WO2006120278A1 - Method of fixing carbon dioxide using a culture of cyanobacteria - Google Patents
Method of fixing carbon dioxide using a culture of cyanobacteria Download PDFInfo
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- WO2006120278A1 WO2006120278A1 PCT/ES2006/070056 ES2006070056W WO2006120278A1 WO 2006120278 A1 WO2006120278 A1 WO 2006120278A1 ES 2006070056 W ES2006070056 W ES 2006070056W WO 2006120278 A1 WO2006120278 A1 WO 2006120278A1
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- fixing
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- polysaccharide
- microorganism
- fixation
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- 238000000034 method Methods 0.000 title claims abstract description 47
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 title abstract description 46
- 229910002092 carbon dioxide Inorganic materials 0.000 title abstract description 23
- 239000001569 carbon dioxide Substances 0.000 title abstract description 23
- 241000192700 Cyanobacteria Species 0.000 title description 8
- 229920002444 Exopolysaccharide Polymers 0.000 claims abstract description 39
- 238000004519 manufacturing process Methods 0.000 claims abstract description 16
- 241001464430 Cyanobacterium Species 0.000 claims abstract description 10
- 241000192542 Anabaena Species 0.000 claims abstract description 9
- 239000002551 biofuel Substances 0.000 claims abstract description 8
- 239000002803 fossil fuel Substances 0.000 claims abstract description 6
- 244000005700 microbiome Species 0.000 claims description 29
- 229920001282 polysaccharide Polymers 0.000 claims description 27
- 239000005017 polysaccharide Substances 0.000 claims description 27
- 230000000243 photosynthetic effect Effects 0.000 claims description 18
- 239000002028 Biomass Substances 0.000 claims description 15
- 230000008569 process Effects 0.000 claims description 14
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 12
- 229910052799 carbon Inorganic materials 0.000 claims description 12
- 241000192531 Anabaena sp. Species 0.000 claims description 10
- 239000002609 medium Substances 0.000 claims description 10
- BVKZGUZCCUSVTD-UHFFFAOYSA-M Bicarbonate Chemical compound OC([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-M 0.000 claims description 9
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 claims description 9
- 239000001963 growth medium Substances 0.000 claims description 5
- 239000007788 liquid Substances 0.000 claims description 5
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- 241000196324 Embryophyta Species 0.000 description 10
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- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
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- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 description 1
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- 229920001586 anionic polysaccharide Polymers 0.000 description 1
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- ATNHDLDRLWWWCB-AENOIHSZSA-M chlorophyll a Chemical compound C1([C@@H](C(=O)OC)C(=O)C2=C3C)=C2N2C3=CC(C(CC)=C3C)=[N+]4C3=CC3=C(C=C)C(C)=C5N3[Mg-2]42[N+]2=C1[C@@H](CCC(=O)OC\C=C(/C)CCC[C@H](C)CCC[C@H](C)CCCC(C)C)[C@H](C)C2=C5 ATNHDLDRLWWWCB-AENOIHSZSA-M 0.000 description 1
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- 229910021645 metal ion Inorganic materials 0.000 description 1
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Classifications
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
- C12P19/00—Preparation of compounds containing saccharide radicals
- C12P19/04—Polysaccharides, i.e. compounds containing more than five saccharide radicals attached to each other by glycosidic bonds
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/46—Removing components of defined structure
- B01D53/62—Carbon oxides
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/84—Biological processes
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M43/00—Combinations of bioreactors or fermenters with other apparatus
- C12M43/04—Bioreactors or fermenters combined with combustion devices or plants, e.g. for carbon dioxide removal
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/50—Carbon oxides
- B01D2257/504—Carbon dioxide
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02C—CAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
- Y02C20/00—Capture or disposal of greenhouse gases
- Y02C20/40—Capture or disposal of greenhouse gases of CO2
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/151—Reduction of greenhouse gas [GHG] emissions, e.g. CO2
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/59—Biological synthesis; Biological purification
Definitions
- the invention is therefore related to the use of said method to reduce or eliminate CO 2 emissions produced by power generation plants and a variety of industrial processes, but also, on the other hand, the use of their products As a biofuel it is possible to reduce the consumption of fossil fuels.
- Said system consists of a solar light collection module consisting of tubes of transparent material (rigid plexiglass) of 24 mm internal diameter and 30 mm external diameter and a total length of 90 m, located horizontally in parallel and connected to each other by half of pieces in the form of "u" of the same material, with a photosynthetically active surface of 2.2 m 2 and 55 I of useful volume. Two rubber balls with a diameter slightly smaller than the inside diameter of the tubes circulate to prevent the deposit of cells in their walls.
- These tubes are submerged in water, which acts as a thermostatting element of the crop, in a bath of dimensions 1, 8x6.0x0.15 m, equipped with a closed circulation circuit with heating and cooling elements.
- the cell suspension is stirred and circulated through the tubes by the delivery of sterile air under pressure generated by a compressor (air-lift).
- the tubular system ends in a 52 cm high by 26 cm external diameter cylinder, located 2.8 m high from the horizontal of the reactor.
- gas outlet protected by a 0.22 ⁇ m filter
- input for rapid filling of the reactor fresh medium input to operate in continuous culture and level sensor.
- pH and temperature probes In the lower part of the cylinder are also the pH and temperature probes. These probes are connected to a control unit.
- the pH value is maintained between 8.0 and 8.5 by means of the injection of CO2 through a solenoid valve regulated by a pH controller.
- the CO2 is injected into the horizontal zone of the return tube of the cell suspension towards the light collection module.
- the photosynthetic consumption of CO 2 by the cells of the cyanobacteria causes an increase in the pH of the medium, which, upon exceeding the value of 8.5, triggers the injection of a stream of CO 2 pure gas, with which the medium is acidified, stopping The injection of CO 2 once the pH 8.0 is recovered.
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- Engineering & Computer Science (AREA)
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- Health & Medical Sciences (AREA)
- Biomedical Technology (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Wood Science & Technology (AREA)
- Zoology (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Analytical Chemistry (AREA)
- Bioinformatics & Cheminformatics (AREA)
- Biotechnology (AREA)
- Microbiology (AREA)
- Biochemistry (AREA)
- General Engineering & Computer Science (AREA)
- General Health & Medical Sciences (AREA)
- Genetics & Genomics (AREA)
- Sustainable Development (AREA)
- Combustion & Propulsion (AREA)
- Molecular Biology (AREA)
- Preparation Of Compounds By Using Micro-Organisms (AREA)
- Apparatus Associated With Microorganisms And Enzymes (AREA)
Abstract
The invention relates to a method of fixing carbon dioxide (CO2) by cultivating any halotolerant nitrogen-fixing cyanobacterium which can produce an exopolysaccharide that is excreted to the medium. The inventive method can be used to reduce or eliminate CO2 emissions from industrial processes, such as from electrical power plants. The invention also relates to the biofuel use of an exopolysaccharide that is produced from the cultivation of cyanobacterium Anabaena which has a high calorific value. By using the aforementioned exopolysaccharide as a biofuel, it is possible to reduce fossil fuel consumption in industrial processes that use same.
