CN108929883A - II E of sporulation related gene spo is influencing the application in strain growth and producing enzyme - Google Patents
II E of sporulation related gene spo is influencing the application in strain growth and producing enzyme Download PDFInfo
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- 102000004190 Enzymes Human genes 0.000 title claims abstract description 33
- 108090000790 Enzymes Proteins 0.000 title claims abstract description 33
- 230000028070 sporulation Effects 0.000 title claims abstract description 16
- 241001328122 Bacillus clausii Species 0.000 claims abstract description 36
- 241000726221 Gemma Species 0.000 claims abstract description 19
- 102000013142 Amylases Human genes 0.000 claims abstract description 14
- 108010065511 Amylases Proteins 0.000 claims abstract description 14
- 108090000623 proteins and genes Proteins 0.000 claims abstract description 13
- 230000004927 fusion Effects 0.000 claims abstract description 11
- 239000004382 Amylase Substances 0.000 claims abstract description 9
- 235000019418 amylase Nutrition 0.000 claims abstract description 9
- 238000012408 PCR amplification Methods 0.000 claims description 26
- 238000004925 denaturation Methods 0.000 claims description 26
- 230000036425 denaturation Effects 0.000 claims description 26
- 108020004414 DNA Proteins 0.000 claims description 24
- 241000894006 Bacteria Species 0.000 claims description 22
- 239000007788 liquid Substances 0.000 claims description 18
- 239000012154 double-distilled water Substances 0.000 claims description 16
- 230000000694 effects Effects 0.000 claims description 16
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 14
- 238000000137 annealing Methods 0.000 claims description 13
- WIIZWVCIJKGZOK-RKDXNWHRSA-N chloramphenicol Chemical compound ClC(Cl)C(=O)N[C@H](CO)[C@H](O)C1=CC=C([N+]([O-])=O)C=C1 WIIZWVCIJKGZOK-RKDXNWHRSA-N 0.000 claims description 13
- 229960005091 chloramphenicol Drugs 0.000 claims description 13
- 108091008146 restriction endonucleases Proteins 0.000 claims description 13
- 230000029087 digestion Effects 0.000 claims description 11
- 239000003292 glue Substances 0.000 claims description 11
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 claims description 10
- 239000000872 buffer Substances 0.000 claims description 10
- 238000001816 cooling Methods 0.000 claims description 10
- 239000002609 medium Substances 0.000 claims description 10
- 238000011084 recovery Methods 0.000 claims description 10
- 230000005611 electricity Effects 0.000 claims description 9
- 239000001963 growth medium Substances 0.000 claims description 9
- 239000002773 nucleotide Substances 0.000 claims description 9
- 125000003729 nucleotide group Chemical group 0.000 claims description 9
- 108091028043 Nucleic acid sequence Proteins 0.000 claims description 7
- 238000006243 chemical reaction Methods 0.000 claims description 7
- 239000013612 plasmid Substances 0.000 claims description 7
- FBPFZTCFMRRESA-KVTDHHQDSA-N D-Mannitol Chemical compound OC[C@@H](O)[C@@H](O)[C@H](O)[C@H](O)CO FBPFZTCFMRRESA-KVTDHHQDSA-N 0.000 claims description 6
- 229930195725 Mannitol Natural products 0.000 claims description 6
- 239000001888 Peptone Substances 0.000 claims description 6
- 108010080698 Peptones Proteins 0.000 claims description 6
- 239000000594 mannitol Substances 0.000 claims description 6
- 235000010355 mannitol Nutrition 0.000 claims description 6
- 235000019319 peptone Nutrition 0.000 claims description 6
- 239000007787 solid Substances 0.000 claims description 6
- 241000193830 Bacillus <bacterium> Species 0.000 claims description 5
- 229940041514 candida albicans extract Drugs 0.000 claims description 5
- 238000002360 preparation method Methods 0.000 claims description 5
- 239000011780 sodium chloride Substances 0.000 claims description 5
- 238000005406 washing Methods 0.000 claims description 5
- 239000012138 yeast extract Substances 0.000 claims description 5
- 239000003153 chemical reaction reagent Substances 0.000 claims description 4
- 239000012092 media component Substances 0.000 claims description 3
- 235000015097 nutrients Nutrition 0.000 claims description 3
- 238000012216 screening Methods 0.000 claims description 3
- FRXSZNDVFUDTIR-UHFFFAOYSA-N 6-methoxy-1,2,3,4-tetrahydroquinoline Chemical compound N1CCCC2=CC(OC)=CC=C21 FRXSZNDVFUDTIR-UHFFFAOYSA-N 0.000 claims description 2
- 241001052560 Thallis Species 0.000 claims description 2
- 230000003321 amplification Effects 0.000 claims description 2
- 239000000203 mixture Substances 0.000 claims description 2
- 238000003199 nucleic acid amplification method Methods 0.000 claims description 2
- 235000009508 confectionery Nutrition 0.000 claims 1
- 238000007873 sieving Methods 0.000 claims 1
- 101150013191 E gene Proteins 0.000 abstract description 15
- 238000004519 manufacturing process Methods 0.000 abstract description 15
- 239000012634 fragment Substances 0.000 abstract description 7
- 238000009825 accumulation Methods 0.000 abstract description 4
- 238000010960 commercial process Methods 0.000 abstract 1
- 239000000243 solution Substances 0.000 description 21
- 239000000047 product Substances 0.000 description 16
- 238000000034 method Methods 0.000 description 12
- 229920002472 Starch Polymers 0.000 description 8
- 238000000855 fermentation Methods 0.000 description 8
- 230000004151 fermentation Effects 0.000 description 8
- 239000008107 starch Substances 0.000 description 8
- 235000019698 starch Nutrition 0.000 description 8
- 238000000246 agarose gel electrophoresis Methods 0.000 description 7
- 230000001580 bacterial effect Effects 0.000 description 7
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 6
- 230000009182 swimming Effects 0.000 description 6
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 5
- 230000015572 biosynthetic process Effects 0.000 description 5
- 238000005259 measurement Methods 0.000 description 5
- 238000003756 stirring Methods 0.000 description 5
- 239000003795 chemical substances by application Substances 0.000 description 3
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 description 3
- 235000019441 ethanol Nutrition 0.000 description 3
- 239000002054 inoculum Substances 0.000 description 3
- 239000003550 marker Substances 0.000 description 3
- 238000004064 recycling Methods 0.000 description 3
- ZCYVEMRRCGMTRW-UHFFFAOYSA-N 7553-56-2 Chemical compound [I] ZCYVEMRRCGMTRW-UHFFFAOYSA-N 0.000 description 2
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical compound CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- 238000002835 absorbance Methods 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- 230000002068 genetic effect Effects 0.000 description 2
- 238000011534 incubation Methods 0.000 description 2
- 229910052740 iodine Inorganic materials 0.000 description 2
- 239000011630 iodine Substances 0.000 description 2
- 239000006210 lotion Substances 0.000 description 2
- 239000002002 slurry Substances 0.000 description 2
- 101150042065 spo0A gene Proteins 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- 238000011144 upstream manufacturing Methods 0.000 description 2
- 229920001817 Agar Polymers 0.000 description 1
- 241000193388 Bacillus thuringiensis Species 0.000 description 1
- 239000002028 Biomass Substances 0.000 description 1
