CN102660603B - Method for rapid purification of bacterial capsular polysaccharide - Google Patents
Method for rapid purification of bacterial capsular polysaccharide Download PDFInfo
- Publication number
- CN102660603B CN102660603B CN201210112393.6A CN201210112393A CN102660603B CN 102660603 B CN102660603 B CN 102660603B CN 201210112393 A CN201210112393 A CN 201210112393A CN 102660603 B CN102660603 B CN 102660603B
- Authority
- CN
- China
- Prior art keywords
- capsular polysaccharide
- polysaccharide
- acid
- bacterial
- purification
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Landscapes
- Polysaccharides And Polysaccharide Derivatives (AREA)
- Medicines Containing Antibodies Or Antigens For Use As Internal Diagnostic Agents (AREA)
Abstract
The invention discloses a method for rapid purification of bacterial capsular polysaccharide. The method can fast remove pollutants comprising proteins and nucleic acid from a specific bacterial fermentation broth and retains purified capsular polysaccharide. The method comprises the following steps of fermentation of capsular polysaccharide-containing bacteria, acid adjustment of a pH value of a fermentation broth, precipitation of thalli and impurities of the fermentation broth, centrifugation, microfiltration, ultrafiltration condensation and filter wash so that a crude bacterial capsular polysaccharide solution is obtained. A basic principle of the method comprises that through acid adjustment, a pH value of a fermentation broth is in a range of 3 to 5 so that thalli having whole shapes and other impurities are removed and capsular polysaccharide is retained in the fermentation broth and thus purification of capsular polysaccharide is realized. The method can be used for purification of capsular polysaccharide of pneumococcocci, haemophilus influenzae type b, epidemic meningococcocci and typhoid bacillus.
Description
Technical field:
The present invention relates to field of biological pharmacy, particularly relate to one and can remove pollutent from ferment product, the method for purified capsular polysaccharide
Background technology:
Streptococcus pneumoniae, b type hemophilus influenzae, epidemic meningitis coccus and Corynebacterium diphtheriae are the important pathogenic bacterias threatening human life.Vaccine development prevents the infection of these germs to be targets that medical circle is struggled for many years.From the sixties in last century, means find that these bacteriums have a common morphological structure feature by experiment, and be exactly that surface of cell membrane is wrapped in one deck pod membrane, this layer of pod membrane is wrapped in each surface of cell membrane by polysaccharide to be formed, therefore claim capsular polysaccharide.In human body, pod membrane plays decisive role for these Pathogenicity of Bacterias, because by preventing antibody to be adsorbed onto on bacterial film, pod membrane can disturb immunocyte to the phagolysis of bacterium, makes bacterium to breed in vivo and to cause a disease.Research finds, bacterial eapsular polysaccharide has good immunogenicity as vaccine, and the adult with sound immunologic function can be stimulated to produce antibody to resist the infection with capsular polysaccharide bacterium; But due to the developing immune system imperfection of less than 2 years old children, do not have immunne response to capsular polysaccharide, and this crowd threatens the most serious crowd by these pathogenic bacterium, exploitation can protect the vaccine of this crowd to be the emphasis problem of medical circle.From the eighties in last century, research finds, when capsular polysaccharide is with covalent linkage and protein bound, after Toxoid,tetanus, diphtheria toxoid or CRM197 (variation diphtheria anatoxine), form polysaccharide-protein combined vaccine, the immune response being directed to capsular polysaccharide can be produced in 2 years old Infants Below body, since then, a kind of synthetic vaccine birth being attached to protein carrier with bacterial eapsular polysaccharide.
At present, commercially have 23 valency pneumococcal polysaccharide vaccines for what prevent grownup streptococcus pneumoniae coccus to infect, and 7 valencys of pre-child-resistant, 10 valencys and 13 valency pneumococcal Polysaccharide Conjugate Vaccines widely use in the world.In addition, typhoid fever (vi) polysaccharide vaccine, b type hemophilus influenzae polysaccharide conjugate vaccine, 4 valency epidemic meningitis polysaccharide conjugate vaccines have also been applied for many years.
Chemically in structure, different bacteriums has different capsular polysaccharides, and same bacterium different serotypes bacterium also has different capsular polysaccharides, as streptococcus pneumoniae has 90 kinds of different serotypes, meningococcus has A, B, C, W135 and Y group, and they all have the capsular polysaccharide of different chemical structures.Research finds, often kind of capsular polysaccharide has strict repeated chemical structure, and this chemical structure can form by a monosaccharide units or containing the oligosaccharide that the most nearly 7-8 monosaccharide residue forms.This repeated unit can be linear or containing non-carbohydrate substituted radical bifurcation structure, and these non-carbohydrate substituted radicals can be O-ethanoyl (O-acetyl), Phosphoric acid glycerol esters (glycerol phosphate) or pyruvic acid (pyruvate); In addition, some capsular polysaccharides of streptococcus pneumoniae may contain uncommon monosaccharide residue, as diamino (diamino-), and deoxidation and point fork chain sugar etc.The diversity of this bacterial polysaccharides structure, brings challenge and difficulty to these polysaccharide methods of purifying.
