CN105385718A - Fermentation preparation method of gamma-polyglutamic acid and strain - Google Patents
Fermentation preparation method of gamma-polyglutamic acid and strain Download PDFInfo
- Publication number
- CN105385718A CN105385718A CN201510802173.XA CN201510802173A CN105385718A CN 105385718 A CN105385718 A CN 105385718A CN 201510802173 A CN201510802173 A CN 201510802173A CN 105385718 A CN105385718 A CN 105385718A
- Authority
- CN
- China
- Prior art keywords
- fermentation
- gamma
- polyglutamic acid
- subtilis
- culture
- 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.)
- Pending
Links
Landscapes
- Preparation Of Compounds By Using Micro-Organisms (AREA)
- Micro-Organisms Or Cultivation Processes Thereof (AREA)
Abstract
The invention provides a fermentation method of gamma-polyglutamic acid and/or a method for increasing the fermentation yield of gamma-polyglutamic acid. The fermentation method comprises the following steps: inoculating bacillus subtilis (such as HBY-PBS-ZY55) generating gamma-polyglutamic acid into a fermentation medium in which n-hexane, Tween-80 and/or betaine are added to carry out fermented culture and further adding n-hexane optionally in the period of fermented culture in the step (1). Besides, the invention also provides a method for obtaining bacillus subtilis generating gamma-polyglutamic acid at high yield, a strain obtained by the method and an application of bacillus subtilis.
Description
Technical field
The invention belongs to field of microbial fermentation, specifically, the present invention relates to the method utilizing fermentable to produce gamma-polyglutamic acid-, the invention still further relates in addition for the preferred bacterial strain etc. in the method.
Background technology
Gamma-polyglutamic acid-(referred to as γ-PGA or PGA) is the homogeneous peptides that L-glutamic acid monomer is formed with the amido linkage polymerization on γ-position.It has water-soluble; biodegradable; not containing toxicity; the fields such as foodstuffs industry, makeup, health care, water treatment, wastewater treatment, sanitary product, medical treatment can be widely used in, such as, can be used as thickening material, cryoprotectant, sustained release dosage, pharmaceutical carrier, biological adhesive, wetting Agent for Printing Inks, Biodegradable fibers, super absorbent resin, biological flocculant and heavy metal ion absorption agent etc.
The main preparation methods of gamma-polyglutamic acid-has: chemical synthesis, extraction method, enzyme transforming process and microbe fermentation method.Because first three methods yields poorly, cost is higher, pollutes large, mainly utilizes microbe fermentation method to prepare gamma-polyglutamic acid-at present.
Prior art is mainly on microorganisms producing bacterial classification and bacterial strain to the focus utilizing fermentable to produce gamma-polyglutamic acid-, such as, Chinese patent application No. 02151746 method disclosing subtilis NX-2 and use it to prepare gamma-polyglutamic acid-;
Chinese patent application No. 200410010509 method disclosing subtilis zju-7 and use it to prepare gamma-polyglutamic acid-;
No. 200610155278th, Chinese patent application discloses and utilizes subtilis and Corynebacterium glutamicum to mix the method preparing gamma-polyglutamic acid-;
Chinese patent application No. 200710130248 method disclosing subtilis CGMCCNo.2108 and use it to prepare gamma-polyglutamic acid-, production peak can reach 34.1g/L;
Chinese patent application No. 200810027184 method disclosing subtilis PGA-7 and use it to prepare gamma-polyglutamic acid-, production peak can reach 27.3g/L;
Chinese patent application No. 200810150830 method disclosing subtilis XN01 and use it to prepare gamma-polyglutamic acid-;
Chinese patent application No. 201010271196 method disclosing subtilis PGS-1 and use it to prepare gamma-polyglutamic acid-;
No. 201210018185th, Chinese patent application discloses and utilizes subtilis SY-ND and bacillus megaterium SY-Z5 to mix the method preparing gamma-polyglutamic acid-, and then for the production of microbial flocculant;
Chinese patent application the 201210371764th and No. 201210371783 methods disclosing subtilis GXA-28 and use it to prepare gamma-polyglutamic acid-, output can reach 20-30g/L;
No. 201210555304th, Chinese patent application discloses the subtilis FRD518 of genetically engineered restructuring VHb gene and uses it to prepare the method for gamma-polyglutamic acid-, and production peak can reach 65g/L.
The present inventor finds, the defect that above-mentioned prior art is the most serious is that fermentation time is all longer, and reach higher or production peak, fermentation time needs to reach 48-96 hour, is very unfavorable for suitability for industrialized production.And the present inventor is not subject to the restriction that above-mentioned prior art pays close attention to direction, surprisingly, adding of normal hexane, tween-80 and/or trimethyl-glycine, the output of gamma-polyglutamic acid-can be promoted, especially improve the output of short fermentation, amplification reaches as high as more than 20%; In addition, screen the optimization of the use of subtilis HBY-PBS-ZY55 and the fed-batch fermentation for it obtained according to the present inventor, reach more than 36g/L at the gamma-polyglutamic acid-output Absorbable organic halogens being in a short time no more than 36 hours (even 28 hours).Wherein, subtilis HBY-PBS-ZY55 is the non-genomic engineering bacteria not having transformed VHb gene, therefore also has the prospect of further genetic modification improving yield.
Summary of the invention
Technical problem to be solved by this invention is to provide method, the application and bacterial strain etc. of new gamma-polyglutamic acid-fermentation aspect, and it especially can be made namely to obtain high yield by fermentation culture in a short time.
Specifically, in first aspect, the invention provides the fermentation process of gamma-polyglutamic acid-, it comprises:
(1) inoculate in the fermention medium that with the addition of normal hexane, tween-80 and/or trimethyl-glycine carry out fermentation culture by producing the subtilis (e.g., HBY-PBS-ZY55) of gamma-polyglutamic acid-;
(2) optionally during the fermentation culture of step (1), normal hexane is added further;
(3) gamma-polyglutamic acid-in fermenting culture is collected.