Description
TÍTULOTITLE
PROCEDIMIENTO PARA FIJAR DIÓXIDO DE CARBONO MEDIANTE LAPROCEDURE FOR FIXING CARBON DIOXIDE THROUGH THE
UTILIZACIÓN DE UN CULTIVO DE CIANOBACTERIASUSE OF A CIANOBACTERIA CULTURE
SECTOR DE LA TÉCNICASECTOR OF THE TECHNIQUE
Medio Ambiente. El objeto de Ia presente invención es un proceso para fijar y eliminar dióxido de carbono (CO2), proveniente de emisiones de procesos industriales, mediante el cultivo de una cianobacteria fijadora de nitrógeno, halotolerante y capaz de producir un exopolisacárido (EPS).Environment. The object of the present invention is a process for fixing and eliminating carbon dioxide (CO2), from industrial process emissions, by cultivating a nitrogen-fixing cyanobacterium, halotolerant and capable of producing an exopolysaccharide (EPS).
ESTADO DE LA TÉCNICASTATE OF THE TECHNIQUE
El dióxido de carbono o anhídrido carbónico (CO2), a pesar de ser un gas minoritario en Ia atmósfera terrestre (0,03%, v/v), constituye uno de sus componentes más importantes, ya que es sustrato en Ia fotosíntesis, por una parte, y principal producto de Ia respiración de los seres vivos y de Ia combustión de los productos energéticos por otra. Actualmente se registra un aumento del nivel de CO2 en Ia atmósfera, del que se hace responsable al incremento en Ia utilización de combustibles fósiles (carbón, petróleo, gas natural), que puede conllevar un sobrecalentamiento de Ia superficie terrestre (efecto invernadero). Un importante problema que afecta al desarrollo económico de muchos países es su elevado nivel de emisiones de CO2, Io que puede situarlos en una precaria situación en un futuro mercado de emisiones.Carbon dioxide or carbon dioxide (CO 2 ), despite being a minor gas in the Earth's atmosphere (0.03%, v / v), is one of its most important components, since it is a substrate in photosynthesis, on the one hand, and the main product of the respiration of living beings and the combustion of energy products on the other. Currently there is an increase in the level of CO 2 in the atmosphere, which is responsible for the increase in the use of fossil fuels (coal, oil, natural gas), which can lead to overheating of the earth's surface (greenhouse effect). A major problem affecting the economic development of many countries is the high level of CO2 emissions, which can put them in a precarious situation in the future emissions market.
Para resolver estos problemas se hace necesario desarrollar e implantar nuevas tecnologías que permitan generar energía con menores niveles de emisión de CO2, así como otras que permitan eliminar CO2, reduciendo su nivel en los gases de escape generados industrialmente. El primer aspecto supone una sustitución tecnológica difícil de abordar a corto plazo por muchos países.To solve these problems it becomes necessary to develop and deploy new technologies to generate energy with lower CO2 emission and other needed to eliminate CO 2, reducing its level in the exhaust gases generated industrially. The first aspect involves a technological substitution difficult to address in the short term by many countries.
Respecto al segundo aspecto, se están llevando a cabo diversos estudios que consideran desde Ia fijación del CO2 por masas forestales a su retención en el mar, bolsas de gas o suelos petrocálcicos, haciéndose énfasis especial en diversas alternativas de aprovechamiento de Ia fijación fotosintética del CO2.
De hecho, entre las diferentes opciones basadas en favorecer los sumideros naturales de CO2, Ia fijación fotosintética de CO2 mediante el cultivo de microalgas y cianobacterias es, en principio, Ia alternativa más prometedora, ya que dichos microorganismos son los más efectivos fijadores de CO2 del planeta, con rendimientos más de cinco veces superiores a las plantaciones de maíz, constituyendo además uno de los grupos más versátiles de Ia biosfera. Asimismo, Ia naturaleza hidráulica de los cultivos facilita su manipulación, así como Ia instalación de los mismos contiguos a Ia propia fuente emisora de CO2, mientras que, en general, el resto de los propuestos sumideros naturales de carbono solo fijan CO2 del liberado a Ia atmósfera, constituyendo contaminación difusa.Regarding the second aspect, various studies are being carried out that consider from the fixation of CO 2 by forest masses to its retention in the sea, gas bags or petrocalcic soils, with special emphasis on various alternatives for taking advantage of the photosynthetic fixation of the CO 2 . In fact, among the different options based on favoring natural CO 2 sinks, the photosynthetic fixation of CO 2 through the cultivation of microalgae and cyanobacteria is, in principle, the most promising alternative, since these microorganisms are the most effective fixative agents of CO2 of the planet, with yields more than five times higher than corn plantations, also constituting one of the most versatile groups in the biosphere. Likewise, the nature hydraulic crop facilitates handling and the installation thereof contiguous to Ia own radio source of CO 2, whereas, in general, other natural sinks proposed only carbon CO2 fixation of the released Ia atmosphere, constituting diffuse pollution.
El cultivo de microorganismos fotosintéticos utiliza el CO2 como fuente de carbono, convirtiéndolo en carbono orgánico fijado en forma de los diferentes compuestos orgánicos que constituyen Ia biomasa, así como otros productos fotosintéticos que pueden liberar las células, tales como los polisacáridos. Una posible opción para el aprovechamiento de Ia biomasa y/u otros productos fotosintéticos generados mediante Ia fijación de CO2, es su aprovechamiento como fuente de energía, al ser materiales con considerable contenido energético o calor de combustión. Esta reutilización como combustible de los productos fotosintéticos supone un reciclaje de carbono y conlleva una paralela reducción en el consumo de combustibles fósiles.The culture of photosynthetic microorganisms uses CO2 as a source of carbon, converting it into organic carbon fixed in the form of the different organic compounds that constitute the biomass, as well as other photosynthetic products that can release cells, such as polysaccharides. A possible option for the use of biomass and / or other photosynthetic products generated through CO2 fixation, is its use as a source of energy, being materials with considerable energy content or heat of combustion. This reuse as a fuel for photosynthetic products involves carbon recycling and leads to a parallel reduction in fossil fuel consumption.
La eficiencia y el éxito de Ia utilización de cultivos de microorganismos fotosintéticos para Ia fijación de CO2 dependen en gran medida del microorganismo seleccionado (especie, cepa, etc.), así como del sistema de producción empleado y de Ia optimización de los parámetros de cultivo. Adicionalmente han de considerarse las propiedades de los productos fotosintéticos generados y las posibilidades de su posterior aprovechamiento. Las emisiones de CO2 a Ia atmósfera constituyen un problema global. Sería conveniente desarrollar un sistema que elimine o al menos reduzca las emisiones de CO2 en las propias fuentes emisoras del contaminante, de manera eficiente, barata, sencilla y versátil, consiguiendo altas tasas de fijación
de CO2, y generando al mismo tiempo productos fotosintéticos con aplicaciones de interés.The efficiency and success of the use of photosynthetic microorganism cultures for the fixation of CO 2 depend largely on the selected microorganism (species, strain, etc.), as well as the production system used and the optimization of the parameters of culture. Additionally, the properties of the generated photosynthetic products and the possibilities of their subsequent use must be considered. The emissions of CO 2 into the atmosphere constitute a global problem. It would be desirable to develop a system that eliminates or at least reduces the emissions of CO 2 emission sources of the pollutant own, efficiently, inexpensive, simple and versatile, achieving high rates of fixation of CO2, and at the same time generating photosynthetic products with applications of interest.
