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    • 专利摘要:
    The present invention relates to a computerized method for regulating an air purification system comprising a bioreactor. In particular, the system may comprise a photo-bioreactor for the treatment of urban air, in particular for the purification of CO2. The system can be connected to the sewerage network and / or to a water distribution network (drinking and / or city). The connection and the emptying system can in particular maintain a fluid isolation between the two types of networks. The system may optionally be instrumented with measurement sensors and / or actuators for regulating the internal activity of the bioreactor. Different modes of regulation of a grid of bioreactors are described. Status data from connected networks (eg water, wastewater, cooling, heat networks) contribute to the regulation of a network of geolocated bioreactors. Aspects of software are described. The supervision of the grid of bioreactors can in particular be carried out remotely via onboard communication devices.
    公开号:FR3043331A1
    申请号:FR1560666
    申请日:2015-11-06
    公开日:2017-05-12
    发明作者:Herve Labaquere；Arnaud Heinrich；Chezelles Marie-Cecile De
    申请人:Suez Environnement SA；
    IPC主号:
    专利说明:

    METHOD FOR REGULATING AIR CLEANING SYSTEMS
    FIELD OF THE INVENTION The invention relates to methods for regulating air purification systems, and air purification systems, in particular urban air, said systems being in particular controlled remotely. and / or being regulated according to different types of servocontrol.
    State of the art
    A carbon sink or carbon dioxide (CO2) sink is a reservoir, natural or artificial, that absorbs carbon from the atmosphere and helps to reduce the amount of atmospheric carbon dioxide. The size of such tanks is variable. The main natural carbon sinks are oceans, soils (humus, peat bogs) and some vitalist environments (forest in formation). Carbon sinks considered by industrialists include bioreactors, generally based on the process of photosynthesis.
    The patent application FR2945215 discloses, for example, a method for treating ambient air, characterized in that it consists in placing in the environment to be treated a reservoir containing a medium in which autotrophic microorganisms such as algae develop. by photobioreaction by means of a light source (18) placed in or near the reservoir, the reservoir allowing exchanges between the medium and the air of the environment to be treated, the autotrophic microorganisms generating elements calcified from the dioxide of carbon present in the environment to be treated. This approach has disadvantages, which oppose the massive use of such facilities. For example, a significant technical problem is the need for compost collection, which is difficult in urban areas (eg logistics, odor nuisance) and also from an economic point of view.
    There is a need for advanced air handling processes and systems, particularly in urban areas. Summary of the invention
    The present invention relates to a computerized method for regulating an air purification system comprising a bioreactor. In particular, the system may comprise a photo-bioreactor for the treatment of urban air, in particular for the purification of C02. The system can be connected to the sewerage network and / or to a water distribution network (drinking and / or city). The connection and the emptying system can in particular maintain a fluid isolation between the two types of networks. The system may optionally be instrumented with measurement sensors and / or actuators for regulating the internal activity of the bioreactor. Different modes of regulation of a grid of bioreactors are described. Status data from connected networks (eg water, wastewater, cooling, heat networks) contribute to the regulation of a network of geolocated bioreactors. Aspects of software are described. The supervision of the grid of bioreactors can in particular be carried out remotely via onboard communication devices.
    A micro algae bioreactor regulation device is disclosed, enabling it to connect the urban public space to a collective sanitation network and thus achieve a virtuous cycle of carbon dioxide capture and biogas production.
    A micro algae bioreactor regulation device is disclosed, enabling it to connect the urban public space to a collective sanitation network and thus achieve a virtuous cycle of carbon dioxide capture and biogas production.
    Advantageously, the carbon well according to the invention can be integrated into the street furniture.
    Advantageously, the carbon well according to the invention is connectable or connected to the urban sewerage network.
    Advantageously, by capitalizing on existing sanitation networks, the invention creates a new and additional economic use value of these sanitation networks.
    Advantageously, an appropriate and / or automated management of the emptying of the biochemical reactor maintains a maximum CO2 absorption capacity, for example by optimizing the growth of the biomass of the microalgae.
    Advantageously, embodiments of the invention make it possible to measure the quantity of organic matter discharged to the network and in particular to prevent the return of foul odors, olfactory and / or visual nuisances, or even nuisances (eg cockroaches, insects, worms, rats, etc.) to the public space.
    Advantageously, the carbon well according to the invention can be networked. Developments describe the management of a park or network of urban wells: the regulation of such urban well networks can be carried out according to different modalities.
    Advantageously, in addition or in substitution, the system according to the invention allows the production of biogas.
    Advantageously, the system according to the invention makes it possible to carry out a virtuous cycle for capturing carbon dioxide.
    Advantageously, the system according to the invention responds to several major concerns of contemporary cities: a) the reduction of greenhouse gases b) the improvement of the quality of urban air c) the production of renewable energy.
    Advantageously, the methods and systems according to the invention participate in the energy transition.
    Advantageously, according to the embodiments, the methods and systems according to the invention can be applied to the treatment of (i) C02-charged urban air (road traffic zones, subway exit, parking), (ii) the treatment of the industrial era (combustion fumes of industrial air eg boiler room, incineration, etc.) but also to (iii) treatment of domestic air ("improved ficus")
    Advantageously, in one embodiment, the system according to the invention improves the quality of the air by capturing the carbon dioxide.
    In some embodiments, certain chemical compounds (e.g., pollutants) and / or particles or classes of particles are captured (e.g., precipitated and evacuated).
    DESCRIPTION OF THE FIGURES Other characteristics and advantages of the invention will become apparent with the aid of the description which follows and the figures of the appended drawings in which:
    Figure 1 illustrates a particular example of an embodiment of the invention specific to the urban environment;
    Figure 2 illustrates an embodiment of the invention for the treatment of urban air;
    Figure 3 shows aspects of an example of a reactor emptying system for connection to the sewerage network;
    FIG. 4 illustrates exemplary aspects of the invention, including modes of management of the connected reactor and optional features;
    FIG. 5 shows an example of a network of bioreactors according to the invention.
    Detailed description of the invention
    The general principle of the invention is to have a biochemical reactor in the environment, to control the biochemical reactions taking place in this reactor, for example by injecting material and / or energy and, after biochemical treatment within the reactor, to recover transformed material and / or energy, directly or indirectly. At least a portion of the biochemical agents of the reactor is directed to a network 120 (eg public sanitation). The management of a park or a network consisting of a plurality of reactors can be regulated in different ways.
    The systems and methods according to the invention can be broken down into numerous variants. Variants include in particular the number and type of reactor, the type and surfaces of capture and / or emission of reactor by-products, the type of connection to one or more networks - for example public sanitation but not only -, the modalities of regulation of a network consisting of a plurality of at least partially interconnected reactors, the general dimensioning of the installations (from millimetric quantities to major installations, of skyscraper type), etc.
    Various embodiments are described below.
    A computer-implemented method of regulating an air purification system comprising a bioreactor is disclosed, the method comprising the steps of receiving measurements of the concentration levels of one or more pollutants and / or particles in air flows in and out of a bioreactor containing water and biomass at least partially purifying some of these pollutants and / or particles; based on control parameters including measurements of the concentration rates received, determining a volume of biomass to be discharged from the bioreactor to a sanitation network connected to the bioreactor.
