CN103374540B - Corynebacterium glutamicum and application thereof - Google Patents
Corynebacterium glutamicum and application thereof Download PDFInfo
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- CN103374540B CN103374540B CN201310351990.9A CN201310351990A CN103374540B CN 103374540 B CN103374540 B CN 103374540B CN 201310351990 A CN201310351990 A CN 201310351990A CN 103374540 B CN103374540 B CN 103374540B
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- ZDXPYRJPNDTMRX-VKHMYHEASA-N L-glutamine Chemical compound OC(=O)[C@@H](N)CCC(N)=O ZDXPYRJPNDTMRX-VKHMYHEASA-N 0.000 claims abstract description 68
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Abstract
The invention relates to the microbial field, and discloses corynebacterium glutamicum strains and application thereof. A corynebacterium glutamicum MHZ-0510 strain has a preservation number CGMCC No.7939; a corynebacterium glutamicum MHZ-0511 strain has a preservation number CGMCC No.7940; the two strains have significantly improved ability of fermentation for generating L-glutamine, compared with that of the original strain of wild type of corynebacterium glutamicum B498, and can be widely applied to fermentation production of L-glutamine. The corynebacterium glutamicum strains involved in the invention are obtained by screening aminoglycoside antibiotics, such as streptomycin and neomycin, have resistance to the aminoglycoside antibiotics including streptomycin and neomycin, and have improved ability to synthesis of L-glutamine, thus increasing the yield of L-glutamine. Therefore, aminoglycoside antibiotics can be widely applied to screen of L-glutamine.
Description
Technical field
The present invention relates to microorganism field, relate to Corynebacterium glutamicum and application thereof specifically.
Background technology
L-glutaminate, formal name used at school is 2-amino-5-carboxyl valeramide, is the acid amides of L-glutamic acid.L-glutaminate molecular formula is C
10h
20n
4o
6, molecular weight is 292.289, and structural formula is
L-glutaminate is one of amino acid the abundantest in body fluid, and accounting for 61% of human body total free aminoacids, is the conditionally essential amino acid that human body is the most general, can not lack.L-glutaminate major storage in human body is in skeletal muscle, and its concentration is higher than 30 times of internal milieu, just discharges when needing.L-glutaminate has multiple effect, as immunologic function can be strengthened, safeguard acid base equilibrium, increase cell volume, the synthesis of strengthen muscle cell protein, participate in the biosynthesizing of the mucoprotein constituent glucosamine of alimentary canal mucous membrane, thus promote the reparation of mucosal epithelium, contribute to the elimination of ulcer focus.Meanwhile, L-glutaminate promotes brain metabolism by hemato encephalic barrier, improves brain function, and the same with L-glutamic acid is the important nutrition agent of brain metabolism.In addition, L-glutaminate also can be used for treating the fatigue recovery after athletic movement syndrome and highly intensive labour or work, rebuilds immunity system, is conducive to treatment and supports liver function, reducing the side effect of radiation and chemotherapy in cancer therapy.So a kind of important biochemical reagents are not only by glutamine, be also a kind of extremely rising new drug simultaneously.
L-glutaminate is widely used abroad as medicinal amino acid, and Germany is loaded into pharmacopeia because it has good curative effect in the diseases such as stomach ulcer, gastritis, duodenal ulcer as medicine; In Japan, L-glutaminate has obtained general use as stomach and intestine class medicine and strong sirloin product; The health care medicine that the U.S. is used for the treatment of the diseases such as stomach ulcer is also quite extensive to the use of L-glutaminate; China also due to the excellent characteristics in the recovery of its patient after surgery, and is widely used in medical industry.
The production method of L-glutaminate mainly contains chemical synthesis, enzymic synthesis and fermentation method.Wherein chemical synthesis reactions steps is various.Although and enzymic synthesis reactions steps relatively simply but wherein required reactant Triphosaden (ATP) is expensive, the substrate of enzymatic reaction simultaneously NH
4+, byproduct adenosine diphosphate (ADP) (ADP) all obviously suppresses the generation of L-glutaminate, therefore can not meet the needs of large-scale industrial production.And fermentation method has the advantages such as raw material sources are extensive, production cost is low, quality product is controlled, product is single, it is therefore L-Gln production method the most frequently used at present.
