CN109456951B - Method for increasing trehalose synthase yield - Google Patents
Method for increasing trehalose synthase yield Download PDFInfo
- Publication number
- CN109456951B CN109456951B CN201811395709.0A CN201811395709A CN109456951B CN 109456951 B CN109456951 B CN 109456951B CN 201811395709 A CN201811395709 A CN 201811395709A CN 109456951 B CN109456951 B CN 109456951B
- Authority
- CN
- China
- Prior art keywords
- leu
- asp
- pro
- gly
- arg
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
- C12N9/00—Enzymes; Proenzymes; Compositions thereof; Processes for preparing, activating, inhibiting, separating or purifying enzymes
- C12N9/10—Transferases (2.)
- C12N9/1048—Glycosyltransferases (2.4)
- C12N9/1051—Hexosyltransferases (2.4.1)
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
- C12P19/00—Preparation of compounds containing saccharide radicals
- C12P19/12—Disaccharides
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12Y—ENZYMES
- C12Y204/00—Glycosyltransferases (2.4)
- C12Y204/01—Hexosyltransferases (2.4.1)
- C12Y204/01245—Alpha,alpha-trehalose synthase (2.4.1.245)
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Zoology (AREA)
- Health & Medical Sciences (AREA)
- Wood Science & Technology (AREA)
- Bioinformatics & Cheminformatics (AREA)
- Genetics & Genomics (AREA)
- General Health & Medical Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Biochemistry (AREA)
- Biotechnology (AREA)
- Microbiology (AREA)
- Medicinal Chemistry (AREA)
- Molecular Biology (AREA)
- Biomedical Technology (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Micro-Organisms Or Cultivation Processes Thereof (AREA)
Abstract
The invention discloses a method for improving the output of trehalose synthase, belonging to the technical field of genetic engineering and the technical field of enzyme engineering. The method greatly improves the expression quantity of the trehalose synthase in host cells by connecting the short peptide with the amino acid sequence shown as SEQ ID NO.4 at the N end of the trehalose synthase parent through the linker with the amino acid sequence shown as SEQ ID NO.3, and has great significance for promoting the large-scale industrialization of trehalose and reducing the production cost of trehalose.
Description
Technical Field
The invention relates to a method for improving the output of trehalose synthase, belonging to the technical field of genetic engineering and the technical field of enzyme engineering.
Background
Trehalose is a non-reducing disaccharide composed of two glucose molecules bonded via an α, α -1,1 bond, and is widely found in bacteria, fungi, algae, lower plants and insects. The research shows that the sugar has unique biological function, has the functions of protecting biological macromolecules, protecting cell membranes and protecting proteins from being damaged by freezing, drying, osmotic pressure change and the like, and has wide application in the fields of food, medicine, cosmetics, agriculture and the like.
The production of trehalose in China starts relatively late and is imported from Japan before mainly, but the price of imported trehalose is as high as 4-5 ten thousand yuan per ton, so that the trehalose is very expensive for industrial production, and the production cost of enterprises can be greatly increased.
In recent years, companies such as Shandong Tianli, Nemonton plum blossom, Hunan Huiyi rise and the like have started to produce trehalose autonomously, the market scale is increased by 1 million tons every year, and the market prospect is very wide.
However, trehalose from various companies is a newly developed product, the production process is different, the product quality is quite unstable, and particularly the yield does not reach the leading level, so that a method for improving the yield of trehalose is urgently needed.
Early commercial trehalose was extracted from yeast. In 1990, the price is about $ 700/kg, the extraction rate is too low, and the cost is too high; in 1995, Japan utilizes a double-enzyme method to realize industrial production, so that the price of trehalose is greatly reduced from the original 2 ten thousand yen/kg to 280 yen/kg in 1997; the industrialization of trehalose is realized by a two-enzyme method for the first time in 2002 in China, and the price is 79 yuan/kg.
The double-enzyme method takes starch as a raw material, and generates trehalose under the action of maltooligosyl trehalose hydrolase and maltooligosyl trehalose synthase, the production process of the method is complex and difficult to popularize, and only a few companies can produce trehalose all over the world at present; the trehalose synthase uses maltose as a substrate, and one-step conversion to generate trehalose is a relatively economic production method, but still many problems need to be researched and solved, wherein the production of the trehalose synthase is a key point.
Therefore, the method for improving the expression level of the trehalose synthase has great significance for promoting large-scale industrialization of trehalose and reducing industrial cost.
Disclosure of Invention
In order to solve the problems, the invention provides a method for improving the yield of trehalose synthase. The method greatly improves the expression quantity of the trehalose synthase in host cells by connecting the short peptide with the amino acid sequence shown as SEQ ID NO.4 at the N end of the trehalose synthase parent through the linker with the amino acid sequence shown as SEQ ID NO.3, and has great significance for promoting the large-scale industrialization of trehalose and reducing the production cost of trehalose.