    In one development, the method further comprises a step of evacuating said determined volume of biomass into said sanitation network.
    In one development, the method comprises a step of reintroducing a volume of water into the bioreactor, for example after draining. New water can also be introduced before a combined water / biomass drain. The water supply (entry of the bioreactor) and the evacuation of the biomass (output of the bioreactor) are interdependent variables (or correlated or managed in combination). In some embodiments, fresh water is not supplied by the network, but only by an integrated tank. In some embodiments, an additional filter makes it possible to renew almost all of the water of the culture medium. In some embodiments, the volume of biomass removed is offset by an equivalent volume of fresh water.
    The sanitation network can be a public network (ie sewers), or a private network (eg industrial).
    A bioreactor may contain various microbiological agents that can treat air (atmospheric, ambient, industrial, urban, domestic, etc.) by purifying (ie removing and / or filtering and / or fixing and / or precipitating and / or metabolizing) some chemical compounds in the air, including one or more pollutants and / or toxic or harmful particles.
    In order to maintain optimal treatment or air purification efficiency, i.e., an optimal metabolism in the bioreactor, it is advantageous to partially empty it, at certain times, in certain proportions and under certain carefully chosen conditions.
    A pollutant (atmospheric) is a chemical element in excess of a predefined threshold.
    A pollutant is a biological, physical or chemical alteragen, which, beyond one or more predefined thresholds, and sometimes under certain conditions (potentiation), develops negative impacts on all or part of an organism, an ecosystem or the environment in general. A pollutant may in some cases be defined as a contaminant of one or more compartments of the ecosystems (air, water, soil) and / or an organism (eg humans) or affecting the ecosystem, beyond a predefined threshold or standard (scientific and / or legal).
    The pollutants can be of different nature (solid substance, liquid or gaseous), abnormally present in a given environment. The pollutants can be "micropollutants" ie toxic active products (mineral or organic) at minute concentrations (of the order of pg / l or less) or "macro-pollutants" ie substances or molecules of natural origin or not, being in the environment at abnormal concentrations, with negative effects on the Living.
    Particulate Matter (PM) refers to particles suspended in the Earth's atmosphere. Particulate matter as a whole is now classified as carcinogenic to humans.
    The nonlimiting list of pollutants and / or particles that can be manipulated and / or handled by the processes or systems according to the invention comprises, in particular: sulfur dioxide (SO 2), nitrogen oxides (NOx) whose carbon dioxide, Nitrogen (NO2), fine PM10, PM2.5, carbon monoxide (CO), benzene (C6H6), arsenic (As), cadmium (Cd), nickel (Ni), lead ( Pb), polycyclic aromatic hydrocarbons (PAHs) such as benzo [a] pyrene (B [a] P) and, more generally, greenhouse gases (eg CO2 carbon dioxide, hyperoxidizing ozone 03, nitrous oxide) N20, sulfur hexafluoride SF6 and halocarbons including CFCs).
    The biological treatments of the air can also concern the deodorization, for example starting from bacteria which will capture organic odoriferous molecules such as mercaptans or hydrogen sulfide.
    In a development, the bioreactor is connected to a water distribution network for supplying the culture medium of said bioreactor. The water supply (entry of the bioreactor) and the evacuation of the biomass (output of the bioreactor) are interdependent variables (or correlated or managed in combination). In some embodiments, fresh water is not supplied by the network, but only by an integrated tank. In some embodiments, an additional filter makes it possible to renew almost all of the water of the culture medium. In some embodiments, the volume of biomass removed is offset by an equivalent volume of fresh water.
    In a development, the purified air is the ambient air, in particular the ambient air in an urban environment. The geolocation of one or more reactors can be optimized to optimize the air treatment.
    In a development, at least one pollutant is a gaseous pollutant in the ambient air, preferably the C02 greenhouse gas (i.e. above a certain natural and / or legal threshold).
    In a particular case, the invention may constitute a carbon sink.
    In such a case, the CO2 rates are measured at the input and at the output (continuously, or periodically, or intermittently, or opportunistically i.e. on event). If the C02 uptake decreases, for example, it can be determined that biomass is in excess; in this case, a portion of the biomass is removed and / or new water is introduced into the culture medium.
    In a development, the bioreactor is a photo-bioreactor and the regulation parameters comprise parameters associated with the internal activity of the bioreactor, these parameters comprising one or more data chosen from: the pH, the temperature, the turbidity, the measured conductivity in the culture medium of the bioreactor, and the quantification of the luminous flux received by the culture medium of the bioreactor.
    In a development, the control parameters furthermore comprise data external to the bioreactor, these external data including data associated with the state of the wastewater network and / or data associated with the state of the water supply network. of the bioreactor.
    Data external to the bioreactor include system input (water) and outlet (sanitation) data. Sewerage network data include water / sludge level data, maintenance data, topological or topographic data or mapping, etc. Bioreactor water supply network status data includes water quality, pressure, flow rate, maintenance data, etc.
    In a development, the control parameters include data for measuring the level of wastewater in the sewerage system. The term "wastewater level" also refers to "circulating effluent level" or "sludge level".
    In a development, the control parameters include measurement data and / or weather forecasts.
    Weather data can have direct or at least indirect consequences on sewer levels. High sludge levels (heavy rainfall) would tend to increase the transport capacity of the biomass discharged. However, high levels can sometimes saturate downstream WWTPs, generally leading to bioreactor outflows at low levels in the wastewater system.
    In a development, the method further comprises management rules for determining the volume of biomass to be evacuated (the volume to be evacuated is determined by application of management rules, e.g. according to fuzzy logic or expert system)
    Management rules can be predefined. In whole or in part, they can be remotely modifiable. The rules make it possible to manage the biomass (light influx, water supply, nutrient supply, etc.) in particular to optimize the growth cycles, stop the activity if needed, etc. Rules can be static and / or invariant. They can be dynamic (e.g. linked rules).
    In a development, the bioreactor includes measurement sensors and / or remotely controllable actuators for regulating the activity of the reactor.
    In a development, the method comprises a step of receiving the data associated with a plurality of bioreactors connected to the same sewerage network, which sanitation network is optionally connected to one or more biogas plants.
    In one development, the plurality of bioreactors is connected to the same water distribution network for supplying the culture medium with bioreactors.
    The plurality of bioreactors connected to the same sewerage network constitutes a network or a grid. Bioreactors are geolocated; their respective geographical location is determined or determinable. Supervised globally or by peer-to-peer negotiation, neighboring states of a given bioreactor may be known.
    In a development, the method comprises a step of regulating the plurality of bioreactors based on geolocation data of said bioreactors, data associated with the state of the wastewater network and / or data associated with the state of the wastewater network. bioreactor water supply and / or data associated with the state of biogas production.
    The regulation of the grid of bioreactors may in particular comprise multiobjective optimization steps, the objectives being associated with one or more bioreactors and / or with the sewerage network and / or with the water supply network and / or with the production biogas downstream.
