CN102191287B - Cis-fermentation preparation method of lysine - Google Patents
Cis-fermentation preparation method of lysine Download PDFInfo
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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Abstract
Description
技术领域 technical field
本发明属于氨基酸发酵领域,具体而言,本发明涉及L-赖氨酸的发酵方法,其包括将编码吡啶核苷酸转氢酶变体的多核苷酸导入产L-赖氨酸的菌,从而使所获得的菌表达所述吡啶核苷酸转氢酶变体;和在发酵条件下培养获得的菌。另外,本发明还提供了所述发酵方法中所用的中间产物,和利用所述发酵方法进一步生产产品等。The invention belongs to the field of amino acid fermentation, in particular, the invention relates to a fermentation method of L-lysine, which comprises introducing a polynucleotide encoding a variant of pyridine nucleotide transhydrogenase into an L-lysine-producing bacterium, Thereby making the obtained bacteria express the pyridine nucleotide transhydrogenase variant; and cultivating the obtained bacteria under fermentation conditions. In addition, the present invention also provides intermediate products used in the fermentation method, and further products produced by the fermentation method.
背景技术 Background technique
L-赖氨酸是重要的氨基酸原料,可以作为调味品、食品、饲料添加剂使用,也可以作为保健品、药品中的有效或辅料成分,广泛应用于食品业、饲料业、制药业及其他化学工业中。当前,L-赖氨酸的生产主要是通过微生物的发酵生产的,如可以利用棒状杆菌生产。L-lysine is an important amino acid raw material, which can be used as condiment, food, feed additive, and also as an effective or auxiliary ingredient in health care products and medicines. It is widely used in food industry, feed industry, pharmaceutical industry and other chemical industries. in industry. At present, the production of L-lysine is mainly produced by fermentation of microorganisms, such as coryneform bacteria.
用于发酵生产的微生物可以是野生型微生物,但是更多的是通过诱变或基因工程获得的产量更高的营养缺陷型、耐药变异型和代谢变异型微生物。对于基因工程获得的性状改良的微生物来说,其中至关重要的就是性质优异的基因。The microorganisms used for fermentation production can be wild-type microorganisms, but most of them are auxotrophs, drug-resistant mutants and metabolic mutants with higher yields obtained through mutagenesis or genetic engineering. For the microorganisms with improved traits obtained by genetic engineering, the most important thing is the genes with excellent properties.
吡啶核苷酸转氢酶是L-赖氨酸代谢途径上重要的酶。尽管野生型吡啶核苷酸转氢酶的亚基已经被公开(可参见NCBI(http://www.ncbi.nlm.nih.gov)蛋白和基因登录号NP416120.1和AAC74674.1;也可参见中国专利ZL94194707),但是该酶变体的研究却没有报道。Pyridine nucleotide transhydrogenase is an important enzyme in the metabolic pathway of L-lysine. Although subunits of wild-type pyridine nucleotide transhydrogenase have been published (see NCBI (http://www.ncbi.nlm.nih.gov) protein and gene accession numbers NP416120.1 and AAC74674.1; See Chinese Patent ZL94194707), but the research on this enzyme variant has not been reported.
本发明人经过长期艰苦研究,令人意外地发现了新的吡啶核苷酸转氢酶,其显著提高了相应酶的活性,在导入工程菌发酵的时候也获得了更高的赖氨酸产量。After long-term arduous research, the inventor unexpectedly discovered a new pyridine nucleotide transhydrogenase, which significantly improved the activity of the corresponding enzyme, and also obtained higher lysine production when it was introduced into engineering bacteria for fermentation .
发明内容 Contents of the invention
本发明要解决的技术问题在于提供L-赖氨酸的发酵方法,其包括将编码吡啶核苷酸转氢酶变体的多核苷酸导入产L-赖氨酸的菌,从而使所获得的菌表达所述吡啶核苷酸转氢酶变体,其中所述吡啶核苷酸转氢酶变体相对于野生型吡啶核苷酸转氢酶的活性提高。另外,本发明还提供了所述发酵方法中所用的中间产物,和利用所述发酵方法进一步生产产品等The technical problem to be solved by the present invention is to provide a fermentation method for L-lysine, which includes introducing a polynucleotide encoding a pyridine nucleotide transhydrogenase variant into an L-lysine-producing bacterium, so that the obtained bacteria expressing the pyridine nucleotide transhydrogenase variant, wherein the activity of the pyridine nucleotide transhydrogenase variant is increased relative to the wild-type pyridine nucleotide transhydrogenase. In addition, the present invention also provides the intermediate product used in the fermentation method, and the further production of products using the fermentation method, etc.
