SU668939A1 - Method of separating aqueous culture medium - Google Patents
Method of separating aqueous culture mediumInfo
- Publication number
- SU668939A1 SU668939A1 SU772504952A SU2504952A SU668939A1 SU 668939 A1 SU668939 A1 SU 668939A1 SU 772504952 A SU772504952 A SU 772504952A SU 2504952 A SU2504952 A SU 2504952A SU 668939 A1 SU668939 A1 SU 668939A1
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- suspension
- decanter
- yeast
- contact surfaces
- aqueous medium
- Prior art date
Links
Classifications
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- 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
- C12N1/00—Microorganisms, e.g. protozoa; Compositions thereof; Processes of propagating, maintaining or preserving microorganisms or compositions thereof; Processes of preparing or isolating a composition containing a microorganism; Culture media therefor
- C12N1/02—Separating microorganisms from their culture media
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
- B01D17/02—Separation of non-miscible liquids
- B01D17/0208—Separation of non-miscible liquids by sedimentation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
- B01D17/02—Separation of non-miscible liquids
- B01D17/04—Breaking emulsions
- B01D17/045—Breaking emulsions with coalescers
Landscapes
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Genetics & Genomics (AREA)
- Thermal Sciences (AREA)
- Biotechnology (AREA)
- Organic Chemistry (AREA)
- Zoology (AREA)
- Wood Science & Technology (AREA)
- Bioinformatics & Cheminformatics (AREA)
- Physics & Mathematics (AREA)
- Biomedical Technology (AREA)
- Microbiology (AREA)
- Virology (AREA)
- Tropical Medicine & Parasitology (AREA)
- Biochemistry (AREA)
- General Engineering & Computer Science (AREA)
- General Health & Medical Sciences (AREA)
- Medicinal Chemistry (AREA)
- Preparation Of Compounds By Using Micro-Organisms (AREA)
- Apparatus Associated With Microorganisms And Enzymes (AREA)
- Micro-Organisms Or Cultivation Processes Thereof (AREA)
Description
(54) СПОСОБ ВЬЩЕЛЕНИЯ ВОДНОЙ КУШЯУРАЛЬНОЙ СРЕДЫ(54) METHOD FOR CREATING WATER FOOD MEDIUM
1one
Способ относитс к микробиологической промышленности ,а именно к способу разделени микробиологических суспензий,полученных при культивировании микроорганизмов на углеводородах.Известен способ выделени биомассы микроорганизмов из суспензии микроорганизмов, выращенных на углеводородах, путем декантации 1), Дл увеличени степени отделени водной культуральной среда в суспензию микроорганизмов диспергируют воздух, который способствует улучшению флотировани и отделени микроорганизмов.The method relates to the microbiological industry, namely to the method of separating microbiological suspensions obtained by cultivating microorganisms on hydrocarbons. A method is known for separating the biomass of microorganisms from a suspension of microorganisms grown on hydrocarbons by decanting 1), to increase the degree of separation of aqueous culture medium into suspension of microorganisms air, which helps to improve flotation and the separation of microorganisms.
Однако такой способ требует значительного расхода энергии на введение в аппарат и диспергирование воздуха.However, this method requires significant energy consumption for the introduction into the apparatus and the dispersion of air.
Предлагаемый способ позвол ет увеличить ВЫХОД ВОДНОЙ среды в степень сгущени микробиологической суспензии.The proposed method allows to increase the output of the aqueous medium to the degree of thickening of the microbial suspension.
Дл этого процесс декантации осуществл ют с использованием контактных поверхностей в виде ЛИСТОВ, сит, колец Рашига или токарной стружки при нагрузке суспензии до 10 см на 1 см поверхности контакта в течение 1 час и скорости потока суспензии 0,5-10 см в 1 мин.For this, the decantation process is carried out using contact surfaces in the form of SHEETS, sieves, Raschig rings or turning chips with a suspension load of up to 10 cm per 1 cm of the contact surface for 1 hour and a flow rate of suspension of 0.5-10 cm per minute.
При этом концентрацию углеводородов в суспензии микроорганизмов поддерживают в пределах 5-80%.The concentration of hydrocarbons in the suspension of microorganisms is maintained in the range of 5-80%.
Контактными поверхност ми, изготовленными из стали, керамики или тефлона (политетрафторэтилена ) заполн ют аппарат-декантатор, В котором происходит разделение микробиологических суспензий.Contact surfaces made of steel, ceramics or Teflon (polytetrafluoroethylene) are filled with a decanter apparatus, in which the separation of microbiological suspensions takes place.
