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
  • C12M23/00—Constructional details, e.g. recesses, hinges
  • C12M23/02—Form or structure of the vessel
  • C12M23/12—Well or multiwell plates
• • 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
  • C12M29/00—Means for introduction, extraction or recirculation of materials, e.g. pumps
  • C12M29/10—Perfusion

Definitions

• the invention relates to a method and an apparatus for the cultivation of tissue cells.
• tissue engineering The cultivation of tissue cells plays a role in so-called "tissue engineering".
• the aim here is to artificially create cell tissue with body-specific properties.
• cells are cultivated on certain biomatrices (structures). Areas of application for "tissue engineering” are z.
• Biomaterials, drug compatibility tests or toxicity tests for certain substances are biomaterials, drug compatibility tests or toxicity tests for certain substances.
• the production of functional tissues can be carried out in several steps, with important points being the control of the differentiation in the cultivated tissue and a specific geometric structure of the implant (e.g.
• Bottle cultures propagated in a special nutrient medium to increase the number of cells.
• tissue support For further cultivation, one possible concept is to apply the cells to a special tissue support. This can be filter pads, fleeces or matrices with a sponge structure, optionally act from biodegradable polymers. The tissues created in this way are then cultivated until a tissue with the desired properties has formed.
• the most common method is cultivation under so-called static conditions in special culture bottles (T-bottle, 12-well plate, etc.), which are placed in a special incubator with appropriate temperature control and an atmosphere enriched with carbon dioxide.
• the used nutrient medium is exchanged for fresh one at certain intervals. Fumigation (supply of oxygen) usually takes place from the atmosphere of the
• the tissues can be introduced into a bioreactor (a so-called perfusion chamber) which is continuously flowed through with culture medium and in which an improved and controlled supply of substrates and oxygen as well as a disposal of
• Metabolic products can take place.
• the culture medium can be pumped out of a fumigated receptacle in a circuit or, alternatively, can be discarded after passing through the perfusion chamber once.
• the object of the present invention is therefore to provide a method and an apparatus for cultivating tissue cells with which the disadvantages described can be eliminated.
• the tissue cells should be adequately supplied with gas and nutrient medium.
• a gas stream is generated which is opposite to the direction of flow of the nutrient medium. This ensures, above all with an arrangement of several tissue cultures, that all tissue cultures are adequately supplied with gas, in particular with oxygen, and that there is no undesired depletion of oxygen over the length of the culture area.
• the thin layer of the nutrient medium above the tissue cells is 0.1 ... 3.0 mm, preferably 0.5 ... 1.0 mm.
• the formation of a thin nutrient medium layer above the tissue cells can preferably be achieved by passing nutrient medium into a culture area in which the tissue cells are located. An overflow from the culture area is then generated with the nutrient medium, and the nutrient medium arrives in a collecting chamber after the tissue cells have overflowed. The nutrient medium is then removed again from the collecting chamber.
• the method according to the invention is particularly suitable for the cultivation of human, animal and vegetable Cells.
• the person skilled in the art knows which nutrient medium is required for cultivation.
• the nutrient medium can be composed accordingly.
• Oxygen required there is usually a need for carbon dioxide in plant cells.
• Buffer capacity or pH adjustment may be required.
• the method according to the invention is suitable for the multiplication of implantable cells.
• Cells that are implanted in the human or animal body are, in particular, skin or bone tissue cells as well as cartilage and vascular cells.
• the method is also suitable for obtaining implantable cartilage constructs or bone constructs. Especially for obtaining such constructs, the method according to the invention offers the advantage that the tissue cells assume three-dimensional structures and can nevertheless be adequately supplied with nutrient medium and oxygen.
• the method according to the invention is also suitable for carrying out activity and toxicity tests.
• the effect of medication, environmental toxins and the like on the tissue cells can be investigated in order to enable an alternative to animal testing.
• the substance to be examined can be classified according to its either use the respective aggregate state in the gas phase or add it to the nutrient medium in solid or liquid form.
• FIGS. 1 and 2 show a schematic representation of a treatment apparatus with a gas supply unit and exhaust air duct connected to it,
• FIG. 3 shows a schematic illustration of a treatment apparatus with individual inserts
• FIG. 4 shows a schematic representation of a treatment apparatus with carriers for adherent cell cultures
• FIG. 5 is a schematic representation of a treatment apparatus without a special gas line
• Figure 6 is a schematic representation of a treatment apparatus for pressurization.
• Figure 1 is a device for the cultivation of
• Tissue cells are shown with a treatment apparatus 1, in which the treatment apparatus 1 has a culture area 2, in which tissue cells, not shown, are brought into contact with nutrient medium.
