CN110117527A - A kind of reinforcing discharge method of stem cell metabolic waste - Google Patents

A kind of reinforcing discharge method of stem cell metabolic waste Download PDF

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Publication number
CN110117527A
CN110117527A CN201910403670.0A CN201910403670A CN110117527A CN 110117527 A CN110117527 A CN 110117527A CN 201910403670 A CN201910403670 A CN 201910403670A CN 110117527 A CN110117527 A CN 110117527A
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stem cell
metabolic waste
cell metabolic
culture solution
metabolin
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华子昂
刘宝全
竹添
张建
王姣
林伟阳
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Harbin University Of Technology International Stem Cell Engineering Research Institute Co ltd
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    • C12MAPPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M29/00Means for introduction, extraction or recirculation of materials, e.g. pumps
    • C12M29/04Filters; Permeable or porous membranes or plates, e.g. dialysis
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    • C12M29/00Means for introduction, extraction or recirculation of materials, e.g. pumps
    • C12M29/18External loop; Means for reintroduction of fermented biomass or liquid percolate
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    • C12N5/00Undifferentiated human, animal or plant cells, e.g. cell lines; Tissues; Cultivation or maintenance thereof; Culture media therefor
    • C12N5/06Animal cells or tissues; Human cells or tissues
    • C12N5/0602Vertebrate cells
    • C12N5/0652Cells of skeletal and connective tissues; Mesenchyme
    • C12N5/0662Stem cells
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    • C12N2513/003D culture

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Abstract

A kind of reinforcing discharge method of stem cell metabolic waste, the present invention relates to the discharge methods of stem cell metabolic waste.Solve the problem of that stem cell metabolic waste can not be discharged in time in the extensive 3D culture systems of existing stem cell.Method: one, culture solution containing stem cell metabolic waste is introduced into buffer container;Two, membrane module is selected;Three, pressurized circulation system makes the culture solution containing stem cell metabolic waste by the specific selection in membrane module through film, then the culture solution for removing stem cell metabolin is returned in buffer container, the stem cell metabolic waste isolated is transported in recyclable device by the discharge system of stem cell metabolic waste;Four, nutrition composition is added to the culture solution of removing stem cell metabolin, subsequently into stem cell incubator.The present invention is used for the reinforcing discharge method of stem cell metabolic waste.