The technical scheme of the invention is as follows:
the invention provides a trehalose synthetase mutant, wherein short peptides with amino acid sequences shown as SEQ ID No.4 are connected at the N end of a trehalose synthetase parent through a linker with amino acid sequences shown as SEQ ID No. 3.
In one embodiment of the present invention, the amino acid sequence of the trehalose synthase parent is as shown in SEQ ID No. 9.
In one embodiment of the invention, the amino acid sequence of the trehalose synthase mutant is shown as SEQ ID No. 8.
The present invention provides a gene encoding the above mutant.
The invention provides a recombinant plasmid carrying the gene.
In one embodiment of the present invention, the plasmid vector is any one of pUC series, pET series, or pGEX.
The present invention provides a host cell carrying the above gene or the above recombinant plasmid.
In one embodiment of the invention, the host cell is a bacterial or fungal cell.
The invention provides the application of the mutant or the gene or the recombinant plasmid or the host cell in the aspects of high-efficiency expression of trehalose synthase and production of trehalose.
The invention provides a method for efficiently expressing trehalose synthase, which comprises the step of inoculating the host cell into a fermentation culture medium for fermentation to obtain the trehalose synthase.
Has the advantages that:
the trehalose synthase from Thermobifida fusca YX is modified, so that the expression quantity of the trehalose synthase in host cells is greatly improved (improved by 1.9 times compared with wild type), and the trehalose synthase has great significance for promoting large-scale industrialization of trehalose and reducing the production cost of trehalose.
Detailed Description
The present invention will be further illustrated below with reference to specific examples and comparative examples.
The detection methods referred to in the following examples are as follows:
the enzyme activity detection method comprises the following steps:
preheating: 1.9mL of 0.2% maltodextrin solution (DE 9-13 pH 6.0 phosphate buffer) was placed in a stoppered test tube and preheated in a 50 ℃ water bath for 10 min.
Reaction: adding 0.1mL of diluted crude enzyme solution, uniformly oscillating, accurately timing for 10min, adding 3mLDNS, uniformly oscillating, and terminating the reaction; boiling for 7min, and cooling.
Measurement: adding distilled water into the reaction system, fixing the volume to 15mL, and uniformly mixing; the absorbance was measured at a wavelength of 540nm and the enzyme activity was calculated.
(enzyme activity is defined as the amount of enzyme required to convert one micromole of glucose per minute into a non-reducing sugar.)
The trehalose conversion rate detection method comprises the following steps:
diluting the reaction product in the example 3, precipitating, measuring the content of trehalose in the reaction product by using High Performance Liquid Chromatography (HPLC), and calculating the conversion rate;
conversion calculation formula is trehalose quality/rice starch quality 100/%;
HPLC detection conditions: mobile phase (acetonitrile: water 80: 20); flow rate: 0.8mL/min, column temperature 40 deg.C, NH2 column (APS-2HYPERSIL, Thermo Scientific), differential refractometer detector (RID).
Example 1: construction of mutants
(1) According to the short peptides (named as P1, P2, P3, P4 and P5 respectively) with the amino acid sequences shown as SEQ ID NO.4, SEQ ID NO.5, SEQ ID NO.6, SEQ ID NO.10 and SEQ ID NO.11 respectively, the genes are chemically synthesized and are respectively connected to the N ends of the trehalose synthase gene sequence with the amino acid sequence shown as SEQ ID NO.9 respectively, and the genes are cloned between the Xho I and HindIII enzyme cutting sites of a plasmid pET24a (+), so as to construct recombinant plasmids pET24a (+)/P1-enzyme, pET24a (+)/P2-enzyme, pET24a (+)/P3-enzyme, pET24a (+)/P4-enzyme and pET24a (+)/P5-enzyme;
(2) chemically synthesizing genes thereof according to linker (named as L1, L2 and L3) with amino acid sequences shown as SEQ ID NO.1, SEQ ID NO.2 and SEQ ID NO.3 respectively, and connecting the genes to pMD18-T vectors respectively to obtain recombinant plasmids pMD18-T/L1, pMD18-T/L2 and pMD 18-T/L3;
(3) the recombinant plasmid is used as a template, a primer is designed, a linearized recombinant plasmid fragment in the step (1) and a linearized linker fragment in the step (2) are obtained through PCR, and homologous recombination is carried out on the two obtained fragments to obtain a mixed plasmid (or a fragment obtained by directly carrying out chemical synthesis and connecting short peptide, a linker and trehalose synthase genes is cloned between Xho I and Hind III enzyme cutting sites of a plasmid pET24a (+), so as to obtain the mixed plasmid).
