CN1584015A - Preparation of valuable sialinic acid from cheap sodium lactate by multi-step coupling bio-conversion - Google Patents
Preparation of valuable sialinic acid from cheap sodium lactate by multi-step coupling bio-conversion Download PDFInfo
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Abstract
A method for preparing valuable sialic acid by cheap sodium lactate through multi-step coupling biotransformation is disclosed. It includes culture containing lactic oxidase strain, construction and culture of E.coli HB101(pBV220-ALD), preparation of N-acetylmannosamine, sialic acid converting synthesis by complete cell containing lactic oxidase and sialic aldolase with cheap sodium lactate as precursor, and separation and purification of sialic acid by ion exchange. It achieves low cost, simple operation and extensive converting conditions.
Description
(1) technical field
The present invention relates to a kind of microorganism catalysis that utilizes and prepare sialic method.Specifically, relate to a kind of two kinds of microorganism intact cells that contain Lactate Oxidase and acetylneuraminate aldolase respectively, prepare the sialic method of high value through multistep coupling bio-transformation by cheap sodium lactate.
(2) background technology
Sialic acid (Sialic acid, SA), be neuraminic acid (Neuraminie acid, NA) and the general name of derivative, it is a class natural sugar compounds that extensively is present in the biosystem, separated and the evaluation from first sialic acid, people have just carried out a large amount of research to its biology and physiologically active.It is found that the acylneuraminate compound bringing into play indispensable effect in the many important biologies of life entity, physiological process, they participate in cell and cell directly, the interaction of cell and microorganism, cell and toxin, cell and abzyme.Sialic acid and derivative thereof have very at aspects such as treatment influenza, nervous system disease, inflammation, tumours, and important use is worth.(5-acetamido-3,5-dideoxy-D-glycero-D-galacto-non-2-ulosonic acid Neu5Ac) are wherein most representative gang to the N-n acetylneuraminic acid n.
At present, sialic suitability for industrialized production research also be not a lot, this and sialic extensive use are incompatible.The about 50-100 dollar of the price/gram of present world market.The sialic main method of industrial production is chemosynthesis, but the chemosynthesis sialic acid at least will be through the reaction of tens steps, form a large amount of intermediate products, cause very big difficulty for sialic back sepn process, this also is to cause one of very expensive reason of present sialic price.1991, Lekh Raj Juneja etc. from birds, beasts and eggs membrane of yolk and frenulum in a large amount of sialic acids that extract, the U.S. has also reported from cow's milk whey and casein and has extracted sialic acid, but because the content of sialic acid in animal tissues is lower, separate and the purification process more complicated, yield is lower, therefore, is difficult to carry out big suitability for industrialized production.Nineteen fifty-seven, Barry and Goebel at first find sialic with polymer one polysialic acids in intestinal bacteria K235, people found polysialic acids in succession in other bacterial strain afterwards, can obtain the sialic acid monomer after acid or enzymic hydrolysis, this provides important prerequisite for the microbiological industry production that realizes polysialic acids.
1958, reported first such as Comb under the katalysis of acetylneuraminate aldolase (EC4.1.3.3) sialic acid can be N-acetylmannosamine (ManNAc) and pyruvic acid by biological degradation, people expect utilizing this biodegradable inverse process thus, come the sialic biosynthesizing of catalysis by acetylneuraminate aldolase.The eighties in 20th century, Auge, Wong and Whitesides group have reported respectively and have used acetylneuraminate aldolase to do the formation that catalyzer has been realized C-C key between ManNAc and the pyruvic acid, obtained sialic acid thus.They impel this balanced reaction to carry out to the sialic acid compound direction by adding excessive greatly pyruvic acid.Along with the structure of acetylneuraminate aldolase genetic engineering bacterium, this method is more and more important in sialic scale operation.
Yet, produce sialic acid in this way, must note some problems: (1) ManNAc costs an arm and a leg, and needs to obtain by the isomerization of N-acetylglucosamine (GlcNAc); (2) ManNAc has similar chemical property with GlcNAc, separates very difficulty; (3) GlcNAc is the inhibitor of acetylneuraminate aldolase; (4) acetylneuraminate aldolase is to the Km value higher (0.7M) of ManNAc reaction; (5) acetylneuraminate aldolase mainly is the sialic DeR of catalysis, must add the doubly excessive pyruvic acid of 7-10 and promote reversed reaction, such way, the one, improved cost greatly, the 2nd, the existence of a large amount of pyruvic acid has caused very big difficulty for sialic separation and purification.
Along with the deep development of research, these problems have obtained partly solving.Spivak and Roseman have reported under alkaline condition, have obtained ManNAc from GlcNAc: will carry out rotary evaporation after the reaction solution furnishing neutrality, part GlcNAc crystallization is separated out, use hot ethanol reflux extraction enrichment ManNAc then.Sugai etc. nineteen ninety-five by in enzyme reactor, add pyruvate decarbonylation base enzyme with reaction system in excessive pyruvic acid be degraded to acetaldehyde and carbonic acid gas, thereby product and difficulty on pyruvic acid separates when having reduced the biosynthesizing sialic acid.
1991, Wandrey etc. adopted diverse method, can obtain sialic acid continuously from relatively inexpensive GlcNAc.They are raw material with GlcNAc and pyruvic acid, by allomerase and two step of acetylneuraminate aldolase enzymic catalytic reaction, have synthesized sialic acid in enzyme mebrane reactor.Though this method has very high yield, allomerase does not also obtain suitability for industrialized production, is not easy to obtain.Marukin company has also adopted the method for allomerase simultaneously, and they allow entire reaction course carry out under alkaline condition, but this has caused the acetylneuraminate aldolase activity to be suppressed and the decline of isomerization speed.
1997, Mahmoudian group adopted and allows pyruvic acid and bisulfite form complex compound to remove the method for pyruvic acid.Afterwards, they adopted the method for enrichment ManNAc again, made in the reaction system ManNAc excessive, removed this step of pyruvic acid and save.But the method that forms complex compound has been introduced new impurity again, needs further to remove.
From top several synthetic methods as can be seen, up to the present, also do not find very perfect method to solve existing a series of problems in isomerization process and the aldehyde compression process, production cost is very big, causes sialic holding at high price.
(3) summary of the invention
The present invention is directed in the above-mentioned existing method deficiency that product cost is higher relatively.The problem to be solved in the present invention is, a kind of substrate Sodium.alpha.-hydroxypropionate and GlcNAc by cheapness is provided, and unites the sialic method of preparation that transforms by Lactate Oxidase and acetylneuraminate aldolase.This method has cheap, and is simple to operate, can effectively remove the characteristics of Sodium.alpha.-ketopropionate to the product inhibition of Lactate Oxidase.
What the present invention relates to a kind ofly prepares the sialic method of high value by cheap sodium lactate through multistep coupling bio-transformation, and concrete steps are as described below:
(1) Lactate Oxidase bacterial classification: select one of acinetobacter calcoaceticus (Acinetobacter sp.) ATCC11171, pseudomonas (Pseudomonas sp.) ATCC11452.
(2) slant culture: above-mentioned bacterial strains is inoculated in that to contain mass volume ratio be 1.5～2.0% agar and is added with on the solid inclined-plane minimum medium that mass volume ratio is 0.2～3% DL type or L type Sodium.alpha.-hydroxypropionate, cultivated 15～30 hours for 25 ℃～45 ℃.
(3) first order seed is cultivated: with the bacterial strain of step (2) cultivation, encircle with inoculation articulating 1～2 under aseptic condition that to contain mass volume ratio in 20～100mL be in 0.2～3% the DL type or L type Sodium.alpha.-hydroxypropionate liquid-based basal culture medium BLM, under 25 ℃～45 ℃ conditions, shaking culture is 10～30 hours on shaking table, makes first order seed.
(4) enlarged culturing: with the inoculum size of 5% volume ratio, connecing first order seed contains in the DL type or L type Sodium.alpha.-hydroxypropionate BLM that mass volume ratio is 0.2-3% in 300～1000mL, under 25 ℃～45 ℃ conditions, shaking culture is 10～30 hours on shaking table, makes secondary seed.
(5) fermentor cultivation: with the inoculum size of 5% volume ratio, connecing secondary seed contains among the BLM that mass volume ratio is 0.2～3% DL type or L type Sodium.alpha.-hydroxypropionate in 1.8～8L, under 25 ℃～45 ℃ conditions, cultivated 15～40 hours, be that DNP and pyruvic acid effect generate red-brown 2 with 2,4 dinitrophenyl hydrazine during this time, the method for 4-dinitrophenylhydrazone detects the enzyme of cell Lactate Oxidase and lives, when enzyme work reaches 0.9～2.0U/ml, stop fermentation culture.