- 241000193470 Clostridium sporogenes Species 0.000 description 1
- 101710151559 Crystal protein Proteins 0.000 description 1
- 238000007400 DNA extraction Methods 0.000 description 1
- 230000005526 G1 to G0 transition Effects 0.000 description 1
- 102000045595 Phosphoprotein Phosphatases Human genes 0.000 description 1
- 108700019535 Phosphoprotein Phosphatases Proteins 0.000 description 1
- 240000004808 Saccharomyces cerevisiae Species 0.000 description 1
- VMHLLURERBWHNL-UHFFFAOYSA-M Sodium acetate Chemical compound [Na+].CC([O-])=O VMHLLURERBWHNL-UHFFFAOYSA-M 0.000 description 1
- 102000004243 Tubulin Human genes 0.000 description 1
- 108090000704 Tubulin Proteins 0.000 description 1
- 239000012190 activator Substances 0.000 description 1
- 239000008272 agar Substances 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 229940097012 bacillus thuringiensis Drugs 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000012620 biological material Substances 0.000 description 1
- 238000004364 calculation method Methods 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 239000000306 component Substances 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
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- 230000007812 deficiency Effects 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- BNIILDVGGAEEIG-UHFFFAOYSA-L disodium hydrogen phosphate Chemical compound [Na+].[Na+].OP([O-])([O-])=O BNIILDVGGAEEIG-UHFFFAOYSA-L 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000012224 gene deletion Methods 0.000 description 1
- 238000012214 genetic breeding Methods 0.000 description 1
- 230000035784 germination Effects 0.000 description 1
- 230000002779 inactivation Effects 0.000 description 1
- 239000003262 industrial enzyme Substances 0.000 description 1
- 230000000977 initiatory effect Effects 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 238000011177 media preparation Methods 0.000 description 1
- 239000012533 medium component Substances 0.000 description 1
- 239000002207 metabolite Substances 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 239000008363 phosphate buffer Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 230000001376 precipitating effect Effects 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 102000004169 proteins and genes Human genes 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 230000006798 recombination Effects 0.000 description 1
- 238000005215 recombination Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 238000012772 sequence design Methods 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 239000001632 sodium acetate Substances 0.000 description 1
- 235000017281 sodium acetate Nutrition 0.000 description 1
- AJPJDKMHJJGVTQ-UHFFFAOYSA-M sodium dihydrogen phosphate Chemical compound [Na+].OP(O)([O-])=O AJPJDKMHJJGVTQ-UHFFFAOYSA-M 0.000 description 1
- 229910000162 sodium phosphate Inorganic materials 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 239000006228 supernatant Substances 0.000 description 1
- 238000012549 training Methods 0.000 description 1
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- 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
- C12N15/00—Mutation or genetic engineering; DNA or RNA concerning genetic engineering, vectors, e.g. plasmids, or their isolation, preparation or purification; Use of hosts therefor
- C12N15/09—Recombinant DNA-technology
- C12N15/63—Introduction of foreign genetic material using vectors; Vectors; Use of hosts therefor; Regulation of expression
- C12N15/74—Vectors or expression systems specially adapted for prokaryotic hosts other than E. coli, e.g. Lactobacillus, Micromonospora
- C12N15/75—Vectors or expression systems specially adapted for prokaryotic hosts other than E. coli, e.g. Lactobacillus, Micromonospora for Bacillus
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- C12N9/00—Enzymes; Proenzymes; Compositions thereof; Processes for preparing, activating, inhibiting, separating or purifying enzymes
- C12N9/14—Hydrolases (3)
- C12N9/24—Hydrolases (3) acting on glycosyl compounds (3.2)
- C12N9/2402—Hydrolases (3) acting on glycosyl compounds (3.2) hydrolysing O- and S- glycosyl compounds (3.2.1)
- C12N9/2405—Glucanases
- C12N9/2408—Glucanases acting on alpha -1,4-glucosidic bonds
- C12N9/2411—Amylases
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Abstract
The present invention relates to II E of sporulation related gene spo to influence the application in strain growth and producing enzyme.The present invention is in such a way that plug-in type inactivates, by II E partial gene fragments of spo and CmrGene Fusion, II E-Cm of fusion sporIt is inserted into II E gene order of Bacillus clausii spo, make II E gene of spo can not normal expression and inactivate, II E gene deactivated strain of spo can not only be such that gemma production rate significantly reduces to 0.3%, and makes the quickening more obvious than original strain of the engineered strain speed of growth, realize the fermenting and producing of the amylase of the accumulation and higher vigor of cell quantity in a shorter time.The present invention constructs the Bacillus clausii of low gemma yield, and overcome Bacillus clausii cannot achieve the problem of high density is continuously fermented in commercial process, can effectively improve the production intensity of target enzyme, be with a wide range of applications.
Description
Technical field
The present invention relates to II E of sporulation related gene spo to influence the application in strain growth and producing enzyme, belongs to point
Sub- biology techniques field.
Background technique
Bacillus clausii (Bacillus clausii) is industrial enzyme production bacterial strain, in process of production with gemma
Formation fermentation can be had an impact, the yield of limited target enzyme, reduce production efficiency.Constructing gemma missing bacterium is to a gram Lloyd's
The important directions that the cell factories such as bacillus are transformed.There are many sporulation related gene, as spo0A, sigmaE,
SigmaK etc., single-gene function and Interaction among genes relationship existing research report of these genes during sporulation,
In, II E of Spo is the Major modulators in gemma process, is in forespore forming process necessary to SigmaF factor activator
Phosphoprotein phosphatase, in genoneme formation, the tubulin homologous protein FtsZ positioned at cell center is passing through a spiral shell
It can be re-positioned near bacterium the two poles of the earth after rotation structural transition, this repositioning of expression initiation of II E of spo, one wherein
Site inspires bacterium mal-distribution, and then pushes being differentiated to form for gemma.Further study show that gemma gene not only influences
The formation of gemma also has adjustment effect, such as the spo0A of certain threshold value for the structure of bacterial strain, growth, metabolite generation etc.
It can promote the formation of thallus envelope;III D of spo in bacillus thuringiensis be only formed gemma institute it is necessary, also with crystal
Protein expression is related;In clostridium sporogene, sporulation related gene can influence sporulation, also with acetone, butanol etc.
