BIOREACTOR FOR THE CULTIVATION OF CELLS

Abstract

A bioreactor for the cultivation of cells, comprising at least one vessel which is designed to accommodate cells to be cultivated and at least one culture medium in a vessel interior enclosed at least partially by walls of the vessel in relation to an environment, and comprising a movement device which can be connected to a drive unit and at least partially moves the cells to he cultivated or applies a force to same. An elastic element is arranged in the vessel interior, which is configured such that at least one part of the culture medium can he received at least in a region of the elastic element and the cells to he cultivated at least intermittently adhere in and/or on at least sections of the elastic element, and the movement device is designed to at least intermittently deform the elastic element.

Claims

1. A bioreactor (1) for the cultivation of cells, comprising at least one vessel (2) which is adapted to accommodate the cells to be cultivated and at least one culture medium in a vessel interior (3) which is at least partially closed off from an environment by walls (6) of the vessel (2), and comprising a movement device (4) which can be connected to a drive unit (5) and which at least intermittently moves the cells to be cultivated or applies a force to them, characterized in that an elastic element (7) is arranged in the vessel interior (3), which is designed such that at least part of the culture medium can be accommodated at least in a region of the elastic element, and that the cells to be cultivated at least intermittently adhere at least in certain regions in and/or on the elastic element, and that the movement device (4) is adapted to deform the elastic element (7) at least intermittently.

2. The bioreactor according to claim 1, characterized in that the elastic element (7) comprises sponge-like material.

3. The bioreactor according to claim 2, characterized in that the sponge-like material comprises a foam.

4. The bioreactor according to claim 1, characterized in that the elastic element (7) comprises in vitro meat, bacteria, at least one polymer, a protein structure, glucomannan, zein, collagen, alginate, chitosan and/or cellulose.

5. The bioreactor according to claim 1, characterized in that the movement device (4) closes off the vessel interior (3) from the environment at least in certain regions.

6. The bioreactor according to claim 1, characterized in that at least one closable inlet (8) and outlet (9) are provided in each case, through which a flow channel for an air and/or gas flow between the vessel interior (3) and a fluid supply (10) or the environment can be established at least intermittently.

7. The bioreactor according to claim 6, characterized in that an inlet valve (11) is arranged in the inlet (8) and an outlet valve (12) is arranged in the outlet (9) and are designed in such a manner that opening and closing the inlet valve (11) and/or the outlet valve (12) is effected by a pressure change in the vessel interior (3).

8. The bioreactor according to claim 1, characterized in that the vessel (2) comprises at least one closable access (13) via which a connection from outside the vessel (2) to the vessel interior (3) can be established at least intermittently.

9. The bioreactor according to claim 1, characterized in that the drive unit (5) has at least one mechanically, pneumatically, hydraulically, electrically or electropneumatically driven drive element (14) which acts on the movement device (4) to generate a movement.

10. The bioreactor according to claim 1, characterized in that the movement device (4) has at least one piston which is movably mounted in or on the vessel (2) and during the movement of which the elastic element (7) is compressed and relaxed at least in certain regions at successive time intervals.

11. The bioreactor according to claim 10, characterized in that the drive unit (5) comprises at least one rotatably mounted cam as a drive element (14) which initiates the movement of the piston.

12. The bioreactor according to claim 1, characterized in that the movement device (4) has at least one membrane and/or screw which is movably mounted in or on the vessel (2) and during the movement of which the elastic element (7) is compressed and relaxed at least in certain regions at successive time intervals.

13. The bioreactor according to claim 1, characterized in that the movement device (4) has at least one membrane which at least partially closes off the vessel interior (3) from the environment and which, during operation, is at least intermittently deformed by a piston element connected directly or indirectly to the drive unit (5).

14. The bioreactor according to claim 13, characterized in that during operation, the membrane contacts the elastic element (7) at least intermittently.

15. The bioreactor according to claim 13, characterized in that during operation, the piston element is adapted to carry out a stroke of 90 to 110 mm, in particular of about 100 mm.