Correspondingly, in second aspect, present invention provides the method improving gamma-polyglutamic acid-fermentation yield, it comprises:
(1) inoculate in the fermention medium that with the addition of normal hexane, tween-80 and/or trimethyl-glycine carry out fermentation culture by producing the subtilis (e.g., HBY-PBS-ZY55) of gamma-polyglutamic acid-;
(2) optionally during the fermentation culture of step (1), normal hexane is added further;
(3) gamma-polyglutamic acid-in fermenting culture is collected.
The method of second aspect present invention can obtain more gamma-polyglutamic acid-s than the method for not adding normal hexane, tween-80 and/or trimethyl-glycine accordingly, and in the specific embodiment of the present invention, gamma-polyglutamic acid-fermentation yield can improve more than 20%.
In this article, produce the subtilis dawn known to those skilled in the art of gamma-polyglutamic acid-, such as, mentioned by background technology part of the present invention, the subtilis that the present invention preferably adopts will be described in more detail below; The leavening temperature dawn known to those skilled in the art of subtilis is 34-38 DEG C, and the present invention preferably adopts 36 DEG C or 36.5 DEG C etc.
In this article, term "and/or" has the general meaning understood, namely coordination be " with " or the relation of "or".Such as, with the addition of normal hexane, tween-80 and/or trimethyl-glycine, can be only with the addition of normal hexane, can be only with the addition of tween-80, can be only with the addition of trimethyl-glycine, can be only with the addition of normal hexane and tween-80, can be only with the addition of normal hexane and trimethyl-glycine, can be only with the addition of tween-80 and trimethyl-glycine, also can be with the addition of normal hexane, tween-80 and trimethyl-glycine.
In this article, as do not particularly not pointed out the additive in substratum, substratum is only the substratum not adding corresponding additive.Such as, in the present invention, the fermention medium of fermentation culture can be preferably following formula (g/L): glucose 60-80, fructose 5-10, Sodium Glutamate 20-40, calcium chloride 1-1.5, K
2hPO
41.3-1.8, MgSO
47H
2o0.4-0.6, Dried Corn Steep Liquor Powder 5-15, yeast powder 5-10, Trisodium Citrate 10-20, ammonium chloride 10-30, manganous sulfate 0.05-0.2, ferrous sulfate 0.015-0.025, NaCl3-8, pH7.1-7.6; More preferably can be following formula (g/L): glucose 70, fructose 8, Sodium Glutamate 30, calcium chloride 1.2, K
2hPO
41.5, MgSO
47H
2o0.5, Dried Corn Steep Liquor Powder 10, yeast powder 8, Trisodium Citrate 15, ammonium chloride 20, manganous sulfate 0.1, ferrous sulfate 0.02, NaCl5, pH7.4.
In the present invention, the subtilis preferably producing gamma-polyglutamic acid-activation culture and obtaining in seed culture medium.Also preferably wherein, seed culture medium can be following formula (g/L): glucose 10-30, yeast extract 5-10, peptone 5-15, ammonium chloride 2-5, KH
2pO
41-5, MgSO
47H
2o0.2-1, calcium chloride 0.5-1, NaCl3-8, pH7.1-7.6; More preferably can be following formula (g/L): glucose 20, yeast extract 8, peptone 10, ammonium chloride 3, KH
2pO
43, MgSO
47H
2o0.5, calcium chloride 0.8, NaCl5, pH7.4.
In the present invention, preferably fermentation or fermentation culture are short-terms.The present inventor, by the research of various aspect, all have been surprisingly found that the factor that can improve short fermentation output in many-sides such as bacterial strain, medium additives and fermentation steps.In the present invention, the time of preferred fermentation culture is no more than 36 hours, is more preferably 26-36 hour, as 26-28 hour or 32-36 hour etc.
Preferably in the method for the present invention first or second aspect, the addition of normal hexane is 5-50ml/L, is preferably 8-30ml/L, is more preferably 10-20ml/L; The addition of tween-80 is 0.1-1ml/L, is preferably 0.2-0.8ml/L, is more preferably 0.45-0.55ml/L; And/or the addition of trimethyl-glycine is 0.05-0.5g/L, is preferably 0.1-0.3g/L, is more preferably 0.15-0.25g/L.The present inventor studies discovery, and the dose-effect relationship of additive is not correlation, and such as too much normal hexane can not bring more output increased.In this article, interpolation is that those skilled in the art can understand and implement, and the addition of such as 5ml/L adds the corresponding additive of 5ml exactly in 1L substratum or culture.
More surprisingly, in the present invention, owing to decreasing fermentation period, the present inventor finds that the colourity of fermented liquid also reduces, decolouring difficulty in the collection of gamma-polyglutamic acid-(extraction) technique is greatly reduced, in the method for therefore the present invention first or second aspect the collection of step (3) preferably can by adding alcohol settling to collect without the need to or reduce extra decolorization process.
In the third aspect, the invention provides the method for the subtilis obtaining high yield gamma-polyglutamic acid-, it comprises:
(1) by the subtilis liquid culture of product gamma-polyglutamic acid-to be mutagenic, then dilute;
(2) the dilution bacterium liquid that step (1) obtains is carried out uv irradiating under dark condition;
(3) the bacterium liquid through irradiating step (2) obtained lucifuge on plate screening substratum is cultivated;
(4) step (3) is cultivated the single bacterium colony obtained and carry out fermentation culture (preferred short fermentation cultivation) respectively; With,
(5) output of the gamma-polyglutamic acid-of measuring process (4) fermentation generation, selects the subtilis of high yield (preferably short fermentation high yield) gamma-polyglutamic acid-.
Preferably in the method for third aspect present invention, the subtilis of high yield gamma-polyglutamic acid-is the subtilis of short fermentation high yield gamma-polyglutamic acid-.Wherein, high yield refers under identical fermentation condition higher than the output of the gamma-polyglutamic acid-of the subtilis of product gamma-polyglutamic acid-to be mutagenic accordingly; As indicated without contrary, short-term has defined meaning above, preferably more than 36 hours, is more preferably 26-36 hour, as 26-28 hour or 32-36 hour etc.
