GB1138452A - Improvements in or relating to continuous phased culturing of cells - Google Patents

Improvements in or relating to continuous phased culturing of cells

Info

Publication number
GB1138452A
GB1138452A GB963566A GB963566A GB1138452A GB 1138452 A GB1138452 A GB 1138452A GB 963566 A GB963566 A GB 963566A GB 963566 A GB963566 A GB 963566A GB 1138452 A GB1138452 A GB 1138452A
Authority
GB
United Kingdom
Prior art keywords
cell culture
phased
nutrient medium
cycle
culture
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.)
Expired
Application number
GB963566A
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.)
Canadian Patents and Development Ltd
Original Assignee
Canadian Patents and Development 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 Canadian Patents and Development Ltd filed Critical Canadian Patents and Development Ltd
Publication of GB1138452A publication Critical patent/GB1138452A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • 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
    • C12M41/00Means for regulation, monitoring, measurement or control, e.g. flow regulation
    • C12M41/30Means for regulation, monitoring, measurement or control, e.g. flow regulation of concentration
    • C12M41/32Means for regulation, monitoring, measurement or control, e.g. flow regulation of concentration of substances in solution

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • Zoology (AREA)
  • Wood Science & Technology (AREA)
  • Microbiology (AREA)
  • Sustainable Development (AREA)
  • Biotechnology (AREA)
  • Biomedical Technology (AREA)
  • Biochemistry (AREA)
  • General Engineering & Computer Science (AREA)
  • General Health & Medical Sciences (AREA)
  • Genetics & Genomics (AREA)
  • Analytical Chemistry (AREA)
  • Micro-Organisms Or Cultivation Processes Thereof (AREA)
  • Apparatus Associated With Microorganisms And Enzymes (AREA)

Abstract

1,138,452. Antibiotic-producing micro-organisms. CANADIAN PATENTS & DEVELOPMENT Ltd. 4 March, 1966 [8 March, 1965], No. 9635/66. Heading C2A. [Also in Division C6] The phasing of a cell culture is improved by growing the cell culture in a nutrient medium at a predetermined rate of growth, the quantity of medium being only sufficient for the cells to complete their cycle at that growth rate, and at the doubling time of the culture the cell culture is divided into two equal halves while further nutrient medium is added such that each of the halves has sufficient nutrient medium for the cells to complete their cycle. In the phased condition usually at least 70-80% of the cells are at an identical stage of growth over their cell cycle. The further nutrient medium may be added immediately prior to the doubling time in such an amount as to double the volume of the cell culture, and at the doubling time the cell culture is divided into two equal halves whereby the cells in the halves may complete a similar cell cycle. The procedure may be continually repeated with at least one half of the cell culture to provide for a continuing production of the phased cell culture, while the other half is employed for the harvesting of a desired cell metabolite (even one of transient production such as ribonucleic acid) at the time when it is produced in an optimum amount, as determined by analysis of the metabolite production on previous cell cycles of the phased cell culture; the metabolite may be harvested either during a repeating phased cycle or after the particular cell culture has proceeded beyond this to a post cycle for further growth under modified conditions. In the production of penicillin with batch culture, the penicillin is a secondary metabolite produced in the stationary stage which follows the primary growth. In the phased culture process, however, this metabolite may be harvested in the post cycle at the optimum time determined experimentally and due to the phasing of the cell culture the yield is stated to be greatly increased over that of the randomized batch process. The phased culture process may be applied to micro-organisms (bacteria yeasts and moulds) and to plant- and animal-tissue cells. The following species of micro-organisms are particularly mentioned: Candida utilis, Saccharomyces cerewisiae, Saccharomyces rouxii, Saccharomyces magnoliae, Streptomyces bovis, Streptomyces venezuleae, Aspergillus aerogenes, Aspergillus suboxydans and Pseudomonad sp. The process is described with reference to the cultivation of Candida utilis on nitrogen-limiting media based on glucose or glycerol. Detailed analyses are presented of the varying amount of metabolites produced during phases of differing durations. Referring to Fig. 1, a mixture 12 of cell culture and nutrient medium is maintained at a constant temperature for the cultivation by recirculation by a pump 13 from the cyclone column 10 to a water jacketed limb 11. It is arranged that at, or immediately prior to, the doubling time a dosing vessel 21 will have been filled with nutrient medium, delivered at a constant rate from reservoir 33, to such an extent that a constant volume of nutrient medium is syphoned off into the cyclone column 10 and that one-half of the resulting mixture either is syphoned off into a collector 39 or is withdrawn by manual operation of a clamp 41 into a second culturing system 10<SP>1</SP> from which product is collected in a harvesting vessel 46.
GB963566A 1965-03-08 1966-03-04 Improvements in or relating to continuous phased culturing of cells Expired GB1138452A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US43773465A 1965-03-08 1965-03-08

Publications (1)

Publication Number Publication Date
GB1138452A true GB1138452A (en) 1969-01-01

Family

ID=23737661

Family Applications (1)

Application Number Title Priority Date Filing Date
GB963566A Expired GB1138452A (en) 1965-03-08 1966-03-04 Improvements in or relating to continuous phased culturing of cells

Country Status (2)

Country Link
GB (1) GB1138452A (en)
NL (1) NL6602946A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2393064A1 (en) * 1977-06-02 1978-12-29 Merck & Co Inc AVERAGE AUTOMATED VIRUS COLLECTION
GB2131012A (en) * 1982-08-26 1984-06-13 Nippon Zeon Co Process for producing S- adenosyl methionine

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2393064A1 (en) * 1977-06-02 1978-12-29 Merck & Co Inc AVERAGE AUTOMATED VIRUS COLLECTION
GB2131012A (en) * 1982-08-26 1984-06-13 Nippon Zeon Co Process for producing S- adenosyl methionine

Also Published As

Publication number Publication date
DE1517746A1 (en) 1970-04-16
NL6602946A (en) 1966-09-09

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