    The method of regulating the grid or the network of bioreactors may in particular aim to maximize the fixation of CO2 in atmospheric air by one or more bioreactors. It is also possible, in the alternative, to maximize the production of biogas from the biomass discharged by one or more bioreactors.
    In a development, the objectives or optimization criteria of one or more bioreactors include the minimization or maximization or optimization of the capture of one or more predefined substances (pollutants / particles) in the environment since one or more or several bioreactors, the qualitative and / or quantitative growth state of the biomass present in one or more bioreactors, the gaseous emission or the liquid or solid discharge of predefined substances from one or more bioreactors.
    In a development, the criteria for optimizing the discharges of a bioreactor into the sewerage network include the taking into account of external data of meteorological forecasts, these data notably including data of rainfall, temperature and sunshine.
    A computer program product is disclosed, said computer program comprising code instructions for performing one or more of the method steps, when said program is run on a computer.
    An air handling system is disclosed comprising means for carrying out one or more of the steps of the method.
    In a development, the system includes a bioreactor, air inlets and outlets; the bioreactor being configured to be connected to a sewerage network for the evacuation of at least a portion of the biomass.
    The reactor can be fixed and installed in the urban environment but it can also be removable and / or temporary. It is suitable for connection to a sewerage network, but may include additional means of evacuation of biomass (for example in excess).
    In one development, the bioreactor is a photo-bioreactor comprising photosynthetic microorganisms.
    The photosynthetic microorganisms suspended in water may be photosynthetic bacteria and / or cyanobacteria and / or eukaryotic microalgae and / or cells isolated from multicellular plants and / or gametophytes of macroalgae and / or protonemata of foam. If necessary, the tank or vessel or enclosure containing the biomass is at least partially transparent to light (generally transparent or translucent glass or plastic).
    In a development, the bioreactor is connected to a water distribution network to supply the culture medium of the bioreactor.
    In a development, the water distribution network is a network of pre-treated non-potable city water.
    The reactor according to the invention may not be connected at all to an inlet water network: the reactor according to the invention may be "preloaded" with water. Advantageously, it may be connectable and / or connected to a water network, which may be a drinking water network and / or a non-potable city water network (pre-treated Seine water).
    In one development, the system further includes a bioreactor drain system maintaining fluid isolation between the water system and the sewerage system.
    In one development, the drain system includes at least two tanks and remotely controllable solenoid valves, the tanks being configured to be alternately drained to maintain fluid isolation between the water system and the sewer system.
    In a development, the bioreactor is connected to a heat network and / or a cold network.
    In a development, the bioreactor connected according to the invention comprises a device for regulating the temperature of the bioreactor. The temperature of the bioreactor can be regulated, in particular with a heat exchanger and / or a heat network and / or heaters.
    A heat exchanger can be used (gas cooler or heating device) but advantageously the system according to the invention will be coupled with an existing infrastructure, such as a heat network (district heating network or private or industrial heating network) or a cold network. The heat network can be a steam network (e.g. private or public), a geothermal network. A cold network is the equivalent of a heat network, but dedicated to the transport and distribution of "frigories" rather than calories.
    In one development, the system includes one or more artificial light sources for regulating the activity of the bioreactor.
    Optionally, the system according to the invention may comprise reflectors and / or concentrators of natural light, to improve the activity of the bioreactor.
    In a development, the system includes one or more photovoltaic panels for powering one or more sources of artificial light.
    Optionally, the system according to the invention may comprise reflectors and / or concentrators of natural light, to improve the activity of the bioreactor.
    In a development, the system comprises one or more sensors selected from a pH meter, an indoor thermometer, an external thermometer, an oximetric probe, a level sensor, a conductivity sensor of the culture medium, a sensor adapted to the measurement the rate of CO 2 in the air of the bioreactor and / or the atmosphere, a sensor suitable for measuring the level of O 2 in the air of the bioreactor and / or the atmosphere and a sensor adapted to the measurement of CO 2 dissolved in the culture medium of biomass.
    In a development, the bioreactor further comprises one or more actuators for regulating the inlet and / or outlet air flows, and / or for agitating the reactor biomass, and / or for regulating the natural light influx and / or or artificial and / or to regulate the temperature. In particular, to regulate means to be able to adjust or adjust.
    In a development, the flow rates of the air inlets and / or air outlets of the bioreactor are controllable or configurable (in particular at a distance). I / O or I / O can be controlled remotely. They allow aerobic and / or anaerobic operations, depending on the type of reactor used. In a development, the connected bioreactor according to the invention comprises one or more ventilation devices. These devices comprise for example one or more fans and / or compressors.
    In a development, the bioreactor connected according to the invention further comprises one or more actuators adapted to stir the biomass of the reservoir.
    In a development, the bioreactor connected according to the invention further comprises one or more actuators adapted or configured to regulate the natural and / or artificial light influx. The system according to the invention may comprise blinds or shutters for example. The opacity of the panes or walls of the tank exposing the microalgae can also be controlled.
    In one development, the connected bioreactor according to the invention comprises one or more access routes for the injection of biological and / or chemical compounds into the bioreactor. For example, the system according to the invention may comprise accesses allowing the injection into the reactor of products such as fertilizers, solvents, additives or dyes.
    In a development, the bioreactor connected according to the invention further comprises means for discharging at least a portion of the biomass independent of the sewerage network. Excess or unnecessary or ineffective biomass can be evacuated locally, without going through the sewerage network (or not exclusively, for example temporarily or extra).
    In one development, the system further includes a communication device for remotely controlling the activity of the bioreactor.
    In one development, the system further comprises a bidirectional communication device for remotely controlling the activity of the bioreactor. The activity of the bioreactor is regulated by the management of water inputs, biomass evacuated, light inputs or nutrients.
    Sensor data can be accessed remotely. The control of the actuators can be carried out remotely (regulation of the activity of the bioreactor, in particular by controlling the inputs of water, nutrients, solar and natural influx, agitation of the biomass and aeration )
    In one development, the system comprises a plurality of bioreactors.
    Bioreactors can be positioned in a predefined geographic area to maximize CO2 capture and / or maximize O2 emissions to the atmosphere of the geographic area.
    In one development, one or more bioreactors are connected to one or more biogas devices.
    A bioreactor can be associated with a biogas production unit in the immediate vicinity. In the general case, the biogas production entity is located at a distance. A plurality of bioreactors may be connected via the sewerage system to a biogas plant (eg methane).
    Figure 1 illustrates a particular example of an embodiment of the invention specific to the urban environment.
    In one embodiment, as illustrated in FIG. 1, the reactor is a photo-bioreactor (PBR) or microalgae bioreactor 100. Microalgae are exposed to light through transparent surfaces 101 for example, the glazed surfaces are arranged on a street furniture type Morris column 102). The carbon sink is integrated into or takes the form of street furniture installed within the public space. Micro-algae carry out cycles of biochemical photosynthesis and constitute a carbon sink: carbon dioxide is partially captured or fixed by algae and dioxygen is released into the environment 104. The biomass of micro algae evolves over time . At a certain predefined threshold, and according to different modalities, part of the biomass created is eliminated, for example via drain lines 106 to one or more sewage networks 120. In a particular embodiment, the effluent, composed of micro-algae and their culture medium, resulting from the C02 absorption process is evacuated via a particular connection 105 to the urban sanitation network 120.