Description

A kind of reinforcing discharge method of stem cell metabolic waste
Technical field
The present invention relates to the discharge methods of stem cell metabolic waste.
Background technique
In recent years, international, domestic stem cell market development is rapid, and stem cell clinical treatment is done by public recognition and acceptance Cell requirements are constantly promoted.Stem cell culture develops from 2D to 3D, makes great efforts the output for expanding stem cell.In the big rule of stem cell In mould 3D culture systems, sufficiently grow in order to which stem cell is effectively ensured it is necessary that in cultivating system (stem cell incubator) Stem cell metabolic waste must be discharged in time, otherwise just will affect stem cell growth, even cause stem cell dead.Pass through merely Replacement culture solution is able to solve the discharge of stem cell metabolic waste, but will cause the huge waste of culture solution simultaneously.
Summary of the invention
The invention solves in the extensive 3D culture systems of existing stem cell, stem cell metabolic waste can not be discharged in time The problem of, and a kind of reinforcing discharge method of stem cell metabolic waste is provided.
A kind of reinforcing discharge method of stem cell metabolic waste is to sequentially include the following steps:
One, the culture solution containing stem cell metabolic waste is introduced into buffer container;
In the culture solution containing stem cell metabolic waste, stem cell metabolic waste is ammonia, lactic acid class and titanium dioxide One of carbon or in which several mixing;
When the described stem cell metabolic waste when containing ammonia, the concentration of ammonia is greater than in the culture solution containing stem cell metabolic waste 3mmol/L;
When the stem cell metabolic waste class containing lactic acid, lactic acid class in the culture solution containing stem cell metabolic waste Concentration is greater than 24.8mmol/L;
When the stem cell metabolic waste carbonated, titanium dioxide in the culture solution containing stem cell metabolic waste The concentration of carbon is greater than 40%;
Two, membrane module is selected;
Three, the discharge system of pressurized circulation system and stem cell metabolic waste is established, pressurized circulation system makes containing dry The culture solution of cell metabolism waste penetrates film by the specific selection in membrane module, then will remove the training of stem cell metabolin Nutrient solution returns in buffer container, and the stem cell metabolic waste isolated is transported to back by the discharge system of stem cell metabolic waste In receiving apparatus;
Four, nutrition composition is added to the culture solution of removing stem cell metabolin, it is subsequently into stem cell incubator, i.e., complete At a kind of reinforcing discharge method of stem cell metabolic waste.
The beneficial effects of the present invention are:
The culture solution containing stem cell metabolic waste is placed in a buffer container using the present invention, it will using membrane technology Stem cell metabolic waste in culture solution selectively removes, then the nutrition composition of stem cell culture is added into culture solution, circulation Using stem cell medium, guarantee the reinforcing discharge of stem cell metabolic waste, culture solution dosage reduces 50%~75%, effectively drops Low stem cell toxigenic capacity 30%~75%.
The present invention is used for a kind of reinforcing discharge method of stem cell metabolic waste.
Specific embodiment
Specific embodiment 1: a kind of reinforcing discharge method of stem cell metabolic waste of present embodiment is according to the following steps It carries out:
One, the culture solution containing stem cell metabolic waste is introduced into buffer container;
In the culture solution containing stem cell metabolic waste, stem cell metabolic waste is ammonia, lactic acid class and titanium dioxide One of carbon or in which several mixing;
When the described stem cell metabolic waste when containing ammonia, the concentration of ammonia is greater than in the culture solution containing stem cell metabolic waste 3mmol/L;
When the stem cell metabolic waste class containing lactic acid, lactic acid class in the culture solution containing stem cell metabolic waste Concentration is greater than 24.8mmol/L;
When the stem cell metabolic waste carbonated, titanium dioxide in the culture solution containing stem cell metabolic waste The concentration of carbon is greater than 40%;
Two, membrane module is selected;
Three, the discharge system of pressurized circulation system and stem cell metabolic waste is established, pressurized circulation system makes containing dry The culture solution of cell metabolism waste penetrates film by the specific selection in membrane module, then will remove the training of stem cell metabolin Nutrient solution returns in buffer container, and the stem cell metabolic waste isolated is transported to back by the discharge system of stem cell metabolic waste In receiving apparatus;
Four, nutrition composition is added to the culture solution of removing stem cell metabolin, it is subsequently into stem cell incubator, i.e., complete At a kind of reinforcing discharge method of stem cell metabolic waste.
The culture solution that present embodiment removes stem cell metabolin returns in buffer container, after adding nutrition composition Nutrition is provided into stem cell incubator for stem cell.
Present embodiment completes the discharge of specific stem cell metabolic waste using the permselective membrane of specificity.
The reinforcing discharge method of present embodiment stem cell metabolic waste is applied to stem cell and cultivates field.
