WO2010015724A1 - Composition of a material having a porous structure, composition preparation method and use of composition - Google Patents
Composition of a material having a porous structure, composition preparation method and use of composition Download PDFInfo
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- WO2010015724A1 WO2010015724A1 PCT/ES2009/070331 ES2009070331W WO2010015724A1 WO 2010015724 A1 WO2010015724 A1 WO 2010015724A1 ES 2009070331 W ES2009070331 W ES 2009070331W WO 2010015724 A1 WO2010015724 A1 WO 2010015724A1
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/04—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of alkali metals, alkaline earth metals or magnesium
- B01J20/043—Carbonates or bicarbonates, e.g. limestone, dolomite, aragonite
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/10—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate
- B01J20/12—Naturally occurring clays or bleaching earth
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
- B01J20/28014—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their form
- B01J20/28016—Particle form
- B01J20/28021—Hollow particles, e.g. hollow spheres, microspheres or cenospheres
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
- B01J20/28054—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their surface properties or porosity
- B01J20/28057—Surface area, e.g. B.E.T specific surface area
- B01J20/28059—Surface area, e.g. B.E.T specific surface area being less than 100 m2/g
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
- B01J20/28054—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their surface properties or porosity
- B01J20/28069—Pore volume, e.g. total pore volume, mesopore volume, micropore volume
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/30—Processes for preparing, regenerating, or reactivating
- B01J20/3014—Kneading
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/30—Processes for preparing, regenerating, or reactivating
- B01J20/3078—Thermal treatment, e.g. calcining or pyrolizing
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- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B38/00—Porous mortars, concrete, artificial stone or ceramic ware; Preparation thereof
- C04B38/06—Porous mortars, concrete, artificial stone or ceramic ware; Preparation thereof by burning-out added substances by burning natural expanding materials or by sublimating or melting out added substances
- C04B38/063—Preparing or treating the raw materials individually or as batches
- C04B38/0635—Compounding ingredients
- C04B38/064—Natural expanding materials, e.g. clay
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- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05D—INORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C; FERTILISERS PRODUCING CARBON DIOXIDE
- C05D3/00—Calcareous fertilisers
- C05D3/02—Calcareous fertilisers from limestone, calcium carbonate, calcium hydrate, slaked lime, calcium oxide, waste calcium products
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- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05G—MIXTURES OF FERTILISERS COVERED INDIVIDUALLY BY DIFFERENT SUBCLASSES OF CLASS C05; MIXTURES OF ONE OR MORE FERTILISERS WITH MATERIALS NOT HAVING A SPECIFIC FERTILISING ACTIVITY, e.g. PESTICIDES, SOIL-CONDITIONERS, WETTING AGENTS; FERTILISERS CHARACTERISED BY THEIR FORM
- C05G5/00—Fertilisers characterised by their form
- C05G5/45—Form not covered by groups C05G5/10 - C05G5/18, C05G5/20 - C05G5/27, C05G5/30 - C05G5/38 or C05G5/40, e.g. soluble or permeable packaging
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2220/00—Aspects relating to sorbent materials
- B01J2220/40—Aspects relating to the composition of sorbent or filter aid materials
- B01J2220/42—Materials comprising a mixture of inorganic materials
Definitions
- the invention relates to new materials with porous structure and their industrial use in the elimination of acid gases and vapors and their use in agriculture as soil fertilizers.
- the sulphurous anhydride and nitrogen oxides which are the compounds together with the ammonia that contribute most to the formation of acid rain, are generated mainly in the units that incinerate fossil fuels or their derivatives.
- clays are known that have plastic properties, that is, sufficiently moist, they are deformable when a slight pressure is applied while maintaining the shape, and they become rigid when dried and vitreous when subjected to high temperatures.
- they are natural phyllosilicates composed of small particles or crystals, generally of colloidal size, which give rise to materials of great surface development with capacity for both physical adsorption and chemical interaction.
- Bentonite is a very fine grain clay of the montmorillonite type and has a chemical structure and composition that confers a high specific surface area, high cation exchange capacity, great plasticity and ease of molding.
- the bentonite shaped material may incorporate as a load significant amounts of different materials, including calcium carbonates or magnesium; This fact is a way of great interest for the preparation of adsorbent / reactive compounds of acid gases with geometry suitable for industrial use.