16. The bioreactor according to claim 15, characterized in that during operation, the piston element at least intermittently performs a linear or circular movement.

17. The bioreactor according to claim 1, characterized in that a sealing element (15) is arranged at least in regions between the movement device (4) and the vessel (2), which sealing element seals the vessel interior (3) in a liquid-tight and/or gas-tight manner against the environment.

18. The bioreactor according to claim 1, characterized in that the elastic element (7) is at least partially surface-treated.

19. The bioreactor according to claim 1, characterized in that at least one fixing element (16) is provided for fixing the elastic element (7) at least in certain regions to an inner side of at least one vessel wall (6) facing the vessel interior and/or to the movement device (4).

20. A use of a bioreactor for the production of artificial meat, for bacterial biofilm formation, for the cultivation of bacteria, for the production of a protein and/or for the cultivation of mammalian cells, comprising culturing suitable cells in the bioreactor of claim 1.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0033] FIG. 1 shows a bioreactor according to the invention in an operating situation with relaxed elastic element

[0034] FIG. 2 shows a bioreactor according to the invention in an operating situation with compressed elastic element, and

[0035] FIG. 3 shows a schematic illustration of a bioreactor according to the invention, the movement device of which has a piston and a piston rod.

[0036] FIG. 4 shows a picture of a special embodiment of a bioreactor designed according to the invention.

[0037] FIG. 5 shows a picture of an embodiment of the opened vessel of a bioreactor designed according to the invention with the elastic element which is arranged in the vessel interior and lies on an elevation of the vessel bottom.

DETAILED DESCRIPTION

[0038] In the following, the invention will be explained in more detail by means of exemplary embodiments with reference to the figures without limiting the general idea of the invention.

[0039] FIG. 1 shows a bioreactor 1 designed according to the invention with a sterilizable vessel 2, in the vessel interior 3 of which an elastic element 7 in the form of a sponge and a movement device 4 mounted to be movable relative to the vessel wall 6 are arranged. The elastic element 7 is fixed in the vessel interior by means of hooks which serve as fixing elements 16. On the surface and in the pores of the elastic element 7, cells are arranged which are cultivated in a suitable manner so that large-area or even three-dimensional cell structures, for example muscle fibers or artificial meat, can be produced.

[0040] Essential for the bioreactor 1 shown in FIG. 1 is that the movement device 4, which according to the explained exemplary embodiment, has a piston which can be moved along an inner side of the vessel wall 6 and during an operation intermittently deforms the elastic element 7 in the vessel interior 3 with the cells adhering thereto, wherein the elastic element is alternately compressed and relaxed, resulting in a corresponding change in volume. For this purpose, the piston of the movement device 4 moves alternately in opposite directions, either into the vessel 2 or out of the vessel, so that suitably an alternate compression and relaxation of the elastic element 7 and thus a stimulation of the cells adhering to the elastic element takes place, whereby improved cell growth can be implemented. A further advantage is that the elastic element 7 which, in this case, comprises sponge-like material, alternately absorbs and releases culture medium 18, so that the cells are evenly supplied with the nutrients contained in the culture medium 18 and still come into sufficient contact with the gaseous atmosphere contained in the vessel interior, in particular with the oxygen and or CO.sub.2 contained therein.

[0041] Between the piston of the movement device 4 and an inner side of the lateral vessel walls 6, a further sealing element 15 is provided, which ensures a reliable sealing of the vessel interior 3 against the environment According to the exemplary embodiment shown here, the sealing element 15 is designed in the form of a sealing ring and is attached to the piston of the movement device 4 so that it is moved together with the latter.

[0042] On a side opposite to the vessel interior 3, the movement device 4 is in operative connection with a drive unit 5 which as drive element 14 has a cam that is rotatably mounted and driven by an electric motor. A rotation of the cam causes the piston of the movement device 4 to move alternately either in the direction of the vessel interior or in the direction of the cam, wherein during the movement in the direction of the vessel interior 3, the elastic element 7 with the cells adhering thereto is compressed. This operating condition in which the elastic member 7 is compressed is shown in FIG. 2.