Preparing vaccine with capsular polysaccharide, comprise polysaccharide vaccine or polysaccharide conjugate vaccine, all needing the capsular polysaccharide with meeting certain mass standard to prepare as raw material.In order to obtain highly purified capsular polysaccharide, fermenting bacteria can be carried out with the liquid medium of being rich in nutrition composition, and then from fermented liquid purified capsular polysaccharide, the principal pollutant will removed in purge process comprise bacterioprotein, nucleic acid and medium component, if when preparing pneumococcal capsular polysaccharide, also need the pollution of control C-polysaccharide.
The foundation of bacterial eapsular polysaccharide purifying process experienced by evolution for many years, in traditional method purified capsular polysaccharide process, pollution of nucleic acid in Polysaccharide removing solution is more difficult to reach purity requirement needed for vaccine preparation, because the chemical property of the capsular polysaccharide of different bacterium is different, often kind of bacterial eapsular polysaccharide needs to remove pollution of nucleic acid with special methods, does not have a kind of method can the capsular polysaccharide of other bacterium of purifying.Some bacterial eapsular polysaccharide needs to be precipitated by a large amount of ethanol, meanwhile, with different organic solvent extractions, as ether etc., helps purifying.Alcohol settling usually can protein pollutant effectively in Polysaccharide removing, and its concentration is reduced to lower level; But, be difficult to be reduced to the level that the vaccine for injection requires, comprise and adopt organic solvents, chloroform and butanols mixed solvent or phenol, mix with polysaccharide soln, jolt 4-6 hour, then, with low-speed centrifugal, the metaprotein be gathered between aqueous phase and organic phase can with the separation of polysaccharides in aqueous phase.But the shortcoming of this method is in extraction process, and polysaccharide can be degraded, and ruptures or loses its luv space conformation, and the polysaccharide be purified has not been effective immunogen.Polytropy due to different bacterium polysaccharide structures limits the validity of these separation methods.Thus, reaching a conclusion is do not have a kind of method can the capsular polysaccharide of purifying different bacterium effectively in early stage traditional method.
However, have and be severally purified into high purity and preserve its immunogenic different bacterium capsular polysaccharide method and invented, particularly when purifying different serotypes pneumococcal capsular polysaccharide, these methods effectively can be purified into and comprise 24 kinds of serotype capsular polysaccharides.Comprise 1,2,3,4,5,6A, 6B, 7F, 8,9N, 9V, 10A, 11A, 12F, 14,15B, 17F, 18C, 19A, 19F, 20,22F, 23F and 33F, and for preparing the capsular polysaccharide raw material of 23 valency pneumococcal polysaccharide vaccines.
1980, the patent US4242501 of American Cyanamid Company company of the U.S. has set forth a kind of purifying pneumococcal capsular polysaccharide method, on this patent basis, the said firm have registered another patent US4686102 in 1987 again subsequently, in order to the Pneumococcal serotype capsular polysaccharide that purifying 23 is different.The basic technology approach of this patent is after streptococcus pneumoniae fermentation, add Sodium desoxycholate (sodiumdeoxycholate) dissolution of bacteria, capsular polysaccharide on thalline is released in fermented liquid, after centrifugal segregation cell debris, with alcohol settling twice, this step can remove a large amount of pollutents comprising protein; Add the polysaccharide soln after cetyl trimethylammonium bromide to alcohol settling, remove pollutent further.By controlling cetyl trimethylammonium bromide concentration, can get off by adsorption precipitation major part serotype polysaccharide precipitation, these precipitate polysaccharides can be dissolved in sodium chloride solution subsequently, those undissolved macromolecule contaminants of centrifugal segregation.But, have four kinds of serotype polysaccharide can not form precipitation with cetyl trimethylammonium bromide, the effect adding cetyl trimethylammonium bromide is deposit fouling thing, these pollutents of centrifugal segregation.Subsequently, then add ethanol to remove cetyl trimethylammonium bromide.After centrifugal segregation precipitation, add the pollutent that charcoal absorption is residual, as albumen and nucleic acid.Finally, purified capsular polysaccharide is obtained by dialysis.From technological process, although the method establishes the purification platforms of a pneumococcal capsular polysaccharide, can be purified into different serotypes polysaccharide by same method, step is numerous and diverse, should not grasp; Wherein further comprises multistep alcohol settling, centrifugal, time-consuming, cost of equipment is high; And unsuitable expanding production.Cetyl trimethylammonium bromide settling step technical sophistication, different serotypes treatment process is different.In addition, the polysaccharide be finally purified only can meet the quality standard of preparation 23 valency pneumonia polysaccharide vaccine, namely albumen and nucleic acid content are lower than 2%-7%, cannot meet existing pneumococcal Polysaccharide Conjugate Vaccine to albumen in polysaccharide raw material and nucleic acid content lower than 1% specification of quality.
