Patent Application
20210388298
The present invention relates to the biotechnological sector and, in particular, concerns an apparatus and method for optimizing the growth processes of photosynthetic organisms such as for example, microalgae and cyanobacteria.
Specifically, the present invention relates to an apparatus and method for the culture of photosynthetic organisms by means of the use of an optical system of artificial lighting.
The most advantageous implementation—that is to say with the best efficiency—of the present invention provides for the combination of the optical system of artificial lighting according to the present invention and the photobioreactor devised by some of the present inventors and described in the European Patent no. EP 2 830 413 B1.
The preferred fields of application of the present invention are those typical of biotechnologies, ranging from nutraceuticals to cosmetics, from the production of biofuels to the fixation of greenhouse gases.
Traditional technologies for the implementation of processes for the growth of photosynthetic organism involve the use of natural or artificial light.
An example of a technical solution with natural light is described in European Patent no. EP 2 830 413 B1.
The main drawback of the aforementioned solution lies in the fact that the system completely depends on natural light, so that neither intensity nor spectrum can be modified, moreover the photosynthetic activity is confined to the day-time phase only, limiting the overall efficiency of the system.
In the case of artificial light, the light source is normally constituted by fluorescent tubes; examples of this technical solution are described in United States Patent applications no. US 2011/312062 A1 and no. US 2014/073035 A1.
The main drawback of the aforementioned solution lies in the fact that the light incidence is not uniform on the surface of exposure to the photosynthetic organisms under culture from the point of view of the light spectrum (quality of the radiated light) and from the point of view of the irradiated power (quantity of light irradiated), as well as in terms of frequency; in other words, the fluorescent tubes are only able to emit constant light spectrum and frequency, while the power is closely linked to the operating hours and therefore degrades over time.
Consequently, since it is not possible to vary in real-time the composition of the light spectrum, the light power and the power-up frequency, it is not possible to manage the apparatus based on the real needs of the process of growth of photosynthetic organisms.
In particular, photosynthetic organisms, such as microalgae, for example, have specific light absorption requirements and are also dependent on different growth phases.
Thus far, the need to have an apparatus capable of managing both power and light spectrum in a variable and precise way, guaranteeing their uniformity and constancy over time in terms of incident and lighting light spectrum, to production needs varying from time to time is therefore unsatisfied.
The Applicant, with the apparatus and method thereof for the culture of photosynthetic organisms according to the present invention, intends to remedy this lack.
It is an object of the present invention to overcome the drawbacks of the known art linked to the impossibility of realizing processes for the growth of photosynthetic organism based on specific requirements.
In particular, the present invention intends to solve the problem of how to manage both the power and the light spectrum in a variable and precise way, guaranteeing their uniformity in terms of incident and lighting light spectrum, in order to meet the production needs varying from time to time.
More particularly, the present invention intends to solve the problem of how to manage both the power and the light spectrum in a variable and precise way, guaranteeing ideal growth conditions based on the plant species involved.
Such objectives are achieved with the apparatus and method thereof for the culture of photosynthetic organisms according to the present invention which, advantageously and thanks to the presence of an optical device, allows the operating conditions to be varied and adjusted according to the specific requirements.
Advantageously, the present invention allows
Specifically, the aforementioned and other objects and advantages of the invention, as will appear from the following description, are achieved with an apparatus for the culture of photosynthetic organisms according to claim 1.
Preferred embodiments and variants of the apparatus according to the present invention form the subject matter of the dependent claims 2 to 7.
Another aspect of the present invention relates to a method for the culture of photosynthetic organisms which uses the apparatus according to the present invention and forms the object of claim 8.
Preferred embodiments and variants of the method according to the present invention form the subject matter of the dependent claims 9 to 13.
It is understood that all the appended claims form an integral part of the present description and that each of the technical features claimed therein is possibly independent and can be used autonomously with respect to the other aspects of the invention.
