CN1130463C - Fermentation process by expressing recombined protein in bacillus - Google Patents
Fermentation process by expressing recombined protein in bacillus Download PDFInfo
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- CN1130463C CN1130463C CN 00119866 CN00119866A CN1130463C CN 1130463 C CN1130463 C CN 1130463C CN 00119866 CN00119866 CN 00119866 CN 00119866 A CN00119866 A CN 00119866A CN 1130463 C CN1130463 C CN 1130463C
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Abstract
The present invention relates to a fermentation technology for expressing recombined protein in bacillus. Starch serves as a component of a main carbon source of a fermentation medium, and the productivity of the recombined protein can be greatly enhanced. Under the optimization conditions of growth conditions and expression conditions of the bacillus subtilis gene engineering bacterial strain of the recombined protein gene, the productivity of the recombined protein can be enhanced by 8.5 to 9.3 times as compared with the non-optimization conditions. The cost of the culture medium is low, and the fermentation technology is simple and practical. The present invention is applied to industrial production, and has wide prospect.
Description
The present invention relates to the genus bacillus expression system, be specifically related to secrete the optimization of the genetically engineered genus bacillus culture condition of recombinant protein.
In general, utilize genetic engineering means to produce specific recombinant protein, we can be secreted into outside the born of the same parents by expectation target albumen.Foreign protein is secreted into outside the born of the same parents, growth of having avoided foreign protein to gather in host cell suppressing host cell and the murder by poisoning that may bring to host cell.Many foreign proteins will become has bioactive albumen also to need through modification partly, and these modifications have considerable part to carry out in the excretory process.Can be from fermented liquid directly extract target product, avoided smudge cells and from the fermented liquid that mixes cell debris and content purified product, for suitability for industrialized production, the purity of production efficiency and cost and target product all will greatly be optimized.
The genus bacillus expression system has following advantage: 1, can be outside born of the same parents the protein secreting that function is arranged, and 2, non-virulent, 3, do not have a tangible preference codon (Harwood, C.R. (ed), Bacillus, Plenum, New York, 1989).Genus bacillus is less demanding to growing environment, is easy to reach than high-cell density.These superiority are that genus bacillus is applied to industrialized production and has brought huge advantage.
After expression system was determined, the composition of substratum just became the important factor in order that can recombinant protein reach high expression level.The substratum of producing recombinant protein can be a synthetic medium, or natural medium.But all should be liquid nutrient medium.Usually, the substratum moiety comprises carbon source, as glucose; Nitrogenous source, as yeast extract paste, peptone, extractum carnis, urea etc.; Inorganic salt are as Na
+, K
+, Mg
2, Ca
2+, Trisodium Citrate etc.Glucose is present in the substratum with carbon source as the most general cultivation.Have the promotor to the glucose concn sensitivity in expression plasmid, during as p43 etc., the concentration that can recombinant protein reach glucose in high expression level and the substratum has very confidential relation.The glucose of high density can produce the catabolite repression phenomenon, inhibition of gene expression (Milton H.Saier, Jr., Biotechnology and Bioengineering 1998; V.58; No.2-3, pp.170-174).If will eliminate or reduce its secondary face rings, have only the technology that adopts lower concentration stream to add glucose during the fermentation, this just needs to increase manpower, and material resources are come monitoring glucose concentration, it is disadvantageous that controlling flow acceleration, cost and artificial expend industrialization expansion production.
Therefore, adopt the one-tenth of other carbon source to assign to replace glucose to improve zymotechnique in fermention medium, the research work that improves Recombinant Protein Expression amount and productivity is that Practical significance is arranged very much.
For this reason, the purpose of this invention is to provide a kind of in genus bacillus the zymotechnique of express recombinant protein, wherein in fermention medium, adopt the composition of starch as main carbon source, can improve the productivity of recombinant protein greatly.
The invention provides a kind of in genus bacillus the zymotechnique of express recombinant protein, wherein in fermention medium general glucose with the inexpensive carbon source easily of another kind: starch replaces.In whole culturing process, starch constantly is decomposed into oligose fragment for Bacillus subtilus excretory extracellular enzyme, for thalline absorbs, become a kind of natural, the stream adding system that need not to regulate and control, not only exempted artificial stream and added the loaded down with trivial details technology of carbon source, and the growth of thalline and expression level all improve a lot.
Host bacterium genus bacillus of the present invention comprises subtilis, bacillus pumilus or bacillus megaterium etc.Because adopt starch to replace glucose in the fermention medium of the present invention, therefore, applicable to having in the expression plasmid as p43, HpaII etc. are to the promotor of glucose-sensitive.
The zymotechnique of the present invention's express recombinant protein in genus bacillus is specially adapted to the zymotechnique of fermentor tank level.Zymotechnique comprises three steps:
A. first order seed is cultivated
The bacterial classification inoculation that liquid nitrogen is preserved is cultivated to 3ml LB substratum, and nutrient solution is scrawled the LB agar plate to clear single bacterium colony occurring, and single bacterium colony of picking inserts in the 3ml LB substratum to be cultivated.