[0043] Hooks used as fixing elements 16 are arranged not only on the vessel wall 6 forming the bottom of the vessel 2, but also on that side of the piston of the movement device 4 that faces the vessel interior 3 and thus the elastic element 7. With these hook-shaped fixing elements 16, the elastic element is fixed in its position in the vessel interior 3 and, for example, an unintentional slipping is reliably prevented.

[0044] Furthermore, an inlet 8 with an inlet valve 11 and an outlet 9 with an outlet valve 12 are provided in the region of the piston of the movement device 4. Via the inlet, gas and/or culture medium 18 can be introduced into the vessel interior 3 from a corresponding fluid supply 10 and discharged accordingly via the outlet 9. Opening and closing the valves 11, 12 arranged in the inlet 8 and in the outlet 9 takes place here in dependence on the pressure prevailing in the vessel interior 3. Such a control of the valves 11, 12 has the great advantage that opening and closing the valves 11, 12 can be implemented in a comparatively simple and safe manner. Alternatively or additionally, it is conceivable to provide a central control unit 17 which generates suitable control signals for implementing an effective cultivation process and exchanges signals uni- or bidirectionally with the inlet and outlet valves 11, 12, but also with a drive unit 5, at least one sensor element, a fluid supply 10 and/or a device for specific temperature control of the vessel interior 3. A corresponding signal and/or data transmission can take place in a wired or wireless manner.

[0045] FIG. 1 shows a bioreactor 1 designed according to the invention in an operating state in which the piston of the movement device 4 is in a state moved out of the vessel interior 3, so that the elastic element 7 is relaxed and can at least partially receive culture medium 18.

[0046] In contrast, FIG. 2 shows a bioreactor 1 designed according to the invention in an operating state in which the piston of the movement device 4 is in a state maximally retracted into the vessel interior 3, so that the elastic element 7 is compressed to a minimum volume. In this case, the cam used as the drive element 14 of the drive unit 5 is rotated counterclockwise by about 260° to the left compared to the operating state shown in FIG. 1, as a result of which a corresponding movement of the piston has been initiated.

[0047] By selectively varying the shape of a cam and/or changing the rotational speed, both the degree of deformation and the speed at which the elastic element 7 arranged in the vessel interior 3 is deformed can be changed. Both the speed of a change in shape and the degree of a change in shape of the elastic element 7 take place in this case as a function of the parameters required for optimum cultivation of the cells arranged in the vessel interior 3 and in or on the elastic element 7.

[0048] By means of the bioreactor 1 shown in FIGS. 1 and 2, it is possible in a comparatively simple manner to set physiological growth parameters adapted to the respective cell type when cultivating cells of prokaryotic or eukaryotic origin. In particular, the type and magnitude of the stimuli which are to stimulate the cells to grow can be varied. A bioreactor 1 designed according to the invention enables the cultivation of special cell groups due to the application of external stimuli on a larger scale. Furthermore, even three-dimensional tissue structures for medicine or muscle fibers as starting material for cultivated meat can be produced. In this regard, a bioreactor designed according to the invention has the three main components shown in FIGS. 1 and 2, namely a sterilizable vessel 2, a movement device 4 with a piston, an alternately compressed and relaxed elastic element 7, and a fluid supply with an inlet 8 and an outlet 9 for the required gas exchange.

[0049] Furthermore, an access 13 is provided, which according to the illustrated exemplary embodiment is provided for taking samples of the culture medium 18 and/or the cells arranged in the vessel interior 3 as needed.