To 1998, the patent US5714354 of American Home Products company of the U.S. proposed and a kind ofly carrys out improving one's methods of purifying pneumococcal capsular polysaccharide without alcohol settling.The method is 20 capsular polysaccharides by precipitating with cetyl trimethylammonium bromide in 23 kinds of Pneumococcus serotypes, then use the pollutent in the next further separating polyose of activated carbon filtration, di grey matter salt (Hydroxyapatite) chromatography and anion-exchange chromatography, this purification process step can be purified into most of serotype capsular polysaccharide.And other 3 can not with the purifying of the serotype (serotype 7F, 14 and 33F) of cetyl trimethylammonium bromide precipitation, be adopt modifying method to carry out purifying, comprise anionite-exchange resin chromatography.Compare with last patent purifying process, this purifying process can save 75% purification time, and expense also reduces, and does not need specific installation.The quality of all 23 serotype capsular polysaccharides that the method is purified reaches the quality index of polysaccharide vaccine.
Coexist 1998, the patent US5847112 of Merck company of the U.S. also issues a kind of method of purifying pneumonia capsular polysaccharide.Basic skills is for carrying out separating polyose from fermentation broken bacterium liquid in two steps with ethanol; The first step comes precipitate cell debris and pollutent with the ethanol of low per-cent, as C-polysaccharide, retains polysaccharide in solution; Next, other pollutent stayed in the solution, to precipitate capsular polysaccharide, abandons by the ethanol adding high density.After being dissolved by precipitate polysaccharides, then use ordinary method, such as nucleic acid and protease digestion, or organic solvent, remove albumen and the nucleic acid of pollution further, rough polysaccharide is obtained by alcohol settling and freeze-drying.Subsequently, refining full polysaccharide or partially-hydrolyzed polysaccharide is obtained by anion-exchange chromatography purifying.Although higher purity rubric can be reached with the polysaccharide that above two kinds of methods are purified, step is still numerous and diverse, and process regulation requires high.The particularly precipitate and separate step length consuming time of multi-step.
The patent US20060228381 of Wyeth company of the U.S. proposes a kind of method of more succinct purifying pneumococcal capsular polysaccharide.Basic Ways is with after beans substratum fermentation streptococcus pneumoniae, add Sodium desoxycholate to dissolve thalline, then add below acid-conditioning solution pH to 5.5 and come bulk deoxidation Sodium cholic acid and most of soluble proteins, by the cell debris in centrifuging and ultrafiltration removal solution and throw out.Thus obtained rough polysaccharide still needs traditional method to be further purified, and comprise the impurity remained with activated carbon filtration, hydroxyapatite column absorption, and ultrafiltration filter wash obtains refined polysaccharide.The feature of such purification process is to break this step of bacterium secondary fermentation liquid by most pollutent by acidifying, as albumen, nucleic acid, intracellular toxin etc., is separated, simplifies subsequent technique, shorten purification time with the capsular polysaccharide in solution.But, due to be use carry out purifying with Sodium desoxycholate lysate, the C-glycocalix contained in the cell walls of some serotype discharges, because C-polysaccharide is similar with the chemical property of capsular polysaccharide, not easily be removed in purification process subsequently, cause C-polysaccharide content in purified polysaccharide too high.
The present invention, by summarizing the purification process of existing bacterial eapsular polysaccharide, proposes one purification process more fast, and all standard of the purified capsular polysaccharide obtained all reaches existing WHO quality standard.
Summary of the invention:
The object of this invention is to provide a kind of method of rapid purification of bacterial capsular polysaccharide, it can remove pollutent wherein fast from specific bacteria fermented liquid, comprises albumen and nucleic acid, retains the capsular polysaccharide solution of purifying, comprises the steps:
Step one, the fermentation of capsular polysaccharide bacterium: the bacterium going out specific capsular polysaccharide in the fermentation cylinder for fermentation that bacteria culture medium is housed;
Step 2, adds the thalline in Acid precipitation fermented liquid and impurity: the pH value of acid adding regulating step one gained fermented liquid, and control ph≤5, precipitate thalline and impurity by this method;
Step 3, adopts throw out in centrifuging removal step two fermented liquid, collects the supernatant liquor after centrifugation;
Step 4, carries out micro-filtration by microfiltration membrane to the centrifuged supernatant that step 3 obtains, to remove remaining cell fragments wherein and insoluble finely ground particle substance;
Step 5, ultrafiltration and concentration and filter wash: concentrate the micro-filtrate with filter wash step 4 with ultra-filtration membrane, obtain crude bacterial capsular polysaccharide solution.
In the method for above-mentioned rapid purification of bacterial capsular polysaccharide, described bacterium comprises: streptococcus pneumoniae, b type hemophilus influenzae, epidemic meningitis coccus and Corynebacterium diphtheriae.
In the method for above-mentioned rapid purification of bacterial capsular polysaccharide, acid added in step 2 is any one in phosphoric acid, acetic acid, hydrochloric acid, sulfuric acid or nitric acid.
In the method for above-mentioned rapid purification of bacterial capsular polysaccharide, in step 2, the scope of pH value is between 3.0 ~ 5.0.
In the method for above-mentioned rapid purification of bacterial capsular polysaccharide, in step 4, the membrane pore size of microfiltration membrane used is 0.22,0.45, any one in 0.65,1.0 μm.
