CN109207402A - One bacillus coagulans and its liquid fermentation enzyme producing method - Google Patents
One bacillus coagulans and its liquid fermentation enzyme producing method Download PDFInfo
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- C12N9/2402—Hydrolases (3) acting on glycosyl compounds (3.2) hydrolysing O- and S- glycosyl compounds (3.2.1)
- C12N9/2468—Hydrolases (3) acting on glycosyl compounds (3.2) hydrolysing O- and S- glycosyl compounds (3.2.1) acting on beta-galactose-glycoside bonds, e.g. carrageenases (3.2.1.83; 3.2.1.157); beta-agarase (3.2.1.81)
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- C12Y302/00—Hydrolases acting on glycosyl compounds, i.e. glycosylases (3.2)
- C12Y302/01—Glycosidases, i.e. enzymes hydrolysing O- and S-glycosyl compounds (3.2.1)
- C12Y302/01023—Beta-galactosidase (3.2.1.23), i.e. exo-(1-->4)-beta-D-galactanase
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Abstract
The invention belongs to fermentation engineering field, in particular to a plant height produces the bacillus coagulans and its liquid fermentation technology of beta galactosidase.The bacillus coagulans are specially bacillus coagulans (Bacillus coagulans) mutant strain BR-171, and deposit number is CGMCC No.14413.The bacterial strain can be stablized, efficiently produce beta galactosidase, and by 50L fermentor liquid submerged fermentation, while through fed-batch fermentation culture 84h, producing enzyme is up to 4000u/ml or more.The beta galactosidase optimal reaction pH of the bacterial strain production is 5.0, still has 80% or more vigor in the range of beta galactosidase pH2.5~8.5, and the pH tolerance range of the enzyme is suitble to most of dairy products；Beta galactosidase optimum temperature is 60 DEG C, and remaining enzyme activity still reaches 88.4% after 2h is kept the temperature at 65 DEG C, has significant heat resistance；In Dairy Industry industrial value with higher.
Description
Technical field:
The invention belongs to fermentation engineering field, in particular to a plant height produces the bacillus coagulans of beta galactosidase
And its liquid fermentation technology.
Background technique:
It condenses gemma bar (Bacillus coagulans), gram-positive bacteria, belongs to hard (or thick) wall bacterium door.Condense bud
Belong to bacillus on spore bacillus taxology, cell is in the shape of a rod, terminal spore, atrichia, decomposes carbohydrate and generates Pfansteihl, is
Homofermentative lactic bacterium.Optimum growth temperature is 45-50 DEG C, optimal pH 6.6-7.0.Bacillus coagulans are amphimicrobians
Bacterium can grow in the environment of aerobic and anaerobic, adapt to the intestinal environment of hypoxemia, have higher tolerance to acid and bile
Property, it is able to carry out lactic fermentation, the Pfansteihl of generation can reduce gut pH, inhibit harmful bacteria, and can promote Bifidobacterium
The growth and breeding of equal beneficial bacteriums.
Beta galactosidase (EC3.2.1.238) scientific name is β-D- galactoside galactohydrolase, commonly uses entitled lactose
Enzyme, the enzyme can be catalyzed the hydrolysis of galactolipin glycosidic bond, and hydrolysis lactose generates glucose and galactolipin.Lactose is special in mammal milk
Some carbohydrates, most carbohydrates are lactose in milk, but lactose is only hydrolyzed into glucose and gala by beta galactosidase
It could be absorbed by body small intestinal cell after sugar.
Beta galactosidase is widely used in Dairy Industry.In milk and diary product process, it is added safe
Beta galactosidase, making its digestion is glucose and galactolipin, and such milk is referred to as low-lactose milk.Low-lactose milk not only may be used
To meet the needs of normal consumer, the person that more can satisfy lactose intolerance, the edible cream of congenital beta-Galactosidase deficiency person
Product, the needs for fully absorbing dairy products nutrition.
Beta galactosidase is from a wealth of sources, and the beta galactosidase being commercialized at present is mainly derived from microorganism, packet
Include Escherichia coli (Escherichia coli), aspergillus niger (Aspergillus niger), aspergillus oryzae (Aspergillus
Oryzae), kluyveromyces (Kluyveromyces), Saccharomyces fragilis (Saccharomyces fragilis) etc..Condense gemma
Bacillus (Bacillus coagulans) is the lactic acid bacteria of one kind " generally believing safety " through U.S. FDA approval, is had quick
Hydrolyze the characteristic that lactose fermentation produces acid.The enzyme activity of the produced beta galactosidase of natural bacterium producing multi enzyme preparation is generally lower at present, excellent
Natural strains scarcity of resources, therefore select novel high yield enzyme strain excellent and be of great significance.