It will be immediately apparent that countless modifications could be made to what described (for example, regarding shape, sizes, arrangements and parts with equivalent functionalities and usable microorganisms) without departing from the scope of protection of the invention as claimed in the appended claims.
Further advantageous features will become more apparent from the following description of preferred, but not exclusive embodiments provided purely by way of example and not of limitation.
The present invention will be described hereinafter by way of some preferred embodiments, provided by way of example and not of limitation, with reference to the accompanying drawings. These drawings illustrate different aspects and examples of the present invention and, where appropriate, similar structures, components, materials and/or elements in different figures are denoted by similar reference numerals.
While the invention is susceptible to various modifications and alternative constructions, some preferred embodiments are shown in the drawings and will be described in detail hereinbelow.
It should be understood, however, that there is no intention to limit the invention to the specific embodiments illustrated, but, on the contrary, the invention is intended to cover all modifications, alternative constructions, and equivalents that fall within the scope of the invention as defined in the claims.
In the following description, therefore, the use of “for example”, “etc.”, “or” indicates not exclusive alternatives without any limitation, unless otherwise indicated; the use of “also” means “including, but not limited to” unless otherwise indicated; the use of “includes/comprises” means “includes/comprises but not limited to” unless otherwise indicated.
The apparatus and method of the present invention are based on the innovative concept of using, instead of the usual incandescent and/or fluorescent natural or artificial light sources, an optical device for artificial lighting comprising an optical guide, a plurality of LEDs and a regulation and control panel.
Actually, the Inventors have observed and discovered that the aforesaid optical device for artificial lighting makes it possible to carry out processes of growth and conditioning of photosynthetic organisms based on specific needs.
In the present description, the term “panel” means a planar panel made of transparent material that constitutes a pressure circuit, preferably a coil, with an input point and an output point.
In the present description, the term “photobioreactor” means an apparatus consisting of one or more panels, connection and control hydraulic devices, liquid handling systems, a degassing apparatus and a lighting apparatus as well as a series of control sensors.
In the present description, the term “photosynthetic organisms” means eukaryotic and prokaryotic organisms having microscopic dimensions, with phototrophic (obtaining energy from light) and in general autotrophic metabolism (using inorganic carbon as a carbon source); the photosynthetic microorganisms according to the present definition are generally found, but not exclusively, in an aquatic environment.
The system can be used not only in conditions of autotrophic, but also mixotrophic and heterotrophic growth, for example by carrying out growth in the absence of light and possibly using the optical illuminator as a source for photostimulation aimed at the biosynthesis of metabolites. In the present description, the term “illuminator” means a system consisting of a series of LEDs, an optical guide used to direct and diffuse the emission, and an electronic control unit for managing the process parameters.
With reference to
at least one device for artificial lighting 10, 10′ of said photosynthetic microorganisms 50, 50′,
wherein said at least one device for artificial lighting 10, 10′ is an optical device and comprises
Referring to
With particular reference to the general embodiment of the apparatus according to the present invention, illustrated in
With particular reference to the preferred embodiment of the apparatus according to the present invention, illustrated in
Preferably the at least one mono-emissive 10 or bi-emissive optical device 10′ for artificial lighting is placed in direct contact with said at least first panel 20, 20′.
Preferably the at least one regulation and control panel 4, 4′ comprises
The apparatus 100, 100′ according to the present invention allows the spectrum to range between 200 and 900 nm and the light intensity to range between 1% and 100%, the spectrum and the light intensity dynamically varying according to the operating specifications of the device for artificial lighting 10, 10′.
Reference is now made to
To determine these isolines, a panel having a base of 1,500 mm and a height of 1,000 mm has been considered; the photosynthetic lighting values refer to the incident light on the photobioreactor panel, with a distance between the illuminator and the panel varying from the direct contact up to about 15 mm.
As can be seen from the image, the uniformity of incidence of light is greater than 80% and such lighting has been simulated considering an electric absorption of the illuminator of about 200 W.