Present embodiment makes the stem cell metabolic waste in stem cell medium selectively using membrane separation technique Discharge, while retaining the nutrition composition in stem cell medium (function ingredients) recycling, the culture of stem cell is effectively reduced Cost;Core is to select optimum seperation film for stem cell metabolin.
The beneficial effect of present embodiment is: using present embodiment by the training containing stem cell metabolic waste Nutrient solution is placed in a buffer container, is selectively removed the stem cell metabolic waste in culture solution using membrane technology, then Xiang Pei The nutrition composition of stem cell culture is added in nutrient solution, stem cell medium is recycled, and guarantees the reinforcing of stem cell metabolic waste Discharge, culture solution dosage reduce 50%~75%, stem cell toxigenic capacity 30%~75% are effectively reduced.
Specific embodiment 2: the present embodiment is different from the first embodiment in that: it is special described in step 3 Property permselective membrane be hollow-fibre membrane or rolled film.It is other same as the specific embodiment one.
Specific embodiment 3: unlike one of present embodiment and specific embodiment one or two: institute in step 3 The concentration of ammonia is less than 2mmol/L in the culture solution for the removing stem cell metabolin stated;Removing stem cell generation described in step 3 The concentration for thanking to lactic acid class in the culture solution of object is less than 24.8mmol/L;The culture of stem cell metabolin is removed described in step 3 The concentration of carbon dioxide is less than 40% in liquid.It is other the same as one or two specific embodiments.
Specific embodiment 4: unlike one of present embodiment and specific embodiment one to three: institute in step 3 The pressurized circulation system stated is the pressurized circulation system that control valve and peristaltic pump cooperatively form.It is other with specific embodiment one to Three is identical.
Specific embodiment 5: unlike one of present embodiment and specific embodiment one to four: institute in step 3 The recyclable device stated is the recyclable device equipped with recovered liquid.It is other identical as specific embodiment one to four.
Beneficial effects of the present invention are verified using following embodiment:
Embodiment one:
A kind of reinforcing discharge method of stem cell metabolic waste is to sequentially include the following steps:
One, in sterile clean culture environment, the culture solution containing stem cell metabolic waste is introduced into buffer container;
The stem cell metabolic waste is ammonia, and the concentration of ammonia is greater than in the culture solution containing stem cell metabolic waste 3mmol/L;
Two, membrane module is selected;
Three, the discharge system of pressurized circulation system and stem cell metabolic waste is established, pressurized circulation system makes containing dry The culture solution of cell metabolism waste penetrates film by the specific selection in membrane module, then will remove the training of stem cell metabolin Nutrient solution returns in buffer container, and the stem cell metabolic waste isolated is transported to back by the discharge system of stem cell metabolic waste In receiving apparatus;
Four, nutrition composition is added to the culture solution of removing stem cell metabolin, it is subsequently into stem cell incubator, i.e., complete At a kind of reinforcing discharge method of stem cell metabolic waste.
The concentration that ammonia in the culture solution of stem cell metabolin is removed described in step 3 is less than 2mmol/L;
Specific selection described in step 3 is the hollow-fibre membrane for removing ammonia through film;It is special described in step 3 Property permselective membrane purchase scientific and technological (Xiamen) Co., Ltd at the beginning of state;
Pressurized circulation system described in step 3 is the pressurized circulation system that control valve and peristaltic pump cooperatively form.
Recyclable device described in step 2 is the recyclable device equipped with acid recovery liquid.
The present embodiment method needs to keep system sterile.
The present embodiment effectively improves the service efficiency of stem cell medium, conventional stem cell medium dosage from 15 liters/ Batch is reduced to 4 liters/batch, and stem cell toxigenic capacity is effectively reduced, and the toxigenic capacity of 70,000,000 stem cells is dropped from about 80,000 Down to 40,000.
Embodiment two:
One, in sterile clean culture environment, the culture solution containing stem cell metabolic waste is introduced into buffer container;
The stem cell metabolic waste is lactic acid, and the concentration of lactic acid is greater than in the culture solution containing stem cell metabolic waste 30mmol/L;
Two, membrane module is selected;
Three, the discharge system of pressurized circulation system and stem cell metabolic waste is established, pressurized circulation system makes containing dry The culture solution of cell metabolism waste penetrates film by the specific selection in membrane module, then will remove the training of stem cell metabolin Nutrient solution returns in buffer container, and the stem cell metabolic waste isolated is transported to back by the discharge system of stem cell metabolic waste In receiving apparatus;
Four, nutrition composition is added to the culture solution of removing stem cell metabolin, it is subsequently into stem cell incubator, i.e., complete At a kind of reinforcing discharge method of stem cell metabolic waste.
The concentration that lactic acid class in the culture solution of stem cell metabolin is removed described in step 3 is less than 24.8mmol/L;
Specific selection described in step 3 is the rolled film for removing lactic acid through film;Specificity described in step 3 Permselective membrane purchase scientific and technological (Xiamen) Co., Ltd at the beginning of state;
Pressurized circulation system described in step 3 is the pressurized circulation system that control valve and peristaltic pump cooperatively form.
The present embodiment method needs to keep system sterile.
The present embodiment effectively improves the service efficiency of stem cell medium, conventional stem cell medium dosage from 14 liters/ Batch is reduced to 4 liters/batch, is effectively reduced stem cell toxigenic capacity, and the toxigenic capacities of 70,000,000 stem cells is from about 6~8 Ten thousand are reduced to 1.8~2.4 ten thousand.
Embodiment three:
A kind of reinforcing discharge method of stem cell metabolic waste is to sequentially include the following steps:
One, in sterile clean culture environment, the culture solution containing stem cell metabolic waste is introduced into buffer container;
The stem cell metabolic waste is carbon dioxide, carbon dioxide in the culture solution containing stem cell metabolic waste Concentration is greater than 40%;
Two, membrane module is selected;
Three, the discharge system of pressurized circulation system and stem cell metabolic waste is established, pressurized circulation system makes containing dry The culture solution of cell metabolism waste penetrates film by the specific selection in membrane module, then will remove the training of stem cell metabolin Nutrient solution returns in buffer container, and the stem cell metabolic waste isolated is transported to back by the discharge system of stem cell metabolic waste In receiving apparatus;
Four, nutrition composition is added to the culture solution of removing stem cell metabolin, it is subsequently into stem cell incubator, i.e., complete At a kind of reinforcing discharge method of stem cell metabolic waste.
The concentration of carbon dioxide in the culture solution of stem cell metabolin is removed described in step 3 less than 40%;
Specific selection described in step 3 is the hollow-fibre membrane of carbon dioxide removal through film;Described in step 3 Specific selection buy scientific and technological (Xiamen) Co., Ltd at the beginning of state through film;
Pressurized circulation system described in step 2 is the pressurized circulation system that control valve and peristaltic pump cooperatively form.
Recyclable device described in step 3 is the recyclable device equipped with alkali collection liquid.
The present embodiment method needs to keep system sterile.
The present embodiment effectively improves the service efficiency of stem cell medium, conventional stem cell medium dosage from 15 liters/ Batch is reduced to 5 liters/batch, and stem cell toxigenic capacity is effectively reduced, and the toxigenic capacity of 70,000,000 stem cells is left from about 60,000 The right side is reduced to 20,000 or so.
Example IV:
A kind of reinforcing discharge method of stem cell metabolic waste is to sequentially include the following steps:
One, in sterile clean culture environment, the culture solution containing stem cell metabolic waste is introduced into buffer container;
The stem cell metabolic waste is the mixing of ammonia, lactic acid class and carbon dioxide, contains stem cell metabolic waste The concentration of ammonia is greater than 3mmol/L in culture solution;The concentration of lactic acid class is greater than in culture solution containing stem cell metabolic waste 30mmol/L;The concentration of carbon dioxide is greater than 40% in culture solution containing stem cell metabolic waste;
Two, membrane module is selected;
Three, the discharge system of pressurized circulation system and stem cell metabolic waste is established, pressurized circulation system makes containing dry The culture solution of cell metabolism waste penetrates film by the specific selection in membrane module, then will remove the training of stem cell metabolin Nutrient solution returns in buffer container, and the stem cell metabolic waste isolated is transported to back by the discharge system of stem cell metabolic waste In receiving apparatus;
Four, nutrition composition is added to the culture solution of removing stem cell metabolin, it is subsequently into stem cell incubator, i.e., complete At a kind of reinforcing discharge method of stem cell metabolic waste.
The concentration that ammonia in the culture solution of stem cell metabolin is removed described in step 3 is less than 2mmol/L;In step 3 The concentration of lactic acid class is less than 24.8mmol/L in the culture solution of the removing stem cell metabolin;Removing described in step 3 The concentration of carbon dioxide is less than 40% in the culture solution of stem cell metabolin;
Specific selection described in step 2 through film be remove ammonia hollow-fibre membrane, removing lactic acid rolled film and The hollow-fibre membrane of carbon dioxide removal;Specific selection described in step 2, which buys scientific and technological at the beginning of state (Xiamen) through film, to be had Limit company;
Pressurized circulation system described in step 2 is the pressurized circulation system that control valve and peristaltic pump cooperatively form.
Recyclable device described in step 3 is the recyclable device equipped with alkali collection liquid.
The present embodiment method needs to keep system sterile.
The present embodiment effectively improves the service efficiency of stem cell medium, conventional stem cell medium dosage from 15 liters/ Batch is reduced to 4 liters/batch, and stem cell toxigenic capacity is effectively reduced, and the toxigenic capacity of 70,000,000 stem cells is left from about 60,000 The right side is reduced to 1.7 ten thousand or so.