Preferably in the method for third aspect present invention, each step ground is implemented can the step preferably described in the concrete real-time mode of the present invention and/or substratum wherein.Such as, in step (1), cultivate and be preferably cultured to OD
600for 10-12, and/or, dilution preferably dilution 10
6doubly.And for example, in step (2), uv irradiating preferably 30cm place irradiation 180 seconds under 30W ultraviolet lamp.Also as, in step (3), plate screening substratum contains 1% (W/W) lithium chloride.
In fourth aspect, the subtilis of the high yield gamma-polyglutamic acid-that the method that the invention provides third aspect present invention obtains, the subtilis of the short fermentation high yield gamma-polyglutamic acid-especially preferably providing the method for third aspect present invention to obtain.Wherein, as indicated without contrary, high yield and short-term have defined meaning above.
The subtilis of preferred fourth aspect present invention is preserved in subtilis (BacillusSubtillis) HBY-PBS-ZY55 of China typical culture collection center (CCTCC) on May 20th, 2014 with deposit number CCTCCNO.M2014213, preservation address is: China, Wuhan, Wuhan University.
In the 5th, the invention provides the application of subtilis in the fermentation of gamma-polyglutamic acid-of fourth aspect present invention, the application of the subtilis of fourth aspect present invention in the short fermentation of gamma-polyglutamic acid-is especially preferably provided.Wherein, as indicated without contrary, short-term has defined meaning above.
Preferably in the application of fifth aspect present invention, the method for the fermentation of gamma-polyglutamic acid-is included in fermentation and maintains dissolved oxygen amount >=10%, such as, maintained by the adjustment of fermentor tank liquid amount, air flow and/or stirring velocity etc.; Such as, and/or it is 10-15g/L that the method for the fermentation of gamma-polyglutamic acid-comprises maintenance sugar (e.g., glucose) content, is added maintaining by feed supplement.The present inventor finds, maintain dissolved oxygen amount and maintain the output that sugared content can significantly improve gamma-polyglutamic acid-, especially the latter significantly can also shorten fermentation period, makes more easily to realize short fermentation.
Preferably in the present invention, the fermention medium of fermentation can be preferably following formula (g/L): glucose 20-40, fructose 5-10, Sodium Glutamate 20-40, calcium chloride 1-1.5, K
2hPO
41.3-1.8, MgSO
47H
2o0.3-0.8, Dried Corn Steep Liquor Powder 5-15, yeast powder 5-15, Trisodium Citrate 10-20, ammonium chloride 10-30, manganous sulfate 0.05-0.2, ferrous sulfate 0.01-0.03, NaCl3-8, pH7.1-7.6, add defoamer 0.1-1ml/3L in addition; More preferably can be following formula (g/L): glucose 30, Sodium Glutamate 30, calcium chloride 1.2, K
2hPO
41.5, MgSO
47H
2o0.5, fructose 8, Dried Corn Steep Liquor Powder 10, yeast powder 5, Trisodium Citrate 15, ammonium chloride 20, manganous sulfate 0.1, ferrous sulfate 0.02, NaCl5, pH7.4, adds defoamer 0.5ml/3L in addition.
Also preferably in the present invention, the supplemented medium of feeding medium during fermentation can be following formula (g/L): glucose 500-1000, MgSO
47H
2o2-5, calcium chloride 2-5, Dried Corn Steep Liquor Powder 15-30; More preferably can be following formula (g/L): glucose 750, MgSO
47H
2o3, calcium chloride 3, Dried Corn Steep Liquor Powder 25.
The present inventor also investigated more complicated fermention medium and supplemented medium, can obtain better effect, be recorded in the specific embodiment of the present invention, but above-mentioned fermention medium and supplemented medium are particularly preferred.
Also preferred in the application of fifth aspect present invention in addition, the method for the fermentation of gamma-polyglutamic acid-is the method for first aspect present invention.
In other respects, present invention also offers the technical schemes such as the method recorded in this specification sheets (especially following examples) or substratum, just look like the technical scheme such as the method recorded in specification sheets of the present invention (especially following examples) or substratum this with repeat again in detail in the claims to describe the same.
Such as, the invention provides fermention medium, it can be following formula (g/L): glucose 10-30, fructose 5-10, Sodium Glutamate 5-15, calcium chloride 1-1.5, K
2hPO
41.5, MgSO
47H
2o0.3-0.8, Dried Corn Steep Liquor Powder 5-15, yeast powder 5-15, Trisodium Citrate 10-20, ammonium chloride 10-30, manganous sulfate 0.05-0.2, ferrous sulfate 0.02, NaCl3-8, pH7.1-7.6, adds defoamer 0.1-1ml/3L in addition; More preferably can be following formula (g/L): glucose 25, Sodium Glutamate 10, calcium chloride 1.2, K
2hPO
41.5, MgSO
47H
2o0.5, fructose 8, Dried Corn Steep Liquor Powder 10, yeast powder 5, Trisodium Citrate 15, ammonium chloride 20, manganous sulfate 0.1, ferrous sulfate 0.02, NaCl5, pH7.4, adds defoamer 0.5ml/3L in addition.
And for example, it can be following formula (g/L) to the invention provides supplemented medium: glucose 300-1000, MgSO
47H
2o2-5, calcium chloride 2-5, Dried Corn Steep Liquor Powder 15-30, Trisodium Citrate 10-20, ammonium chloride 10-20, K
2hPO
41-2; More preferably can be following formula (g/L): glucose 650, MgSO
47H
2o3, calcium chloride 3, Dried Corn Steep Liquor Powder 25, Trisodium Citrate 15, ammonium chloride 15, K
2hPO
41.5.
Beneficial effect of the present invention is: the method provided and subtilis improve gamma-polyglutamic acid-output, reduce fermentation period, improve plant factor, reduces the colourity of production cost and fermented liquid, is applicable to industrialization and produces; The subtilis genetic stability provided in addition is strong, can repeat to go down to posterity.