Referring to
In particular, the apparatus 100″ comprises:
According to the present invention, the photobioreactor can accommodate all aquatic photosynthetic microorganisms for their growth; by way of example, but not limited to, the aquatic photosynthetic microorganisms comprise green algae (Chlorophyta, for example, Chlorella sp.), diatoms (Chrysophyta), dinoflagellates (Dinophyta), red microalgae (Rhodophyta, for example, Cyanidium sp.), protists (for example, Euglena sp.) and photosynthetic bacteria (cyanobacteria, for example, Spirulina sp.).
The subject invention is characterized by an emitted radiant light power of about 300 μmol/s equally divided between the two emitting surfaces; it is specified that it can intervene in substitution/compensation of natural light in hybrid systems.
The invention is supplied with a voltage of 220-240 V-50 Hz, for maximum absorption of 500 W.
The LED technology used guarantees an expected life-time of about 50,000 hours.
To improve the energy efficiency of the system, it is possible to optimize the optical guide and the thermal management of the variable-spectrum LED illuminators.
Furthermore, with reference to
Preferably, the at least one regulation and control panel 4, 4′ is operated so as to vary the spectrum between 200 and 900 nm and the light intensity between 1% and 100%, the spectrum and the light intensity dynamically varying according to the operating specifications of the device for artificial lighting 10, 10′.
Preferably, photosynthetic microorganisms are selected from green algae (Chlorophyta), diatoms (Chrysophyta), dinoflagellates (Dinophyta), red microalgae (Rhodophyta), protists, and photosynthetic bacteria such as cyanobacteria.
More preferably, photosynthetic microorganisms are selected from Chlorella sp., Cyanidium sp., Euglena sp. and Spirulina sp.
Preferably, the predetermined time is equal to or greater than two days and the desired level of growth of said photosynthetic microorganisms 50, 50′ is equal to or greater than a corresponding growth rate p equal to 0.01 g/L/day.
According to the present invention the apparatus 100, 100′ is also applicable to a panel 10, 10′ operating at ambient pressure.
The most advantageous implementation—that is to say with the best efficiency—of the present invention provides, however, for the combination of the optical system of artificial lighting according to the present invention and the photobioreactor devised by some of the same inventors and described in the European Patent no. EP 2 830 413 B1, that is to say with panel 10, 10′ which operates under pressure.
More precisely, the present invention allows implementing the growth efficiency of photosynthetic microorganisms within a hydraulic circuit under pressure, artificially illuminated under controlled conditions according to the European Patent no. EP 2 830 413 B1.
Specifically, the present invention allows to provide a compact structure capable of receiving two under-pressure alveolar panels for the growth of photosynthetic microorganisms, interposing a panel of plastic material therebetween, i.e. the optical guide, suitable for the uniform diffusion of both the light spectrum and the light power emitted by different LED illuminators orthogonally positioned with respect to it; the LEDs that constitute the illuminators are able to generate light with different wavelengths of various intensity and varying frequency, allowing to cover the specific process needs of the photosynthetic micro-organism considered.
The combination of the present invention and the photobioreactor described in European Patent no. EP 2 830 413 B1 also comprises:
The combination of the present invention and the photobioreactor described in European Patent no. EP 2 830 413 B1 improves performances in terms of compactness, versatility (intended as a modification of growth and conditioning parameters), growth rate, nutrient bio-fixation and energy efficiency of the system compared to an incandescent or fluorescent lighting system.
In particular, the aforementioned combination allows to significantly reduce the overall dimensions of the panels which constitute the single module of a planar photobioreactor since between the two panels, which constitute the base unit, the required space is only 1.5 cm instead of 7-10 cm required by the footprint of a normal fluorescent tube illuminator.
Moreover, in this way, the final system results optimally integrated, having a more compact shape, significantly reducing the area occupied per unit of volume. It also increases the ease of plant handling/maintenance and versatility, since the modules can be placed side by side or superimposed on one another, making stacks having a growing capacity of the biomass process according to production needs.
