A kind of method improving chrysanthemum esters digestive enzyme expression
[technical field]
The present invention relates to field of microbial fermentation, be specifically related to prokaryotic expression system one and can improve chrysanthemum esters digestive enzyme table
The method of the amount of reaching.
[background technology]
Prokaryotic expression system, is one of current most widely used heterologous gene expression system, and conventional has escherichia coli
Expression system, bacillus subtilis expression system, Expression System of streptomyces etc., the most normal with escherichia expression system the most again
See.Escherichia expression system advantage is can to obtain gene expression product within a short period of time and required cost is relative
Ratio is less expensive, has been applied to the expression of chrysanthemum esters digestive enzyme.BLR (DE3) is a kind of protease-deficient Type B bacterial strain, for
The BL21recA that A.Roca (University of Wisconsin) builds derives bacterium, can stablize some with repetitive sequence
Genes of interest.
Pyrethrin pesticide is a widely used insecticide of class, has been widely applied in modern agriculture, due to they
Extensively application creates certain impact to ecological environment, and this environmental problem of pesticide residues receives publicity in recent years, utilizes biology
Biodegrading process can solve Pesticides Residues, becomes the study hotspot of environmental science.The scholars such as domestic existing Zhongshan University are to it
The screening of digestive enzyme and the clone of degrading enzyme gene have done a series of research.As CN 201010547206.8 has recombinated est825,
Construct recombinant expressed E. coli BL21 (DE3)/pET-28a-est825 to be used for preparing digestive enzyme.Huang Hao etc.
People uses lactose fermentation in CN 201210412214.0, improves the yield of digestive enzyme, and right above-mentioned enzyme powder yield is the most relatively
Low.
[summary of the invention]
It is an object of the invention to for prior art not enough, develop a kind of side improving chrysanthemum esters digestive enzyme expression
Method.
For reaching above-mentioned purpose, the invention provides a kind of method improving chrysanthemum esters digestive enzyme expression, including following
Step:
1) preparation produces strain E. coli BLR (DE3)/pET-28a-est825;
The sequence of est825 is referred to patent CN 201210412214.0, and genetic engineering builds the operation of host cell
It is referred to patent CN 201010547206.8.
2) seed culture is carried out;
3) fermentation culture is carried out: when fed-batch fermentation cultivates the OD to thalline600nmWhen value reaches 120-140, disposably add
The mixing inducing solution (molar concentration rate is 7:3) of lactose+isopropylthio galactose (IPTG), makes above-mentioned mixing in fermentation liquid
The concentration of induction is 9-13g/L, is down to temperature and starts induction, Induction Process relaying afterflow glycerol adding and yeast powder to 30-35 DEG C
Mixing feed supplement liquid, maintaining the concentration of glycerol in fermentation liquid is 1-2g/L, and the time of induction continues 6-7h;
In some embodiments, the substrate cultivation base of fermentation can be NZCYM culture medium or LB culture medium;At other
In embodiment, the pH of described fermentation medium is 6.8, and described fermentation medium includes following components: glycerol 5-8g/L, albumen
Peptone 3-10g/L, yeast powder 3-8g/L, (NH4)2SO4 5-10g/L, MgSO4 7H2O 1-3g/L, KH2PO4 3.4-6.85g/
L, K2HPO4·12H2O 5.68-11.35g/L, liquid microelement 1-2mL/L, kanamycin 50-100mg/L.
4), after fermentation ends, centrifugal collection thalline at a temperature of 4-8 DEG C, by thalline with containing 0.005mol/L benzyl
The phosphate buffered saline of the pH6.5-7.0 of sulfuryl fluoride becomes the bacteria suspension of mass concentration 15%-20%, by bacteria suspension at 4-8
20KHz ultrasonication at a temperature of DEG C, broken liquid is centrifugal prepares supernatant, and lyophilizing i.e. obtains enzyme powder.