- Bentonite is used in numerous products and processes (Kendall,
- the present invention relates to new materials, with porous structure, preferably formed as hollow cylinders, their industrial use in the elimination of acid gases and vapors and their use in agriculture as soil fertilizers.
- the present invention relates to a composition of adsorbent / reagent material characterized in that it includes bentonite together with carbonates of alkaline earth elements of mineral or organic origin, in this case from calcareous algae.
- bentonite powders and selected carbonates are mixed dry and homogeneously; subsequently, the mixture is kneaded with water in a high shear kneader.
- a pseudoplastic mass is produced that easily incorporates the carbonate particles.
- the mass obtained after kneading is molded or extruded to obtain the desired shape and then preferably dried at room temperature for at least 2 hours and at 80-150 ° C for at least four hours; subsequently the material is heat treated between 300 ° C and 900 ° C for at least 2 hours in air.
- adsorbent materials can be obtained with important operational advantages for the purification of fluids in dynamic regime or for incorporation into the soil as a fertilizer or fertilizer potentializer of conventional fertilizers.
- These hollow cylinders can be of the "macaroni" type smooth, striated, straight, curved, regular or irregular cut, of any shape and size.
- the passage of the fluid to be purified through the adsorbent material arranged in this geometric form gives rise to a fluid dynamic that combines a turbulent regime caused by the flow that passes between the cylinders with a laminar regime that takes place in the passage of the fluid inside the hollow cylinders.
- This situation gives rise to a unique behavior that significantly improves the effectiveness of the adsorption phenomenon when compared to the units formed in a hive where the fluid passes through it according to a laminar regime.
- the material offers greater contact area per unit volume than systems containing pellets or solid materials and its macroporous structure provides adequate space for a better development of desirable biological processes.
- the present invention further relates to a process for preparing the compositions indicated above. According to a preferred embodiment of the process, this includes the following steps:
- bentonite and calcium carbonate are mixed exclusively with a proportion of bentonite between 20 and 30% by weight.
- Heat treatments of the material prepared with bentonite and calcium carbonate at temperatures below 400 0 C give rise to pieces that are too sensitive to abrasion and the collapse of the physical structure due to water. These limitations practically disappear when the material is treated for times greater than 2 hours at temperatures between 500 0 C and 800 0 C. From 600 0 C, the carbonate is transformed into calcium oxide with CO2 evolution. At temperatures of 700 0 C for a time not less than 2 hours, all carbonates break down.
- the pieces formed and thermally stabilized at 700 0 C have a high content of new macropores, mainly caused by the gaps or spaces that are caused by the evolution of carbon dioxide. Consequently, an increase in the value of the total pore volume is observed with the temperature and the treatment time; for the initial composition calcium carbonate / bentonite of 70:30, the pieces treated at 600 ° C / 2 h have a total pore volume of 0.27 ml g ⁇ 1 , for 700 ° C / 2 h the value increases to 0.76 mi g "1 , and for 800 ° C / 2h it goes to 0.79 mi g " 1 .
- the present invention also relates to the use of a composition made as described above, as an adsorbent / reagent material for the elimination of acid gases and vapors in a dynamic regime.
- gases contaminated with sulfur dioxides, hydrochloric acid or hydrofluoric acid or mixtures thereof are passed through this material in the form of a hollow cylinder, the reaction of these acid gases with the calcium oxide it contains occurs, effectively forming extraordinary sulfite, sulfate, chlorides and calcium fluorides that are deposited filling the pores of the material.
- the saturated material arranged in a moving bed, can easily be replaced (for example, by a pneumatic system) by the fresh material without problems of corrosion, deposits, or sludge treatment.
- the calcium carbonate used may be of mineral origin or high-calcareous algae can also be used in said salt with similar yields.
- these materials when they are treated in stage e) at temperatures between 500 0 C and 600 0 C for at least 2 hours, they can be used as neutralizing or remineralizing agents for water treatment, lowering their CO 2 content and providing the necessary carbonate and bicarbonate ions.
- this includes the following steps:
- bentonite and calcareous algae are mixed with a proportion of bentonite of 10 and 15% by weight.