In aforesaid method, the unit (U) that the Lactate Oxidase enzyme is lived is defined as: 37 ℃, per minute catalytic substrate lactic acid transforms the enzyme amount that generates 1 μ mol pyruvic acid.
Above-mentioned liquid-based basal culture medium BLM, concrete prescription by mass volume ratio is:
KH
2PO
40.1%, K
2HPO
43H
2O 0.08%, NH
4Cl 0.1%, MgSO
47H
2O 0.05%, CaCl
22H
2O0.005%, yeast powder 0.1%, metal ion mixed solution 0.12%; Regulate under 7.0,115 ℃ of conditions of pH and sterilized 20 minutes.
The prescription of metal ion mixed solution following (g/L):
Na
2EDTA，50；ZnSO
4·7H
2O，20；MnCl
2·4H
2O，5；(NH
4)
6Mo
7O
24·4H
2O，1，；FeSO
4·7H
2O，5；CuSO
4·5H
2O，1.5；CoCl
2·H
2O，1.6；CaCl
2·2H
2O，5.5。
(6) collect thalline: got under 5,000 rev/mins of conditions of fermented liquid of step (5) centrifugal 5～8 minutes, and with physiological saline washing 2～3 times, with identical centrifugal condition, the collecting precipitation thalline is biological catalyst A with the thalline of gained, and is 4 ℃ of storages, standby.
(7) structure of acetylneuraminate aldolase bacterial strain: the method structure colibacillus engineering strain with routine is E.coli HB101 (pBV220-ALD).
The structure of recombinant strain: adopt conventional method to prepare the genomic dna of E.coli K12 bacterial strain, the method that this process can prepare with reference to a small amount of of bacterial genomes in " the fine works molecular biology guide " of Science Press's publication, the genomic dna of extraction E.coli K12 bacterial strain; Use synthetic primer pcr amplification from the genomic dna of E.coli K12 bacterial strain to obtain the acetylneuraminate aldolase gene; Use EcoRI, PstI double digestion plasmid pBV220, be connected with the acetylneuraminate aldolase gene that amplification obtains then, obtain recombinant plasmid pBV220-ALD; Again recombinant plasmid pBV220-ALD is imported carrier E.coli HB101 through transforming, obtain engineering strain E.coli HB101 (pBV220-ALD);
Wherein the host is E.coli HB101; Acetylneuraminate aldolase (EC4.1.3.3) gene is obtained by pcr amplification in the genomic dna of E.coli K12 bacterial strain; Plasmid is pBV220; The primer of 5 ' end is AGGAATTCATGGCAACGAATTTAC, adds the site of an EcoRI; The primer of 3 ' end is TCCTGCAGTCACCCGCGCTCTT, adds the site of a PstI.
(8) the dull and stereotyped cultivation: the bacterial strain of step (7) gained is scoring to contains on the penbritin LB flat board that contains 100 μ g/mL that mass volume ratio is 1.5% agar, cultivated 10～12 hours for 25 ℃～40 ℃.
(9) first order seed: under aseptic condition,, be inoculated in the liquid nutrient medium that contains 100 μ g/mL penbritins of 5mL 25 ℃～40 ℃ shaking table shaking culture 10～12 hours then with a single bacterium colony on aseptic toothpick picking step (8) flat board.
(10) secondary seed: under aseptic condition, get nutrient solution that step (9) cultivated and be 2% inoculum size with volume ratio, be inoculated into 30mL～500mL and contain in the LB liquid nutrient medium of penbritin of 100 μ g/mL, 25 ℃～40 ℃ shaking table shaking culture 5～10 hours.
(11) fermentor cultivation: under aseptic condition, the nutrient solution of getting step (10) gained is the M9 liquid nutrient medium of the improvement of inoculum size inoculation 2L～10L of 8% with volume ratio, cultivated 5～12 hours for 25 ℃～40 ℃, changing temperature is 42 ℃～50 ℃ cultivations 3～7 hours.
The M9 liquid nutrient medium of above-mentioned improvement, concrete prescription by mass volume ratio is:
Peptone 0.5%～2%; Yeast powder 0.25%～0.6%; Na
2HPO
47H
2O 0.5%～2%; KH
2PO
40.1%～0.5%; NaCl 0.02%～0.1%; NH
4Cl 0.05%～0.2%; CaCl
20.0011%; Glucose 0.2%～2%; Sterilized 15 minutes for 115 ℃.
(12) collect thalline: it is centrifugal 5～30 minutes that step (11) is cultivated 5,000 rev/mins of cultures that obtain; Physiological saline washing thalline with 0.85% 1～3 time, with identical centrifugal condition, the collecting precipitation thalline; Place 0 ℃～-30 ℃ refrigerator and cooled to freeze preservation thalline, promptly obtain biological catalyst B, stand-by.
(13) N-kharophen seminose is the isomerization of ManNAc: the N-acetylglucosamine of getting 100～400g be the dissolution of sodium hydroxide of GlcNAc and 2.2～8.8g in 1～4L water, then under the condition of room temperature, isomerization reaction 36～96 hours.
(14) concentrate: is 5～7 with the isomerization solution of step (13) gained through the ion exchange resin of 732H type or with glacial acetic acid adjusting pH value; Then at vacuum tightness 0.08～0.1MPa, concentrate or add the Virahol of 6-10 times of volume under 30 ℃～70 ℃ the condition, remove post precipitation again at vacuum tightness 0.08～0.1MPa, concentrate under 30 ℃～70 ℃ the condition, obtain the solid mixture of xanchromatic GlcNAc and ManNAc.
(15) ManNAc enrichment: the yellow solid with step (14) obtains, extracted 0.5～2 hour with the methyl alcohol immersion 12～36 hours of 0.5～3 times of volume or with methanol eddy, suction filtration obtains the pregnant solution of ManNAc with solid-liquid separation.
(16) concentrate ManNAc: with the pregnant solution that obtains in the step (15),, concentrate under 30 ℃～70 ℃ the condition, obtain the buttery material, be the ManNAc enriched substance, in-20 ℃ of refrigerators, preserve stand-by at vacuum tightness 0.08～0.1MPa.
(17) transformation experiment: the biological catalyst A of step (6) gained and the biological catalyst B of step (12) gained are mixed with the ManNAc enriched substance of substrate Sodium.alpha.-hydroxypropionate and step (16) gained; At 5 ℃～40 ℃, under pH 6.0～9.0 conditions, 180 rev/mins vibrated 5～50 hours, made substrate Sodium.alpha.-hydroxypropionate, ManNAc, biological catalyst A, biological catalyst B and air thorough mixing, finished conversion.
The concentration of substrate Sodium.alpha.-hydroxypropionate is 200～700mM in the above-mentioned reaction mixture; The concentration of ManNAc enriched substance is 40～100g/L; The concentration of biological catalyst A: wet cell 5～80g/L; The concentration of biological catalyst B: wet cell 1～10g/L.
(18) pre-treatment of conversion fluid: with the conversion fluid of step (17) gained, regulate pH to 4～5 with 732H type resin or glacial acetic acid, with 5,000～12,000 rev/min centrifugal 5～10 minutes, remove the biological catalyst A and the biological catalyst B that are added in the step (17), obtain supernatant liquor, be and contain sialic conversion fluid pretreatment fluid.
(19) plastic resin treatment: with one of HZ201 * 8 resins, 330 resins or 717 resins of selecting for use, wash pillar with the aqueous sodium hydroxide solution of the 1N～2N of 3～6 times of column volumes with 0.5～2 times of column volume flow velocity per hour, with deionized water ion exchange column is washed till neutrality then; Be formic acid type with 0.5～2 times of column volume flow velocity with ion exchange resin conversion with the aqueous formic acid of the 1N～3N of 3～6 times of volumes with resin again, with deionized water with resin wash to pH6～7, stand-by then.
(20) upper prop: the conversion fluid pretreatment fluid of step (18) gained is handled the ion exchange column of gained with step (19) on 0.5～2 times of column volume flow velocity, and whether have sialic acid spill, promptly stop to go up sample if spill if detecting in the effluent liquid in the upper prop process.