具体而言,在第一方面,本发明提供了L-赖氨酸的发酵方法,其包括:Specifically, in the first aspect, the present invention provides a fermentation method of L-lysine, which includes:
(1)将编码吡啶核苷酸转氢酶变体的多核苷酸导入产L-赖氨酸的菌,从而使所获得的菌表达所述吡啶核苷酸转氢酶变体,其中所述吡啶核苷酸转氢酶变体相对于野生型吡啶核苷酸转氢酶的活性提高;和(1) Introducing polynucleotides encoding pyridine nucleotide transhydrogenase variants into L-lysine-producing bacteria, so that the obtained bacteria express the pyridine nucleotide transhydrogenase variants, wherein the The pyridine nucleotide transhydrogenase variant has increased activity relative to wild-type pyridine nucleotide transhydrogenase; and
(2)在发酵条件下培养步骤(1)获得的菌。(2) Cultivate the bacteria obtained in step (1) under fermentation conditions.
其中,野生型吡啶核苷酸转氢酶是本领域技术人员所知晓的,包括α亚基和β亚基,其中α亚基和β亚基的序列分别如NCBI(http://www.ncbi.nlm.nih.gov)蛋白和基因登录号NP416120.1和AAC74674.1所示。酶活性的测定方法是现有已知的,如可以采用本发明具体实施方式中所述的方法来测定酶活性,这样就可以确认吡啶核苷酸转氢酶变体的活性是否有提高。Wherein, the wild-type pyridine nucleotide transhydrogenase is known to those skilled in the art, including α subunit and β subunit, wherein the sequences of α subunit and β subunit are respectively as in NCBI (http://www.ncbi .nlm.nih.gov) protein and gene accession numbers NP416120.1 and AAC74674.1. The methods for measuring enzyme activity are known in the art. For example, the method described in the specific embodiments of the present invention can be used to measure enzyme activity, so that it can be confirmed whether the activity of the pyridine nucleotide transhydrogenase variant is improved.
优选本发明第一方面的发酵方法中,所述多核苷酸依次编码吡啶核苷酸转氢酶α亚基变体和吡啶核苷酸转氢酶β亚基变体,即编码吡啶核苷酸转氢酶α亚基变体的多核苷酸位于编码吡啶核苷酸转氢酶β亚基变体的多核苷酸的上游。在本发明的具体实施方式中,所述多核苷酸的核苷酸序列如SEQ ID No:1所示。Preferably, in the fermentation method of the first aspect of the present invention, the polynucleotide sequentially encodes a pyridine nucleotide transhydrogenase α subunit variant and a pyridine nucleotide transhydrogenase β subunit variant, that is, encodes a pyridine nucleotide The polynucleotide for the transhydrogenase alpha subunit variant is located upstream of the polynucleotide encoding the pyridine nucleotide transhydrogenase beta subunit variant. In a specific embodiment of the present invention, the nucleotide sequence of the polynucleotide is shown in SEQ ID No: 1.
其中,所述吡啶核苷酸转氢酶α亚基变体在M102、L127或Q322的位置上被其他天然氨基酸替换,优选替换选自M102L、L127R和Q322K,最优选其氨基酸序列如SEQ ID No:2所示。本领域技术人员可以根据吡啶核苷酸转氢酶α亚基变体的氨基酸序列推导出其编码核苷酸序列,优选是密码子优化的核苷酸序列,如针对发酵所用的菌密码子使用情况优化的。在本发明的具体实施方式中,所述吡啶核苷酸转氢酶α亚基变体由如SEQ ID No:3所示的多核苷酸编码。Wherein, the pyridine nucleotide transhydrogenase α subunit variant is replaced by other natural amino acids at the position of M102, L127 or Q322, preferably replaced by M102L, L127R and Q322K, most preferably its amino acid sequence such as SEQ ID No : 2 shown. Those skilled in the art can deduce its encoding nucleotide sequence based on the amino acid sequence of the pyridine nucleotide transhydrogenase α subunit variant, preferably a codon-optimized nucleotide sequence, such as the codon usage of bacteria used for fermentation Situation optimized. In a specific embodiment of the present invention, the variant of the alpha subunit of pyridine nucleotide transhydrogenase is encoded by a polynucleotide as shown in SEQ ID No: 3.