Claims (5)

1. a kind of reinforcing discharge method of stem cell metabolic waste, it is characterised in that a kind of reinforcing discharge of stem cell metabolic waste Method is to sequentially include the following steps:
One, the culture solution containing stem cell metabolic waste is introduced into buffer container;
In the culture solution containing stem cell metabolic waste, stem cell metabolic waste is in ammonia, lactic acid class and carbon dioxide One kind or in which several mixing;
When the described stem cell metabolic waste when containing ammonia, the concentration of ammonia is greater than in the culture solution containing stem cell metabolic waste 3mmol/L;
When the stem cell metabolic waste class containing lactic acid, the concentration of lactic acid class in the culture solution containing stem cell metabolic waste Greater than 30mmol/L;
When the stem cell metabolic waste carbonated, carbon dioxide in the culture solution containing stem cell metabolic waste Concentration is greater than 40%;
Two, membrane module is selected;
Three, the discharge system of pressurized circulation system and stem cell metabolic waste is established, pressurized circulation system makes containing stem cell The culture solution of metabolic waste penetrates film by the specific selection in membrane module, then will remove the culture solution of stem cell metabolin Back in buffer container, the stem cell metabolic waste isolated is transported to recycling dress by the discharge system of stem cell metabolic waste In setting;
Four, nutrition composition is added to the culture solution of removing stem cell metabolin, subsequently into stem cell incubator, that is, completes one The reinforcing discharge method of kind stem cell metabolic waste.
2. a kind of reinforcing discharge method of stem cell metabolic waste according to claim 1, it is characterised in that in step 3 The specific selection is hollow-fibre membrane or rolled film through film.
3. a kind of reinforcing discharge method of stem cell metabolic waste according to claim 1, it is characterised in that in step 3 The concentration of ammonia is less than 2mmol/L in the culture solution of the removing stem cell metabolin;Removing stem cell described in step 3 The concentration of lactic acid class is less than 24.8mmol/L in the culture solution of metabolin;The training of stem cell metabolin is removed described in step 3 The concentration of carbon dioxide is less than 40% in nutrient solution.
4. a kind of reinforcing discharge method of stem cell metabolic waste according to claim 1, it is characterised in that in step 3 The pressurized circulation system is the pressurized circulation system that control valve and peristaltic pump cooperatively form.
5. a kind of reinforcing discharge method of stem cell metabolic waste according to claim 1, it is characterised in that in step 3 The recyclable device is the recyclable device equipped with recovered liquid.
CN201910403670.0A 2019-05-15 2019-05-15 A kind of reinforcing discharge method of stem cell metabolic waste Pending CN110117527A (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2023012523A1 (en) * 2019-12-02 2023-02-09 Avant Meats Company Limited System for producing cultivated meats, tissues and associated products from cells

Citations (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5447853A (en) * 1985-05-09 1995-09-05 Teijin Limited Method of producing useful high-molecular-weight substances by culturing proliferous animal cells, and culture system therefor
CN1384874A (en) * 1999-09-21 2002-12-11 阿文蒂斯药物德国有限公司 Method for cultivating cells, membrane module, utilziation of membrane module and reaction system for cultivation of said cells
CN1778887A (en) * 2005-10-09 2006-05-31 南京工业大学 High-density bacterium culturing method and its biological reactor
CN101199436A (en) * 2007-11-28 2008-06-18 中国人民解放军第三军医大学第一附属医院 Three-dimensional liver cell culture bioreactor
CN101490240A (en) * 2006-07-10 2009-07-22 高木产业株式会社 Cell or tissue cultivation apparatus and method of cultivation
CN103249840A (en) * 2010-12-09 2013-08-14 东丽株式会社 Method for producing chemical by continuous fermentation
CN103261427A (en) * 2010-12-22 2013-08-21 东丽株式会社 Method for producing chemical by continuous fermentation
CN103282109A (en) * 2010-12-27 2013-09-04 东丽株式会社 Hollow fiber membrane module and method for producing chemicals
WO2014034146A1 (en) * 2012-09-03 2014-03-06 三菱レイヨン株式会社 Cell culture module
CN103732733A (en) * 2011-06-06 2014-04-16 里珍西斯私人有限公司 Expansion of stem cells in hollow fiber bioreactors
CN103834696A (en) * 2013-10-23 2014-06-04 中国科学院过程工程研究所 Method for producing lactic acid through continuously fermenting batches of lignocellulose hydrolysate by coupling fermenting and membrane separation
CN103857789A (en) * 2011-08-31 2014-06-11 世元世龙技术株式会社 Method for preparing a basic culture medium for mesenchymal stem cells, basic culture medium for mesenchymal stem cells, and cell therapeutic agent cultured and differentiated using same
WO2016140213A1 (en) * 2015-03-05 2016-09-09 東洋紡株式会社 Cell culture method using hollow fiber module
CN106011187A (en) * 2008-09-30 2016-10-12 东丽株式会社 Method for producing chemical product and continuous fermentation apparatus
CN107400633A (en) * 2017-08-17 2017-11-28 上海白泽医疗器械有限公司 Doughnut exchanger and doughnut switch type culture systems
CN107922919A (en) * 2015-05-29 2018-04-17 勃林格殷格翰国际公司 The perfusion of cell control in continuous culture
CN109628407A (en) * 2019-01-28 2019-04-16 哈药集团技术中心 The method of high density long-term cultivation expression anti-vegf Humanized monoclonal antibodies recombinaant CHO cell

