CN102526720A - Preparation method of influenza virus vaccine - Google Patents

Preparation method of influenza virus vaccine Download PDF

Info

Publication number
CN102526720A
CN102526720A CN2012100076872A CN201210007687A CN102526720A CN 102526720 A CN102526720 A CN 102526720A CN 2012100076872 A CN2012100076872 A CN 2012100076872A CN 201210007687 A CN201210007687 A CN 201210007687A CN 102526720 A CN102526720 A CN 102526720A
Authority
CN
China
Prior art keywords
cell
virus
strain
monoclonal
influenza
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.)
Granted
Application number
CN2012100076872A
Other languages
Chinese (zh)
Other versions
CN102526720B (en
Inventor
刘坤
王希良
张良艳
姚志东
邢丽
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Institute of Microbiology and Epidemiology of AMMS
Original Assignee
Institute of Microbiology and Epidemiology of AMMS
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Institute of Microbiology and Epidemiology of AMMS filed Critical Institute of Microbiology and Epidemiology of AMMS
Priority to CN2012100076872A priority Critical patent/CN102526720B/en
Publication of CN102526720A publication Critical patent/CN102526720A/en
Application granted granted Critical
Publication of CN102526720B publication Critical patent/CN102526720B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • Medicines Containing Antibodies Or Antigens For Use As Internal Diagnostic Agents (AREA)
  • Micro-Organisms Or Cultivation Processes Thereof (AREA)

Abstract

The invention discloses a preparation method of influenza virus vaccine and belongs to the technical field of vaccine preparation. The method comprises the steps that: firstly, mammal cells are subjected to monocloning, a monoclonal cell bank is built, then, monoclonal cell strains adapted by influenza viruses are sieved, next, the virus adaptability cell strain virus culture condition is optimized, finally, virus adaptability cell strains are cultured in a bioreactor, influenza viruses are inoculated when the cells grow to a certain density, the viruses are cultured through referring to the optimized virus culture condition, the viruses are subjected to concentration, purification, inactivation and cracking after being harvested, the hemagglutinin content is measured, and the influenza virus vaccine is prepared. The method disclosed by the invention has the advantages that the virus yield is greatly improved, and safety, validity and stability are realized.