(21) wash-out: the ion exchange column that step (20) was handled, pillar washed with the deionized water of 2～4 times of column volumes with 0.5～2 times of column volume flow velocity per hour earlier; With the column volume of identical flow velocity with 1～4 times of the first wash-out of the aqueous formic acid of 0.5N～1N, the aqueous formic acid wash-out of usefulness is collected in the effusive sialic effluent liquid of component that contains in the aqueous formic acid elution process with 1N～3N again.
(22) concentrate: the effluent liquid with step (21) is collected at vacuum tightness 0.08～0.1MPa, concentrates 2～6 times under 25 ℃～50 ℃ the condition.
(23) glacial acetic acid precipitation: with adding volume ratio in the concentrated solution of step (22) gained is 4～10 times glacial acetic acid, leaves standstill crystallization 2～6 days under 4 ℃.
(24) the sialic acid crystal is collected: the magma that step (23) obtains is removed glacial acetic acid with method of pumping filtration, is 3～6 times glacial acetic acid washing crystal with volume ratio; With the crystal of gained, at 30 ℃～70 ℃, vacuum tightness is under the condition of 0.08～0.1MPa at last, dry 2～8 hours.
(25) sample detection:, use with the sialic acid powder of step (24) gained
13The purity of CNMR and HPLC testing product.
The preferred pseudomonas of bacterial classification (Pseudomonas sp.) ATCC11452 described in the above-mentioned steps (1).
The employed liquid nutrient medium of bacterial strain that relates in above-mentioned steps (2), (3), (4), (5) is liquid-based basal culture medium BLM.
Preferred 30～37 ℃ of yeast culture temperature described in above-mentioned steps (2), (3), (4), (5).
Preferred 15～30 hours of yeast culture time described in above-mentioned steps (2), (3), (4), (5).
DL type or L type Sodium.alpha.-hydroxypropionate concentration preferred 0.5～2% in above-mentioned steps (2), (3), (4), (5).
Colibacillus engineering strain described in the above-mentioned steps (7) is for containing the reorganization bacterium E.coli HB101 (pBV220-ALD) of acetylneuraminate aldolase (EC4.1.3.3) gene.
Preferred 30 ℃～40 ℃ of culture temperature in above-mentioned steps (8), (9), (10).
Cultivating the used substratum of intestinal bacteria in above-mentioned steps (9), (10) is liquid LB substratum, and concrete prescription is (mass/volume): peptone 1%; Yeast powder 0.5%; Sodium-chlor 1%; Sterilized 20 minutes for 121 ℃.
Preferred 30 ℃～40 ℃ of above-mentioned steps (11) mid-early stage culture temperature, the later stage is induced preferred 42 ℃～45 ℃ of the temperature of process.
The M9 substratum of the improvement described in the above-mentioned steps (11), concrete prescription by mass volume ratio is: peptone 1%; Yeast powder 0.5%; Na
2HPO
47H
2O 1.28%; KH
2PO
40.3%; NaCl 0.05%; NH
4Cl0.1%; CaCl
20.0011%; Glucose 0.4%; Sterilized 15 minutes for 115 ℃.
The penbritin that relates in the above-mentioned steps is prepared by sterile distilled water.
Biological catalyst A in the above-mentioned steps (17) is meant the intact cell of pseudomonas (Pseudomonas sp.) ATCC11452 that contains Lactate Oxidase; Biological catalyst B is meant the intact cell of the engineering strain E.coli HB101 (pBV220-ALD) that contains acetylneuraminate aldolase.
The concentration of biological catalyst A in the above-mentioned steps (17): wet cell 15～60g/L; The concentration of biological catalyst B: wet cell 3～7g/L.
Preferred 400～the 500mM of concentration of the substrate Sodium.alpha.-hydroxypropionate in the above-mentioned steps (17).
Preferred 15 ℃～35 ℃ of conversion reaction temperature in the above-mentioned steps (17).
Conversion reaction pH preferred 6.5～8.5 in the above-mentioned steps (17).
The preferred HZ201 of resin * 8 of selecting for use in the above-mentioned steps (19).
In the above-mentioned steps (25), relate to
13CNMR is analyzed by the FX-90Q nuclear magnetic resonance analyser, and solvent is a heavy water.
In the above-mentioned steps (25), the HPLC method that relates to adopts the Agilentl100 instrument, and chromatographic column is a Prontosil120-3-AMINO post (150 * 3.0mm), 0.5mM sulfuric acid is moving phase, flow velocity 0.5mL/min detects down with UV-detector 205nm, and column temperature is 30 ℃.
The present invention is that a kind of utilization contains the intact cell of Lactate Oxidase and the full cell of E.coli that contains acetylneuraminate aldolase as the biological catalyst sialic acid synthetase, and utilizes HZ201 * sialic method of 8 ion exchange resin separation and purification.
The acinetobacter calcoaceticus that the present invention relates to (Acinetobacter sp.) ATCC11171, pseudomonas (Pseudomonas sp.) ATCC11452, have D type Lactate Oxidase (D-LOD) and L type Lactate Oxidase (L-LOD) activity simultaneously, and the process of this enzyme catalysis lactic acid generation pyruvic acid does not produce hydrogen peroxide.
What the present invention relates to can be represented with following chemical equation through the transforming principle that the multistep coupling transforms preparation high value sialic acid method by cheap sodium lactate:
The present invention has following characteristics:
(1) transforms the production sialic acid with thalline that contains Lactate Oxidase and the thalline that contains acetylneuraminate aldolase as the catalyzer coupling.
(2) can produce sialic acid from more cheap substrate Sodium.alpha.-hydroxypropionate.
(3), thereby eliminate the substrate restraining effect of pyruvic acid to Lactate Oxidase simultaneously because the further consumption of pyruvic acid in sialic acid synthetic process has reduced the accumulation of pyruvic acid.
(4) contain that the substratum of Lactate Oxidase bacterial strain requirement is simple, cost is low.
(5) can transform DL-lactic acid or L-lactic acid, generate pyruvic acid, the substrate cost is low.
(6) the cell permeability of this bacterial strain is good, does not need fragmentation, can directly transform with intact cell, and is easy to operate.
(7) biological catalyst can be removed with filtration method or centrifuging, and it is cheap that later separation is extracted expense.
(4) description of drawings
The HPLC collection of illustrative plates of Fig. 1 standard substance.
Wherein, the 1.817min place is the peak of GlcNAc and ManNAc; 4.562min locate peak into Neu5Ac; 7.091min locate to be the pyruvic acid peak.
Fig. 2 Neu5Ac crystalline HPLC collection of illustrative plates.
(5) embodiment
Embodiment 1: contain the cultivation of Lactate Oxidase bacterial strain
1, the cultivation of pseudomonas (Pseudomonas sp.) ATCC11452
(1) Lactate Oxidase bacterial classification: select pseudomonas (Pseudomonas sp.) ATCC11452;
(2) slant culture: pseudomonas (Pseudomonas sp.) ATCC11452 is inoculated in that to contain mass volume ratio be 1.5% agar and is added with on the solid inclined-plane minimum medium that mass volume ratio is 1% L type Sodium.alpha.-hydroxypropionate, cultivated 20 hours for 30 ℃;
(3) first order seed is cultivated: with the bacterial strain of step (2) cultivation, encircle with inoculation articulating 1 under aseptic condition that to contain mass volume ratio in 30mL be among 1% the L type Sodium.alpha.-hydroxypropionate liquid-based basal culture medium BLM, under 30 ℃ of conditions, shaking culture is 10 hours on shaking table, makes first order seed;
(4) enlarged culturing: with the inoculum size of 5% volume ratio, connecing first order seed, to contain mass volume ratio in 500mL be that under 30 ℃ of conditions, shaking culture is 16 hours on shaking table, makes secondary seed among 2% the L type Sodium.alpha.-hydroxypropionate BLM;
(5) fermentor cultivation: with the inoculum size of 5% volume ratio, connecing secondary seed contains among the BLM that mass volume ratio is 2% L type Sodium.alpha.-hydroxypropionate in 8L, under 30 ℃ of conditions, cultivated 16 hours, be that DNP and pyruvic acid effect generate red-brown 2 with 2,4 dinitrophenyl hydrazine during this time, the method for 4-dinitrophenylhydrazone detects the enzyme of cell Lactate Oxidase and lives, when enzyme work reaches every milliliter of nutrient solution 1.2U, stop fermentation culture;
Above-mentioned liquid-based basal culture medium BLM, concrete prescription by mass volume ratio is:
KH
2PO
40.1%, K
2HPO
43H
2O 0.08%, NH
4Cl 0.1%, MgSO
47H
2O 0.05%, CaCl
22H
2O0.005%, yeast powder 0.1%, metal ion mixed solution 0.12%; Regulate under 7.0,115 ℃ of conditions of pH and sterilized 20 minutes;
The prescription of metal ion mixed solution following (g/L):
Na
2EDTA，50；ZnSO
4·7H
2O，20；MnCl
2·4H
2O，5；(NH
4)
6Mo
7O
24·4H
2O，1，；FeSO
4·7H
2O，5；CuSO
4·5H
2O，1.5；CoCl
2·H
2O，1.6；CaCl
2·2H
2O，5.5；
(6) collect thalline: the fermented liquid 5 of getting step (5), under 000 rev/min of condition centrifugal 8 minutes, and be 0.85% sodium chloride aqueous solution washing 2 times with mass volume ratio, with identical centrifugal condition, the collecting precipitation thalline obtains wet thallus 166 gram, is biological catalyst A with the thalline of gained, 4 ℃ of storages, standby.