For the ease of understanding, below will be described in detail the present invention by specific embodiment.It is important to note that these descriptions are only exemplary descriptions, do not form limitation of the scope of the invention.According to the discussion of this specification sheets, many changes of the present invention, to change concerning one of ordinary skill in the art be all apparent.In addition, the present invention refer to open source literature, and these documents are to more clearly describe the present invention, and their entire contents is all included in and carried out reference herein, just looks like that repeated description is excessively the same in this article for their full text.
Embodiment:
Below in conjunction with example, the present invention is specifically described, wherein agents useful for same is all bought by commercial channel and is obtained, wherein subtilis HBY-PBS-ZY55 is preserved in China typical culture collection center (CCTCC) according to the Patent Deposit program of microorganism in addition, deposit number is CCTCCNO.M2014213, and preservation day is on May 20th, 2014).
The acquisition of embodiment 1 subtilis HBY-PBS-ZY55
The subtilis HBY-PBS-3L preserved with the applicant, for starting strain, is adopted UV-LiCl complex mutation method, is obtained the mutant strain HBY-PBS-ZY55 of stable high yield by multiplex screening.
Specifically, will at slant medium (formula (g/L): peptone 10, yeast extract 5, NaCl5, agar 20, pH7.0) upper isolated starting strain HBY-PBS-3L is inoculated into liquid seed culture medium (formula (g/L): glucose 20, yeast extract 8, peptone 10, ammonium chloride 3, KH
2pO
43, MgSO
47H
2o0.5, calcium chloride 0.8, NaCl5, pH7.4) in, with 36 DEG C and shaking speed 220r/min, 8h is cultivated in concussion, measures its OD value, record OD under 600n wavelength
600for 10-12, be then diluted to 10 with seed culture medium
-6, be prepared into bacteria suspension.
Then under dark condition, carry out ultraviolet mutagenesis (ultraviolet lamp power 30W), namely getting the above-mentioned bacteria suspension of 5ml joins in the sterile petri dish be placed on magnetic stirring apparatus, 30cm place under ultraviolet lamp, irradiate 120s, 150s, 180s, after 210s, coat respectively containing 0.5%, 1%, plate screening substratum (the formula (g/L): glucose 10 of 1.5% (W/W) lithium chloride, yeast extract 5, peptone 10, Sodium Glutamate 10, agar 20, toluylene red 0.1, pH7.0) on, 36 DEG C of lucifuges cultivate 16h, calculate lethality rate, obtain drawing best mutagenic condition: uv irradiating 180s, in plate screening substratum, lithium chloride addition is 1%.Single bacterium colony of survival is obtained with this best mutagenic condition.
Above-mentioned mutagenic obtained single bacterium colony is inoculated in seed culture medium respectively, with 36 DEG C and shaking speed 220r/min, 8h is cultivated in concussion, then with the inoculum size of 5% (V/V), be inoculated in Medium of shaking flask fermentation (formula (g/L): glucose 70, Sodium Glutamate 30, calcium chloride 1.2, K
2hPO
41.5, MgSO
47H
2o1.2, cane molasses 8, Dried Corn Steep Liquor Powder 10, yeast powder 10, Trisodium Citrate 15, ammonium chloride 20, manganous sulfate 0.1, ferrous sulfate 0.02, NaCl5, pH7.4) in, with 36 DEG C and shaking speed 220r/min, 30-36h is cultivated in concussion.
Get certain volume fermented liquid and leave standstill removal bubble, after bubble is removed completely, thin up is 4 times of original volume; The centrifugal 15min of 9000r/min, removing thalline, the supernatant liquor getting certain volume adds the dehydrated alcohol of 3 times of volumes, after continuous stirring, 4 DEG C of hold over night, the centrifugal 10min of 9000r/min, remove supernatant liquor, to be precipitated and weigh through lyophilize, and calculate the output of gamma-polyglutamic acid-, and judge the quality of each bacterial strain according to output.Therefrom screening obtains superior strain HBY-PBS-ZY55, and it is preserved in China typical culture collection center (CCTCC), and deposit number is CCTCCNO.M2014213, and preservation day is on May 20th, 2014).
The subtilis PGA-7 of this superior strain, bacterial strain after its ten generations of going down to posterity and its starting strain and No. 200810027184th, Chinese patent application as above carries out shake flask fermentation cultivation, the output of sampling and measuring gamma-polyglutamic acid-when cultivating 32h and 36h respectively.Result is as shown in table 1, superior strain of the present invention, even if through going down to posterity, constantly little in 32 of short fermentation, not only can reach the fermentation yield of high yield, and reach high point, and the output continuing fermentation promotes little; And starting strain as a comparison and the output of existing PGA-7 in short fermentation are all not as superior strain of the present invention, and need the fermentation time more grown could improving yield further.So no matter from the fermentation yield of gamma-polyglutamic acid-, or on fermentation efficiency, superior strain of the present invention has the meaning of practical application more.
The horizontal comparison of gamma-polyglutamic acid-short fermentation of each bacterial strain of table 1
Embodiment 2 improves the technique study of gamma-polyglutamic acid-fermentation yield
Use superior strain HBY-PBS-ZY55 of the present invention and existing subtilis PGA-7 to use diverse ways to carry out contrast fermentation respectively, wherein the process of fermentation process 1 is as follows:
Will at slant medium (formula (g/L): peptone 10, yeast extract 5, NaCl5, agar 20, pH7.0) upper isolated inoculation is to liquid seed culture medium (formula (g/L): glucose 20, yeast extract 8, peptone 10, ammonium chloride 3, KH
2pO
43, MgSO
47H
2o0.5, calcium chloride 0.8, NaCl5, pH7.4) in, with 36 DEG C and shaking speed 220r/min, 8h is cultivated in concussion.Then by obtain inoculum with the inoculum size of 5% (V/V), be inoculated in Medium of shaking flask fermentation (formula (g/L): glucose 70, fructose 8, Sodium Glutamate 30, calcium chloride 1.2, K
2hPO
41.5, MgSO
47H
2o0.5, Dried Corn Steep Liquor Powder 10, yeast powder 10, Trisodium Citrate 15, ammonium chloride 20, manganous sulfate 0.1, ferrous sulfate 0.02, NaCl5, pH7.4) in, with 36 DEG C and shaking speed 220r/min, 30h is cultivated in concussion.Finally measure and calculate the output of the gamma-polyglutamic acid-in shake flask fermentation culture.
