CN104004814A - Method for precisely controlling monoclonal antibody product quality through animal cell fed-batch cultivation - Google Patents

Method for precisely controlling monoclonal antibody product quality through animal cell fed-batch cultivation Download PDF

Info

Publication number
CN104004814A
CN104004814A CN201310055762.7A CN201310055762A CN104004814A CN 104004814 A CN104004814 A CN 104004814A CN 201310055762 A CN201310055762 A CN 201310055762A CN 104004814 A CN104004814 A CN 104004814A
Authority
CN
China
Prior art keywords
culture
cell
monoclonal antibody
antibody
days
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.)
Pending
Application number
CN201310055762.7A
Other languages
Chinese (zh)
Inventor
段须杰
刘睿
徐卫涛
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.)
Jiangsu Simcere Pharmaceutical Co Ltd
Original Assignee
Jiangsu Simcere Pharmaceutical R&D Co Ltd
Jiangsu Simcere Pharmaceutical Co Ltd
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 Jiangsu Simcere Pharmaceutical R&D Co Ltd, Jiangsu Simcere Pharmaceutical Co Ltd filed Critical Jiangsu Simcere Pharmaceutical R&D Co Ltd
Priority to CN201310055762.7A priority Critical patent/CN104004814A/en
Publication of CN104004814A publication Critical patent/CN104004814A/en
Pending legal-status Critical Current

Links

Landscapes

  • Preparation Of Compounds By Using Micro-Organisms (AREA)
  • Micro-Organisms Or Cultivation Processes Thereof (AREA)

Abstract

The invention discloses a control strategy of the process of cultivating and producing monoclonal antibody medicine through mammal cells. The modes of lowering cultivation temperature, shortening the cultivation cycle and the like are adopted, so that post-translational modifying features, such as charge distribution and glycoform, of monoclonal antibodies are effectively controlled. The process has the advantages of being good in stability, high in operability, little in difference between batches, and the application range of the process is greatly widened.