In the method for above-mentioned rapid purification of bacterial capsular polysaccharide, in step 5, ultra-filtration membrane used any one film that to be molecular weight be in 5kD to 500kD scope.
In the method for above-mentioned rapid purification of bacterial capsular polysaccharide, in step 5, filter wash solution used is pure water, damping fluid or salts solution or their mixed solution.
In the capsular polysaccharide solution obtained by above-mentioned purification process, comprise soluble proteins and nucleic acid impurities content reduces all significantly.
The present invention can be used for, from containing purified polysaccharide capsular polysaccharide bacterium, just illustrating herein, and being not limited to these bacteriums, as streptococcus pneumoniae different serotypes, comprise 1,2,3,4,5,6A, 6B, 7F, 8,9N, 9V, 10A, 11A, 12F, 14,15B, 17F, 18C, 19A, 19F, 20,22F, 23F and 33F, b type hemophilus influenzae, epidemic meningitis coccus, and Corynebacterium diphtheriae.
In the present invention, step 2 adds Acid precipitation thalline and impurity is core, namely by adding phosphoric acid by between zymocyte liquid pH regulator to 3.0-5.0, precipitates thalline, albumen and nucleic acid by this scheme.
In the present invention, centrifugal, micro-filtration and ultrafiltration and concentration three-step approach is adopted to remove throw out in step 2 fermented liquid and insoluble particle, effect is very good, different according to bacterial species, or pneumococcal serotype is different, selects 0.22,0.45,0.65 or 1.0 μm of film carrys out the centrifuged supernatant of micro-filtration acquisition, removes cell granulations residual in solution and fragment, and insoluble particles; With 30 to 500kD film, ultrafiltration and concentration is carried out to micro-filtrate, and carry out ultrafiltration cleaning solution with deionized water or damping fluid, remove small molecule contaminants, by the purification process of these steps, the 90-98% albumen in capsular polysaccharide solution and 95-99% nucleic acid can be removed, the throw out in fermented liquid is removed more thorough.
Embodiment:
A kind of method of rapid purification of bacterial capsular polysaccharide, with traditional main difference of carrying out purification process from the ferment product after broken bacterium/or bacteriolyze be, the present invention is by being removed fast and easily by the pollutent in solution, retains the capsular polysaccharide of the intact molecular weight in solution.The present invention can be used for, and as streptococcus pneumoniae, b type hemophilus influenzae, the purifying of epidemic meningitis coccus and Corynebacterium diphtheriae capsular polysaccharide, in the polysaccharide soln after purifying, foreign protein and nucleic acid content can reduce 90-98%.The purifying capsular polysaccharide cumbersome of current employing, the precipitate and separate step containing multistep, not easily industrialization scale operation, needs the input of equipment valuable in a large number and manpower to operate.
The purifying process of bacterial eapsular polysaccharide is through semicentennial Vicissitude, and along with novel biomaterial is constantly released, macromolecule purifying technology is also improved thereupon, to adapt to the standard improved constantly biotechnological formulation quality.For the vaccine prepared with bacterial eapsular polysaccharide, as pneumococcal polysaccharide vaccine and polyvalent pneumococcal polysaccharide combination vaccine, b type hemophilus influenzae combined vaccine, meningococcal polysaccharide vaccine and polysaccharide conjugate vaccine, and Typhoid Vi Polysaccharide Vaccine and Vi polysaccharide conjugate vaccine, the quality standard of its capsular polysaccharide is also in continuous improve, for the impurity protein content permissible criterion in polysaccharide, from the eighties 23 in last century, one of the quality standard of valency pneumococcal polysaccharide vaccine is that requirement impurity protein and nucleic acid standard are lower than 2-7%, the capsular polysaccharide raw materials quality standard used to the various different bacterium polysaccharide conjugate vaccines of 2000 is lower than 1%.The purifying process of bacterial eapsular polysaccharide is also from early stage nearly 16 road techniques, be improved to the 10 road main technological steps adopted at present, shorten time and the cost of purifying needs, meanwhile, also reach the standard of modern polysaccharide vaccine formulation requirements qualitatively.
The present invention is on the basis detected the intermediate product of existing bacterial eapsular polysaccharide purifying process link and assess, and optimize further and the purifying process platform of foundation, can be purified into the capsular polysaccharide of different bacterium fast, easily, step is as follows:
Step one, the fermentation of capsular polysaccharide bacterium: the bacterium going out specific capsular polysaccharide in the fermentation cylinder for fermentation that bacteria culture medium is housed;
Step 2, adds the thalline in Acid precipitation fermented liquid and impurity: the pH value of acid adding regulating step one gained fermented liquid, and control ph≤5, precipitate thalline and impurity by this method;
Step 3, adopts throw out in centrifuging removal step two fermented liquid, collects the supernatant liquor after centrifugal;
Step 4, carries out micro-filtration by microfiltration membrane to the centrifuged supernatant that step 3 obtains, to remove remaining cell fragments wherein and insoluble finely ground particle substance;
Step 5, concentrates the micro-filtrate with filter wash step 4 with ultra-filtration membrane, obtains crude bacterial capsular polysaccharide solution;
By above five polysaccharide purification processing steps, can by the major impurity in solution, content as albumen and nucleic acid reduces 90-98%, and meanwhile, the immunogenicity of the capsular polysaccharide be purified, the integrity of molecule are all better than or are equal to the polysaccharide that existing purification process obtains.
