LIGHT-DIODE REACTOR

Abstract

The present invention relates to a reactor including a tank (1) and a lighting device (2a-2g) disposed in the tank (1), said lighting device being flexible in at least one direction.

Description

Description Title of the invention: LIGHT DIODE REACTOR FIELD OF THE INVENTION.

[0001] — The present invention relates to the general technical field of reactors integrated lighting, particularly for the cultivation of photosynthetic microorganisms. BACKGROUND OF THE INVENTION.

[0002] — The notion of bioreactor here designates a reactor within which develop biological phenomena, such as growth of crops of a single type or consortium of microorganisms (notably microalgae), in very specific fields various such as effluent treatment, production of biomass containing bio- molecules of interest (i.e. biomolecules that we know how to exploit) and / or metabolite products.

[0003] — A bioreactor typically comprises a tank (cylindrical or parallelepiped) containing a culture medium for biological species (yeasts, bacteria, fungi microscopic, algae, animal and plant cells) for: biomass production, or for the production of a metabolite, or for the bioconversion of a molecule of interest.

[0004] — Various types of operating conditions may be necessary for the growth of biological species within such a bioreactor; we thus know, in particular, autotrophic (or photoautotrophic) growth regimes with a supply of light (on also speaks of photosynthesis). It should also be noted that light can act on the metabolism of cells by inducing or repressing the production of certain compounds, independently of growth and photosynthesis. A supply of light during cultivation can therefore be useful even when the microorganisms are heterotrophs.

[0005] = In the following, we will focus more specifically on photo-bioreactors, that is to say to bioreactors in which a supply of light (continuously, cyclically, or in the form of pulses) is implemented.

[0006] — Photo-bioreactors have already been proposed in which the light supply is carried out from inside the tank. Document US 3,986,297 proposes in particular a photo- bioreactor in which the supply of light is achieved by immersion, in the medium of culture, means of illumination (such as xenon lamps). A disadvantage of This solution is that the efficiency of the photo-bioreactor is inversely proportional to its dimensions. Thus, the more the dimensions of the photo-bioreactor increase, the more its effectiveness decreases.