Description

Adopt zooblast feeding culture mode accurately to control the method for monoclonal antibody quality product
Technical field
The present invention relates to animal cell culture field.More specifically, the present invention relates to a kind of method that adopts zooblast feeding culture mode accurately to control monoclonal antibody quality product.
Background technology
Animal cell culture starts from the beginning of this century, to scale in 1962, start to expand, be developed so far and become the technological method extensively adopting in biology, medical research and application, utilize animal cell culture to produce monoclonal antibody, vaccine and the somatomedin etc. with important medical value, become the integral part of medicine bioengineering hi-tech industry.Due to the biological characteristics of zooblast vitro culture, the complicacy of related products structure and quality and coherence request, animal cell large-scale culture technique is still difficult to meet the demand of the scale production with important medical value biological products, in the urgent need to further research and development cell cultures technique.
Animal cell culture training method mainly contains three kinds, batch cultivation, feeding culture and perfusion culture.Also have such as the mixed mode (Hybrid) being undertaken by the ATF system of U.S. Refine company and cultivate in recent years.For batch cultivation, in reactor, add supplemented medium continuously or off and on, in the Extending culture cycle, obtain higher cell density and antibody production.And perfusion culture culture cycle is longer, conventionally, at 2-3 month, therefore culture process is had relatively high expectations, be suitable for the production of less stable protein drug.
Charge distribution and glycosylation be as the important indicator of protein post-translational modification, for folding, transportation and the location of protein, plays an important role, closely related with recombinant glycoprotein biological activity, transformation period and katabolism etc. in vivo.The charge distribution of protein and glycosylation process are subject to the impact of several factors, comprise the difference of cell category, substratum, the control of the difference of culturing process, the transhipment time of golgi body, the utilization of the precursor substances such as the state of cell and intracellular nucleic acid etc.By optimal conditions, improve the glycosylation of protein, guarantee the consistence of Protein Glycosylation Overview between different batches, will greatly increase the result for the treatment of of recombinant glycoprotein medicine.
Culture temperature, as the important control parameter of animal cell culture, directly has influence on output and the quality of monoclonal antibody.By optimizing culture temperature, can improve the output of monoclonal antibody, can change the charge distribution of antibody simultaneously, affect the ratio of acidic components and basic component, and then affect antibody pharmacokinetics behavior in animal body.Culture cycle is also most important for cell cultures, and along with the prolongation of culture cycle, cell density and motility rate decline gradually, and metabolism toxic byproduct builds up, and the glycosylation of antagonist produces material impact.High mannose can be accelerated antibody removing in animal body, shortens the transformation period, and may produce immunogenicity, and then affect the effect of antibody.Research shows, along with the prolongation of culture cycle, the ratio regular meeting of high mannose increases gradually.Therefore control the suitable production cycle extremely important for obtaining high-quality antibody.
Summary of the invention
The object of the present invention is to provide a kind of method that adopts zooblast feeding culture mode accurately to control monoclonal antibody quality product.
In order to solve the problems of the technologies described above, technical scheme provided by the invention is:
Technical scheme provided by the invention comprises the steps:
(1) cell cultures initial temperature 36-37 ℃, cultivates 5-8 days, adds fed-batch medium when Chinese hamster ovary celI grows to suitable density, carries out feeding culture;
(2) when Growth of Cells approaches plateau, reduce temperature to 31-33 ℃, carry out feeding culture, reduce temperature and finish cell cultures after 2-7 days.
After experiment finishes, carry out antibody charge distribution and sugared type ratio and detect, control antibody acidic components and be less than 25%, high mannose ratio is less than 5%.
In one embodiment, the cell inoculum density of described method is 0.3-0.6*10 6cells/ml, PH scope 6.7-7.4, dissolved oxygen 30-50% air saturation, mixing speed 50-300rpm.
In another embodiment, described method dissolved oxygen 40% air saturation, mixing speed 80-250rpm.
In another embodiment, the culture cycle of described method is 7-15 days.
The present invention selects feeding culture mode to carry out monoclonal antibody expression, reduces culture temperature between when appropriate, and selects the appropriate incubation cycle, to reach charge distribution and the glycosylation feature of accurate control antibody.
Culture temperature is a key factor that affects antibody producing.Zooblast growth is conventionally 37 ℃ of left and right.With this understanding, cell proliferation rate is very fast.After temperature declines, cellular metabolism is slack-off gradually, and in maintenance phase, cell can keep higher motility rate, now take and expresses antibody as main.In addition, temperature also can affect the charge distribution of antibody.For example, reduce the acidic components that temperature can reduce antibody.
Culture cycle is another important factor that affects antibody producing.Along with the prolongation of culture cycle, declining all appears in cell density and motility rate, and metabolism toxic byproduct builds up, and the deterioration of culture environment can affect the glycosylation feature of antibody.Research discovery, the ratio of high mannose increases along with the prolongation of culture cycle.Therefore shorten the ratio that culture cycle is conducive to reduce high mannose.
Present method adopts control by stages strategy.
First stage, i.e. step (1), cell cultures initial temperature is controlled at 36-37 ℃, cultivates 4-8 days, and cell Fast Growth is to plateau, to obtaining higher cell density;
Subordinate phase, step (2), reduces temperature to 31-33 ℃, reduces cellular metabolism on the one hand, maintains higher Cell viability, and enhancing antibody is synthetic on the other hand, reduces the acidic components of antibody simultaneously, and is conducive to the stable of albumen.
The present invention adopts feeding culture mode to carry out monoclonal antibody expression, has process stabilizing good stability, workable, batch between little etc. the feature of difference, be very suitable for animal cell culture manufacture order clonal antibody.
Accompanying drawing explanation
Fig. 1 display segment is cultivated and contrast culture cell density comparison diagram.
Fig. 2 display segment is cultivated and contrast culture antibody expression amount comparison diagram.
Fig. 3 display segment is cultivated and contrast culture charge distribution comparison diagram.
Fig. 4 display segment is cultivated and contrast culture high mannose ratio comparison diagram.
Fig. 5 display segment is cultivated and contrast culture cell density comparison diagram.