Example 2: validation of mutants
Growing the mixed plasmid and transformed E.coli BL21(DE3) host bacteria in an LB liquid culture medium (containing 30 mu g/mL kanamycin) for 8-10 h, inoculating seed fermentation liquor into a TB culture medium (containing 30 mu g/mL kanamycin) according to the inoculum size of 5%, culturing in a shaker at 37 ℃ for 48h, centrifuging the fermentation liquor at 4 ℃ and 8000rpm for 10min to remove bacteria, and collecting the centrifuged supernatant, namely the crude enzyme solution.
And carrying out enzyme activity detection on the obtained crude enzyme solution to obtain recombinant bacteria with higher enzyme activity than that of recombinant bacteria containing recombinant plasmids pET24a (+)/enzyme, wherein the recombinant bacteria respectively contain recombinant plasmids pET24a (+)/P1-L3-enzyme, pET24a (+)/P3-L2-enzyme, pET24a (+)/P2-L3-enzyme and pET24a (+)/P5-L1-enzyme.
The enzyme activity of trehalose synthase secreted by recombinant bacteria containing recombinant plasmids pET24a (+)/P1-L3-enzyme, pET24a (+)/P3-L2-enzyme, pET24a (+)/P2-L3-enzyme and pET24a (+)/P5-L1-enzyme was compared with that secreted by recombinant bacteria containing recombinant plasmids pET24a (+)/enzyme.
The results are as follows: the enzyme activity of the trehalose synthase secreted by the recombinant bacteria containing the recombinant plasmids pET24a (+)/P1-L3-enzyme and pET24a (+)/P3-L2-enzyme is obviously improved compared with the enzyme activity of the trehalose synthase secreted by the recombinant bacteria containing the recombinant plasmids pET24a (+)/enzyme, and is respectively 2.3 times and 1.9 times of the enzyme activity of the trehalose synthase secreted by the recombinant bacteria containing the recombinant plasmids pET24a (+)/enzyme; the enzyme activity of the trehalose synthase secreted by the recombinant bacteria containing the recombinant plasmids pET24a (+)/P2-L3-enzyme and pET24a (+)/P5-L1-enzyme is not obviously changed compared with the enzyme activity of the trehalose synthase secreted by the recombinant bacteria containing the recombinant plasmids pET24a (+)/enzyme, and is only 1.1 time and 1.3 times of the enzyme activity of the trehalose synthase secreted by the recombinant bacteria containing the recombinant plasmids pET24a (+)/enzyme.
Example 3: use of mutants
Adding 300g/L (containing 10% of glucose) of maltose into a reactor, adding a certain amount of crude enzyme liquid of wild enzyme and mutant P1-L3-enzyme and P3-L2-enzyme which have amino acid sequences shown in SEQ ID NO.7 and SEQ ID NO.8 respectively, adjusting the pH to 8.0 by using 20% sodium hydroxide aqueous solution, reacting for 30-50 hours in a water bath shaker at 30 ℃ and 150rpm, sampling at fixed time, boiling for 10 minutes, stopping reaction, centrifuging the sample at 12000rpm for 10 minutes, taking supernatant, filtering by using a 0.45 mu m ultrafiltration membrane after being diluted appropriately, and carrying out HPLC analysis;
wherein, the chromatographic conditions are as follows: differential refractometer, NH2 column (APS-2HYPERSIL, Therm)o Scientific), mobile phase (water: acetonitrile ═ 1:4), flow rate: 0.8mL/min-1Column temperature: at 40 ℃.
The conversion of maltose (mass ratio of trehalose to maltose) was calculated from the trehalose production, and the results are shown in Table 1, wherein the conversion of trehalose produced by the wild enzyme was 62.5% and the conversion of trehalose produced by mutants P1-L3-enzyme and P3-L2-enzyme was 61.7% and 73.4% respectively, which were not lower than that of the wild enzyme, using industrial grade maltose (containing 10% glucose) as the substrate.
TABLE 1 conversion of technical maltose as substrate for trehalose production
Enzyme | Conversion (%) |
Wild enzyme | 62.5% |
P1-L3-enzyme | 61.7% |
P3-L2-enzyme | 73.4% |
Although the present invention has been described with reference to the preferred embodiments, it should be understood that various changes and modifications can be made therein by those skilled in the art without departing from the spirit and scope of the invention as defined in the appended claims.