The process of fermentation process 2 is same as the process of fermentation process 1 substantially, and difference is also containing 0.5ml/L tween-80 in Medium of shaking flask fermentation;
The process of fermentation process 3 is same as the process of fermentation process 1 substantially, and difference is also containing 0.2g/L trimethyl-glycine in Medium of shaking flask fermentation;
The process of fermentation process 4,5,6 is same as the process of fermentation process 1 substantially, and difference is also respectively containing 10ml/L, 20mL/L, 30mL/L normal hexane in Medium of shaking flask fermentation;
The process of fermentation process 7 is same as the process of fermentation process 1 substantially, and difference in shake flask fermentation culture, adds 30ml/L normal hexane when shake flask fermentation is cultivated and proceeded to 18h;
The process of fermentation process 8 is same as the process of fermentation process 1 substantially, and difference in shake flask fermentation culture, adds 10ml/L, 20ml/L and 10ml/L normal hexane when shake flask fermentation is cultivated and proceeded to the 0th (namely in Medium of shaking flask fermentation), 16h and 24h respectively;
The process of fermentation process 9 is same as the process of fermentation process 1 substantially, difference is also containing 0.5ml/L tween-80,0.2g/L trimethyl-glycine and 10ml/L normal hexane in Medium of shaking flask fermentation, then in shake flask fermentation culture, adds 20ml/L and 10ml/L normal hexane when shake flask fermentation cultivation proceeds to 16h and 24h respectively.
Result is as shown in table 2, and HBY-PBS-ZY55 is obvious than the yield heterosis of PGA-7 in short fermentation; The interpolation of tween-80, trimethyl-glycine and normal hexane can improve the fermentation yield of each bacterial strain, and the amount of wherein adding normal hexane when Preliminary fermentation too much can make output increased passivation on the contrary, and carries out adding a small amount of normal hexane in process be highly profitable in fermentation.
The each bacterial strain of table 2 makes the output of the gamma-polyglutamic acid-differently obtained
The condition optimizing research of embodiment 3 subtilis HBY-PBS-ZY55 short fermentation
Subtilis HBY-PBS-ZY55 is used to ferment.
The basic fermentation process 1 with reference to embodiment 2 of fermentation process 1 and 2 carries out, and difference is the formula of Medium of shaking flask fermentation, wherein, and the formula 1 (g/L) of Medium of shaking flask fermentation: glucose 65, Sodium Glutamate 30, calcium chloride 1.2, K
2hPO
41.5, MgSO
47H
2o1.2, cane molasses 8, corn steep liquor 15, soybean meal hydrolysate 10, Trisodium Citrate 15, ammonium chloride 20, manganous sulfate 0.05, ferrous sulfate 0.02, NaCl5, pH7.4, when fermenting 32h, yield level reaches high point, is 23.2g/L;
The formula 2 (g/L) of Medium of shaking flask fermentation: glucose 65, Sodium Glutamate 30, calcium chloride 1.2, K
2hPO
41.5, MgSO
47H
2o1.2, fructose 8, Dried Corn Steep Liquor Powder 15, yeast powder 10, Trisodium Citrate 15, ammonium chloride 20, manganous sulfate 0.1, ferrous sulfate 0.02, NaCl5, pH7.4, when fermenting 32h, yield level reaches high point, is 24.7g/L.
The basic fermentation process 1 with reference to embodiment 2 of fermentation process 3 and 4 carries out, difference is the formula of Medium of shaking flask fermentation and changes shake flask fermentation into ferment tank, wherein, the formula 3 (g/L) of Medium of shaking flask fermentation (i.e. ferment tank substratum): glucose 65, Sodium Glutamate 30, calcium chloride 1.2, K
2hPO
41.5, MgSO
47H
2o1.2, cane molasses 8, corn steep liquor 15, soybean meal hydrolysate 10, Trisodium Citrate 15, ammonium chloride 20, manganous sulfate 0.05, ferrous sulfate 0.02, NaCl5, pH7.4; Ferment tank condition: the volume 5L of fermentor tank, liquid amount 50%, mixing speed 200-800r/min and air flow 1-2.5VVM thus maintain dissolved oxygen amount>=10%, temperature 36.5 DEG C, when fermenting 32h, yield level reaches high point, is 30.2g/L;
The formula 4 (g/L) of Medium of shaking flask fermentation (i.e. ferment tank substratum): glucose 65, Sodium Glutamate 30, calcium chloride 1.2, K
2hPO
41.5, MgSO
47H
2o1.2, fructose 8, Dried Corn Steep Liquor Powder 15, yeast powder 10, Trisodium Citrate 15, ammonium chloride 20, manganous sulfate 0.1, ferrous sulfate 0.02, NaCl5, pH7.4; Ferment tank condition: the volume 5L of fermentor tank, liquid amount 60%, mixing speed 200-800r/min and air flow 1-2.5VVM thus maintain dissolved oxygen amount>=10%, temperature 36.5 DEG C, when fermenting 30h, yield level reaches high point, is 31.8g/L.