[0050] According to the special embodiment of the invention described here, the elastic element 7 is formed as a sponge made of glucomannan. However, depending on the cells to be cultivated in each case, the elastic element can also comprise other materials which are suitable for serving as a carrier for the cells to be cultivated and which can at least partially receive culture medium 18. By means of at least one suitable fixing element, the elastic element 7 can be fixed in the vessel interior 3 in an advantageous manner. For this purpose, the configurations shown in FIGS. 1 and 2 provide that hooks for anchoring are arranged on the bottom of the bioreactor 1 and on the underside of the piston of the movement device 4. The elastic element 7 serves in each case as a structural matrix for the attachment of the cells to be cultivated.

[0051] FIG. 3 additionally shows a schematic illustration of a bioreactor 1 designed according to the invention, the movement device 1 and fluid supply of which, however, are designed differently from the bioreactor 1 shown in FIGS. 1 and 2. The functional principle essential to the invention, namely the compression of an elastic element 7 arranged in the vessel interior 3 together with the cells to be cultivated adhering thereto, which compression is effected by a movement device 4, is also implemented with the device shown in FIG. 3. The essential difference to the bioreactor 1 shown in FIGS. 1 and 2 is that the movement device 4 comprises a piston and a piston rod which establishes the connection between the piston acting on the elastic element 7 in the vessel interior 3 and a drive unit 5 arranged outside the vessel 2. According to this embodiment, the piston rod protrudes through the vessel wall 6 such that a comparatively small sealing element 15 is arranged between the sealing surfaces of the vessel wall 15 and the piston rod. In this case, the supply and discharge of at least one fluid into and/or out of the vessel interior 3 is takes place via an inlet 8 and an outlet 9 which are arranged within the vessel wall 6 and thus establish a connection between the vessel interior 3 or a fluid supply system (not shown in this view). The remaining components, such as different accesses or a control unit, as shown in FIGS. 1 and 2, cannot be seen in the schematic illustration according to FIG. 3, but can also be used in this special embodiment without limiting the general idea of the invention.

[0052] The movement of the movement device 4 and thus of the elastic element 7 in the vessel interior 3 is generated by means of a suitable drive unit 5. For this purpose, the drive unit 5 in the figures has a cam as a drive element 14 which can be part of a camshaft and, due to its movement, initiates an up and down movement of the piston. Of course, it is also conceivable to implement the invention by means of other drive units, drive elements and/or movement devices than those shown in the figures. It is always essential to the invention that an elastic element with cells adhering thereto is arranged inside the vessel of the bioreactor, which elastic element is alternately deformed, in particular compressed and relaxed, by means of a movement device. Advantageously, a sponge-like material which can be of synthetic or natural origin is used for such an elastic element. Here, the physically induced stimulation of the cells to be cultivated is achieved by the mechanical compression and relaxation of the elastic element forming the cell-containing matrix. In this manner, not only the required gas supply, in particular the air exchange via the valves arranged in the inlet and outlet is implemented, but at the same time also a constant, homogeneous supply of nutrients by the culture medium which is alternately absorbed and released by the elastic element.

[0053] Thus, a bioreactor designed according to the invention represents a simple and efficient technical solution for stimulating cells and biofilms for the desired phenotypic transformation, for example, differentiation of myoblasts into microtubules. Furthermore, such a bioreactor is easily scalable, has components that are comparatively wear-resistant and enables particularly gentle cell cultivation.

[0054] Furthermore, FIG. 4 shows a special embodiment of a bioreactor 1 designed according to the invention. By means of a prototype, the general functionality of such a bioreactor 1 has already been demonstrated using an elastic element, in or on which no cells were provided, and water as culture medium 18.