另外,其中所述吡啶核苷酸转氢酶β亚基变体在A398或D400的位置上被其他天然氨基酸替换,优选替换选自A398S和D400H,最优选其氨基酸序列如SEQ ID No:4所示。本领域技术人员可以根据吡啶核苷酸转氢酶α亚基变体的氨基酸序列推导出其编码核苷酸序列,优选是密码子优化的核苷酸序列,如针对发酵所用的菌密码子使用情况优化的。在本发明的具体实施方式中,所述吡啶核苷酸转氢酶β亚基变体由如SEQ ID No:5所示的多核苷酸编码。In addition, wherein the pyridine nucleotide transhydrogenase β subunit variant is replaced by other natural amino acids at the position of A398 or D400, preferably the replacement is selected from A398S and D400H, most preferably its amino acid sequence is as shown in SEQ ID No: 4 Show. Those skilled in the art can deduce its encoding nucleotide sequence based on the amino acid sequence of the pyridine nucleotide transhydrogenase α subunit variant, preferably a codon-optimized nucleotide sequence, such as the codon usage of bacteria used for fermentation Situation optimized. In a specific embodiment of the present invention, the variant of the beta subunit of pyridine nucleotide transhydrogenase is encoded by a polynucleotide as shown in SEQ ID No:5.
所述多核苷酸可以通过各种本领域技术人员所熟知的方式被导入产L-赖氨酸的菌,只要能够使产L-赖氨酸的菌表达所述吡啶核苷酸转氢酶变体即可。所述多核苷酸可以直接被导入,例如利用微粒体、基因枪等导入细胞;也可以间接被导入,例如可以通过构建在质粒载体上导入细胞。导入的所述多核苷酸可以整合在细胞的基因组上表达,也可以游离表达。通常,由于产L-赖氨酸的菌本身不适于作为克隆宿主菌,因此优选所述多核苷酸是通过穿梭质粒导入产L-赖氨酸的菌的。其中,所述穿梭质粒优选是大肠杆菌和产L-赖氨酸的菌的穿梭质粒。这样便能够很方便地在大肠杆菌宿主中进行DNA重组操作。The polynucleotide can be introduced into the L-lysine-producing bacteria by various methods well known to those skilled in the art, as long as the L-lysine-producing bacteria can express the pyridine nucleotide transhydrogenase Just body. The polynucleotide can be introduced directly, for example, into cells by microsomes, gene guns, etc.; it can also be introduced indirectly, for example, it can be introduced into cells by constructing it on a plasmid vector. The introduced polynucleotide can be integrated and expressed in the genome of the cell, or can be expressed freely. Usually, since the L-lysine-producing bacteria itself is not suitable as a cloning host, it is preferred that the polynucleotide is introduced into the L-lysine-producing bacteria through a shuttle plasmid. Wherein, the shuttle plasmid is preferably a shuttle plasmid of Escherichia coli and L-lysine-producing bacteria. In this way, DNA recombination operations can be conveniently performed in E. coli hosts.
产L-赖氨酸的菌有许多种,本领域技术人员所知晓的包括埃希氏杆菌、棒状杆菌和沙雷氏杆菌,优选是棒状杆菌。在本发明的具体实施方式中,所述产L-赖氨酸的菌是Corynebacterium glutamicum。There are many kinds of L-lysine-producing bacteria, those known to those skilled in the art include Escherichia, Corynebacterium and Serratia, preferably Corynebacterium. In a specific embodiment of the present invention, the L-lysine-producing bacterium is Corynebacterium glutamicum.
优选本发明第一方面的发酵方法中,所述发酵条件的发酵温度为28-35℃,优选为29-33℃,更优选为30-32℃,如30℃。Preferably, in the fermentation method of the first aspect of the present invention, the fermentation temperature of the fermentation condition is 28-35°C, preferably 29-33°C, more preferably 30-32°C, such as 30°C.
也优选本发明第一方面的发酵方法中,所述发酵条件的培养基包含糖,NH4Cl,CaCl2,KH2PO4,蛋白胨,MgSO4,FeSO4,MnSO4,生物素,和叶酸。在本发明的具体实施方式中,所述培养基的配方为:40g蔗糖,20g NH4Cl,2g CaCl2,1gKH2PO4,1g 蛋白胨,500mg MgSO4·7H2O,15mg FeSO4·7H2O,10mgMnSO4·7H2O,200μg生物素,和50μg叶酸,pH7.3,用水补足至1升。It is also preferred that in the fermentation method of the first aspect of the present invention, the medium of the fermentation condition comprises sugar, NH 4 Cl, CaCl 2 , KH 2 PO 4 , peptone, MgSO 4 , FeSO 4 , MnSO 4 , biotin, and folic acid . In a specific embodiment of the present invention, the formula of the medium is: 40g sucrose, 20g NH 4 Cl, 2g CaCl 2 , 1gKH 2 PO 4 , 1g peptone, 500mg MgSO 4 7H 2 O, 15mg FeSO 4 7H 2 O, 10 mg MnSO 4 ·7H 2 O, 200 μg biotin, and 50 μg folic acid, pH 7.3, made up to 1 liter with water.