L-glutaminate output height is inseparable with adopted microbial strains, L-glutaminate produces bacterial classification mainly from glutamate producing bacterium, as bar bacterium (Corynebacterium sp.), tyrothricin (Brevibacterium sp.), micrococci (Micrococcus sp.).In addition, non-glutamic acid is also had to produce bacterium, as some variation bacterial classifications of flavobacterium (Flavobacterium rigense).Wherein Corynebacterium glutamicum is one of bacterial classification conventional in L-glutaminate fermentation, but its L-glutaminate output is not high, far can not meet the large-scale industrial production of L-glutaminate.
Summary of the invention
In view of this, the object of the present invention is to provide Corynebacterium glutamicum and application thereof, to improve the output of L-glutaminate, meet the large-scale industrial production of L-glutaminate.
For achieving the above object, the present invention adopts following technical scheme:
The invention provides a kind of Corynebacterium glutamicum, be deposited in China Committee for Culture Collection of Microorganisms's common micro-organisms center, deposit number is CGMCC No.7939.
Invention also provides the application of Corynebacterium glutamicum in production L-glutaminate that deposit number is CGMCC No.7939.
Present invention also offers a kind of Corynebacterium glutamicum, be deposited in China Committee for Culture Collection of Microorganisms's common micro-organisms center, deposit number is CGMCC No.7940.
Invention also provides the application of Corynebacterium glutamicum in production L-glutaminate that deposit number is CGMCC No.7940.
Present invention also offers a kind of production method of L-glutaminate, the Corynebacterium glutamicum of to be CGMCC No.7939 or deposit number by deposit number be CGMCC No.7940 is inoculated in seed culture medium, and to carry out expansion numerous, then by expand numerous after culture proceed to fermention medium fermentation, maintaining pH value between yeast phase is 4-8.
As preferably, the pH value between described yeast phase is 4.9-7.4.
As preferably, described seed culture medium is made up of 20g/L glucose, 0.5g/L potassium primary phosphate, 1.0g/L dipotassium hydrogen phosphate, 30g/L corn steep liquor, 0.4g/L magnesium sulfate, 5.5g/L urea, and pH value is 7.0-7.2.
As preferably, described fermention medium is made up of 160g/L glucose, 40g/L ammonium chloride, 10g/L corn steep liquor, 0.5g/L dipotassium hydrogen phosphate, 0.5g/L potassium primary phosphate, 0.5g/L magnesium sulfate, 50g/L calcium carbonate, 0.005g/L ferrous sulfate, 0.025g/L manganous sulfate, 0.005g/L zinc sulfate, 1.4g/L urea, and pH value is 7.0-7.2.
Present invention also offers the application of aminoglycoside antibiotics in screening L-glutaminate superior strain.
As preferably, described aminoglycoside antibiotics is Streptomycin sulphate or Liu Suanyan NEOMYCIN SULPHATE.
From above technical scheme, deposit number of the present invention is the Corynebacterium glutamicum MHZ-0510 of CGMCC No.7939, and the ability that its fermentation generates L-glutaminate comparatively wild type glutamic acid bar bacterium significantly improves, L-glutaminate output increased 25.0%.Deposit number of the present invention be its fermentation of Corynebacterium glutamicum MHZ-0511 of CGMCC No.7940 generate L-glutaminate ability equally comparatively wild type glutamic acid bar bacterium significantly improve, L-glutaminate output increased 18.75%.Therefore, the Corynebacterium glutamicum of deposit number of the present invention to be CGMCC No.7939 and deposit number be CGMCC No.7940 can be widely used in the production of L-glutaminate.Corynebacterium glutamicum of the present invention obtains through the screening of the aminoglycoside antibiotics such as Streptomycin sulphate or Liu Suanyan NEOMYCIN SULPHATE, it has the resistance to the aminoglycoside antibiotics such as Streptomycin sulphate or Liu Suanyan NEOMYCIN SULPHATE, and improve L-glutaminate synthesis capability, thus L-glutaminate output is improved.Therefore, aminoglycoside antibiotics can be widely used in the screening of L-glutaminate.