Utilizando el alga verde Chlorococcum littorale se ha conseguido fijar cerca de 1 g de CO2 por litro y día en recipientes de 20 I de capacidad (Kurano N, lkemoto H, Miyashita H, Hasegawa T, Hata H and Miyachi S (1995). Fixation and utilization of carbón dioxide by microalgal photosynthesis. Energy Convers. Management 36 (6-9), 689 -692). Con Ia tecnología que aquí se propone se puede conseguir valores de fijación de CO2 comprendidos entre 2 y 6 g CO2 por litro y día.Using the green algae Chlorococcum littorale it has been possible to fix about 1 g of CO 2 per liter and day in containers of 20 I capacity (Kurano N, lkemoto H, Miyashita H, Hasegawa T, Hata H and Miyachi S (1995). Fixation and utilization of carbon dioxide by microalgal photosynthesis. Energy Convers. Management 36 (6-9), 689-692). With the technology proposed here, CO 2 fixation values between 2 and 6 g CO2 per liter and day can be achieved.
La patente norteamericana WO0205932 "Photosynthetic carbón dioxide mitigation", utiliza cianobacterias termófilas (Cyanidium caldarium) inmovilizadas sobre membranas, empleando un sistema de energía híbrida para su iluminación (convierten Ia luz solar en electricidad mediante placas fotovoltaicas y suministran luz de 400-700 nm de longitud de onda a las células). El producto de fijación del CO2 es Ia biomasa, sin considerar Ia producción de otros compuestos. La biomasa producida debe ser retirada con asiduidad de las membranas mediante un complejo sistema de limpieza, Io que redunda negativamente en Ia economía y rendimiento del proceso, dificultando asimismo su escalado.US patent WO0205932 "Photosynthetic carbon dioxide mitigation" uses thermophilic cyanobacteria (Cyanidium caldarium) immobilized on membranes, using a hybrid energy system for lighting (converting sunlight into electricity using photovoltaic panels and supply 400-700 nm light wavelength to the cells). The fixation product of CO 2 is biomass, without considering the production of other compounds. The biomass produced must be regularly removed from the membranes through a complex cleaning system, which negatively results in the economy and performance of the process, making it difficult to scale.
En Ia presente invención, el principal producto de Ia fijación de CO2 es un polisacárido que las células excretan al medio. Dicho exopolisacárido (EPS) posee propiedades que Ie confieren interés práctico para una diversidad de aplicaciones industriales (Bender J, Rodríguez-Eaton S, Ekanemesang UM and Phillips P (1994). Characterization of metal-binding bioflocculants produced by the cyanobacterial component of mixed microbial mats. Appl Environ Microbiol 60, 2311-2315); De Philippis R and Vicenzini M (1998). Exocellular polysaccharides from cyanobacteria and their possible applications. FEMS Microbiology Reviews 22, 151-175; Flaibani A, Olsen Y and Painter TJ (1989). Polysaccharides in desert reclamation: Compositions of exocellular proteoglycan complexes produced by filamentous blue-green edaphic algae. Carbohydr Res 190, 235-248; Sutherland IW (1996). Extracellular
polysaccharides. En: Biotechnology, VCH, Weinheim (Rehm, HJ and Reed, G eds.) vol 6, 615-657). Este sistema utiliza directamente luz solar para el desarrollo de Ia fijación de CO2 y permite su fácil escalado.In the present invention, the main product of the fixation of CO 2 is a polysaccharide that the cells excrete in the medium. Said exopolysaccharide (EPS) possesses properties that confer practical interest for a variety of industrial applications (Bender J, Rodríguez-Eaton S, Ekanemesang UM and Phillips P (1994). Characterization of metal-binding bioflocculants produced by the cyanobacterial component of mixed microbial mats. Appl Environ Microbiol 60, 2311-2315); From Philippis R and Vicenzini M (1998). Exocellular polysaccharides from cyanobacteria and their possible applications. FEMS Microbiology Reviews 22, 151-175; Flaibani A, Olsen Y and Painter TJ (1989). Polysaccharides in desert reclamation: Compositions of exocellular proteoglycan complexes produced by filamentous blue-green edaphic algae. Carbohydr Res 190, 235-248; Sutherland IW (1996). Extracellular polysaccharides In: Biotechnology, VCH, Weinheim (Rehm, HJ and Reed, G eds.) Vol 6, 615-657). This system uses direct sunlight for developing the fixation of CO 2 and permits easy scaling.
BREVE DESCRIPCIÓN DE LA INVENCIÓNBRIEF DESCRIPTION OF THE INVENTION
Tal como se ha mencionado previamente, sería conveniente disponer de un procedimiento de fijación de CO2 capaz de reducir Ia concentración de este gas en Ia atmósfera, acoplado a Ia generación de un producto orgánico susceptible de aprovechamiento. La presente invención describe un procedimiento para fijar CO2 mediante Ia utilización de un cultivo de microorganismos fotosintéticos acoplado a Ia producción de un exopolisacárido, que posee considerable calor de combustión y otras propiedades que Ie confieren interés práctico.As previously mentioned, it would be convenient to have a CO 2 fixation procedure capable of reducing the concentration of this gas in the atmosphere, coupled with the generation of an organic product that can be used. The present invention describes a method for fixing CO 2 by means of the use of a culture of photosynthetic microorganisms coupled to the production of an exopolysaccharide, which has considerable heat of combustion and other properties that confer practical interest.
Por tanto, en un aspecto, Ia invención se relaciona con dicho procedimiento para fijar CO2 que comprende las siguientes etapas: a- cultivar un microorganismo fotosintético en un sistema adecuado. b- suministrar al cultivo CO2 u otra forma inorgánica de carbono derivada de él, tal como bicarbonato ( HCO3) y/o carbonato CCO3), a concentraciones elevadas, y c- recoger los productos de Ia fijación del CO2 y de otras formas de carbono inorgánico de él derivadas (bicarbonato, carbonato), generados por dicho cultivo.Therefore, in one aspect, the invention relates to said method for fixing CO 2 comprising the following steps: a- cultivating a photosynthetic microorganism in a suitable system. b- supply CO 2 or another inorganic form of carbon derived from it, such as bicarbonate (HCO 3 ) and / or CCO 3 carbonate), at high concentrations, and c- collect the products of CO 2 fixation and other forms of inorganic carbon derived from it (bicarbonate, carbonate), generated by said culture.
El microorganismo cultivado es una cianobacteria fijadora de N2, halotolerante, que fotosintetiza un exopolisacárido que excreta al medio. Esta cianobacteria puede ser cultivada en sistemas abiertos o cerrados. El suministro de CO2 (en concentraciones elevadas, y siempre superiores a las naturales atmosféricas) puede realizarse directamente en forma de gas o tras su solubilización en un líquido (como tal CO2, como bicarbonato o carbonato) que sería empleado como medio de cultivo. El CO2 en concentración elevada puede provenir de plantas de generación de electricidad, de cementeras o de plantas industriales que desarrollen procesos generadores de CO2.
Como uno de los productos fotosintéticos mayoritarios de Ia fijación de carbono inorgánico (CO2, bicarbonato, carbonato) mediante el cultivo de estas cianobacterias se obtiene un exopolisacárido (EPS) que se libera al medio.The cultured microorganism is a N 2 fixing cyanobacterium, halotolerant, that photosynthesizes an exopolysaccharide that excretes in the environment. This cyanobacterium can be grown in open or closed systems. The supply of CO 2 (in high concentrations, and always higher than natural atmospheric) can be carried out directly in the form of gas or after its solubilization in a liquid (such as CO 2 , such as bicarbonate or carbonate) that would be used as a culture medium . CO 2 in high concentration can come from power generation plants, cement plants or industrial plants that develop CO 2 generating processes. As one of the majority photosynthetic products of the fixation of inorganic carbon (CO 2 , bicarbonate, carbonate) through the cultivation of these cyanobacteria, an exopolysaccharide (EPS) is obtained that is released into the environment.
