的方法二获得纯化酶cutinaseM2,使用Bradford法测量蛋白浓度为8.4mg/mL。将底物哌嗪(11.6μmol,2g/L)、乙酸乙烯酯(34.8μmol)加入到N,N-二甲基甲酰胺中,加入30.0μL的cuitinaseM2重组角质酶溶液,酶终浓度为0.5mg/mL;催化体系终体积为500μL;于30℃催化反应12h,通过Agilent8890GC气相仪测定1-乙酰哌嗪产率为51.42%,1,4-二乙酰哌嗪产率为14.26%(气相检测结果图见图2)。Purified enzyme cutinase M2 was obtained according to method 2 in Example 2, and the protein concentration was measured by Bradford method to be 8.4 mg/mL. Substrate piperazine (11.6 μmol, 2 g/L) and vinyl acetate (34.8 μmol) were added to N, N-dimethylformamide, and 30.0 μL of cutinase M2 recombinant cutinase solution was added, and the final enzyme concentration was 0.5 mg/mL; the final volume of the catalytic system was 500 μL; the catalytic reaction was carried out at 30° C. for 12 h, and the yield of 1-acetylpiperazine was 51.42% and the yield of 1,4-diacetylpiperazine was 14.26% as determined by Agilent 8890GC gas phase instrument (see Figure 2 for gas phase detection results).
对比例1:Comparative Example 1:
参照实施例2所述的方法制备野生型角质酶:Prepare wild-type cutinase by referring to the method described in Example 2:
步骤1:将野生型Aspergillusoryzae角质酶修饰的质粒pET-28a-Aspergillusoryzae导入大肠杆菌BL21中,LB-kana液体培养基于37℃条件下培养至OD600于0.6至0.8之间,加入终浓度0.5mM的IPTG,于16℃温度下诱导16h;离心条件为:4℃、8000rpm条件下离心5min;使用PBS离心洗涤菌体,重悬,得到重组大肠杆菌悬浮液。Step 1: The wild-type Aspergillus oryzae cutinase-modified plasmid pET-28a-Aspergillus oryzae was introduced into Escherichia coli BL21, cultured in LB-kana liquid medium at 37°C until OD 600 was between 0.6 and 0.8, added IPTG with a final concentration of 0.5 mM, and induced at 16°C for 16 hours; the centrifugation conditions were: centrifugation at 4°C and 8000 rpm for 5 minutes; the bacteria were washed by centrifugation with PBS, and resuspended to obtain a recombinant Escherichia coli suspension.
步骤2:使用高压细胞破碎仪将菌体破碎,并于4℃、13500rpm条件下离心30min,舍弃沉淀,得到粗酶液。Step 2: Use a high-pressure cell disruptor to disrupt the bacteria and centrifuge at 4°C and 13,500 rpm for 30 min. Discard the precipitate to obtain a crude enzyme solution.
步骤3:使用5个柱体积的BindingBuffer平衡镍柱,粗酶液反复上样三次,使用5个柱体积的WashingBuffer冲洗杂蛋白,使用3个柱体积的ElutionBuffer收集目标蛋白,最终得到野生型Aspergillusoryzae角质酶,使用Bradford法测量蛋白浓度为3.2mg/mL。Step 3: Use 5 column volumes of Binding Buffer to equilibrate the nickel column, repeatedly load the crude enzyme solution three times, use 5 column volumes of Washing Buffer to wash away the impurities, and use 3 column volumes of Elution Buffer to collect the target protein. Finally, the wild-type Aspergillus oryzae cutinase was obtained. The protein concentration was measured by Bradford method and was 3.2 mg/mL.