Summary of the invention:
To solve the above-mentioned problems, the mutagenic strain with good heat resistance will be provided herein, while improves hair
Ferment technique improves the enzyme activity for producing beta galactosidase, has boundless potentiality to be exploited and application prospect to Enzymes Industry.
Generally lower for the enzyme activity of current the produced beta galactosidase of natural bacterium producing multi enzyme preparation, excellent Natural strains are deficient
Weary status, the purpose of the present invention is to provide a kind of coagulating bacillus strains of high yield beta galactosidase.
Application and its liquid fermentation method the present invention also provides the bacterial strain of above-mentioned production beta galactosidase.
The bacterial strain of high yield beta galactosidase provided by the invention is specially bacillus coagulans (Bacillus
coagulans)BR-171.It is general that the bacterial strain has been preserved in China Committee for Culture Collection of Microorganisms on July 13rd, 2017
Logical microorganism center (abbreviation CGMCC, address are as follows: city of BeiJing, China Chaoyang District North Star West Road 1 institute 3, postcode 100101) is protected
Hiding number is CGMCC No.14413.
The bacterial strain is had by separating from soil through screening and obtaining through room temperature atmospheric plasma mutagenesis screening and is produced β-
Galactosidase is high-efficient, the good characteristic of stability.
Fermentation broth enzyme activity of the bacterial strain through deep liquid aerobic fementation beta galactosidase is in 4000U/mL or more.
The beta galactosidase optimal reaction pH of the bacterial strain production is 5.0, in beta galactosidase pH2.5-8.5 range
Interior preservation 1h still has 80% or more vigor, and the pH tolerance range of the enzyme is suitble to most of dairy products；Beta galactosidase
Optimum temperature is 60 DEG C, and remaining enzyme activity still reaches 88.4% after 2h is kept the temperature at 65 DEG C, has significant heat resistance；In cream
Product industry industrial value with higher.
Stating bacillus coagulans the present invention also provides more than one is the liquid depth for producing bacterial strain and preparing beta galactosidase
Layer aerobic fementation method, includes the following steps:
(1) bacillus coagulans mutant strain BR-171 slant strains first order seed culture: are accessed into 500 milliliters of shaking flasks
In, 100 milliliters of culture medium loading amount, 180 revs/min of rotary shaker, 34-35 DEG C of cultivation temperature, incubation time 10-15h；
(2) secondary seed culture: first order seed is accessed in 500 milliliters of secondary seed shaking flasks according to 10% inoculum concentration,
Condition of culture is identical as first order seed；
(3) three-level seed culture: secondary seed is accessed in 3000 milliliters of three-level seed flasks with 10% inoculum concentration, culture
800 milliliters of base loading amount, 100 revs/min of rotary shaker, 34-35 DEG C of cultivation temperature, incubation time 10-15h；
(4) first class seed pot culture: by three-level seed with 3.5% inoculum concentration access total measurement (volume) be 50L first class seed pot,
Culture medium loading amount 30L, 32-36 DEG C of cultivation temperature, mixing speed 200-400rpm, ventilation quantity (V/V) 1:1-2, tank pressure
0.05MPa, incubation time 10-20 hours；
(5) fermented and cultured: by first class seed pot strain with 5-10% inoculum concentration access fermentor, 32-36 DEG C of cultivation temperature,
Mixing speed 200-700r/m, ventilation quantity (V/V) 1:1-3, tank press 0.05MPa, incubation time 70-100h；
(6) fermentating controling condition:
Dissolved oxygen control: by adjusting speed of agitator and ventilation quantity, fermentation process dissolved oxygen 15-30% is controlled；
PH control: it by mending ammonium hydroxide or phosphoric acid,diluted, controls pH in fermentation process and is maintained at 7.0-7.2；
Control of additive raw material: when the content of reducing sugar in fermentation liquid is to 5mg/mL-8mg/mL, starting to add supplemented medium,
Feed supplement amount makes fermentation liquid content of reducing sugar be maintained 2mg/mL-5mg/mL；
Put tank standard: 60-80% thallus aging self-dissolving, enzyme activity increases slowly.