Step 6, adopts prior art to carry out subsequent purification to bacterial eapsular polysaccharide.
The principle of design of method of the purification of bacterial capsular polysaccharide that the present invention proposes and the control of test conditions as follows:
(1), the control of bacterial fermentation processes
Be purified into highly purified capsular polysaccharide, the link to each in polysaccharide production process may pollute is needed to be controlled, decreasing pollution thing of particularly should trying one's best on fermenting step enters into the fermented liquid for purified polysaccharide, wherein, the foreign-matter contamination discharged due to bacterial cell disruption, as albumen and nucleic acid, and the impurity contained in substratum, comprise albumen, nucleic acid and impurity polysaccharide etc. are the main sources of pollutent.For streptococcus pneumoniae, this bacterium is gram-positive microorganism, can tolerate oxygen, and its form has multifarious feature, can transform between smooth (Transparent) and coarse (Opaque) colonial morphology.When being in smooth bacterium state, bacterium surface only has a small amount of capsular polysaccharide, is the form that human body nasal cavity endophyte falls to existing; And the bacterium surface being in rough bacteria state contains a large amount of capsular polysaccharides, be the form that the streptococcus pneumoniae in blood of human body exists, the existence of capsular polysaccharide can stop host immune cell phagolysis, makes bacterium can survive and breed.
Experiment shows in liquid medium within, and the part capsular polysaccharide of Pneumococcal Surface parcel can be shed in fermented liquid, can be used for purified capsular polysaccharide.Obviously, obtain capsular polysaccharide from phage surface, must obtain after bacterial cell disruption, this just makes the pollutent such as impurity protein, nucleic acid in bacterial body all be released in fermented liquid, thus adds the difficulty of purified polysaccharide.In order to avoid this problem, simultaneously, according to pneumococcal cultural characters, first the present invention adopts strict anaerobic fermentation, make streptococcus pneumoniae in fermented liquid based on rough bacteria state, with this understanding, streptococcus pneumoniae can produce a large amount of capsular polysaccharides, and part capsular polysaccharide can be released into nutrient solution from bacterium surface.Controlling the pH value (7.0-7.6) in neutral range of fermented liquid, polysaccharide can stably exist in solution and not degrade.On the other hand, because streptococcus pneumoniae contains N,O-Diacetylmuramidase, when after bacterial death, this enzyme self-dissolving can be discharged, therefore, fermentation to be stopped in time at fermentation using bacteria to growth platform after date, gather in the crops, to reduce bacterial death, discharge entocyte, the situation polluting fermented liquid occurs.
The pneumovax used in the market, comprise 23 valency pneumonia polysaccharide vaccines and 13 valency pneumococcal Polysaccharide Conjugate Vaccines, and b type hemophilus influenzae polysaccharide conjugate vaccine, producing capsular polysaccharide raw material used is all dissolve thalline by adding in tensio-active agent to fermented liquid, purifying is carried out with the capsular polysaccharide discharged on bacteria cell wall, in fact the source of final capsular polysaccharide has two approach, namely drops to from bacterium surface the polysaccharide discharged by cell walls after polysaccharide fermented liquid and bacteriolyze during the fermentation.Although when carrying out purified capsular polysaccharide in this way, starting polysaccharide total amount will more than only from the initial amount of purified capsular polysaccharide the fermented liquid supernatant liquid removing thalline; But, impurity component content in bacteriolyze fermented liquid in starting soln will far above fermented liquid supernatant liquid, this adds burden to subsequent purification operation, need more step to carry out purifying, therefore, polysaccharide on the one hand in solution can lose increase in too much purification step, its yield with from fermented supernatant fluid, carry out purifying compare, do not preponderate; On the other hand, add after tensio-active agent carrys out bacteriolyze, although more polysaccharide can be discharged, be present in the impurity polysaccharide component of cell walls, such as C-polysaccharide is also released.And the chemical property of C-polysaccharide is similar with capsular polysaccharide, in follow-up purge process, remove very difficult.In product on existing market, C-polysaccharide pollutes is distinct issues, because C-polysaccharide is in testing process, be easily counted into capsular polysaccharide, but C-polysaccharide does not have immunogenicity, body can not be stimulated to produce protection antibody and carry out sterilization.Consequently be mixed in preparation and cause the immune effect of polysaccharide vaccine to be affected.
(2), the control of fermented liquid acidization
After obtaining the fermented liquid containing capsular polysaccharide, by itself and pollutent, comprise thalline, albumen and nucleic acid, the step carrying out being separated is numerous and diverse, common method has centrifugal segregation macrobead thalline, subsequently by filtering, remove short grained cell debris to obtain the Clarified fermentation supernatant liquor containing capsular polysaccharide.In the purge process in downstream, adopt such as alcohol settling, nucleic acid and protease digestion, organic solvent and phenol extraction and ultrafiltration cleaning step to be further purified, finally obtain purified polysaccharide.