2, the cultivation of acinetobacter calcoaceticus (Acinetobacter sp.) ATCC11171
(1) Lactate Oxidase bacterial classification: select acinetobacter calcoaceticus (Acinetobacter sp.) ATCC11171;
(2) slant culture: acinetobacter calcoaceticus (Acinetobacter sp.) ATCC11171 is inoculated in that to contain mass volume ratio be 1.5% agar and is added with on the solid inclined-plane minimum medium that mass volume ratio is 1% L type Sodium.alpha.-hydroxypropionate, cultivated 20 hours for 30 ℃;
(3) first order seed is cultivated: with the bacterial strain of step (2) cultivation, encircle with inoculation articulating 2 under aseptic condition that to contain mass volume ratio in 30mL be among 1% the L type Sodium.alpha.-hydroxypropionate liquid-based basal culture medium BLM, under 30 ℃ of conditions, shaking culture is 10 hours on shaking table, makes first order seed;
(4) enlarged culturing: with the inoculum size of 5% volume ratio, connecing first order seed, to contain mass volume ratio in 500mL be that under 30 ℃ of conditions, shaking culture is 16 hours on shaking table, makes secondary seed among 2% the L type Sodium.alpha.-hydroxypropionate BLM;
(5) fermentor cultivation: with the inoculum size of 5% volume ratio, connecing secondary seed contains among the BLM that mass volume ratio is 2% L type Sodium.alpha.-hydroxypropionate in 8L, under 30 ℃ of conditions, cultivated 16 hours, be that DNP and pyruvic acid effect generate red-brown 2 with 2,4 dinitrophenyl hydrazine during this time, the method for 4-dinitrophenylhydrazone detects the enzyme of cell Lactate Oxidase and lives, reach every milliliter of nutrient solution during high 0.53U to enzyme work, stop fermentation culture;
Above-mentioned liquid-based basal culture medium BLM, concrete prescription by mass volume ratio is:
KH
2PO
40.1%, K
2HPO
43H
2O 0.08%, NH
4Cl 0.1%, MgSO
47H
2O 0.05%, CaCl
22H
2O0.005%, yeast powder 0.1%, metal ion mixed solution 0.12%; Regulate under 7.0,115 ℃ of conditions of pH and sterilized 20 minutes;
The prescription of metal ion mixed solution following (g/L):
Na
2EDTA，50；ZnSO
4·7H
2O，20；MnCl
2·4H
2O，5；(NH
4)
6Mo
7O
24·4H
2O，1，；FeSO
4·7H
2O，5；CuSO
4·5H
2O，1.5；CoCl
2·H
2O，1.6；CaCl
2·2H
2O，5.5；
Collect thalline: the fermented liquid 5 of getting step (5), under 000 rev/min of condition centrifugal 8 minutes, and be 0.85% sodium chloride aqueous solution washing 2 times with mass volume ratio, with identical centrifugal condition, the collecting precipitation thalline obtains wet thallus 157.6 gram, is biological catalyst A with the thalline of gained, 4 ℃ of storages, standby.
Embodiment 2: the structure of engineering strain intestinal bacteria E.coli HB101 (pBV220-ALD)
The structure of acetylneuraminate aldolase bacterial strain: the method structure colibacillus engineering strain with routine is E.coli HB101 (pBV220-ALD):
The structure of recombinant strain: adopt conventional method to prepare the genomic dna of E.coli K12 bacterial strain, the method that this process can prepare with reference to a small amount of of bacterial genomes in " the fine works molecular biology guide " of Science Press's publication, the genomic dna of extraction E.coli K12 bacterial strain; Use synthetic primer pcr amplification from the genomic dna of E.coli K12 bacterial strain to obtain the acetylneuraminate aldolase gene; Use EcoR I, Pst I double digestion plasmid pBV220, be connected with the acetylneuraminate aldolase gene that amplification obtains then, obtain recombinant plasmid pBV220-ALD; Again recombinant plasmid pBV220-ALD is imported carrier E.coli HB101 through transforming, obtain engineering strain E.coli HB101 (pBV220-ALD);
Wherein the host is that E.coli HB101 is available from Research for Industrial Microbial Germ preservation center, Beijing; Acetylneuraminate aldolase (EC4.1.3.3) gene is obtained by pcr amplification in the genomic dna at E.coli K12 bacterial strain (available from Research for Industrial Microbial Germ preservation center, Beijing); Plasmid is pBV220 (available from Research for Industrial Microbial Germ preservation center, Beijing); Primer synthesizes in Shanghai gives birth to worker Bioisystech Co., Ltd, and the primer of 5 ' end is AGGAATTCATGGCAACGAATTTAC, adds the site of an EcoR I; The primer of 3 ' end is TCCTGCAGTCACCCGCGCTCTT, adds the site of a Pst I.
Embodiment 3: the cultivation of engineering strain intestinal bacteria E.coli HB101 (pBV220-ALD)
(1) the dull and stereotyped cultivation: engineering strain intestinal bacteria E.coli HB101 (pBV220-ALD) is scoring to contains on the penbritin LB flat board that contains 100 μ g/mL that mass volume ratio is 1.5% agar, cultivated 12 hours for 30 ℃;
(2) first order seed: under aseptic condition,, be inoculated in the liquid nutrient medium that contains 100 μ g/mL penbritins of 5mL 30 ℃ of shaking table shaking culture 12 hours then with a single bacterium colony on aseptic toothpick picking step (1) flat board;
(3) secondary seed: under aseptic condition, getting nutrient solution that step (2) cultivated is 2% inoculum size with volume ratio, is inoculated into 240mL and contains in the LB liquid nutrient medium of penbritin of 100 μ g/mL, 30 ℃ of shaking table shaking culture 6 hours;
(4) fermentor cultivation: under aseptic condition, the nutrient solution of getting step (3) gained is the M9 liquid nutrient medium of the improvement of 8% inoculum size inoculation 3L with volume ratio, cultivates 7 hours for 30 ℃, changes temperature and be 42 ℃ to cultivate 4 hours;
The M9 liquid nutrient medium of the improvement described in the above-mentioned steps (4), concrete prescription by mass volume ratio is: peptone 1%; Yeast powder 0.5%; Na
2HPO
47H
2O 1.28%; KH
2PO
40.3%; NaCl0.05%; NH
4Cl 0.1%; CaCl
20.0011%; Glucose 0.4%; Sterilized 15 minutes for 115 ℃.
(5) collect thalline: it is centrifugal 15 minutes that step (4) is cultivated 5,000 rev/mins of cultures that obtain; And be 0.85% sodium chloride aqueous solution washing thalline 2 times with mass volume ratio, with identical centrifugal condition, the collecting precipitation thalline obtains wet thallus 17.5 grams; Thalline is placed-20 ℃ refrigerator and cooled freeze preservation, promptly obtain biological catalyst B, stand-by.
The preparation of embodiment 4:N-kharophen seminose
(1) N-kharophen seminose is the isomerization of ManNAc: the N-acetylglucosamine of getting 200g be the dissolution of sodium hydroxide of GlcNAc and 4.4g in 2L water, then under the condition of room temperature, isomerization reaction 48 hours;
(2) concentrate: it is 6 that the isomerization solution of step (1) gained is regulated the pH value with glacial acetic acid; At vacuum tightness 0.95MPa, concentrate under 60 ℃ the condition then, obtain the solid mixture of xanchromatic GlcNAc and ManNAc;
(3) ManNAc enrichment: with the yellow solid that step (2) obtains, the methyl alcohol that is 500ml with 1 times of volume soaked 24 hours, and suction filtration obtains the pregnant solution of ManNAc with solid-liquid separation;
(4) concentrate ManNAc: with the pregnant solution that obtains in the step (3),, concentrate under 60 ℃ the condition, obtain the buttery material, be the ManNAc enriched substance, be weighed as 83.44 grams, in-20 ℃ of refrigerators, preserve stand-by at vacuum tightness 0.95MPa.