The explanation of biological deposits information
Bacterial strain MHZ-0510: Classification And Nomenclature: Corynebacterium glutamicum, Corynebacterium glutamicum is deposited in China Committee for Culture Collection of Microorganisms's common micro-organisms center on July 19th, 2013, address is No. 3, Yard 1, BeiChen xi Road, Chaoyang District, Beijing City, Institute of Microorganism, Academia Sinica, deposit number is CGMCC No.7939.
Bacterial strain MHZ-0511: Classification And Nomenclature: Corynebacterium glutamicum, Corynebacterium glutamicum is deposited in China Committee for Culture Collection of Microorganisms's common micro-organisms center on July 19th, 2013, address is No. 3, Yard 1, BeiChen xi Road, Chaoyang District, Beijing City, Institute of Microorganism, Academia Sinica, deposit number is CGMCC No.7940.
Embodiment
The embodiment of the invention discloses Corynebacterium glutamicum and application thereof.Those skilled in the art can use for reference present disclosure, and suitable improving technique parameter realizes.Special needs to be pointed out is, all similar replacements and change apparent to those skilled in the art, they are all deemed to be included in the present invention.Bacterial strain of the present invention is described by preferred embodiment, related personnel obviously can not depart from content of the present invention, spirit and scope product as herein described is changed or suitably change with combination, realize and apply the technology of the present invention.
For realizing object of the present invention, the present invention adopts following technical scheme:
The present invention with wild type glutamic acid bar bacterium B498(purchased from Shanghai City Industry Wei Biological Research Institute) for starting strain, with N-methyl-N ' nitro-N nitrosoguanidine for mutagenic compound carry out chemomorphosis to it, then the suspension bacteria liquid of the Corynebacterium glutamicum B498 after mutagenesis is coated on respectively on the substratum containing Streptomycin sulphate or Liu Suanyan NEOMYCIN SULPHATE.From filtering out the bacterial strain with streptomycin resistance containing streptomycin medium, called after bacterial strain MHZ-0510.From filtering out the bacterial strain with neomycin resistance containing Liu Suanyan NEOMYCIN SULPHATE substratum, called after bacterial strain MHZ-0511.
The method of " common bacteria system identification handbook " that above-mentioned bacterial strain MHZ-0510 and MHZ-0511 filtered out edits according to the elegant pearl in east, Cai Miaoying is carried out physio-biochemical characteristics detection to it by the present invention, and detected result is consistent with wild type glutamic acid bar bacterium.In addition, analyze through 16S DNA detection, bacterial strain MHZ-0510 and MHZ-0511 and wild type glutamic acid bar bacterium homology, up to 99%, in conjunction with physiological and biochemical property, identify that it is Corynebacterium glutamicum.
For above-mentioned Corynebacterium glutamicum, present invention applicant is deposited in China Committee for Culture Collection of Microorganisms's common micro-organisms center on July 19th, 2013, address is No. 3, Yard 1, BeiChen xi Road, Chaoyang District, Beijing City, Institute of Microorganism, Academia Sinica, wherein, the deposit number of bacterial strain MHZ-0510 is CGMCC No.7939, and the deposit number of bacterial strain MHZ-0511 is CGMCC No.7940.
In an embodiment, the L-glutaminate of Corynebacterium glutamicum MHZ-0510, MHZ-0511 of the present invention and wild type glutamic acid bar bacterium B498 simultaneous test of fermenting shows, the L-glutaminate content of Corynebacterium glutamicum MHZ-0510 fermentation synthesis of the present invention is 4.0g/L, and the ferment L-glutaminate content of synthesis of wild type glutamic acid bar bacterium B498 is 3.2g/L, L-glutaminate output increased 25.0%.The ferment L-glutaminate content of synthesis of Corynebacterium glutamicum MHZ-0511 of the present invention is 3.8g/L, and the ferment L-glutaminate content of synthesis of wild type glutamic acid bar bacterium B498 is 3.2g/L, L-glutaminate output increased 18.75%.Showing that Corynebacterium glutamicum MHZ-0510 and MHZ-0511 of the present invention can be applied to produces in L-glutaminate, L-glutaminate output increased.Therefore, the invention provides Corynebacterium glutamicum MHZ-0510 and MHZ-0511 and producing the application in L-glutaminate, namely the Corynebacterium glutamicum of deposit number to be the Corynebacterium glutamicum of CGMCC No.7939 and deposit number be CGMCC No.7940 is producing the application in L-glutaminate.