    A carbon well 100 according to the invention can be placed in a judicious or timely or strategic or relevant or optimized location within the public space, that is to say in a place where the urban air is particularly busy in C02. For example, the carbon well may be placed near a subway air vent 111 and near a garage exit 112.
    More generally, in terms of uptake, the urban areas with high CO2 emissions provide suitable locations for the installation of the system according to the invention: road tunnels, interchanges, particularly heavy traffic areas, such as the Paris ring road etc. In addition, in terms of emissions, favorable locations include sensitive areas such as schools, hospitals or densely populated urban housing areas. Computer modeling and / or measurements of air circulation and air quality can optimize the different compromises made between optimisations in terms of C02 capture (and / or pollutants) and optimizations in terms of of oxygen (or other selected byproduct).
    The embodiments use one or more bioreactors arranged in series and / or in parallel. A bioreactor ("fermenter" or "propagator") is a system in which microorganisms (eg yeasts, bacteria, microscopic fungi, algae, animal and plant cells, homogeneously or in combination) for the production of biomass are multiplied. and / or for the production of a metabolite or the bioconversion of a molecule of interest.
    A bioreactor generally comprises a) a tank or a vessel or enclosure, for example glass or stainless steel; the shape of the tank may be flat (glass plates containing micro-algae) or circular or in any other form b) access routes for the circulation of air between the indoor environment and the outside environment (these channels may be temporarily closed or clogged); (c) access routes for the injection of water and / or nutrients (fertilizers) and / or chemical compounds (solvents, additives, dyes); the water injected into the culture medium may be drinking water and / or non-potable water, for example water from the Seine water network pretreated by the City of Paris; in other words, the reactor according to the invention can use feedwater and / or tap water d) sometimes actuators (for example a stirring system for mixing or circulating the biomass in the reactor (eg turbines, articulated arms, etc.) e) sensors or sensors (for measuring temperature, pH, dissolved oxygen concentration, internal level, etc.); the sensors can therefore include one or more pH meters, thermometers, oximetric probes, pressure sensors, level sensors, etc. These different sensors or probes can be positioned appropriately and optimized within the bioreactor so as to derive a faithful image of the internal biodynamics of the reactor.
    A bioreactor is generally regulated by a computer-implemented control system for measuring, recording and controlling all operating parameters of the reactor. A bioreactor may in some cases be autonomous i.e. self-regulated by the implementation of management rule not requiring external intervention. In some cases, the bioreactor according to the invention may comprise an emergency stopping tank (in case of drift of the creation of biomass, the latter may be stopped by the injection of bleach or a mixture including weeding and / or fungicidal fluids).
    In one embodiment, the bioreactor comprises a photobioreactor (based on the cycle of photosynthesis). This type of reactor is known. Patent application FR2978159 discloses, for example, a photobioreactor for the closed circuit production of a concentrated algal solution comprising a container containing the algal solution, and a means for exposing the algal solution to light; the exposure means comprises at least one vertical sleeve made of a flexible material, transparent, resistant to traction, this sleeve being suspended from a support and filled with a liquid which ensures a cylindrical shape to this sleeve, which is in contact by its outer wall with the algal solution.
    In certain other embodiments, other types of reactors may be used, in combination or substitution of the photobioreactor, ie according to different biochemical processes (eg with bacteria whose function has been determined by synthetic biology techniques or genetic engineering).
    In one embodiment, one or more dyes may be used. In this way, street furniture implementing the invention may appear to the public in different colors (e.g. pink, blue or multiple colors) and not necessarily green (as may be micro-algae).
    In one embodiment, the reactor according to the invention may further comprise one or more sources of artificial light. For example, the system according to the invention may comprise light emitting diodes (LEDs for Light Emitting Diode) or growth lamps, whose light spectrum may be adapted or optimized for the growth of microalgae (absorption bands specific to photosynthesis)
    In one embodiment, the reactor according to the invention may comprise means for capturing the solar luminous flux, possibly including concentrating means (eg reflective panels or reflectors, magnifiers, etc.) and / or modulation means of the light source. light impulse (eg shutters or slats, reclining blinds, variable opacity of glazed surfaces, etc.).
    In one embodiment, the reactor according to the invention may comprise a combination of natural and artificial light influx. Advantageously, artificial light sources can overcome temporary deficits of natural light, via accumulators and / or solar panels for example. Even without a point deficit, the use of artificial sources can maintain photosynthesis of microalgae at high levels. Many regulations of the activity of the bioreactor become possible. For example, photovoltaic panels recharged during the day can feed the light sources at night and ensure the growth of algae, allowing for an uninterrupted photosynthesis of micro-algae (or equivalent). The combined use of the two types of sources can also make it possible to maintain a constant luminous flux.
    Light flows (artificial and / or natural) passing through glazed or transparent or translucent surfaces (exposing microalgae for photosynthetic cycles) can be configurable and / or controlled, in order to regulate the evolution of biomass. For example, blinds or shutters can be used to modulate light flows appropriately. The opacity of the windows can also be configurable (the application of an electric current can obscure or lighten a window). In one embodiment, one or more miniature reactors are integrated into solar panels with configurable opacity.
    The sizing of the systems according to the invention is very variable.
    In one embodiment, an "urban" type reactor may have a capacity of 1 m3 of microalgae equivalent to the production of oxygen of about fifty trees (e.g. plane trees). A carbon sink containing 1 m3 of microalgae fixes about 1 tonne of CO2 per year, releases more than 600 kg of oxygen into the city air, produces more than 350 m3 of bio methane and allows network injection more than 3500 kWh of bio gas.
    In one embodiment, a reactor (of the "industrial" type) used by the invention may have a capacity of 6000 m3 (representing 5000 tonnes per year of captured CO 2, which is of the order of magnitude of the biomass equivalent to the 850-hectare Bois de Boulogne).
    The concrete forms of implementation of the systems and methods according to the invention can therefore be declined in many ways, especially in the form of street furniture (eg Morris column, bus shelter, billboards, roofing ...), urban equipment (eg glazed roofs, roadways, etc.), industrial installations (eg air purification reactor near industrial areas), domestic appliances (eg improved air purifier and connected to the sewer system, etc.) . The exposure surfaces of micro algae or biochemical agents are variable, from a few square meters to buildings entirely covered with glazed or transparent or translucent surfaces exposing micro algae or biochemical agents.
    In one embodiment of the invention, air ventilation may be natural, i.e. the network of bioreactors captures carbon dioxide near the facilities. Additional ventilation means may also be used to increase or optimize CO 2 capture. The means of ventilation and / or concentration and / or compression of urban air may include one or more fans. A fan can be integrated into street furniture including a bioreactor. A plurality of fans may also be integrated into the street furniture or the bioreactor itself. The dimensions of the fans are variable, from macroscopic orders of magnitude (e.g., from HF fans to millimetric ventilation devices) or even microscopic (e.g., use of MEMS).