A correct exposure to light allows photosynthetic microorganisms to perform CO2 bio-fixation processes optimally, making this technology a valuable system for the mitigation of this important greenhouse gas.
The increase in light emission efficiency through the subject invention immediately affects the managing costs of the system, keeping investment costs in the same order of magnitude when compared with more traditional products.
Thanks to the possibility of managing the control logic, which allows to set case-specific light parameters to optimize the growth of photosynthetic microorganisms and to vary them over time, the aforementioned combination guarantees high versatility features and is suitable for autotrophic, mixotrophic and heterotrophic growth, even in conditions that have been prohibitive or never hypothesized to date.
An implementation of the aforementioned combination will constitute the raising of the IP sealing level from the current IP 40 to IP 68.
The invention is described below in greater detail with reference to the following Examples, which are to be construed as purely illustrative but without limitation of the present invention.
In particular, examples of embodiments with various types of photosynthetic organisms are described, specifying for each type of organism the configuration and operation of the optical guide.
For the present example, a batch culture of a photosynthetic micro-organism, in particular, a green microalga, for example, Chlorella sp., has been considered. Growth has been carried out in totally autotrophic conditions aimed at the bio-fixation of carbon dioxide.
The batch/autotrophic cultivation of microalgae requires an aqueous growth solution that includes all inorganic minerals and the inlet of a gas flow containing a smaller or larger fraction of carbon dioxide needed to meet the needs for the microalgae replication and growth. Moreover, the initial start of the cultivation of the photobioreactor object of the patent involves the use of a minimum quantity of starting biomass (inoculum), so that the initial concentration of the biomass has an optical density (OD)>0.08 Abs at 680 nm.
Based on the premises given above, the conduct of such cultivation involves the following steps:
Step 1—Preparation of the Microalgal Biomass for the Photobioreactor Inoculum
The preparation of the initial inoculum can take place in photobioreactors on a laboratory scale (0.01-20 L). The starting microalga can be taken from an agar growth medium (the maintenance type preferred at long-term or in case of purchase of the species used in international organisms banks). The initial biomass can also be taken from a previously prepared aqueous solution. The laboratory-scale photobioreactor, the aqueous growth solutions, the measuring apparatuses in contact with the growth solution and the gas inlet apparatuses must be properly sterilized before their use. It is preferable to maintain the initial concentration (OD) of the microalga in the photobioreactor, at the time of the inoculation, greater than or equal to 0.100 Abs of Optical Density in order to reduce the initial lag phase in the cell growth. The parameter can be measured, for example, by reading on the spectrophotometer at 680 nm. For the described example, the growth of Chlorella was carried out using the “BBM medium” nutrient solution (Bold 1949, Bischoff& Bold 1963 and subsequent modifications) with controlled lighting with 10-500 μmol m2 s−1 Photosynthetic Photon Flow Density (PPFD), with or without day-night cycle.
An appropriate aeration of the solution by introducing a gas mixture containing a certain percentage of carbon dioxide (>0.04% at 100% v/v) is necessary to supply the microalgae with the gaseous nutrients necessary for the photosynthesis (carbon dioxide) and to remove photosynthetic waste gases (molecular oxygen). To ensure the adequate dissolution of the injected gases and a rapid diffusion among the microalgae in the growth solution, it is necessary to ensure a turbulent motion of the aqueous solution, for example by orbital agitation and/or a porous gas aerator and an airlifting column. The batch cell growth in the laboratory system is monitored at regular intervals by measuring the optical density (OD) as described above. The measured values, if shown on a graph as a function of the culture start time, allow drawing the characteristic cell growth sigmoid chart. At the end of the exponential growth phase, the accumulated biomass will be recovered and transferred to a new photobioreactor with a greater volume by an appropriate dilution (as described above) in a new volume of “BBM medium” growth solution. The cycles of refreshing and increasing the culture volume are repeated until the sufficient quantity of microalgal biomass (OD min>0.080 abs at 680 nm) is obtained to proceed with the inoculation in the photobioreactor covered by the patent.