将底物哌嗪(11.6μmol,2g/L)、乙酸乙烯酯(34.8μmol)加入到N,N-二甲基甲酰胺中,加入78.8μL的野生型Aspergillusoryzae角质酶溶液,酶终浓度为0.5mg/mL;催化体系终体积为500μL;于30℃催化反应12h,通过Agilent8890GC气相仪测定1-乙酰哌嗪、1,4-二乙酰哌嗪的产率分别为48.94%、1.93%。The substrate piperazine (11.6 μmol, 2 g/L) and vinyl acetate (34.8 μmol) were added to N,N-dimethylformamide, and 78.8 μL of wild-type Aspergillus oryzae cutinase solution was added, and the final enzyme concentration was 0.5 mg/mL; the final volume of the catalytic system was 500 μL; the catalytic reaction was carried out at 30°C for 12 hours, and the yields of 1-acetylpiperazine and 1,4-diacetylpiperazine were determined by Agilent 8890GC gas chromatograph to be 48.94% and 1.93%, respectively.
该对比例还设置了空白组,空白组为将底物哌嗪(11.6μmol,2g/L)、乙酸乙烯酯(34.8μmol)加入到N,N-二甲基甲酰胺中;空白组加入30μLPBS缓冲液;体系终体积为500μL;于30℃催化反应12h,通过Agilent8890GC气相仪测定1-乙酰哌嗪、1,4-二乙酰哌嗪的产率分别为42.91%、3.83%。A blank group was also set up in this comparative example, in which substrate piperazine (11.6 μmol, 2 g/L) and vinyl acetate (34.8 μmol) were added to N,N-dimethylformamide; 30 μL PBS buffer was added to the blank group; the final volume of the system was 500 μL; the catalytic reaction was carried out at 30° C. for 12 h, and the yields of 1-acetylpiperazine and 1,4-diacetylpiperazine were determined by Agilent 8890GC gas chromatograph to be 42.91% and 3.83%, respectively.
由对照组和对比例1获得的数据可知,相比于空白组,对照组的1,4-二乙酰哌嗪的产率更低,由于哌嗪与乙酸乙烯酯会自发进行乙酰化反应,生成1-乙酰哌嗪、1,4-二乙酰哌嗪,因此上述结果表明野生型角质酶对1,4-二乙酰哌嗪没有明显的催化乙酰化效果。From the data obtained from the control group and Comparative Example 1, it can be seen that compared with the blank group, the yield of 1,4-diacetylpiperazine in the control group is lower. Since piperazine and vinyl acetate spontaneously undergo acetylation reaction to generate 1-acetylpiperazine and 1,4-diacetylpiperazine, the above results indicate that the wild-type cutinase has no obvious catalytic acetylation effect on 1,4-diacetylpiperazine.
由实施例3、实施例4和对比例1获得的数据可得,相对于空白组、未突变组,重组突变角质酶对双转乙酰产物1,4-二乙酰哌嗪的产率具有明显的提高效果。From the data obtained in Example 3, Example 4 and Comparative Example 1, it can be seen that, compared with the blank group and the non-mutated group, the recombinant mutant cutinase has a significant effect on improving the yield of the double transacetyl product 1,4-diacetylpiperazine.
实施例5:利用角质酶突变体cutinaseM1合成1,4二乙酰哌嗪Example 5: Synthesis of 1,4-diacetylpiperazine using the cutinase mutant cutinaseM1
步骤1:将cuitinaseM1修饰的质粒pET-28a-cutinaseM1导入大肠杆菌BL21中,LB-kana液体培养基于37℃条件下培养至OD600于0.6至0.8之间,加入终浓度0.5mM的IPTG,于16℃温度下诱导16h;离心收集菌体,离心条件为:4℃、8000rpm条件下离心5min;使用PBS离心洗涤菌体,重悬,得到重组大肠杆菌悬浮液。Step 1: Introduce the cutinaseM1-modified plasmid pET-28a-cutinaseM1 into Escherichia coli BL21, culture in LB-kana liquid medium at 37°C until OD600 is between 0.6 and 0.8, add IPTG with a final concentration of 0.5mM, and induce at 16°C for 16h; collect the cells by centrifugation, the centrifugation conditions are: 4°C, 8000rpm for 5min; wash the cells by centrifugation with PBS, resuspend them, and obtain a recombinant Escherichia coli suspension.
步骤2:使用高压细胞破碎仪将菌体破碎,并于4℃、13500rpm条件下离心30min,舍弃沉淀,得到粗酶液。Step 2: Use a high-pressure cell disruptor to disrupt the bacteria and centrifuge at 4°C and 13,500 rpm for 30 min. Discard the precipitate to obtain a crude enzyme solution.