在第二方面,本发明提供了L-赖氨酸饲料添加剂的制备方法,其包括:In a second aspect, the present invention provides a method for preparing an L-lysine feed additive, comprising:
(1)实施本发明第一方面的发酵方法中的步骤(2);和(1) implementing step (2) in the fermentation method of the first aspect of the present invention; and
(2)收集发酵液依次进行膜分离并对滤液进行喷雾干燥;(2) collecting the fermented liquid to carry out membrane separation successively and carrying out spray drying to the filtrate;
(3)对步骤(2)喷雾干燥获得的颗粒进行筛分;(3) sieving the particles obtained by spray drying in step (2);
(4)将筛分得到的粒径大于等于1.5mm的颗粒破碎,并将其与筛分得到的粒径小于1.5mm的颗粒混合,再次进行喷雾干燥;和(4) crushing particles with a particle size greater than or equal to 1.5mm obtained through sieving, and mixing them with particles with a particle size smaller than 1.5mm obtained through sieving, and spray drying again; and
(5)对步骤(4)喷雾干燥获得的颗粒进行筛分,收集粒径小于1.5mm的颗粒。(5) Sieve the particles obtained by spray drying in step (4), and collect particles with a particle diameter less than 1.5 mm.
其中,为了使最终颗粒饲料添加剂的形状更为均匀,流化床干燥机内尾气温度不宜过高,通常不应高于85℃,优选保持在80±3℃。Among them, in order to make the shape of the final granular feed additive more uniform, the temperature of the tail gas in the fluidized bed dryer should not be too high, usually not higher than 85°C, preferably kept at 80±3°C.
本发明第二方面的制备方法还可以在实施本发明第一方面的发酵方法中的步骤(2)之前,包括实施本发明第一方面的发酵方法中的步骤(1)。但是,这通常不是优选的,因此本发明第二方面的制备方法不包括实施本发明第一方面的发酵方法中的步骤(1),而包括在发酵条件下培养产L-赖氨酸的菌(尤其是高产L-赖氨酸的菌)的步骤,这也涵盖在本发明的范围内。The preparation method of the second aspect of the present invention may also include implementing step (1) of the fermentation method of the first aspect of the present invention before implementing step (2) of the fermentation method of the first aspect of the present invention. However, this is generally not preferred, so the preparation method of the second aspect of the present invention does not include implementing step (1) in the fermentation method of the first aspect of the present invention, but includes cultivating L-lysine-producing bacteria under fermentation conditions (especially high L-lysine-producing bacteria), this is also covered within the scope of the present invention.
由于本发明第二方面的制备方法已经能够生产出符合国家标准的颗粒饲料添加剂,因此优选其中不包括包衣的过程,相应可以降低成本,更便于商业推广。Since the preparation method of the second aspect of the present invention can already produce granular feed additives that meet national standards, it is preferable to not include a coating process, which can reduce costs and facilitate commercial promotion.
在第三方面,本发明提供了根据本发明得到的产品以及本发明中使用的中间产物。In a third aspect, the invention provides products obtained according to the invention and intermediates used in the invention.
具体而言,本发明提供了根据本发明第二方面的制备方法得到的L-赖氨酸饲料添加剂,优选其中不含包衣剂(如,环糊精等)。Specifically, the present invention provides the L-lysine feed additive obtained according to the preparation method of the second aspect of the present invention, preferably without coating agent (such as cyclodextrin, etc.).