(7) extraction of the beta galactosidase and refining methd are as follows:
3% pearlite filtering aid is added into above-mentioned fermentation liquid, carries out plate compression；1%20# silicon will be added in pressing filtering liquid
Diatomaceous earth carries out refined filtration；Refined filtration liquid is concentrated by ultrafiltration with ultrafiltration membrane；Stabilizer (2% salt), preservative are added in concentrate
(3 ‰ sodium benzoates, 1.5 ‰ potassium sorbates), then with sterile film be filtered degerming to get to inscribe beta galactosidase at
Product enzyme preparation.
The level-one, second level, the culture medium group of three-level seed culture become (quality percent by volume):
Lactose 3%, yeast powder 0.5%, glucose 1%, peptone 0.5%, beef extract 0.6%, dipotassium hydrogen phosphate
0.8%, insufficient section pure water is supplied, pH7.5,121-123 DEG C of sterilizing 30min.
The culture medium base group of the seed tank culture becomes (quality percent by volume):
Lactose 3%, yeast powder 0.8%, maltodextrin 15%, peptone 0.5%, corn pulp 0.5%, dipotassium hydrogen phosphate
1.5%, magnesium sulfate 0.1%, insufficient section pure water is supplied, pH7.5,121-123 DEG C of sterilizing 35min.
The culture medium group of the fermentation tank culture becomes (quality percent by volume):
Lactose 3%, yeast powder 1.0%, corn flour 15%, beancake powder 3.0%, corn pulp 1%, calcium chloride 0.5%, phosphoric acid
Hydrogen dipotassium 1.5%, magnesium sulfate 0.1%, sodium citrate 0.5%, insufficient section pure water are supplied, pH7.5,121-123 DEG C of sterilizing
35min。
The supplemented medium group becomes (quality percent by volume): lactose 1%, maltodextrin 50%, soya-bean cake hydrolyzate
3.0%, insufficient section pure water is supplied, pH7.5,121-123 DEG C of sterilizing 35min.
The concocting method of the culture medium of the fermented and cultured are as follows:
Raw material is accurately weighed in proportion, and pure water, corn flour, the beancake powder in raw material are put into material-compound tank, adjusted
Medium temperature amylase (3u/g corn flour) and alpha-amylase (30u/g corn flour) is added in pH6.0, while warming while stirring is extremely
Then 70 DEG C of heat preservation 15min are to slowly warm up to 90 DEG C of heat preservation 20min and liquefy, are eventually adding other raw materials, stir evenly,
Initial pH7.5 is adjusted, 121-123 DEG C of sterilizing 35min is spare.
The soya-bean cake hydrolyzate the preparation method comprises the following steps: soya-bean cake is uniformly mixed with water according to mass ratio 1:5-7, be then added
The lime of soya-bean cake quality 5-7%, stirs evenly, and in 120 DEG C of reaction 65min, is down to room temperature, both obtains soya-bean cake hydrolyzate.
The utility model has the advantages that
The present invention provides a kind of coagulating bacillus strains suitable for industrialized production beta galactosidase, and optimize
Corresponding fermentation mechanism.The fermentation mechanism, process is easy to operate, and condition of culture is mild, and fermentation enzyme activity is average in 4000U/mL
More than, the production cost of unit enzyme activity is reduced, meets the needs in market significantly.Enable beta galactosidase in dairy products
Industry is more widely applied.
Detailed description of the invention:
Fig. 1 is 3 fermentation process enzyme activity of embodiment with incubation time change curve；
The most suitable action pH of Fig. 2 beta galactosidase；
Fig. 3 beta galactosidase pH tolerability curves；
The optimum temperature of Fig. 4 beta galactosidase；
The thermal stability curve of Fig. 5 beta galactosidase.
Specific embodiment:
More detailed description is done to the present invention below by way of specific embodiment, case is embodied by way of example only, no
As the restriction to the scope of the present invention.
Culture medium is as follows used in the process of fluid present invention submerged fermentation prepares beta galactosidase:
Level-one, second level, the culture medium group of three-level seed culture become (quality percent by volume):
Lactose 3%, yeast powder 0.5%, glucose 1%, peptone 0.5%, beef extract 0.6%, dipotassium hydrogen phosphate
0.8%, insufficient section pure water is supplied, pH7.5,121-123 DEG C of sterilizing 30min.