The research of chrysanthemum esters biodegradable enzyme is the most relatively fewer, through the numerous studies of the present inventor, the choosing of host cell
Select, for expressing this biodegradable enzyme, exceed more than 20% than using expression under BL21 (DE3) same case;Use and close
The suitable lactose of ratio and the mixed solution of lactose analog carry out adding a small amount of Phenylmethanesulfonyl fluoride in induction and disruption solution
Can beneficially obtain higher enzyme powder volume of production.By the preparation method of the present invention, can obtain being not less than the high activity of 200g/L
The enzyme powder amount of chrysanthemum esters digestive enzyme.
Detailed description of the invention
The following stated is the preferred embodiment of the present invention, and what the present invention was protected is not limited to the following side of being preferable to carry out
Formula.It should be pointed out that, for a person skilled in the art these innovation and creation conceive on the basis of, the some deformation made and
Improve, broadly fall into protection scope of the present invention.
The assay method that the glycerol of example below, cell concentration and enzyme are lived is with reference to patent CN 201210412214.0.
Embodiment 1
1. using recombination bacillus coli E.coli BLR (DE3)/pET-28a-est825 as producing strain, will with glycerol pipe
Produce strain to preserve at a temperature of-86 DEG C.
2. seed culture: the strain that produces in glycerol pipe is accessed shake-flask seed culture medium by the inoculum concentration of 1.5%, to turn
Speed for 220r/min, temperature be 37 DEG C, condition of culture in constant-temperature table, cultivate 10h;The pH of described shake-flask seed culture medium is
7.0, described shake-flask seed culture medium is the LB culture medium containing kanamycin 50mg/L.
3. fermentation culture: cultured seed liquor is accessed the fermentation equipped with 5.5L fermentation medium with the inoculum concentration of 4%
Through row fermentation culture in tank, the time of fermentation culture is 26h, maintains oxygen dissolving value 20%, and ventilation is 3vvm, speed of agitator
1000r/min, fermentation temperature 37 DEG C, the pH using the ammonia of 25% and the hydrochloric acid solution of 3mol/L to control fermentation liquid is 6.8;Send out
The pH of ferment culture medium is 6.8, and this experiment fermentation medium comprises: glycerol 5g/L, peptone 10g/L, yeast powder 8g/L, (NH4)2SO45g/L, MgSO4·7H2O 3g/L, KH2PO43.4g/L, K2HPO4·12H2O 11.35g/L, liquid microelement 1mL/L,
Kanamycin 50mg/L.Above-mentioned liquid microelement includes: CaCl22.0g/L, ZnSO4·7H2O 5.0g/L, MnSO4·H2O
0.5g/L, Na2-EDTA 18.0g/L, FeSO4·7H2O 10.0g/L, CuSO4·5H2O 2.5g/L, CoCl2·6H2O0.2g/
L, (NH4)6Mo7O24·4H2O 0.1g/L。
4. fed-batch fermentation is cultivated: after fermentation culture 4h, stream glycerol adding and the mixing feed supplement liquid of yeast powder, controls the ratio of thalline
Growth rate is 0.1-0.2h-1, fed-batch fermentation cultivation stage duration is 7h;The mixing feed supplement of described glycerol and yeast powder
Liquid includes following components: glycerol 500g/L, yeast powder 100g/L, kanamycin 50mg/L;
5. carry out fermentation culture: when fed-batch fermentation cultivates the OD to thalline600nmWhen value reaches about 130, disposably add
The mixing inducing solution (molar concentration rate is 7:3) of lactose+IPTG, making the concentration of above-mentioned mixing induction in fermentation liquid is 9/L, fall
Start induction, Induction Process relaying afterflow glycerol adding and the mixing feed supplement liquid of yeast powder to temperature to 30 DEG C, maintain in fermentation liquid
The concentration of glycerol is 1g/L, and the time of induction continues 7h.