The preparation of embodiment 5:N-n acetylneuraminic acid n (Neu5Ac)
(1) transformation experiment: the biological catalyst A that the Lactate Oxidase vigor of gained is high is that wet cell 3 grams (being that concentration is 30 grams per liters) of pseudomonas (Pseudomonassp.) ATCCll452 and biological catalyst B 0.7 gram (being that concentration is 7 grams per liters) of gained mix with ManNAc enriched substance 5 grams (being that concentration is 50 grams per liters) of substrate Sodium.alpha.-hydroxypropionate 5.6 grams (being that concentration is 500mM) and gained, with the distilled water constant volume to 100ml, in the triangular flask of the 300ml that packs into; At 30 ℃, under pH 7.5 (regulating the pH value with the method that the adds acetate) condition, 180 rev/mins vibrated 48 hours, made substrate Sodium.alpha.-hydroxypropionate, ManNAc, biological catalyst A, biological catalyst B and air thorough mixing, finished conversion.
(2) pre-treatment of conversion fluid:, regulate pH to 4 with glacial acetic acid, with 12 with the conversion fluid of step (1) gained, 000 rev/min centrifugal 5 minutes, remove the biological catalyst A and the biological catalyst B that are added in the step (1), obtain supernatant liquor, be and contain sialic conversion fluid pretreatment fluid.
(3) plastic resin treatment: with 20ml HZ201 * 8 resins (Shanghai China shake resin company limited), wash pillar with 20ml/ hour flow velocity, with deionized water ion exchange column is washed till neutrality then with the aqueous sodium hydroxide solution of the 2N of 60ml; Be formic acid type with 20ml/ hour flow velocity with ion exchange resin conversion with the aqueous formic acid of the 2N of 60ml with resin again, with deionized water with resin wash to pH6, stand-by then.
(4) upper prop: the ion exchange column of the conversion fluid pretreatment fluid of step (2) gained being handled gained with step (3) on 12ml/ hour the flow velocity.
(5) wash-out: the ion exchange column that step (4) was handled, earlier with the deionized water of 60ml volume flow velocity flushing pillar with 60ml/ hour; With the aqueous formic acid elder generation wash-out 60ml column volume of identical flow velocity, with the aqueous formic acid wash-out of identical flow velocity, be collected in the effusive sialic effluent liquid of component that contains in the aqueous formic acid elution process with 1N again with 1N with 0.5N.
(6) concentrate: the effluent liquid with step (5) is collected at vacuum tightness 0.095MPa, concentrates 6 times under 40 ℃ the condition.
(7) glacial acetic acid precipitation: with adding volume ratio in the concentrated solution of step (6) gained is 5 times glacial acetic acid, leaves standstill crystallization 2 days under 4 ℃.
(8) the sialic acid crystal is collected: the magma that step (7) obtains is removed glacial acetic acid with method of pumping filtration, is 5 times glacial acetic acid washing crystal with volume ratio; With the crystal of gained, at 50 ℃, vacuum tightness is under the condition of 0.095MPa at last, dry 4 hours.
(9) sample detection:, be 98% with the purity of HPLC testing product with sialic acid powder 1 gram of step (8) gained.
The preparation of embodiment 6:N-n acetylneuraminic acid n (Neu5Ac)
(1) transformation experiment: the biological catalyst A that the Lactate Oxidase vigor of gained is high is that wet cell 3 grams (being that concentration is 30 grams per liters) of pseudomonas (Pseudomonassp.) ATCCll452 and biological catalyst B 0.7 gram (being that concentration is 7 grams per liters) of gained mix with ManNAc enriched substance 5 grams (being that concentration is 50 grams per liters) of substrate Sodium.alpha.-hydroxypropionate 5.6 grams (being that concentration is 500mM) and gained, with the distilled water constant volume to 100ml, in the triangular flask of the 300ml that packs into; At 30 ℃, under pH7.5 (regulating the pH value with the method that the adds acetate) condition, 180 rev/mins vibrated 48 hours, made substrate Sodium.alpha.-hydroxypropionate, ManNAc, biological catalyst A, biological catalyst B and air thorough mixing, finished conversion.
(2) pre-treatment of conversion fluid:, regulate pH to 4 with glacial acetic acid, with 12 with the conversion fluid of step (1) gained, 000 rev/min centrifugal 5 minutes, remove the biological catalyst A and the biological catalyst B that are added in the step (1), obtain supernatant liquor, be and contain sialic conversion fluid pretreatment fluid.
(3) plastic resin treatment: with anti-717 resins (the anti-resin processing plant in Shandong, Jining, Shandong) in 20ml Shandong, wash pillar with 20ml/ hour flow velocity, with deionized water ion exchange column is washed till neutrality then with the aqueous sodium hydroxide solution of the 2N of 60ml; Be formic acid type with 20ml/ hour flow velocity with ion exchange resin conversion with the aqueous formic acid of the 2N of 60ml with resin again, with deionized water with resin wash to pH6, stand-by then.
(4) upper prop: the ion exchange column of the conversion fluid pretreatment fluid of step (2) gained being handled gained with step (3) on 12ml/ hour the flow velocity.
(5) wash-out: the ion exchange column that step (4) was handled, earlier with the deionized water of 60ml volume flow velocity flushing pillar with 60ml/ hour; With the aqueous formic acid elder generation wash-out 60ml column volume of identical flow velocity, with the aqueous formic acid wash-out of identical flow velocity, be collected in the effusive sialic effluent liquid of component that contains in the aqueous formic acid elution process with 1N again with 1N with 0.5N.
(6) concentrate: the effluent liquid with step (5) is collected at vacuum tightness 0.095MPa, concentrates 6 times under 40 ℃ the condition.
(7) glacial acetic acid precipitation: with adding volume ratio in the concentrated solution of step (6) gained is 7 times glacial acetic acid, leaves standstill crystallization 5 days under 4 ℃.
(8) the sialic acid crystal is collected: the magma that step (7) obtains is removed glacial acetic acid with method of pumping filtration, is 5 times glacial acetic acid washing crystal with volume ratio; With the crystal of gained, at 50 ℃, vacuum tightness is under the condition of 0.095MPa at last, dry 6 hours.
(9) sample detection:, be 94% with the purity of HPLC testing product with sialic acid powder 0.6 gram of step (8) gained.
The preparation of embodiment 6:N-n acetylneuraminic acid n (Neu5Ac)
(1) transformation experiment: the biological catalyst A that the Lactate Oxidase vigor of gained is high is that wet cell 12 grams (being that concentration is 12 grams per liters) of pseudomonas (Pseudomonassp.) ATCCll452 and biological catalyst B 3.5 grams (being that concentration is 3.5 grams per liters) of gained mix with ManNAc enriched substance 20 grams (being that concentration is 20 grams per liters) of substrate Sodium.alpha.-hydroxypropionate 22.5 grams (being that concentration is 200mM) and gained, with the distilled water constant volume to 1000ml, in the triangular flask of the 5000ml that packs into; At 30 ℃, under pH7 (regulating the pH value with the method that the adds acetate) condition, 180 rev/mins vibrated 48 hours, made substrate Sodium.alpha.-hydroxypropionate, ManNAc, biological catalyst A, biological catalyst B and air thorough mixing, finished conversion.
(2) pre-treatment of conversion fluid:, regulate pH to 4 with glacial acetic acid, with 12 with the conversion fluid of step (1) gained, 000 rev/min centrifugal 5 minutes, remove the biological catalyst A and the biological catalyst B that are added in the step (1), obtain supernatant liquor, be and contain sialic conversion fluid pretreatment fluid.
(3) plastic resin treatment: with 200ml HZ201 * 8 resins (Shanghai China shake resin company limited), wash pillar with 200ml/ hour flow velocity, with deionized water ion exchange column is washed till neutrality then with the aqueous sodium hydroxide solution of the 2N of 600ml; Be formic acid type with 200ml/ hour flow velocity with ion exchange resin conversion with the aqueous formic acid of the 2N of 600ml with resin again, with deionized water with resin wash to pH6, stand-by then.
(4) upper prop: the ion exchange column of the conversion fluid pretreatment fluid of step (2) gained being handled gained with step (3) on 120ml/ hour the flow velocity.