Dicho polisacárido, dadas sus propiedades energéticas, puede ser utilizado como biocombustible, bien en Ia propia planta que generó el CO2 contaminante o bien en otras instalaciones.Said polysaccharide, given its energy properties, can be used as a biofuel, either in the plant itself that generated the polluting CO 2 or in other facilities.
En una realización particular se utiliza Ia especie Anabaena, y preferentemente Ia cepa Anabaena sp. ATCC 33047, que produce un EPS que posee un calor de combustión similar al del carbón o Ia madera, de al menos 14 kJ/g.In a particular embodiment, the Anabaena species is used, and preferably the Anabaena sp. ATCC 33047, which produces an EPS that has a heat of combustion similar to that of coal or wood, of at least 14 kJ / g.
El procedimiento de Ia presente invención presenta una alta tasa de fijación de CO2 y producción de exopolisacárido, pudiendo, en el caso de Anabaena, generar al menos 1 ,3 g de polisacárido además de, al menos, 0,4 g de biomasa por litro y día y fijar 1 ,6 kg de CO2 por cada kg de polisacárido producido.The process of the present invention has a high rate of fixation of CO 2 and production of exopolysaccharide, being able, in the case of Anabaena, to generate at least 1.3 g of polysaccharide in addition to at least 0.4 g of biomass per liter and day and fix 1, 6 kg of CO 2 for each kg of polysaccharide produced.
En otro aspecto, Ia invención se relaciona por tanto con Ia utilización de dicho procedimiento para reducir o eliminar las emisiones de CO2 producidas por centrales de generación eléctrica y una diversidad de procesos industriales, pero también, por otra parte, el uso de sus productos como biocombustible posibilita reducir el consumo de combustibles fósiles.In another aspect, the invention is therefore related to the use of said method to reduce or eliminate CO 2 emissions produced by power generation plants and a variety of industrial processes, but also, on the other hand, the use of their products As a biofuel it is possible to reduce the consumption of fossil fuels.
La invención se relaciona además con Ia utilización del polisacárido generado a partir de Ia fijación de CO2 por Anabaena, como agente emulsificante, estabilizante o espesante en industria alimentaria, textil, de pinturas, papelera, cosmética y farmacéutica.The invention also relates to the use of the polysaccharide generated from the fixation of CO 2 by Anabaena, as an emulsifying, stabilizing or thickening agent in the food, textile, paint, paper, cosmetic and pharmaceutical industries.
Dicho polisacárido también puede ser utilizado para Ia adsorción, concentración, o eliminación de metales (pesados) en aguas residuales de diversa procedencia (urbanas, industria pesada, minería, etc.), así como para el
acondicionamiento y recuperación de suelos para uso agrícola. Igualmente, el EPS puede ser utilizado como agente antiviral, o como sustrato de procesos fermentativos.Said polysaccharide can also be used for adsorption, concentration, or elimination of (heavy) metals in wastewater of diverse origin (urban, heavy industry, mining, etc.), as well as for the conditioning and recovery of soils for agricultural use. Similarly, EPS can be used as an antiviral agent, or as a substrate for fermentation processes.
DESCRIPCIÓN DETALLADA DE LA INVENCIÓNDETAILED DESCRIPTION OF THE INVENTION
En un aspecto, Ia invención se relaciona con un procedimiento para fijar CO2 mediante Ia utilización de un cultivo de microorganismos fotosintéticos, en adelante procedimiento de Ia invención, que comprende las siguientes etapas: a) cultivar dicho microorganismo en un sistema adecuado b) suministrar al cultivo CO2 u otra forma inorgánica de carbono derivada de él, tal como bicarbonato ( HCO3) y/o carbonato CCO3), a concentraciones elevadas, y c) recoger los productos de Ia fijación del CO2 y de otras formas de carbono inorgánico de él derivadas (bicarbonato, carbonato), generados por dicho cultivo, siendo el microorganismo cultivado cualquier cianobacteria fijadora de nitrógeno, halotolerante, y capaz de producir un exopolisacárido (EPS) que se excreta al medio.In one aspect, the invention relates to a method for fixing CO2 by using a culture of photosynthetic microorganisms, hereinafter the method of the invention, which comprises the following steps: a) cultivating said microorganism in a suitable system b) supplying the CO2 culture or other inorganic form of carbon derived from it, such as bicarbonate (HCO 3 ) and / or carbonate CCO 3 ), at high concentrations, and c) collecting the products of the fixation of CO 2 and other forms of inorganic carbon of he derivatives (bicarbonate, carbonate), generated by said culture, the cultured microorganism being any nitrogen fixing cyanobacterium, halotolerant, and capable of producing an exopolysaccharide (EPS) that is excreted in the medium.
El procedimiento de Ia invención contempla que el cultivo del microorganismo seleccionado pueda realizarse tanto en sistemas abiertos como cerrados. El cultivo de microorganismos en sistema abierto es más económico, pero en contrapartida permite escaso control de parámetros importantes para Ia adecuada marcha del proceso. Los sistemas de cultivo cerrado permiten un mejor y más estricto control de las condiciones de operación del cultivo, que redunda en productividades superiores y productos de mayor calidad, pero se trata de sistemas más sofisticados y más caros. En una realización particular de Ia invención se utilizó un sistema de cultivo cerrado, concretamente un fotobiorreactor tubular cerrado, colocado a Ia intemperie. En otra realización particular de Ia invención se constató Ia viabilidad del cultivo, a Ia intemperie, en estanques abiertos de 1 y 10 m2 de superficie.
El aporte de carbono inorgánico a concentraciones elevadas mencionado en el punto b) del procedimiento de Ia invención se efectúa bien directamente en forma de CO2 gas o bien tras su solubilización en un líquido (como tal CO2, bicarbonato y/o carbonato) que posteriormente se utiliza como medio de cultivo del microorganismo. La concentración de CO2 inicial suministrada al cultivo, en todos los casos es superior a Ia atmosférica, 0,03% (v/v). La fuente emisora de dicho CO2 puede seleccionarse entre una planta de generación de electricidad, una cementera, o una planta de procesos industriales, entre otras. En una realización particular de Ia invención se suministra el CO2 en forma de gas, el cual se inyecta a un fotobiorreactor tubular cerrado a través de sus válvulas de entrada de gases. En otra realización particular de Ia invención sería posible suministrar el CO2 fijado en agua de mar que se utilizaría posteriormente como medio de cultivo. La utilización de agua de mar no repercutiría negativamente en el crecimiento del microorganismo puesto que se trata de una cepa halotolerante.The process of the invention contemplates that the culture of the selected microorganism can be carried out both in open and closed systems. The cultivation of microorganisms in the open system is more economical, but in counterpart it allows little control of important parameters for the adequate progress of the process. Closed cropping systems allow a better and stricter control of the operating conditions of the crop, which results in higher productivity and higher quality products, but these are more sophisticated and more expensive systems. In a particular embodiment of the invention, a closed culture system was used, specifically a closed tubular photobioreactor, placed outdoors. In another particular embodiment of the invention, the viability of the crop, outdoors, in open ponds with a surface area of 1 and 10 m 2 was observed. The contribution of inorganic carbon at high concentrations mentioned in point b) of the process of the invention is carried out either directly in the form of CO 2 gas or after its solubilization in a liquid (such as CO 2 , bicarbonate and / or carbonate) that subsequently it is used as a culture medium for the microorganism. The concentration of initial CO 2 supplied to the crop, in all cases is higher than atmospheric, 0.03% (v / v). The emitting source of said CO 2 can be selected from an electricity generation plant, a cement plant, or an industrial process plant, among others. In a particular embodiment of the invention, CO 2 is supplied in the form of a gas, which is injected into a closed tubular photobioreactor through its gas inlet valves. In another particular embodiment of the invention it would be possible to supply the CO 2 fixed in seawater that would be used later as a culture medium. The use of seawater would not negatively affect the growth of the microorganism since it is a halotolerant strain.