The fermenting and producing of organic matter is related.And in Bacillus clausii, II E gene deletion strains of Spo are constructed, it can be in control gram
While the formation of Lloyd's's bacillus spore, the accumulation of strain growth speed and biomass is improved, improves the ectoenzymes such as amylase
Fermentative activity.
Summary of the invention
In view of the deficiencies of the prior art, the present invention provides II E of sporulation related gene spo influence strain growth and
Application in producing enzyme.
Technical scheme is as follows:
II E of sporulation related gene spo is influencing the application in strain growth and producing enzyme, II E's of gene spo
Nucleotide sequence is as shown in SEQ ID NO.1.
Preferred according to the present invention, the producing enzyme is to produce amylase, and the enzyme activity of amylase is 5~6 times of starting strain.
Preferred according to the present invention, II E of sporulation related gene spo is in influencing strain growth and producing enzyme
Using steps are as follows:
(1) genomic DNA for extracting Bacillus clausii, using genomic DNA as template progress PCR amplification, obtained gram
Lloyd's's bacillus spore forms II E of related gene spo, and the nucleotide sequence of II E of gene spo is as shown in SEQ ID NO.1;
(2) PCR amplification is carried out by template of pHT01 plasmid, amplification obtains CmrSegment, CmrThe nucleotide sequence of segment is such as
Shown in SEQ ID NO.2;
(3) by Cm made from II E of gene spo made from step (1) and step (2)rSegment is melted using over-lap PCR
It closes, obtains II E-Cm of fusion spor;
(4) by II E-Cm of fusion spo of step (3)rAfter digestion, then concentration converts Bacillus clausii
Competent cell is screened to obtain positive restructuring bacterium, that is, can be applied to thalli growth and producing enzyme.
Preferred according to the present invention, in the step (1), PCR amplification primer nucleotide sequences are as follows, and underscore is
BamHI restriction enzyme site:
II E-F of spo:CGCGGATCCCCTTAAAAGCGGAGCCAAAAC;
II E-R:GCCAGCAAAAAGCGTTCCTACAAGTAAGCC of spo;
PCR amplification system is as follows, 50 μ L of total volume:
2 × HiFi-PCR Master 25 μ L, II E-F of primer spo 2.5 μ L, II E-R of primer spo 2.5 μ L, Ke Lao
Family name's subtilis genomic dna 2.5 μ L, ddH2O 17.5μL;
PCR amplification program is as follows:
95 DEG C of initial denaturation 5min;95 DEG C of denaturation 30s, 53 DEG C of annealing 30s, 72 DEG C of extension 1min45s, totally 30 recycle;72
DEG C continue to extend 10min.
Preferred according to the present invention, in the step (2), PCR amplification primer nucleotide sequences are as follows, and underscore is
BamHI restriction enzyme site:
Cmr- F:CTTGTAGGAACGCTTTTTGCTGGCCTTTTGCTC;
Cmr- R:CGCGGATCCTAGTGACTGGCGATGCTG;
PCR amplification system is as follows, 50 μ L of total volume:
2 × HiFi-PCR Master 25 μ L, primer Cmr- F 2.5 μ L, primer Cmr2.5 μ L, pHT01 plasmid of-R, 2.5 μ
L, ddH2O 17.5μL;
PCR amplification program is as follows:
95 DEG C of initial denaturation 5min;95 DEG C of denaturation 30s, 55 DEG C of annealing 30s, 72 DEG C of extension 2min40s, totally 30 recycle;72
DEG C continue to extend 10min.
According to the present invention it is further preferred that in the step (3), the amplimer nucleotide sequence of over-lap PCR is as follows,
Underscore is BamHI restriction enzyme site:
II E-F of spo:CGCGGATCCCCTTAAAAGCGGAGCCAAAAC;
Cmr- R:CGCGGATCCTAGTGACTGGCGATGCTG;
First round over-lap PCR amplification system is as follows, 25 μ L of total volume:
II E segment of 2 × HiFi-PCR Master 12.5 μ L, glue recovery product spo 2 μ L, glue recovery product CmrSegment 2
μ L, ddH2O 8.5μL;
First round over-lap PCR amplification program is as follows:
95 DEG C of initial denaturation 5min;95 DEG C of denaturation 30s, 55 DEG C of annealing 30s, 72 DEG C of extension 2min40s, 5 recycle;72 DEG C after
It renews and stretches 10min;
Second wheel over-lap PCR amplification system is that following reagent is added on the basis of first round PCR amplification system:
2 × HiFi-PCR Master 12.5 μ L, II E-F of primer spo 1 μ L, primer Cmr- R 1 μ L, ddH2O 10.5μ
L;
Second wheel over-lap PCR amplification program is as follows:
95 DEG C of initial denaturation 5min;95 DEG C of denaturation 30s, 55 DEG C of annealing 30s, 72 DEG C of extension 4min25s, totally 30 recycle;72
DEG C continue to extend 10min.
Preferred according to the present invention, in the step (4), digestion system is as follows, 40 μ L of total volume:
20 μ L, 10 × K Buffer of overlapping PCR products, 4 I restriction endonuclease of μ L, BamH 2 μ L, ddH2O 14μL;
Digestion condition are as follows: 37 DEG C, 1.5h.
It is preferred according to the present invention, in the step (4), II E-Cm of fusion spo after concentrationrConcentration be 300~
500ng/μL。
According to the present invention it is further preferred that in the step (4), Bacillus clausii competent cell, step are converted
It is rapid as follows:
By the digestion products after concentration under conditions of 1500~1800V electrotransformation Bacillus clausii competent cell
4~5ms, then under the conditions of 37 DEG C in liquid resuscitation culture medium cultivate 3~4h to get.
It is further preferred that the liquid resuscitation nutrient media components are as follows, it is weight percentage:
Peptone 1%, yeast extract 0.5%, sodium chloride 1%, sorbierite 9%, mannitol 7%, excess water, pH=7.0
~7.4.
It is further preferred that the preparation step of the Bacillus clausii competent cell is as follows:
The fresh Bacillus clausii single colonie of picking, culture to cell concentration OD600=0.9~1.0, it is placed on ice
It is cooling, it is centrifuged after cooling, is then turned buffer washing thalline 3~5 times with the electricity of pre-cooling, electricity turns to dispense after thallus is resuspended in buffer
To the sterile EP tube of pre-cooling, Bacillus clausii competent cell is made.
Wherein, it is as follows to turn buffer composition for the electricity:
The sorbierite that mass percent is 9.1%, the mannitol that mass percent is 9.1%, percent by volume 10%
Glycerol, excess water.
Preferred according to the present invention, in the step (4), screening step is as follows:
Bacillus clausii after conversion is coated with the LB plate containing chloramphenicol, 37 DEG C of cultures 12~for 24 hours, it chooses positive
Bacterial strain, it is identified to get.