(5) wash-out: the ion exchange column that step (4) was handled, earlier with the deionized water of 600ml volume flow velocity flushing pillar with 600ml/ hour; With the aqueous formic acid elder generation wash-out 600ml column volume of identical flow velocity, with the aqueous formic acid wash-out of identical flow velocity, be collected in the effusive sialic effluent liquid of component that contains in the aqueous formic acid elution process with 1N again with 1N with 0.5N.
(6) concentrate: the effluent liquid with step (5) is collected at vacuum tightness 0.095MPa, concentrates 3 times under 40 ℃ the condition.
(7) glacial acetic acid precipitation: with adding volume ratio in the concentrated solution of step (6) gained is 8 times glacial acetic acid, leaves standstill crystallization 3 days under 4 ℃.
(8) the sialic acid crystal is collected: the magma that step (7) obtains is removed glacial acetic acid with method of pumping filtration, is 5 times glacial acetic acid washing crystal with volume ratio; With the crystal of gained, at 50 ℃, vacuum tightness is under the condition of 0.095MPa at last, dry 2 hours.
(9) sample detection:, be 97.2% with the purity of HPLC testing product with sialic acid powder 6 gram of step (8) gained.The preparation of embodiment 7:N-n acetylneuraminic acid n (Neu5Ac)
(1) transformation experiment: the biological catalyst A that the Lactate Oxidase vigor of gained is high is that wet cell 60 grams (being that concentration is 30 grams per liters) of pseudomonas (Pseudomonassp.) ATCCll452 and biological catalyst B 15 grams (being that concentration is 7.5 grams per liters) of gained mix with ManNAc enriched substance 100 grams (being that concentration is 50 grams per liters) of substrate Sodium.alpha.-hydroxypropionate 122 grams (being that concentration is 544mM) and gained, with the distilled water constant volume to 2000ml, in 5 liters the bright fermentor tank of shellfish of packing into; At 30 ℃, under pH7.5 (the regulating the pH value) condition,, make substrate Sodium.alpha.-hydroxypropionate, ManNAc, biological catalyst A, biological catalyst B and air thorough mixing with the stirring velocity of 400rpm with the method that adds acetate, finish conversion after 48 hours.
(2) pre-treatment of conversion fluid:, regulate pH to 4 with glacial acetic acid, with 12 with the conversion fluid of step (1) gained, 000 rev/min centrifugal 5 minutes, remove the biological catalyst A and the biological catalyst B that are added in the step (1), obtain supernatant liquor, be and contain sialic conversion fluid pretreatment fluid.
(3) plastic resin treatment: with 400ml HZ201 * 8 resins (Shanghai China shake resin company limited), wash pillar with 400ml/ hour flow velocity, with deionized water ion exchange column is washed till neutrality then with the aqueous sodium hydroxide solution of the 2N of 1200ml; Be formic acid type with 400ml/ hour flow velocity with ion exchange resin conversion with the aqueous formic acid of the 2N of 1200ml with resin again, with deionized water with resin wash to pH6, stand-by then.
(4) upper prop: the ion exchange column of the conversion fluid pretreatment fluid of step (2) gained being handled gained with step (3) on 240ml/ hour the flow velocity.
(5) wash-out: the ion exchange column that step (4) was handled, earlier with the deionized water of 1200ml volume flow velocity flushing pillar with 1200ml/ hour; With the aqueous formic acid elder generation wash-out 1200ml column volume of identical flow velocity, with the aqueous formic acid wash-out of identical flow velocity, be collected in the effusive sialic effluent liquid of component that contains in the aqueous formic acid elution process with 1N again with 1N with 0.5N.
(6) concentrate: the effluent liquid with step (5) is collected at vacuum tightness 0.095MPa, concentrates 6 times under 40 ℃ the condition.
(7) glacial acetic acid precipitation: with adding volume ratio in the concentrated solution of step (6) gained is 5 times glacial acetic acid, leaves standstill crystallization 2 days under 4 ℃.
(8) the sialic acid crystal is collected: the magma that step (7) obtains is removed glacial acetic acid with method of pumping filtration, is 5 times glacial acetic acid washing crystal with volume ratio; With the crystal of gained, at 50 ℃, vacuum tightness is under the condition of 0.095MPa at last, dry 4 hours.
(9) sample detection:, be 95% with the purity of HPLC testing product with sialic acid powder 11.5 gram of step (8) gained.
The preparation of embodiment 8:N-n acetylneuraminic acid n (Neu5Ac)
(1) transformation experiment: the biological catalyst A that the Lactate Oxidase vigor of gained is high is that wet cell 12 grams (being that concentration is 24 grams per liters) of pseudomonas (Pseudomonassp.) ATCCll452 and biological catalyst B 1.75 grams (being that concentration is 3.5 grams per liters) of gained mix with ManNAc enriched substance 20 grams (being that concentration is 40 grams per liters) of substrate Sodium.alpha.-hydroxypropionate 20 grams (being that concentration is 357mM) and gained, with the distilled water constant volume to 500ml, in the triangular flask of the 3000ml that packs into; At 30 ℃, under pH7.5 (regulating the pH value with the method that the adds acetate) condition, 180 rev/mins vibrated 48 hours, made substrate Sodium.alpha.-hydroxypropionate, ManNAc, biological catalyst A, biological catalyst B and air thorough mixing, finished conversion.
(2) pre-treatment of conversion fluid:, regulate pH to 4 with glacial acetic acid, with 12 with the conversion fluid of step (1) gained, 000 rev/min centrifugal 5 minutes, remove the biological catalyst A and the biological catalyst B that are added in the step (1), obtain supernatant liquor, be and contain sialic conversion fluid pretreatment fluid.
(3) plastic resin treatment: with 100ml HZ201 * 8 resins (Shanghai China shake resin company limited), wash pillar with 100ml/ hour flow velocity, with deionized water ion exchange column is washed till neutrality then with the aqueous sodium hydroxide solution of the 2N of 300ml; Be formic acid type with 100ml/ hour flow velocity with ion exchange resin conversion with the aqueous formic acid of the 2N of 300ml with resin again, with deionized water with resin wash to pH6, stand-by then.
(4) upper prop: the ion exchange column of the conversion fluid pretreatment fluid of step (2) gained being handled gained with step (3) on 60ml/ hour the flow velocity.
(5) wash-out: the ion exchange column that step (4) was handled, earlier with the deionized water of 300ml volume flow velocity flushing pillar with 60ml/ hour; With the aqueous formic acid elder generation wash-out 300ml column volume of identical flow velocity, with the aqueous formic acid wash-out of identical flow velocity, be collected in the effusive sialic effluent liquid of component that contains in the aqueous formic acid elution process with 1N again with 1N with 0.5N.
(6) concentrate: the effluent liquid with step (5) is collected at vacuum tightness 0.095MPa, concentrates 6 times under 40 ℃ the condition.
(7) glacial acetic acid precipitation: with adding volume ratio in the concentrated solution of step (6) gained is 5 times glacial acetic acid, leaves standstill crystallization 2 days under 4 ℃.
(8) the sialic acid crystal is collected: the magma that step (7) obtains is removed glacial acetic acid with method of pumping filtration, is 5 times glacial acetic acid washing crystal with volume ratio; With the crystal of gained, at 50 ℃, vacuum tightness is under the condition of 0.095MPa at last, dry 4 hours.
Sample detection:, be 96.4% with the purity of HPLC testing product with sialic acid powder 3.88 gram of step (8) gained.
The preparation of embodiment 9:N-n acetylneuraminic acid n (Neu5Ac)
(1) transformation experiment: the biological catalyst A that the Lactate Oxidase vigor of gained is high is that wet cell 30 grams (being that concentration is 60 grams per liters) of pseudomonas (Pseudomonassp.) ATCCll452 and biological catalyst B 2.5 grams (being that concentration is 5 grams per liters) of gained mix with ManNAc enriched substance 20 grams (being that concentration is 40 grams per liters) of substrate Sodium.alpha.-hydroxypropionate 25 grams (being that concentration is 446mM) and gained, with the distilled water constant volume to 500ml, in the triangular flask of the 3000ml that packs into; At 30 ℃, under pH7 (regulating the pH value with the method that the adds acetate) condition, 180 rev/mins vibrated 48 hours, made substrate Sodium.alpha.-hydroxypropionate, ManNAc, biological catalyst A, biological catalyst B and air thorough mixing, finished conversion.