Mediante el procedimiento de Ia invención y como consecuencia de Ia fijación de CO2, se obtienen diversos productos fotosintéticos, de los que al menos uno es un exopolisacárido (EPS), pudiendo llegar a constituir este EPS el producto fotosintético mayoritario.Through the process of the invention and as a consequence of the fixation of CO 2 , various photosynthetic products are obtained, of which at least one is an exopolysaccharide (EPS), this EPS being able to constitute the majority photosynthetic product.
En una realización particular de Ia invención, el microorganismo cultivado pertenece a Ia especie Anabaena, en concreto Ia cepa Anabaena sp. ATCC 33047. Esta estirpe, Anabaena sp. ATCC 33047, posee elevada tasa de crecimiento, incluso a elevada densidad de población, tolera amplios intervalos de pH, temperatura, irradiancia y concentración de sales, presenta capacidad de fijar nitrógeno (por Io que no necesita aporte de fertilizante nitrogenado y se reduce el riesgo de contaminaciones), alta productividad y elevada eficiencia para Ia fijación de CO2, siendo de fácil recolección (Moreno J, Vargas MA, Olivares H, Rivas J and Guerrero MG (1998). Exopolysaccharide production by the cyanobacterium Anabaena sp. ATCC 33047 in batch and continuous culture. J Biotechnol 60, 175-182; Moreno J, Vargas MA, Madiedo JM, Muñoz J, Rivas J and Guerrero MG (2000). Chemical and rheological properties of an extracellular polysaccharide produced by the cyanobacterium Anabaena sp.
ATCC 33047. Biotechnol Bioeng 67, 283-290). Especialmente destacable es su elevada tasa de generación de EPS, que es aún mayor en condiciones de estrés, llegando a mostrar una productividad de EPS al menos 3 veces superior a Ia de generación de biomasa. Estas características hacen a esta cianobacteria una candidata idónea para su empleo en Ia biofijación efectiva del CO2 presente en gases de escape o en otras fuentes contaminantes emisoras de este gas.In a particular embodiment of the invention, the cultured microorganism belongs to the Anabaena species, specifically the Anabaena sp. ATCC 33047. This lineage, Anabaena sp. ATCC 33047, has a high growth rate, even at high population density, tolerates wide ranges of pH, temperature, irradiance and concentration of salts, has the ability to fix nitrogen (so it does not need nitrogen fertilizer and reduces the risk of contamination), high productivity and high efficiency for the fixation of CO 2 , being easy to collect (Moreno J, Vargas MA, Olivares H, Rivas J and Guerrero MG (1998). Exopolysaccharide production by the cyanobacterium Anabaena sp. ATCC 33047 in batch and continuous culture J Biotechnol 60, 175-182; Moreno J, Vargas MA, Madiedo JM, Muñoz J, Rivas J and Guerrero MG (2000) Chemical and rheological properties of an extracellular polysaccharide produced by the cyanobacterium Anabaena sp. ATCC 33047. Biotechnol Bioeng 67, 283-290). Especially noteworthy is its high rate of EPS generation, which is even higher under stress conditions, reaching an EPS productivity at least 3 times higher than that of biomass generation. These characteristics make this cyanobacteria an ideal candidate for use in the effective biofixation of CO 2 present in exhaust gases or in other polluting sources emitting this gas.
Dicho EPS producido por Ia especie Anabaena posee un calor de combustión similar al de Ia madera o el carbón. En una realización particular de Ia invención, el calor de combustión de dicho EPS es de al menos 14 kJ/g.Said EPS produced by Anabaena species has a heat of combustion similar to that of wood or coal. In a particular embodiment of the invention, the heat of combustion of said EPS is at least 14 kJ / g.
El procedimiento de Ia invención proporciona un mecanismo eficaz y eficiente de fijación de CO2, acoplado a Ia producción de un EPS susceptible de ser aprovechado. En una realización particular de Ia invención se obtuvieron al menos 1 ,3 g por litro y día de polisacárido además de al menos 0,4 g de biomasa por litro y día. En otra realización particular se verificó Ia fijación de 1 ,6 kg de CO2 por cada kg de polisacárido producido. En otra realización particular de este procedimiento se fijaron entre 2 y 6 g de CO2 por litro y día.The method of the invention provides an effective and efficient mechanism for fixing CO 2, coupled to the production of a susceptible EPS be exploited. In a particular embodiment of the invention, at least 1.3 g per liter and day of polysaccharide were obtained in addition to at least 0.4 g of biomass per liter and day. In another particular embodiment, the fixation of 1.6 kg of CO 2 was verified for each kg of polysaccharide produced. In another particular embodiment of this procedure, between 2 and 6 g of CO 2 were fixed per liter and day.
En otro aspecto, Ia invención se relaciona con Ia utilización del procedimiento para reducir o eliminar emisiones de CO2 que proceden de procesos industriales, preferentemente de las centrales de generación de electricidad, y para reducir el consumo de combustibles fósiles en aquellos procesos industriales que los utilizan, mediante su sustitución por productos de fijación de CO2 obtenidos en dicho procedimiento.In another aspect, the invention relates to the use of the process to reduce or eliminate CO 2 emissions that come from industrial processes, preferably from power generation plants, and to reduce the consumption of fossil fuels in those industrial processes that They used, by replacing products CO 2 fixation obtained in said process.
Tanto Ia biomasa o material celular, como el EPS generado mediante este proceso, utilizando cultivos de Ia especie Anabaena, como Ia mezcla de biomasa y EPS, pueden ser utilizados para diversos fines, siendo una de sus posibles aplicaciones su combustión para Ia generación de calor o electricidad, ya que tanto Ia biomasa como el EPS poseen considerable calor de combustión (igual o superior a 14 kJ/g). Por Io tanto, en otro aspecto, Ia invención se relaciona con Ia utilización del EPS obtenido, como biocombustible. En una
realización particular de Ia invención el EPS obtenido se podría utilizar como biocombustible en Ia misma planta generadora de las emisiones contaminantes de CO2.Both the biomass or cellular material, and the EPS generated by this process, using Anabaena species crops, such as the mixture of biomass and EPS, can be used for various purposes, being one of its possible applications its combustion for heat generation or electricity, since both biomass and EPS have considerable heat of combustion (equal to or greater than 14 kJ / g). Therefore, in another aspect, the invention relates to the use of the EPS obtained, as a biofuel. In a Particular embodiment of the invention, the EPS obtained could be used as biofuel in the same plant that generates the CO 2 pollutant emissions.
