GB2075547A - Apparatus for cultivating micro organisms - Google Patents
Apparatus for cultivating micro organisms Download PDFInfo
- Publication number
- GB2075547A GB2075547A GB8113700A GB8113700A GB2075547A GB 2075547 A GB2075547 A GB 2075547A GB 8113700 A GB8113700 A GB 8113700A GB 8113700 A GB8113700 A GB 8113700A GB 2075547 A GB2075547 A GB 2075547A
- Authority
- GB
- United Kingdom
- Prior art keywords
- biomass
- support
- micro
- plates
- organisms
- 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.)
- Granted
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/02—Aerobic processes
- C02F3/12—Activated sludge processes
- C02F3/20—Activated sludge processes using diffusers
- C02F3/208—Membrane aeration
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/02—Aerobic processes
- C02F3/06—Aerobic processes using submerged filters
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/02—Aerobic processes
- C02F3/10—Packings; Fillings; Grids
-
- 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
- C12M23/04—Flat or tray type, drawers
-
- 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
- C12M27/00—Means for mixing, agitating or circulating fluids in the vessel
- C12M27/18—Flow directing inserts
- C12M27/20—Baffles; Ribs; Ribbons; Auger vanes
-
- 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
- C12M29/04—Filters; Permeable or porous membranes or plates, e.g. dialysis
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/30—Wastewater or sewage treatment systems using renewable energies
- Y02W10/37—Wastewater or sewage treatment systems using renewable energies using solar energy
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Wood Science & Technology (AREA)
- Bioinformatics & Cheminformatics (AREA)
- Microbiology (AREA)
- Zoology (AREA)
- Biochemistry (AREA)
- Environmental & Geological Engineering (AREA)
- Biotechnology (AREA)
- Biomedical Technology (AREA)
- General Engineering & Computer Science (AREA)
- General Health & Medical Sciences (AREA)
- Genetics & Genomics (AREA)
- Water Supply & Treatment (AREA)
- Biodiversity & Conservation Biology (AREA)
- Hydrology & Water Resources (AREA)
- Sustainable Development (AREA)
- Clinical Laboratory Science (AREA)
- Biological Treatment Of Waste Water (AREA)
- Apparatus Associated With Microorganisms And Enzymes (AREA)
- Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
Abstract
Apparatus for sewage treatment and method of cultivating micro organisms. The apparatus includes a tank 10 in which the cultivation medium flows, for example sewage or trade effluent to be treated. Within the tank are hollow plates 11 into which flows an oxygenation gas. The plates have walls of gas-permeable material to the outer face of which the micro organisms adhere. Air or oxygen within the plates pass through the wall and through the layer of micro organisms, to provide an aerobic biomass 20 (Fig. 3). This biomass is thicker or more active than the aerobic layer 21 of apparatus where the biomass is acted upon only from the outer faces. Tubes or troughs may be used instead of plates; the tubes may be upright or horizontal with the air or oxygen passing therethrough. The troughs may be open topped. The plate, tube or trough consists of a frame 14, a net 15 mounted on the frame and supporting the gas- permeable walls, which may be of micro porous material 16. <IMAGE>
Description
SPECIFICATION
Apparatus for and method of cultivating microorganisms
This invention relates to apparatus for and a method of cultivating micro-organisms and is particularly but not exclusively for the biological removal of organic material from liquids, such as the removal of pollutents from sewage and trade effluent.
Two known forms of apparatus for sewage treatment are biological or percolating filters, and rotary biological discs. The filters include beds of stones or plastics media which provide a relatively large surface area (relative to the volume of the filter) on which a biomass can grow, and the discs also provide a relatively large surface area and build up a layer of biomass as they rotate their lower halves through the liquid to be treated.
Figs. 1 and 2 illustrate a stone and a portion of a disc respectively and show a biomass 21 to 23 on each, there being an outer layer 21 of effective aerobic material, and inner layer 22 of anaerobic and a central layer 23 which is partly aerobic and partly anaerobic.
A disadvantage of the known processes is that the inner depth of the biomass is anaerobic and the effective aerobic layer of biomass is extremely thin; hence, the need for relatively large surface areas.
It is an object of this invention to provide apparatus in which the layer of effective aerobic biomass is increased in thickness or is more active.
According to one aspect of the present invention there is provided apparatus for the cultivation of micro-organism comprising a container, a gas-permeable support member within the. container and forming therewith a first zone for holding cultivation medium and a second zone for oxygenating gas, whereby microorganisms cultured in the first zone adhere to the adjacent surface of the support and oxygenating gas passes from the second zone through the support and the adherent micro-organisms.
According to another aspect of the present invention, there is provided a method of cultivating micro-organisms comprising the steps of permitting a culture to adhere to and grow upon one face of a gas permeable support to form a biomass thereon and passing oxygenating gas through the support from the opposite side and through the adherent biomass thereby to culturate an aerobic biomass on the support.