B. secondary seed is cultivated
To cultivate in the first order seed nutrient solution access 50ml LB substratum.
C. fermentor cultivation
The secondary seed nutrient solution is inserted in the 1L fermention medium, cultivate in fermentor tank, the fermenting process controlled variable is as follows: temperature 25-40 ℃; PH5.0-8.5; Air flow 0.2-1.6L/min; Stir speed (S.S.) 250-950r/min; Dissolved oxygen is controlled at 15-30%; The seed inoculum size is 1-10%.
The fermention medium of using in the fermentor cultivation flow process adopts the composition of starch as main carbon source.Shown in fermention medium composed as follows:
Component parts (weight)
Peptone 1-30
Yeast extract paste 1-30
Trisodium Citrate 0.1-5
K
2HPO
4 1-5
Starch 5-100
Above each component is mixed, add water to 1000 parts of weight, autoclaving.
The present invention is based on penicillin G acylase (the penicillin acylase of report among the Chinese patent application CN 99113885.6 below; EC 3.5.1.11 is called for short PGA) as an example of recombinant protein; adopt to express the bacillus subtilis genetic engineering bacterial strain pga-SIBAS205 of PGA, set forth by optimization and have the growth of Bacillus subtilus bacterial strain of recombinant protein gene and the productivity that expression condition improves recombinant protein.
Experimental result shows: utilize starch can improve cell density and recombinant protein output greatly as the main carbon source in the substratum, and the concentration of starch in substratum can cell growth and the secretion of recombinant protein constitute influence.By comparison, the secretion of recombinant protein is very responsive to the glucose concn that exists in the substratum, and the glucose of higher concentration can cause catabolite repression and suppress the secretion of recombinant protein.Table 1 is listed different carbon sources to the influence of PGA secretory volume (reconstitution cell is containing or not in the LB substratum of carbonaceous sources, 37 ℃ growth 48 hours).
The different carbon sources of table 1 are to the influence of PGA secretory volume
*With
*Referring to the note in the table 2
| Substratum institute carbonaceous sources | Do not have | Glucose 1g/L | Glucose＞2.5g/L | Glycerine 1g/L | Lactose 1g/L | Sucrose 30g/L | Dextrin 30g/L | Starch 10g/L |
| A 600 * PGA ** (U/ml) | 3.0 4.0 | 3.5 5.0 | 3.5-4 0 | 5.0 0 | 3.5 5.0 | 10 7.0 | 12 8.4 | 15 17 |
The concentration range 5g/L-100g/L of starch in the substratum.In the fermentor tank level, when starch concentration is lower than 30g/L, increase with concentration, the recombinant protein productive rate increases; And starch concentration is between 30g/L-60g/L, and it is little that the growth of recombinant protein and expressing has been distinguished.If blindly increase carbon source concentration, its result can make the substratum thickness, influences dissolved oxygen level, also is a kind of waste to starting material.
Be example with the penicillin G acylase recombinant protein again, under the Different Optimization condition of identical expression system, the Recombinant Protein Expression situation is as shown in table 2.Optimize the productivity ratio of back PGA and optimize the preceding 8.5-9.3 of raising doubly.
Advantage of the present invention: Chinese patent application CN 99113885.6 adopts the genetically engineered Bacillus subtilus of constitutive expression to produce bacterium as recombinant protein, it is fast that target protein produces speed, producing bacterium goes down to posterity stable, production technique is simplified, the present invention on this basis, adopt starch as the main carbon source composition in the fermention medium, further the production efficiency of recombinant protein is reached a new high again.And the whole fermentation process condition is more extensive, does not need complicated control process, very helps suitability for industrialized production and uses.
The present invention is further elaborated by following examples, but does not limit the scope of the invention.
Embodiment 1
1, bacterial classification: bacillus subtilis genetic engineering bacterial strain pga-SIBAS205 (referring to CN 99113885.6).
2, substratum:
(1) seed culture medium is formed
Yeast extract paste 6.25g
Peptone 10g
Sodium-chlor 10g
Above each component is mixed, add water to weight 1000g, autoclaving.
(2) fermention medium is formed
Peptone 15g
Yeast extract paste 25g
Trisodium Citrate 1g
K
2HPO
4 3g
Starch 30g
Above each component is mixed, add water to weight 1000g, autoclaving.
3, fermentation:
(1) seed culture
A) first order seed is cultivated
The bacterial classification inoculation that liquid nitrogen is preserved is to 3ml test tube LB (containing kantlex 10ug/ml), and 37 ℃, 250r/min cultivated 16-18 hour.Nutrient solution is drawn LB agar plate (containing kantlex 10ug/ml), cultivates 24 hours for 37 ℃.Get single bacterium colony of sterilization toothpick picking, insert in the 3ml LB substratum (containing kantlex 10ug/ml), 37 ℃, 250r/min cultivated 16-18 hour.