The basic fermentation process 1 with reference to embodiment 2 of fermentation process 5 and 6 carries out, difference is the formula of Medium of shaking flask fermentation and changes shake flask fermentation into fermentor tank fed-batch fermentation, wherein, the formula 5 (g/L) of Medium of shaking flask fermentation (namely initial ferment tank substratum): glucose 30, Sodium Glutamate 30, calcium chloride 1.2, K
2hPO
41.5, MgSO
47H
2o0.5, fructose 8, Dried Corn Steep Liquor Powder 10, yeast powder 10, Trisodium Citrate 15, ammonium chloride 20, manganous sulfate 0.1, ferrous sulfate 0.02, NaCl5, pH7.4, every tank adds THIF-298 defoamer 0.5ml (can purchased from Yantai Thinking Finechem Technology Co., Ltd.) in addition; The formula 5 (g/L) of supplemented medium: glucose 750, MgSO
47H
2o3, calcium chloride 3, Dried Corn Steep Liquor Powder 25; Ferment tank condition: the volume 5L of fermentor tank, liquid amount 60%, mixing speed 200-800r/min and air flow 1-2.5VVM thus maintain dissolved oxygen amount>=10%, temperature 36.5 DEG C, glucose content in culture in sampling and measuring fermentor tank, when lower than (when coming across fermentation 10-12h at first) during 15g/L, add supplemented medium, glucose content in culture is made in fermentor tank to maintain 15g/L, feed supplement stops to during fermentation 24h, when 26h, yield level reaches high point, is 36.8g/L;
The formula 6 (g/L) of Medium of shaking flask fermentation (namely initial ferment tank substratum): glucose 25, Sodium Glutamate 10, calcium chloride 1.2, K
2hPO
41.5, MgSO
47H
2o0.5, fructose 8, Dried Corn Steep Liquor Powder 10, yeast powder 10, Trisodium Citrate 15, ammonium chloride 20, manganous sulfate 0.1, ferrous sulfate 0.02, NaCl5, pH7.4, every tank adds every tank in addition and adds THIF-298 defoamer 0.5ml (can purchased from Yantai Thinking Finechem Technology Co., Ltd.) in addition, the formula 6A (g/L) of supplemented medium: glucose 650, MgSO
47H
2o3, calcium chloride 3, Dried Corn Steep Liquor Powder 25, Trisodium Citrate 15, ammonium chloride 15, K
2hPO
41.5, the formula 6B (g/L) of supplemented medium: Sodium Glutamate 400, ferment tank condition: the volume 5L of fermentor tank, liquid amount 60%, mixing speed 200-800r/min and air flow 1-2.5VVM thus maintain dissolved oxygen amount>=10%, temperature 36.5 DEG C, glucose content and content of glutamic acid in culture in sampling and measuring fermentor tank, when glucose content lower than during 10g/L and/or content of glutamic acid lower than (come across at first cultivate to 12-13h time) during 10g/L, add supplemented medium A and/or B, glucose content in culture is made in fermentor tank to maintain 10-15g/L (namely stopping supplemented medium A higher than during 15g/L) and content of glutamic acid maintains 10g/L, simultaneously after starting to add supplemented medium, also the sodium hydroxide or the hydrochloric acid that start to add 1mol/L make pH control 6.8 ± 0.1, feed supplement stops to during fermentation 24h, when 28h, yield level reaches high point, for 37.6g/L.
From above-mentioned fermentation results, for subtilis HBY-PBS-ZY55, the fine setting of substratum, the adjustment that even supplemented medium is stricter, little on the shortening impact of the raising of fermentation yield and fermentation time, and control dissolved oxygen amount level and significantly can improve fermentation yield; By feed supplement, especially maintain sugared content, significantly can improve fermentation yield further, but also significantly can shorten fermentation time.
Claims (10)
1. the fermentation process of gamma-polyglutamic acid-or the method for raising gamma-polyglutamic acid-fermentation yield, it comprises:
(1) inoculate in the fermention medium that with the addition of normal hexane, tween-80 and/or trimethyl-glycine carry out fermentation culture by producing the subtilis (e.g., HBY-PBS-ZY55) of gamma-polyglutamic acid-;
(2) optionally during the fermentation culture of step (1), normal hexane is added further;
(3) gamma-polyglutamic acid-in fermenting culture is collected.
2. method according to claim 1, wherein, the addition of normal hexane is 5-50ml/L, is preferably 8-30ml/L, is more preferably 10-20ml/L; The addition of tween-80 is 0.1-1ml/L, is preferably 0.2-0.8ml/L, is more preferably 0.45-0.55ml/L; And/or the addition of trimethyl-glycine is 0.05-0.5g/L, is preferably 0.1-0.3g/L, is more preferably 0.15-0.25g/L.
3. method according to claim 1, wherein, fermentation culture is short-term, and the time of preferred fermentation culture was no more than 36 hours, is more preferably 26-36 hour, as 26-28 hour or 32-36 hour.
4. method according to claim 1, wherein, the subtilis of the product gamma-polyglutamic acid-in step (1) activation culture and obtaining in seed culture medium.
5. obtain the method for the subtilis of high yield (preferably short fermentation high yield) gamma-polyglutamic acid-, it comprises:
(1) the subtilis liquid culture of product gamma-polyglutamic acid-to be mutagenic (is preferably cultured to OD
600for 10-12), then dilution (preferably dilutes 10
6doubly);
(2) the dilution bacterium liquid that step (1) obtains is carried out under dark condition uv irradiating (preferably under 30W ultraviolet lamp the irradiation of 30cm place 180 seconds);
(3) the bacterium liquid through irradiating step (2) obtained lucifuge on plate screening substratum is cultivated;
(4) step (3) is cultivated the single bacterium colony obtained and carry out fermentation culture (preferred short fermentation) respectively;
(5) output of the gamma-polyglutamic acid-of measuring process (4) fermentation generation, selects the subtilis of high yield (preferably short fermentation high yield) gamma-polyglutamic acid-.
6. the subtilis of high yield (the preferably short fermentation high yield) gamma-polyglutamic acid-of method acquisition according to claim 5, preferably it is preserved in subtilis (BacillusSubtillis) HBY-PBS-ZY55 of China typical culture collection center (CCTCC) on May 20th, 2014 with deposit number CCTCCNO.M2014213.