Los EPS producidos por los microorganismos pueden tener aplicaciones en Ia industria agroalimentaria y/o farmacéutica (Sutherland IW (1996) Extracellular polysaccharides. En: Biotechnology VCH, Weinheim (Rehm HJ and Reed G eds.), vol 6, 615-657). Los polisacáridos aniónicos son de utilidad para Ia detección, adsorción, concentración y/o eliminación de iones metálicos de aguas residuales (Bender J, Rodríguez-Eaton S, Ekanemesang UM and Phillips P (1994). Characterization of metal-binding bioflocculants produced by the cyanobacterial component of mixed microbial mats. Appl Environ Microbiol 60, 2311-2315; Bertocchi C, Navarini L and Cesara A (1990). Polysaccharides from cyanobacteria. Carbohydr Polym 12, 127-153). Igualmente, los EPS pueden utilizarse para inducir Ia floculación de partículas sólidas en el tratamiento de aguas residuales urbanas, así como en el acondicionamiento y recuperación de suelos para uso agrícola (Flaibani A, Olsen Y and Painter TJ (1989). Polysaccharides in desert reclamation: Compositions of exocellular proteoglycan complexes produced by filamentous blue-green edaphic algae. Carbohydr Res 190, 235-248). Algunos polisacáridos de microorganismos, especialmente de los de tipo fotoautotrófico poseen actividad antiviral (Yim JH, Kim SJ, Ahn SH, Lee ChK, Rhie KT and Lee HK (2004). Antiviral Effects of Sulphated Exopolysaccharide from the Marine Microalga Gyrodinium impudicum Strain KG03. Mar Biotechnol 6, 17-25). Por tanto, otro aspecto de Ia invención se relaciona con Ia utilización del EPS generado a partir de los cultivos de Ia especie Anabaena como agente emulsificante, estabilizante o espesante en industria alimentaria, textil, de pinturas, papelera, cosmética y/o farmacéutica, así como su utilización para Ia concentración y/o eliminación de metales en aguas residuales de diversa procedencia (urbanas, industria pesada, minería, etc.). Asimismo Ia invención se relaciona con el empleo de este EPS en el acondicionamiento y recuperación de suelos para uso agrícola, como potencial agente antiviral y como sustrato de procesos fermentativos.
El siguiente ejemplo sirve para ilustrar Ia invención y no debe ser considerado con fines limitativos de Ia misma.The EPS produced by the microorganisms can have applications in the agri-food and / or pharmaceutical industry (Sutherland IW (1996) Extracellular polysaccharides. In: Biotechnology VCH, Weinheim (Rehm HJ and Reed G. eds.), Vol 6, 615-657). Anionic polysaccharides are useful for the detection, adsorption, concentration and / or elimination of metal ions from wastewater (Bender J, Rodríguez-Eaton S, Ekanemesang UM and Phillips P (1994). Characterization of metal-binding bioflocculants produced by the cyanobacterial component of mixed microbial mats. Appl Environ Microbiol 60, 2311-2315; Bertocchi C, Navarini L and Cesara A (1990). Polysaccharides from cyanobacteria. Carbohydr Polym 12, 127-153). Similarly, EPS can be used to induce flocculation of solid particles in the treatment of urban wastewater, as well as in the conditioning and recovery of soils for agricultural use (Flaibani A, Olsen Y and Painter TJ (1989). Polysaccharides in desert reclamation : Compositions of exocellular proteoglycan complexes produced by filamentous blue-green edaphic algae. Carbohydr Res 190, 235-248). Some microorganism polysaccharides, especially those of the photoautotrophic type have antiviral activity (Yim JH, Kim SJ, Ahn SH, Lee ChK, Rhie KT and Lee HK (2004). Antiviral Effects of Sulphated Exopolysaccharide from the Marine Microalga Gyrodinium impudicum Strain KG03. Mar Biotechnol 6, 17-25). Therefore, another aspect of the invention relates to the use of EPS generated from the Anabaena species as an emulsifying, stabilizing or thickening agent in the food, textile, paint, paper, cosmetic and / or pharmaceutical industry, as well as as its use for the concentration and / or elimination of metals in wastewater of diverse origin (urban, heavy industry, mining, etc.). Likewise, the invention relates to the use of this EPS in the conditioning and recovery of soils for agricultural use, as a potential antiviral agent and as a substrate for fermentation processes. The following example serves to illustrate the invention and should not be considered for limiting purposes thereof.
EJEMPLO DE REALIZACIÓN DE LA INVENCIÓNEXAMPLE OF EMBODIMENT OF THE INVENTION
CULTIVO DE Anabaena sp. EN FOTOBIORREACTOR TUBULAR CERRADOCROP OF Anabaena sp. IN CLOSED TUBULAR PHOTOBIOR REACTOR
En esta realización particular de Ia invención se ha seleccionado Ia cianobacteria fijadora de N2 Anabaena sp. ATCC 33047, teniendo en cuenta sus especiales características de eficiencia fijadora de CO2 y su alta productividad.In this particular embodiment of the invention the fixing cyanobacterium of N 2 Anabaena sp. ATCC 33047, taking into account its special characteristics of CO 2 fixing efficiency and its high productivity.
El cultivo de Anabaena sp. ATCC 33047 se llevó a cabo a Ia intemperie en un fotobiorreactor tubular cerrado, siendo Ia fuente de iluminación Ia luz solar. Dicho sistema consta de un módulo de captación de luz solar constituido por tubos de material transparente (plexiglás rígido) de 24 mm de diámetro interno y 30 mm de diámetro externo y una longitud total de 90 m, situados horizontalmente en paralelo y conectados entre sí por medio de piezas en forma de "u" del mismo material, con una superficie fotosintéticamente activa de 2,2 m2 y 55 I de volumen útil. Dos bolas de caucho de diámetro ligeramente inferior al diámetro interior de los tubos circulan para evitar el depósito de células en las paredes de los mismos. Estos tubos se encuentran sumergidos en agua, que actúa como elemento termostatizador del cultivo, en un baño de dimensiones 1 ,8x6,0x0,15 m, provisto de circuito cerrado de circulación con elementos calefactores y enfriadores. En este sistema de cultivo, Ia suspensión celular se agita y se hace circular a través de los tubos por Ia impulsión de aire estéril a presión generado por un compresor (air-lift). El sistema tubular termina en un cilindro de 52 cm de alto por 26 cm de diámetro externo, situado a 2,8 m de altura desde Ia horizontal del reactor. En Ia tapa de este cilindro existen varios orificios para: salida de gas (protegido por un filtro de 0,22 μm), entrada para llenado rápido del reactor, entrada de medio fresco para operar en cultivo continuo y sensor de nivel. En Ia parte inferior del cilindro se encuentran
además las sondas de pH y temperatura. Estas sondas se conectan con una unidad de control.The cultivation of Anabaena sp. ATCC 33047 was carried out outdoors in a closed tubular photobioreactor, the light source being sunlight. Said system consists of a solar light collection module consisting of tubes of transparent material (rigid plexiglass) of 24 mm internal diameter and 30 mm external diameter and a total length of 90 m, located horizontally in parallel and connected to each other by half of pieces in the form of "u" of the same material, with a photosynthetically active surface of 2.2 m 2 and 55 I of useful volume. Two rubber balls with a diameter slightly smaller than the inside diameter of the tubes circulate to prevent the deposit of cells in their walls. These tubes are submerged in water, which acts as a thermostatting element of the crop, in a bath of dimensions 1, 8x6.0x0.15 m, equipped with a closed circulation circuit with heating and cooling elements. In this culture system, the cell suspension is stirred and circulated through the tubes by the delivery of sterile air under pressure generated by a compressor (air-lift). The tubular system ends in a 52 cm high by 26 cm external diameter cylinder, located 2.8 m high from the horizontal of the reactor. In the cover of this cylinder there are several holes for: gas outlet (protected by a 0.22 μm filter), input for rapid filling of the reactor, fresh medium input to operate in continuous culture and level sensor. In the lower part of the cylinder are also the pH and temperature probes. These probes are connected to a control unit.