另外,本发明提供了吡啶核苷酸转氢酶变体,其包括吡啶核苷酸转氢酶α亚基变体和吡啶核苷酸转氢酶β亚基变体。优选所述吡啶核苷酸转氢酶α亚基变体在M102、L127或Q322的位置上被其他天然氨基酸替换,优选替换选自M102L、L127R和Q322K,最优选其氨基酸序列如SEQ ID No:2所示。另外,也优选所述吡啶核苷酸转氢酶β亚基变体在A398或D400的位置上被其他天然氨基酸替换,优选替换选自A398S和D400H,最优选其氨基酸序列如SEQ ID No:4所示。本发明还分别提供了上述吡啶核苷酸转氢酶α亚基变体和吡啶核苷酸转氢酶β亚基变体。In addition, the present invention provides pyridine nucleotide transhydrogenase variants, which include pyridine nucleotide transhydrogenase α subunit variants and pyridine nucleotide transhydrogenase β subunit variants. Preferably, the pyridine nucleotide transhydrogenase α subunit variant is replaced by other natural amino acids at the position of M102, L127 or Q322, preferably the replacement is selected from M102L, L127R and Q322K, most preferably its amino acid sequence is as SEQ ID No: 2. In addition, it is also preferred that the pyridine nucleotide transhydrogenase beta subunit variant is replaced by other natural amino acids at the position of A398 or D400, preferably the replacement is selected from A398S and D400H, most preferably its amino acid sequence is as shown in SEQ ID No: 4 shown. The present invention also provides the above-mentioned pyridine nucleotide transhydrogenase α subunit variants and pyridine nucleotide transhydrogenase β subunit variants respectively.
相应地,本发明提供了编码吡啶核苷酸转氢酶变体的多核苷酸,即顺序编码吡啶核苷酸转氢酶α亚基变体和吡啶核苷酸转氢酶β亚基变体的多核苷酸,优选其核苷酸序列如SEQ ID No:1所示。本发明还分别提供了编码上述吡啶核苷酸转氢酶α亚基变体和吡啶核苷酸转氢酶β亚基变体的多核苷酸,优选它们的核苷酸序列分别如SEQ ID No:3和5所示。Correspondingly, the present invention provides polynucleotides encoding pyridine nucleotide transhydrogenase variants, that is, sequentially encoding pyridine nucleotide transhydrogenase α subunit variants and pyridine nucleotide transhydrogenase β subunit variants The polynucleotide, preferably its nucleotide sequence is as shown in SEQ ID No: 1. The present invention also provides polynucleotides encoding the above-mentioned pyridine nucleotide transhydrogenase α subunit variants and pyridine nucleotide transhydrogenase β subunit variants, preferably their nucleotide sequences are respectively as SEQ ID No : 3 and 5.
本发明具有以下有益效果:赖氨酸的发酵产量得到有效提高;发酵液质量稳定;变体酶与野生型酶结构差异不大,都可以顺利降解,无安全隐患;发酵液可以直接用于生产颗粒饲料添加剂;生产颗粒饲料添加剂的步骤简便,无需引入包衣剂即可达到国家标准的要求。The invention has the following beneficial effects: the fermentation yield of lysine is effectively improved; the quality of the fermentation liquid is stable; the structural difference between the variant enzyme and the wild-type enzyme is not large, and both can be degraded smoothly without potential safety hazard; the fermentation liquid can be directly used in production Granular feed additive: The steps of producing granular feed additive are simple, and the requirements of national standards can be met without the introduction of coating agents.
为了便于理解,以下将通过具体的实施例对本发明进行详细地描述。需要特别指出的是,这些描述仅仅是示例性的描述,并不构成对本发明范围的限制。依据本说明书的论述,本发明的许多变化、改变对所属领域技术人员来说都是显而易见的。In order to facilitate understanding, the present invention will be described in detail below through specific examples. It should be pointed out that these descriptions are only exemplary descriptions and do not limit the scope of the present invention. Many variations and modifications of the present invention will be apparent to those skilled in the art from the discussion of this specification.
另外,本发明引用了公开文献,这些文献是为了更清楚地描述本发明,它们的全文内容均纳入本文进行参考,就好像它们的全文已经在本文中重复叙述过一样。In addition, the present invention refers to published documents, which are for the purpose of more clearly describing the present invention, the entire contents of which are incorporated herein by reference as if they had been recited herein in their entirety.
具体实施方式 Detailed ways
以下通过实施例进一步说明本发明的内容。如未特别指明,实施例中所用的技术手段为本领域技术人员所熟知的常规手段和市售的常用仪器、试剂,可参见《分子克隆实验指南(第3版)》(科学出版社)、《微生物学实验(第4版)》(高等教育出版社)以及相应仪器和试剂的厂商说明书等参考。The content of the present invention is further illustrated below by way of examples. If not otherwise specified, the technical means used in the examples are conventional means well known to those skilled in the art and commercially available common instruments and reagents, which can be found in "Molecular Cloning Experiment Guide (3rd Edition)" (Science Press), "Microbiological Experiments (4th Edition)" (Higher Education Press) and the manufacturer's instructions of corresponding instruments and reagents.