步骤3:使用5个柱体积的BindingBuffer平衡镍柱,粗酶液反复上样三次,使用5个柱体积的WashingBuffer冲洗杂蛋白,使用3个柱体积的ElutionBuffer收集目标蛋白,最终得到纯化酶cutinaseM1,使用Bradford法测量蛋白浓度为12.5mg/mL。Step 3: Use 5 column volumes of Binding Buffer to equilibrate the nickel column, repeatedly load the crude enzyme solution three times, use 5 column volumes of Washing Buffer to wash away the impurities, and use 3 column volumes of Elution Buffer to collect the target protein. Finally, the purified enzyme cutinase M1 was obtained. The protein concentration was measured by Bradford method and was 12.5 mg/mL.
步骤4:将底物哌嗪(8.7μmol,0.75g/L)、乙酸乙烯酯(26.1μmol)加入到N,N-二甲基甲酰胺中,加入80μL的cuitinaseM1重组角质酶溶液,酶终浓度为1.0mg/mL;催化体系终体积为1000μL;于30℃催化反应12h,通过Agilent8890GC气相仪测定1-乙酰哌嗪产率为46.72%,1,4-二乙酰哌嗪产率为9.11%。Step 4: Add the substrate piperazine (8.7 μmol, 0.75 g/L) and vinyl acetate (26.1 μmol) to N,N-dimethylformamide, add 80 μL of cuitinaseM1 recombinant cutinase solution, and the final enzyme concentration is 1.0 mg/mL; the final volume of the catalytic system is 1000 μL; the catalytic reaction is carried out at 30° C. for 12 h, and the yield of 1-acetylpiperazine is 46.72% and the yield of 1,4-diacetylpiperazine is 9.11% as determined by Agilent 8890GC gas chromatograph.
实施例6:利用角质酶突变体cutinaseM2合成1,4二乙酰哌嗪Example 6: Synthesis of 1,4-diacetylpiperazine using the cutinase mutant cutinaseM2
步骤1:将cuitinaseM2修饰的质粒pET-28a-cutinaseM2导入大肠杆菌BL21中,LB-kana液体培养基于37℃条件下培养至OD600于0.6至0.8之间,加入终浓度0.5mM的IPTG,于16℃温度下诱导16h;离心收集菌体,离心条件为:4℃、8000rpm条件下离心5min;使用PBS离心洗涤菌体,重悬,得到重组大肠杆菌悬浮液。Step 1: Introduce the cutinaseM2-modified plasmid pET-28a-cutinaseM2 into Escherichia coli BL21, culture in LB-kana liquid medium at 37°C until OD600 is between 0.6 and 0.8, add IPTG with a final concentration of 0.5mM, and induce at 16°C for 16h; collect the cells by centrifugation, the centrifugation conditions are: 4°C, 8000rpm for 5min; wash the cells by centrifugation with PBS, resuspend them, and obtain a recombinant Escherichia coli suspension.
步骤2:使用高压细胞破碎仪将菌体破碎,并于4℃、13500rpm条件下离心30min,舍弃沉淀,得到粗酶液。Step 2: Use a high-pressure cell disruptor to disrupt the bacteria and centrifuge at 4°C and 13,500 rpm for 30 min. Discard the precipitate to obtain a crude enzyme solution.
步骤3:使用5个柱体积的BindingBuffer平衡镍柱,粗酶液反复上样三次,使用5个柱体积的WashingBuffer冲洗杂蛋白,使用3个柱体积的ElutionBuffer收集目标蛋白,最终得到纯化酶cutinaseM2,使用Bradford法测量蛋白浓度为15.9mg/mL。Step 3: Use 5 column volumes of Binding Buffer to equilibrate the nickel column, repeatedly load the crude enzyme solution three times, use 5 column volumes of Washing Buffer to wash away the impurities, and use 3 column volumes of Elution Buffer to collect the target protein. Finally, the purified enzyme cutinase M2 was obtained. The protein concentration was measured by Bradford method and was 15.9 mg/mL.