Sequence listing
<110> Hunan Vigorboom Biotech Co., Ltd
<120> a method for increasing the yield of trehalose synthase
<160> 11
<170> PatentIn version 3.3
<210> 1
<211> 10
<212> PRT
<213> Artificial sequence
<400> 1
Gly Gly Gly Gly Ser Gly Gly Gly Gly Ser
1 5 10
<210> 2
<211> 15
<212> PRT
<213> Artificial sequence
<400> 2
Gly Gly Gly Gly Ser Gly Gly Gly Gly Ser Gly Gly Gly Gly Ser
1 5 10 15
<210> 3
<211> 18
<212> PRT
<213> Artificial sequence
<400> 3
Gly Ser Gly Gly Gly Gly Ser Gly Gly Gly Gly Ser Gly Gly Gly Gly
1 5 10 15
Ser Gly
<210> 4
<211> 8
<212> PRT
<213> Artificial sequence
<400> 4
Lys Glu Lys Glu Lys Asp Lys Asp
1 5
<210> 5
<211> 16
<212> PRT
<213> Artificial sequence
<400> 5
Lys Glu Lys Glu Lys Asp Lys Asp Lys Glu Lys Glu Lys Asp Lys Asp
1 5 10 15
<210> 6
<211> 24
<212> PRT
<213> Artificial sequence
<400> 6
Lys Glu Lys Glu Lys Asp Lys Asp Lys Glu Lys Glu Lys Asp Lys Asp
1 5 10 15
Lys Glu Lys Glu Lys Asp Lys Asp
20
<210> 7
<211> 645
<212> PRT
<213> Artificial sequence
<400> 7
Gly Gly Gly Gly Ser Gly Gly Gly Gly Ser Gly Gly Gly Gly Ser Lys
1 5 10 15
Glu Lys Glu Lys Asp Lys Asp Lys Glu Lys Glu Lys Asp Lys Asp Lys
20 25 30
Glu Lys Glu Lys Asp Lys Asp Met Thr Thr Gln Pro Ala Pro Gly Ala
35 40 45
Arg Pro Thr Pro Thr Gly Ser Val Pro Asp Thr Phe Thr His Ala Lys
50 55 60
Pro Arg Asp Pro Tyr Trp Tyr Lys His Ala Val Phe Tyr Glu Val Leu
65 70 75 80
Val Arg Gly Phe Tyr Asp Ser Asn Gly Asp Gly Thr Gly Asp Leu Arg
85 90 95
Gly Leu Ile Glu Lys Leu Asp Tyr Leu Gln Trp Leu Gly Ile Asp Cys
100 105 110
Leu Trp Leu Leu Pro Ile Tyr Glu Ser Pro Leu Arg Asp Gly Gly Tyr
115 120 125
Asp Val Ser Asp Tyr Met Lys Ile Leu Pro Glu Phe Gly Arg Ile Ser
130 135 140
Asp Phe Val Glu Leu Val Glu Lys Ala His Gln Arg Gly Ile Arg Val
145 150 155 160
Ile Thr Asp Leu Val Met Asn His Thr Ser Asp Gln His Pro Trp Phe
165 170 175
Gln Ala Ser Arg His Asp Pro Asp Gly Pro Tyr Gly Asn Phe Tyr Val
180 185 190
Trp Ser Asp Thr Thr Glu Arg Tyr Ser Asp Ala Arg Ile Ile Phe Ile
195 200 205
Asp Thr Glu Gln Ser Asn Trp Thr Tyr Asp Glu Val Arg Gly Gln Tyr
210 215 220
Tyr Trp His Arg Phe Phe Ser His Gln Pro Asp Leu Asn Phe Glu Asn
225 230 235 240
Pro Asp Val Gln Asp Ala Ile Leu Glu Val Met Arg Phe Trp Leu Asp
245 250 255
Leu Gly Ile Asp Gly Phe Arg Leu Asp Ala Val Pro Tyr Leu Tyr Glu
260 265 270
Arg Glu Gly Thr Asn Cys Glu Asn Leu Lys Glu Thr His Glu Phe Leu
275 280 285
Lys Arg Ile Arg Ala Glu Val Asp Arg Leu Tyr Pro Asp Arg Val Leu
290 295 300
Leu Ser Glu Ala Asn Gln Trp Pro Ala Asp Val Val Asp Tyr Phe Gly
305 310 315 320
Asp Tyr Glu Ser Gly Gly Asp Glu Cys His Met Asn Phe His Phe Pro
325 330 335
Leu Met Pro Arg Met Phe Met Ala Val Arg Arg Glu Gln Arg Tyr Pro
340 345 350
Ile Ser Glu Ile Leu Ala Gln Thr Pro Pro Ile Pro Arg Asn Cys Gln
355 360 365
Trp Ala Ile Phe Leu Arg Asn His Asp Glu Leu Thr Leu Glu Met Val
370 375 380