The culture medium group of seed tank culture becomes (quality percent by volume):
Lactose 3%, yeast powder 0.8%, maltodextrin 15%, peptone 0.5%, corn pulp 0.5%, dipotassium hydrogen phosphate
1.5%, magnesium sulfate 0.1%, insufficient section pure water is supplied, pH7.5,121-123 DEG C of sterilizing 35min.
The culture medium group of the fermentation tank culture becomes (quality percent by volume):
Lactose 3%, yeast powder 1.0%, corn flour 15%, beancake powder 3.0%, corn pulp 1%, calcium chloride 0.5%, phosphoric acid
Hydrogen dipotassium 1.5%, magnesium sulfate 0.1%, sodium citrate 0.5%, insufficient section pure water are supplied, pH7.5,121-123 DEG C of sterilizing
35min。
The supplemented medium group becomes (quality percent by volume): lactose 1%, maltodextrin 50%, soya-bean cake hydrolyzate
3.0%, insufficient section pure water is supplied, pH7.5,121-123 DEG C of sterilizing 35min.
The concocting method of the culture medium of the fermented and cultured are as follows:
Raw material is accurately weighed in proportion, and pure water, corn flour, the beancake powder in raw material are put into material-compound tank, adjusted
Medium temperature amylase (3u/g corn flour) and alpha-amylase (30u/g corn flour) is added in pH6.0, while warming while stirring is extremely
Then 70 DEG C of heat preservation 15min are to slowly warm up to 90 DEG C of heat preservation 20min and liquefy, are eventually adding other raw materials, stir evenly,
Initial pH7.5 is adjusted, 121-123 DEG C of sterilizing 35min is spare.
The soya-bean cake hydrolyzate the preparation method comprises the following steps: soya-bean cake is uniformly mixed with water according to mass ratio 1:5-7, be then added
The lime of soya-bean cake quality 5-7%, stirs evenly, and in 120 DEG C of reaction 65min, is down to room temperature, both obtains soya-bean cake hydrolyzate.
The screening of 1 starting strain of embodiment
(1) 2g soil sample is taken from cattle farm cultivation base, be added in the small triangular flask containing the cooling sterile water of 50mL, shaking table
200r/min shakes 20min, is then placed in 80 DEG C of water-baths, water-bath 10min, constantly shakes triangular flask and mixes soil sample, stands
100 μ L of 5min Aspirate supernatant, successively gradient dilution to 10-1~10-9Concentration chooses 10-3, 10-4, 10-5, 10-6Concentration coating
Beef extract-peptone plate, 37 DEG C of cultures for 24 hours, continue 30 DEG C of cultures for 24 hours.
(2) according to the shape of microbe colony, size, surface texture, marginal texture, quality, gloss, transparency, color
With generation can lysochrome etc. feature, isolated single bacterium colony is chosen with oese, moves on to screening and culturing medium plate
On, and number, 34 DEG C of culture 48h.
The screening and culturing medium composition are as follows: lactose 1%, beef extract 0.3%, sodium chloride 0.5%, peptone 1.0%, agar
Powder 1.5%, l000mL, pH7.2,121 DEG C of sterilizing 20min of distilled water.
(3) after cultivating 48h on plate after bacterial strain, the dominant colony on different number plates is inoculated into screening and culturing medium
On inclined-plane, preservation is for secondary screening use.
(4) after the bacterial strain of the different numbers of preservation being inoculated into slant activation 2 times respectively, activated strain is accessed into kind
Sub- culture medium, 180r/min, cultivate 18h by 37 DEG C.Fermentation medium is inoculated by 5% inoculum concentration again, 200r/min, 28 DEG C,
Ferment 48h.Thallus is removed into gained fermentation liquid 10000r/min centrifugation, fermented liquid supernatant liquid carries out the survey of beta galactosidase enzyme activity
Fixed experiment.
The seed culture medium becomes: lactose 2%, glucose 2%, peptone 1%, NaH2PO4·2H2O 0.02%,
Na2HPO4·2H2O 0.04%, MgSO4·7H2O 0.005%, 100mL, pH7.4,121 DEG C of sterilizing 20min of distilled water.