Present invention employs and the fermented liquid containing thalline is directly carried out acidifying, precipitate thalline once, albumen and nucleic acid impurities, this method will reduce traditional multi-step minimizing technology widely.Different according to raw bacteriogenic kind, or the difference of serotype, when by the pH regulator of solution to 3.0-5.0 scope time, the thalline of 90%-98% in fermented liquid can be precipitated, albumen and nucleic acid.Souring soln acid used can be phosphoric acid, acetic acid, hydrochloric acid, sulfuric acid, the mixed solution of the different concns of nitric acid or these acid solutions.Acidificatoin time is 10 minutes-24 hours, needs to decide according to different bacteriums or serotype.During acidifying, broth temperature can be 4-37 DEG C.By the control to above condition, the principal pollutant such as the thalline in fermented liquid, albumen and nucleic acid can form precipitation fast, and capsular polysaccharide stably can exist in solution and reaches the object of separating impurity.
(3), the control of centrifugal and/or microfiltration process
By ordinary method, as centrifugal and/or micro-filtration remove precipitation, in purification platforms program of the present invention, first carry out the ferment product after centrifugal acidifying with online whizzer, to remove oarse-grained precipitation, comprise throw out and thalline.Centrifuging temperature is 4-25 DEG C.Centrifugation time was at 30 minutes-120 minutes.Subsequently, remove cell debris in solution and small-particle insolubles further by micro-filtration, the molecular weight ranges of microfiltration membrane is at 0.22 to 1 μm.Collect the clarification filter solution containing capsular polysaccharide, abandon micro-filtration phegma.
(4), the control of ultrafiltration and concentration and filter wash process
In purification technique platform program of the present invention, ultrafiltration and concentration is carried out to micro-filtrate and the ultra-filtration membrane molecular weight that cleaning adopts can be any one in 5,10,30,50,100 or 500Kd, need to decide according to bacterial species or particular serotype.Concentrated final solution volume range is 2-10 times of original solution, determines according to bacterial species or serotype difference.Adopt any one in pure water, damping fluid, salts solution or acidifying salt soln during ultrafiltration filter wash concentrated solution processing step, need the stability of more different serotypes polysaccharide to decide.By above purification process, the foreign matter content in solution progressively reduces, following table be streptococcus pneumoniae part serotype capsular polysaccharide solution through purifying rear impurity concentration determination result:
From upper table, according to the difference of Pneumococcus serotypes, by purification process of the present invention, can 90-98% albumen in Polysaccharide removing solution, and the effect that nucleic acid is removed is more obvious, can reach 97-99%.
To it should be noted that, purified capsular polysaccharide technique of the present invention, can use with other purification process.In general, available purification process of the present invention removes most of impurity after carrying out preliminary purification to the polysaccharide in fermented liquid, then in the purifying process in downstream, other finished purification method can be adopted, such as activated carbon filtration, phosphorus hydroxyl grey matter rock adsorbs, chromatography, alcohol settling, and the methods combining such as phenol extraction is further purified, removes residual albumen or contaminant nucleic acid, and obtain refined polysaccharide.
Need further it is emphasised that, purification process of the present invention is key one step of rapid purification of bacterial capsular polysaccharide.A part for other purifying capsular polysaccharide technique can be applied to, by conjunction with other polysaccharide purification method, albumen and nucleic acid content can be down to less than 1.0%.
Above to invention has been summary, in order to further describe and understand, following object lesson can be read.The object describing these examples is only used to that the present invention will be described, instead of limits the invention within the scope of these examples.
Embodiment 1:
Purified capsular polysaccharide from the fermented liquid of Pneumococcus serotypes 19F, concrete grammar step is as follows:
Step one, the fermentation of capsular polysaccharide bacterium: the bacterium going out specific capsular polysaccharide in the fermentation cylinder for fermentation that bacteria culture medium is housed;
(1), main seed and work Spawn preparation
Pneumococcus serotypes 19F obtains from American Type Culture Collecti (American Type Culture Collection), by the strain inoculation in freeze-dried semen pipe in 5ml yeast-acid hydrolysis casein nutrient solution, cultivate 12-24 hour, when bacterial growth is to OD for 36 DEG C ± 2 DEG C
600when reading is 0.6-2.0, turned by bacterium liquid in the fresh yeast-acid hydrolysis casein nutrient solution being seeded to 150ml, at 36 DEG C ± 2 DEG C, cultivate 5-20 little of exponential phase of growth, stop cultivating, packing freeze-drying, being stored in 2-8 DEG C is main seed.
The strain inoculation of the main seed freeze-drying pipe of Pneumococcus serotypes 19F, in 5ml yeast-acid hydrolysis casein nutrient solution, cultivates 12-24 hour, when bacterial growth is to OD for 36 DEG C ± 2 DEG C
600when reading is 0.6-2.0, bacterium liquid is turned in the fresh yeast-acid hydrolysis casein nutrient solution being seeded to 150ml, at 36 DEG C ± 2 DEG C, cultivate 5-20 little of exponential phase of growth, stop cultivating, packing freeze-drying, be stored in the 2-8 DEG C of work seed for this serotype.