[0007] — Photo-bioreactors have also been proposed in which the light supply is carried out from the outside of the tank. In particular, a well-controlled configuration consists of equipping the tank with portholes allowing the penetration of light generated from outside the tank (natural or artificial light). A disadvantage of such a configuration is that the portholes limit the illumination surface and absorb or reflect a significant portion of the photons emitted by the lighting source. Whether the light is supplied from inside or outside the tank, the productivity of a photobioreactor is directly linked to its specific surface area (ratio of illuminated surface area to culture volume). It is therefore necessary for the photobioreactor to have a large illuminated specific surface area. Whether flat or cylindrical, a disadvantage of current photo-bioreactors is that they must occupy a large floor space for their productivity to be acceptable. Furthermore, whatever the light source chosen to illuminate the culture medium (Neon, LEDs, Natural Light), its contribution in photonic energy is carried out in a very localized manner, so that: most of the photons emitted by the light source cannot be biologically consumed by the microorganism due to a energy overload, the dissipation of heat generated by the light source is poorly controlled, It is complex and expensive to produce large-scale photo-bioreactors. measurements. An aim of the present invention is to propose an economical photo-bioreactor, both in terms of investment and operating costs, and whose land use is reduced. Another aim of the invention is to provide a large capacity photo-bioreactor (tank of 1000 liters or more) in which the yield in quantity of photons (umol-ph-s-1) supplied by a luminous surface per unit of power (Watt) is optimized. BRIEF DESCRIPTION OF THE INVENTION. For this purpose, the invention proposes a reactor including: a tank intended to contain a mass to be treated, the tank comprising a wall lower forming a bottom, an upper wall opposite the lower wall, and at least one side wall between the bottom and top walls, a set of flexible lighting devices contained within the tank and intended to promote the treatment of the mass, at least one electrical power supply module connected to each lighting device, remarkable in that each flexible lighting device includes: a peripheral framework composed of: of two flexible longitudinal edges, and of two transverse borders, each transverse edge extending between a respective pair of free ends of the longitudinal edges, and a flexible central sheet on the edges of which the peripheral frame is mounted spherical, the flexible central sheet including: at least one flexible plate, a flexible coating layer transparent to radiation luminous, said coating layer extending over the plate flexible, a group of light diodes extending between the flexible plate and the flexible coating layer, said light diodes being oriented so as to generate light radiation in a direction opposite to the flexible plate. This solution provides a more ergonomic photo-bioreactor in which the extraction of the lighting devices is facilitated. Indeed, the flexibility of each lighting device allows it to be extracted by moving it in a horizontal direction above the tank, for example by circulating it on rollers of a roller conveyor positioned above the tank. It is thus possible to reduce the height required to extract said lighting device(s) from the tank, for example as part of a maintenance operation. This solution also makes it possible to obtain a photo-bioreactor with better yields (energy on the one hand, and biomass production on the other) than existing photo-bioreactors. Indeed, the flexibility of each lighting device allows it to conform to the geometry of the photo-bioreactor, and thus to maximize the illuminated surface / illuminated volume ratio directly in contact with the culture medium. Furthermore, the flexibility of the plate(s) makes it possible to improve the kinetics of movement of the medium in certain areas of the photo-bioreactor, in particular by limiting the formation of circular secondary flows around a main flow of the medium, as will be described in more detail below with reference to the figures. Preferred but non-limiting aspects of the assembly according to the invention are the following: each light emitting diode can be an organic light emitting diode flexible (OLED), each light diode being in contact with a diode adjacent light; each light-emitting diode can be chosen from a conventional light-emitting diode (LED), or a mini light-emitting diode (mini LED), the light-emitting diodes being spaced from each other by a distance greater than or equal to 50um; each transverse border can be flexible so that the peripheral frame is flexible in two orthogonal directions; each transverse edge may be rigid such that the peripheral frame is flexible in a single direction parallel to the longitudinal edges; each transverse edge may include a rigid frame and a rigid strand of lesser length than the rigid frame, the rigid frame and the strand being connected by a pivot connection such that the strand is able to pivot relative to the frame; each flexible border may comprise a succession of rigid segments connected to each other by pivot links so that each segment is able to pivot relative to an adjacent segment; each flexible edge may consist of a bead made of a material identical to a material constituting the flexible plate; said and at least one lighting device may be parallelepipedal in shape, the reactor including a rigid support structure comprising housings, each housing being intended to receive a respective flexible lighting device and being configured so as to bend the lighting device in the tank; each light emitting diode may comprise a stack of structures, each structure being adapted to emit light radiation in a respective wavelength range; the reactor may also comprise at least one controller (6) configured to control said and at least one electrical energy supply module (5); said and at least one controller can be configured to control a variation in energy supplied by said and at least one power supply module in order to modify over time the emission spectrum of said and at least one lighting device; said and at least one controller can be configured to: control the continuous activation of said and at least one module electrical power supply such that said and at least one lighting device (2a, 2b) generates light radiation continuous, control the discontinuous activation of said and at least one module electrical power supply such that said and at least one lighting device (2a, 2b) generates light radiation discontinuous in the form of flashes composed of alternating phases dark and light phases, for example at a frequency between 10 and 50 kHz; the material constituting said coating layer may be flexible glass; the material constituting the coating layer may be a syn- resin synthetic or semi-synthetic resin chosen from (meth)acrylic resins re- crosslinked, crosslinked styrene resins, polyurethane resins, polyester resins, silicone resins, fluorinated resins, resins prepared from inorganic substances such as silica, carbonate calcium and barium sulfate; at least two light diodes of the plurality of light diodes may be of different sizes; the plurality of light-emitting diodes may comprise: at least one ultraviolet emitting light diode, and / or at least one phosphorescent light diode. BRIEF DESCRIPTION OF THE FIGURES. Other advantages and characteristics of the reactor according to the invention will emerge more clearly from the following description of several variant embodiments, given as non-limiting examples, from the attached drawings in which: [Fig.1] is a schematic perspective representation of an example of bioreactor; [Fig.2] is a schematic representation of a first example of a tablecloth central unit of a lighting device; [Fig.3] is a schematic cross-sectional representation of a example of a light diode structure; [Fig.4] is a schematic representation of the light distribution of the light emitted by a conventional light-emitting diode (LED); [Fig.5] is a schematic representation of the light distribution of the light emitted by an organic light-emitting diode (OLED); [Fig.6] is a schematic representation of a second example of a tablecloth central unit of a lighting device; [Fig.7] is a representation of a third example of a central sheet of a lighting device; [Fig.8] is a schematic cross-sectional representation of a bio- prior art reactor; [Fig.9] is a partial schematic representation of a flow in the bioreactor shown in [Fig.8]; [Fig.10] is a schematic cross-sectional representation of a alternative embodiment of a bioreactor according to the invention: [Fig.11] is a schematic representation of a maintenance system of bioreactor according to the invention; [Fig.12] is a schematic representation of another embodiment variant of the bioreactor according to the invention; [Fig.13] is a graph representing the productivity of a chlorella in the variant embodiment of the bioreactor illustrated in [Fig.12]; [Fig.14] is a curve illustrating the maximum concentration of microalgae depending on a distance between two adjacent lighting devices; [Fig.15] is a schematic diagram illustrating the difference between lighting continuous and discontinuous lighting; [Fig.16] represents microalgae concentration curves as a function of a spacing between two adjacent lighting devices in the case of a continuous lighting on the one hand and in the case of discontinuous lighting on the other part, [Fig.17] is a schematic representation in front view of a device lighting, [Fig.18] is a schematic representation in side view of a border of peripheral framework, [Fig.19] is a schematic representation in top view of a border of peripheral framework. DETAILED DESCRIPTION OF THE INVENTION. We will now describe different examples of photo-bioreactors according to the invention with reference to the figures. In these different figures, equivalent elements are designated by the same numerical reference. 