It is further preferred that the LB solid that it is 25 μm of ol/mL containing chloramphenicol concentration that the LB plate containing chloramphenicol, which is,
Culture medium.
Beneficial effect
1, the work present invention firstly discloses II E of sporulation related gene spo in terms of controlling strain growth speed
With in such a way that plug-in type inactivates, by II E partial gene fragments of spo and CmrGene Fusion, II E-Cm of fusion spor
Be inserted into II E gene order of Bacillus clausii spo in, make II E gene of spo can not normal expression and inactivate, II E base of spo
Because deactivated strain can not only be such that gemma production rate significantly reduces to 0.3%, and the engineered strain speed of growth is made to compare original bacteria
Strain is obvious to be accelerated, and the accumulation of cell quantity in a shorter time is realized;
2, the engineered strain that the present invention constructs improves the fermentation enzyme activity of amylase, and it is raw to be conducive to bacillus category enzyme preparation
Produce the genetic breeding and industrialized production of bacterial strain.
Detailed description of the invention
Fig. 1 is the agarose gel electrophoresis figure of II E genetic fragment of Bacillus clausii spo of the present invention;
In figure: swimming lane M is that DNA molecular amount marks (DNA marker), and swimming lane 1~3 is II E gene band of spo, size
For 793bp;
Fig. 2 is Cm of the present inventionrThe agarose gel electrophoresis figure of genetic fragment;
In figure: swimming lane M is that DNA molecular amount marks (DNA marker), and swimming lane 1~4 is CmrGene band, size are
1259bp;
Fig. 3 is the agarose gel electrophoresis figure that II E gene of Bacillus clausii spo of the present invention inactivates transformant verifying;
In figure: swimming lane M is that DNA molecular amount marks (DNA marker), and swimming lane 1~4 is transformant band, and size is
2028bp;
Fig. 4 is that II E deactivated strain of spo and starting strain cell concentration change line chart;
In figure: II E of B.clausii QL-1 Δ spo is II E deactivated strain of spo, and B.clausii QL-1 is bacterium germination
Strain.
Specific embodiment
Below with reference to embodiment, technical scheme is described further, but institute's protection scope of the present invention is not limited to
This.
Term used in this method generally there are those of ordinary skill in the art usually to manage unless otherwise specified
The meaning of solution.
Below in an example, be not described in detail and various processes and method are routine sides as known in the art
Method.The source of agents useful for same, product name and it is necessary to list its constituent person, are indicated on the first occurrence, thereafter
Same reagents used unless otherwise specified, is the same as indicated for the first time.
Biological material source:
Bacillus clausii (Bacillus clausii) in embodiment is received wound connection biotechnology purchased from Beijing North and is ground
Study carefully institute, bacterium numbering: BNCC160124, for common commercially available bacterial strain;
Plasmid pHT01 matches biological Co., Ltd purchased from Hangzhou treasured.
LB solid medium component is as follows, is mass percent:
Peptone 1%, yeast extract 0.5%, sodium chloride 1%, agar 2%, excess water, pH=7.0~7.4;
LB nutrient media components are as follows, are mass percent:
Peptone 1%, yeast extract 0.5%, sodium chloride 1%, excess water, pH=7.0~7.4
Embodiment 1: the preparation of target gene fragment
(I) is extracted Bacillus clausii genomic DNA and (is said according to Ezup pillar bacterial genomes DNA extraction agent box
Bright book)
According to the nucleotide sequence design primer of II E gene of spo, BamHI restriction enzyme site is introduced in upstream primer, under
It swims primer and adds Cmr10, the end the 5' base of segment, primer are synthesized by Sangon Biotech (Shanghai) Co., Ltd..Using
2 × HiFi-PCR Master polymerase of precious bioengineering Co., Ltd, using Bacillus clausii genomic DNA as template
Expand II E gene of spo.Primer nucleotide sequences are as follows, and what wherein underscore represented is BamHI restriction enzyme site.
II E-F of spo:CGCGGATCC CCTTAAAAGCGGAGCCAAAAC
II E-R:GCCAGCAAAAAGCGTTCCTACAAGTAAGCC of spo;
PCR amplification system is as follows, 50 μ L of total volume:
2 × HiFi-PCR Master 25 μ L, II E-F of primer spo 2.5 μ L, II E-R of primer spo 2.5 μ L, Ke Lao
Family name's subtilis genomic dna 2.5 μ L, ddH2O 17.5μL;
PCR amplification program is as follows:
95 DEG C of initial denaturation 5min;95 DEG C of denaturation 30s, 53 DEG C of annealing 30s, 72 DEG C of extension 1min45s, totally 30 recycle;72
DEG C continue to extend 10min.
Agarose gel electrophoresis examines PCR product, as a result as shown in Figure 1, the length of II E of target gene spo is 793bp
(SEQ ID NO.1), II E of PCR product spo that clone is obtained carry out glue using SanPrep pillar DNA plastic recovery kit
Recycling, -20 DEG C of gained DNA solution save backup.
(II) target gene CmrThe acquisition of gene
Using pHT01 plasmid as template, the Cm that is obtained through PCR amplificationrGenetic fragment.
Wherein the primer nucleotide sequences of PCR amplification are as follows, and BamHI restriction enzyme site, upstream primer are introduced in downstream primer
In addition II 14, the end E 3' base of spo, what wherein underscore represented is BamHI restriction enzyme site:
Cmr- F:CTTGTAGGAACGCTTTTTGCTGGCCTTTTGCTC
Cmr- R:CGCGGATCCTAGTGACTGGCGATGCTG;
PCR amplification system, 50 μ L of total volume:
2 × HiFi-PCR Master 25 μ L, primer Cmr- F 2.5 μ L, primer Cmr2.5 μ L, pHT01 plasmid of-R, 2.5 μ
L, ddH2O 17.5μL;
PCR amplification program is as follows:
95 DEG C of initial denaturation 5min;95 DEG C of denaturation 30s, 55 DEG C of annealing 30s, 72 DEG C of extension 2min40s, totally 30 recycle;72
DEG C continue to extend 10min.
Agarose gel electrophoresis examines PCR product, as a result as shown in Fig. 2, target gene CmrLength be 1259bp (SEQ
ID NO.2), the PCR product Cm that clone is obtainedrGlue recycling is carried out using SanPrep pillar DNA plastic recovery kit, DNA is molten
- 20 DEG C of liquid save backup.