(2), fermentation using bacteria
Take out seed pipe from work seed bank to be seeded to 5ml yeast-acid hydrolysis casein nutrient solution, be cultured to bacterial growth Midexponential at 36 DEG C ± 2 DEG C.Bacterium liquid is turned in the fresh yeast-acid hydrolysis casein nutrient solution being seeded to 150ml, at 36 DEG C ± 2 DEG C, cultivate 5-20 little of exponential phase of growth, 50ml bacterium liquid is turned and is seeded in 2L fresh yeast-acid hydrolysis casein nutrient solution, at 36 DEG C ± 2 DEG C, be cultured to mid-term exponential phase of growth and be prepared into fermentation seed liquid, fermentation seed liquid being seeded in 50 liters of fermentor tanks that 30 liters of yeast-acid hydrolysis casein nutrient solution is housed.Maintain fermented liquid pH 6.8 ± 0.2 with sodium hydroxide, treat that bacterial growth is to late exponential stage.
Step 2, adds Acid precipitation thalline and impurity: add the pH value that phosphoric acid regulates fermented liquid, makes the pH value of fermented liquid control between 3 ~ 5, quiet to 10-60 minute, precipitates thalline and impurity by this method;
Step 3, adopts throw out in centrifuging removal step two fermented liquid, collects centrifuged supernatant;
With online whizzer at 4-10 DEG C, with 8, centrifugal 10 ~ 90 minutes of 000 ~ 10,000rpm, removes thalline and throw out;
Step 4, carries out micro-filtration by microfiltration membrane to the centrifuged supernatant that step 4 obtains, and to remove remaining cell fragments wherein and insoluble finely ground particle substance, by 0.22 μm of membrane microfiltration fermentation centrifuged supernatant, collects filtered liquid, abandons phegma;
Step 5, the micro-filtrate with filter wash step 4 is concentrated with ultra-filtration membrane, obtain crude bacterial capsular polysaccharide solution, micro-filtrate is concentrated to after 10 times of original volume with 30Kd membrane ultrafiltration, filter wash is carried out with pure water, remove the impurity such as albumen residual in solution and nucleic acid, vacuum-freeze-dry polysaccharide, store at-70 DEG C.
Step 6, adopts prior art to carry out subsequent purification to bacterial eapsular polysaccharide.
Claims (6)
1. a method for rapid purification of bacterial capsular polysaccharide, comprises the following steps:
Step one, the fermentation of capsular polysaccharide bacterium: the bacterium going out specific capsular polysaccharide in the fermentation cylinder for fermentation that bacteria culture medium is housed;
Step 2, adds the thalline in Acid precipitation fermented liquid and impurity: the pH value of acid adding regulating step one gained fermented liquid, and control ph≤5, precipitate thalline and impurity by this method;
Step 3, adopts throw out in centrifuging removal step two fermented liquid, collects the supernatant liquor after centrifugal;
Step 4, carries out micro-filtration by microfiltration membrane to the centrifuged supernatant that step 3 obtains, to remove remaining cell fragments wherein and insoluble finely ground particle substance;
Step 5, ultrafiltration and concentration and filter wash: concentrate the micro-filtrate with filter wash step 4 with ultra-filtration membrane, obtain crude bacterial capsular polysaccharide solution;
Described bacterium is streptococcus pneumoniae.
2. the method for rapid purification of bacterial capsular polysaccharide according to claim 1, is characterized in that: acid added in step 2 is any one in phosphoric acid, acetic acid, hydrochloric acid, sulfuric acid or nitric acid.
3. the method for rapid purification of bacterial capsular polysaccharide according to claim 1, is characterized in that: in step 2, the scope of pH value is between 3.0 ~ 5.0.
4. the method for rapid purification of bacterial capsular polysaccharide according to claim 1, is characterized in that: in step 4, the membrane pore size of microfiltration membrane used is 0.22,0.45, any one in 0.65,1.0 μm.
5. the method for rapid purification of bacterial capsular polysaccharide according to claim 1, is characterized in that: ultra-filtration membrane used in step 5 any one film that to be molecular weight be in 5kD to 500kD scope.