The fermentation medium composition are as follows: lactose 2%, glucose 4%, peptone 2%, NaH2PO4·2H2O 0.02%,
Na2HPO4·2H2O 0.04%, MgSO4·7H2O 0.005%, CaCl20.01%, MnSO40.002%, distilled water
100mL, pH7.4,121 DEG C of sterilizing 20min.
(5) it selects and produces the strong bacterial strain progress glycerol preservation of beta galactosidase enzyme activity, obtain setting out for bacterial strain of the present invention
Bacterial strain.
The mutagenic and breeding of 2 bacterial strain of embodiment
(1) after drawing starting strain activation, thalline were collected by centrifugation, and thallus is resuspended with 5% glycerol, is counted with blood counting chamber
Until it is 10 that bacterium is dense7-108A/mL, in this, as the bacteria suspension that sets out.
(2) normal temperature and pressure plasma system is opened, with alcohol swab wiping operation indoor and outdoor, and opens ultraviolet lamp sterilizing
30min.It takes 10 μ L bacteria suspensions to select the rough surface in slide glass after sterilizing, and is aseptically transferred to slide glass with tweezers
On operating room table top.Helium valves are opened, throughput is set and mutation time carries out mutagenesis.Mutation time be respectively set as 90s,
120s,150s,180s,210s.Slide glass is placed in the EP pipe containing 990 μ L sterile salines after each mutagenesis, whirlpool
Shake 1min in whirlpool.Dilution spread is placed on culture in 34 DEG C of incubators.
(3) plate primary dcreening operation
It will pass through in the single colonie switching primary dcreening operation culture medium that mutagenesis is grown, 30 DEG C of culture 3d.It is small to primary dcreening operation in super-clean bench
The 10%Na of pipe sprinkling sterilizing2CO3Solution is stood several minutes；The tubule of picking colour changed into yellow carries out descending row by shade
Column, number.Successively switching saves inclined-plane, and 30 DEG C of cultures are to spore maturation, in 4 DEG C of preservations of refrigerator.
The plate primary dcreening operation culture medium are as follows: lactose 2%, peptone 1%, (NH4)2SO40.14%, KH2PO420.1%,
CaCl20.03%, MgSO40.3%, Toween-8 0.2%, FeSO40.05%, MnSO40.016%, ZnSO4
0.014%, CoCl20.02%, remaining is water, pH5.5.1% ortho-nitrophenyl of micro-filtration degerming is added in sterilizing after being cooled to 60 degree
Phenol-β-D- galactoside (ONPG) mother liquor, is added in the 1.5mL centrifuge tube of sterilizing after shaking up；
(4) shaking flask secondary screening
In secondary screening culture medium, 34 DEG C are cultivated 48 hours the colony inoculation that primary dcreening operation is obtained, and detect beta galactosidase enzyme
It is living.
The secondary screening culture medium composition: lactose 3%, peptone 1.5%, (NH4)2SO40.2%, KH2PO420.15%,
CaCl20.035%, MgSO40.35%, Toween-8 0.2%, FeSO40.1%, MnSO40.02%, ZnSO4
0.02%, CoCl20.03%, insufficient section pure water is supplied, pH7.0-8.0,121-123 DEG C of sterilizing 30-35min.
(5) strain stability detects:
Live high-enzyme strain obtained by secondary screening is subjected to secondary culture, and tracks shaking flask and detects its enzyme activity.Through shaking flask secondary screening, finally
It determines production bacterial strain, and is named as BR-171, be preserved in China Committee for Culture Collection of Microorganisms's common micro-organisms
Center, deposit number are CGMCC NO.14413.The characteristic of the bacterial strain is that production beta galactosidase is high-efficient, and stability is good.