实施例1吡啶核苷酸转氢酶变体基因构建体的制备The preparation of embodiment 1 pyridine nucleotide transhydrogenase variant gene construct
根据我们设计的序列,通过商业途径委托上海生工生物技术有限公司合成编码两个吡啶核苷酸转氢酶亚基变体的吡啶核苷酸转氢酶变体基因构建体并构建入大肠杆菌-棒状杆菌穿梭质粒pMS2(可购自美国典型微生物保藏中心(ATCC),商品编号ATCC 67189)中。克隆过程参照《分子克隆实验指南》以及所用商品化试剂的操作指南进行,简要过程如下:According to the sequence we designed, Shanghai Sangon Biotechnology Co., Ltd. was commissioned to synthesize a pyridine nucleotide transhydrogenase variant gene construct encoding two pyridine nucleotide transhydrogenase subunit variants through commercial channels and constructed it into Escherichia coli - The Corynebacterium shuttle plasmid pMS2 (available from the American Type Microorganisms Collection (ATCC), item number ATCC 67189). The cloning process was carried out according to the "Molecular Cloning Experiment Guide" and the operation guide of the commercial reagents used. The brief process is as follows:
通过DNA自动合成仪,合成吡啶核苷酸转氢酶变体基因构建体的核酸片段,用T4多核苷酸激酶(购自TaKaRa公司)将这些核酸片段的5’端进行磷酸化,然后等摩尔比混合这5个核酸片段后于65℃变性5分钟,退火降温至16℃,加入T4DNA连接酶(购自TaKaRa公司)连接12小时。然后,取1μL上述连接产物在50μL反应体积中进行PCR扩增,其中正向引物如序列表的SEQ ID No:6所示(引入了EcoR I内切酶位点)、反向引物如序列表的SEQ ID No:7所示(引入了Xba I内切酶位点),反应条件为:以94℃变性4分钟,然后以94℃变性30秒、63℃退火60秒并72℃延伸30秒进行35个循环,最后以72℃延伸4分钟并降温至4℃。The nucleic acid fragments of the pyridine nucleotide transhydrogenase variant gene construct were synthesized by an automatic DNA synthesizer, and the 5' ends of these nucleic acid fragments were phosphorylated with T4 polynucleotide kinase (purchased from TaKaRa Company), and then equimolar After mixing the 5 nucleic acid fragments, denature at 65°C for 5 minutes, anneal and cool down to 16°C, and add T4 DNA ligase (purchased from TaKaRa Company) for 12 hours of ligation. Then, take 1 μL of the above ligation product and carry out PCR amplification in a 50 μL reaction volume, wherein the forward primer is shown in SEQ ID No: 6 of the sequence listing (the EcoR I endonuclease site is introduced), and the reverse primer is as shown in the sequence listing The SEQ ID No: 7 (introduced the Xba I endonuclease site), the reaction conditions are: denaturation at 94°C for 4 minutes, then denaturation at 94°C for 30 seconds, annealing at 63°C for 60 seconds and extension at 72°C for 30 seconds 35 cycles were performed, with a final extension at 72°C for 4 minutes and cooling to 4°C.
琼脂糖凝胶电泳上述PCR产物,回收约2.9kb大小的片段,用EcoR I和Xba I双酶切该片段,并与经这两个内切酶酶切的pMS2质粒用T4DNA连接酶进行连接,转化入大肠杆菌Top10F’中。挑出阳性克隆,抽提出其中的质粒,经测序验证,相应核苷酸序列如序列表的SEQ ID No:1所示,顺序编码了如SEQ ID No:2和SEQ ID No:4所示的两个吡啶核苷酸转氢酶亚基变体的完整ORF,由公司将构建好的质粒(命名为pMS2-cispnt)以及相应大肠杆菌转化株(命名为E.coli-cispnt)寄回。The above PCR product was electrophoresed on agarose gel, and a fragment of about 2.9kb size was recovered, and the fragment was double-digested with EcoR I and Xba I, and connected with the pMS2 plasmid digested by these two endonucleases with T4DNA ligase, Transformed into E. coli Top10F'. The positive clones were picked out, and the plasmids were extracted. After sequencing verification, the corresponding nucleotide sequence was shown in SEQ ID No: 1 of the sequence table, and the sequences were encoded as shown in SEQ ID No: 2 and SEQ ID No: 4. The complete ORFs of the two pyridine nucleotide transhydrogenase subunit variants will be sent back by the company with the constructed plasmid (named pMS2-cispnt) and the corresponding Escherichia coli transformant (named E.coli-cispnt).