Fig. 6 display segment is cultivated and contrast culture cell density comparison diagram.
Fig. 7 display segment is cultivated and contrast culture antibody production comparison diagram.
Embodiment
The invention will be further described in description below in conjunction with accompanying drawing by embodiment, but this is not limitation of the present invention, those skilled in the art are according to basic thought of the present invention, can make various modifications and improvement, but only otherwise depart from basic thought of the present invention, all within the scope of the present invention.
Embodiment 1CHO cell expressing monoclonal antibody A
1. material: the Chinese hamster ovary celI strain (ATCC) of stably express monoclonal antibody A, commercial base substratum and supplemented medium (U.S. Thermo Fisher company, U.S. Life Technologies company).
2. bio-reactor:
3L glass biological reaction device (Dutch Applikon company), 500L disposable bioreactor (U.S. match Mo Feishier company)
3.3L reactor cell cultures sectionalized control method:
The Chinese hamster ovary celI strain of stably express monoclonal antibody A, inoculum density 0.3-0.6*10 6cells/ml, 36.5 ± 0.5 ℃ of initial culture temperature, pH is controlled at 6.7-7.4, mixing speed 150rpm, dissolved oxygen 40% air saturation, is cultured to the 5th day and reduces temperature to 32.5 ± 0.5 ℃, culture cycle 10-11 days.
4.3L reactor cell cultures sectionalized control method and the comparison of contrast culture method:
(1) contrast culture method: the Chinese hamster ovary celI strain of stably express monoclonal antibody A, inoculum density 0.3-0.6*10 6cells/ml, 36.5 ± 0.5 ℃ of initial culture temperature, pH is controlled at 6.7-7.4, mixing speed 150rpm, dissolved oxygen 40% air saturation, culturing process maintains steady temperature.
(2) segmentation culture method and contrast culture method cell density are measured: the conventional counting method of blood cell that adopts of cell cultures counting detects cell density, the results are shown in accompanying drawing 1.
(3) segmentation culture method and the flow measurement of contrast culture method protein expression: cultivate the 9th, 10,11 days, adopt ProteinA affinity chromatography method to measure, the results are shown in accompanying drawing 2.
(4) segmentation culture method and contrast culture method charge distribution detect: adopt high performance liquid phase ion exchange chromatography (WCX stratographic analysis post), the results are shown in accompanying drawing 3.
(5) segmentation culture method and contrast culture method sugar type analysis: with reference to commercially available 2-AB marker detection test kit (U.S. Glyko company), the results are shown in accompanying drawing 4.
(6) result comparison
The comparison of cell density: in two kinds of cell culture processes, from the 1st day to the 5th day, cell was all in vigorous vegetative period; The 5th day Growth of Cells approaches high-density; After this, Growth of Cells is in maintenance phase, and cell density curve presents a plateau, the high-density no significant difference of two kinds of method cells, and segmentation culture method is cultivated density while finishing higher than contrast culture method, sees accompanying drawing 1.
Antibody expression amount comparison: in two kinds of cell culture processes, the 9th, 10,11 days, the expressing quantity of segmentation culture method all, higher than contrast culture method approximately 25%, was shown in accompanying drawing 2.
Charge distribution comparison: in two kinds of cell culture processes, the 9th, 10,11 days, the acidic components proportion of segmentation culture method antibody was starkly lower than contrast culture method, sees accompanying drawing 3.
Sugar type analysis comparison: in two kinds of cell culture processes, along with the prolongation of incubation time, high mannose ratio increases gradually, and segmentation culture method, compared with contrast culture Fa Lvegao, reaches 7% left and right, sees accompanying drawing 4.Because antibody production under segmentation culture condition is higher, and acidic components ratio is lower, therefore by shortening the method for culture cycle, effectively controls the seminose ratio of antibody.
The 500L one-time reaction device cell culture processes of culture cycle is cultivated and is shortened in 5 segmentations:
The Chinese hamster ovary celI strain of stably express monoclonal antibody A, inoculum density 0.3-0.6*10 6cells/ml, 36.5 ± 0.5 ℃ of initial culture temperature, pH is controlled at 6.7-7.4, mixing speed 80rpm, dissolved oxygen 40% air saturation, cultivates and within the 5th day, reduces temperature to 33 ℃, culture cycle 7 days.
Cultivation results:
Cell density: cultivate cooling in the 5th day, cell arrives high-density, and after this Growth of Cells is in maintenance phase, and Growth of Cells presents plateau, sees accompanying drawing 5.
Expressing quantity: cultivate the 7th day, antibody production is 262mg/L.
Antibody charge distribution: cultivate the 7th day, acidic components ratio is 19.0%.
Sugar type analysis: cultivate the 7th day, high mannose ratio is 4.2%.
Embodiment 2CHO cell expressing monoclonal antibody B
1. material:
The Chinese hamster ovary celI strain (ATCC) of stably express monoclonal antibody B, commercial base substratum and supplemented medium (U.S. Thermo Fisher company, U.S. Life Technologies company).
2. bio-reactor
3L glass biological reaction device (Dutch Applikon company).
3.CHO cell segmentation culture method:
By the Chinese hamster ovary celI strain of stably express monoclonal antibody B, inoculum density 0.3-0.6*10 6cells/ml, 36.5 ± 0.5 ℃ of initial culture temperature, pH is controlled at 6.7-7.4, mixing speed 250rpm, dissolved oxygen 40% air saturation, is cultured to the 3rd day and starts flow feeding substratum, be cultured to the 8th day and reduce temperature to 31.5 ± 0.5 ℃, culture cycle 14-15 days.
4. the present invention reaches the object that improves product production and improve quality product by segmentation culture method.
(1) contrast culture method, cell cultures temperature maintains 36.5 ± 0.5 ℃, and other culture condition are identical with cooling culture method.
(2) segmentation culture method and contrast culture method cell density are measured: the conventional counting method of blood cell that adopts of cell cultures counting detects cell density, the results are shown in accompanying drawing 6.
(3) segmentation culture method and the flow measurement of contrast culture method protein expression: adopt ProteinA affinity chromatography method to measure, the results are shown in accompanying drawing 7.
(4) segmentation culture method and contrast culture method charge distribution are measured: adopt high performance liquid phase ion exchange chromatography (WCX stratographic analysis post), the results are shown in accompanying drawing 3.
(5) result comparison
Compare with contrast culture technique, segmentation is cultivated and obviously to be extended cell plateau, cultivates 15 days Cell viabilities still more than 75%, and expression amount can reach 1.63g/L, and output improves approximately 25%.After cooling, antibody acidic components also have obvious reduction.In addition, under two kinds of culture condition, high mannose ratio is all less than 6%, the results are shown in Table 1.
Table 1
Culture process Acidic components ratio (%) High mannose ratio (%)
Segmentation is cultivated 11.0 4.1
Contrast culture 15.3 4.9