Step 2. Preparation of the Photobioreactor for the Conduction of Microalgal Cultivation in Batch/Autotrophic Mode
Before proceeding with the inoculation of the microalgae in the photobioreactor object of the patent for the conduction of the cultivation of Chlorella in batch/autotrophic mode, it is necessary to carry out preliminary preparation operations.
It is necessary to sanitize the closed cultivation system by washing with a disinfectant solution suitable for contact with the photobioreactor construction materials. At the end of the sanitization, it is necessary to remove the residues of the sanitizing solution with repeated washing of the system.
At the time of the inoculation, the photobioreactor is filled with the nutrient solution (BBM medium) up to the desired operating level, with a minimum level of approximately ⅕ of the nominal volume of the photobioreactor. The nutrient solution contains all the inorganic compounds, in optimal quantities, to perform the growth of the microalgae in batch/autotrophic conditions until the stationary growth phase.
Step 3. Conduction of Microalgal Growth and Bio-fixation of Carbon Dioxide
The microalgal biomass obtained with the previous operations of preparation of the inoculum (Step 1) is introduced into the photobioreactor object of the patent and previously prepared at the start of cultivation, as described in Step 2. During the growth period, it is possible to vary the composition of the nutrient solution to meet specific nutritional needs of the microalga or to modify the growth conditions of the accumulated biomass through the introduction of new nutrients in the photobioreactor.
For the conduction of cultivation in batch/autotrophic conditions, it is necessary to control and monitor the chemical/physical parameters within the system which, in the example shown, reflect the growth requirements of the selected microalga, Chlorella.
Lighting:
Growth is carried out under controlled and modulated lighting according to the terms described in the patent. It is possible to adjust the intensity between 10-500 μmol m−2 s−1 Photosynthetic Photon Flow Density (PPFD), with or without day-night cycle.
Furthermore, it is possible to qualitatively modify the lighting spectrum according to the absorption requirements of the cultivated microalga and the desired growth and conditioning needs. In the case described, the growth is carried out using the lighting spectrum characteristic of the white LED with a continuous lighting cycle (24 h/24 h) in order to keep the microalgae in the photosynthetic phase and obtain the continuous bio-fixation of the carbon dioxide injected into the system.
Flow of the Nutrient Solution:
The recirculation and handling system of the nutrient solution (hydraulic recirculation pump) is equipped with a speed regulation system. The speed of the nutrient solution recirculation system must be adjusted appropriately in a range that can vary from 5 to 20 L/min in order to guarantee the adequate frequency of exposure of the microalgae to light, the adequate mixing of nutrients and microalgae, and to ensure the adequate dissolution of the injected gases as well as their rapid diffusion among microalgae. The recirculation speed can be changed during the conduction of the cultivation based on the needs of growth and conditioning.
Gas Flow:
Depending on the conditions of growth or conditioning required, it is possible to proceed with mechanical (through run-off) or forced aeration, by introducing air or gas containing a certain portion of carbon dioxide (>0.01% at 100% v/v). The introduction of gas is necessary to supply the microalgae with the gaseous nutrients necessary for photosynthesis (carbon dioxide). The intake flow of gaseous nutrient must be effectively regulated to allow the effective dissolution of carbon dioxide and its bio-fixation in carbonaceous compounds by the photosynthetic activity of microalgae. The accurate calibration of the carbon dioxide flow has allowed reaching bio-fixation ratios >80% with the emission of gas composed at 99.999% by carbon dioxide.
On-Line Monitoring Parameters:
In order to optimize the cell growth rate (μ=g/L/d) and therefore the bio-fixation of carbon dioxide, the proposed example provides for the use of digital and analogue sensors to monitor the environmental parameters of the growth solution and the cell growth.