(III) is by Cm made from II E of gene spo made from step (I) and step (II)rSegment is carried out using over-lap PCR
II E-Cm of spo is made in fusionrSegment;
Used primer nucleotide sequences are as follows, and what underscore represented is BamHI restriction enzyme site:
II E-F of spo:CGCGGATCC CCTTAAAAGCGGAGCCAAAAC
Cmr- R:CGCGGATCC TAGTGACTGGCGATGCTG
First round over-lap PCR amplification system is as follows, 25 μ L of total volume:
II E segment of 2 × HiFi-PCR Master 12.5 μ L, glue recovery product spo 2 μ L, glue recovery product CmrSegment 2
μ L, ddH2O 8.5μL;
First round over-lap PCR amplification program is as follows:
95 DEG C of initial denaturation 5min;95 DEG C of denaturation 30s, 55 DEG C of annealing 30s, 72 DEG C of extension 2min40s, 5 recycle;72 DEG C after
It renews and stretches 10min.
Second wheel over-lap PCR amplification system is that following reagent is added on the basis of first round PCR amplification system:
2 × HiFi-PCR Master 12.5 μ L, II E-F of primer spo 1 μ L, primer Cmr- R 1 μ L, ddH2O 10.5μ
L;
Second wheel over-lap PCR amplification program is as follows:
95 DEG C of initial denaturation 5min;95 DEG C of denaturation 30s, 55 DEG C of annealing 30s, 72 DEG C of extension 4min25s, totally 30 recycle;72
DEG C continue to extend 10min.
Equally, agarose gel electrophoresis examines PCR product, detects II E-Cm of target gene sporLength be
2028bp (SEQ ID NO.3), II E-Cm of PCR product spo that clone is obtainedrIt is recycled and is tried using SanPrep pillar DNA glue
Agent box carries out glue recycling, and -20 DEG C of gained DNA solution saves backup.
Embodiment 2: Bacillus clausii competence is prepared
The fresh Bacillus clausii single colonie of (I) picking, is inoculated in 10mL LB culture medium, 37 DEG C, 200r/min
Cultivate 12h;
(II) takes 2.0mL bacterium solution to be transferred to 50mL GM culture medium, and 37 DEG C, 200r/min cultivate 4h to OD600=1.0;
(III) bacterium solution is transferred to 50mL centrifuge tube, ice bath 10min;
(IV) 4 DEG C after ice bath, 5000r/min is centrifuged 5min, collects thallus;
(V) electricity of the thallus pre-cooling after being centrifuged turns buffer (ETM) and washs 3 times;
(VI) after washing, turn buffer using 1000 μ L electricity and thallus is resuspended;
(VII) competent cell prepared dispenses 100 μ L/ pipe, and -80 DEG C of preservations are spare.
Wherein, GM culture medium: LB culture medium+0.5mol/L sorbierite;
Electricity turns buffer (ETM): the sorbierite that mass percent is 9.1%, the mannitol that mass percent is 9.1%,
The glycerol that percent by volume is 10%, excess water.
II E-Cm of embodiment 3:sporSegment electrotransformation Bacillus clausii
(I) is by II E-Cm of sporSegment is digested with restriction enzyme BamH I;
Digestion system (40 μ L) is as follows:
10 × K Buffer, 4 I restriction endonuclease of μ L, BamH 2 μ L, over-lap PCR glue recovery product 20 μ L, ddH2O 14μL;
Digestion condition are as follows: 37 DEG C, 1.5h.
Digestion products are concentrated in (II)
1/10 volume 3mol/L sodium acetate and 2.5 times of volume dehydrated alcohols is added, is placed in -20 DEG C of refrigerator 20min;
12000r/min centrifugation 5min must be precipitated;The ethanol solution of 300 μ L75% (percent by volume) is added in precipitating, it is heavy to be resuspended
It forms sediment;12000r/min, is centrifuged 5min, and 37 DEG C of air-dried 30min remove ethyl alcohol;20 μ L ddH are added2DNA is resuspended in O, and -20 DEG C save,
It is spare.
(III) electrotransformation
Measure II E-Cm of sporFragment concentrations reach 470ng/ μ L, after competent cell and enriched product ice bath 5min
1500V, 5ms electrotransformation, cell cultivates 4h in 37 DEG C of recoveries through liquid resuscitation culture medium RM, after 4000r/min is centrifuged 5min,
100 μ L supernatants, which suspend, to be precipitated, and 25 μm of ol/mL chloramphenicol plates, 37 DEG C of constant temperature incubation 20h are coated with, and screening has chlorampenicol resistant
Transformant;
The liquid resuscitation culture medium RM component is as follows, is weight percentage:
Peptone 1%, yeast extract 0.5%, sodium chloride 1%, sorbierite 9%, mannitol 7%, excess water, pH=7.2.
Embodiment 4: the culture and identification of positive restructuring bacterium
The above-mentioned positive restructuring bacterium colony of picking, is inoculated into the LB liquid medium containing chlorampenicol resistant, 37 DEG C of culture 12h
Afterwards, bacterium solution multigelation 3~4 times, using bacterium solution as template, spo II E-F and Cmr- R is that primer carries out PCR amplification, amplified production
It is verified using agarose gel electrophoresis, verification result is as shown in Figure 3;
The PCR primer sequence is as follows;
II E-F of spo:CGCGGATCC CCTTAAAAGCGGAGCCAAAAC
Cmr- R:CGCGGATCC TAGTGACTGGCGATGCTG
Wherein, restriction enzyme site is identified with underscore.
The PCR amplification system is 25 μ L:
2 × HiFi-PCR Master, 12.5 μ L, 2 II E-F of μ L, spo of bacterium solution 1 μ L, Cmr- R 1 μ L, ddH2O 8.5μL;
PCR amplification program is as follows:
95 DEG C of initial denaturation 5min;95 DEG C of denaturation 30s, 55 DEG C of annealing 30s, 72 DEG C of extension 4min25s, 30 recycle;72℃
Continue to extend 10min.
Embodiment 5: the measurement of gemma production rate
(I) Example 4 is accredited as the strain of positive restructuring bacterium, in the LB solid culture containing 25 μm of ol/mL chloramphenicol
It is activated repeatedly in base 2 times, 37 DEG C of stationary culture 20h;It chooses single bacterium and falls within 10mL LB liquid medium, 37 DEG C, 200r/min culture
12h is inoculated in the 100mL LB liquid medium containing 25 μm of ol/mL chloramphenicol, 37 DEG C, 200r/ with 2% inoculum concentration
Min culture;
The measuring method of (II) gemma production rate are as follows:
The bacterium solution of culture 36h in step (I) is taken, 80 DEG C of water bath processing 10min, ice bath 5min dilute suitable multiple, take
100 μ L are coated with LB plate, and for 24 hours, plate count simultaneously calculates gemma production rate to 37 DEG C of constant temperature incubations, starting strain and nonheat-treated
Positive restructuring bacterial strain compares, and count results are as shown in table 1.
Wherein, gemma production rate (%)=(gemma number/total viable count) × 100%.