Description

A kind of method for preparing of influenza virus vaccine
Technical field
The invention belongs to the vaccine production technical field, be specifically related to a kind of method for preparing of influenza virus vaccine.
Background technology
Influenza infection causes acute respiratory infectious disease-influenza, causes serious harm for human health and social life.Influenza virus type is many, variation is fast, and when new subtype virus occurred, crowd's specific immunity often was difficult to prove effective.
Inoculation epidemic strain vaccine is that flu-prevention is popular, most economical, the effective means of protection Susceptible population.The influenza vaccines that produce that get the Green Light at present mainly are the inactivated vaccines in Embryo Gallus domesticus source, and there are many deficiencies in this vaccine, and are high like production cost, the cycle is long; Anaphylaxis; The Embryo Gallus domesticus continuous passage can cause the virus antigenicity variation, and also there is the pollution of possible exogenous factor etc. in Embryo Gallus domesticus, if particularly bird flu outburst; Chicken crowd mortality, Embryo Gallus domesticus supply and output can become bottleneck.Therefore, the preparation of the influenza virus vaccine of various countries' development mammalian cell cultivation is actively recommended by World Health Organization (WHO).
At present, multiple mammalian cell is applied to the production of some viral vaccines, and generally acknowledge in the Vero cell whole world, the mdck cell U.S., Europe approval.And mdck cell is acknowledged as the only cell line of cultivation influenza virus; This cell is more responsive to influenza virus than other cells known today; Short time can obtain the virus of higher titre; The stability that keeps influenza antigen simultaneously, but mdck cell is not all-round sensitivity for the influenza vaccines Strain that annual WHO issues, and make the virus titer of producing still have the uncertain bottleneck that has become production of vaccine.It is different (Govorkova EA, Murti G, Meignier B with quantity that the type of the influenza virus receptor of bibliographical information mammalian cell of the same race surface existence is arranged; Taisne C DE, Webster RG.African Green Monkey Kidney (Vero) Cells Provide an AlternativeHost Cell System for Influenza A and B Viruses.J Virol, 1996; 70 (8) 5519-5524.), therefore, set up the cell monoclonal storehouse; The responsive monoclonal strain of screening virus; Obtain viral adaptability cell monoclonal, improve viral yield, can be the suitability for industrialized production influenza vaccines and lay the foundation.
Summary of the invention
The object of the present invention is to provide a kind of method for preparing of influenza virus vaccine, improve influenza virus output, make it be applicable to suitability for industrialized production.
A kind of method for preparing of influenza virus vaccine, carry out according to following steps:
(1) foundation in mammalian cell monoclonal storehouse
Mammalian cell is cultivated in culture bottle, treated that cell grows to degree of converging 70-90%, with trypsinization that contains EDTA and counting; Get 100 cell dilutions to the 20ml cell culture fluid, mixing is inoculated in 96 orifice plates; Every hole 200 μ l put in 37 ℃ of cell culture incubators and cultivate, and treat that cell grows to 40-60% degree of converging; Be transferred to after the digestion and continue in 24 orifice plates to cultivate; Each strain monoclonal cell transfer to a hole digests behind the 85-95% degree of converging to be grown to, is transferred in two 24 holes and continues to cultivate, and 85-95% degree of converging to be grown to carries out cell frozen;
(2) screening of viral high-adaptability cell monoclonal strain
Get monoclonal cell and be seeded to 24 orifice plates, overnight incubation is inhaled and is abandoned culture fluid, and PBS washes 2-6 time, adds influenza virus and TPCK-Trypsin, measures the blood clotting titre in the cells and supernatant behind 37 ℃ of cultivation 48-90h, and the blood clotting titre is greater than 2 8Be the strain of viral high-adaptability cell monoclonal;
(3) optimize the Virus culture condition
Get viral high-adaptability cell monoclonal strain shop to 24 orifice plates; Overnight incubation; Optimize temperature, the harvest time of Virus culture, amount and the MOI of infestation index of interpolation TPCK-Trypsin respectively, obtain virus optimum growh parameter in the strain of viral high-adaptability cell monoclonal;
(4) in bioreactor, cultivate the strain of viral high-adaptability cell monoclonal; Collect culture fluid after cultivating 48-90h; The culture fluid of collecting is concentrated through the ultrafilter membrane bag, SDGC purification, ultra from desaccharide, deactivation, is mixed with unit price or multivalence influenza vaccines behind the mensuration hemagglutinin content.
Said mammalian cell is MDCK MDCK, African green monkey kidney cell Vero, PER.C6 cell or human diploid cell.
Said influenza virus is influenza A virus, Influenza B virus or the reprovision Strain with influenza virus phenotype.
The mode of said bioreactor culture virus high-adaptability cell monoclonal strain is microcarrier suspension culture or carrier-free suspension culture.
Microcarrier in the said microcarrier suspension culture is a dextran microcarrier, and consumption is 10-20g/L.