Ser Asp Glu Glu Arg Asp Tyr Met Tyr Ser Glu Tyr Ala Lys Asp Pro
385 390 395 400
Arg Met Arg Ala Asn Met Gly Ile Arg Arg Arg Leu Ala Pro Leu Leu
405 410 415
Glu Asn Asp Leu Asn Gln Ile Lys Leu Phe Thr Ala Leu Leu Leu Ser
420 425 430
Leu Pro Gly Ser Pro Val Leu Tyr Tyr Gly Asp Glu Ile Gly Met Gly
435 440 445
Asp Asn Ile Trp Leu Gly Asp Arg Asp Ser Val Arg Thr Pro Met Gln
450 455 460
Trp Thr Pro Asp Arg Asn Ala Gly Phe Ser Arg Cys Asp Pro Gly Arg
465 470 475 480
Leu Tyr Leu Pro Val Ile Met Asp Pro Ile Tyr Gly Tyr Gln Ala Ile
485 490 495
Asn Val Glu Ala Gln Gln Asn Asn Pro Asn Ser Leu Leu Asn Trp Thr
500 505 510
Arg Asn Met Ile Gln Ile Arg Lys Gln His Pro Val Phe Gly Thr Gly
515 520 525
Asp Phe Thr Glu Leu His Ala Ser Asn Pro Ser Val Phe Ala Phe Val
530 535 540
Arg Glu Tyr Gly Asp Asp Arg Met Leu Cys Val Asn Asn Leu Ser Arg
545 550 555 560
Phe Pro Gln Pro Val Glu Leu Asp Leu Arg Arg Phe Glu Gly Ile Thr
565 570 575
Pro Ile Glu Cys Thr Gly Gly Val His Phe Pro Pro Ile Gly Glu Leu
580 585 590
Pro Tyr Leu Leu Thr Leu Pro Gly His Gly Phe Tyr Trp Phe Gln Leu
595 600 605
Pro Pro Val Ala Glu Glu Gln Pro Leu Ala Gln Pro Val Thr Thr Val
610 615 620
Pro Ala Ala Pro Gln Pro Pro Ala Pro Ala Asp Arg Pro Ala Ser Asp
625 630 635 640
Pro Thr Gln Arg Ser
645
<210> 8
<211> 632
<212> PRT
<213> Artificial sequence
<400> 8
Gly Ser Gly Gly Gly Gly Ser Gly Gly Gly Gly Ser Gly Gly Gly Gly
1 5 10 15
Ser Gly Lys Glu Lys Glu Lys Asp Lys Asp Met Thr Thr Gln Pro Ala
20 25 30
Pro Gly Ala Arg Pro Thr Pro Thr Gly Ser Val Pro Asp Thr Phe Thr
35 40 45
His Ala Lys Pro Arg Asp Pro Tyr Trp Tyr Lys His Ala Val Phe Tyr
50 55 60
Glu Val Leu Val Arg Gly Phe Tyr Asp Ser Asn Gly Asp Gly Thr Gly
65 70 75 80
Asp Leu Arg Gly Leu Ile Glu Lys Leu Asp Tyr Leu Gln Trp Leu Gly
85 90 95
Ile Asp Cys Leu Trp Leu Leu Pro Ile Tyr Glu Ser Pro Leu Arg Asp
100 105 110
Gly Gly Tyr Asp Val Ser Asp Tyr Met Lys Ile Leu Pro Glu Phe Gly
115 120 125
Arg Ile Ser Asp Phe Val Glu Leu Val Glu Lys Ala His Gln Arg Gly
130 135 140
Ile Arg Val Ile Thr Asp Leu Val Met Asn His Thr Ser Asp Gln His
145 150 155 160
Pro Trp Phe Gln Ala Ser Arg His Asp Pro Asp Gly Pro Tyr Gly Asn
165 170 175
Phe Tyr Val Trp Ser Asp Thr Thr Glu Arg Tyr Ser Asp Ala Arg Ile
180 185 190
Ile Phe Ile Asp Thr Glu Gln Ser Asn Trp Thr Tyr Asp Glu Val Arg
195 200 205
Gly Gln Tyr Tyr Trp His Arg Phe Phe Ser His Gln Pro Asp Leu Asn
210 215 220
Phe Glu Asn Pro Asp Val Gln Asp Ala Ile Leu Glu Val Met Arg Phe
225 230 235 240
Trp Leu Asp Leu Gly Ile Asp Gly Phe Arg Leu Asp Ala Val Pro Tyr
245 250 255
Leu Tyr Glu Arg Glu Gly Thr Asn Cys Glu Asn Leu Lys Glu Thr His
260 265 270
Glu Phe Leu Lys Arg Ile Arg Ala Glu Val Asp Arg Leu Tyr Pro Asp
275 280 285
Arg Val Leu Leu Ser Glu Ala Asn Gln Trp Pro Ala Asp Val Val Asp
290 295 300
Tyr Phe Gly Asp Tyr Glu Ser Gly Gly Asp Glu Cys His Met Asn Phe
305 310 315 320