The measurement of II E deactivated strain gemma production rate of 1 starting strain of table and spo
It can be seen from the above result that recombination Bacillus clausii (II E gene of spo inactivation) gemma production rate is 0.3%,
Starting strain is that the gemma production rate of 89.5%, spo, II E gene deactivated strain is greatly lowered.
Embodiment 6: the measurement of growth cycle
(I) Example 4 is accredited as the strain of positive restructuring bacterium, in the LB solid culture containing 25 μm of ol/mL chloramphenicol
It is activated repeatedly in base 2 times, 37 DEG C of culture 20h;Choose single bacterium and fall within 10mL LB liquid medium, 37 DEG C, 200r/min cultivate 12h,
It is inoculated in the 100mL LB liquid medium containing 25 μm of ol/mL chloramphenicol with 2% inoculum concentration, 37 DEG C, 200r/min training
It supports;
(II) is sampled every 2~4h, and dilution suitable multiple measures spectrophotometric value under 600nm.
The variation of spectrophotometric value is as shown in figure 4, as the result is shown: II E gene deactivated strain of spo is logarithm in 2~18h
Growth period, 18~28h are stationary phase, are decline phase after 28h, and II E gene deactivated strain OD during measurement of spo600All
Greater than starting strain, thallus accumulation in the unit time is effectively increased.
Embodiment 7: the enzyme activity determination of amylase
The II E gene deactivated strain of spo that (I) starting strain and embodiment 4 are identified is in containing 25 μm of ol/mL chloramphenicol
It is activated repeatedly in LB solid medium 2 times, 37 DEG C of stationary culture 20h;It chooses single bacterium and falls within 10mL LB liquid medium, 37 DEG C,
200r/min cultivates 12h, is inoculated in the 100mL fermentation medium containing 25 μm of ol/mL chloramphenicol with 3% inoculum concentration, 37
DEG C, 200r/min culture;After 72h, fermentation culture is taken, through clasmatosis, starch enzyme purification, obtains enzyme solution to be measured;
(II) amylase enzyme activity determination method particularly includes: draw 20.0mL soluble starch solution in test tube, be added
Phosphate buffer 5.0mL after shaking up, is placed in 60 DEG C of waters bath with thermostatic control and preheats 8min;Step (i) system that 1.0mL has diluted is added
Standby enzyme solution to be measured, immediately timing shake up, and react 5min;1.0mL reaction solution is drawn with automatic pipettor immediately, is added in advance
It does not fill and terminates reaction in the test tube of 0.5mL 0.1mol/L hydrochloric acid solution, add the dilute iodine solution of 5.0mL, not plus dilute iodine of reaction solution
Liquid is blank, measures absorbance under 660nm wavelength, according to tables of data check in absorbance corresponding to enzyme solution concentration.
(III) enzyme activity calculation formula: X=c × n
In formula: the enzyme activity [IU/g (IU/mL)] of X- sample
The concentration (IU/mL) of c- sample enzyme solution
The extension rate of n- sample
Enzyme activity definition: 1mL liquid enzymes, in 60 DEG C, under the conditions of pH=6.0, enzyme amount needed for 1h liquefaction 1g soluble starch, i.e.,
For 1 enzyme activity unit (U/mL).
By the measurement of dry weight, amylase enzyme-activity unit U/mL is scaled U/g.
The fermentation medium preparation method is as follows:
A. 2g (being accurate to 0.001g) soluble starch is weighed in beaker, is tuned into slurry with a small amount of water, while stirring
It is slowly added into 40mL boiling water, the beaker of dress starch is then rinsed with moisture time, washing lotion is poured into wherein, is heated with stirring to completely thoroughly
It is bright, it is cooling, 1g peptone and 2g yeast powder is added, stirring is settled to 50mL to after dissolving, and 121 DEG C, 20min sterilizing is spare.
B. 2.66g Na is weighed2HPO4With 0.66g NaH2PO4, 50mL is settled to after being dissolved in water, 121 DEG C, 20min goes out
Bacterium, it is spare.
A liquid and B liquid cooling are but mixed afterwards, as fermentation medium.
The soluble starch solution preparation method is as follows:
2.000g (being accurate to 0.001g) soluble starch is weighed in beaker, is tuned into slurry, side stirring with a small amount of water
While being slowly added into 70mL boiling water, the beaker of dress starch is then rinsed with moisture time, washing lotion is poured into wherein, is heated with stirring to completely
Transparent, cooling is settled to 100mL.
The phosphoric acid buffer liquid is as follows: weighing 45.23g disodium hydrogen phosphate and 8.07g citric acid, use is water-soluble
Solution is settled to 1000mL, adjusts pH=6.0.
It is computed, amylase enzyme activity is 4.8 × 10 after II E deactivated strain of spo fermentation 72h5U·g-1, starting strain fermentation
Amylase enzyme activity is 0.86 × 10 after 72h5U·g-1, the amylase enzyme activity of II E deactivated strain of spo is the 5.58 of starting strain
Times, II E deactivated strain of spo effectively improves compared with starting strain amylase fermentative activity.