Beneficial effect of the present invention: the present invention is through setting up cell monoclonal storehouse, screening viral high-adaptability cell monoclonal strain, using extensive bioreactor and carry out the mass cell cultured method and produce influenza virus vaccine; Overcome traditional Embryo Gallus domesticus and produce that the influenza vaccines production cost is high, the cycle is long; Anaphylaxis, Embryo Gallus domesticus continuous passage can cause shortcomings such as virus antigenicity variation; Improve viral yield greatly, safety, effective, stable.
Description of drawings
Fig. 1 is the blood clotting titre detection that the influenza A H1N1 influenza virus vaccine strain is cultivated in the strain of MDCK monoclonal cell.
Fig. 2 is the microphotograph that the viral adaptability cell monoclonal strain of large-scale culture is grown on microcarrier cytodex 3.
Fig. 3 is the electromicroscopic photograph behind the influenza virus purification of cell culture.
Fig. 4 is a SDS-PAGE electrophoretogram behind the influenza virus purification of cell culture;
Among the figure, the H1N1 influenza virus in M-albumen marker, 1-cell source, the H1N1 influenza virus in 2-Embryo Gallus domesticus source.
The specific embodiment
Below in conjunction with accompanying drawing and specific embodiment the present invention is further specified.
Embodiment 1
To screen the strain of influenza A H1N1 influenza virus vaccine strain (A/reassortant/NYMC X-179A) high-adaptability mdck cell monoclonal, to use this monoclonal cell strain production unit price influenza A H1N1 influenza virus vaccine is example.
(1) foundation in mdck cell monoclonal storehouse:
Will be from the mdck cell (p=53) of the biological article collecting center of Unite States Standard (ATCC) introduction at 75cm 2Cultivate in the culture bottle, treat that cell grows to degree of converging 80%,, get 100 cell dilutions to the 20ml cell culture fluid with trypsinization that contains EDTA and counting; Mixing is inoculated in 96 orifice plates, every hole 200 μ l; Put in 37 ℃ of cell culture incubators and cultivate, the next day, observe, and changes liquid in good time; Treat that cell grows to 50% degree of converging, be transferred to after the digestion and continue in 24 orifice plates to cultivate each strain monoclonal cell transfer to a hole; Wait to grow to digestion behind 90% degree of converging, be transferred in two 24 holes and continue to cultivate, wait to grow to 90% degree of converging and get an amount of cell and carry out frozenly, set up mdck cell monoclonal storehouse.
(2) the viral high-adaptability cell monoclonal of screening strain
The monoclonal cell of getting equal number is seeded to 24 orifice plates; Overnight incubation; Culture fluid is abandoned in suction, and PBS washes 3 times, adds equivalent influenza virus (10 μ l) and 1 μ g/ml TPCK-Trypsin with the cell maintenance medium dilution; Measure the blood clotting titre in the cells and supernatant behind 37 ℃ of cultivation 72h, the blood clotting titre is greater than 2 8Be influenza virus adaptability cell strain M77 (Fig. 1).
(3) optimize the Virus culture condition
High cell strain (M77) shop that adapts to of influenza virus of acquisition of getting equal number is to 24 orifice plates, and overnight incubation is optimized temperature, the harvest time of Virus culture, amount and infestation index (MOI=0.001,0.005,0.01 of interpolation TPCK-Trypsin respectively; 0.025,0.1,0.25,0.5; 1,1.5,2,3; 5,7), obtain influenza virus optimum growh parameter in adapted strain, thereby obtain the susceptible poison of more multithread.The influenza virus optimal culture conditions is: cultivation temperature is 37 ℃, adds 1 μ g/ml TPCK-Trypsin, and the MOI of infestation index is between 0.001 to 0.005, and viral harvest time is 72h.
(4) the large-scale culture cell is to cultivate influenza virus and vaccine production
The capital equipment that uses is the U.S. 7.5L of a NBS company bioreactor, and working volume is 4L.In the bioreactor tank body, add 40g cytodex 3 type microcarriers (GE Healthcare); Add 2L phosphate buffer PBS simultaneously; 8 pounds of high pressure 40min, emptying PBS adds 10% hyclone DMEM cell culture fluid; Adjustment bioreactor rotating speed, temperature and ventilation, overnight incubation in advance.The cell inoculation of 4 10 confluent monolayer cells factories of digestion is gone in the jar, and cultivation temperature is made as 37 ℃, and speed of agitator is made as 65rpm; Dissolved oxygen is made as 40%; PH is made as 7.4, cultivates, and 8h measures glucose content in the culture fluid at interval; Culture fluid in the drain tank when glucose content<1g/L renews bright culture fluid and continues to cultivate.Treat that cell covers with microcarrier (Fig. 2), all culture fluid in the drain tank uses Hank ' s liquid that tank body and microcarrier are washed 3 times, adds the cell maintenance medium 4L that contains 1 μ g/ml TPCK-Trypsin, inoculates influenza virus (MOI=0.001-0.005 of infestation index) simultaneously.8h measures and keeps the liquid concentration of glucose at interval, adds glucose when being lower than 1g/L to 4g/L, collects virus-culturing fluid behind the 72h, contains high concentration influenza virus (Fig. 3) in the culture fluid.The virus-culturing fluid of results is concentrated through 300kD molecular weight ultrafilter membrane bag, SDGC purification (electrophoresis detection behind the purification is as shown in Figure 4), ultra from desaccharide, formalin-inactivated, Triton X-100 cracking; The single expansion measured hemagglutinin content, is mixed with influenza vaccines according to 15 μ g HA (hemagglutinin)/agent.