B) secondary seed is cultivated
Seed liquor is inserted the 250ml that contains the 50ml fermention medium with 5% inoculum size shake in the bottle, cover bottleneck with eight layers of sterile gauze, 37 ℃, 250r/min cultivated 16-18 hour.
(2) fermentor cultivation
Secondary seed 50ml inserted in the B.Braun 1.2L automatic fermenter contain the 1L fermention medium cultivated pH5.0-8.5 48 hours.Air flow 0.2-1.6L/min, stir speed (S.S.) 250-950r/min.Dissolved oxygen is controlled at 15-30%.Under the more situation of foam, drip a small amount of defoamer bubble enemy.37 ℃, cultivated 48 hours.The results are shown in Table 2, with optimize before compare, optimize the back cell density and improve 2.39 times, the productivity of PGA improves 8.5 times.
Embodiment 2
1, bacterial classification: bacillus subtilis genetic engineering bacterial strain pga-SIBAS205 (referring to CN 99113885.6).
2, substratum:
(1) seed culture medium is formed with embodiment 1.
(2) fermention medium is formed
Peptone 20g
Yeast extract paste 20g
Trisodium Citrate 3g
K
2HPO
4 4g
Starch 60g
Above each component is mixed, add water to weight 1000g, autoclaving.
3, fermentation step is with embodiment 1.The results are shown in Table 2, with optimize before compare, cell density improves 2.77 times, the productivity of PGA improves 9.3 times.
Table 2 PGA is the expression under the Different Optimization condition in the subtilis expression system
| (contain glucose 1g/L) before the fermentor tank level optimization | After the fermentor tank level optimization (embodiment 1 starch-containing 30g/L) | After the fermentor tank level optimization (embodiment 2 starch-containing 60g/L) | |
| A600 * | 11 | 26.3 | 30.5 |
| PGA productivity (U after 48 hours ferments **/h) | 0.084 | 0.713 | 0.782 |
*The detection of cell density: with bacterium liquid dilution certain multiple, be blank, measure the 600nm optical density(OD) with distilled water.Make the spectrodensitometry value between 0.1-0.7, on duty with spectrodensitometry again with extension rate, be A600.
*Penicillin G acylase unit of activity U.
The penicillin G acylase vitality test, adopt the NIPAB method:
10 μ l enzyme liquid add 490 μ l phosphoric acid buffers, and (0.05mol/L, pH7.5), 37 ℃ of temperature are bathed.The 0.9mg/ml NIPAB solution (6-nitro-3-phenylacetamide yl benzoic acid) that adds 37 ℃ of preheatings of 1ml again.Reacted 4 minutes, and added 1ml 95% ethanol termination reaction, measure the variation of 405nm absorbancy.
Blank 10 μ l enzyme liquid are that phosphoric acid buffer replaces.
Enzyme activity is defined as: to produce the amount of 6-nitro-required penicillin acylase of 3-amino-phenylformic acid of 1 μ mol be 1 unit in hydrolysis in 1 minute.
The enzyme activity calculation formula is: enzyme activity concentration (U/ml)=7 * A
405
Claims (2)
1, a kind of in genus bacillus the zymotechnique of express recombinant protein, comprise the first order seed cultivation, secondary seed is cultivated and three steps of fermentor cultivation, it is characterized in that adopting in the fermention medium that the fermentor cultivation step is used the composition of starch as main carbon source.
2, zymotechnique as claimed in claim 1 is characterized in that the composed as follows of described fermention medium:
Component parts (content)
Peptone 1-30
Yeast extract paste 1-30
Trisodium Citrate 0.1-5
K
2HPO
4 1-5
Starch 5-100
Above each component is mixed, and adding water to weight is 1000 parts.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 00119866 CN1130463C (en) | 2000-09-01 | 2000-09-01 | Fermentation process by expressing recombined protein in bacillus |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 00119866 CN1130463C (en) | 2000-09-01 | 2000-09-01 | Fermentation process by expressing recombined protein in bacillus |
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|---|---|
| CN1291655A CN1291655A (en) | 2001-04-18 |
| CN1130463C true CN1130463C (en) | 2003-12-10 |
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| CN 00119866 Expired - Fee Related CN1130463C (en) | 2000-09-01 | 2000-09-01 | Fermentation process by expressing recombined protein in bacillus |
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Owner name: SHANGHAI INST. OF LIFE SCIENCE, CAS Free format text: FORMER NAME OR ADDRESS: SHANGHAI INST. OF BIOCHEMISTRY, CHINESE ACADEMY OF SCIENCES |
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Address after: 200031 No. 320, Yueyang Road, Shanghai Patentee after: Shanghai Institute of life Sciences, Chinese Academy of Sciences Address before: 200031 No. 320, Yueyang Road, Shanghai Patentee before: Shanghai Research Institute of Biochemistry Chinese Academy of Sciences |
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Granted publication date: 20031210 Termination date: 20160901 |