This invention relates to a system for producing photosynthetic microorganisms suspended in water.
A photobioreactor is a system that produces photosynthetic microorganisms suspended in water, such as multicellular plants, small plants such as gametophytes, photosynthetic bacteria, cyanobacteria, eukaryotic microalgae, isolated macroalgal cells and moss protonemata.
This production involves culture, most often clonal, in an aqueous medium under illumination. Amplification to industrial volumes up to hundreds of cubic meters is carried out in successive steps where the volume of one step is used to inoculate the next volume. To harvest the microbial population and ensure biomass production, the volume of each step can be partially renewed daily (continuous culture) or completely changed (batch culture). These steps correspond to photobioreactors of increasing volume.
Photosynthetic microorganisms produce biomass only when they receive a quantity of light energy, called irradiance, greater than a minimum irradiance Gc. However, since an algae culture is an absorbent medium that attenuates light, the light decreases with the thickness of the culture according to an exponential law.
To increase the biomass productivity of culture systems, it is advisable to increase the supply of light energy and/or decrease the culture volume for a given illumination surface (i.e. increase the specific surface illuminated). Thus, productivity in terms of culture volume (i.e. volume productivity) is usually distinguished from productivity in terms of illuminated surface (i.e. surface productivity).
In order to be able to change the volume of the photobioreactor during the steps described above, and to standardize the irradiance received by the microorganisms, the Toshihiko Kondo document “Efficient hydrogen production using a multi-layered photobioreactor and a photosynthetic bacterium mutant with reduced pigment” proposed multi-layered photobioreactors which dilute strong incident light and diffuse it uniformly in the reactor. Layers can be gradually added to the photobioreactor to allow the volume of the photobioreactor to be changed.
However, systems designed on this principle face a major limitation, namely the tendency to form deposits, called biofilms, on the illuminating walls, which over time decreases the light intensity in the reactor volume and therefore production efficiency. This phenomenon is all the greater when the culture thickness (i.e. the distance between light plates) is small. The confinement of the medium indeed increases, as well as the biomass concentration, due to the increase in the specific illuminating surface area, which leads to higher volume productivity.
To avoid biofilm formation, it has been proposed to insert mechanical cleaning devices into the cavity receiving the culture medium, but such cleaning devices are not compatible with thin cavities. In practice, the culture thickness must therefore be at least a few centimeters, typically greater than 1 cm, which does not allow high volume productivity to be obtained.
In the end, these systems, designed on the principle of submerged illuminated plates, have low volume productivity and a strong tendency to foul.
In terms of technologies allowing high volume productivity, one example is the document FR2950899, which describes a photobioreactor comprising an illumination panel inclined by an average slope in a direction of inclination over which a solution flows. This makes it possible to obtain a minimum thickness of a few millimeters and therefore high volume productivity. Thus, the illumination panel is not in contact with the culture, which prevents biofilms. Such a solution is, however, incompatible with a modular photobioreactor with internal illumination.
One aim of the invention is to propose a solution that will allow the volume of the photobioreactor to be changed while maintaining an intensified and efficient volume production of biomass.
This aim is achieved in the context of the present invention by means of a photobioreactor module adapted to be assembled with an identical adjacent module, comprising:
The culture thickness, defined by the spaces between the plates, is very low, which allows high volume productivities. Biofilm formation is prevented by effective bubbling between the two plates. Indeed, due to the thinness of the cavity, the gas bubbles rising up the sides of the panels mechanically clean said panels as they pass. The injection of gas, necessary for the culture of microorganisms (supply of nutrients), also helps to promote the movement of the culture medium, which makes it possible to standardize the irradiation of microorganisms present in the cavity.
The module is also designed to guarantee constant volume and surface productivities. The modular nature of the photobioreactor indeed makes it possible to increase production capacity in a simple and linear way, by adding modules that maintain optimal exposure of the microorganisms to light. The modules can be added to the photobioreactor to be able to change the volume of the photobioreactor from a few liters to several m3. Due to the thinness of the cavity and the illumination on both sides (the culture thickness is therefore equal to half the cavity thickness), such a module makes it possible to manufacture a photobioreactor with high volume productivity, regardless of the number of modules assembled.
The invention is advantageously completed by the following features, taken individually or in any one of their technically possible combinations.
The invention also relates to a photobioreactor, comprising an assembly of several modules as described above, each module defining, with an adjacent module, a cavity suitable for containing the culture medium.
The photobioreactor comprises an assembly of several modules and a control unit configured to control the injection of gas bubbles into the culture medium contained in the cavity, alternately over a first section of the width of the cavity, then over a second section of the width of the cavity.
The photobioreactor comprises of a frame with guide rails on which the modules are supported so as to keep the modules in position relative to each other.
The photobioreactor comprises a device for pressing the assembly to keep the modules in tight contact with each other.
The pressing device comprises a first end plate and a second end plate, between which the modules are arranged, and an actuator suitable for exerting pressure on the second plate to bring the second plate closer to the first plate.
The photobioreactor comprises a device for controlling the temperature of the culture medium.
The modules include an instrumented module, the instrumented module comprising one or more sensors in contact with the culture medium.
Other objectives, features and advantages will emerge from the following detailed description with reference to the drawings given by way of non-limiting illustration, wherein:
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The distance between two panels 1 defines the thickness of the cavity 14, while the width of the panel 1 defines the width of the cavity 14, and the height of the panel 1 the height of the cavity 14.