His Phe Pro Leu Met Pro Arg Met Phe Met Ala Val Arg Arg Glu Gln
325 330 335
Arg Tyr Pro Ile Ser Glu Ile Leu Ala Gln Thr Pro Pro Ile Pro Arg
340 345 350
Asn Cys Gln Trp Ala Ile Phe Leu Arg Asn His Asp Glu Leu Thr Leu
355 360 365
Glu Met Val Ser Asp Glu Glu Arg Asp Tyr Met Tyr Ser Glu Tyr Ala
370 375 380
Lys Asp Pro Arg Met Arg Ala Asn Met Gly Ile Arg Arg Arg Leu Ala
385 390 395 400
Pro Leu Leu Glu Asn Asp Leu Asn Gln Ile Lys Leu Phe Thr Ala Leu
405 410 415
Leu Leu Ser Leu Pro Gly Ser Pro Val Leu Tyr Tyr Gly Asp Glu Ile
420 425 430
Gly Met Gly Asp Asn Ile Trp Leu Gly Asp Arg Asp Ser Val Arg Thr
435 440 445
Pro Met Gln Trp Thr Pro Asp Arg Asn Ala Gly Phe Ser Arg Cys Asp
450 455 460
Pro Gly Arg Leu Tyr Leu Pro Val Ile Met Asp Pro Ile Tyr Gly Tyr
465 470 475 480
Gln Ala Ile Asn Val Glu Ala Gln Gln Asn Asn Pro Asn Ser Leu Leu
485 490 495
Asn Trp Thr Arg Asn Met Ile Gln Ile Arg Lys Gln His Pro Val Phe
500 505 510
Gly Thr Gly Asp Phe Thr Glu Leu His Ala Ser Asn Pro Ser Val Phe
515 520 525
Ala Phe Val Arg Glu Tyr Gly Asp Asp Arg Met Leu Cys Val Asn Asn
530 535 540
Leu Ser Arg Phe Pro Gln Pro Val Glu Leu Asp Leu Arg Arg Phe Glu
545 550 555 560
Gly Ile Thr Pro Ile Glu Cys Thr Gly Gly Val His Phe Pro Pro Ile
565 570 575
Gly Glu Leu Pro Tyr Leu Leu Thr Leu Pro Gly His Gly Phe Tyr Trp
580 585 590
Phe Gln Leu Pro Pro Val Ala Glu Glu Gln Pro Leu Ala Gln Pro Val
595 600 605
Thr Thr Val Pro Ala Ala Pro Gln Pro Pro Ala Pro Ala Asp Arg Pro
610 615 620
Ala Ser Asp Pro Thr Gln Arg Ser
625 630
<210> 9
<211> 606
<212> PRT
<213> Artificial sequence
<400> 9
Met Thr Thr Gln Pro Ala Pro Gly Ala Arg Pro Thr Pro Thr Gly Ser
1 5 10 15
Val Pro Asp Thr Phe Thr His Ala Lys Pro Arg Asp Pro Tyr Trp Tyr
20 25 30
Lys His Ala Val Phe Tyr Glu Val Leu Val Arg Gly Phe Tyr Asp Ser
35 40 45
Asn Gly Asp Gly Thr Gly Asp Leu Arg Gly Leu Ile Glu Lys Leu Asp
50 55 60
Tyr Leu Gln Trp Leu Gly Ile Asp Cys Leu Trp Leu Leu Pro Ile Tyr
65 70 75 80
Glu Ser Pro Leu Arg Asp Gly Gly Tyr Asp Val Ser Asp Tyr Met Lys
85 90 95
Ile Leu Pro Glu Phe Gly Arg Ile Ser Asp Phe Val Glu Leu Val Glu
100 105 110
Lys Ala His Gln Arg Gly Ile Arg Val Ile Thr Asp Leu Val Met Asn
115 120 125
His Thr Ser Asp Gln His Pro Trp Phe Gln Ala Ser Arg His Asp Pro
130 135 140
Asp Gly Pro Tyr Gly Asn Phe Tyr Val Trp Ser Asp Thr Thr Glu Arg
145 150 155 160
Tyr Ser Asp Ala Arg Ile Ile Phe Ile Asp Thr Glu Gln Ser Asn Trp
165 170 175
Thr Tyr Asp Glu Val Arg Gly Gln Tyr Tyr Trp His Arg Phe Phe Ser
180 185 190
His Gln Pro Asp Leu Asn Phe Glu Asn Pro Asp Val Gln Asp Ala Ile
195 200 205
Leu Glu Val Met Arg Phe Trp Leu Asp Leu Gly Ile Asp Gly Phe Arg
210 215 220
Leu Asp Ala Val Pro Tyr Leu Tyr Glu Arg Glu Gly Thr Asn Cys Glu
225 230 235 240
Asn Leu Lys Glu Thr His Glu Phe Leu Lys Arg Ile Arg Ala Glu Val
245 250 255
Asp Arg Leu Tyr Pro Asp Arg Val Leu Leu Ser Glu Ala Asn Gln Trp