Se procedió a Ia introducción en el sistema de cultivo de una suspensión de células de Anabaena sp. ATCC 33047 con una concentración de clorofila comprendida entre 5 y 10 mg por litro de cultivo. Dicha suspensión se mantuvo en circulación a una velocidad comprendida entre 0,2 y 0,4 m s"1 por un periodo de 72 horas, durante el que se mantiene el cultivo en régimen estanco, con control de temperatura, máxima de 35 °C durante el día y de 18 °C durante Ia noche, y sometido a una irradiancia solar. Transcurridas las 72 horas, el cultivo se somete a régimen continuo, con adición continuada de medio de cultivo fresco (que cubre todos los requerimientos nutricionales del microorganismo) durante el periodo de luz. La suspensión celular se mantiene circulando por los tubos durante 45 días.The introduction into the culture system of a cell suspension of Anabaena sp. ATCC 33047 with a concentration of chlorophyll between 5 and 10 mg per liter of culture. Said suspension was kept in circulation at a speed between 0.2 and 0.4 ms "1 for a period of 72 hours, during which the culture is maintained in a watertight regime, with temperature control, maximum of 35 ° C during the day and 18 ° C overnight, and subjected to solar irradiance After 72 hours, the culture is subjected to continuous regime, with continued addition of fresh culture medium (which covers all the nutritional requirements of the microorganism) during the period of light The cell suspension is kept circulating in the tubes for 45 days.
Durante el proceso, el valor del pH se mantiene entre 8,0 y 8,5 mediante Ia inyección de CO2 a través de una electroválvula regulada por un controlador de pH. El CO2 se inyecta en Ia zona horizontal del tubo de retorno de Ia suspensión celular hacia el módulo de captación de luz. El consumo fotosintético de CO2 por las células de Ia cianobacteria provoca una elevación del pH del medio, que al superar el valor de 8,5 dispara Ia inyección de una corriente de CO2 gas puro, con Io que se acidifica el medio, deteniéndose Ia inyección de CO2 una vez que se recupera el valor de pH 8,0.During the process, the pH value is maintained between 8.0 and 8.5 by means of the injection of CO2 through a solenoid valve regulated by a pH controller. The CO2 is injected into the horizontal zone of the return tube of the cell suspension towards the light collection module. The photosynthetic consumption of CO 2 by the cells of the cyanobacteria causes an increase in the pH of the medium, which, upon exceeding the value of 8.5, triggers the injection of a stream of CO 2 pure gas, with which the medium is acidified, stopping The injection of CO 2 once the pH 8.0 is recovered.
Manteniendo el cultivo en el sistema y condiciones anteriormente señaladas, Ia concentración de exopolisacárido en el medio alcanzó valores de hasta 8 g por litro, con una productividad de EPS de hasta 4 g por litro y día. La recogida de Ia suspensión enriquecida con el EPS generado y Ia biomasa que Io acompaña se realiza de manera continua durante el periodo de luz a un flujo de aproximadamente 2 litros por hora.
Maintaining the culture in the system and conditions indicated above, the concentration of exopolysaccharide in the medium reached values of up to 8 g per liter, with an EPS productivity of up to 4 g per liter per day. The collection of the suspension enriched with the EPS generated and the accompanying biomass is carried out continuously during the light period at a flow of approximately 2 liters per hour.
Claims
1.- Procedimiento para fijar CO2 mediante Ia utilización de un cultivo de microorganismos fotosintéticos que comprende las siguientes etapas: a) cultivar dicho microorganismo en un sistema adecuado, b) suministrar al cultivo CO2 u otra forma inorgánica de carbono derivada de él, tal como bicarbonato ( HCO3) y/o carbonato CCO3), a concentraciones elevadas, y c) recoger los productos de Ia fijación del CO2 y de otras formas de carbono inorgánico de él derivadas (bicarbonato, carbonato), generados por dicho cultivo, caracterizado porque el microorganismo cultivado en a) es cualquier cianobacteria fijadora de nitrógeno, halotolerante y capaz de producir un exopolisacárido que se excreta al medio.1.- Procedure for fixing CO2 by means of the use of a culture of photosynthetic microorganisms comprising the following steps: a) cultivating said microorganism in a suitable system, b) supplying the CO2 culture or other inorganic form of carbon derived therefrom, such as bicarbonate (HCO 3 ) and / or CCO 3 carbonate, at high concentrations, and c) collect the products of the fixation of CO2 and other forms of inorganic carbon derived from it (bicarbonate, carbonate), generated by said crop, characterized in that The microorganism grown in a) is any nitrogen-fixing cyanobacterium, halotolerant and capable of producing an exopolysaccharide that is excreted in the medium.
2.- Procedimiento para fijar CO2 según Ia reivindicación 1 caracterizado porque dicho cultivo de microorganismos se realiza en un sistema cerrado, preferentemente en un fotobiorreactor tubular cerrado.2. Method for fixing CO 2 according to claim 1, characterized in that said microorganism culture is carried out in a closed system, preferably in a closed tubular photobioreactor.
3.- Procedimiento para fijar CO2 según Ia reivindicación 1 caracterizado porque dicho cultivo de microorganismos se realiza en un sistema abierto.3. Method for fixing CO 2 according to claim 1 characterized in that said culture of microorganisms is carried out in an open system.
4.- Procedimiento para fijar CO2 según cualquiera de las reivindicaciones de Ia 1 a Ia 3 caracterizado porque el CO2 a concentración elevada se suministra al cultivo en forma gaseosa, preferentemente suministrando dicho gas directamente desde Ia fuente emisora de CO2.4. Method for CO2 set according any of claims 1 to Ia 3 Ia wherein the CO 2 at high concentration is supplied to the culture in gaseous form, preferably by supplying said gas directly from Ia source emitting CO2.
5.- Procedimiento para fijar CO2 según cualquiera de las reivindicaciones de Ia 1 a Ia 3 caracterizado porque el CO2 en concentraciones elevadas se suministra al cultivo fijado en medio líquido, utilizándose posteriormente dicho medio líquido como medio de cultivo del microorganismo. 5. Method for fixing CO 2 according to any of claims 1 to 3, characterized in that the CO 2 in high concentrations is supplied to the fixed culture in liquid medium, said liquid medium being subsequently used as the microorganism culture medium.
6.- Procedimiento para fijar CO2 según Ia reivindicación 5 caracterizado porque dicho medio líquido donde se fija el CO2 y se cultiva el microorganismo, es agua salada, preferentemente agua de mar6. Method for fixing CO2 according to claim 5, characterized in that said liquid medium where CO 2 is fixed and the microorganism is grown, is salt water, preferably seawater
7.- Procedimiento para fijar CO2 según cualquiera de las reivindicaciones 4, 5 y 6 caracterizado porque Ia fuente emisora de CO2 es una planta de generación de electricidad, una cementera, o una planta de procesos industriales.7. Method for fixing CO 2 according to any of claims 4, 5 and 6 characterized in that the emitting source of CO 2 is a power generation plant, a cement plant, or an industrial process plant.