    In one embodiment, a known compressor of the state of the art can be used, for example with a power of 75 W. In such a configuration, for a reactor of about 1 m 3, the incoming air flow is typically of the order of 6 m3 / h peak and 2 m3 / h on average.
    The direction of the wind and more generally local air flows around the urban installations including the fans can be modeled and / or measured (for example by means of anemometers eg laser embedded on the street furniture and / or arranged according to a network of independent sensors but coupled with the systems according to the invention).
    According to one aspect of the invention, it is disclosed an urban air purification system having a connection to the sewerage network.
    The sanitation network is usually public (sewers). In some embodiments, in addition to or in substitution for the public sanitation network, private or "proprietary" or dedicated networks may be used. Evacuation of compost or effluent can be done (exclusively) via connection to the sewerage network. Advantageously, this embodiment does not require dedicated logistics.
    In an alternative embodiment, the evacuation of compost or effluent can be carried out (exclusively) by physical removal; for example, garbage collection trucks access through traps to surplus or dried compost aggregates. Drones or automated vehicles can collect aggregates, for example concentrated. Advantageously, this embodiment does not require access to the sewerage network.
    In one embodiment, the discharge of the compost or effluent can be carried out partially by physical collection and partly by connection to the sewerage network. Advantageously, this embodiment makes it possible to optimize the mesh, that is to say the optimization of the distribution of the carbon wells according to the invention in an urban environment (multi-criteria optimization as regards the capture of the materials to be transformed, l emission of processed materials, disposal of by-products according to the availability of access points to the sewerage network, etc.)
    Figure 2 illustrates an embodiment of the invention for the treatment of urban air.
    The carbon sink 100 captures the ambient urban air 103, releases oxygen 104 into the atmosphere and excess microalgae 105 in the sewerage network 120. The carbon sink effluents according to the invention are added and are combined with the wastewater streams, which reach the purification plant 200. After a first settling step 201, the sludge is digested (by bacteria) in step 202 and biogas 203 is produced (by anaerobic digestion). , or other), which is reinjected into the energy networks 210.
    In a particular embodiment, the system according to the invention may comprise a microalgae photo-bioreactor 100. The process for capturing atmospheric carbon dioxide 103 is coupled with a process for converting carbon into biohydrocarbon 203 by methanation. . The microalgae are transported to a purification plant 200 having a methanization process contributing in terms of organic substrate to the said anaerobic digestion stream 203.
    The photobioreactor 100 may comprise unicellular algae of the Chlorella type, which capture C02. Many other types of strain are possible, notably allowing the fixation or the capture or the precipitation of particles present in the air (urban or industrial). One of the processes underlying the operation of the bioreactor according to the invention is that of photosynthesis.
    In variants, the absorption of CO2 can also be done using amine solvents, in particular ethanolamine (2-aminoethanol). By being in contact with acid gases (such as CO 2), an aqueous solution of 2-aminoethanol forms a salt at room temperature. The solution is then transported in a closed medium where it is heated to about 120 ° C., which, according to the principle of Le Chaager, releases CO 2 (pure) and regenerates, in aqueous solution, 2-aminoethanol. Alternatives to this chemical process include absorption techniques by rapid temperature / pressure variation, gas separation, cryogenics or the use of hydroxides.
    Finally, other embodiments of the invention may comprise entirely different biochemical processes.
    Figure 3 shows aspects of an example of a reactor emptying system for connection to the sewerage network. The term "process water" refers to the water produced by the industrial process according to the invention. It is in this case a water loaded microalgae (at least in some embodiments) and / or the liquid constituting the microalgae culture medium.
    The diagram of Figure 3 details in particular the operation of the evacuation system (draining) of process water to the sewerage network. The interface between the CO 2 absorption process and the sewerage network can indeed be realized by a specific emptying system.
    The draining system according to the invention comprises for its connection a connection to the water network 301 (potable and / or non-potable, for example water from the Seine water network pre-treated by the City of Paris), a process water supply 302 (microalgae culture), used process water collector charged with algae 303, evacuation to sanitation network 304 and control / power terminal block 306 (power supply).
    An external control signal 313 originating from the automated supervision or from a human operator controls the opening of the solenoid valve 311 ensuring the filling of the tank 309. After closure of the valve 311, a weight measurement is carried out by the sensor of 308 force then the tank is drained via the drain connection 304 by controlling the solenoid valve 312. After closing the valve 312, a new weight measurement is performed by the force sensor 308. The mass of rejected solution is obtained by difference of the two previous measurements. The sequential opening of the solenoid valves 311 and 312 ensures the hydraulic disconnection with the sewerage network. In other words, the disconnection of the reservoirs implies that the process water supply valve 311 is closed during the discharge phase to the sewerage network for which the valve 312 is open.
    During the filling phase of the tank 309, the volume of fresh water injected into the process is measured by the volumetric meter 307. A daily balance is established by the central control unit 305 by difference between the incoming water mass and the mass of solution leaving the device. The absence of organic matter deposition in the tank 309 is guaranteed by a non-adherent inner lining associated with a cleaning cycle triggered by the control of the solenoid valve 312.
    In the embodiment of the invention comprising the cultivation of microalgae, the risks of migration or rise of microalgae by the different lines (eg to 301, 302 or 303) is low or negligible, since the microphones Algae are photo-dependent (micro-algae excursions will be limited in space). In embodiments of the invention utilizing different biochemical processes, the evacuation lines may include check valves and / or be chemically treated to minimize or avoid biochemical lifts.
    In one embodiment, the system according to the invention may comprise a force sensor 308, which measures, for example, the resistance to a current that is modified as a function of the force exerted. Different techniques concerning the weighing of sand volumes on hydro cureurs can be used. Other complementary techniques for measuring the weight of microalgae are possible. For example, measurements (for example, optics) of algae concentration can be combined with volume measurement (eg by level measurement or thresholds).
    In general, the system according to the invention may comprise a plurality of tanks arranged in parallel.
    In a particular embodiment of the invention, the system may comprise two tanks arranged in parallel. According to this dual configuration, the emptying is performed alternately. The use of two storage tanks 309 and 319 arranged in parallel allows a sequenced or alternating operation which ensures the permanent supply of the process in new water and the hydraulic disconnection with the sewerage network. A given reservoir acts as a "buffer" with respect to the other and makes it possible to maintain a "leakage" flow rate, that is to say a constant new water supply into the photobioreactor. The use of a large number of photobioreactors arranged in parallel reduces the risk of failure of the overall system.
    FIG. 4 illustrates examples of implementations of the invention, in particular modes of management of the connected reactor and optional characteristics.
    In one embodiment, the photo-bioreactor 106 can be placed in the public space 407, connected to the sewerage network 408 and has a supply of feedwater or city 402 and electrical energy 401. The reactor can be instrumented by sensors and automatizers 403, and comprises communication means, for example a remote antenna 404. This remote polling antenna 404 allows in particular bidirectional communication between the system 106 according to the invention. invention and a supervisory position (man and / or machine). A control signal triggers the handling of solenoid valves causing the evacuation of the process water loaded with algae 405 to the storage tanks (for example 309) before being discharged to the purification network 408. The measurement of the mass of rejected algae 405 is established by difference in weight between incoming fresh water and wastewater leaving the device, by means of different sensors.