By way of example, but not exhaustively, the growth of Chlorella in a batch/autotrophic condition involves the monitoring of: pH, dissolved carbon dioxide to evaluate the speed of introduction, dissolution in the aqueous growth solution and the consumption rate (bio-fixation), dissolved molecular oxygen to monitor the photosynthetic activity of microalgae, temperature of the nutrient solution, intensity and spectrum of the light incident on the panel, optical density (abs at 680 nm). The optical density data, shown on a graph in relation to the time of conduction of the cultivation, allows following the characteristic sigmoid pattern of cell growth in a closed batch system of microalgae. The parameters recorded by the sensors are used as early diagnostic elements for the evaluation of the state of growth and vitality of the microalgal biomass.
Off-line Monitoring Parameters:
Dry Weight—Biomass Concentration
In order to monitor the change in biomass concentration during the conduction of batch cultivation, it is possible to evaluate the dry weight of the microalgal biomass. A known and homogeneous culture volume can be sampled at regular intervals. The cells isolated and washed from the nutrient solution residues are dried (105° C. for 3 hrs). The concentration data (g/L), shown on a graph in relation to the time of conduction of the cultivation, allows following the characteristic sigmoid pattern of cell growth in a closed batch system of microalgae. Due to the time taken to carry out the evaluation of the dry weight, this parameter is considered, in the example shown, a less rapid diagnostic element compared to the previous parameters for the state of the system. The evaluation of the biomass concentration in the exemplary experiment recorded initial biomass of 0.2 g/L and minimum final biomass (after eleven days of cultivation) of 3 g/L.
Released Gas Analysis—Bio-fixation Mass Balance
To realize the mass balance for the bio-fixation of the carbon dioxide injected into the photobioreactor, the proposed growth example of Chlorella includes gas analysis through a gas analyzer or gas-phase chromatography of the gases released by the system, net of the gas mass absorbed by the microalga to support its metabolic processes.
Variations in the Conduction of the Cultivation System
The example shown illustrates the cultivation system of the microalga Chlorella in batch conditions. However, the cultivation, not only for the purposes of bio-fixation of carbon dioxide, can be carried out in semi-continuous (fed-batch) or continuous mode following the cell growth by means of a spectrophotometer, appropriately calculating the cell growth rate (μ=g/L/d) and preparing the necessary biomass discharges and the necessary additions of nutrient solution.
Step 4. Collection of the Biomass Produced
The biomass produced in the closed growth system of the photobioreactor object of the patent can be collected at the end of the cultivation in batch condition or at periodic intervals in fed-batch and continuous mode. The collection techniques, by way of example and not exhaustively, include:
The biomass collected with the above-described exemplary methods does not undergo significant alterations in the chemical composition and may be destined to subsequent use.
For the present example, a batch culture of a photosynthetic micro-organism, in particular a photosynthetic cyanobacterium, for example, Spirulina sp., has been considered. Growth was carried out in totally autotrophic conditions aimed at the production of biomass and photostimulation for the accumulation of phycocyanin, a high added-value photosynthetic pigment.
The batch/autotrophic cultivation of the cyanobacterium requires an aqueous growth solution that includes all inorganic minerals and the injection of a gas flow containing a smaller or larger fraction of carbon dioxide needed to meet the nutrition needs for the replication and growth. Moreover, the initial start of the cultivation of the photobioreactor object of the patent involves the use of a minimum quantity of starting biomass (inoculum), so that the initial concentration of the biomass has an optical density >0.08 OD at 680 nm.
Based on the premises given above, the conduct of such cultivation involves the following steps:
Step 1—Preparation of the Biomass for the Photobioreactor Inoculum
The present step follows the operations of Example 1, with minor adaptations for the use of the cyanobacterium under examination. In particular, the Spirulina-Medium nutrient solution (modified by Aiba, S. & Ogawa, T. 1977) was used for the cultivation of Spirulina.