1. Generality. With reference to [Fig.1], the bioreactor may comprise: a tank 1 intended to receive a mass to be treated, a plurality of lighting devices 2a-2g, a plurality of diffusion units 3 of carbon dioxide (CO,) in the form of gas bubbles or in the form of a fluid consisting of CO, dissolved in a aqueous medium, an electrical power supply module 5, a controller 6 for controlling the plurality of lighting devices 2a-2g, the plurality of diffusion units 3, and the power supply module electrical energy 5. Each lighting device is intended to be integrated into the tank 1 for the treatment of a culture medium 4 contained in the tank 1. These lighting devices 2a-2g are intended to be completely immersed in the culture medium 4. The lighting devices 2a-2g may be of different heights. Alternatively, the lighting devices 2a-2g may all be of identical height. This makes it possible to simplify the installation of the lighting devices by an operator. In the following, the bioreactor will be described with reference to the treatment of a biomass formed by microorganisms, for example microalgae. It is understood, however, that the following description also applies to other types of reactors in the field of microbiology. In the embodiment illustrated in [Fig.1], the bioreactor comprises: a first group 2a, 2c, 2e, 2g of lighting devices arranged at a non-zero distance from the bottom of the tank. and a second group 2b, 2d, 2f of lighting devices in contact with the bottom of the tank. To increase the mixing and homogenization of the mass to be treated, the diffusion units 3 can be arranged every two lighting devices so that two successive diffusion units 3 are separated by two adjacent lighting devices. In particular and with reference to [Fig. 1], the diffusion units 3 of the injection system can be arranged periodically downstream of each lighting device of the first group 2a, 2c, 2e, 2g (the reactor being devoid of diffusion unit 3 downstream of the lighting device of the second group 2b). Thus, after having circulated under the lighting device of the first group 2a, 2c, 2e, 2g, the mass to be treated is driven vertically towards the top of the tank | (i.e. direction opposite to the bottom) by the CO bubbles; (or the fluid containing the dissolved CO;) emitted (or emitted) by the diffusion units 3. The mass to be treated passes above the lighting device of the second group 2b, 2d, 2f and falls back towards the bottom of the tank | by gravity. This creates a circulation of the mass to be treated through tank 1, which improves the mixing and homogenization of the mass to be treated. The power supply module 5 makes it possible to supply each lighting device 2a-2g with electrical energy. In particular, each lighting device 2a-2g is electrically connected to the power supply module 5 via one (or more) electrically conductive connection cable(s). The electrical energy supplied by the power supply module 5 is then converted into light radiation by each lighting device 2a-2g to illuminate the culture medium 4. Controller 6 is used to control the bioreactor. In particular, controller 6 is used to control the electrical power supply module to vary: the excitation regime(s) of each lighting device (for example continuous mode for certain lighting devices, and flash mode at a frequency between | and 150 kHz for other lighting devices), and / or the emission spectrum(s) of each lighting device (for example in white light for certain lighting devices and in blue light for other lighting devices), etc. The reader will appreciate that within the same lighting device, different excitation regimes and / or emission spectra can be implemented, as will be described in more detail below. 2. Tank The tank | is intended to contain the culture medium 4. It comprises a bottom and at least one side wall. In the embodiment illustrated in [Fig. 1], the tank 1 is substantially parallelepipedal. It is composed of a base, four side walls and an at least partially removable cover. In other embodiments, the tank 1 may be cylindrical and include a lower base forming a bottom, an upper base forming a lid, and a side wall between the lower and upper bases. The material constituting the walls of the tank | can be stainless steel or equivalent. Of course, other materials can be chosen depending on the intended application (Plexiglass®, Polypropylene, Concrete, etc.). In all cases, the tank is preferably made of a material resistant to cleaning products (bleach, peroxide, etc.). 3. Lighting device, Each lighting fixture is flexible. The flexibility of each lighting fixture allows it to be shaped to the shape of the tank, for example by curving it (totally or partially) in the case of a cylindrical tank. In the context of the present invention, a component is said to be “flexible” when it is made of a material having mechanical properties allowing elastic deformation of said component. The flexible material can for example have: a modulus of elasticity greater than 0.05 Mpa, for example between 0.1 Mpa and 300 Gpa, el a breaking limit greater than 100 MPa, for example between 200 MPa and 5SGPa. Flexibility is further achieved through the geometry of the 2a-2g lighting device, particularly its thickness. As illustrated in [Fig.17], the flexible lighting device 2 comprises: a peripheral frame 51, and a central tablecloth 52. As will be described in more detail below, the frame 51 and the web 52 are flexible in at least one direction. 3.1. Peripheral framework The peripheral frame 51 makes it possible to support the central sheet 52. As illustrated in [Fig.17], the peripheral frame 51 comprises: two longitudinal edges 511 extending parallel to each other, and two transverse borders 512 extending parallel to the longitudinal borders- tudinales 511, each transverse edge 511 extending between a respective pair of free ends of the longitudinal edges 512. The edges 511, 512 of the peripheral frame 51 constitute reinforcements for the central sheet 52. In particular, they make it possible to protect the central sheet 52 during handling of the lighting device 2, and thus limit the risks of damage to the central sheet 52. Furthermore, the edges 511, 512 can make it possible to constrain the sheet 52 into a desired shape in the absence of external stress. For example, in the embodiment illustrated in [Fig. 17], the edges 511, 512 make it possible to conform the central sheet 52 in a plane when the lighting device is suspended (and no force is applied to the edges to bend the lighting device). For this purpose, the edges may be rigid or have non-zero flexibility. To constrain the shape of the sheet when its flexibility is non-zero, each edge 511, 512 has a stiffness coefficient greater than the stiffness coefficient of the central sheet 52. In the following, each edge 511, 512 with non-zero flexibility will be referred to as a “flexible edge”, even if the stiffness coefficient of said edge is greater than the stiffness coefficient of the central sheet 52. In some embodiments, the four edges 511, 512 are flexible. In this case, the peripheral frame 51 is flexible in two orthogonal directions D1, D2. In other embodiments, only two parallel edges 511 (for example the longitudinal edges) are flexible, the other two edges 512 (for example the transverse edges) being rigid. In this case, the peripheral frame 51 is flexible in a single direction. The fact that the peripheral frame 52 is flexible in only one direction makes it possible to improve its hold (maintaining its shape) in a direction orthogonal to its movement when the lighting device is handled, for example in the context of a maintenance operation. Each edge 511 may be rigid over only a portion of its length. For example, in the embodiment illustrated in [Fig. 19], each transverse edge 512 is composed of a rigid frame 512” and a strand 512”” of shorter length than the rigid frame 512, the rigid frame 512’ and the strand 512” being connected by a pivot connection 512”” so that the strand 512” can move in rotation relative to the rigid frame 512’. This makes it possible to create a fin (forming a deflector) at a transverse edge of the lighting device 2, for example to improve the mixing of the mass to be treated, etc. With reference to [Fig. 18], each flexible edge 511 may consist of a succession of rigid segments 513 connected together by pivot links 514 allowing each segment to pivot about an axis of the pivot link relative to at least one of the segments adjacent to it. This makes it possible to bend the end of the lighting device to conform it to the geometry of the photobioreactor, as will be described in more detail below with reference to FIGS. 8 to 10. Alternatively, each flexible edge may consist of a bead made of the same material as the plate. This makes it possible to simplify the design of each lighting device.In particular, the material constituting each flexible edge may be polymethyl methacrylate (PMMA), or a methacrylic resin (such as methyl methacrylate, ethyl ethacrylate, butyl methacrylate, propyl or isopropyl methacrylate), or a resin of the polystyrene, polycarbonate, polyacrylate type. Advantageously, a rigid support structure (not shown) comprising housings in each of which a respective flexible lighting device is housed can be provided in the tank. Such a support structure - each housing of which can be defined by one (or more) guide rail(s) in which the associated lighting device is able to slide - makes it possible to shape the flexible lighting device in order to bend its end in the photo-bioreactor. 