    Various aspects of management of a connected reactor according to the invention are described below.
    In general, the decrease of the temperature, the pH and the organic matter concentration of the effluents can be obtained by dilution effect: water (potable or non-potable, for example non-potable water pretreated Seine water network of the City of Paris) can be added to achieve the minimum predefined values required.
    In one embodiment, a minimum water level can be left at the bottom of the tank (for example 309) after emptying to stop odors coming from the sewerage network 408 in the manner of a siphon. The tanks are for example provided with a vent with activated carbon filter.
    A disconnection device (303, 311, 309, 308, 311) can provide protection for the mains water system.
    In one embodiment, the process water passes through storage tanks 309 and 319, the opening of the filling and emptying valves being alternated.
    Effluent discharges can be by flushing effect, which generally has the effect of cleaning the discharge line and preventing the build-up of solid matter. Optionally, the tanks are provided with a non-adherent liner.
    Weather forecasts can advantageously be taken into account in the regulation of effluent discharges; for example, rain or thunderstorm alerts transmitted via the on-board communication means or remote-reporting antennas 404 increase the probability of high level in the sewerage networks, in which case the oil changes may be delayed in the time for certain parts of the grid or network of bioreactors connected according to the invention or, on the contrary, accelerated ie implemented opportunistically in certain other sectors.
    Certain specific shapes of the tanks and their non-adherent inner lining may help to ensure the absence of organic deposition. In some cases, a rinsing with the water of the network can be carried out (daily or according to measurements carried out locally).
    The system according to the invention may comprise an urban cladding (possibly instrumented) comprising a photo-bioreactor (usually instrumented), connected to the sanitation network (monitored)
    In one embodiment, the envelope or the urban cladding (eg Morris column, bus shelter, building facade, pavement or sidewalk portion, public toilets possibly paid for) may include sensors (eg photovoltaic panels or equivalent, with or without accumulator or battery, presence or motion detectors, measurement of the C02 input and output, measurement of the oxygen or of a determined pollutant, input and / or output, etc.) and / or actuators (top speakers, shutters operable remotely, etc.). The dressing of the bioreactor may include one or more fans (inlets and outlets), access to compost removal or portions of biomass, access to nutrient additions. In some embodiments, the confinement envelope of the bioreactor may also include perfume diffusion means (for annihilating or masking unwanted odors), acoustic diffusion means, computer display screens (eg card display visual or textual information is not exclusive to the exposure of micro-algae, which can grow behind semi or partially transparent screens), means of projection (projection of information on the pavement or the walls), calculation means (eg processors) and communication means (wired or wireless, specific to the system according to the invention and / or to serve as public relay antennas), etc. Tangible and / or logical means corresponding for example to social functions can be made available to the public (e.g. biomass health reports, images of its evolution) or means allowing interactivity with the public.
    In connection with the bioreactor, a number of parameters may be monitored and / or controlled. These parameters may include (for example and if applicable), in particular: the rate of CO 2 of the inlet air, the CO2 content of the outlet air, the level of dissolved CO 2 (for example in the culture medium), pressure at the outlet of the compressor (fan), turbidity (eg rheology measurements of the reactor's internal biomass), concentration of microalgae by optical measurement of the density of the culture medium, indoor temperature (probed in different bioreactor locations), the temperature outside the reactor (for example the temperature measured in the street), the light impulse (in particular the measurement of solar gains and / or the level of artificial lighting), the pH (acidity or basicity biomass or process water medium), conductivity (from biomass or process water medium, RedOX, N03 and / or P04 concentrations.
    In one embodiment, the temperature of the reactor can be regulated by means of a connection to an existing heat network and / or geothermal and / or by the use of a heat exchanger placed in the vicinity of the heating network. sanitation.
    A negative efficiency alarm can be triggered, for example if the averaged CO 2 flow becomes negative.
    According to the embodiments (and according to the data types), the sampling of the data can be performed every 30 seconds, every 5 minutes, every 15 minutes, every hour or according to predefined thresholds (and / or configurable ).
    The bioreactor or the urban cladding may comprise one or more sensors whose measurements allow after processing of information by a computing unit the measurement of the quantity of organic matter discharged to the sewerage network. In one embodiment, the discharges or effluents of the bioreactor are measured and monitored (qualitatively and / or quantitatively), in particular remotely (eg wired or wireless communication means, by remote read, encrypted or unencrypted, etc.) . The TV system can be particular-mono directional or bidirectional.
    A number of parameters relating to the sewerage network may be monitored and / or regulated. These parameters may include, but are not limited to, the water level (to adjust the flushes at appropriate times and / or at appropriate locations in the grid of network bioreactors), the physical properties of the sludge measured locally or globally and statistically. (eg PH, turbidity, conductivity, RedOX, N03 and / or P04 concentrations).
    In general and without limitation, the sensors (or sensors) embedded by the system according to the invention (for example in the urban dressing of the photo bioreactor and / or in the bioreactor itself and / or in the sewerage network ) may include one or more sensors or sensors selected from pressure, flow, temperature, oxygen, velocity, motion, position, location, radioactivity, energy, product or component sensors chemicals (eg nitric oxide, ozone, smoke, pollutants, etc.) or biological products or components (eg viruses, contaminants, pollen, etc.). The sensors can include one or more MEMS, magnetometers, hygrometers, gyroscopes, accelerometers, biosensors, radars, sonars, cameras, 3D scanners etc.
    In general and not limitation, the actuators or actuators may be of the pneumatic, hydraulic, electrical, mechanical, magnetic, pelletier, piezoelectric or electroluminescent, etc. They may for example include one or more cylinders, motors, heating resistors, lamps, acoustic enclosures, electromagnets, or even heat coolers, ionizers, valves, valves, winders, etc.
    In general, the overall system supervision covers the control of (i) urban dressing and its sensors / actuators, (ii) the bioreactor as such, and (iii) the sanitation network. Global supervision may include the reception, analysis and prediction of meteorological type data. For example, rainfall forecasts can influence different drainages of networked bioreactors (some areas will be drained before others, for example). Factors related to temperature and light input with direct consequences on biomass evolution can also be monitored.
    The supervision of the overall system and / or of one or more reactors in particular can be performed automatically, semi-automatically or manually. It can be done remotely and / or locally (some operations may require certain permissions and / or physical presence on site). The regulation of the system can be carried out in a fixed manner ("checkpoint") and / or in mobility. In general, a web portal with web services and / or software applications ("apps") can provide access to and / or control of reactor monitoring data. Via one or more "apps", possibly secure, a variety of terminals can be used for the data consultation and / or the takeover of a reactor or grid of reactors, including smartphones, tablets, laptops or servers. Access rights can be defined. User interfaces using touch, augmented reality and / or virtual technologies can be used.