In addition, present invention also offers a kind of L-glutaminate production method, the Corynebacterium glutamicum of to be CGMCCNo.7939 or deposit number by deposit number be CGMCC No.7940 is inoculated in seed culture medium, and to carry out expansion numerous, then by expand numerous after culture proceed to fermention medium fermentation, maintaining pH value between yeast phase is 4-8.
Wherein, as preferably, the pH value between yeast phase is 4.9-7.4.
Then production method of the present invention can be separated L-glutaminate according to this area ordinary method till can being performed until and no longer producing L-glutaminate.
Fermention medium for the numerous seed culture medium of expansion and fermentation is known in this field, and those skilled in the art all can adopt suitable substratum to carry out the fermentation of L-glutaminate.
As preferably, seed culture medium of the present invention is made up of 20g/L glucose, 0.5g/L potassium primary phosphate, 1.0g/L dipotassium hydrogen phosphate, 30g/L corn steep liquor, 0.4g/L magnesium sulfate, 5.5g/L urea, and pH value is 7.0-7.2.
As preferably, fermention medium of the present invention is made up of 160g/L glucose, 40g/L ammonium chloride, 10g/L corn steep liquor, 0.5g/L dipotassium hydrogen phosphate, 0.5g/L potassium primary phosphate, 0.5g/L magnesium sulfate, 50g/L calcium carbonate, 0.005g/L ferrous sulfate, 0.025g/L manganous sulfate, 0.005g/L zinc sulfate, 1.4g/L urea, and pH value is 7.0-7.2.
Aminoglycoside antibiotics (Aminoglycosides) is the tobramycin antibiotic be formed by connecting by oxo bridge by aminosugar and aminocyclitol.There are the native amino glucosides classes such as the Streptomycin sulphate etc. from streptomycete, the gentamicin from micromonospora, also have the semi-synthetic aminoglycosides such as amikacin.Aminoglycoside antibiotics is for the synthesis of the effect mainly anti-bacteria protein of bacterium, point of application is at the aminoacyl site of the 16S RNA area decoder of cell 30S ribosomal subunit, it can affect the whole process of bacterioprotein synthesis, hinder the synthesis of initial recombination thing, Induction of bacterial resultant fault albumen and prevent the release of synthetic proteins, thus cause bacterial death.
Streptomycin sulphate and Liu Suanyan NEOMYCIN SULPHATE are aminoglycoside antibioticss, bacterioprotein is disturbed to synthesize by being incorporated on intracellular rrna, make it the protein of resulting anomaly, and bacterial cell membrane permeability is increased, important physiologically substance in cell is caused to leak outside and present germicidal action, comparatively strong to bacterium germicidal action stationary phase, be sterilization stationary phase class microbiotic.
At wild strain after the screening of the aminoglycoside antibiotics such as Streptomycin sulphate or Liu Suanyan NEOMYCIN SULPHATE, may due to aminoglycoside antibioticss such as the protein resistant Streptomycin sulphate of described Corynebacterium glutamicum resulting anomaly or Liu Suanyan NEOMYCIN SULPHATEs, the protein of these exceptions causes L-glutaminate synthetase series to relieve the feedback inhibition of some product, thus cause the L-glutaminate output of mutant strain to be improved, or the glutamine translocator function on described Corynebacterium glutamicum cytolemma changes and facilitates the speed that glutamine goes out from intracellular transport, thus cause the L-glutaminate output of mutant strain to be improved.And Corynebacterium glutamicum MHZ-0510 and MHZ-0511 of the present invention obtains through Streptomycin sulphate or Liu Suanyan NEOMYCIN SULPHATE screening, be provided with the resistance to Streptomycin sulphate or Liu Suanyan NEOMYCIN SULPHATE, and improve L-glutaminate synthesis capability.Therefore present invention also offers the application of aminoglycoside antibiotics in screening L-glutaminate superior strain.