260 265 270
Pro Ala Asp Val Val Asp Tyr Phe Gly Asp Tyr Glu Ser Gly Gly Asp
275 280 285
Glu Cys His Met Asn Phe His Phe Pro Leu Met Pro Arg Met Phe Met
290 295 300
Ala Val Arg Arg Glu Gln Arg Tyr Pro Ile Ser Glu Ile Leu Ala Gln
305 310 315 320
Thr Pro Pro Ile Pro Arg Asn Cys Gln Trp Ala Ile Phe Leu Arg Asn
325 330 335
His Asp Glu Leu Thr Leu Glu Met Val Ser Asp Glu Glu Arg Asp Tyr
340 345 350
Met Tyr Ser Glu Tyr Ala Lys Asp Pro Arg Met Arg Ala Asn Met Gly
355 360 365
Ile Arg Arg Arg Leu Ala Pro Leu Leu Glu Asn Asp Leu Asn Gln Ile
370 375 380
Lys Leu Phe Thr Ala Leu Leu Leu Ser Leu Pro Gly Ser Pro Val Leu
385 390 395 400
Tyr Tyr Gly Asp Glu Ile Gly Met Gly Asp Asn Ile Trp Leu Gly Asp
405 410 415
Arg Asp Ser Val Arg Thr Pro Met Gln Trp Thr Pro Asp Arg Asn Ala
420 425 430
Gly Phe Ser Arg Cys Asp Pro Gly Arg Leu Tyr Leu Pro Val Ile Met
435 440 445
Asp Pro Ile Tyr Gly Tyr Gln Ala Ile Asn Val Glu Ala Gln Gln Asn
450 455 460
Asn Pro Asn Ser Leu Leu Asn Trp Thr Arg Asn Met Ile Gln Ile Arg
465 470 475 480
Lys Gln His Pro Val Phe Gly Thr Gly Asp Phe Thr Glu Leu His Ala
485 490 495
Ser Asn Pro Ser Val Phe Ala Phe Val Arg Glu Tyr Gly Asp Asp Arg
500 505 510
Met Leu Cys Val Asn Asn Leu Ser Arg Phe Pro Gln Pro Val Glu Leu
515 520 525
Asp Leu Arg Arg Phe Glu Gly Ile Thr Pro Ile Glu Cys Thr Gly Gly
530 535 540
Val His Phe Pro Pro Ile Gly Glu Leu Pro Tyr Leu Leu Thr Leu Pro
545 550 555 560
Gly His Gly Phe Tyr Trp Phe Gln Leu Pro Pro Val Ala Glu Glu Gln
565 570 575
Pro Leu Ala Gln Pro Val Thr Thr Val Pro Ala Ala Pro Gln Pro Pro
580 585 590
Ala Pro Ala Asp Arg Pro Ala Ser Asp Pro Thr Gln Arg Ser
595 600 605
<210> 10
<211> 8
<212> PRT
<213> Artificial sequence
<400> 10
Leu Glu Leu Glu Leu Lys Leu Lys
1 5
<210> 11
<211> 16
<212> PRT
<213> Artificial sequence
<400> 11
Leu Glu Leu Glu Leu Lys Leu Lys Leu Glu Leu Glu Leu Lys Leu Lys
1 5 10 15
Claims (8)
1. A trehalose synthase mutant is characterized in that the N end of a trehalose synthase parent is connected with a short peptide with an amino acid sequence shown in SEQ ID NO.4 through a linker with an amino acid sequence shown in SEQ ID NO.3, and the amino acid sequence of the trehalose synthase parent is shown in SEQ ID NO. 9; the amino acid sequence of the trehalose synthetase mutant is shown as SEQ ID NO. 8.
2. A gene encoding the mutant of claim 1.
3. A recombinant plasmid carrying the gene of claim 2.
4. The recombinant plasmid of claim 3, wherein the plasmid vector is any one of pUC series, pET series, or pGEX.
5. A host cell carrying the gene of claim 2, or the recombinant plasmid of claim 3 or 4.
6. The host cell of claim 5, wherein the host cell is a bacterial or fungal cell.
7. Use of the mutant of claim 1, or the gene of claim 2, or the recombinant plasmid of claim 3 or 4, or the host cell of claim 5 or 6 for expressing trehalose synthase.