实施例2大肠杆菌的活性测定及棒状杆菌的发酵实验The activity assay of embodiment 2 escherichia coli and the fermentation experiment of coryneform bacterium
根据现有的转氢酶活性测定方法(可参见Clarke DM等.Cloning andexpression of the transhydrogenase gene of Escherichia coli.J.Bacteriol.,162:367-373),对转化有pMS2-cispnt质粒的E.coli-cispnt菌株与作为对照的阴性Top10F’菌株分别测定转氢酶活性,发现的E.coli-cispnt菌株的酶比活性比阴性Top10F’菌株的酶比活性提高了163%,远高于现有技术中用野生型吡啶核苷酸转氢酶表达的酶比活性提高比率。According to the existing assay method for transhydrogenase activity (see Clarke DM et al. Cloning and expression of the transhydrogenase gene of Escherichia coli. J. Bacteriol., 162: 367-373), E.coli transformed with pMS2-cispnt plasmid -cispnt bacterial strain and the negative Top10F' bacterial strain as a control measure the transhydrogenase activity respectively, and the specific enzyme activity of the found E.coli-cispnt bacterial strain is 163% higher than that of the negative Top10F' bacterial strain, much higher than the prior art Enzyme specific activity increase rate with wild-type pyridine nucleotide transhydrogenase expressed in .
通过电转化法将pMS2-cispnt质粒转入L-赖氨酸发酵的棒状杆菌工程菌(可购自美国典型微生物保藏中心(ATCC),商品编号ATCC 31269)中,其简要过程是:将棒状杆菌在50mL LB液体培养基中振荡培养至OD500达到0.7,离心收集菌体,用0℃预冷的10%(V/V)甘油溶液洗涤后将菌体重悬于200μL预冷的10%(V/V)甘油溶液中,加入pMS2-cispnt质粒,混合均匀后转移入0.1cm电击杯中,于2kV持续5ms的条件进行电击,然后立即加入1mL含0.5%(M/M)葡萄糖的液体LB培养基,于42℃温浴5分钟,然后涂布在含100μg/mL氨苄青霉素和35μg/mL卡那霉素的固体LB培养基上于30℃培养36小时。生长出的转化菌株提取总DNA后,用上述正向引物和反向引物PCR扩增,琼脂糖凝胶电泳发现有约2.9kb大小的片段,表明已经将如序列表的SEQ ID No:1所示的基因构建体导入了棒状杆菌工程菌中。同时将pMS2质粒电转化入L-赖氨酸发酵的棒状杆菌工程菌,形成阴性对照菌。The pMS2-cispnt plasmid is transferred into L-lysine-fermenting coryneform bacteria engineering bacteria (available from the American Type Microorganism Collection (ATCC), product number ATCC 31269) by electroporation, and its brief process is: the coryneform bacteria Shake culture in 50mL LB liquid medium until OD500 reaches 0.7, collect the bacteria by centrifugation, wash with 0°C pre-cooled 10% (V/V) glycerol solution, and resuspend the bacteria in 200 μL pre-cooled 10% (V/V) V) In glycerol solution, add pMS2-cispnt plasmid, mix well, transfer to 0.1cm electric shock cup, conduct electric shock at 2kV for 5ms, then immediately add 1mL liquid LB medium containing 0.5% (M/M) glucose , incubated at 42°C for 5 minutes, and then spread on solid LB medium containing 100 μg/mL ampicillin and 35 μg/mL kanamycin and cultured at 30°C for 36 hours. After the total DNA was extracted from the transformed bacterial strain that grew out, it was amplified by PCR with the above-mentioned forward primer and reverse primer. Agarose gel electrophoresis found a fragment of about 2.9 kb in size, indicating that it had been prepared as shown in SEQ ID No: 1 of the sequence table. The gene construct shown was introduced into the Corynebacterium engineering bacteria. At the same time, the pMS2 plasmid was electrotransformed into L-lysine fermented coryneform bacteria to form negative control bacteria.