It is as shown in table 1 to choose superior strain BR-171 continuous passage 6 times shake flask results:
1. bacterial strain BR-171 Detection of Stability result of table
| Algebra | Shaking flask enzyme activity (U/mL) | Opposite enzyme activity (%) |
| F1 | 1589 | 100 |
| F2 | 1601 | 100.8 |
| F3 | 1551 | 97.6 |
| F4 | 1571 | 98.9 |
| F5 | 1610 | 101.3 |
| F6 | 1591 | 100.1 |
3 liquid fermentation of embodiment produces inscribe beta galactosidase and its Hydrolysis kinetics
(1) bacillus coagulans mutant strain BR-171 slant strains first order seed culture: are accessed into 500 milliliters of shaking flasks
In, 100 milliliters of culture medium loading amount, 180 revs/min of rotary shaker, 34-35 DEG C of cultivation temperature, incubation time 11h；
(2) secondary seed culture: first order seed is accessed in 500 milliliters of secondary seed shaking flasks according to 10% inoculum concentration,
Condition of culture is identical as first order seed；
(3) three-level seed culture: secondary seed is accessed in 3000 milliliters of three-level seed flasks with 10% inoculum concentration, culture
800 milliliters of base loading amount, 100 revs/min of rotary shaker, 34-35 DEG C of cultivation temperature, incubation time 11h；
(4) first class seed pot culture: by three-level seed with 3.5% inoculum concentration access total measurement (volume) be 50L first class seed pot,
Fermentation medium loading amount 30L, 35 DEG C of cultivation temperature, mixing speed 300rpm, ventilation quantity (V/V) 1:2, tank presses 0.05MPa, culture
Time 15 hours；
(5) fermented and cultured: first class seed pot strain is accessed into fermentor with 8% inoculum concentration, 35 DEG C of cultivation temperature, stirring is fast
500r/m, ventilation quantity (V/V) 1:1.5 are spent, tank presses 0.05MPa, incubation time 84h；
(6) fermentating controling condition:
Dissolved oxygen control: by adjusting speed of agitator and ventilation quantity, fermentation process dissolved oxygen 15-30% is controlled；
PH control: it by mending ammonium hydroxide or phosphoric acid,diluted, controls pH in fermentation process and is maintained at 7.0-7.2；
Control of additive raw material: when the content of reducing sugar in fermentation liquid is down to 5mg/mL, start to add supplemented medium, feed supplement amount
Fermentation liquid content of reducing sugar is set to be maintained 2mg/mL-5mg/mL；
Put tank standard: 60-80% thallus aging self-dissolving, enzyme activity increases slowly.
Such as the enzymatic production situation that the following table 2 is 6 batch of 30L fermentor, average producing enzyme level is 4091U/mL, meanwhile, it is right
BF-4 batch enzyme activity changes with incubation time maps, and is as shown in Figure 1 enzyme activity with the change curve of incubation time.
Enzymatic production of the 2. bacterial strain BR-171 of table in 6 batch of 30L fermentor
| Batch fermentation | Fermentation period (h) | It ferments enzyme activity (U/mL) |
| BF-1 | 84 | 3984 |
| BF-2 | 84 | 4201 |
| BF-3 | 84 | 4115 |
| BF-4 | 84 | 4231 |
| BF-5 | 84 | 3997 |
| BF-6 | 84 | 4021 |
(7) extraction of the beta galactosidase and refining methd are as follows:
3% pearlite filtering aid is added into above-mentioned fermentation liquid, carries out plate compression；1%20# silicon will be added in pressing filtering liquid
Diatomaceous earth carries out refined filtration；Refined filtration liquid is concentrated by ultrafiltration with ultrafiltration membrane；Stabilizer (2% salt), preservative are added in concentrate
(3 ‰ sodium benzoates, 1.5 ‰ potassium sorbates), then with sterile film be filtered degerming to get to inscribe beta galactosidase at
Product enzyme preparation.
Soya-bean cake hydrolyzate the preparation method comprises the following steps: soya-bean cake is uniformly mixed with water according to mass ratio 1:6, soya-bean cake matter is then added
The lime of amount 6%, stirs evenly, in 120 DEG C of reaction 65min, is down to room temperature, both obtains soya-bean cake hydrolyzate.