[0055] The bioreactor 1 shown in FIG. 4 has a drive unit 5 with a pneumatic cylinder 21 pressurized with compressed air in which a piston rod 19 is guided, the end of which facing the vessel 2 is connected to a piston element 20 of the movement device 4. The tests were carried out with a double-acting pneumatic cylinder 21 ZDM 25/100 according to ISO 6432, the piston rod 19 of which has an outer diameter of 25 mm and which carries out a maximum stroke of 100 mm. The pneumatic cylinder 21 is mounted on a frame 23 which is made of stainless steel and has a base plate 24 as its base. The movement device 4 also has a membrane 22, in this case a silicone membrane, which closes off the vessel interior 3 of the vessel 2 at the top from the environment and which, in operation, is deformed by the piston element 20 during a movement of the piston rod 19 and as a result is moved at least intermittently downwards in the direction of the elastic element 7 which is arranged in the vessel interior 3 and is compressed as a result

[0056] Furthermore, the bioreactor 1 shown in FIG. 4 has a vessel 2 with a lower connection with a spout as access 13 for sampling and a connection with a spout combining an inlet 8 and an outlet 9 for gas exchange. A silicone hose with a hose clamp for shut-off is fixed to the lower spout while a silicone hose with a hydrophobic PTFE air filter (PTFE=polytetrafluoroethylene) is connected at the top. On the flat vessel bottom, a round and internally hollow elevation made of stainless steel and provided with holes is arranged to accommodate an elastic element 7.

[0057] For a special test run, the movement of the piston element was set to 4-5 cycles per minute, with one cycle corresponding to an upward and downward movement. A commercially available Konjac sponge made of glucomannan from BlueFox was used as the elastic element 7, which forms a three-dimensional structure during operation, for example, for the production of artificial meat or for bacterial biofilm formation. Before the use in the bioreactor 1, this sponge forming the elastic element 7 was autoclaved in 100 ml of phosphate-buffered saline (PBS) with a composition of 8.0 g sodium chloride (NaCl), 0.2 g potassium chloride (KCl), 1.42 g disodium hydrogen phosphate (Na.sub.2HPO.sub.4), 1.78 g disodium hydrogen phosphate dihydrate (Na.sub.2HPO.sub.4.2H.sub.2O), and 0.27 g potassium dihydrogen phosphate (KH.sub.2PO.sub.4), pH 7.4, and placed in 100 ml of fresh phosphate buffered saline (PBS) overnight at room temperature.

[0058] To perform the test, the elastic element 7, here the Konjac sponge, was placed on the elevation and about 350 ml of liquid was filled into the vessel interior 3 so that the sponge was well saturated and half of it was in the liquid.

[0059] The vessel interior 3 is separated from the environment by a membrane 22, in this case a commercially available round silicone lid with a diameter of at least 15 cm, wherein the membrane 22 forms part of the movement device 4 for specific deformation of the elastic element 7. The membrane 22 is fixed by a metal ring 26 on the upper side of the vessel wall 6 by means of screws.

[0060] During operation, the pneumatic cylinder of the drive unit 5 was pressurized with compressed air at a pressure of 4-5 bar (0.4-0.5 MPa) and the piston rod 19 was moved in the desired pumping cycle of 4-5 cycles per minute. The piston rod 19 and the piston element 20 attached thereto are arranged centrally directly above the membrane 22 in such a manner that, in operation, the piston element 20 presses the membrane 22 downward during a downward movement and the membrane surface, at least in a central region, bulges downward at least 5 cm, thereby deforming the elastic element 7 in the form of the Konjac sponge, forcing culture medium 18 out of the elastic element 7 and displacing air from the vessel interior 3. During an upward movement of the piston element 20, in turn, air flows into the vessel interior 3 and the elastic element 7 sucks in culture medium 18. A commercial incubator was used as the vessel 2 for the test run, and the test was conducted at an ambient temperature of 27° C. for at least 24 hours. It was found that the prototype was fully functional and exhibited stable operating behavior over a long period of time.