8. A method for expressing trehalose synthase by inoculating the host cell of claim 5 or 6 into a fermentation medium for fermentation to obtain trehalose synthase.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201811395709.0A CN109456951B (en) | 2018-11-22 | 2018-11-22 | Method for increasing trehalose synthase yield |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201811395709.0A CN109456951B (en) | 2018-11-22 | 2018-11-22 | Method for increasing trehalose synthase yield |
Publications (2)
Publication Number | Publication Date |
---|---|
CN109456951A CN109456951A (en) | 2019-03-12 |
CN109456951B true CN109456951B (en) | 2021-03-30 |
Family
ID=65611230
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201811395709.0A Active CN109456951B (en) | 2018-11-22 | 2018-11-22 | Method for increasing trehalose synthase yield |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN109456951B (en) |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101629166A (en) * | 2009-08-20 | 2010-01-20 | 南宁中诺生物工程有限责任公司 | Mutant of trehalose synthetase from corynebacterium glutamicum and application thereof |
CN107488641B (en) * | 2017-09-13 | 2019-11-26 | 江南大学 | A kind of malt oligosaccharide based mycose synthetase mutant and its application |
CN108395483A (en) * | 2018-02-13 | 2018-08-14 | 天津大学 | A kind of synthetic method of the multi-functional fusion protein of three block based on mussel attachment proteins/amphoteric ion polypeptide and application |
-
2018
- 2018-11-22 CN CN201811395709.0A patent/CN109456951B/en active Active
Also Published As
Publication number | Publication date |
---|---|
CN109456951A (en) | 2019-03-12 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN108330095B (en) | Recombinant corynebacterium glutamicum for accumulating N-acetylneuraminic acid and application thereof | |
CN110592059B (en) | Maltooligosyl trehalose synthase mutant | |
CN111172127A (en) | Application of sucrose phosphorylase in preparation of glycerol glucoside | |
CN107446900B (en) | A kind of trehalose synthase and its preparation method and application | |
CN108753747B (en) | MTSase mutant with improved thermal stability and trehalose yield | |
CN109402081B (en) | Amylosucrase mutant and preparation method and application thereof | |
CN110055233B (en) | MTSase mutant with improved thermal stability and application thereof | |
CN109486791B (en) | Preparation and application of maltogenic amylase mutant | |
CN109456951B (en) | Method for increasing trehalose synthase yield | |
CN109355268B (en) | Method for efficiently expressing recombinase | |
CN111172089A (en) | Method for synthesizing trehalose by using recombinant trehalose synthase | |
CN108753746B (en) | Maltooligosyl trehalose synthase mutant with improved thermal stability | |
CN113817709B (en) | Carbohydrate binding domain CBM68 and uses thereof | |
CN110257361A (en) | A kind of algin catenase and its gene and application | |
CN106754848B (en) | Alkaline pectinase mutant with improved thermal stability | |
CN113151327B (en) | Mutant of bacillus cereus high-yield maltopentaose alpha-amylase and application thereof | |
CN115011622A (en) | Screening method and application of D-psicose 3-epimerase mutant | |
CN109354627B (en) | Method for increasing yield of trehalose hydrolase | |
CN109439641A (en) | A kind of application of maltogenic amylase production bacterial strain | |
CN110951716A (en) | Circumscribed alginate lyase VsAly7D, recombinant strain thereof and application thereof | |
CN110564748A (en) | poria cocos cellulose endonuclease gene and expression vector and protein thereof | |
KR101826927B1 (en) | A microorganism having enhanced levansucrase productivity and a method of producing levan using the microorganism | |
CN109321481B (en) | Bacterial strain for producing maltogenic amylase | |
CN114752581B (en) | Alpha-galactosidase mutant and application thereof | |
CN111793663B (en) | Starch pullulanase with wide pH value adaptability and application thereof |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant | ||
TR01 | Transfer of patent right |
Effective date of registration: 20220215 Address after: 421800 room 211-212, zijingfu (building a-4a, Mingang new town), beside National Highway 107, TIYU North Road, Xili neighborhood committee, Wulipai street, Leiyang City, Hengyang City, Hunan Province Patentee after: Hunan Jindai Technology Development Co.,Ltd. Address before: 421800 Building 1, Dongjiang Industrial Park, Leiyang Economic Development Zone, Hunan Province Patentee before: HUNAN HUISHENG BIOTECHNOLOGY Co.,Ltd. |
|
TR01 | Transfer of patent right |