4 liquid fermentation of embodiment produces inscribe beta galactosidase and its Hydrolysis kinetics
(1) bacillus coagulans mutant strain BR-171 slant strains first order seed culture: are accessed into 500 milliliters of shaking flasks
In, 100 milliliters of culture medium loading amount, 180 revs/min of rotary shaker, 34-35 DEG C of cultivation temperature, incubation time 15h；
(2) secondary seed culture: first order seed is accessed in 500 milliliters of secondary seed shaking flasks according to 10% inoculum concentration,
Condition of culture is identical as first order seed；
(3) three-level seed culture: secondary seed is accessed in 3000 milliliters of three-level seed flasks with 10% inoculum concentration, culture
800 milliliters of base loading amount, 100 revs/min of rotary shaker, 34-35 DEG C of cultivation temperature, incubation time 15h；
(4) first class seed pot culture: by three-level seed with 3.5% inoculum concentration access total measurement (volume) be 50L first class seed pot,
Fermentation medium loading amount 30L, 32 DEG C of cultivation temperature, mixing speed 400rpm, ventilation quantity (V/V) 1:1, tank presses 0.05MPa, culture
Time 20 hours；
(5) fermented and cultured: first class seed pot strain is accessed into fermentor with 10% inoculum concentration, 32 DEG C of cultivation temperature, is stirred
Speed 700r/m, ventilation quantity (V/V) 1:3, tank press 0.05MPa, incubation time 90h；
(6) fermentating controling condition:
Dissolved oxygen control: by adjusting speed of agitator and ventilation quantity, fermentation process dissolved oxygen 15-30% is controlled；
PH control: it by mending ammonium hydroxide or phosphoric acid,diluted, controls pH in fermentation process and is maintained at 7.0-7.2；
Control of additive raw material: when the content of reducing sugar in fermentation liquid is down to 8mg/mL, start to add supplemented medium, feed supplement amount
Fermentation liquid content of reducing sugar is set to be maintained 2mg/mL-5mg/mL；
Put tank standard: 60-80% thallus aging self-dissolving, enzyme activity increases slowly；
When fermentation ends, producing enzyme level is 4532U/mL fermentation liquid.
(7) extraction of the beta galactosidase and refining methd are as follows:
3% pearlite filtering aid is added into above-mentioned fermentation liquid, carries out plate compression；1%20# silicon will be added in pressing filtering liquid
Diatomaceous earth carries out refined filtration；Refined filtration liquid is concentrated by ultrafiltration with ultrafiltration membrane；Stabilizer (2% salt), preservative are added in concentrate
(3 ‰ sodium benzoates, 1.5 ‰ potassium sorbates), then with sterile film be filtered degerming to get to inscribe beta galactosidase at
Product enzyme preparation.
Soya-bean cake hydrolyzate the preparation method comprises the following steps: soya-bean cake is uniformly mixed with water according to mass ratio 1:7, soya-bean cake matter is then added
The lime of amount 7%, stirs evenly, in 120 DEG C of reaction 65min, is down to room temperature, both obtains soya-bean cake hydrolyzate.
The enzyme activity determination method of 5 beta galactosidase of embodiment
Total system is 1mL, contains 700 μ L deionized waters, the kaliumphosphate buffer of 100 μ L 500mmol/L pH6.0,100 μ L
The oNPG of 20mmol/L, blending incubation after five minutes, are added 100 μ L through appropriate diluted enzyme solution, mix, 55 DEG C warm bath 10 minutes,
The Na of 2mL 0.5mmol/L is added immediately2CO3Reaction is terminated, with light absorption value, that is, oNP life at spectrophotometer measurement 410nm
Cheng Liang.The unit of activity of enzyme is defined as: the enzyme amount that hydrolysis in 1 minute generates 1 μm of ol oNP is 1 unit of activity U.
The most suitable action pH range of 6 enzyme of embodiment
On the basis of the beta galactosidase product of the produced enzyme activity 11401U/mL of the present invention, under the conditions of 60 DEG C, press
According to enzyme activity determination method described in embodiment 5, respectively in different pH value (3.0,4.0,4.5,5.0,5.5,6.0,7.0) buffer
In, the enzyme activity change curve of measurement is as shown in Fig. 2, beta galactosidase optimal reaction pH is 5.0.In addition, in difference
1h is saved under pH (2.5,3.5,4.5,5.5,6.5,7.5,8.5) buffer, measures enzyme activity change curve such as Fig. 3, it should
Enzyme has preferable pH tolerance at pH2.5-8.5, and opposite enzyme activity remains to reach 80% or more at pH2.5-8.5.
Above-mentioned difference pH buffer is respectively as follows: 50mmol/L acetic acid-sodium acetate buffer solution pH2.5~6.5,50mmol/L phosphorus
Sour hydrogen dipotassium-potassium phosphate buffer pH6.5~8.5.
The optimum temperature of 7 beta galactosidase of embodiment
It is 5.0 conditions in pH value on the basis of the beta galactosidase product of the produced enzyme activity 11401U/mL of the present invention
Under, respectively under different temperatures (40,50,55,60,65,70,80), measure enzyme activity, the enzyme activity change curve of measurement
As shown in figure 4, the optimum temperature of enzyme is 60 DEG C.