• the treatment apparatus 1 has an inlet 32 and an outlet 33 for the nutrient medium, so that the nutrient medium from one end 30 of the culture area 2 to the other end 31 can flow.
• the nutrient medium then arrives in a collecting chamber 4.
• the nutrient medium is drawn off from the collecting chamber 4 via the line 6.
• a pump 17 transports the nutrient medium in the circuit via line 5 back into the culture area 2. With the help of the pump 17, the
• 1 also provides a gas supply unit 13, by means of which a definable mixture of different gases, for example from air, oxygen, nitrogen and carbon dioxide, can be produced and supplied to the treatment apparatus 1.
• the gas supply unit 13 can also have flow meters 18, 19 and a sterile filter 20.
• Humidifiers 21 can also be provided in order to moisten the gas with water before it is introduced into the treatment apparatus 1.
• Via line 10 the gas passes through the gas inlet opening 8 into the interior 12 of the treatment apparatus 1.
• Gas is applied to the nutrient medium located in the culture area 2. The gas flows in the opposite direction to the flow of the nutrient medium via the nutrient medium and leaves the interior 12 of the
• a line 11 is connected to the gas outlet opening 9, via which the gas is led to an exhaust air duct 22.
• the exhaust air line contains a sterile trap 23 and an exhaust air filter 24.
• the flow rate of the nutrient medium also has an influence on the growth of the tissue cells.
• the one chosen in Figure 1 Experimental arrangements were fed up to 5 ml of nutrient medium per minute. The delivery rate was preferably 0.25 to 1 ml / min. In the experimental arrangement shown in FIG. 2, only up to 30 ml / day, preferably 2.5 to 10 ml / day, were delivered.
• fresh nutrient medium is constantly sucked out of a storage bottle 26 by means of a pump 25 and fed into the culture area 2 of the treatment apparatus 1. Used medium is collected in a collecting bottle 27.
• FIG. 3 shows the treatment apparatus 1 in an enlarged view. Inlets and outlets for gas and nutrient medium are indicated by arrows.
• the treatment apparatus 1 has a bottom profile 34, which is provided for receiving supports 14, 16 for the tissue cells.
• An overflow edge 28 is formed on the bottom profile 34, via which the nutrient medium can flow from the culture area 2 into a collecting chamber 4.
• the overflow edge 28 is formed in the exemplary embodiment shown by an elevated side wall 3 of the floor profile 34.
• These embodiments also have the special feature that special inserts 15 are provided for pre-structured, three-dimensional supports 14, which can be compact or macroporous.
• the inserts 15 are detachably connected to the bottom profile 34. They can preferably be screwed into the bottom profile 34 from below. In the installed state of the inserts 15, the tissue cells are then positioned so that a thin layer of nutrient medium can flow over them. After this The nutrient medium then flows over the tissue cells into the collecting chamber 4.
• the carrier 14 shown in Figure 3 are preferably arranged in one or two rows in a flow channel, not shown.
• the width of the flow channel can be 5 to 7 cm. Larger widths may have the disadvantage that a uniform flow profile cannot form in the flow channel. In contrast, the length of the flow channel does not play a role
• Role If possible, however, it should not be larger than 20 to 25 cm, so that about 5 to 10 supports 14 can be accommodated in the flow channel.
• FIG. 4 shows, as a further special feature, special carriers 16 which are designed for adherent cell cultures.
• the carrier 16 are preferably made of glass or suitable plastics. Like the carriers 14 according to FIG. 3, they are positioned such that the nutrient medium can flow in a thin layer over the tissue cells located in the inserts 16 and reach the collecting chamber 4.
• FIG. 5 shows a treatment apparatus 1 in which gas enters the interior 12 by diffusion.
• a gap-shaped opening is provided in the upper part 7 as the gas inlet opening 8, which can also be closed with a diaphragm to avoid contamination.
• Derivatives for the nutrient medium continue to exist. They are identified by arrows.
• a device with such a treatment apparatus 1 does not require any special fumigants.
• the cultivation of tissue cells can be carried out in a heating cabinet without additional equipment.
• FIG. 6 shows an embodiment with a treatment apparatus 1 in which the interior 12 is pressurized.
• a defined overpressure can be set via suitable valves 29 a-d, by means of which, for example, the passage of gaseous substances into the nutrient medium is facilitated and the supply of the tissue cells with these substances is improved.

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

Applications Claiming Priority (3)

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• 2002
  • 2002-02-27 DE DE2002108311 patent/DE10208311B4/de not_active Expired - Lifetime
• 2003
  • 2003-02-27 DE DE10390723T patent/DE10390723D2/de not_active Expired - Fee Related
  • 2003-02-27 CA CA002477583A patent/CA2477583A1/en not_active Abandoned
  • 2003-02-27 US US10/505,896 patent/US20050106720A1/en not_active Abandoned
  • 2003-02-27 EP EP03722203A patent/EP1478729A2/de active Pending
  • 2003-02-27 WO PCT/DE2003/000668 patent/WO2003072697A2/de active Application Filing
  • 2003-02-27 AU AU2003229484A patent/AU2003229484A1/en not_active Abandoned
  • 2003-02-27 JP JP2003571387A patent/JP2005518207A/ja not_active Withdrawn

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