According to a further aspect of the present invention there is provided apparatus for the biological removal of organic material from liquids, comprising a container through which liquid to be treated is passed and in which is located one or more support members on each of which a layer of biomass grows, the or each member being of a gas permeable material and so formed that only one face of the material is in contact with the liquid to be treated, the other face being in contact with a source of air or oxygen.
Embodiments of the present invention will now be described, by way of example, with reference to the accompanying drawings, in which:~
Fig. 3 illustrates in section a member according to the invention with a biomass thereon;
Fig. 4 illustrates apparatus according to one embodiment of the present invention;
Fig. 5 illustrates a plate for use in the apparatus of Fig. 4;
Fig. 6 illustrates plates arranged in accordance with a second embodiment;
Fig. 7 illustrates the plate of Fig. 6;
Fig. 8 illustrates a tank for the plates of Fig. 6;
Fig. 9 illustrates a plate for use in a third embodiment of the invention;
Fig. 10 is a frame for use in conjunction with the plate of Fig. 9;
Fig. 11 illustrates the use of the plate and frame of Figs. 9 and 10; and
Fig. 12 illustrates the apparatus of the third embodiment.
The apparatus is particularly useful for the biological removal of organic material from liquids, such as the removal of pollutants from sewage and trade effluent.
Referring firstly to Figs. 4 and 5, one embodiment of the apparatus comprises a tank 10 into which depend a plurality of support members in the form of hollow plates 1 1, alternate plates being displaced transversely so as to provide a zigzag flow path for the sewage to be treated. The sewage enters the tank at one end 12 and exits at the longitudinally opposite end 13. The interior of the tank not occupied by the plates forms a zone for the cultivated medium, i.e. the sewage.
Each plate 1 1 is formed as illustrated in Fig. 5; a U-shaped frame 14 carries a sleeve of netting 15 and the combined frame and netting support a covering of gas permeable material, for example a micro-porous material 16 (Fig. 3), such as a PTFE material laminated to a woven nylon fabric. The micro-porous material prevents liquid passing through its walls to the interior, but permitting air or oxygen to pass through the walls from the interior, such a material is sold under the Trade
Mark GOTETEX. The netting may be of the kind sold under the registered Trade Mark NETLON.
The upper end of each plate 1 1 is closed by an overlapping strip 17 which has an inlet 18 and outlet 1 9 for air or oxygen to flow within the plate thus providing a zone for oxygenating gas.
The air or oxygen may be induced to flow within the plate by any suitable means; for example, from a pressurised bottle, or by a pump which either pumps the medium into the plate or extracts it by a vacuum system. Solar energy may also be used to induce convection flow.
An aerobic biomass 20 (Fig. 3), i.e. microorganisms cultivated in the cultivation zone, forms on the external wall of the plates and is fed by the air/oxygen passing through the plates, as well as by oxygen if any in the liquid being treated. This liquid may be aerated to increase its oxygen level.
As a result of the plate formations, which permit air/oxygen to act on the biomass layer from both inner and outer faces thereof, the resulting effective aerobic biomass layer 20 will be thicker or more active than one (21) which is acted upon only from the outer face, as illustrated in Figs. 1 and 2.
Fig. 3 illustrates the biomass layer produced in accordance with the invention shown as a solid aerobic mass 20.
In a second embodiment (Figs. 6 to 8), the member is a plate 30 which includes a U-shaped frame 31 of which the limbs 32 are horizontal and connected to a hollow upright, mounting 33 the upper end 34 of which is hook-shaped to engage the side wall of a tank 35. The frame is covered by netting 36 over which is mounted the micro-porous material (not shown). The hollow mounting 33 has inlets and outlets 37, 38 by which air or oxygen can flow within the plate.
Two sets of plates 30', 30" are provided, one set 30' being mounted nearer to the upper end of the mounting than the other set 30"; thus, the plates can be arranged in the tank as illustrated in
Fig. 6, so that sewage to be treated passes over the lowered plates 30" and under the raised plates 30'. A baffle 39 is provided on the lowered plates to prevent the flow passing directly under the array of plates.
The plates as described in this embodiment may be usefully provided in a tank 35 of the combined settlement and bio-treatment type.
Baffles may be provided in the tanks of the embodiments hereinbefore described for the usual purpose of increasing the distance travelled by the liquid to be treated, regulating the velocity of the liquid and possibly to aid shedding of biomass by virtue of increased velocity. In addition, turbulence increases the availability of organic matter to the biomass.
In a third embodiment (Figs. 9 to 12), the support member is a plate 40 which includes a frame 41 within which a series of baffles 42 are located; these extend from one or other of two opposed sides of the frame and terminate short of the respective opposite sides to form a zig-zag path for the air/oxygen flow. The frame is covered in netting and with micro-porous material (not shown). Air/oxygen is passed into the interior of the plate at one end of the baffles and exits from the other end, as indicated by arrows in Fig. 9.
A second frame 50 is also provided and has the same general shape as the frame 41; also it has similar baffles 51 but it is not covered by netting and micro-porous material. This second frame 50 has an inlet 52 and outlet 53 by which sewage to be treated passes into and out of the baffled area of the frame, and the plate 40 has one aperture 43 which registers with one or other of the inlet or outlet 52. 53 to permit passage of the sewage therethrough, i.e. through aperture 43.
In use, plates 40 and frames 50 are stacked alternately into a column, the plates and frames lying horizontally. Each alternate plate 40 is reversed, so that the aperture 43 of one plate lies above the inlet 52 of a frame and the aperture of another plate lies below the outlet of that frame as illustrated in Fig. 1 The sewage is fed in a
cascading fashion through each of the frames which air/oxygen is fed into each plate.
Groups of stacked plates and frames can be
spaced from an adjacent or subjacent group by
a spacer 60.
In each of the apparatuses described in the
three embodiments, action of the air or oxygen
within the plates encourages a relatively thick or
more active aerobic growth on the outer faces of the micro-porous material of each plate. Thus a
relatively thicker or more active layer of aerobic growth is produced on a relatively smaller surface
area than in known apparatus. Apart from the use
of pumps to induce air/oxygen flow, there are no
moving parts.
An important advantage of the apparatus and
method as hereinbefore described is that the organic matter to be destroyed and the air or oxygen which the organisms in the biomass use to
effect this destruction enter the biomass from
opposite sides, thus ensuring a maximum availability of both to the organisms.
The apparatus as hereinbefore described can be combined with other plant for biological processes, chemical processes and physical processes. In addition, the plates could be used in overloaded plants.
Other embodiments of apparatus in accordance with the invention can include the use of tubes or troughs wherein a framework supports the microporous material and air or oxygen flows in or through the tubes or troughs while the sewage to be treated flows around the tubes or troughs.
While the apparatus is primarily intended from treatment of sewage and trade effluent it is also applicable to the growth and harvesting of specific types (Strains) of biomass and in the production of useful chemical products which are produced by aerobic fermentation of micro-organism, for example antibiotics.
Claims (10)
1. Apparatus for the cultivation of microorganisms comprising a container, a gas permeable support member within the container and forming therewith a first zone for holding cultivation medium and a second zone for oxygenating gas, whereby micro-organisms cultured in the first zone adhere to the adjacent surface of the support and oxygenating gas passes from the second zone through the support and the adherent micro-organisms.
2. Apparatus as claimed in claim 1, in which the support member is a hollow body within which the oxygenating gas flows.
3. Apparatus as claimed in claim 2 in which the hollow body includes a frame supporting a microporous material.
4. Apparatus as claimed in claim 1,2 or 3 in which a plurality of support members are located in the container in spaced parallel formation.
5. Apparatus as claimed in claim 4 in which the adjacent members are offset to provide a zig-zag flow of cultivating medium.
6. Apparatus as claimed in any one of claims 1 to 5, in which the cultivating medium is sewage or trade effluent from which pollution is to be removed.
7. Apparatus for the biological removal of organic material from liquids, comprising a container through which liquid to be treated is passed and in which is located one or more support members on each of which a layer of biomass grows, the or each member being of a gas permeable material and so formed that only one face of the material is in contact with the liquid to be treated, the other face being in contact with a source of air or oxygen.
8. A method of cultivating micro-organisms comprising the steps of permitting a culture to adhere to and grow upon one face of a gas permeable support to form a biomass thereon and passing oxygenating gas through the support from the opposite face and through the adherent biomass thereby to cultivate an aerobic biomass on the support.
9. Apparatus for the cultivation of microorganisms substantially as hereinbefore described with reference to Figs. 4 and 5 or Figs. 6 to 8 or
Figs. 9 to 12 of the accompanying drawings.