Claims (4)

1. one kind adopts stream of cells to add the method that training method is prepared monoclonal antibody, it is characterized in that described method comprises the steps: 1) cell cultures initial temperature is 36-37 ℃, cultivate 5-8 days, when Chinese hamster ovary celI grows to suitable density, add fed-batch medium, carry out feeding culture; 2) reduce temperature to 31-33 ℃, carry out feeding culture, reduce temperature and finish cell cultures after 2-7 days.
2. method according to claim 1, is characterized in that, the cell inoculum density of described method is 0.3-0.6*10 6cells/ml, PH scope 6.7-7.4, dissolved oxygen 30-50% air saturation, mixing speed 50-300rpm.
3. method according to claim 1, is characterized in that, described method dissolved oxygen 40% air saturation, mixing speed 80-250rpm.
4. method according to claim 1, is characterized in that, the culture cycle of described method is 7-15 days.
CN201310055762.7A 2013-02-21 2013-02-21 Method for precisely controlling monoclonal antibody product quality through animal cell fed-batch cultivation Pending CN104004814A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201310055762.7A CN104004814A (en) 2013-02-21 2013-02-21 Method for precisely controlling monoclonal antibody product quality through animal cell fed-batch cultivation

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201310055762.7A CN104004814A (en) 2013-02-21 2013-02-21 Method for precisely controlling monoclonal antibody product quality through animal cell fed-batch cultivation