6. the method for rapid purification of bacterial capsular polysaccharide according to claim 1, it is characterized in that: in step 5, filter wash solution used is pure water, damping fluid or salts solution or their mixed solution.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210112393.6A CN102660603B (en) | 2012-04-17 | 2012-04-17 | Method for rapid purification of bacterial capsular polysaccharide |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210112393.6A CN102660603B (en) | 2012-04-17 | 2012-04-17 | Method for rapid purification of bacterial capsular polysaccharide |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN102660603A CN102660603A (en) | 2012-09-12 |
| CN102660603B true CN102660603B (en) | 2015-03-25 |
Family
ID=46770179
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201210112393.6A Active CN102660603B (en) | 2012-04-17 | 2012-04-17 | Method for rapid purification of bacterial capsular polysaccharide |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102660603B (en) |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107043431B (en) * | 2017-02-23 | 2020-06-30 | 上海瑞宙生物科技有限公司 | Purification method of bacterial capsular polysaccharide |
| EA201992636A1 (en) * | 2017-05-05 | 2020-04-17 | Серум Инститьют Оф Индия Прайват Лимитед | METHOD FOR REMOVING IMPURITIES FROM DRUGS BASED ON BACTERIAL CAPSULAR POLYSACCHARIDES |
| CN113234770B (en) * | 2021-06-15 | 2024-06-14 | 广州知易生物科技有限公司 | Preparation method of bacteroides fragilis capsular polysaccharide A |
| CN116693706B (en) * | 2022-02-24 | 2024-10-11 | 成都生物制品研究所有限责任公司 | Purification method of streptococcus pneumoniae capsular polysaccharide |
| CN114755406B (en) * | 2022-03-28 | 2023-10-24 | 南京农业大学 | Streptococcus suis type9 ELISA antibody detection method and kit thereof |
| CN117512031B (en) * | 2023-10-16 | 2024-06-25 | 江苏金迪克生物技术股份有限公司 | Purification method of pneumococcal capsular polysaccharide |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2000143522A (en) * | 1998-11-05 | 2000-05-23 | Tayca Corp | Tolerance inducing agent |
| CN101155833A (en) * | 2005-04-08 | 2008-04-02 | 惠氏公司 | Separation of contaminants from streptococcus pneumoniae polysaccharide by ph manipulation |
| CN101663327A (en) * | 2007-03-23 | 2010-03-03 | 惠氏公司 | Produce the purification process of the shortening of streptococcus pneumoniae (STREPTOCOCCUS PNEUMONIAE) capsular polysaccharide |
-
2012
- 2012-04-17 CN CN201210112393.6A patent/CN102660603B/en active Active
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2000143522A (en) * | 1998-11-05 | 2000-05-23 | Tayca Corp | Tolerance inducing agent |
| CN101155833A (en) * | 2005-04-08 | 2008-04-02 | 惠氏公司 | Separation of contaminants from streptococcus pneumoniae polysaccharide by ph manipulation |
| CN101663327A (en) * | 2007-03-23 | 2010-03-03 | 惠氏公司 | Produce the purification process of the shortening of streptococcus pneumoniae (STREPTOCOCCUS PNEUMONIAE) capsular polysaccharide |
Also Published As
| Publication number | Publication date |
|---|---|
| CN102660603A (en) | 2012-09-12 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102660601B (en) | The method of rapid purification of bacterial capsular polysaccharide | |
| CN102660603B (en) | Method for rapid purification of bacterial capsular polysaccharide | |
| CN102660602B (en) | Method for rapidly purifying bacteria capsular polysaccharide | |
| CN101663327B (en) | Shortened purification process for the production of capsularstreptococcus pneumoniae polysaccharides | |
| WO2013026385A1 (en) | Preparation method for quadrivalent meningococcal polysaccharide vaccine | |
| CN104945527A (en) | Galactomannan antigen and preparation method thereof | |
| KR20160127028A (en) | A novel downstream process for purifying polysaccharides | |
| CN113603804B (en) | Refining method of streptococcus pneumoniae capsular polysaccharide | |
| CN117512031B (en) | Purification method of pneumococcal capsular polysaccharide | |
| CN107082819A (en) | A kind of purification process of streptococcus pneumoniae capsular polysaccharide | |
| CN104530250A (en) | Method for purifying pneumococcal capsular polysaccharide | |
| CN101864471B (en) | Microbial fermentation method for producing hyaluronic acid | |
| US10702596B2 (en) | Polysaccharide purification for vaccine production using lytic enzymes, tangential flow filtration, and multimode chromatography | |
| KR102472936B1 (en) | Polysaccharide Purification for Vaccine Manufacturing Using Soluble Enzymes, Tangential Flow Filtration, and Multimodal Chromatography | |
| CN100540675C (en) | A kind of Sepharose of use 4FF gel carries out the method for purifying to bacterial polysaccharides | |
| CN104592408A (en) | Method for purifying capsular polysaccharide | |
| CN117756959B (en) | Preparation method of streptococcus pneumoniae capsular polysaccharide | |
| CN116693706B (en) | Purification method of streptococcus pneumoniae capsular polysaccharide | |
| CN117756958A (en) | Method for preparing streptococcus pneumoniae capsular polysaccharide or polysaccharide degradation thereof | |
| CN103833865B (en) | A kind of preparation method of streptococcus pneumoniae capsular polysaccharide | |
| TWI545192B (en) | Method for preparing capsular polysaccharides of streptococcus pneumoniae serotype | |
| CN111378054B (en) | Purification method of dysentery bacillus specific polysaccharide | |
| WO2024062494A1 (en) | Method for the purification of capsular polysaccharides | |
| CN115820436A (en) | Method for improving ganoderma lucidum mycelium polysaccharide | |
| CN110923280A (en) | Tetrodotoxin preparation and purification method thereof |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |