SG10201901708SA - Perfusion culturing methods and uses thereof - Google Patents
Perfusion culturing methods and uses thereofInfo
- Publication number
- SG10201901708SA SG10201901708SA SG10201901708SA SG10201901708SA SG10201901708SA SG 10201901708S A SG10201901708S A SG 10201901708SA SG 10201901708S A SG10201901708S A SG 10201901708SA SG 10201901708S A SG10201901708S A SG 10201901708SA SG 10201901708S A SG10201901708S A SG 10201901708SA
- Authority
- SG
- Singapore
- Prior art keywords
- degrees
- culture medium
- culturing
- rpm
- methods
- Prior art date
Links
Classifications
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS 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
- C12M23/00—Constructional details, e.g. recesses, hinges
- C12M23/02—Form or structure of the vessel
- C12M23/08—Flask, bottle or test tube
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
- C12P21/00—Preparation of peptides or proteins
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS 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
- C12M23/00—Constructional details, e.g. recesses, hinges
- C12M23/50—Means for positioning or orientating the apparatus
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
- C12N9/00—Enzymes; Proenzymes; Compositions thereof; Processes for preparing, activating, inhibiting, separating or purifying enzymes
- C12N9/14—Hydrolases (3)
- C12N9/24—Hydrolases (3) acting on glycosyl compounds (3.2)
- C12N9/2402—Hydrolases (3) acting on glycosyl compounds (3.2) hydrolysing O- and S- glycosyl compounds (3.2.1)
- C12N9/2465—Hydrolases (3) acting on glycosyl compounds (3.2) hydrolysing O- and S- glycosyl compounds (3.2.1) acting on alpha-galactose-glycoside bonds, e.g. alpha-galactosidase (3.2.1.22)
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
- C12N2527/00—Culture process characterised by the use of mechanical forces, e.g. strain, vibration
Abstract
PERFUSION CULTURING METHODS AND USES THEREOF A BSTRACT Provided herein are improved methods of culturing a mammalian cell that include providing conical containing mammalian suspended about % to 5 about 8 0% of the volume of the container of a first liquid culture medium; incuba ting the container for a period of time at about 31 C to about 40 C at a reactor angle of about 5 degrees to about 85 degrees (e.g., about 40 degrees to about 55 degrees) from horizontal and with an agita tion of about 2 0 revoluti ons per minute (RPM) to about 1000 RPM; and continuously or periodically , during the period of time, removing a first volume of the 10 first liquid culture medium that is substantially free of mammalian cells and adding to the first l iquid culture medium a second volume of a second liquid culture medium, wherein the first and second volumes are about equal, and methods of culturing a mammalian cell that include culturing in a gradient perfusion process a mammalian cell suspended in a l iquid culture medium under conditions that generate in the medium a fluid sheer force 15 and dissolved oxygen (O 2 ) concentration that is the same as (or essentially the same as ) that achieved in a gas -permeable coni cal container containing 4% to 4 0% volume of the container of liquid culture medium when p ositioned at a reactor angle of about 5 degrees to 85 degrees (e.g., 40 to 55 from , incubate d at a temperature of about 31 C to about 40 C, and agi tated at a freq uency of 20 about 2 0 revolutions per mi nute (RPM) to about 1000 RPM . Also provided are various methods that utilize these culturing methods. [Figure 1] 25
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US201261717486P | 2012-10-23 | 2012-10-23 |
Publications (1)
Publication Number | Publication Date |
---|---|
SG10201901708SA true SG10201901708SA (en) | 2019-03-28 |
Family
ID=49546634
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SG11201503085VA SG11201503085VA (en) | 2012-10-23 | 2013-10-23 | Perfusion culturing methods and uses thereof |
SG10201901708SA SG10201901708SA (en) | 2012-10-23 | 2013-10-23 | Perfusion culturing methods and uses thereof |
Family Applications Before (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SG11201503085VA SG11201503085VA (en) | 2012-10-23 | 2013-10-23 | Perfusion culturing methods and uses thereof |
Country Status (9)
Country | Link |
---|---|
US (1) | US20140154726A1 (en) |
EP (2) | EP2912160B1 (en) |
CN (2) | CN108192822A (en) |
AU (2) | AU2013334602B2 (en) |
CA (1) | CA2889022A1 (en) |
HK (1) | HK1214292A1 (en) |
MX (2) | MX363702B (en) |
SG (2) | SG11201503085VA (en) |
WO (1) | WO2014066519A1 (en) |
Families Citing this family (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
SG10201806083RA (en) * | 2013-02-22 | 2018-08-30 | Genzyme Corp | Microcarrier perfusion culturing methods and uses thereof |
US10421949B2 (en) | 2013-02-22 | 2019-09-24 | Genzyme Corporation | Microcarrier perfusion culturing methods and uses thereof |
AR095196A1 (en) * | 2013-03-15 | 2015-09-30 | Regeneron Pharma | SERUM FREE CELL CULTIVATION MEDIA |
TW202204596A (en) * | 2014-06-06 | 2022-02-01 | 美商健臻公司 | Perfusion culturing methods and uses thereof |
TWI707949B (en) * | 2014-06-09 | 2020-10-21 | 美商健臻公司 | Seed train processes and uses thereof |
RU2713126C2 (en) * | 2014-10-24 | 2020-02-03 | Джензим Корпорейшн | Method for preventing contamination of system |
IL308064A (en) | 2014-12-22 | 2023-12-01 | Genzyme Corp | Methods of culturing a mammalian cell |
CN105385731B (en) * | 2015-12-25 | 2018-10-30 | 上海莱士血液制品股份有限公司 | A kind of perfusion cultural method of eight factors of expression recombination |
KR20180047404A (en) * | 2016-10-31 | 2018-05-10 | 삼성바이오에피스 주식회사 | Process for reducing undesirable by-product in cell culture |
KR102604992B1 (en) * | 2017-03-31 | 2023-11-24 | 베링거 인겔하임 인터내셔날 게엠베하 | perfusion medium |
US20200323958A1 (en) * | 2017-11-13 | 2020-10-15 | Amgen Inc. | Methods for producing protein products |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2411178B8 (en) * | 2004-02-20 | 2008-07-11 | Cesco Bioengineering Co Ltd | Apparatus and method for preparing and culturing cells |
DK1891205T3 (en) * | 2005-06-15 | 2018-03-19 | Zhejiang Jinyishengshi Bioengineering Co Ltd | SUSPENSION CULTURE CONTAINERS |
WO2006138143A1 (en) * | 2005-06-15 | 2006-12-28 | Amprotein Corporation | Suspension culture vessels |
WO2008024769A2 (en) * | 2006-08-21 | 2008-02-28 | Raven Biotechnologies, Inc. | Intensified perfusion production method |
WO2009034186A2 (en) * | 2007-09-13 | 2009-03-19 | Helmholtz-Zentrum für Infektionsforschung GmbH | Process for cell cultivation |
US20090233334A1 (en) * | 2008-03-11 | 2009-09-17 | Excellgene Sa | Cell cultivation and production of recombinant proteins by means of an orbital shake bioreactor system with disposable bags at the 1,500 liter scale |
US20100076380A1 (en) * | 2008-06-16 | 2010-03-25 | Amprotein Corporation | Bioreactors |
WO2010120514A2 (en) | 2009-03-31 | 2010-10-21 | The Trustees Of The University Of Pennsylvania | Antigen-binding proteins comprising recombinant protein scaffolds |
-
2013
- 2013-10-23 CN CN201810153403.8A patent/CN108192822A/en active Pending
- 2013-10-23 CN CN201380067513.8A patent/CN104903436B/en not_active Expired - Fee Related
- 2013-10-23 EP EP13786587.9A patent/EP2912160B1/en active Active
- 2013-10-23 SG SG11201503085VA patent/SG11201503085VA/en unknown
- 2013-10-23 SG SG10201901708SA patent/SG10201901708SA/en unknown
- 2013-10-23 US US14/061,657 patent/US20140154726A1/en not_active Abandoned
- 2013-10-23 MX MX2015005206A patent/MX363702B/en unknown
- 2013-10-23 CA CA2889022A patent/CA2889022A1/en not_active Abandoned
- 2013-10-23 AU AU2013334602A patent/AU2013334602B2/en not_active Ceased
- 2013-10-23 WO PCT/US2013/066410 patent/WO2014066519A1/en active Application Filing
- 2013-10-23 EP EP20188132.3A patent/EP3747984A1/en not_active Withdrawn
-
2015
- 2015-04-23 MX MX2019003638A patent/MX2019003638A/en unknown
-
2016
- 2016-03-02 HK HK16102431.5A patent/HK1214292A1/en unknown
-
2018
- 2018-08-30 AU AU2018222985A patent/AU2018222985A1/en not_active Abandoned
Also Published As
Publication number | Publication date |
---|---|
HK1214292A1 (en) | 2016-07-22 |
AU2013334602B2 (en) | 2018-05-31 |
MX363702B (en) | 2019-03-29 |
MX2019003638A (en) | 2019-09-02 |
US20140154726A1 (en) | 2014-06-05 |
WO2014066519A1 (en) | 2014-05-01 |
AU2013334602A1 (en) | 2015-05-14 |
MX2015005206A (en) | 2016-08-03 |
AU2018222985A1 (en) | 2018-09-20 |
EP2912160A1 (en) | 2015-09-02 |
CA2889022A1 (en) | 2014-05-01 |
CN104903436A (en) | 2015-09-09 |
SG11201503085VA (en) | 2015-05-28 |
EP2912160B1 (en) | 2020-07-29 |
EP3747984A1 (en) | 2020-12-09 |
CN108192822A (en) | 2018-06-22 |
CN104903436B (en) | 2018-03-30 |
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