[0061] In addition, FIG. 5 shows the opened vessel 2 with the elastic element 7 which is arranged in the vessel interior 3 and lies on an elevation 25 of the vessel bottom. The elastic element 7 shown here, which forms a three-dimensional structure during operation, for example for the production of artificial meat or for bacterial biofilm formation, is a commercially available Konjac sponge made of glucomannan from the company BlueFox. Before being placed in the vessel interior 3 of the bioreactor 1, this sponge forming the elastic element 7 was autoclaved in 100 ml of phosphate-buffered saline (PBS) with a composition of 8,0 g sodium chloride (NaCl), 0.2 g potassium chloride (KCl), 1.42 g disodium hydrogen phosphate (Na.sub.2HPO.sub.4), 1.78 g disodium hydrogen phosphate dihydrate (Na.sub.2HPO.sub.4.2H.sub.2O), and 0.27 g potassium dihydrogen phosphate (KH.sub.2PO.sub.4), pH 7.4 and placed in 100 ml of fresh phosphate-buffered saline (PBS) overnight at room temperature.

[0062] In the following, the cultivation of the bacterial strain Streptomyces spec. using a bioreactor 1 designed according to the invention is described as an example, wherein Streptomyces sp. DSM No.: 40434 (DSMZ, Germany) was used for the initial growth test in the new bioreactor 1. The Streptomyces strain was grown in 50 ml of complete medium 2YTPG (16 g/L tryptones, 10 g/L yeast extract, 5 g/L sodium chloride (NaCl), 5 g/L glucose, 3 g/L potassium dihydrogen phosphate (KH2PO4), 9 g/L dipotassium hydrogen phosphate (K.sub.2HPO.sub.4-3H.sub.2O) in a 250 ml baffled Erlenmeyer flask and incubated at 180 rpm and 28° C. for 24 hours. Cells were then pelletized in a 50 ml reaction vessel at 4700 rpm for 10 min and then resuspended in 25 ml minimal medium R2 (Hopwood D. A., Bibb M. J., Chater K. F., Kieder T., Bruton C. J., Kieser H. M., Lydiate D. J., Smith C. P., Ward J. M., Schrempf H. 1985. Genetic manipulation of Streptomycetes—a laboratory manual. The John Innes Foundation, Norwich) for pigment formation. The cells were added to 325 ml of minimal medium in a bioreactor 1 designed as shown in FIG. 4 and incubated at 28° C. for >72 hours. Instead of an elastic element 7 made of glucomannan, a commercial polyurethane sponge was used as the elastic element. For this test run, the flask movement was set to 4-5 cycles per minute. Cells could be detached from elastic element 7 after completion of the test run for fermentation, visible by turbidity of the medium. Under a microscope (Olympus BX41), hyphae structures typical of streptomyces were clearly visible. The antibiotic and pigment actinorhodin produced by the bacteria could be extracted with methanol and caused the specific red coloration of the solution. The pigment formation showed that a bioreactor 1 formed according to the invention can be used for the production of industrially relevant substances, such as antibiotics.

[0063] In a further test, red fluorescent protein tdTomato was produced in E. coli using a bioreactor 1 designed according to the invention, which in turn was designed according to the special configuration shown in FIG. 4. Here, the production of a recombinant protein was investigated as a further test object for the bioreactor 1.

[0064] The aim was to produce red fluorescent protein tdTomato, which is already optically visible in daylight and acts as a pigment. Plasmid pUC57_T7_td-tomato was transformed into chemically competent BL21-AI One Shot E. coli cells according to the manufacturer's instructions (Thermo Fisher Scientific) and plated on LB agar plates, consisting of yeast extract (5 g/L), tryptone (10 g/L), sodium chloride (0.5-10 g/L), and agar (15 g/L) (pH adjusted to 7 with NaOH), with 100 μg/ml ampicillin and incubated at 37° C. overnight. One colony was used to inoculate a test tube with 5 ml of fresh LB medium the next day and incubated overnight at 37° C. and 160 rpm. A glycerol stock containing 25% (w/v) sterile glycerol was made from this culture the next day and used as a starting point for all further tests. In a 250 mL baffled Erlenmeyer flask, the strain was grown as a preculture in 50 mL of medium without induction and allowed to grow overnight at 37° C. and 200 rpm. Then, a bioreactor 1 designed according to the embodiment shown in FIG. 4 was prepared and filled with 300 mL of medium. Thereafter, the cells were pelleted from 50 ml of the preculture in a 50 ml reaction vessel and resuspended in 50 ml of fresh medium. Subsequently, the solubilized cells were added to the medium in the bioreactor 1, the bioreactor 1 was sealed, and were incubated overnight at 37° C. at 2-3 pump cycles per minute. For the bioreactor run, the piston movement was set to 4-5 cycles per minute. The next day, cells, clearly producing the red pigment and thus the recombinant protein tdTomato, could be extracted from the sponge material of the elastic element 7. This illustrated that a bioreactor 1 designed according to the invention can be used for the production of recombinant proteins.