7. the application of subtilis according to claim 6 in the fermentation (preferably short fermentation) of gamma-polyglutamic acid-.
8. application according to claim 7, wherein, the method for the fermentation of gamma-polyglutamic acid-is included in fermentation and maintains dissolved oxygen amount >=10% and/or maintain sugar (e.g., glucose) content is 10-15g/L.
9. application according to claim 7, the method for the wherein fermentation of gamma-polyglutamic acid-is the arbitrary described method of claim 1-4.
10. substratum, its composition is selected from one of following formula:
(1) glucose 60-80g/L, fructose 5-10g/L, Sodium Glutamate 20-40g/L, calcium chloride 1-1.5g/L, K
2hPO
41.3-1.8g/L, MgSO
47H
2o0.4-0.6g/L, Dried Corn Steep Liquor Powder 5-15g/L, yeast powder 5-10g/L, Trisodium Citrate 10-20g/L, ammonium chloride 10-30g/L, manganous sulfate 0.05-0.2g/L, ferrous sulfate 0.015-0.025g/L, NaCl3-8g/L, pH7.1-7.6;
(2) glucose 10-30g/L, yeast extract 5-10g/L, peptone 5-15g/L, ammonium chloride 2-5g/L, KH
2pO
41-5g/L, MgSO
47H
2o0.2-1g/L, calcium chloride 0.5-1g/L, NaCl3-8g/L, pH7.1-7.6;
(3) glucose 20-40g/L, fructose 5-10g/L, Sodium Glutamate 20-40g/L, calcium chloride 1-1.5g/L, K
2hPO
41.3-1.8g/L, MgSO
47H
2o0.3-0.8g/L, Dried Corn Steep Liquor Powder 5-15g/L, yeast powder 5-15g/L, Trisodium Citrate 10-20g/L, ammonium chloride 10-30g/L, manganous sulfate 0.05-0.2g/L, ferrous sulfate 0.01-0.03g/L, NaCl3-8g/L, defoamer 0.1-1ml/3L, pH7.1-7.6;
(4) glucose 500-1000g/L, MgSO
47H
2o2-5g/L, calcium chloride 2-5g/L, Dried Corn Steep Liquor Powder 15-30g/L;
(5) glucose 10-30g/L, fructose 5-10g/L, Sodium Glutamate 5-15g/L, calcium chloride 1-1.5g/L, K
2hPO
41.5g/L, MgSO
47H
2o0.3-0.8g/L, Dried Corn Steep Liquor Powder 5-15g/L, yeast powder 5-15g/L, Trisodium Citrate 10-20g/L, ammonium chloride 10-30g/L, manganous sulfate 0.05-0.2g/L, ferrous sulfate 0.02g/L, NaCl3-8g/L, defoamer 0.1-1ml/3L, pH7.1-7.6;
(6) glucose 300-1000g/L, MgSO
47H
2o2-5g/L, calcium chloride 2-5g/L, Dried Corn Steep Liquor Powder 15-30g/L, Trisodium Citrate 10-20g/L, ammonium chloride 10-20g/L, K
2hPO
41-2g/L.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510802173.XA CN105385718A (en) | 2014-05-21 | 2014-11-20 | Fermentation preparation method of gamma-polyglutamic acid and strain |
Applications Claiming Priority (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2014102133296 | 2014-05-21 | ||
| CN201410213329 | 2014-05-21 | ||
| CN201410664277.4A CN104694590B (en) | 2014-05-21 | 2014-11-20 | The fermentation preparation of gamma-polyglutamic acid-and the bacterial strain of product gamma-polyglutamic acid- |
| CN201510802173.XA CN105385718A (en) | 2014-05-21 | 2014-11-20 | Fermentation preparation method of gamma-polyglutamic acid and strain |
Related Parent Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410664277.4A Division CN104694590B (en) | 2014-05-21 | 2014-11-20 | The fermentation preparation of gamma-polyglutamic acid-and the bacterial strain of product gamma-polyglutamic acid- |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN105385718A true CN105385718A (en) | 2016-03-09 |
Family
ID=53342140
Family Applications (3)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510802173.XA Pending CN105385718A (en) | 2014-05-21 | 2014-11-20 | Fermentation preparation method of gamma-polyglutamic acid and strain |
| CN201410664277.4A Active CN104694590B (en) | 2014-05-21 | 2014-11-20 | The fermentation preparation of gamma-polyglutamic acid-and the bacterial strain of product gamma-polyglutamic acid- |
| CN201510801416.8A Pending CN105441498A (en) | 2014-05-21 | 2014-11-20 | Method for preparing gamma-polyglutamic acid by fermenting |
Family Applications After (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410664277.4A Active CN104694590B (en) | 2014-05-21 | 2014-11-20 | The fermentation preparation of gamma-polyglutamic acid-and the bacterial strain of product gamma-polyglutamic acid- |
| CN201510801416.8A Pending CN105441498A (en) | 2014-05-21 | 2014-11-20 | Method for preparing gamma-polyglutamic acid by fermenting |
Country Status (1)
| Country | Link |
|---|---|
| CN (3) | CN105385718A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110628688A (en) * | 2016-12-23 | 2019-12-31 | 南京轩凯生物科技有限公司 | Bacillus subtilis for producing gamma-polyglutamic acid and application thereof |
| CN113957033A (en) * | 2021-09-22 | 2022-01-21 | 广东肇庆星湖生物科技股份有限公司 | Method for improving production capacity of polyglutamic acid-producing wild strain |
Families Citing this family (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105385717B (en) * | 2015-11-11 | 2018-11-20 | 广东省微生物研究所 | Application of the iron ion in fermentation of bacillus subtilis production low molecular weight gamma-polyglutamic acid |
| CN106222219B (en) * | 2016-08-30 | 2021-04-20 | 齐鲁制药（内蒙古）有限公司 | Material supplementing method for recovering metabolism of abamectin fermentation hyphae |
| CN107937451A (en) * | 2016-10-12 | 2018-04-20 | 镇江市天益生物科技有限公司 | With the method for mushroom waste material production γ polyglutamic acids |
| CN106636240A (en) * | 2016-11-17 | 2017-05-10 | 东莞波顿香料有限公司 | High-concentration gamma-polyglutamic acid and fermentation method thereof |
