GB660145A - Fermentation process - Google Patents
Fermentation processInfo
- Publication number
- GB660145A GB660145A GB2865648A GB2865648A GB660145A GB 660145 A GB660145 A GB 660145A GB 2865648 A GB2865648 A GB 2865648A GB 2865648 A GB2865648 A GB 2865648A GB 660145 A GB660145 A GB 660145A
- Authority
- GB
- United Kingdom
- Prior art keywords
- streptomycin
- temperature
- tubes
- culture medium
- producing organism
- 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
Links
Classifications
-
- 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
- C12M41/00—Means for regulation, monitoring, measurement or control, e.g. flow regulation
- C12M41/12—Means for regulation, monitoring, measurement or control, e.g. flow regulation of temperature
- C12M41/18—Heat exchange systems, e.g. heat jackets or outer envelopes
-
- 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
- C12M29/00—Means for introduction, extraction or recirculation of materials, e.g. pumps
- C12M29/18—External loop; Means for reintroduction of fermented biomass or liquid percolate
-
- 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
- C12P19/00—Preparation of compounds containing saccharide radicals
- C12P19/44—Preparation of O-glycosides, e.g. glucosides
- C12P19/46—Preparation of O-glycosides, e.g. glucosides having an oxygen atom of the saccharide radical bound to a cyclohexyl radical, e.g. kasugamycin
- C12P19/54—Preparation of O-glycosides, e.g. glucosides having an oxygen atom of the saccharide radical bound to a cyclohexyl radical, e.g. kasugamycin the cyclohexyl radical being bound directly to a nitrogen atom of two or more radicals, e.g. streptomycin
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Zoology (AREA)
- Life Sciences & Earth Sciences (AREA)
- Wood Science & Technology (AREA)
- Bioinformatics & Cheminformatics (AREA)
- Health & Medical Sciences (AREA)
- Microbiology (AREA)
- Genetics & Genomics (AREA)
- Biotechnology (AREA)
- Biochemistry (AREA)
- General Health & Medical Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Biomedical Technology (AREA)
- Sustainable Development (AREA)
- Micro-Organisms Or Cultivation Processes Thereof (AREA)
- Analytical Chemistry (AREA)
- Thermal Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Apparatus Associated With Microorganisms And Enzymes (AREA)
- Preparation Of Compounds By Using Micro-Organisms (AREA)
- Physics & Mathematics (AREA)
Abstract
In the production of streptomycin by the aerobic fermentation of a culture medium with a streptomycin-producing organism under conditions of submerged growth, the temperature is controlled by circulating a portion of the wash through a heat exchanger (preferably comprising a set of tubes in parallel contained in a jacket through which heating or cooling media may be passed, the dimensions of the tubes and the circulating system being desirably such that the rate of circulation of the liquid is sufficient to prevent the settling of mycelium therein, e.g. at least 0.7 feet per second). Advantageously the culture medium is first heated to a temperature and for a time sufficient to sterilize it, then cooled to the fermentation temperature and inoculated thereat with the streptomycin-producing organism, e.g. Streptomyces grisens. A suitable arrangement of apparatus is described with drawings.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB2865648A GB660145A (en) | 1948-11-04 | 1948-11-04 | Fermentation process |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB2865648A GB660145A (en) | 1948-11-04 | 1948-11-04 | Fermentation process |
Publications (1)
Publication Number | Publication Date |
---|---|
GB660145A true GB660145A (en) | 1951-10-31 |
Family
ID=10279043
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB2865648A Expired GB660145A (en) | 1948-11-04 | 1948-11-04 | Fermentation process |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB660145A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
NL79006C (en) * | 1950-03-06 | 1955-09-15 | Eugen Georg Stich |
-
1948
- 1948-11-04 GB GB2865648A patent/GB660145A/en not_active Expired
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
NL79006C (en) * | 1950-03-06 | 1955-09-15 | Eugen Georg Stich |
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