SEQUENCE LISTING
<110>Qilu University of Technology
<120>II E of sporulation related gene spo is influencing the application in strain growth and producing enzyme
<160> 3
<170> PatentIn version 3.5
<210> 1
<211> 793
<212> DNA
<213> Bacillus clausii
<400> 1
ccttaaaagc ggagccaaaa cggtgcttta tgattggggc atattcattg ccattcttgg 60
ttttctgcta ggaagggcta tgattttatc agagttgacg ccatttatct tgccattctt 120
ggcggccgtg ttcttgttaa gacgctctca atcactcatt gctgcagctt cattattagc 180
aggtgctgtg ttcagtttcc atggtcagtt gatttttgcg attgcaggga tcgggttttt 240
tcttattctg tacaaatgta tgaaaatgtt catgaagtac cctgctaaat cgctccctta 300
tcttgtgttt tcagctagta tcgccacgag gctgtcactc gtatttttga cagaaggtgg 360
attaagccaa tatgcgatga tgatggctac agtcgaagcg gcgcttagct ttatcctgac 420
aatgatcttt atccaaagca taccgcttgt gacaggaaaa agaggcggac aagcactccg 480
gaatgaagaa attatttgtt taattatttt gcttgcctct gtaatgacag gaacagtcgg 540
ttggacgata aatgaagctg tgcttcagca tagctttgca agttatctcg ttttagtgtt 600
tgcttttgtt ggcggggctg caataggctc gactgtcgga gtggtgacag gcttgatttt 660
aagcttggcc agtttagcaa gtctttatca gatgagtctg cttgcctttg caggcttgtt 720
aggagggttg ttaaaggaag ggaaacggat cggcgtgtca cttggcttac ttgtaggaac 780
gctttttgct ggc 793
<210> 2
<211> 1259
<212> DNA
<213>artificial sequence
<400> 2
cttgtaggaa cgctttttgc tggccttttg ctcacatgtt ctttcctgcg ttatcccctg 60
attctgtgga taaccgtatt accgcctttg agtgagctga taccgctcgc cgcagccgaa 120
cgaccgagcg cagcgagtca gtgagcgagg aagcggaaga gcgcccaata cgcatgctta 180
agttattggt atgactggtt ttaagcgcaa aaaaagttgc tttttcgtac ctattaatgt 240
atcgttttag aaaaccgact gtaaaaagta cagtcggcat tatctcatat tataaaagcc 300
agtcattagg cctatctgac aattcctgaa tagagttcat aaacaatcct gcatgataac 360
catcacaaac agaatgatgt acctgtaaag atagcggtaa atatattgaa ttacctttat 420
taatgaattt tcctgctgta ataatgggta gaaggtaatt actattatta ttgatattta 480
agttaaaccc agtaaatgaa gtccatggaa taatagaaag agaaaaagca ttttcaggta 540
taggtgtttt gggaaacaat ttccccgaac cattatattt ctctacatca gaaaggtata 600
aatcataaaa ctctttgaag tcattcttta caggagtcca aataccagag aatgttttag 660
atacaccatc aaaaattgta taaagtggct ctaacttatc ccaataacct aactctccgt 720
cgctattgta accagttcta aaagctgtat ttgagtttat cacccttgtc actaagaaaa 780
taaatgcagg gtaaaattta tatccttctt gttttatgtt tcggtataaa acactaatat 840
caatttctgt ggttatacta aaagtcgttt gttggttcaa ataatgatta aatatctctt 900
ttctcttcca attgtctaaa tcaattttat taaagttcat ttgatatgcc tcctaaattt 960
ttatctaaag tgaatttagg aggcttactt gtctgctttc ttcattagaa tcaatccttt 1020
tttaaaagtc aatattactg taacataaat atatatttta aaaatatccc actttatcca 1080
attttcgttt gttgaactaa tgggtgcttt agttgaagaa taaaagacca cattaaaaaa 1140
tgtggtcttt tgtgtttttt taaaggattt gagcgtagcg aaaaatcctt ttctttctta 1200
tcttgataat aagggtaact attgccgatc gtccattccg acagcatcgc cagtcacta 1259
<210> 3
<211> 2028
<212> DNA
<213>artificial sequence
<400> 3
ccttaaaagc ggagccaaaa cggtgcttta tgattggggc atattcattg ccattcttgg 60
ttttctgcta ggaagggcta tgattttatc agagttgacg ccatttatct tgccattctt 120
ggcggccgtg ttcttgttaa gacgctctca atcactcatt gctgcagctt cattattagc 180
aggtgctgtg ttcagtttcc atggtcagtt gatttttgcg attgcaggga tcgggttttt 240
tcttattctg tacaaatgta tgaaaatgtt catgaagtac cctgctaaat cgctccctta 300
tcttgtgttt tcagctagta tcgccacgag gctgtcactc gtatttttga cagaaggtgg 360
attaagccaa tatgcgatga tgatggctac agtcgaagcg gcgcttagct ttatcctgac 420
aatgatcttt atccaaagca taccgcttgt gacaggaaaa agaggcggac aagcactccg 480
gaatgaagaa attatttgtt taattatttt gcttgcctct gtaatgacag gaacagtcgg 540
ttggacgata aatgaagctg tgcttcagca tagctttgca agttatctcg ttttagtgtt 600
tgcttttgtt ggcggggctg caataggctc gactgtcgga gtggtgacag gcttgatttt 660
aagcttggcc agtttagcaa gtctttatca gatgagtctg cttgcctttg caggcttgtt 720
aggagggttg ttaaaggaag ggaaacggat cggcgtgtca cttggcttac ttgtaggaac 780
gctttttgct ggccttttgc tcacatgttc tttcctgcgt tatcccctga ttctgtggat 840
aaccgtatta ccgcctttga gtgagctgat accgctcgcc gcagccgaac gaccgagcgc 900
agcgagtcag tgagcgagga agcggaagag cgcccaatac gcatgcttaa gttattggta 960
tgactggttt taagcgcaaa aaaagttgct ttttcgtacc tattaatgta tcgttttaga 1020
aaaccgactg taaaaagtac agtcggcatt atctcatatt ataaaagcca gtcattaggc 1080
ctatctgaca attcctgaat agagttcata aacaatcctg catgataacc atcacaaaca 1140
gaatgatgta cctgtaaaga tagcggtaaa tatattgaat tacctttatt aatgaatttt 1200
cctgctgtaa taatgggtag aaggtaatta ctattattat tgatatttaa gttaaaccca 1260
gtaaatgaag tccatggaat aatagaaaga gaaaaagcat tttcaggtat aggtgttttg 1320
ggaaacaatt tccccgaacc attatatttc tctacatcag aaaggtataa atcataaaac 1380
tctttgaagt cattctttac aggagtccaa ataccagaga atgttttaga tacaccatca 1440
aaaattgtat aaagtggctc taacttatcc caataaccta actctccgtc gctattgtaa 1500
ccagttctaa aagctgtatt tgagtttatc acccttgtca ctaagaaaat aaatgcaggg 1560
taaaatttat atccttcttg ttttatgttt cggtataaaa cactaatatc aatttctgtg 1620
gttatactaa aagtcgtttg ttggttcaaa taatgattaa atatctcttt tctcttccaa 1680
ttgtctaaat caattttatt aaagttcatt tgatatgcct cctaaatttt tatctaaagt 1740
gaatttagga ggcttacttg tctgctttct tcattagaat caatcctttt ttaaaagtca 1800
atattactgt aacataaata tatattttaa aaatatccca ctttatccaa ttttcgtttg 1860
ttgaactaat gggtgcttta gttgaagaat aaaagaccac attaaaaaat gtggtctttt 1920
gtgttttttt aaaggatttg agcgtagcga aaaatccttt tctttcttat cttgataata 1980
agggtaacta ttgccgatcg tccattccga cagcatcgcc agtcacta 2028
Claims (10)
1. II E of sporulation related gene spo is influencing the application in strain growth and producing enzyme, which is characterized in that the gene
The nucleotide sequence of II E of spo is as shown in SEQ ID NO.1.
2. II E of sporulation related gene spo as described in claim 1 is influencing the application in strain growth and producing enzyme,
It is characterized in that, the producing enzyme is to produce amylase, and the enzyme activity of amylase is 5~6 times of starting strain.