3.2. Central tablecloth With reference to figures 2, 6 and 7, the sheet 52 of the lighting device 2 comprises: a flexible plate 21, and at least one light diode 22, 22a, 22b, 22c mounted on the 21 flexible plate(s). For example, in the embodiment illustrated in [Fig. 2], the lighting device 2 comprises a single light diode 22 (for example with an area of ​​6m?). Alternatively and as illustrated in Figures 6 and 7, each lighting device 2 comprises a plurality of light diodes 22, 22a, 22b, 22c (each having a surface area of ​​between 0.01 m? and 6m2). Each light diode 22, 22a, 22b, 22c can be glued to the flexible plate 21. Alternatively, each light diode 22, 22a, 22b, 22c may be laminated on the flexible plate 21 using a lamination interlayer. 3.2.1. Flexible Plague Each flexible plate 21 may be substantially rectangular. However, each plate 21 may have another shape. The material constituting each plate 21 may be polymethyl methacrylate (PMMA) or another transparent material known to those skilled in the art which allows the plate 211 to conduct — by transmission between its front and rear faces — the luminous flux emitted by the light diode(s), such as for example: another transparent methacrylic resin such as methacrylate methyl, ethyl ethacrylate, butyl methacrylate, methacrylate propyl or isopropyl, or a transparent resin such as polystyrene, polycarbonate, polyacrylate, or a glass / a fused silica. Alternatively, the material constituting each plate 21 may be a metal. In some embodiments, the plate may comprise a layer of material reflecting the light flux generated by the light diode(s). This layer of reflective material preferably extends between the plate 21 and the light diode(s). It makes it possible to reflect, orient and focus the light produced by the light diode(s). The layer of reflective material may consist of a film of reflective material such as a metallized aluminum film, or a paint. 3.2.2. Light diode 3.2.2.1. Structure Each light diode comprises one (or more) layer(s) of electroluminescent material(s) framed by two electrodes: one of the electrodes — called the anode — is arranged under the (or each) layer of electroluminescent material, and the other of the electrodes — called the cathode — is arranged on the (or each) layer of electroluminescent material opposite the anode. It will be understood in the following that when a layer A is mentioned as being “on” (respectively “under”) a layer B, the latter may be directly on (respectively under) the layer B, or may be located above (respectively below) the layer B and separated from said layer B by one or more intermediate layers. Furthermore, it will be understood that when a layer A is mentioned as being “on” (respectively “under”) a layer B, the latter may totally or partially cover the layer B (respectively be totally or partially covered by the layer B). Each light emitting diode emits light by electroluminescence using the recombination energy of holes injected from the anode and electrons injected from the cathode. Advantageously, the anode and the cathode can be made of a transparent material, so that the emitted photons pass through each electrode to provide light outside the light diode through its two faces. Referring to [Fig.3], an example of a structure for each light-emitting diode is illustrated. This structure includes: a first electrode 221 in contact with the flexible plate 21, a red emission unit 222 directly on the first electrode 221 and covered with a chemical range that emits in the red, a second electrode 223 directly on the red emission unit 222, a green emission unit 224 directly on the second electrode 223 and covered with a chemical range that emits in the green, a third electrode 225 directly on the green emission unit 224, a blue emission unit 226 directly on the third electrode 225 and covered with a chemical range that emits in the blue, a fourth electrode 227 directly on the blue emission unit 226. Stacking several emission units 222, 224, 226 makes it possible to vary the emission spectrum of the light radiation emitted by the light diode. More specifically, with such a structure the color of the light rays emitted by the light diode can be modified to make it particularly suitable for a specific maturation or growth method, as will be described in more detail below. Each light diode 22, 22a, 22b, 22c can be chosen from: a conventional Light-Emitting Diode (LED) the Anglo-Saxon acronym “Light-Emitting Diode”), a flexible organic light-emitting diode (OLED) according to the Anglo-Saxon acronym "Organic Lieht-Emitting Diode"), or a mini Light-Emitting Diode (or "mini LED" according to the acronym Anglo-Saxon “Mini Light-Emitting Diode”). The flexible nature of OLED light diodes allows the flexibility of lighting devices to be maintained even when the OLED light diodes (arranged on the flexible plate) are in contact with each other. When the light-emitting diodes are of a type other than an OLED, they are spaced apart from each other by a sufficient distance to allow the lighting device to be bent at an angle greater than or equal to 60°, preferably at an angle greater than or equal to 90°, more preferably at an angle greater than or equal to 120°, and even more preferably at an angle equal to 180°. In particular, the light diodes can be spaced from each other by a distance greater than or equal to 50um. The use of mini LED type light diodes allows for smaller light sources than conventional LED type light diodes (size less than 500 um), which makes it possible to increase the number of light sources per unit area (improving brightness and contrast), and to reduce the thickness of the lighting devices. 3.2.2.2. Advantage associated with the use of OLED As illustrated in Figures 4 and 5, the use of flexible OLED 22 type light diodes makes it possible to increase the homogeneity of the light 228 emitted by the lighting device according to the invention in comparison with the light 92 emitted by a conventional LED 91 type light diode. Especially : the incident angle 2 of the light 92 emitted by a light diode of type LED 91 is 120°, as shown in [Fig.4], while the incident angle 2 of the light 228 emitted by a light diode of type Flexible OLED is 178°, as shown in [Fig.5]. Thus, the use of OLED type light diodes ensures better homogeneity of light, and makes it possible to optimize the illuminated volume in the bioreactor. 3.2.3. Outer coating layer With reference to [Fig. 3], each lighting device 2 may optionally comprise an external coating layer 23 covering the light diode(s) and possibly the flexible plate(s) 21. This coating layer 23 protects the light diode(s) and the plate(s) 21 against possible mechanical damage (scratches due to friction, etc.). It also ensures the sealing of the lighting device. In certain embodiments, the coating layer 23 also makes it possible to improve the diffusion of the light emitted by the light diode(s). Indeed, when light is applied to a material, part of the light is reflected, part is absorbed and another part is transmitted through. These parameters can be determined by those skilled in the art using conventional photometry and optical methods. In the context of the present invention, the external coating layer 23 may be a transmission layer making it possible to promote the transmission of the light radiation emitted by the light diode(s) to the outside. In particular, the material constituting the coating layer 23 may be a resin including transparent particles, in particular a thermoplastic resin.In the latter case, the resin must be a synthetic or semi-synthetic resin and be chosen from crosslinked (meth)acrylic resins, the . crosslinked styrene resins, polyurethane resins, polyester resins, silicone resins, fluorinated resins, resins prepared from inorganic substances such as silica, calcium carbonate and barium sulfate. Among these resins, synthetic resins are preferred, in particular, crosslinked (meth)acrylic resins, crosslinked styrene resins, crosslinked (meth)acrylic-styrene copolymer resins and silicone resins are preferred. Crosslinked (meth)acrylic resins, crosslinked styrene resins and their copolymers are particularly preferred because it is possible to prevent their discoloration by ultraviolet rays, in particular by crosslinking processes. The latter therefore have a longer service life than other resins.Preferably, the coating layer 23 comprises a diffusing material having a transmittance preferably of at least 90%, still preferably of at least 95%, still still preferably between 95% and 98%. Preferably, when the coating layer has the function of improving the diffusion of the light emitted by the light diode(s), it