[0065] In a further special test, the functionality of a bioreactor 1 designed according to the invention for the cultivation of mammalian cells was to be demonstrated. Here, the mammalian cell line C2C12 was to be cultivated, which is an immortalized myoblast cell line from Mus musculus (see Yaffe, D., Saxel, O. Serial passaging and differentiation of myogenic cells isolated from dystrophic mouse muscle. Nature 270, 725-727 (1977) https://doi.org/10.1038/270725a0) and is suitable for demonstrating growth of muscle cells and their precursors because of its stable growth. The C2C12 cell line shows rapid differentiation and forms contractile myotubes and produces characteristic muscle proteins. Before the start of the test, a bioreactor 1 designed as shown in FIG. 4 was disassembled into its individual parts which were wrapped in aluminum foil, sterilized by autoclaving, and assembled under a sterile bench. A Konjac sponge (Bluefox, white) was used as the elastic element 7, was placed in 100 ml of PBS (phosphate-buffered saline) and autoclaved after swelling. Then, the elastic element 7 was placed in sterile and fresh 100 ml PBS and incubated with 0.001% poly-L-lysine for coating for better adhesion. Thereafter, the elastic element 7 was washed three times with 100 ml of sterile PBS each time. As medium, 350 ml of Dulbecco's Modified Eagle's Medium with glucose but without pyruvate (DMEM) was used. For inoculation, 2*10.sup.7 cells were used and added to the medium alongside the elastic element 7 of glucomannan. The bioreactor 1 was sealed with a membrane 22 made of silicone and placed under the drive unit 5. This was followed by incubation for at least 72 hours at two to three piston movements per minute at an ambient temperature of 37° C. with 5% CO.sub.2 in the incubator atmosphere. After at least 72 hours, the reactor was opened under a sterile bench, the elastic element 7 in the form of a glucomannan sponge was washed with PBS and then examined microscopically. The microscopic inspection was performed using the Leica DM IL LED inverted laboratory microscope. Contamination with bacteria was not detectable. After trypsinization of the glucomannan material, SYTO9 fluorescent dye (Thermo Fisher Scientific) with the excitation wavelength of 485 nm and emission wavelength of 498 nm was used to stain the detached cells and detect live cells. By means of microscopic analysis, significant fluorescence of C2C12 cells from the glucomannan fraction was detected. Thus, cell growth was detected on the material from glucomannan in the bioreactor 1 designed according to the invention and the bioreactor's suitability for growing animal cells was demonstrated.

REFERENCE LIST

[0066] 1 bioreactor [0067] 2 vessel [0068] 3 vessel interior [0069] 4 movement device [0070] 5 drive unit [0071] 6 vessel wall [0072] 7 elastic element [0073] 8 inlet [0074] 9 outlet [0075] 10 fluid supply [0076] 11 inlet valve [0077] 12 outlet valve [0078] 13 access [0079] 14 drive element [0080] 15 sealing element [0081] 16 fixing element [0082] 17 control unit [0083] 18 culture medium [0084] 19 piston rod [0085] 20 piston element [0086] 21 pneumatic cylinder [0087] 22 membrane [0088] 23 frame [0089] 24 base plate [0090] 25 elevation [0091] 26 metal ring