Publications (1)

Publication Number Publication Date
CN104004814A true CN104004814A (en) 2014-08-27

Family

ID=51365720

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201310055762.7A Pending CN104004814A (en) 2013-02-21 2013-02-21 Method for precisely controlling monoclonal antibody product quality through animal cell fed-batch cultivation

Country Status (1)

Country Link
CN (1) CN104004814A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107904200A (en) * 2017-10-20 2018-04-13 通化东宝生物科技有限公司 A kind of Combined culture base for expressing adalimumab and its application
CN108463730A (en) * 2015-11-05 2018-08-28 格纳西尼有限公司 Including the composition of recombinant human thyroid-stimulating hormone and the method for producing recombinant human thyroid-stimulating hormone
CN112011514A (en) * 2019-05-31 2020-12-01 百济神州(苏州)生物科技有限公司 Cell culture process for improving ADCC activity of antibody

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20050272124A1 (en) * 1994-03-10 2005-12-08 Genentech, Inc. Polypeptide production in animal cell culture
CN1869214A (en) * 2005-05-24 2006-11-29 中国人民解放军军事医学科学院基础医学研究所 Method for high efficiency expressing destination protein
US20070092947A1 (en) * 2005-10-20 2007-04-26 Immunomedics, Inc. Methods and compositions for increasing longevity and protein yield from a cell culture
CN101205530A (en) * 2006-12-20 2008-06-25 上海国健生物技术研究院 Method for high-effectively expressing recombinant protein by employing animal cell fed-batch culture mode
CN102021217A (en) * 2006-12-20 2011-04-20 上海国健生物技术研究院 Method for high efficient expression of monoclonal antibody by means of animal cell fed-batch culture
WO2011095596A1 (en) * 2010-02-04 2011-08-11 Vivalis Fed-batch process using concentrated cell culture medium for the efficient production of biologics in eb66 cells
CN102382794A (en) * 2010-09-01 2012-03-21 山东新时代药业有限公司 Perfusion culture method of mammal cell
CN102559577A (en) * 2010-12-09 2012-07-11 上海中信国健药业股份有限公司 Method for culturing anti-CD25 humanized monoclonal antibodies

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20050272124A1 (en) * 1994-03-10 2005-12-08 Genentech, Inc. Polypeptide production in animal cell culture
CN1869214A (en) * 2005-05-24 2006-11-29 中国人民解放军军事医学科学院基础医学研究所 Method for high efficiency expressing destination protein
US20070092947A1 (en) * 2005-10-20 2007-04-26 Immunomedics, Inc. Methods and compositions for increasing longevity and protein yield from a cell culture
CN101205530A (en) * 2006-12-20 2008-06-25 上海国健生物技术研究院 Method for high-effectively expressing recombinant protein by employing animal cell fed-batch culture mode
CN102021217A (en) * 2006-12-20 2011-04-20 上海国健生物技术研究院 Method for high efficient expression of monoclonal antibody by means of animal cell fed-batch culture
WO2011095596A1 (en) * 2010-02-04 2011-08-11 Vivalis Fed-batch process using concentrated cell culture medium for the efficient production of biologics in eb66 cells
CN102382794A (en) * 2010-09-01 2012-03-21 山东新时代药业有限公司 Perfusion culture method of mammal cell
CN102559577A (en) * 2010-12-09 2012-07-11 上海中信国健药业股份有限公司 Method for culturing anti-CD25 humanized monoclonal antibodies

Non-Patent Citations (5)

* Cited by examiner, † Cited by third party
Title
D. K. ROBINSON等: "Optimization of a Fed-batch Process for Production of a Recombinant Antibody", 《ANNALS OF THE NEW YORK ACADEMY OF SCIENCES》 *
SUNG KWAN YOON等: "Effect of Low Culture Temperature on Specific Productivity, Transcription Level,and Heterogeneity of Erythropoietin in Chinese Hamster Ovary Cells", 《BIOTECHNOLOGY & BIOENGINEERING》 *
元英进: "《制药工艺学》", 30 June 2007, 化学工业出版社 *
翁志兵: "抗CD3人源化单克隆抗体培养优化及大规模培养工艺研究", 《中国优秀硕士学位论文全文数据库 工程科技Ⅰ辑》 *
魏明旺等: "动物细胞大规模培养的主流技术", 《生物产业技术》 *