6. post processing: after fermentation ends, centrifugal collection thalline at a temperature of 4-8 DEG C, by thalline with containing 0.005mol/
The phosphate buffered saline of the pH6.5 of L Phenylmethanesulfonyl fluoride becomes the bacteria suspension of mass concentration 20%, by bacteria suspension at 4 DEG C
At a temperature of, 20KHz ultrasonication, broken liquid is centrifugal prepares supernatant, and lyophilizing i.e. obtains enzyme powder, and enzyme powder yield is 267g/L.Enzyme is lived
For 70000U/g.
Embodiment 2
1. using recombination bacillus coli E.coli BLR (DE3)/pET-28a-est825 as producing strain, will with glycerol pipe
Produce strain to preserve at a temperature of-86 DEG C.
2. seed culture: the strain that produces in glycerol pipe is accessed shake-flask seed culture medium by the inoculum concentration of 1.5%, to turn
Speed for 220r/min, temperature be 37 DEG C, condition of culture in constant-temperature table, cultivate 10h;The pH of described shake-flask seed culture medium is
7.0, described shake-flask seed culture medium is the LB culture medium containing kanamycin 50mg/L.
3. fermentation culture: cultured seed liquor is accessed the fermentation equipped with 5.5L fermentation medium with the inoculum concentration of 4%
Through row fermentation culture in tank, the time of fermentation culture is 26h, maintains oxygen dissolving value 20%, and ventilation is 3vvm, speed of agitator
1000r/min, fermentation temperature 37 DEG C, the pH using the ammonia of 25% and the hydrochloric acid solution of 3mol/L to control fermentation liquid is 6.8;Send out
The pH of ferment culture medium is 6.8, and this experiment fermentation medium comprises: glycerol 8g/L, peptone 3g/L, yeast powder 3g/L, (NH4)2SO410g/L, MgSO4·7H2O 1g/L, KH2PO46.85g/L, K2HPO4·12H2O 5.68g/L, liquid microelement 1mL/
L, kanamycin 50mg/L.Above-mentioned liquid microelement includes: CaCl22.0g/L, ZnSO4·7H2O 5.0g/L, MnSO4·H2O
0.5g/L, Na2-EDTA 18.0g/L, FeSO4·7H2O 10.0g/L, CuSO4·5H2O 2.5g/L, CoCl2·6H2O0.2g/
L, (NH4)6Mo7O24·4H2O 0.1g/L;
4. fed-batch fermentation is cultivated: after fermentation culture 4h, stream glycerol adding and the mixing feed supplement liquid of yeast powder, controls the ratio of thalline
Growth rate is 0.1-0.2h-1, fed-batch fermentation cultivation stage duration is 9h;The mixing feed supplement of described glycerol and yeast powder
Liquid includes following components: glycerol 500g/L, yeast powder 100g/L, kanamycin 50mg/L;
5. carry out fermentation culture: when fed-batch fermentation cultivates the OD to thalline600nmWhen value reaches about 130, disposably add
The mixing inducing solution (molar concentration rate is 7:3) of lactose+IPTG, making the concentration of above-mentioned mixing induction in fermentation liquid is 9/L, fall
Start induction, Induction Process relaying afterflow glycerol adding and the mixing feed supplement liquid of yeast powder to temperature to 30 DEG C, maintain in fermentation liquid
The concentration of glycerol is 1g/L, and the time of induction continues 7h.
6. post processing: after fermentation ends, centrifugal collection thalline at a temperature of 4-8 DEG C, by thalline with containing 0.005mol/
The phosphate buffered saline of the pH6.5 of L Phenylmethanesulfonyl fluoride becomes the bacteria suspension of mass concentration 20%, by bacteria suspension at 4 DEG C
At a temperature of, 20KHz ultrasonication, broken liquid is centrifugal prepares supernatant, and lyophilizing i.e. obtains enzyme powder, and enzyme powder yield is 315g/L.Enzyme is lived
For 72000U/g.
Described above is the detailed description for the preferable possible embodiments of the present invention, but embodiment is not limited to this
Bright patent claim, the equal change completed under the technical spirit suggested by all present invention or modification change, all should belong to
In the contained the scope of the claims of the present invention.