8.- Procedimiento para fijar CO2 según cualquiera de las reivindicaciones de Ia 4 a Ia 7 caracterizado porque Ia concentración de CO2 suministrado es superior al 0,03% (v/v).8. Method for fixing CO 2 according to any of claims 4 to 7, characterized in that the concentration of CO 2 supplied is greater than 0.03% (v / v).
9.- Procedimiento para fijar CO2 según cualquiera de las reivindicaciones de Ia 1 a Ia 8 caracterizado porque el producto mayoritario de Ia fijación de CO2 generado por el cultivo del microorganismo, es un polisacárido que se libera al medio.9. Method for fixing CO 2 according to any of claims 1 to 8, characterized in that the majority product of the fixation of CO 2 generated by the culture of the microorganism, is a polysaccharide that is released into the medium.
10.- Procedimiento para fijar CO2 según cualquiera de las reivindicaciones de Ia 1 a Ia 9 caracterizado porque dicho cultivo de microorganismos es un cultivo de Ia especie Anabaena, preferentemente Ia estirpe Anabaena sp. ATCC 33047.10. Method for fixing CO 2 according to any of claims 1 to 9, characterized in that said culture of microorganisms is a culture of the Anabaena species, preferably the Anabaena sp. ATCC 33047.
11.- Procedimiento para fijar CO2 según Ia reivindicación 10 caracterizado porque fija al menos 1 ,6 kg de CO2 por cada kg de polisacárido producido.11. Method for fixing CO 2 according to claim 10, characterized in that it fixes at least 1.6 kg of CO 2 for each kg of polysaccharide produced.
12.- Procedimiento para fijar CO2 según Ia reivindicación 10 caracterizado porque mediante el cultivo de microorganismos produce al menos 1 ,3 g de polisacárido y 0,4 g de biomasa por litro y día.12. Method for fixing CO 2 according to claim 10, characterized in that, by means of the cultivation of microorganisms, it produces at least 1.3 g of polysaccharide and 0.4 g of biomass per liter and day.
13.- Procedimiento para fijar CO2 según Ia reivindicación 10 caracterizado porque mediante el cultivo de microorganismos fija entre 2 y 6 g de CO2 por litro y día. 13.- Procedure for fixing CO 2 according to claim 10 characterized in that by means of the culture of microorganisms it fixes between 2 and 6 g of CO 2 per liter and day.
14.- Utilización de un procedimiento según cualquiera de las reivindicaciones de Ia 1 a Ia 13, para reducir o eliminar emisiones de CO2 que proceden de procesos industriales, preferentemente de las centrales de generación eléctrica.14.- Use of a method according to any of claims 1 to 13, to reduce or eliminate CO 2 emissions that come from industrial processes, preferably from power generation plants.
15.- Utilización de un procedimiento según cualquiera de las reivindicaciones de Ia 1 a Ia 13 para reducir el consumo de combustibles fósiles en aquellos procesos industriales que los emplean, mediante su sustitución por productos de fijación de CO2 obtenidos en dicho procedimiento.15.- Use of a process according to any of claims 1 to 13 to reduce the consumption of fossil fuels in those industrial processes that use them, by replacing them with CO2 fixation products obtained in said process.
16.- Utilización de un polisacárido (sólo o mezclado con biomasa) obtenido según el procedimiento descrito en Ia reivindicación 10, como biocombustible.16.- Use of a polysaccharide (alone or mixed with biomass) obtained according to the method described in claim 10, as biofuel.
17.- Utilización de un polisacárido (sólo o mezclado con biomasa) según Ia reivindicación 16 como biocombustible en Ia misma planta generadora del gas con alto contenido en CO2.17. Use of a polysaccharide (alone or mixed with biomass) according to claim 16 as biofuel Ia same gas generating plant with high CO 2 content.
18.- Utilización de un polisacárido obtenido según el procedimiento descrito en Ia reivindicación 10, como agente emulsificante, estabilizante o espesante en Ia industria alimentaria, textil, de pinturas, papelera, cosmética y farmacéutica.18.- Use of a polysaccharide obtained according to the method described in claim 10, as an emulsifying, stabilizing or thickening agent in the food, textile, paint, paper, cosmetic and pharmaceutical industry.
19.- Utilización de un polisacárido obtenido según el procedimiento descrito en Ia reivindicación 10, para Ia concentración o eliminación de metales en aguas residuales de diversa procedencia (urbanas, industria pesada, minería, etc.)19.- Use of a polysaccharide obtained according to the procedure described in claim 10, for the concentration or elimination of metals in wastewater of diverse origin (urban, heavy industry, mining, etc.)
20.- Utilización de un polisacárido obtenido según el procedimiento descrito en Ia reivindicación 10, para el acondicionamiento y recuperación de suelos para uso agrícola. 20.- Use of a polysaccharide obtained according to the method described in claim 10, for the conditioning and recovery of soils for agricultural use.
21.- Utilización de un polisacárido obtenido según el procedimiento descrito en Ia reivindicación 10, como agente antiviral.21.- Use of a polysaccharide obtained according to the method described in claim 10, as an antiviral agent.
22.- Utilización de un polisacárido obtenido según el procedimiento descrito en Ia reivindicación 10, sólo o en combinación con Ia biomasa, como sustrato de procesos fermentativos. 22.- Use of a polysaccharide obtained according to the procedure described in claim 10, alone or in combination with the biomass, as a substrate for fermentation processes.
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ES200501126A ES2262432B1 (en) | 2005-05-11 | 2005-05-11 | PROCEDURE FOR SETTING CARBON DIOXIDE THROUGH THE USE OF A CIANOBACTERIA CULTURE. |
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WO2009112624A1 (en) | 2008-03-14 | 2009-09-17 | Endesa Generación, S. A. | Liquid-phase gas collection |
WO2011101469A1 (en) * | 2010-02-22 | 2011-08-25 | Agc Glass Europe | Method for purifying gases including co2 and corresponding device |
WO2012056126A1 (en) * | 2010-10-28 | 2012-05-03 | IFP Energies Nouvelles | Integrated process for producing calcite and biomass using cyanobacteria for the utilization of co2 for energy purposes and the mineral sequestration of co2 |
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FR2915404A1 (en) * | 2007-04-30 | 2008-10-31 | Centre Nat Rech Scient | Reducing carbon dioxide in air using biochemical units, comprises introducing biochemical units, appropriate culture medium and carbon dioxide flow in a reactor, illuminating a reactional mixture, and recuperating a reactional product |
WO2009112624A1 (en) | 2008-03-14 | 2009-09-17 | Endesa Generación, S. A. | Liquid-phase gas collection |
WO2011101469A1 (en) * | 2010-02-22 | 2011-08-25 | Agc Glass Europe | Method for purifying gases including co2 and corresponding device |
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WO2012056126A1 (en) * | 2010-10-28 | 2012-05-03 | IFP Energies Nouvelles | Integrated process for producing calcite and biomass using cyanobacteria for the utilization of co2 for energy purposes and the mineral sequestration of co2 |
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JP2013540448A (en) * | 2010-10-28 | 2013-11-07 | イエフペ エネルジ ヌヴェル | Integrated production method of calcite and biomass using cyanobacteria for energy resource utilization and carbon dioxide mineral fixation |
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