is configured so that the light emitted by the light device has a degree of dispersion preferably greater than or equal to 170°, still preferably greater than or equal to 175°, still preferably between 175° and 180°. Advantageously, the coating layer 23 may also have a function of filtering the wavelengths of the light emitted by the lighting device. In particular, the material constituting the coating layer may be chosen to allow the transmission of light radiation whose wavelengths are between 380 nm and 800 nm, preferably between 400 nm and 720 nm, even more preferably between 420 and 690 nm. Preferably, the thickness of the coating layer 23 is between 0.1 mm and 5.0 mm, preferably between 0.5 mm and 3.0 mm, even more preferably between 0.5 mm and 2.0 mm. For the same thickness, a lighting device according to the invention comprising a coating layer 23 made of flexible diffusing material as defined above, has a better diffusion capacity than the light devices of the prior art and therefore a better W / Lumen / unit surface yield. Thus, for an equivalent microorganism biomass yield, a culture method using a bioreactor comprising a lighting device according to the invention will require less electrical energy. Furthermore, the lighting device described above is safer because it only requires low voltages. The coating layer 23 may also be made of a material (or be covered with a material) that limits its soiling (in particular by preventing the deposition of microalgae on its surface). The coating layer 23 may, for example, consist of a flexible glass of the Corning type (with a thickness between 0.1 mm and 0.7 mm). Such a waterproof glass coating also allows for better exchange of the heat emitted by the light diode(s) towards the culture medium (which can promote the growth of microorganisms contained in the culture medium 4). Such a waterproof glass coating also constitutes a better barrier to the gases injected into the bioreactor. 3.2.4. Examples of lighting devices With reference to Figures 6 and 7, other examples of lighting devices are illustrated. In these embodiments, the central sheet of the lighting device 2 comprises a flexible plate 21 and a plurality of light diodes 22, 22a, 22b, 22c mounted on the flexible plate 21. The use of a plurality of light diodes 22, 22a, 22b, 22c makes it possible to improve the modularity of the lighting device 2, and in particular to vary its size and dimensions in order to adapt them to the size and dimensions of the tank 1. In the embodiment illustrated in [Fig.6], the light diodes are of identical size and identical structure. Alternatively, the light emitting diodes may be of different size and / or type (LED, OLED, mini LED), and / or structure, as illustrated in [Fig.7]. For example, each lighting device 2 may comprise: one (or more) fluorescent light diode(s) 22a, one (or more) ultraviolet emitting light diode(s) 22b (for example “UVOLED”, acronym of the Anglo-Saxon expression “Ultra- Violet Organic Light-Emitting Diodes"), and / or one (or more) 22c phosphorescent light diode(s) (for example “PHOLED”, acronym for the Anglo-Saxon expression “Phosphorescent Organic Light-Emitting Diodes"). The presence of one (or more) ultraviolet emitting light diode(s) 22b allows the emission of UV-C radiation to sterilize the culture medium, and / or eliminate a contaminated culture in a compartment of the bioreactor and / or cause metabolic stress of the culture medium. 3.2.5. Advantages of the lighting device according to the invention The flexible nature of the lighting device makes it possible to delimit a circulation path for the culture medium in which: the pressure losses in the circulation flow of the culture medium are reduced, Unlit areas along this travel path are limited. These phenomena will now be presented with reference to figures 8 to 10 for to enable those skilled in the art to better understand the advantages associated with the use of flexible lighting devices. With reference to [Fig.8], when non-flexible lighting devices 7a-71 are integrated into a parallelepiped tank 1 (of the type comprising a bottom, four side walls and a cover), these are conventionally arranged transversely to the length of the tank, and offset vertically to come into contact successively with the cover and the bottom of the tank 1. Thus: a lighting device 7b, 7d, 7f, 7h in contact with the bottom of the tank 1 is adjacent to two lighting devices 7a, 7c, 7e, 7g, 7i in contact with the tank cover 1, a lighting device 7a, 7c, 7e, 7g, 7i in contact with the cover of the tank | is surrounded by two lighting devices 7b, 7d, 7f, 7h in contact with the bottom of the tank 1. This makes it possible to delimit a slotted circulation path for the culture medium 4. However, such a notched shape induces the presence of “shadow zones” 8 along the circulation path, namely zones at the level of which the culture medium 4 is not (or not sufficiently) illuminated. Furthermore, this notched shape induces pressure losses. In particular, and as illustrated in [Fig.9], when passing between two successive notches of the circulation path, the main flow (or flux) F, of the culture medium is subdivided, each subdivision forming a circular secondary flow F, which recombines with the main flow F,, then subdivides again and so on. This succession of subdivisions and recombinations of the secondary flows F, with the main flow F, induces pressure losses. The flexibility of the lighting devices 2a-2j according to the invention makes it possible to bend the end of the lighting device in order to form an access path composed of a succession of segments rounded at their ends, as illustrated in [Fig.10]. It is thus possible to illuminate the environment at the junction between two successive segments, which reduces the “shadow zones” along the circulation path. Furthermore, the rounded U-shape (obtained by bending the end of successive lighting devices) helps to limit pressure losses at the junction between two successive segments. 3.3. Power Supply Module and Controller As indicated previously, the power supply module 5 illustrated in FIGS. 1 and 2 makes it possible to supply the electrical energy necessary for the generation of light radiation by each light diode 22, 22a, 22b, 22c. Each lighting device 2 can be connected independently to the module power supply 5. This allows each lighting device 2 to be individually removed from the bioreactor during its operation. When the lighting device comprises a plurality of light diodes, each light diode can be individually connected to the power supply module 5. More specifically, the power supply module 5 is electrically connected to the electrodes of each light diode. This makes it possible to individually control the light radiation emitted by each light diode. For this purpose, the power supply module 5 is in communication (wired or wireless) with the controller 6 which is configured to emit control signals allowing in particular: to selectively activate / deactivate each light diode of the device lighting, for example depending on the bioreactor filling rate; It is thus possible to optimize the efficiency of the bioreactor as well as its rise in electrical power, to individually define the excitation regime (continuous or flash regime) of each light diode. Furthermore, the presence of a controller connected to the light diodes makes it possible to detect a possible fault in one (or more) light diode(s). This detection makes it possible to locate the faulty light diode(s) in order to replace it (or them) if necessary. When the light diode(s) of the flexible lighting device have(s) the structure illustrated in [Fig.3], the controller 6 and the power supply module 5 also make it possible to individually define the emission spectrum (white light, blue, red, green, etc.) of each light diode. Indeed, in this case, the power supply module 5 is electrically connected to the first, second, third and fourth electrodes 221, 223, 225, 227. To vary the emission spectrum of each light diode, the controller 6 controls the quantity of electrical energy supplied by the power supply module S to each of the first, second, third and fourth electrodes 221, 223, 225, 227, in order to modulate the intensity of the radiation emitted by each respective emission unit 222, 224, 226. By mixing, the red, green and blue light radiation emitted by the emission units then makes it possible to obtain a specific spectrum (white, yellow, violet light, etc.) adapted to a given application. For example, the growth of a microalga of the Oscillatoria sp type is faster in the case of light radiation whose wavelengths are included in a blue spectrum. Similarly, chlorophyll and carotenoid pigments are observed at high concentrations in blue light radiation. To induce the emission of blue light by a light diode, the controller 6 commands the power supply module 5 to supply only electrical energy to the third and fourth electrodes 225, 227 between which the blue emission unit 226 extends. The growth of a microalga of the Ankistrodesmus type is faster in the case of green light radiation. To induce the emission of green light by a light diode, the controller 6 commands the power supply module 5 to supply electrical energy only to the second and third electrodes 223, 225 between which the green emission unit 224 extends. Lipid accumulation is high in yellow light radiation compared to other light radiation in Ankistrodesmus. To induce the emission of yellow light by a light diode, the controller 6 commands the power supply module 5 to supply electrical energy only to the first, second and third electrodes 221, 223, 225 between which the red and green emission units 222, 224 extend. The mixture of red and green light radiation from the red and green emission units 222, 224 then produces yellow light. It is also possible to favor the emission of light radiation in the ultraviolet spectrum in order to stimulate the production of vitamins, particularly vitamin D3. Thus, the combination of a light diode including a stack of structures 222, 224, 226, a power supply module 5 (connected to the light diode) and a controller 6 (controlling the power supply module 5) makes it possible to modulate the emission spectrum of the light diode. Advantageously, this modulation of the emission spectrum of the light diode can vary over time, to adapt to conditions of biomass growth and / or stress and / or production of metabolites. For example, a user of the bioreactor according to the invention can: at an initial stage, modulate the emission spectrum of the light diodes of so as to induce the emission of blue light rays in order to to increase the growth of microalgae, then at a later stage, modify the emission spectrum of the light diodes so as to induce the emission of yellow light rays in order to to increase the accumulation of lipids by microalgae. 