步骤4:将底物哌嗪(8.7μmol,0.75g/L)、乙酸乙烯酯(26.1μmol)加入到N,N-二甲基甲酰胺中,加入62.8μL的cuitinaseM2重组角质酶溶液,酶终浓度为1.0mg/mL;催化体系终体积为1000μL;于30℃催化反应12h,通过Agilent8890GC气相仪测定1-乙酰哌嗪产率为53.55%,1,4-二乙酰哌嗪产率为15.14%。Step 4: Add the substrate piperazine (8.7 μmol, 0.75 g/L) and vinyl acetate (26.1 μmol) to N,N-dimethylformamide, add 62.8 μL of cuitinaseM2 recombinant cutinase solution, and the final enzyme concentration is 1.0 mg/mL; the final volume of the catalytic system is 1000 μL; the catalytic reaction is carried out at 30° C. for 12 h, and the yield of 1-acetylpiperazine is 53.55% and the yield of 1,4-diacetylpiperazine is 15.14% as determined by Agilent 8890GC gas chromatograph.
实施例7:利用角质酶突变体cutinaseM2合成1,4二乙酰哌嗪Example 7: Synthesis of 1,4-diacetylpiperazine using the cutinase mutant cutinaseM2
步骤1:将cuitinaseM2修饰的质粒pET-28a-cutinaseM2导入大肠杆菌BL21中,LB-kana液体培养基于37℃条件下培养至OD600于0.6至0.8之间,加入终浓度0.5mM的IPTG,于16℃温度下诱导16h;离心获得菌体,离心条件为:4℃、8000rpm条件下离心5min;使用PBS离心洗涤菌体,重悬,得到重组大肠杆菌悬浮液。Step 1: Introduce the cutinaseM2-modified plasmid pET-28a-cutinaseM2 into Escherichia coli BL21, culture in LB-kana liquid medium at 37°C until OD600 is between 0.6 and 0.8, add IPTG with a final concentration of 0.5mM, and induce at 16°C for 16h; obtain the cells by centrifugation, the centrifugation conditions are: 4°C, 8000rpm for 5min; wash the cells by centrifugation with PBS, resuspend them, and obtain a recombinant Escherichia coli suspension.
步骤2:使用高压细胞破碎仪将菌体破碎,并于4℃、13500rpm条件下离心30min,舍弃沉淀,得到粗酶液。Step 2: Use a high-pressure cell disruptor to disrupt the bacteria and centrifuge at 4°C and 13,500 rpm for 30 min. Discard the precipitate to obtain a crude enzyme solution.
步骤3:使用5个柱体积的BindingBuffer平衡镍柱,粗酶液反复上样三次,使用5个柱体积的WashingBuffer冲洗杂蛋白,使用3个柱体积的ElutionBuffer收集目标蛋白,最终得到纯化酶cutinaseM2,使用Bradford法测量蛋白浓度为15.9mg/mL。Step 3: Use 5 column volumes of Binding Buffer to equilibrate the nickel column, repeatedly load the crude enzyme solution three times, use 5 column volumes of Washing Buffer to wash away the impurities, and use 3 column volumes of Elution Buffer to collect the target protein. Finally, the purified enzyme cutinase M2 was obtained. The protein concentration was measured by Bradford method and was 15.9 mg/mL.
步骤4:将底物哌嗪(8.7μmol,0.75g/L)、乙酸乙烯酯(26.1μmol)加入到N,N-二甲基甲酰胺中,加入62.8μL的cuitinaseM2重组角质酶溶液,酶终浓度为1.0mg/mL;催化体系终体积为1000μL;于40℃催化反应12h,通过Agilent8890GC气相仪测定1-乙酰哌嗪产率为45.49%,1,4-二乙酰哌嗪产率为18.55%。Step 4: Add substrate piperazine (8.7 μmol, 0.75 g/L) and vinyl acetate (26.1 μmol) to N,N-dimethylformamide, add 62.8 μL of cuitinaseM2 recombinant cutinase solution, and the final enzyme concentration is 1.0 mg/mL; the final volume of the catalytic system is 1000 μL; the catalytic reaction is carried out at 40° C. for 12 h, and the yield of 1-acetylpiperazine is 45.49% and the yield of 1,4-diacetylpiperazine is 18.55% as determined by Agilent 8890GC gas chromatograph.