    Figure 5 shows an example of a network of bioreactors, i.e. a plurality of reactors interconnected to the sewerage network. Some wells are photo-bioreactors, others are not (eg genetically modified bacteria bioreactors). In terms of topology, the wells 100, 511, 512 and 513 are directly connected to the sewerage network and the wells 501, 502, 503 indirectly connected via the well 100. The reactor 511 is bidirectional: it can reject its effluents in the sewerage network but also extracting material for example for treatment (like the reactor 512). Well 513, like well 100, is a carbon well comprising a photo-bioreactor discharging its effluents into the sewerage system. Well 100 is a photobioreactor networked with several other reactors. In the example, the well 502 is a Morris column according to the invention and the well 100 is an adjacent bus shelter whose biomass tanks communicate. The well 501 corresponds to the facade of a building implementing a system according to the invention. Well 503 is a glazed sidewalk portion according to the invention. The well 531 is a well according to the invention connectable but not connected to the network 120. For this well 531, compost microalgae can be collected on site (or dumped in another sewer network separate network 120). The purification station 200 may be part of the overall regulation.
    Different modes of regulation of a network of connected or connectable carbon wells are described below.
    The modes of regulation can be variable and variously controllable, from the upstream to the downstream, ie since the capture of the air and / or pollutants, the activity of the bioreactor, the management of the discharges of the effluents, the levels of the wastewater measured or simulated in sewerage systems, weather forecasts and their consequences for dilution, etc.).
    Figure 5 shows a park or a network of carbon wells connected and / or connectable to the sewerage network 120 which leads to the purification plant 200, which produces the biogas reinjected into the energy networks.
    The topology of the graph of the interconnected reactors allows a more or less sophisticated regulation, that is to say according to multiple and various feedbacks. The graph corresponds to a grid ("grid") of interconnected entities. This grid of carbon sinks can be supervised by applying complex system control systems (formal logic, fuzzy logic, peer-to-peer negotiations, voting mechanisms), that this regulation is partially the work of man ( human operator or supervisor) and / or because of the machine (local decisions made by computer, arc-reflexes, etc.).
    Well reactors can be instrumented (that is to say embed sensors measuring the state of growth of biomass or many other parameters such as temperature, concentration etc), as well as the sewerage network (eg work in progress, topography, pollutant loads or concentration in different places etc).
    In addition, alongside or by means of measurement sensors quantifying the reality, empirical and / or theoretical models of supervision can allow to regulate the whole system. The perimeter of the system may include the modeling of flows and air quality (eg variable scale granularities, for example from the street to the whole agglomeration), the well network (eg reactor types, cycles biomass, capacities, etc.), the sewerage network itself (eg water levels, maintenance work, weather forecasts, etc.) and the sewage network (eg settling cycles, anaerobic digestion, etc.)
    In one embodiment ("push"), the downstream does not control the upstream (even partially). For example, the wastewater treatment plant 200 passively "passes" the accumulated spills of the carbon sinks in a network. A regulation can then be carried out upstream if necessary, for example by determining the load of the downstream treatment plant (e.g. observed or measured or calculated or simulated). For example, wells can communicate with each other, "dialogue" by implementing peer-to-peer decision-making systems to vote or decide which reactors will be allowed to drain or not, depending on which sequences, etc.
    In one embodiment ("pull"), the downstream controls the upstream (at least partially). For example, the wastewater treatment plant 200, depending on its charge and its own methanization cycles, directly or indirectly controls the emptying of upstream carbon sinks. In the case of a heterogeneous park (combining photo-bioreactors and reactors with synthetic biology with genetically modified bacteria), the treatment plant 200 can influence (or allow or promote or weight or facilitate or accelerate or delay or prohibit or shift ) the emptying of certain wells, taking into account the cumulative dilution effects or the resulting composition of the collected wastewater.
    In ("hybrid") embodiments, upstream and downstream contribute in a variety of ways to global regulation. For example, some reactors with an overload of downstream treatment will increase the opacity of the surfaces exposing the micro-algae to reduce biomass growth. If a local need for air purification becomes urgent (beyond a certain predefined threshold), because an inhabited area becomes polluted, and that simultaneously the downstream absorption capacities do not allow a short-term evacuation, punctual emptying (by truck or ejection of a compost after desiccation) can solve punctual or "peak" problems on the network. As all the reactors are not equipped with dual evacuation modes (physical compost and sewerage network), the management of the graph underlying the carbon sink network according to the invention can allow alternative solutions.
    Examples of management of the grid or network of bioreactors are described below (these scenarios are in no way limiting). In a first scenario, if work is in progress in a particular zone of the sewerage network, the supervisor (human and / or machine) can temporarily stop the emptying of the bioreactors of the area concerned and / or may decrease the metabolism of the bioreactors. by decreasing the contributions of light. In a second scenario, a pollution alert being in progress, the activity of the bioreactors can be maximized as much as possible for each of the bioreactors. In a third scenario, if the quality of the urban air is determined to be satisfactory, the light inputs can keep the algae active but without going to a purification mode. In a fourth scenario, severe thunderstorms are expected, the emptying of bioreactors close to the saturation in biomass can be done in advance to take advantage of transport capacity and batteries of photovoltaic panels can be recharged to the maximum extent to continue the lighting during low light weather disturbances. In a fifth scenario, in case of high level in the sewer system (rain and / or flood and / or during peak hours, eg football match) which high level usually leads to overloads and / or malfunctions downstream treatment plants (and may lead to untreated discharges into the environment), it will usually be avoided to drain in this type of context. Alternatively, appropriate draining sequences may be provided by zones (interzones) and / or within zones (intra-zones), etc. In a sixth scenario, the treatment plant being in maintenance, emptying will be avoided as much as possible.
    The present invention can be implemented from hardware and / or software elements. It may be available as a computer program product on a computer readable medium. The support can be electronic, magnetic, optical or electromagnetic. The terms computer program and software are used herein in a general sense to refer to any type of computer code (eg, application software, firmware, microcode, or any other form of instruction of a computer. computer) that can be used to program one or more processors to implement aspects of the techniques described herein. The means or computer resources can be distributed ("cloud computing"), possibly with peer-to-peer technologies. The software code can be executed on any appropriate processor (for example, a microprocessor) or processor core or set of processors, whether provided in a single computing device or distributed among a plurality of computing devices (eg example as possibly accessible in the environment of the device).
    权利要求:
    Claims (29)
    [1" id="c-fr-0001]
    claims
    A computer implemented method of regulating an air purification system comprising a bioreactor, the method comprising the steps of: - receiving measurements of the concentration levels of one or more pollutants and / or particles in air flows in and out of a bioreactor containing water and biomass at least partially purifying some of these pollutants and / or particles; depending on the regulation parameters comprising the measurements of the concentration levels received, determining a volume of biomass to be discharged from the bioreactor to a sanitation network connected to the bioreactor and a volume of water to be reintroduced into the bioreactor; - evacuate said determined volume of biomass in said sewerage network; - Replenish the bioreactor with the determined volume of water.
    [2" id="c-fr-0002]
    2. Method according to claim 1 wherein the bioreactor is connected to a water distribution network for supplying the culture medium of said bioreactor.