3.4. Diffusion unit The diffusion units 3 illustrated in [Fig.1] are used to supply the bioreactor with nutrients, particularly CO. In particular, the 3 diffusion units allow: to provide the carbon dioxide necessary for the development of the environment culture 4, and to suspend the particles supporting the microorganisms contained in the culture medium. The supply of carbon dioxide can be continuous or discontinuous in response to certain criteria such as time or pH. Carbon dioxide can be introduced: in the form of gas bubbles, or in the form of an aqueous solution pumped or pushed into the bioreactor. The introduction of carbon dioxide in the form of gas bubbles allows for better distribution of CO in tank 1. The diffusion units 3 may be of different types known to those skilled in the art, for example diffusers made of microporous composite materials, with membrane (EPDM, silicone, etc., preferably EPDM), ceramic or slotted, etc.: in the case of gaseous CO, the diffusion units 3 may consist of micro-bubbling heads for the diffusion of bubbles of different diameters, in the case of CO; dissolved in an aqueous medium, the diffusion units 3 may consist of fluid ejection nozzles for diffusion of the fluid containing dissolved CO. The diffusion units 3 may also comprise a membrane contactor. A membrane contactor is a device comprising at least two fluid circulation circuits separated by a transfer membrane. The fluids circulating in said membrane contactor are also referred to as circulation fluid(s). The membrane contactor thus comprises a first circulation circuit of a first circulation fluid for supplying carbon dioxide (CO), called CO2 supply fluid in contact with a first face of the transfer membrane, and a second circulation circuit of a second circulation fluid for receiving CO, called CO receiving fluid, in contact with the second face of the transfer membrane. Each fluid circulation circuit is independent of one another, and may be closed or open.Such a membrane contactor associated with a reactor is described in particular in international application PCT / FEP2022 / 087329. Each diffusion unit 3 is preferably arranged in the immediate vicinity of the bottom of the tank 1. Furthermore, each diffusion unit 3 is arranged between two adjacent lighting devices 2a, 2b, the different diffusion units 3 being arranged so that each diffusion unit 3 is surrounded by lighting devices distinct from the lighting devices 2a, 2b surrounding the other diffusion units 3. In other words, each diffusion unit 3 is separated from the nearest diffusion unit 3 (or nearest units) by two lighting devices 2a, 2b. The diffusion units 3 are connected to a CO supply unit; — such as a booster (in the case of gaseous CO) or a pump (turbine type in the case of CO) fluid) — preferably equipped with a non-return valve to prevent sludge or effluent from rising to the COz supply unit. Such a CO supply unit is known to those skilled in the art and will not be described in further detail below. 4. Maintenance system The flexible nature of the lighting device(s) contained in the tank also makes it easier to maintain the bioreactor according to the invention. With reference to [Fig. 11], an example of a maintenance system is illustrated. This system comprises: a crane mounted on a fixed or mobile chassis, and a gripping tool 100 (hook, grapple, or the like) mounted on the free end of the crane, a plurality of guide rollers 101, 102 for movement by rolling of each lighting device 2. Each lighting device 2 comprises a gripping element (such as a cavity) intended to cooperate with the gripping tool 100 of the maintenance system. The operating principle of the maintenance system is as follows. In a first step, the gripping tool 100 is fixed to the gripping element of the lighting device 2. Once fixed, the gripping tool 100 is moved in a vertical direction towards the outside of the tank 1. In a second step, the gripping tool 100 is moved horizontally between a lower roller 101 and an upper roller 103 of the plurality of guide rollers 101, 102 arranged above the tank 1. The lighting device 2 bends 90°. An upper portion of the lighting device 2 (located between the lower roller 101 and an upper edge of the lighting device 2) then moves in a horizontal direction, while a lower portion (located between the lower roller 101 and a lower edge of the lighting device 2) moves vertically upwards. In a third step, when the entire lighting device 2 extends horizontally between the plurality of guide rollers 101, 102, the gripping tool 100 is immobilized. Thus, the flexible nature of the lighting device(s) 2 makes it possible to reduce the height required to extract said lighting device(s) 2 from the tank 1 for carrying out a maintenance operation. 5. C Cti lu photo-bioré( We will now describe different aspects relating to the sizing of the bio-reactor allowing optimal use of the luminous flux from the lighting devices. 5.1. Photon capture model To understand whether the photon flux from the lighting devices is optimally used by the mass to be treated, we propose to use a model on the capture of photons by microalgae as a function of an emission surface and a geometry of the reactor. The following representation shows the adjustable parameters for deducing productivities in a photobioreactor. Here it will be preferable to minimize the unilluminated fraction of the reactor and increase the surface area receiving the photon flux. The overall model of the surface efficiency of a photobioreactor is as follows: E fA3 VY toner Î Ê {#+2L Bi sf) a,F28. ape raies n (af ie F+œ vai ! & À (ACT Ê gmant NE Le à f {#22%. E. ja 1R+ti | =- 43 m8 EE 2 K (easy Or: fa is the unilluminated volume fraction by design of the reactor (fd = 0 if the entire surface of the reactor is illuminated), Pm is the maximum energy conversion efficiency light into physicochemical energy, @ is the molar quantum efficiency of photosynthesis, a is the linear diffusion modulus, Align ESt the illuminated specific surface area of ​​the reactor on volume, K corresponds to a half-saturation constant of photosynthesis (depends of the microorganism), A corresponds to the average degree of collimation of the incident radiation, 4. is the average photon flux density on the bioreactor surface. The maximum performance of a photobioreactor can be characterized by some simplifications of the constants in an ideal case. Therefore production will depend on the following elements: The dark fraction “S,” which corresponds to the unlit volume ratio (fd=0): Sx = (1-fd)In(1+q / K) in kg / m? / J Where q is the average photon flux density on the bioreactor surface (expressed in umolphotons / s / m”, and where K is the half-saturation constant photosynthesis (30,000 umol / kgx / s), Surface production “P,” due to the capture of the photon flux captured surface: Px = Sx *# A, light EN kg / m° / J with corrective factor of 20% Volume production as a function of the surface photon flux captured reported to the total volume: azumière = Suumière / V,, WHERE V, is the volume of the bio- reactor By applying the previous calculation rules for: an acrylic plate 0.1m wide and 0.1m long an incident light of 350umol / m2 / s, a total reactor volume of 0.008 m°, no shadow area (fd=0), then the maximum theoretical volumetric productivity is estimated at 139 mg / L / J, as illustrated by the table below. [Tables 1] 1 [mn Reactor geometry case Length 0.40 | |Width 0.20 | Illuminated surface 0.08 fe Qn 350.00 prmol / m2 / s K 30000.00 |jumol / kgx / s (8 0.008 fem 08 0.00 fe 0.01 Kg / m° / } 0.08 Kg / m° / 1 0.13918963 |Kg / m° / 1 139 [mg / L13 Theoretical maximum production This is confirmed during an experiment using the bioreactor illustrated in [Fig.12] which comprises a parallelepiped tank 1, eight lighting devices with sides of 0.1 m (0.01 m?) and each including a WOLED (White OLED) placed in contact on five sides of the tank. An average production of 172 mg / L / J over 55 hours (minimum: 100 mg / L / I, maximum: 230 mg / L / I) is obtained, as illustrated in [Fig.13] which represents a Summary graph of chlorella productivity in the bioreactor shown in [Fig.12]. Adding air with 2% CO ensures mixing and provides carbon. 