As preferably, described aminoglycoside antibiotics is Streptomycin sulphate or Liu Suanyan NEOMYCIN SULPHATE.
In order to understand the present invention further, below in conjunction with embodiment, the present invention is described in detail.
Embodiment 1: the screening of Corynebacterium glutamicum MHZ-0510, MHZ-0511 of the present invention
Starting strain-wild type glutamic acid bar bacterium B498 is seeded in 30 DEG C of cultivations in LB liquid nutrient medium and obtains the bacteria suspension being in logarithmic phase in 10 hours, then this bacteria suspension is coated on LB solid plate, put by appropriate N-methyl-N ' nitro-N nitrosoguanidine solid particulate to LB solid plate central authorities, being placed in 30 DEG C of incubators cultivations had the lawn of faint growth to be suspended in appropriate stroke-physiological saline solution around scraping N-methyl-N ' nitro-N nitrosoguanidine particle after 16 hours.The physiological saline being suspended with lawn is coated on respectively on the LB solid plate containing 1.0mg/L Streptomycin sulphate or Liu Suanyan NEOMYCIN SULPHATE, 30 DEG C are continued cultivation 2 days, according to the feature such as colonial morphology, color picking list bacterium colony, wherein from filtering out the bacterial strain with streptomycin resistance containing streptomycin medium, called after bacterial strain MHZ-0510.From filtering out the bacterial strain with neomycin resistance containing Liu Suanyan NEOMYCIN SULPHATE substratum, called after bacterial strain MHZ-0511.
LB liquid nutrient medium/LB solid plate formula is as follows: extractum carnis 5g, peptone 10g, NaCl5g, vitamin H 50 μ g, VitB1 100 μ g, leucine 100mg, homoserine 100mg, Threonine 100mg, methionine(Met) 100mg, agar 18g, dissolves and be settled to 1000mL after regulating pH to 6.8-7.4 with distilled water.
Wherein, the difference of LB liquid nutrient medium and LB solid plate is whether agar adds.Vitamin H, VitB1, leucine, homoserine, Threonine, the nonessential interpolation of methionine(Met), can add according to actual needs.
The method of " the common bacteria system identification handbook " edited according to the elegant pearl in east, Cai Miaoying by above-mentioned bacterial strain MHZ-0510, MHZ-0511 filtered out carries out physio-biochemical characteristics detection to it, and detected result is consistent with wild type glutamic acid bar bacterium.In addition, analyze through 16S DNA detection, bacterial strain MHZ-0510 and MHZ-0511 and wild type glutamic acid bar bacterium homology, up to 99%, in conjunction with physiological and biochemical property, identify that it is Corynebacterium glutamicum.
Embodiment 2: L-glutaminate production method of the present invention and L-glutaminate fermentation simultaneous test
1, fermentation process
Corynebacterium glutamicum MHZ-0510 and MHZ-0511 of the present invention is seeded in respectively expand in the seed culture medium of the following stated numerous, in 30 DEG C of shaking culture 16 hours, gained culture is inoculated in the fermention medium of the following stated, the volume ratio of culture and fermention medium is that 1:10(those skilled in the art suitably can regulate according to the amount of the fermention medium in actual production, this ratio is preferred proportion), 30 DEG C of shaking culture are to no longer producing L-glutaminate (being generally 72 hours).In the fermentation medium during shaking culture, the pH value in maintenance fermention medium is between 6.5-7.4.
Seed culture medium: 20g/L glucose, 0.5g/L potassium primary phosphate, 1.0g/L dipotassium hydrogen phosphate, 30g/L corn steep liquor, 0.4g/L magnesium sulfate, 5.5g/L urea form, and pH value is 7.0-7.2.