Claims (5)

1. the method for preparing of an influenza virus vaccine is characterized in that, carries out according to following steps:
(1) foundation in mammalian cell monoclonal storehouse
Mammalian cell is cultivated in culture bottle, treated that cell grows to degree of converging 70-90%, with trypsinization that contains EDTA and counting; Get 100 cell dilutions to the 20ml cell culture fluid, mixing is inoculated in 96 orifice plates; Every hole 200 μ l put in 37 ℃ of cell culture incubators and cultivate, and treat that cell grows to 40-60% degree of converging; Be transferred to after the digestion and continue in 24 orifice plates to cultivate; Each strain monoclonal cell transfer to a hole digests behind the 85-95% degree of converging to be grown to, is transferred in two 24 holes and continues to cultivate, and 85-95% degree of converging to be grown to carries out cell frozen;
(2) screening of viral high-adaptability cell monoclonal strain
Get monoclonal cell and be seeded to 24 orifice plates, overnight incubation is inhaled and is abandoned culture fluid, and PBS washes 2-6 time, adds influenza virus and TPCK-Trypsin, measures the blood clotting titre in the cells and supernatant behind 37 ℃ of cultivation 48-90h, and the blood clotting titre is greater than 2 8Be the strain of viral high-adaptability cell monoclonal;
(3) optimize the Virus culture condition
Get viral high-adaptability cell monoclonal strain shop to 24 orifice plates; Overnight incubation; Optimize temperature, the harvest time of Virus culture, amount and the MOI of infestation index of interpolation TPCK-Trypsin respectively, obtain virus optimum growh parameter in the strain of viral high-adaptability cell monoclonal;
(4) in bioreactor, cultivate the strain of viral high-adaptability cell monoclonal; Collect culture fluid after cultivating 48-90h; The culture fluid of collecting is concentrated through the ultrafilter membrane bag, SDGC purification, ultra from desaccharide, deactivation, is mixed with unit price or multivalence influenza vaccines behind the mensuration hemagglutinin content.
2. according to the method for preparing of the said a kind of influenza virus vaccine of claim 1, it is characterized in that said mammalian cell is MDCK MDCK, African green monkey kidney cell Vero, PER.C6 cell or human diploid cell.
3. according to the method for preparing of the said a kind of influenza virus vaccine of claim 1, it is characterized in that said influenza virus is influenza A virus, Influenza B virus or the reprovision Strain with influenza virus phenotype.
4. according to the method for preparing of the said a kind of influenza virus vaccine of claim 1, it is characterized in that the mode of said bioreactor culture virus high-adaptability cell monoclonal strain is microcarrier suspension culture or carrier-free suspension culture.
5. according to the method for preparing of the said a kind of influenza virus vaccine of claim 4, it is characterized in that the microcarrier in the said microcarrier suspension culture is a dextran microcarrier, consumption is 10-20g/L.
CN2012100076872A 2012-01-11 2012-01-11 Preparation method of influenza virus vaccine Expired - Fee Related CN102526720B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2012100076872A CN102526720B (en) 2012-01-11 2012-01-11 Preparation method of influenza virus vaccine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2012100076872A CN102526720B (en) 2012-01-11 2012-01-11 Preparation method of influenza virus vaccine

Publications (2)

Publication Number Publication Date
CN102526720A true CN102526720A (en) 2012-07-04
CN102526720B CN102526720B (en) 2013-12-11

Family

ID=46335535

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2012100076872A Expired - Fee Related CN102526720B (en) 2012-01-11 2012-01-11 Preparation method of influenza virus vaccine

Country Status (1)

Country Link
CN (1) CN102526720B (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103160457A (en) * 2013-04-11 2013-06-19 山东信得动物疫苗有限公司 Large-scaled cell-culturing proliferating method and method for using proliferated cell in virus production
CN104046588A (en) * 2014-06-20 2014-09-17 马忠仁 Micro-carrier culture method of bioreactor of MDCK (Madin Darby Canine Kidney) cells and application thereof
CN106754722A (en) * 2016-11-10 2017-05-31 中国食品药品检定研究院 Vero cell line of stabilization expression bovine trypsinogen and application thereof

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1433472A (en) * 1999-11-26 2003-07-30 克鲁塞尔荷兰公司 Production of vaccines
CN101062411A (en) * 2006-04-24 2007-10-31 江苏延申生物科技股份有限公司 Method for producing influenza vaccine in large-scale by using bioreactor
CN101094915A (en) * 2004-05-20 2007-12-26 益得生物医学公司 Process for the production of an influenza vaccine
CN101189326A (en) * 2004-12-23 2008-05-28 米迪缪尼疫苗股份有限公司 Non-tumorigenic MDCK cell line for propagating viruses
CN101627113A (en) * 2006-09-15 2010-01-13 米迪缪尼有限公司 Mdck cell lines supporting viral growth to high titers and bioreactor process using the same