(2) pre-treatment of conversion fluid:, regulate pH to 4 with glacial acetic acid, with 12 with the conversion fluid of step (1) gained, 000 rev/min centrifugal 5 minutes, remove the biological catalyst A and the biological catalyst B that are added in the step (1), obtain supernatant liquor, be and contain sialic conversion fluid pretreatment fluid.
(3) plastic resin treatment: with 100ml HZ201 * 8 resins (Shanghai China shake resin company limited), wash pillar with 100ml/ hour flow velocity, with deionized water ion exchange column is washed till neutrality then with the aqueous sodium hydroxide solution of the 2N of 300ml; Be formic acid type with 100ml/ hour flow velocity with ion exchange resin conversion with the aqueous formic acid of the 2N of 300ml with resin again, with deionized water with resin wash to pH6, stand-by then.
(4) upper prop: the ion exchange column of the conversion fluid pretreatment fluid of step (2) gained being handled gained with step (3) on 60ml/ hour the flow velocity.
(5) wash-out: the ion exchange column that step (4) was handled, earlier with the deionized water of 300ml volume flow velocity flushing pillar with 300ml/ hour; With the aqueous formic acid elder generation wash-out 300ml column volume of identical flow velocity, with the aqueous formic acid wash-out of identical flow velocity, be collected in the effusive sialic effluent liquid of component that contains in the aqueous formic acid elution process with 1N again with 1N with 0.5N.
(6) concentrate: the effluent liquid with step (5) is collected at vacuum tightness 0.095MPa, concentrates 6 times under 40 ℃ the condition.
(7) glacial acetic acid precipitation: with adding volume ratio in the concentrated solution of step (6) gained is 5 times glacial acetic acid, leaves standstill crystallization 2 days under 4 ℃.
(8) the sialic acid crystal is collected: the magma that step (7) obtains is removed glacial acetic acid with method of pumping filtration, is 5 times glacial acetic acid washing crystal with volume ratio; With the crystal of gained, at 50 ℃, vacuum tightness is under the condition of 0.095MPa at last, dry 4 hours.
Sample detection:, be 98.5% with the purity of HPLC testing product with sialic acid powder 3.94 gram of step (8) gained.The HPLC collection of illustrative plates of this sample is seen Fig. 2, and the peak of retention time 4.532 promptly is sialic peak.
Claims (10)
1. one kind prepares the sialic method of high value by cheap sodium lactate through multistep coupling bio-transformation, and its sequence of steps is as follows:
(1) Lactate Oxidase bacterial classification: select one of acinetobacter calcoaceticus (Acinetobacter sp.) ATCC11171, pseudomonas (Pseudomonas sp.) ATCC11452;
(2) slant culture: above-mentioned bacterial strains is inoculated in that to contain mass volume ratio be 1.5～2.0% agar and is added with on the solid inclined-plane minimum medium that mass volume ratio is 0.2～3% DL type or L type Sodium.alpha.-hydroxypropionate, cultivated 15～30 hours for 25 ℃～45 ℃;
(3) first order seed is cultivated: with the bacterial strain of step (2) cultivation, encircle with inoculation articulating 1～2 under aseptic condition that to contain mass volume ratio in 20～100mL be in 0.2～3% the DL type or L type Sodium.alpha.-hydroxypropionate liquid-based basal culture medium BLM, under 25 ℃～45 ℃ conditions, shaking culture is 10～30 hours on shaking table, makes first order seed;
(4) enlarged culturing: with the inoculum size of 5% volume ratio, connecing first order seed contains in the DL type or L type Sodium.alpha.-hydroxypropionate BLM that mass volume ratio is 0.2-3% in 300～1000mL, under 25 ℃～45 ℃ conditions, shaking culture is 10～30 hours on shaking table, makes secondary seed;
(5) fermentor cultivation: with the inoculum size of 5% volume ratio, connecing secondary seed contains among the BLM that mass volume ratio is 0.2～3% DL type or L type Sodium.alpha.-hydroxypropionate in 1.8～8L, under 25 ℃～45 ℃ conditions, cultivated 15～40 hours, be that DNP and pyruvic acid effect generate red-brown 2 with 2,4 dinitrophenyl hydrazine during this time, the method for 4-dinitrophenylhydrazone detects cellular enzymes and lives, when enzyme work reaches 0.9～2.0U/ml, stop fermentation culture;
Above-mentioned liquid-based basal culture medium BLM, concrete prescription by mass volume ratio is:
KH
2PO
40.1%, K
2HPO
43H
2O 0.08%, NH
4Cl 0.1%, MgSO
47H
2O 0.05%, CaCl
22H
2O 0.005%, yeast powder 0.1%, metal ion mixed solution 0.12%; Regulate pH7.0, sterilization is 20 minutes under 115 ℃ of conditions;
The prescription of metal ion mixed solution following (g/L):
Na
2EDTA，50；ZnSO
4·7H
2O，20；MnCl
2·4H
2O，5；(NH
4)
6Mo
7O
24·4H
2O，1，；FeSO
4·7H
2O，5；CuSO
4·5H
2O，1.5；CoCl
2·H
2O，1.6；CaCl
2·2H
2O，5.5；
(6) collect thalline: got under 5,000 rev/mins of conditions of fermented liquid of step (5) centrifugal 5～8 minutes, and with physiological saline washing 2～3 times, with identical centrifugal condition, the collecting precipitation thalline is biological catalyst A with the thalline of gained, and is 4 ℃ of storages, standby;
(7) structure of acetylneuraminate aldolase bacterial strain: the method structure colibacillus engineering strain with routine is E.coliHB101 (pBV220-ALD);
Wherein the host is E.coli HB101; Acetylneuraminate aldolase (EC4.1.3.3) gene is obtained by pcr amplification in the genomic dna of E.coli K12 bacterial strain; Plasmid is pBV220; The primer of 5 ' end is AGGAATTCATGGCAACGAATTTAC, adds the site of an EcoR I; The primer of 3 ' end is TCCTGCAGTCACCCGCGCTCTT, adds the site of a Pst I;
(8) the dull and stereotyped cultivation: the bacterial strain of step (7) gained is scoring to contains on the penbritin LB flat board that contains 100 μ g/mL that mass volume ratio is 1.5% agar;
(9) first order seed: under aseptic condition,, be inoculated in the liquid nutrient medium that contains 100 μ g/mL penbritins of 5 mL 25 ℃～40 ℃ shaking table shaking culture 10～12 hours then with a single bacterium colony on aseptic toothpick picking step (8) flat board;
(10) secondary seed: under aseptic condition, get nutrient solution that step (9) cultivated and be 2% inoculum size with volume ratio, be inoculated into 30mL～500mL and contain in the LB liquid nutrient medium of penbritin of 100 μ g/mL, 25 ℃～40 ℃ shaking table shaking culture 5～10 hours;
(11) fermentor cultivation: under aseptic condition, the nutrient solution of getting step (10) gained is the M9 liquid nutrient medium of the improvement of inoculum size inoculation 2L～10L of 8% with volume ratio, cultivated 5～12 hours for 25 ℃～40 ℃, changing temperature is 42 ℃～50 ℃ cultivations 3～7 hours;
The M9 liquid nutrient medium of above-mentioned improvement, concrete prescription by mass volume ratio is:
Peptone 0.5%～2%; Yeast powder 0.25%～0.6%; Na
2HPO
47H
2O 0.5%～2%; KH
2PO
40.1%～0.5%; NaCl 0.02%～0.1%; NH
4Cl 0.05%～0.2%; CaCl
20.0011%; Glucose 0.2%～2%; Sterilized 15 minutes for 115 ℃;
(12) collect thalline: it is centrifugal 5～30 minutes that step (11) is cultivated 5,000 rev/mins of cultures that obtain; And be 0.85% sodium chloride aqueous solution washing thalline 1～3 time with mass volume ratio, with identical centrifugal condition, the collecting precipitation thalline; Place 0 ℃～-30 ℃ refrigerator and cooled to freeze preservation thalline, promptly obtain biological catalyst B, stand-by;
(13) N-kharophen seminose is the isomerization of ManNAc: the N-acetylglucosamine of getting 100～400g be the dissolution of sodium hydroxide of GlcNAc and 2.2～8.8g in 1～4L water, then under the condition of room temperature, isomerization reaction 36～96 hours;
(14) concentrate: is 5～7 with the isomerization solution of step (13) gained through the ion exchange resin of 732H type or with glacial acetic acid adjusting pH value; Then at vacuum tightness 0.08～0.1MPa, concentrate or add the Virahol of 6-10 times of volume under 30 ℃～70 ℃ the condition, remove post precipitation again at vacuum tightness 0.08～0.1MPa, concentrate under 30 ℃～70 ℃ the condition, obtain the solid mixture of xanchromatic GlcNAc and ManNAc;
(15) ManNAc enrichment: the yellow solid with step (14) obtains, extracted 0.5～2 hour with the methyl alcohol immersion 12～36 hours of 0.5～3 times of volume or with methanol eddy, suction filtration obtains the pregnant solution of ManNAc with solid-liquid separation;