Способ применим дл разделени микробиологических суспензий, полученных при культивировании микроорганизмов на углеводородах, предпочтительно нефт ных дистилл тах, выкипающих В пределах 100-400°С.The method is applicable to the separation of microbiological suspensions obtained by cultivating microorganisms on hydrocarbons, preferably petroleum distillates, boiling away from 100-400 ° C.
Способ осуществл ют следующим образом. .Микробиологическа суспензи из ферментера поступает в декантатор, где раздел етс на две фазы: легкую, содержащую биомассу, углеводороды ,воздух и некоторое количество водной среды, и т желую - водную среду. Легка фаза декантируетс и далее поступает на разделение из вестными способами.При этом отдел етс дополнительное количество водной среды.The method is carried out as follows. The microbiological suspension from the fermenter enters the decanter, where it is divided into two phases: light, containing biomass, hydrocarbons, air and some amount of aqueous medium, and heavy - aqueous medium. The light phase is decanted and then fed to the separation by known methods. In this case, an additional amount of aqueous medium is separated.
Claims (2)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DD19394176A DD126703B1 (en) | 1976-07-19 | 1976-07-19 | Separation of aqueous cultured liquid from biomass suspensions containing hydrocarbon |
Publications (1)
Publication Number | Publication Date |
---|---|
SU668939A1 true SU668939A1 (en) | 1979-06-25 |
Family
ID=5505180
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SU772504952A SU668939A1 (en) | 1976-07-19 | 1977-07-19 | Method of separating aqueous culture medium |
Country Status (12)
Country | Link |
---|---|
BG (1) | BG35407A1 (en) |
CS (1) | CS196159B1 (en) |
DD (1) | DD126703B1 (en) |
DE (1) | DE2730197A1 (en) |
FR (1) | FR2358911A1 (en) |
GB (1) | GB1544374A (en) |
HU (1) | HU177363B (en) |
PL (1) | PL109681B1 (en) |
RO (1) | RO71482A (en) |
SE (1) | SE433360B (en) |
SU (1) | SU668939A1 (en) |
YU (1) | YU178977A (en) |
Family Cites Families (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR1400964A (en) * | 1963-03-09 | 1965-05-28 | Metallgesellschaft Ag | Method and apparatus for the separation of liquids which are not or hardly miscible |
US3530039A (en) * | 1966-01-17 | 1970-09-22 | Exxon Research Engineering Co | Process for fermentation and recovery of microbial cells |
DE1923529A1 (en) * | 1968-05-29 | 1969-12-04 | Ingtech Zentralbuero Veb | Purification of fermentation products |
BE793060A (en) * | 1971-12-24 | 1973-04-16 | Metallgesellschaft Ag | DEVICE FOR SEPARATING LIQUIDS |
FI53075C (en) * | 1973-03-07 | 1978-02-10 | Kemira Oy |
-
1976
- 1976-07-19 DD DD19394176A patent/DD126703B1/en unknown
-
1977
- 1977-07-04 DE DE19772730197 patent/DE2730197A1/en not_active Withdrawn
- 1977-07-12 BG BG7736868A patent/BG35407A1/en unknown
- 1977-07-18 RO RO7791077A patent/RO71482A/en unknown
- 1977-07-18 SE SE7708306A patent/SE433360B/en unknown
- 1977-07-18 GB GB30119/77A patent/GB1544374A/en not_active Expired
- 1977-07-18 YU YU01789/77A patent/YU178977A/en unknown
- 1977-07-19 CS CS774810A patent/CS196159B1/en unknown
- 1977-07-19 FR FR7722120A patent/FR2358911A1/en not_active Withdrawn
- 1977-07-19 PL PL1977199744A patent/PL109681B1/en unknown
- 1977-07-19 HU HU77PE1014A patent/HU177363B/en not_active IP Right Cessation
- 1977-07-19 SU SU772504952A patent/SU668939A1/en active
Also Published As
Publication number | Publication date |
---|---|
DE2730197A1 (en) | 1978-01-26 |
GB1544374A (en) | 1979-04-19 |
DD126703B1 (en) | 1980-10-29 |
DD126703A1 (en) | 1977-08-03 |
CS196159B1 (en) | 1980-03-31 |
SE433360B (en) | 1984-05-21 |
BG35407A1 (en) | 1984-04-15 |
HU177363B (en) | 1981-09-28 |
SE7708306L (en) | 1978-01-20 |
PL199744A1 (en) | 1978-06-05 |
RO71482A (en) | 1982-02-01 |
YU178977A (en) | 1982-08-31 |
FR2358911A1 (en) | 1978-02-17 |
PL109681B1 (en) | 1980-06-30 |
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