Step 2. Preparation of the Photobioreactor for the Conduction in Batch/Autotrophic Mode of Cultivation
The preparation step of the photobioreactor for the production of Spirulina biomass follows the procedures described in Example 1, except the medium used for the growth of cyanobacterium, which in this case is “Spirulina-Medium”.
Step 3. Conduction of Cyanobacterium Growth and Photostimulation of Phycocyanin Accumulation
The cyanobacterium biomass obtained with the previous operations of preparation of the inoculum (Step 1) is introduced into the photobioreactor object of the patent and prepared at the start of cultivation, as described in Step 2. During the growth period, it is possible to vary the composition of the nutrient solution to meet specific nutritional needs of the cyanobacterium or to modify the growth conditions of the accumulated biomass through the introduction of new nutrients into the photobioreactor.
For the conduction of cultivation in batch/autotrophic conditions, it is necessary to control and monitor the chemical/physical parameters within the system which, in the example shown, reflect the growth needs of the selected cyanobacterium, Spirulina.
Lighting:
Growth is carried out under controlled and modulated lighting according to the terms described in the patent. It is possible to adjust the intensity between 10-500 mol m−2 s−1 Photosynthetic Photon Flow Density (PPFD), with or without day-night cycle.
Furthermore, it is possible to qualitatively modify the lighting spectrum according to the absorption requirements of the cultivated alga and the desired growth and conditioning needs. In the case described, the growth is carried out using the lighting spectrum characteristic of the WHITE LED with a continuous lighting cycle (24 h/24 h) in order to maximize the biomass accumulation speed in the photobioreactor and reach the final step of exponential growth in less time. At the end of the exponential growth step, the lighting spectrum of the photobioreactor is modified qualitatively by exposing the cyanobacterium to the light lengths of the area corresponding to the red and deep red (640-800 nm) of the visible light spectrum. The conditioning applied to the cyanobacterium induces photostimulation of the phycocyanin accumulation as a photosynthetic pigment until the stationary phase of growth characteristic of the sigmoid curve is reached.
Flow of the Nutrient Solution:
The recirculation and handling system of the nutrient solution (hydraulic recirculation pump) is equipped with a speed regulation system. The speed of the nutrient solution recirculation system must be adjusted appropriately in a range that can vary from 5 to 20 L/min in order to guarantee the adequate frequency of exposure of the cyanobacteria, in a way similar to Example 1. The recirculation speed can be changed during the conduction of the cultivation based on the needs of growth and conditioning.
Gas Flow:
Depending on the conditions of growth or conditioning required, it is possible to proceed with mechanical (through run-off) or forced aeration, by introducing air or gas containing a certain portion of carbon dioxide (>0.01% at 100% v/v). The introduction is necessary to supply the cyanobacterium with the gaseous nutrients necessary for photosynthesis (carbon dioxide). The inflow of gaseous nutrients must be regulated and positioned effectively to allow the effective dissolution of carbon dioxide, minimizing gas consumption, but ensuring the minimum requirement for optimal growth of the microorganism.
On-Line Monitoring Parameters:
In order to optimize the cell growth rate (p=g/L/d), the proposed example provides for the use of digital and analogue sensors to monitor the environmental parameters of the growth solution and the cell growth similarly to Example 1.
Off-line Monitoring Parameters:
Dry Weight—Biomass Concentration
In order to monitor the change in biomass concentration during the conduction of batch cultivation, it is possible to evaluate the dry weight of the microalgal biomass similarly to Example 1. The evaluation of the biomass concentration in the exemplary experiment recorded initial biomass of 0.1 g/L and minimum final biomass (after eleven days of cultivation) of 5.3 g/L.
Step 4. Collection of the Biomass Produced
The biomass produced in the closed growth system of the photobioreactor object of the patent can be isolated and collected at the end of the cultivation in batch condition, at periodic intervals in fed-batch and continuous mode for the continuous mode. The collected biomass, with a high phycocyanin content, can be used for subsequent processing. The collection techniques, by way of example and not exhaustively, are shown in Example 1.