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The gas injection device 2 comprises gas injection channels 21 distributed over the width of the cavity 14 in the lower part of the panels 1. The gas injection channels 21 are cut into one of the transparent plates 17a, 17b of each module 10 or arranged between the two transparent plates 17a, 17b. The gas injection device 2 typically comprises a tank 22 containing the gas to be injected under pressure, the tank having an outlet in communication with the gas injection channels 21.
The gas injection device 2 injects the gas loaded with carbon dioxide required by the microorganisms via the gas injection channels 21 into the cavity 14. The injected gas forms bubbles that rise up the sides 11, 12 of the panels 1. As they rise, the bubbles are loaded with photosynthetic oxygen generated by the microorganisms. The gas loaded with photosynthetic oxygen generated by the microorganisms is evacuated through an opening 8 provided in the upper part of the panels.
The gas injection device 2 renews the carbon dioxide consumed by the microorganisms and eliminates the photosynthetic oxygen generated by the microorganisms. Indeed, a concentration too high in oxygen and too low in carbon dioxide inhibits the photosynthetic reaction.
By rising up the sides of the panels 11 and 12, the bubbles mechanically clean the inner wall of the cavity 14, preventing the development of a biofilm that would reduce the light intensity in the reactor volume.
The injection of gas also promotes the movement of the culture medium, in order to improve the uniformity of the irradiation of the microorganisms.
The gas injection device 2 is advantageously adapted to inject gas in a pulsed and sequential manner in order to increase the shear effect on the forming biofilm.
A control unit 23 configured to control the injection of gas bubbles into the culture medium contained in the cavity 14, controls the injection of the bubbles alternately the gas injection channels 21 distributed over a first section S1 of the width of the cavity 14, then the gas injection channels 21 distributed over a second section S2 of the width of the cavity 14.
The control unit 23 can also be configured to control alternately the gas injection channels 21 distributed over the first section S1 of a first group of cavities 14, then the gas injection channels 21 distributed over the second section S2 of a second group of cavities 14.
The control unit 23 can also be configured to control alternately the gas injection channels 21 distributed over the first section S1 of a first group of cavities 14 and the gas injection channels 21 distributed over the second section S2 of a second group of cavities 14, then the gas injection channels 21 distributed over the second section S2 of the first group of cavities 14 and the gas injection channels 21 distributed over the first section S1 of the second group of cavities 14.
The first section S1 of the width of the cavity 14 is typically complementary to the second section S2 of the width of the cavity 14.
To that end, the control unit 23 controls the injection of bubbles according to the following sequence:
injection of bubbles through the gas injection channels 21 distributed over a first section S1 of the width of the cavity 14,
injection of bubbles through the gas injection channels 21 distributed over a second section S2 of the width of the cavity 14.
The injection sequence may further include a step of injecting bubbles simultaneously through the gas injection channels 21 distributed over a first section S1 of the width of the cavity 14, and through those distributed over the second section S2 of the width of the cavity 14.
The inventors have shown that injecting gas bubbles alternately on one section S1 of the width of the cavity 14 and then on the other section S2 of the width of the cavity 14 substantially improved the cleaning efficiency.
Indeed, the injection of bubbles entrains the liquid upward. This upward movement is compensated by a downward movement of liquid. However, this downward movement of liquid disrupts the shear effect of the bubbles.
When gas bubbles are injected over a section of the width of the cavity 14 only, the bubbles entrain the liquid upward over said section of the width of the cavity 14 and the liquid descends to the complementary section of the width of the cavity 14 forming a cyclic movement. The downward movement of liquid thus does not disturb the shear effect of the bubbles. The cleaning of the complementary section of the width of the cavity 14 is then carried out by injecting gas bubbles into the complementary section of the width of the cavity 14. Thus, the cavity 14 is finally cleaned over its entire width.
Furthermore, the gas injection device 2 is advantageously adapted to form bubbles having a size of the same order of magnitude as the thickness e to increase the shear effect on the forming biofilm.
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The light source 32 is typically a light-emitting diode. It typically emits white light in a spectral range adapted to improve photosynthetic conversion.
The light source 32 can be common to all the modules 10. In particular, the light source 32 can be sunlight. In this case, the light source 32 comprises a system for capturing the solar flux and transmitting the flux to the optical diffusion devices 31.
The optical diffusion device 31 extends between the two transparent plates 17a, 17b. The internal illumination allows total absorption of emitted flux, control of light attenuation conditions and therefore of biological conversion, and low energy consumption.
The optical diffusion device 31 is typically a side-diffusion device such as a laterally diffused woven optical fiber web or a diffusing glass plate, or a thin polymer sheet in which strips of light-emitting diodes (LEDs) are integrated.
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To that end, the temperature control device 6 comprises, for example, a flow circuit comprising a circulation tube 61 for a cooling liquid and a cooling module 62, the circulation tube 61 extending through the cooling module 62. The circulation tube 61 extends for example through the modules 10 or through the plates 17a, 7b. The coolant can be water, for example.
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Number | Date | Country | Kind |
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1661496 | Nov 2016 | FR | national |
Filing Document | Filing Date | Country | Kind |
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PCT/EP2017/080380 | 11/24/2017 | WO | 00 |