    [3" id="c-fr-0003]
    3. Method according to one of claims 1 to 2 wherein the purified air is the ambient air, in particular the ambient air in an urban environment.
    [4" id="c-fr-0004]
    4. Method according to one of claims 1 to 3, at least one pollutant being a gaseous pollutant in the ambient air, preferably greenhouse gas C02.
    [5" id="c-fr-0005]
    5. Method according to one of claims 1 to 4, the bioreactor being a bioreactor photo and the control parameters comprising parameters associated with the internal activity of the bioreactor, these parameters comprising one or more data selected from: the pH, the temperature, the turbidity, the conductivity measured in the culture medium of the bioreactor, and the quantification of the luminous flux received by the culture medium of the bioreactor.
    [6" id="c-fr-0006]
    6. Method according to one of claims 1 to 5, the control parameters further comprising data external to the bioreactor, these external data comprising data associated with the state of the sewerage network and / or data associated with the status of the water supply network of the bioreactor.
    [7" id="c-fr-0007]
    7. Method according to one of claims 1 to 6, the control parameters comprising data for measuring the level of wastewater present in the sewerage network.
    [8" id="c-fr-0008]
    8. Method according to one of claims 1 to 7, the control parameters comprising metering data and / or weather forecasts.
    [9" id="c-fr-0009]
    9. The method of claim 1, further comprising management rules for determining the volume of biomass to be evacuated.
    [10" id="c-fr-0010]
    10. Method according to one of claims 1 to 9, the bioreactor comprising measurement sensors and / or remotely controllable actuators to regulate the activity of the reactor.
    [11" id="c-fr-0011]
    11. A method according to any one of the preceding claims, comprising a step of receiving the data associated with a plurality of bioreactors connected to the same sewerage network, which sanitation network is optionally connected to one or more production stations. of biogas.
    [12" id="c-fr-0012]
    12. The method of claim 11 wherein the plurality of bioreactors is connected to the same water distribution network for supplying the culture medium of the bioreactors.
    [13" id="c-fr-0013]
    The method according to claim 12, comprising a step of regulating the plurality of bioreactors based on geolocation data of said bioreactors, data associated with the state of the wastewater network and / or data associated with the state of the bioreactor. bioreactor water supply network and / or data associated with the state of biogas production.
    [14" id="c-fr-0014]
    A computer program product, said computer program comprising code instructions for performing the steps of the method of any one of claims 1 to 13 when said program is run on a computer.
    [15" id="c-fr-0015]
    15. Air treatment system comprising means for carrying out the steps of the method according to any one of claims 1 to 13.
    [16" id="c-fr-0016]
    The system of claim 15 comprising a bioreactor, air inlets and outlets; the bioreactor being configured to be connected to a sewerage network for the evacuation of at least a portion of the biomass.
    [17" id="c-fr-0017]
    17. System according to one of claims 15 or 16, the bioreactor being a photo-bioreactor comprising photosynthetic microorganisms.
    [18" id="c-fr-0018]
    18. System according to one of claims 15 to 17, the bioreactor being connected to a water distribution network for supplying the culture medium of the bioreactor.
    [19" id="c-fr-0019]
    19. System according to one of claims 15 to 18, the water distribution network being a pre-treated non-potable city water network.
    [20" id="c-fr-0020]
    20. System according to one of claims 18 or 19, further comprising a system for emptying the bioreactor maintaining a fluid isolation between the water network and the sewerage network.
    [21" id="c-fr-0021]
    21. System according to claim 20, the emptying system comprising at least two tanks and remotely controllable solenoid valves, the tanks being configured to be alternately drained so as to maintain a fluid isolation between the water network and the water supply network. sanitation.
    [22" id="c-fr-0022]
    22. System according to one of claims 15 to 21, the bioreactor being connected to a heat network and / or a cold network.
    [23" id="c-fr-0023]
    23. System according to one of claims 15 to 22, comprising one or more sources of artificial light for regulating the activity of the bioreactor.
    [24" id="c-fr-0024]
    24. System according to claim 23, comprising one or more photovoltaic panels for supplying one or more sources of artificial light.
    [25" id="c-fr-0025]
    25. System according to one of claims 15 to 24, comprising one or more sensors selected from a pH meter, an indoor thermometer, an external thermometer, an oximetric probe, a level sensor, a conductivity sensor of the culture medium. , a sensor suitable for measuring the rate of CO 2 in the air of the bioreactor and / or the atmosphere, a sensor adapted to measuring the level of O 2 in the air of the bioreactor and / or the atmosphere and a sensor adapted to the measurement of CO 2 dissolved in the culture medium of the biomass.
    [26" id="c-fr-0026]
    26. System according to one of claims 15 to 25, the bioreactor further comprising one or more actuators for regulating the inlet and / or outlet air flow rates, and / or for agitating the reactor biomass, and / or to regulate the natural and / or artificial light influx and / or to regulate the temperature.
    [27" id="c-fr-0027]
    27. System according to one of claims 15 to 26, further comprising a communication device for remotely controlling the activity of the bioreactor.
    [28" id="c-fr-0028]
    28. System comprising a plurality of bioreactors according to one of claims 15 to 27.
    [29" id="c-fr-0029]
    29. The system of claim 28, one or more bioreactors being connected to one or more biogas production devices.
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    同族专利:
    公开号 | 公开日
    CN109069988A|2018-12-21|
    US20180304195A1|2018-10-25|
    WO2017077061A1|2017-05-11|
    EP3370852A1|2018-09-12|
    JP6843873B2|2021-03-17|
    US10807037B2|2020-10-20|
    JP2019503817A|2019-02-14|
    FR3043331B1|2019-11-22|
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    法律状态:
    2016-10-28| PLFP| Fee payment|Year of fee payment: 2 |
    2017-05-12| PLSC| Publication of the preliminary search report|Effective date: 20170512 |
    2017-10-26| PLFP| Fee payment|Year of fee payment: 3 |
    2018-10-26| PLFP| Fee payment|Year of fee payment: 4 |
    2019-11-25| PLFP| Fee payment|Year of fee payment: 5 |
    2020-11-25| PLFP| Fee payment|Year of fee payment: 6 |
    2021-11-24| PLFP| Fee payment|Year of fee payment: 7 |
    优先权:
    申请号 | 申请日 | 专利标题
    FR1560666|2015-11-06|
    FR1560666A|FR3043331B1|2015-11-06|2015-11-06|URBAN CARBON WELL|FR1560666A| FR3043331B1|2015-11-06|2015-11-06|URBAN CARBON WELL|
    CN201680071363.1A| CN109069988A|2015-11-06|2016-11-04|For controlling the process of air cleaning system|
    JP2018541557A| JP6843873B2|2015-11-06|2016-11-04|The process of controlling the air purification system|
    US15/771,075| US10807037B2|2015-11-06|2016-11-04|Process for controlling air purification systems|
    PCT/EP2016/076708| WO2017077061A1|2015-11-06|2016-11-04|Process for controlling air purification systems|
    EP16791582.6A| EP3370852A1|2015-11-06|2016-11-04|Process for controlling air purification systems|
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