3. II E of sporulation related gene spo as described in claim 1 is influencing the application in strain growth and producing enzyme,
It is characterized in that, steps are as follows:
(1) genomic DNA for extracting Bacillus clausii carries out PCR amplification by template of genomic DNA, gram Lloyd's is made
Bacillus spore forms II E of related gene spo, and the nucleotide sequence of II E of gene spo is as shown in SEQ ID NO.1;
(2) PCR amplification is carried out by template of pHT01 plasmid, amplification obtains CmrSegment, CmrThe nucleotide sequence of segment such as SEQ
Shown in ID NO.2;
(3) by Cm made from II E of gene spo made from step (1) and step (2)rSegment is merged using over-lap PCR, is obtained
II E-Cm of fusion spor;
(4) by II E-Cm of fusion spo of step (3)rAfter digestion, then concentration converts Bacillus clausii, through sieving
Positive strain is selected to obtain, that is, can be applied to thalli growth and producing enzyme;Preferably, II E-Cm of fusion spo after the concentrationr's
Concentration is 300~500ng/ μ L.
4. application as claimed in claim 3, which is characterized in that in step (1), the primer nucleotide sequences of the PCR amplification
It is as follows:
II E-F of spo:CGCGGATCCCCTTAAAAGCGGAGCCAAAAC;
II E-R:GCCAGCAAAAAGCGTTCCTACAAGTAAGCC of spo;
PCR amplification system is as follows, 50 μ L of total volume:
2 × HiFi-PCR Master 25 μ L, II E-F of primer spo 2.5 μ L of 2.5 μ L, II E-R of primer spo, gram Lloyd's's gemma
Vaccae genomic dna 2.5 μ L, ddH2O 17.5μL;
PCR amplification program is as follows:
95 DEG C of initial denaturation 5min;95 DEG C of denaturation 30s, 53 DEG C of annealing 30s, 72 DEG C of extension 1min45s, totally 30 recycle;72 DEG C after
It renews and stretches 10min.
5. application as claimed in claim 3, which is characterized in that in step (2), the primer nucleotide sequences of the PCR amplification
It is as follows:
Cmr- F:CTTGTAGGAACGCTTTTTGCTGGCCTTTTGCTC;
Cmr- R:CGCGGATCCTAGTGACTGGCGATGCTG;
PCR amplification system is as follows, 50 μ L of total volume:
2 × HiFi-PCR Master 25 μ L, primer Cmr- F 2.5 μ L, primer Cmr2.5 μ L, pHT01 plasmid of-R, 2.5 μ L,
ddH2O 17.5μL;
PCR amplification program is as follows:
95 DEG C of initial denaturation 5min;95 DEG C of denaturation 30s, 55 DEG C of annealing 30s, 72 DEG C of extension 2min40s, totally 30 recycle;72 DEG C after
It renews and stretches 10min.
6. application as claimed in claim 3, which is characterized in that in step (3), the amplimer nucleotide of the over-lap PCR
Sequence is as follows:
II E-F of spo:CGCGGATCCCCTTAAAAGCGGAGCCAAAAC;
Cmr- R:CGCGGATCCTAGTGACTGGCGATGCTG;
First round over-lap PCR amplification system is as follows, 25 μ L of total volume:
II E segment of 2 × HiFi-PCR Master 12.5 μ L, glue recovery product spo 2 μ L, glue recovery product Cmr2 μ L of segment,
ddH2O 8.5μL;
First round over-lap PCR amplification program is as follows:
95 DEG C of initial denaturation 5min;95 DEG C of denaturation 30s, 55 DEG C of annealing 30s, 72 DEG C of extension 2min40s, 5 recycle;72 DEG C after reneing
Stretch 10min;
Second wheel over-lap PCR amplification system is that following reagent is added on the basis of first round PCR system:
2 × HiFi-PCR Master 12.5 μ L, II E-F of primer spo 1 μ L, primer Cmr- R 1 μ L, ddH2O 10.5μL;
Second wheel over-lap PCR amplification program is as follows:
95 DEG C of initial denaturation 5min;95 DEG C of denaturation 30s, 55 DEG C of annealing 30s, 72 DEG C of extension 4min25s, totally 30 recycle;72 DEG C after
It renews and stretches 10min.
7. application as claimed in claim 3, which is characterized in that in step (4), the reaction system of the digestion is as follows, overall
40 μ L of product:
20 μ L, 10 × K Buffer of overlapping PCR products, 4 I restriction endonuclease of μ L, BamH 2 μ L, ddH2O 14μL;
Digestion condition are as follows: 37 DEG C, 1.5h.
8. application as claimed in claim 3, which is characterized in that in step (4), the conversion Bacillus clausii, step
It is as follows:
By the digestion products after concentration under conditions of 1500~1800V electrotransformation Bacillus clausii competent cell 4~
5ms, then under the conditions of 37 DEG C in liquid resuscitation culture medium cultivate 3~4h to get;
Wherein liquid resuscitation nutrient media components are as follows, are weight percentage:
Peptone 1%, yeast extract 0.5%, sodium chloride 1%, sorbierite 9%, mannitol 7%, excess water, pH=7.0~
7.4。
9. application as claimed in claim 8, which is characterized in that the preparation step of the Bacillus clausii competent cell
It is as follows:
The fresh Bacillus clausii single colonie of picking, culture to cell concentration OD600=0.9~1.0, it is placed in cooled on ice,
It is centrifuged after cooling, is then turned buffer washing thalline 3~5 times with the electricity of pre-cooling, electricity turns to dispense after thallus is resuspended in buffer to pre-
Bacillus clausii competent cell is made in cold sterile EP tube;
Wherein it is as follows to turn buffer composition for electricity:
Mass percent be 9.1% sorbierite, mass percent be 9.1% mannitol, percent by volume be 10% it is sweet
Oil, excess water.
10. application as claimed in claim 3, which is characterized in that in step (4), the step of screening is as follows:
By after conversion Bacillus clausii be coated with the LB plate containing chloramphenicol, 37 DEG C culture 12~for 24 hours, choose positive bacteria
Strain, it is identified to get;
Wherein the LB plate containing chloramphenicol is the LB solid medium for being 25 μm of ol/mL containing chloramphenicol concentration.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201810886538.5A CN108929883B (en) | 2018-08-06 | 2018-08-06 | Application of spoIII E gene related to sporulation in influencing growth of strain and producing enzyme |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN201810886538.5A CN108929883B (en) | 2018-08-06 | 2018-08-06 | Application of spoIII E gene related to sporulation in influencing growth of strain and producing enzyme |
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CN110055204A (en) * | 2019-05-10 | 2019-07-26 | 齐鲁工业大学 | A kind of method and application for knocking out II Q and pcf gene of spo and improving the lichen bacillus ferments producing enzyme |
CN113621540A (en) * | 2021-08-11 | 2021-11-09 | 沈阳农业大学 | Bacillus clausii strain and screening method and application thereof |
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