(16) concentrate ManNAc: with the pregnant solution that obtains in the step (15),, concentrate under 30 ℃～70 ℃ the condition, obtain the buttery material, be the ManNAc enriched substance, in-20 ℃ of refrigerators, preserve stand-by at vacuum tightness 0.08～0.1MPa;
(17) transformation experiment: the biological catalyst A of step (6) gained and the biological catalyst B of step (12) gained are mixed with the ManNAc enriched substance of substrate Sodium.alpha.-hydroxypropionate and step (16) gained; At 5 ℃～40 ℃, under pH6.0～9.0 conditions, 180 rev/mins vibrated 5～50 hours, made substrate Sodium.alpha.-hydroxypropionate, ManNAc, biological catalyst A, biological catalyst B and air thorough mixing, finished conversion;
The concentration of substrate Sodium.alpha.-hydroxypropionate is 200～700mM in the above-mentioned reaction mixture; The concentration of ManNAc enriched substance is 40～100g/L; The concentration of biological catalyst A: wet cell 5～80g/L; The concentration of biological catalyst B: wet cell 1～10g/L;
(18) pre-treatment of conversion fluid: with the conversion fluid of step (17) gained, regulate pH to 4～5 with 732H type resin or glacial acetic acid, with 5,000～12,000 rev/min centrifugal 5～10 minutes, remove the biological catalyst A and the biological catalyst B that are added in the step (17), obtain supernatant liquor, be and contain sialic conversion fluid pretreatment fluid;
(19) plastic resin treatment: with one of HZ201 * 8 resins, 330 resins or 717 resins of selecting for use, wash pillar with the aqueous sodium hydroxide solution of 1 N～2 N of 3～6 times of column volumes with 0.5～2 times of column volume flow velocity per hour, with deionized water ion exchange column is washed till neutrality then; Be formic acid type with 0.5～2 times of column volume flow velocity with ion exchange resin conversion with the aqueous formic acid of the 1N～3N of 3～6 times of volumes with resin again, with deionized water with resin wash to pH6～7, stand-by then;
(20) upper prop: the conversion fluid pretreatment fluid of step (18) gained is handled the ion exchange column of gained with step (19) on 0.5～2 times of column volume flow velocity, and whether have sialic acid spill, promptly stop to go up sample if spill if detecting in the effluent liquid in the upper prop process;
(21) wash-out: the ion exchange column that step (20) was handled, pillar washed with the deionized water of 2～4 times of column volumes with 0.5～2 times of column volume flow velocity per hour earlier; With the column volume of identical flow velocity with 1～4 times of the first wash-out of the aqueous formic acid of 0.5N～1N, the aqueous formic acid wash-out of usefulness is collected in the effusive sialic effluent liquid of component that contains in the aqueous formic acid elution process with 1N～3N again;
(22) concentrate: the effluent liquid with step (21) is collected at vacuum tightness 0.08～0.1MPa, concentrates 2～6 times under 25 ℃～50 ℃ the condition;
(23) glacial acetic acid precipitation: with adding volume ratio in the concentrated solution of step (22) gained is 4～10 times glacial acetic acid, leaves standstill crystallization 2～6 days under 4 ℃;
(24) the sialic acid crystal is collected: the magma that step (23) obtains is removed glacial acetic acid with method of pumping filtration, is 3～6 times glacial acetic acid washing crystal with volume ratio; With the crystal of gained, at 30 ℃～70 ℃, vacuum tightness is under the condition of 0.08～0.1MPa at last, dry 2～8 hours;
(25) sample detection:, use with the sialic acid powder of step (24) gained
13The purity of CNMR and HPLC testing product.
2. as claimed in claim 1ly a kind ofly prepare the sialic method of high value through multistep coupling bio-transformation, it is characterized in that the bacterial classification described in the step (1) is pseudomonas (Pseudomonas sp.) ATCC11452 by cheap sodium lactate.
3. as claimed in claim 1ly a kind ofly prepare the sialic method of high value through multistep coupling bio-transformation, it is characterized in that the colibacillus engineering strain described in the step (7) is for containing the reorganization bacterium E.coli HB101 (pBV220-ALD) of acetylneuraminate aldolase (EC4.1.3.3) gene by cheap sodium lactate.
4. as claimed in claim 1ly a kind ofly prepare the sialic method of high value by cheap sodium lactate through multistep coupling bio-transformation, it is characterized in that the M9 substratum of the improvement described in the step (11), concrete prescription by mass volume ratio is:
Peptone 1%; Yeast powder 0.5%; Na
2HPO
47H
2O 1.28%; KH
2PO
40.3%; NaCl 0.05%; NH
4Cl 0.1%; CaCl
20.0011%; Glucose 0.4%; Sterilized 15 minutes for 115 ℃.
5. as claimed in claim 1ly a kind ofly prepare the sialic method of high value through multistep coupling bio-transformation, it is characterized in that biological catalyst A in the step (17) is meant the intact cell of pseudomonas (Pseudomonas sp.) ATCC11452 that contains Lactate Oxidase by cheap sodium lactate; Biological catalyst B is meant the intact cell of the engineering strain E.coli HB101 (pBV220-ALD) that contains acetylneuraminate aldolase.
6. as claimed in claim 1ly a kind ofly prepare the sialic method of high value through multistep coupling bio-transformation, it is characterized in that the concentration of biological catalyst A in the step (17): wet cell 15～60g/L by cheap sodium lactate; The concentration of biological catalyst B: wet cell 3～7g/L.
7. as claimed in claim 1ly a kind ofly prepare the sialic method of high value by cheap sodium lactate through multistep coupling bio-transformation, the concentration that it is characterized in that the substrate Sodium.alpha.-hydroxypropionate in the step (17) is 400～500mM.
8. as claimed in claim 1ly a kind ofly prepare the sialic method of high value through multistep coupling bio-transformation, it is characterized in that the conversion reaction temperature in the step (17) is 15 ℃～35 ℃ by cheap sodium lactate.
9. as claimed in claim 1ly a kind ofly prepare the sialic method of high value through multistep coupling bio-transformation, it is characterized in that the conversion reaction pH in the step (17) is 6.5～8.5 by cheap sodium lactate.
10. as claimed in claim 1ly a kind ofly prepare the sialic method of high value through multistep coupling bio-transformation, it is characterized in that the resin of selecting for use in the step (19) is HZ201 * 8 by cheap sodium lactate.
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103757077A (en) * | 2014-01-20 | 2014-04-30 | 郑州大学 | Culture medium applicable to recombinant protein of escherichia coli fermentation production |
| CN106520864A (en) * | 2016-09-28 | 2017-03-22 | 南京农业大学 | Method for enzymatic synthesis of sialic acid analogue and application thereof |
| CN108841878A (en) * | 2018-06-19 | 2018-11-20 | 四川同晟生物医药有限公司 | A method of coexpression Pfansteihl oxidizing ferment and catalase coupling production Sodium Pyruvate |
| US10378034B2 (en) | 2014-05-27 | 2019-08-13 | Universitetet I Tromsø—Norges Arktiske Universitet | Use of a N-acetylneuraminate lyase derived from the bacterium Aliivibrio salmonicida in the production of neuraminic acid and derivatives thereof |
-
2004
- 2004-05-31 CN CN 200410024222 patent/CN1239695C/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103757077A (en) * | 2014-01-20 | 2014-04-30 | 郑州大学 | Culture medium applicable to recombinant protein of escherichia coli fermentation production |
| US10378034B2 (en) | 2014-05-27 | 2019-08-13 | Universitetet I Tromsø—Norges Arktiske Universitet | Use of a N-acetylneuraminate lyase derived from the bacterium Aliivibrio salmonicida in the production of neuraminic acid and derivatives thereof |
| CN106520864A (en) * | 2016-09-28 | 2017-03-22 | 南京农业大学 | Method for enzymatic synthesis of sialic acid analogue and application thereof |
| CN108841878A (en) * | 2018-06-19 | 2018-11-20 | 四川同晟生物医药有限公司 | A method of coexpression Pfansteihl oxidizing ferment and catalase coupling production Sodium Pyruvate |
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