10. A method of cultivating micro-organisms substantially as hereinbefore described.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB8113700A GB2075547B (en) | 1980-05-02 | 1981-05-05 | Apparatus for cultivating micro-organisms sewage treatment |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB8014719 | 1980-05-02 | ||
GB8113700A GB2075547B (en) | 1980-05-02 | 1981-05-05 | Apparatus for cultivating micro-organisms sewage treatment |
Publications (2)
Publication Number | Publication Date |
---|---|
GB2075547A true GB2075547A (en) | 1981-11-18 |
GB2075547B GB2075547B (en) | 1984-06-06 |
Family
ID=26275400
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB8113700A Expired GB2075547B (en) | 1980-05-02 | 1981-05-05 | Apparatus for cultivating micro-organisms sewage treatment |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB2075547B (en) |
Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3544383A1 (en) * | 1985-07-17 | 1987-01-29 | Ivan Sekoulov | METHOD FOR BIOLOGICALLY AND / OR PHYSICAL ELIMINATION OF UNWANTED WATER INGREDIENTS FROM WATER BY MEANS OF FLOODED BIOFILM REACTORS AND SYSTEM FOR IMPLEMENTING THE PROCESS |
WO1987003615A2 (en) * | 1985-12-14 | 1987-06-18 | Ivan Sekoulov | Process for supplying oxygen from fermentation plant and device for implementation of the process |
GB2191108A (en) * | 1986-06-05 | 1987-12-09 | Willinger Bros | Aquarium filter |
US4749654A (en) * | 1980-11-18 | 1988-06-07 | Chemap Ag | Method and apparatus for the submerged growth of cell cultures |
GB2217346A (en) * | 1988-03-07 | 1989-10-25 | Japan Gore Tex Inc | Culturing apparatus |
US4959322A (en) * | 1989-03-07 | 1990-09-25 | W. L. Gore & Associates, Inc. | Culturing apparatus |
CH676677A5 (en) * | 1989-01-27 | 1991-02-28 | Sulzer Ag | Permeable tubular membrane holding moving medium - transfers material to or from transversely flowing fluid medium |
US5091315A (en) * | 1985-09-03 | 1992-02-25 | The Board Of Trustees Of Stanford University | Bioconversion reactor |
GB2275922B (en) * | 1993-03-11 | 1997-09-10 | Biwater Europ Limited | Bifilm process and plant |
US10119110B2 (en) * | 2009-04-23 | 2018-11-06 | Hemarina | Bioreactor using oxygen-carrying molecules |
CN109592783A (en) * | 2019-01-22 | 2019-04-09 | 湖南中科环保技术有限公司 | A kind of high load capacity filters sewage disposal system ecologically |
-
1981
- 1981-05-05 GB GB8113700A patent/GB2075547B/en not_active Expired
Cited By (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4749654A (en) * | 1980-11-18 | 1988-06-07 | Chemap Ag | Method and apparatus for the submerged growth of cell cultures |
WO1987000517A1 (en) * | 1985-07-17 | 1987-01-29 | Braeutigam Hans Juergen | Flooded biological film reactor for water treatment, with gas charging via a membrane |
DE3544383A1 (en) * | 1985-07-17 | 1987-01-29 | Ivan Sekoulov | METHOD FOR BIOLOGICALLY AND / OR PHYSICAL ELIMINATION OF UNWANTED WATER INGREDIENTS FROM WATER BY MEANS OF FLOODED BIOFILM REACTORS AND SYSTEM FOR IMPLEMENTING THE PROCESS |
US4883594A (en) * | 1985-07-17 | 1989-11-28 | Ivan Sekoulov | Flooded biological film reactor for water treatment, with gas charging via a membrane |
US5091315A (en) * | 1985-09-03 | 1992-02-25 | The Board Of Trustees Of Stanford University | Bioconversion reactor |
WO1987003615A3 (en) * | 1985-12-14 | 1987-11-19 | Ivan Sekoulov | Process for supplying oxygen from fermentation plant and device for implementation of the process |
WO1987003615A2 (en) * | 1985-12-14 | 1987-06-18 | Ivan Sekoulov | Process for supplying oxygen from fermentation plant and device for implementation of the process |
GB2191108A (en) * | 1986-06-05 | 1987-12-09 | Willinger Bros | Aquarium filter |
US4783258A (en) * | 1986-06-05 | 1988-11-08 | Willinger Bros. | Filter cartridge with reuseable framework |
GB2191108B (en) * | 1986-06-05 | 1990-03-14 | Willinger Bros | Filter cartridges |
GB2217346A (en) * | 1988-03-07 | 1989-10-25 | Japan Gore Tex Inc | Culturing apparatus |
CH676677A5 (en) * | 1989-01-27 | 1991-02-28 | Sulzer Ag | Permeable tubular membrane holding moving medium - transfers material to or from transversely flowing fluid medium |
US4959322A (en) * | 1989-03-07 | 1990-09-25 | W. L. Gore & Associates, Inc. | Culturing apparatus |
GB2275922B (en) * | 1993-03-11 | 1997-09-10 | Biwater Europ Limited | Bifilm process and plant |
US10119110B2 (en) * | 2009-04-23 | 2018-11-06 | Hemarina | Bioreactor using oxygen-carrying molecules |
CN109592783A (en) * | 2019-01-22 | 2019-04-09 | 湖南中科环保技术有限公司 | A kind of high load capacity filters sewage disposal system ecologically |
Also Published As
Publication number | Publication date |
---|---|
GB2075547B (en) | 1984-06-06 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PCNP | Patent ceased through non-payment of renewal fee |