实施例8:利用角质酶突变体cutinaseM2合成1,4二乙酰哌嗪Example 8: Synthesis of 1,4-diacetylpiperazine using the cutinase mutant cutinaseM2
步骤1:将cuitinaseM2修饰的质粒pET-28a-cutinaseM2导入大肠杆菌BL21中,LB-kana液体培养基于37℃条件下培养至OD600于0.6至0.8之间,加入终浓度0.5mM的IPTG,于16℃温度下诱导16h;离心收集菌体,离心条件为:4℃、8000rpm条件下离心5min;使用PBS离心洗涤菌体,重悬,得到重组大肠杆菌悬浮液。Step 1: Introduce the cutinaseM2-modified plasmid pET-28a-cutinaseM2 into Escherichia coli BL21, culture in LB-kana liquid medium at 37°C until OD600 is between 0.6 and 0.8, add IPTG with a final concentration of 0.5mM, and induce at 16°C for 16h; collect the cells by centrifugation, the centrifugation conditions are: 4°C, 8000rpm for 5min; wash the cells by centrifugation with PBS, resuspend them, and obtain a recombinant Escherichia coli suspension.
步骤2:使用高压细胞破碎仪将菌体破碎,并于4℃、13500rpm条件下离心30min,舍弃沉淀,得到粗酶液。Step 2: Use a high-pressure cell disruptor to disrupt the bacteria and centrifuge at 4°C and 13,500 rpm for 30 min. Discard the precipitate to obtain a crude enzyme solution.
步骤3:使用5个柱体积的BindingBuffer平衡镍柱,粗酶液反复上样三次,使用5个柱体积的WashingBuffer冲洗杂蛋白,使用3个柱体积的ElutionBuffer收集目标蛋白,最终得到纯化酶cutinaseM2,使用Bradford法测量蛋白浓度为15.9mg/mL。Step 3: Use 5 column volumes of Binding Buffer to equilibrate the nickel column, repeatedly load the crude enzyme solution three times, use 5 column volumes of Washing Buffer to wash away the impurities, and use 3 column volumes of Elution Buffer to collect the target protein. Finally, the purified enzyme cutinase M2 was obtained. The protein concentration was measured by Bradford method and was 15.9 mg/mL.
步骤4:将底物哌嗪(8.7μmol,0.75g/L)、乙酸乙烯酯(26.1μmol)加入到乙酸乙酯中,加入62.8μL的cuitinaseM2重组角质酶溶液,酶终浓度为1.0mg/mL;催化体系终体积为1000μL;于40℃催化反应12h,通过Agilent8890GC气相仪测定1-乙酰哌嗪产率为60.25%,1,4-二乙酰哌嗪产率为13.61%。Step 4: Add substrate piperazine (8.7 μmol, 0.75 g/L) and vinyl acetate (26.1 μmol) to ethyl acetate, add 62.8 μL of cuitinase M2 recombinant cutinase solution, and the final enzyme concentration is 1.0 mg/mL; the final volume of the catalytic system is 1000 μL; the catalytic reaction is carried out at 40° C. for 12 h, and the yield of 1-acetylpiperazine is 60.25% and the yield of 1,4-diacetylpiperazine is 13.61% as determined by Agilent 8890GC gas chromatograph.
虽然本发明已以较佳的实施例公开如上,但其并非用以限定本发明,任何熟悉此技术的人,在不脱离本发明精神和范围内,都可以做各种的改动与修饰,因此,本发明的保护范围应该以权利要求书所界定的为准。Although the present invention has been disclosed as above in the form of preferred embodiments, it is not intended to limit the present invention. Anyone familiar with this technology can make various changes and modifications without departing from the spirit and scope of the present invention. Therefore, the scope of protection of the present invention should be based on the definition of the claims.
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