| CN106591190B (en) * | 2016-12-16 | 2019-07-16 | 大连理工大学 | A kind of bacillus and its preparing the application in gamma-polyglutamic acid |
| CN110195086A (en) * | 2019-06-11 | 2019-09-03 | 天津科技大学 | A method of gamma-polyglutamic acid is produced using soy sauce residues solid state fermentation |
| CN114854635A (en) * | 2022-05-18 | 2022-08-05 | 四川生力源生物工程有限公司 | Fermentation medium of bacillus subtilis and method for producing gamma-polyglutamic acid |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101109010A (en) * | 2007-07-17 | 2008-01-23 | 秦皇岛领先科技发展有限公司 | Mycopremna generating gamma- polyglutamic acid and culturing method thereof |
| CN101235401A (en) * | 2007-02-02 | 2008-08-06 | 上海祥韦思化学品有限公司 | Fermentation method for preparing L-amino acid |
-
2014
- 2014-11-20 CN CN201510802173.XA patent/CN105385718A/en active Pending
- 2014-11-20 CN CN201410664277.4A patent/CN104694590B/en active Active
- 2014-11-20 CN CN201510801416.8A patent/CN105441498A/en active Pending
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101235401A (en) * | 2007-02-02 | 2008-08-06 | 上海祥韦思化学品有限公司 | Fermentation method for preparing L-amino acid |
| CN101109010A (en) * | 2007-07-17 | 2008-01-23 | 秦皇岛领先科技发展有限公司 | Mycopremna generating gamma- polyglutamic acid and culturing method thereof |
Non-Patent Citations (4)
| Title |
|---|
| 元英进: "《制药工艺学》", 30 June 2007, 化学工业出版社 * |
| 常立群等: "甜菜碱对谷氨酸温度敏感突变株发酵的影响", 《发酵科技通讯》 * |
| 张丹等: "《现代化工·冶金·材料·能源》", 30 September 2012, 中国矿业大学出版社 * |
| 邢晨光等: "甜菜碱对枯草芽孢杆菌合成利巴韦林的影响", 《天津科技大学学报》 * |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110628688A (en) * | 2016-12-23 | 2019-12-31 | 南京轩凯生物科技有限公司 | Bacillus subtilis for producing gamma-polyglutamic acid and application thereof |
| CN113957033A (en) * | 2021-09-22 | 2022-01-21 | 广东肇庆星湖生物科技股份有限公司 | Method for improving production capacity of polyglutamic acid-producing wild strain |
Also Published As
| Publication number | Publication date |
|---|---|
| CN105441498A (en) | 2016-03-30 |
| CN104694590B (en) | 2016-03-16 |
| CN104694590A (en) | 2015-06-10 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104694590B (en) | The fermentation preparation of gamma-polyglutamic acid-and the bacterial strain of product gamma-polyglutamic acid- | |
| CN101109010B (en) | Mycopremna generating gamma- polyglutamic acid and culturing method thereof | |
| CN102643770B (en) | Colibacillus capable of generating succinic acid by anaerobic growth in synthetic medium pure and application thereof | |
| CN102911974B (en) | Method for producing gamma-polyglutamic acid though hot fermentation of bacillus subtilis | |
| CN103361289B (en) | Strain for producing L-lysine and method thereof for producing L-lysine | |
| CN103695500A (en) | Method for increasing pulullan yield | |
| Wu et al. | Kinetic analysis and pH-shift control strategy for poly (γ-glutamic acid) production with Bacillus subtilis CGMCC 0833 | |
| CN103497914B (en) | Bacillus subtilis strain and method for gamma-PGA (poly-glutamic acid) by utilizing same | |
| CN104726381A (en) | Bacterial strain for producing L-lysine and L-lysine producing method thereof | |
| CN105002118A (en) | Culturing method of Lb.plantarum capable of highly producing gamma-aminobutyric acid (GABA) and application | |
| CN109609408A (en) | One plant of gamma-polyglutamic acid superior strain and the method for preparing gamma-polyglutamic acid is carried out liquid fermentation using the bacterial strain | |
| CN102586353A (en) | Non-dependent production method of gamma-polyglutamic acid from glutamic acid | |
| CN110129225A (en) | γ~polyglutamic acid producing strains and breeding prepare γ~polyglutamic acid method | |
| CN107760732A (en) | A kind of production method of agriculture level γ polyglutamic acids | |
| CN101993840B (en) | Production process of Islamic xanthan gum as well as Xanthomonasp.YSL-77 used in same and screening thereof | |
| CN103952447A (en) | Method for producing succinic acid by virtue of fermentation under anaerobic conditions | |
| CN114456980B (en) | Gamma-polyglutamic acid high-yield strain and application thereof | |
| CN101463370B (en) | Method for preparing L-lactic acid by fermenting potato starch by Rhizopus oryzae | |
| CN105018409A (en) | Methyl nutritional type bacillus spore-production fermentation medium and culture method thereof | |
| CN103911333B (en) | One strain is produced the bacterial strain of high yield phenylalanine and is produced the method for phenylalanine | |
| CN103725724A (en) | Method of preparing cadaverine by virtue of immobilized hafnia alvei | |
| CN103255084B (en) | Bacillus licheniformis 7172 and application thereof | |
| CN106929456B (en) | A kind of temmoku acinetobacter calcoaceticus MCDA01 and its method for preparing chitin deacetylase | |
| CN101712966A (en) | Method for producing monascus-pigment in liquid submerged fermentation | |
| CN101508962A (en) | Non-glutamic acid dependent form gamma-polyglutamic acid synthesis bacterium and fermentation method |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20160309 |
|
| WD01 | Invention patent application deemed withdrawn after publication |