将上述电转化的阳性棒状杆菌工程菌和阴性对照菌分别在液体LB培养基中振荡培养至OD500达到0.5,以5%的接种量接入赖氨酸发酵培养基(每升培养基配方为:40g蔗糖,20g NH4Cl,2g CaCl2,1g KH2PO4,1g蛋白胨,500mgMgSO4·7H2O,15mg FeSO4·7H2O,10mg MnSO4·7H2O,200μg生物素,和50μg叶酸,用Tris-HCl调节至pH7.3)中以30℃振荡(150rpm)培养72小时。离心收集培养基上清液(即,发酵液),用纸层析法分离并定量培养基中的L-赖氨酸。结果发现,阳性棒状杆菌工程菌的发酵培养基中L-赖氨酸的含量达到了14.8g/L,而阴性对照菌的发酵培养基中L-赖氨酸的含量仅为12.0g/L,表明导入了如序列表的SEQ ID No:1所示的基因构建体,产量提高了23.3%,高于现有技术中导入野生型吡啶核苷酸转氢酶的工程菌的产量提高比率。The above-mentioned electrotransformed positive coryneform bacterium engineering bacteria and negative control bacteria were shaken and cultured in liquid LB medium until the OD500 reached 0.5, and were inserted into the lysine fermentation medium with 5% inoculum (the formula per liter of medium was: 40 g sucrose, 20 g NH 4 Cl, 2 g CaCl 2 , 1 g KH 2 PO 4 , 1 g peptone, 500 mg MgSO 4 7H 2 O, 15 mg FeSO 4 7H 2 O, 10 mg MnSO 4 7H 2 O, 200 μg biotin, and 50 μg Folic acid, adjusted to pH 7.3 with Tris-HCl) and cultured at 30° C. with shaking (150 rpm) for 72 hours. The culture supernatant (ie, fermentation broth) was collected by centrifugation, and L-lysine in the culture medium was separated and quantified by paper chromatography. As a result, it was found that the content of L-lysine in the fermentation medium of positive coryneform bacteria engineering bacteria reached 14.8g/L, while the content of L-lysine in the fermentation medium of negative control bacteria was only 12.0g/L, It shows that the gene construct shown in SEQ ID No: 1 of the sequence table has been introduced, and the yield has been increased by 23.3%, which is higher than the yield increase ratio of the engineering bacteria introduced with wild-type pyridine nucleotide transhydrogenase in the prior art.
实施例3L-赖氨酸饲料添加剂的制备The preparation of embodiment 3L-lysine feed additive
用实施例2制备的发酵液通过Suntar-III型超滤膜(可购自三达膜科技有限公司)进行膜分离。然后,将滤液直接以雾状喷入流化床干燥机内并保持尾气温度在80±3℃不变,收集出料的颗粒。对出料的颗粒进行筛分,对于粒径大于等于1.5mm的颗粒送入破碎机破碎,然后将破碎后的颗粒与筛分得到的粒径小于1.5mm的颗粒混合并再次喷入流化床干燥机内并保持尾气温度在80±3℃不变,收集出料的颗粒并筛分出粒径小于1.5mm的颗粒,即为L-赖氨酸饲料添加剂。粒径大于1.5mm的颗粒再次破碎后,与下一批次的滤液干燥得到的出料的颗粒混合。The fermentation broth prepared in Example 2 was separated by a Suntar-III ultrafiltration membrane (available from Suntar Membrane Technology Co., Ltd.). Then, spray the filtrate directly into the fluidized bed dryer in the form of mist and keep the tail gas temperature at 80±3°C, and collect the discharged particles. Sieve the discharged particles, send the particles with a particle size greater than or equal to 1.5mm to the crusher for crushing, and then mix the crushed particles with the particles with a particle size smaller than 1.5mm obtained by screening and spray them into the fluidized bed again Keep the tail gas temperature in the dryer at 80±3°C, collect the discharged particles and sieve out the particles with a particle size of less than 1.5mm, which are L-lysine feed additives. After the particles with a particle size greater than 1.5mm are crushed again, they are mixed with the discharged particles obtained by drying the filtrate of the next batch.
以上制备的L-赖氨酸饲料添加剂经检测,含水量<1%;颗粒粒径小于1.5mm,无明显可见粉尘;混合变异系数为7~9;堆积密度为550~630g/L;不含其他添加剂,完全达到了国家标准。The above-prepared L-lysine feed additive has been tested and found to have a water content of <1%; a particle size of less than 1.5 mm, without visible dust; a mixing coefficient of variation of 7 to 9; a bulk density of 550 to 630 g/L; Other additives have fully met the national standard.
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