5.2. Determining the optimal quantity of lighting devices The goal is to determine the optimal surface area for the diffusion of light flux for the reactor. Of course, the number and arrangement of lighting devices can vary depending on the quantity of biomass that is to be produced. To produce 711 mg / L / J of biomass per m°* of culture in a volume of 1 m°, by applying the formulas of the global modeling described above, 24 m? of lighting devices emitting 750 umol / m? / s are necessary. This number is directly related to the desired output, volume, geometry and light intensity. We obtain the following table: [Tables 2] Case geometry reactor Surface Column Ext 24.00 | Q 750.00 [umo | K 30000.00 | |umol / kgx / s —7 vs . [Ve [Lo mr right fa s, ° P, continuous - P, continuous rt correction |mg / L / J 1.00 qe Bu 0.00 4 0.02 Kg / m / s 059 |Ke / m] t 1071114724 [Kg / mê / 1 3 1 \mg / L3 Theoretical maximum production 53.3. Determination of a maximum quantity of biomass not to be exceeded The objective is to determine the maximum concentration of biomass not to be exceeded in order to avoid having a dark zone in the environment (i.e. maintain an f=0), In the following, we consider a bioreactor having a tank with the following dimensions: 1 meter x 1 meter x 1 meter (L*1*H in meters). The volume of the tank is therefore 1 m? It is also assumed that each lighting device has dimensions of 1 meter per side and emits on both sides. The emitting surface of each lighting device is therefore 2 m?. [Tables 3] Reactor characteristic Length-m |1 Width-m 1 = - |lm Volume -m3 |1 The spacing between the different lighting devices is then given by the following formula: D=(L-— Evo) / (2 X Nbpiaques) = (1 - 0.06) / (72 x 12), and divre= D - thickness of a lighting device With: L: Width of a lighting device; Eos: Total thickness; Nb: number of lighting devices; D: Distance between two lighting devices, d: free space in two lighting devices. [Tables 4] Characteristics of the plates Number of lighting devices |12 simple Thickness “Ze” of a lighting device [0.005 - m Total thickness - m 0.06 Spacing “D” between the rear faces of two successive lighting devices 0.156 - m Free space “d” between lighting devices |0.145 - m In case the lighting devices have dimensions of 1*1 meter, twelve lighting devices are required in the bioreactor. Arranging them in a sandwich, the total thickness of the lighting devices measures 0.06 meters. The lighting devices are placed every 0.156 m in the middle and with a free space of 0.145 m. It is necessary to determine the maximum concentration that must not be exceeded in order to avoid having a dark zone in the culture medium and to maintain an f;=0, i.e. a sufficient photon flux up to the adjacent zone. Ideally, a concentration of 0.3 g / L / J should not be exceeded, as illustrated in [Fig.14] representing a maximum concentration of microalgae depending on the distance between adjacent lighting devices. The luminous intensity as a function of the distance Z can be expressed from the following formula: I(z)=I,ee-kieBez Or: Is corresponds to the incident light, is a coefficient (absorption, K, is efficient of absorption B corresponds to the biomass concentration, Z corresponds to the length of the tank. If we consider that from 50 umol / m? / s, the quantity of light is insufficient to have sufficient yields, it is possible to determine the maximum concentration not to be exceeded. Here with 0.03 meters (due to the lighting devices placed in sandwich) the maximum concentration not to be exceeded is 1.5 g / L. 3.4. Homogeneity of light, The homogeneity of light from a lighting device including an OLED is greater than or equal to 99%, ensuring better performance than a lighting device including an LED. A PMMA plate with prisms has a diffusion capacity of 70% to 90% depending on the thickness and the quantity of LEDs placed on the sides. The amount of energy to be sent to the surface is therefore less in the case of a lighting device including an OLED. For an equivalent biomass yield per unit volume, it will be necessary to inject between 10 and 30% more electrical energy in the case of a lighting device including an LED. 5.5. Useful volume of the bioreactor The useful volume of the bioreactor is larger (economic advantage) with a lighting device including a flexible lighting device. This use of flexible lighting devices makes it possible to optimize the useful volume of the reactor by two to sixteen times, given that: the thickness of a PMMA or polycarbonate plate can measure 0.01 m and 0.08 m, and that the thickness of a flexible lighting device of 0.005 m. 5.6. Incident angle The homogeneity of light by the incident angle of the OLED layers of 178° in opposition to LEDs of 120°, This ensures better homogeneity of light in the bioreactor. We preferred to use an OLED with the widest possible angle: greater than 120°. Indeed, it is difficult to obtain an angle greater than 120° with LEDs. This reduces the volume of culture optimized for microalgae cultivation. This angle allows an improvement in the coverage of the illuminated volume of 20% compared to a classic LED plate with a power of 700 uE and 0.1 g / L of algal concentration. The illuminated volume is therefore defined by the following formula: Illuminated volume = ((Trar?) / 360°) *L*ncors)+(L*1*h)*n faces in m*. The table below provides a comparison of the volumes illuminated with a classic LED type diode and an OLED type diode. [Tables 5] Case LEDs |r 0.385|0.19 |0.13 [0.1 |0.08 [0.06 |o.05 [0.05 |0.04 [0.04 |0.03 0.03 |0.03 5 5 |s 5 5 Angle [30 |30 |30 J0 |30 [0 |30 J30 |30 J30 |s0 ]30 |30 alpha Volume [1.391 [0.54 [0.33 [0.24 |0.18 [0.14 [0.12 [0.11 [009 [0.08 [0.07 [0.06 [0.06 total - 9 |1 there 7 \8 |3 lo |8 |7 |5 |4 |a m3 Case OLEDs |r 0.385 |0.19 [0.13 jo [0.08 0.06 |0.05 |o.05 0.04 [0.04 0.03 [0.03 [0.03 | 5 5 |s 5 5 [Angle |s8 [ss |ss |ss [ss |ss |ss |ss [ss |ss [ss |ss |ss Angle 88 188 [88 |88 [88 |88 |88 |88 [88 [88 |88 |88 |88 alpha Volume |1.68 [0.62 |0.36 |0.26 |0.20 |0.16 [0.13 [0.12 |0.10 [0.09 |0.08 |0.07 10.07 total - m3 Gain % |20.83|13.5 19.99 |8.08 |6.70 15.59 |4.82 |4.42 |4.02 [3.61 [3.19 |2.76 [2.76 OLEDs 3 VS LEDs 2.2. Possibility of varying the distance between the lighting devices depending on the light flow in continuous or flash mode We will now describe different aspects relating to the sizing of the bio-reactor by considering a discontinuous supply of light, that is to say by considering that each lighting device generates a discontinuous light radiation composed of a close alternation of dark phases and illuminated phases (flashes), for example at a frequency between 10 and 50 kHz. Consider a system with an average continuous intensity of 1000 umol.ms-! at the lighting devices. When this continuous average intensity is then set to flash while maintaining an average irradiance of 1000 umol.m?.s"! it is then possible to obtain flash waves of 10000 umol.m?.s-!, For information, [Fig.15] illustrates the difference between discontinuous lighting 31 and continuous lighting 32: the cycle time is given by the following formula: tcycle = tlight + tdark (s) / or frequency (Hz) the light fraction is given by the following formula: : (tlight / (tlight + tdark )) the integrated irradiance is given by the following formula: I, = L- 9 With: @ = 10% ; 1, = 1000 umol.m?.s"}, 1, = 1; - umol.m*.s"}, I= 10000 umol.m?.s"!. This wave of photons makes it possible to increase the entry distance of the photons into the medium and therefore to increase the distance between the lighting devices with an identical biomass concentration. Indeed, as illustrated in [Fig.16], the transition from a continuous light supply to a discontinuous light supply makes it possible to increase the distance between two adjacent lighting devices while maintaining the other parameters identical. With reference to [Fig.16], the distance between two adjacent lighting devices can be extended to 0.055 meters in flash with a concentration of 1.5 g / L. 6. Conclusions The solution described above has many advantages: the hydraulics of the photo-bioreactor via flexible lighting devices is improved, in particular thanks to an optimization of the traffic flow of the culture medium in certain areas of the photo-bioreactor, maintenance of the photo-bioreactor is facilitated thanks to the flexibility of the dis- lighting positives, the useful volume of the photo-bioreactor is larger (advantage economical) compared to existing lighting solutions, The flexibility of OLED lighting devices also makes it possible to provide more light in dead zones of the photo-bioreactor, the use of a plate and an external coating layer of glass thin allows to reduce the sticking effect (“fouling”) of microalgae on the lighting devices, better insulation of electronic components between them, limiting electrical risks, better optical transmittance, better chemical stability, a better barrier to gases injected into the photo-bioreactor, better exchange of calories generated by light diodes lighting devices, compared to an outer coating layer of PMMA or polycarbonate. The reader will have understood that numerous modifications can be made to the invention described above without materially departing from the new teachings and advantages described here.