The thermal stability of 8 beta galactosidase of embodiment
On the basis of the beta galactosidase product of enzyme activity 11401U/mL, under the conditions of pH value is 5.0, respectively not
2h is kept the temperature under synthermal (30,35,40,45,50,55,60,65,70,75,80), according to enzyme activity determination side described in embodiment 3
Method measures remaining enzyme activity, as shown in figure 5, keeping the temperature remaining enzyme activity after 2h at 65 DEG C is 88.4%, has good heat-resisting preservation
Activity can be widely applied in hot industry production.
Claims (5)
1. a kind of bacillus coagulans of high yield beta galactosidase, which is characterized in that the bacillus coagulans are specially solidifying
Bacillus (Bacillus coagulans) BR-171 is tied, deposit number is CGMCC No.14413.
2. bacillus coagulans as described in claim 1, which is characterized in that using BR-171 fermenting and producing beta galactosidase
Method is specific as follows:
(1) first class seed pot culture: seed liquor is accessed into first class seed pot with 3.5% inoculum concentration, 32-36 DEG C of cultivation temperature, is stirred
Mix speed 200-400rpm, ventilation quantity 1:1-2, tank presses 0.05MPa, and incubation time 10-20 hours；
(2) fermented and cultured: first class seed pot strain is accessed into fermentor with 5-10% inoculum concentration, 32-36 DEG C of cultivation temperature, is stirred
Speed 200-700r/m, ventilation quantity 1:1-3, tank press 0.05MPa, dissolved oxygen 15-30%, pH7.0-7.2；Incubation time 70-
100h；
Control of additive raw material: when the content of reducing sugar in fermentation liquid is to 5mg/mL-8mg/mL, start to add supplemented medium, feed supplement
Amount makes fermentation liquid content of reducing sugar be maintained 2mg/mL-5mg/mL；
Put tank standard: 60-80% thallus aging self-dissolving, enzyme activity increases slowly.
3. bacillus coagulans as claimed in claim 2, which is characterized in that the culture medium of the fermented and cultured forms are as follows: cream
Sugar 3%, yeast powder 1.0%, corn flour 15%, beancake powder 3.0%, corn pulp 1%, calcium chloride 0.5%, dipotassium hydrogen phosphate
1.5%, magnesium sulfate 0.1%, sodium citrate 0.5%, insufficient section pure water supplies, pH7.5,121-123 DEG C of sterilizing 35min.
The supplemented medium composition are as follows: lactose 1%, maltodextrin 50%, soya-bean cake hydrolyzate 3.0%, insufficient section pure water
It supplies, pH7.5,121-123 DEG C of sterilizing 35min.
4. the application of bacillus coagulans described in claim 1.
5. bacillus coagulans described in claim 1 are preparing the application in beta galactosidase.
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Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102653746A (en) * | 2012-04-12 | 2012-09-05 | 大连大学 | Method for producing low-temperature beta-galactosidase through microbial fermentation |
| CN103614313A (en) * | 2013-09-30 | 2014-03-05 | 徐州工程学院 | Strain for producing high temperature resistance beta-galactosidase through fermentation, and screening method thereof |
| CN104130990A (en) * | 2014-08-08 | 2014-11-05 | 南京林业大学 | Beta-galactosidase and application thereof |
-
2018
- 2018-10-11 CN CN201811183211.8A patent/CN109207402B/en active Active
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102653746A (en) * | 2012-04-12 | 2012-09-05 | 大连大学 | Method for producing low-temperature beta-galactosidase through microbial fermentation |
| CN103614313A (en) * | 2013-09-30 | 2014-03-05 | 徐州工程学院 | Strain for producing high temperature resistance beta-galactosidase through fermentation, and screening method thereof |
| CN104130990A (en) * | 2014-08-08 | 2014-11-05 | 南京林业大学 | Beta-galactosidase and application thereof |
Non-Patent Citations (2)
| Title |
|---|
| NAVNEET BATRA等: "Production and characterization of a thermostable beta-galactosidase from Bacillus coagulans RCS3", 《BIOTECHNOL APPL BIOCHEM》 * |
| 宋春雷等: "凝结芽孢杆菌产β-半乳糖苷酶条件的优化", 《中国农业大学学报》 * |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
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