Patent Citations (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5447853A (en) * 1985-05-09 1995-09-05 Teijin Limited Method of producing useful high-molecular-weight substances by culturing proliferous animal cells, and culture system therefor
CN1384874A (en) * 1999-09-21 2002-12-11 阿文蒂斯药物德国有限公司 Method for cultivating cells, membrane module, utilziation of membrane module and reaction system for cultivation of said cells
CN1778887A (en) * 2005-10-09 2006-05-31 南京工业大学 High-density bacterium culturing method and its biological reactor
CN101490240A (en) * 2006-07-10 2009-07-22 高木产业株式会社 Cell or tissue cultivation apparatus and method of cultivation
CN101199436A (en) * 2007-11-28 2008-06-18 中国人民解放军第三军医大学第一附属医院 Three-dimensional liver cell culture bioreactor
CN106011187A (en) * 2008-09-30 2016-10-12 东丽株式会社 Method for producing chemical product and continuous fermentation apparatus
CN103249840A (en) * 2010-12-09 2013-08-14 东丽株式会社 Method for producing chemical by continuous fermentation
CN103261427A (en) * 2010-12-22 2013-08-21 东丽株式会社 Method for producing chemical by continuous fermentation
CN103282109A (en) * 2010-12-27 2013-09-04 东丽株式会社 Hollow fiber membrane module and method for producing chemicals
CN103732733A (en) * 2011-06-06 2014-04-16 里珍西斯私人有限公司 Expansion of stem cells in hollow fiber bioreactors
CN103857789A (en) * 2011-08-31 2014-06-11 世元世龙技术株式会社 Method for preparing a basic culture medium for mesenchymal stem cells, basic culture medium for mesenchymal stem cells, and cell therapeutic agent cultured and differentiated using same
WO2014034146A1 (en) * 2012-09-03 2014-03-06 三菱レイヨン株式会社 Cell culture module
CN103834696A (en) * 2013-10-23 2014-06-04 中国科学院过程工程研究所 Method for producing lactic acid through continuously fermenting batches of lignocellulose hydrolysate by coupling fermenting and membrane separation
WO2016140213A1 (en) * 2015-03-05 2016-09-09 東洋紡株式会社 Cell culture method using hollow fiber module
CN107922919A (en) * 2015-05-29 2018-04-17 勃林格殷格翰国际公司 The perfusion of cell control in continuous culture
CN107400633A (en) * 2017-08-17 2017-11-28 上海白泽医疗器械有限公司 Doughnut exchanger and doughnut switch type culture systems
CN109628407A (en) * 2019-01-28 2019-04-16 哈药集团技术中心 The method of high density long-term cultivation expression anti-vegf Humanized monoclonal antibodies recombinaant CHO cell

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
WENDLING F, ET AL.: "A self-renewing, bipotential erythroid/mast cell progenitor in continuous cultures of normal murine bone marrow.", 《J CELL PHYSIOL.》 *

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2023012523A1 (en) * 2019-12-02 2023-02-09 Avant Meats Company Limited System for producing cultivated meats, tissues and associated products from cells

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