Claims

Claims

1. Reactor including: a tank (1) intended to contain a mass to be treated, the tank (1) comprising a lower wall forming a base, a su- upper wall opposite the lower wall, and at least one wall lateral between the lower and upper walls, a set of flexible lighting devices contained in the tank and intended to promote the treatment of the mass, at least one electrical power supply module connected to each lighting device, characterized in that each flexible lighting device comprises: a peripheral framework composed of: of two flexible longitudinal edges, and of two transverse borders, each transverse edge extending between a pair of ends respective free longitudinal edges, and a flexible central sheet (52) on the edges of which is mounted the peripheral frame, the central flexible sheet (52) including: at least one flexible plate (21), a transparent flexible coating layer (23) to light radiation, said layer of re- garment extending over the flexible plate, a group of light diodes (22, 22a, 22b, 22c) extending between the flexible plate and the re- layer flexible garment, said light diodes being oriented so as to generate light radiation in a direction opposite to the flexible plate.

2. A reactor according to claim 1, wherein each light diode is a flexible organic light-emitting diode (OLED), each light diode being in contact with an adjacent light diode.

3. The reactor of claim 1, wherein each light diode is chosen from a conventional light-emitting diode (LED), or a mini light-emitting diode (mini LED), the diodes lights being spaced from each other by a greater distance or equal to 50um.

4. A reactor according to any one of claims 1 to 3, wherein each cross border is flexible so that the peri- spherical is flexible in two orthogonal directions (D1, D2).

5. Reactor according to any one of claims 1 to 3, in which each transverse edge is rigid so that the peripheral frame is flexible in a single direction (D1) parallel to the long edges gitudinal.

6. A reactor according to any one of claims | to 3, wherein each transverse edge includes a rigid reinforcement (512) and a strand rigid (512”) of less length than the rigid frame (512’), the rigid frame (512') and the strand (512”) being connected by a link pivot so that the strand (512'') is able to pivot relative to the frame (512').

7. A reactor according to any one of claims | to 6, wherein each flexible border comprises a succession of rigid segments (513) connected together by pivot links (514) so ​​that each segment is pivotable relative to an adjacent segment.

8. A reactor according to any one of claims 1 to 6, wherein Each flexible border consists of a bead made of a material identical to a material constituting the flexible plate.

9. A reactor according to any one of claims 1 to 8, wherein said and at least one lighting device is of parallel shape- piped, the reactor including a rigid support structure comprising housing, each housing being intended to receive a device respective flexible lighting and being configured to bend the lighting device in the tank.

10. Reactor according to one of claims 1 to 9, in which each diode light comprises a stack of structures (222, 224, 226), each structure being adapted to emit light radiation in a respective wavelength range.

11. | A reactor according to claim 10, which further comprises at least a controller (6) configured to control said and at least one module (5) electrical power supply.

12. A reactor according to claim 11, wherein said and at least one controller (6) is configured to control an energy variation supplied by said and at least one power supply module (5) in order to modify over time the emission spectrum of said and at least one lighting device (2, 2a-2j).

13. A reactor according to any one of claims 11 or 12, in which said and at least one controller is configured to: control the continuous activation of said and at least one module electrical power supply so that said and at least one lighting device (2a, 2b) generates a continuous light radiation, control the discontinuous activation of said and at least one module electrical power supply so that said and at least one lighting device (2a, 2b) generates a discontinuous light radiation in the form of flashes composed of an alternation of dark phases and phases illuminated, for example at a frequency between 10 and 50 kHz.

14. A reactor according to any one of claims 1 to 13, wherein the material constituting said coating layer is flexible glass.

15. A reactor according to any one of claims 1 to 13, wherein the material constituting the coating layer is a syn- resin synthetic or semi-synthetic chosen from (meth)acrylic resins crosslinked, crosslinked styrene resins, polyurethane resins, polyester resins, silicone resins, fluorinated resins, resins prepared from inorganic substances such as silica, calcium carbonate and barium sulfate.

16. A reactor according to any one of claims 1 to 15, wherein at least two light diodes of the plurality of light diodes are of different sizes.

17. A reactor according to any one of claims 1 to 16, wherein the plurality of light-emitting diodes comprises: at least one ultraviolet emitting light diode (22b), and / Or at least one phosphorescent light diode (22c).