To demonstrate the effectiveness of the present invention, experimental tests have been carried out and the data specified below have been collected; these data allow to compare the effectiveness of the present invention with respect to the known solutions, in particular with respect to the invention of the European Patent no. EP 2 830 413 B1.
In particular, given the same algal species, comparative data are shown below between fluorescent light with neon and LED lighting, energy consumption savings, higher productivity/lower growth time depending on the variation in the quality/quantity of the light.
The growth of Tetradesmus obliquus (Turpin) (for example, Scenedesmus obliquus (Turpin) Kutzing) in a planar photobioreactor, which refers to the invention of the European Patent no. EP 2 830 413 B1, was compared with the growth of the same green microalga in a photobioreactor with LED lighting object of the present invention, maintaining the same conditions: composition of the culture medium, pH, temperature, day-night lighting cycle, CO2 supply, flow. In order to obtain an objective comparison between the two cultivation systems, the light intensity (expressed as μmol/m−2/s−1 Photosynthetic Photon Flow Density) in the two growth conditions was kept equal for the entire conduction of experiments.
The results obtained, expressed as “Growth Rate” (g/L/day) showed an average value of 0.02 g/L/day in the case of neon lighting in the photobioreactor according to the invention of European Patent no. EP 2 830 413 B1 and an average value equal to 0.05 g/L/day in the photobioreactor with LED lighting, object of the present invention.
From this, it can be seen that, under the same growing conditions, the reproduction speed is more than twice as high.
As mentioned above, the present invention has been compared with the invention of the European Patent no. EP 2 830 413 B1, with the same algal species, in terms of power consumption savings and greater productivity/less growth time depending on the variation of the quality/quantity of the light, which were determined as described below.
Measurement of Power Consumption Savings
The power consumed by the illuminators was measured by using an amperometric clamp on two systems operating under the following conditions:
The comparison between the two systems resulted in a power absorption which for the three-neon tubes system is equal to 174 W, while for the LED system is equal to 64 W, for the five-neon tubes system is equal to 290 W, while for the LED system is equal to 106 W. In both cases, savings amount to a reduction in power consumption of over 60%.
Measurement of Productivity According to the Variation of the Quantity of Light
From the tests carried out for the evaluation of power savings reported above, the parameters of growth and productivity have also been inferred. The comparison is reported under equal conditions of the two lighting systems in the 40 PAR configuration. In this case, with neon lighting, an increase of 43% in biomass in 5 days is obtained while using the LED lighting system, the increase in biomass over the same period is equal to 66%. The comparison is carried out only on white light, as traditional neon systems do not allow to influence the composition of the spectrum.
The results of the comparison are summarized in the Table below.
The aforementioned Table shows that, under the same conditions in the most economical energy-saving scenario, the LED lighting system consumes about 60% less than the traditional lighting system. Reduction that does not result into a decrease in biomass production since, under the same growth conditions, the LED lighting system over 5 days of observation has a productivity of about 20% more than the traditional system.
It is, therefore, apparent that the technical solution according to the present invention is capable of achieving the stated and expected results.
As it can be deduced from the foregoing, the innovative technical solution described herein has the following advantageous features:
From the description above it is, therefore, apparent how the apparatus and method according to the present invention allow to achieve the intended objects.
Therefore, it is apparent to a person skilled in the art that it is possible to make modifications and further variants to the solution described with reference to the accompanying figures, without departing from the teaching of the present invention and the scope of protection, as defined by the appended claims.
| Number | Date | Country | Kind |
|---|---|---|---|
| 102018000010479 | Nov 2018 | IT | national |
This application is the national stage entry of International Application No. PCT/IB2019/059732, filed on Nov. 13, 2019, which is based upon and claims priority to Italian Patent Application No. 102018000010479, filed on Nov. 21, 2018, the entire contents of which are incorporated herein by reference.
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/IB2019/059732 | 11/13/2019 | WO | 00 |