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108463730A (en) * 2015-11-05 2018-08-28 格纳西尼有限公司 Including the composition of recombinant human thyroid-stimulating hormone and the method for producing recombinant human thyroid-stimulating hormone
CN107904200A (en) * 2017-10-20 2018-04-13 通化东宝生物科技有限公司 A kind of Combined culture base for expressing adalimumab and its application
CN107904200B (en) * 2017-10-20 2018-10-16 通化东宝生物科技有限公司 It is a kind of expression adalimumab Combined culture base and its application
CN112011514A (en) * 2019-05-31 2020-12-01 百济神州(苏州)生物科技有限公司 Cell culture process for improving ADCC activity of antibody

Similar Documents

Publication Publication Date Title
CN103773732B (en) The production technology of definite culture medium, its application and the large-scale culture mammalian cell of a kind of chemical composition
JP2016214254A (en) Improved cell culture media
CN107267462B (en) Serum-free culture medium for inducing pluripotent stem cells to rapidly generate
US20200255785A1 (en) Online biomass capacitance monitoring during large scale production of polypeptides of interest
CN101663391A (en) Cell culture method using amino acid-enriched medium
CN106987554A (en) Suspension cell strain and its acclimation method
CN104560882B (en) A kind of Chinese hamster ovary celI culture process for reducing acidic variants content
CN104004814A (en) Method for precisely controlling monoclonal antibody product quality through animal cell fed-batch cultivation
CN102382794B (en) Perfusion culture method of mammal cell
CN106244527B (en) Source of people iPS stem cell in vitro directed differentiation is the kit and method of cardiac muscle cell
CN101831403B (en) Method for amplifying mesenchymal stem cells of human umbilical cord and placenta in vitro
CN101270380A (en) Screening method for hybrid tumor cell monoclonal preparation
CN101333513B (en) Non-blood serum low density culture medium for animal cell and use thereof
CN112725223B (en) Method for improving plasmid fermentation yield
Rhiel et al. On‐line monitoring of human prostate cancer cells in a perfusion rotating wall vessel by near‐infrared spectroscopy
CN104894054A (en) Monkey embryo renal epithelial cell Marc-145 suspension adapted strain and application thereof in culture of PRRSV (porcine reproductive and respiratory syndrome virus) and production of PRRSV vaccine
Kresnowati et al. Model-based analysis and optimization of bioreactor for hematopoietic stem cell cultivation
CN109576212B (en) Culture method of seed cells in high-density inoculation culture and application thereof
CN101974435B (en) Method for quickly screening neomycin strain breeding
CN102021217B (en) Method for high efficient expression of monoclonal antibody by means of animal cell fed-batch culture
CN102660505B (en) Subcloned cell strain TF-1-A2, preparation method thereof and application
CN112063562A (en) Escherichia coli fermentation method for efficiently expressing supercoiled plasmid DNA
CN102965334B (en) Mouse fetal liver cell PL08, its establishment method and application in culture and proliferation of erythroid progenitors
TWI555847B (en) Culture and production of adipose - derived stem cells and their stem cell secretions
CN102604884B (en) Fermentation culture method of cells

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C41 Transfer of patent application or patent right or utility model
TA01 Transfer of patent application right

Effective date of registration: 20160712

Address after: 210042 Xuanwu District, Xuanwu District, Jiangsu, Nanjing No. 699 -18

Applicant after: Jiangsu Simcere Pharmaceutical Co., Ltd.

Address before: 210042 Xuanwu District, Xuanwu District, Jiangsu, Nanjing No. 699 -18

Applicant before: Jiangsu Simcere Pharmaceutical Research Company Limited

Applicant before: Jiangsu Simcere Pharmaceutical Co., Ltd.

RJ01 Rejection of invention patent application after publication
RJ01 Rejection of invention patent application after publication

Application publication date: 20140827