Fermention medium: 160g/L glucose, 40g/L ammonium chloride, 10g/L corn steep liquor, 0.5g/L dipotassium hydrogen phosphate, 0.5g/L potassium primary phosphate, 0.5g/L magnesium sulfate, 50g/L calcium carbonate, 0.005g/L ferrous sulfate, 0.025g/L manganous sulfate, 0.005g/L zinc sulfate, 1.4g/L urea form, and pH value is 7.0-7.2.
2, L-glutaminate fermentation simultaneous test
Corynebacterium glutamicum MHZ-0510, MHZ-0511 of the present invention and wild type glutamic acid bar bacterium B498 are fermented according to aforementioned production method simultaneously, yeasting, the inoculum size of three kinds of bacterial strains are all identical, measure the L-glutaminate content synthesized by three kinds of bacterial strains after stopping fermentation by bio-sensing instrument.
Result shows, and wild type glutamic acid bar bacterium B498 output is 3.2g/L, and Corynebacterium glutamicum MHZ-0510 output of the present invention is 4.0g/L, and its L-glutaminate output comparatively starting strain wild type glutamic acid bar bacterium B498 improves 25.0%.Corynebacterium glutamicum MHZ-0511 output of the present invention is 3.8g/L, and its L-glutaminate output comparatively starting strain wild type glutamic acid bar bacterium B498 improves 18.75%.Show deposit number of the present invention to be the Corynebacterium glutamicum MHZ-0510 of CGMCC No.7939 and deposit number be that the Corynebacterium glutamicum MHZ-0511 of the CGMCC No.7940 ability generating L-glutaminate of fermenting significantly improves, the fermentative production of L-glutaminate can be widely used in.
The explanation of above embodiment just understands method of the present invention and core concept thereof for helping.It should be pointed out that for those skilled in the art, under the premise without departing from the principles of the invention, can also carry out some improvement and modification to the present invention, these improve and modify and also fall in the protection domain of the claims in the present invention.
Claims (8)
1. a Corynebacterium glutamicum, is deposited in China Committee for Culture Collection of Microorganisms's common micro-organisms center, and deposit number is CGMCC No.7939.
2. deposit number is the application of Corynebacterium glutamicum in production L-glutaminate of CGMCC No.7939.
3. a Corynebacterium glutamicum, is deposited in China Committee for Culture Collection of Microorganisms's common micro-organisms center, and deposit number is CGMCC No.7940.
4. deposit number is the application of Corynebacterium glutamicum in production L-glutaminate of CGMCC No.7940.
5. the production method of a L-glutaminate, it is characterized in that, the Corynebacterium glutamicum of to be CGMCC No.7939 or deposit number by deposit number be CGMCC No.7940 is inoculated in seed culture medium, and to carry out expansion numerous, then by expand numerous after culture proceed to fermention medium fermentation, maintaining pH value between yeast phase is 4-8.
6. production method according to claim 5, it is characterized in that, the pH value between described yeast phase is 4.9-7.4.
7. production method according to claim 5, it is characterized in that, described seed culture medium is made up of 20g/L glucose, 0.5g/L potassium primary phosphate, 1.0g/L dipotassium hydrogen phosphate, 30g/L corn steep liquor, 0.4g/L magnesium sulfate, 5.5g/L urea, and pH value is 7.0-7.2.
8. production method according to claim 5, it is characterized in that, described fermention medium is made up of 160g/L glucose, 40g/L ammonium chloride, 10g/L corn steep liquor, 0.5g/L dipotassium hydrogen phosphate, 0.5g/L potassium primary phosphate, 0.5g/L magnesium sulfate, 50g/L calcium carbonate, 0.005g/L ferrous sulfate, 0.025g/L manganous sulfate, 0.005g/L zinc sulfate, 1.4g/L urea, and pH value is 7.0-7.2.
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CN107227283A (en) * | 2017-05-26 | 2017-10-03 | 廊坊梅花生物技术开发有限公司 | A kind of Corynebacterium glutamicum and its construction method and application |
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