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1433472A (en) * 1999-11-26 2003-07-30 克鲁塞尔荷兰公司 Production of vaccines
CN101094915A (en) * 2004-05-20 2007-12-26 益得生物医学公司 Process for the production of an influenza vaccine
CN101189326A (en) * 2004-12-23 2008-05-28 米迪缪尼疫苗股份有限公司 Non-tumorigenic MDCK cell line for propagating viruses
CN101062411A (en) * 2006-04-24 2007-10-31 江苏延申生物科技股份有限公司 Method for producing influenza vaccine in large-scale by using bioreactor
CN101627113A (en) * 2006-09-15 2010-01-13 米迪缪尼有限公司 Mdck cell lines supporting viral growth to high titers and bioreactor process using the same

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103160457A (en) * 2013-04-11 2013-06-19 山东信得动物疫苗有限公司 Large-scaled cell-culturing proliferating method and method for using proliferated cell in virus production
CN103160457B (en) * 2013-04-11 2014-10-01 山东信得动物疫苗有限公司 Large-scaled cell-culturing proliferating method and method for using proliferated cell in virus production
CN104046588A (en) * 2014-06-20 2014-09-17 马忠仁 Micro-carrier culture method of bioreactor of MDCK (Madin Darby Canine Kidney) cells and application thereof
CN106754722A (en) * 2016-11-10 2017-05-31 中国食品药品检定研究院 Vero cell line of stabilization expression bovine trypsinogen and application thereof

Also Published As

Publication number Publication date
CN102526720B (en) 2013-12-11

Similar Documents

Publication Publication Date Title
CN102816732B (en) MDCK cell line suitable for full suspended serum-free culture and its application in culturing of influenza virus and production of influenza virus vaccines
CN102000326B (en) Method for producing rabies vaccine for human
CN101979517B (en) Method for producing influenza viruses in large scale by using bioreactor
CN102406931B (en) Pandemic influenza virus split vaccine
CN104001167A (en) Process for preparing avian influenza inactivated vaccine by full suspended culture cells and product
CN102911910A (en) Human embryo lung fibroblast strain and method for using human embryo lung fibroblast strain for producing hand-foot-mouth viral vaccine
CN102133398A (en) Method for industrially producing animal influenza vaccine by using bioreactor
CN102526720B (en) Preparation method of influenza virus vaccine
CN102178946A (en) Application of baby hamster kidney(BHK)-21 cell serum-free suspension culture technology in foot-and-mouth disease vaccine production
CN102861329A (en) Production method of canine parvovirus inactivated vaccine by utilizing bioreactor
CN102127524B (en) Method for proliferating avian influenza viruses in bioreactor with cell carrier
CN107988143A (en) One plant of BHK-21 cells Gs cell line
CN102732487B (en) Method for large scale cultivation in bioreactor
CN102676460B (en) Method for vaccinating avian influenza virus through microcarrier suspension culture cell
CN103468649B (en) Rapid adaptation method of rabies vaccine virus strains for human body on diploid cells of human body
CN105749270A (en) Rotavirus vaccine and preparation method thereof
CN103387958B (en) The application of human embryonic lung fibroblast SV-7 in virus culture
CN102002481A (en) Production method of porcine reproductive and respiratory syndrome virus
CN103146655A (en) Seed selection of high-immunogenicity rabies virus fixed strain and application thereof in vaccine development
CN102657859A (en) Method for producing avian influenza vaccine by using cells cultured by spherical microcarrier bioreactor
CN103468650A (en) Application of human embryonic lung fibroblast strains in preparation of rabies inactivated vaccine
CN103215233B (en) Optimized process method for amplifying enterovirus type 71 by use of bioreactor
CN103060276A (en) Preparation method for human diploid cell rabies vaccine virus solution
CN104694458B (en) MDCK clonal cell lines and its application
CN106399261A (en) Method for producing foot-and-mouth disease seed virus by suspension cultivation on BHK21 cells through microcarriers

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
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20131211

Termination date: 20210111

CF01 Termination of patent right due to non-payment of annual fee