- the material prepared with bentonite and calcareous algae with a 10% bentonite content and treated at 500 0 C for 4 hours in air has a specific surface area of 7 m 2 g "1 and a total pore volume of 0.28 mi g " 1 .
- the present invention also relates to the use of a composition made as described above, as a fertilizer and acidic or sandy soil improvement material, introducing the numerous nutrient elements present in the calcareous algae and offering a hollow cylinder shape with walls. macroporous that favor in an extraordinary way the biological phenomena that take part in the growth of the plants.
- the cylinders prepared in this way are used as beds (temporary covering of the soil) in poultry farms that improve the health of the installation, favor the fattening of the animals and increase the quality of the product.
- the bentonite used as raw material in this invention was supplied by Tolsa SA under the name Atox, with a surface BET specific of 130 m 2 g "1 and a particle size of 75% less than 45 ⁇ m.
- a natural bentonite supplied by Oil-Dry Corporation called Bentonite of Paraná with a specific BET surface of 95 m 2 was used g "1 and a particle size of 82% less than 44 ⁇ m.
- the precipitated calcium carbonate used in this invention called SOCAL P2V was supplied by the Solvay Group with a purity of 98.8%, an average particle size of 1.5 ⁇ m and a specific surface area of 7 m 2 g "1 .
- the calcareous algae was supplied by Algarea Mineragáo Industria e Comercio Ltda. (Brazil) and corresponds particularly to the species Lithothamnium spp.
- the average value of its weight composition is 90.9% calcium carbonate, 3% magnesium as Mg and 0.75 silica as SiO 2 .
- the rest corresponds to compounds of more than 20 existing elements in small quantities. 90% of the disintegrated particles of this dry material are less than 5.2 ⁇ m in size.
- the porous texture of this material has an average specific surface area of 6 m 2 g "1 with textural development centered on macroporosity (pores with a diameter of 50-10,000 nm) and absence of micropores.
- Socal P2V calcium carbonate supplied by Solvay and Bentonite del Paraná supplied by Oil-Dry Corporation As raw materials, Socal P2V calcium carbonate supplied by Solvay and Bentonite del Paraná supplied by Oil-Dry Corporation is used; both materials in powder form. 332.6 g are mixed. of bentonite, with a humidity of 7%, with 705 g. of calcium carbonate, with a humidity of 0.7%. After obtaining a homogeneous mixture, it is taken to a double sigma kneader and kneading is started by slowly adding deionized water; once the addition of water is finished, kneading is maintained for 4 hours. The mass thus obtained is formed by an extruder obtaining hollow cylinders 10 mm long, 4.5 mm outside diameter and 2.5 mm inside diameter. Shaped parts, air dried at room temperature for 24 hours and subsequently treated at 15O 0 C for 24 hours in air and 700 0 C for 2 hours in air.
- the hollow cylinders thus obtained have a specific surface area of 30 m 2 g "1 , a negligible micropore volume, a mesopore volume of 0.08 cm 3 g " 1 and a macropore volume of 0.68 cm 3 g "1 .
- the mechanical properties of the cylinders obtained are suitable for industrial use; thus, its structure proved to be perfectly stable to water or water vapor.
- the material prepared in the previous example is tested to determine its adsorption capacity in a dynamic regime.
- the tests are carried out at temperatures of 20-24 0 C and a pressure close to atmospheric.
- the air to be treated contains 4% molar volume of water and 700 ppm of SO2. It operates at a spatial velocity of 2014 h "1 (CN.) And at a linear velocity of passage of gases through the bed of 0.2 Nrrrs "1 ;
- the adsorption of SO 2 is measured to a concentration at the output of 50 ppm.
- hollow, fluted cylinders 10 mm long, 5 mm outside diameter and 3 mm inside diameter are prepared, using as raw materials bentonite supplied by Tolsa, SA (Spain) with the designation Atox and calcareous algae supplied by Algarea Mineragáo Industria e Comercio Ltda. (Brazil).
- SA Sand
- Atox and calcareous algae supplied by Algarea Mineragáo Industria e Comercio Ltda.
- the weight ratio bentonite / seaweed is 20:80.
- the thermal treatment of shaped depressions and dried cylinders is carried out at 500 0 C for 4 hours in air.
- the product obtained has a BET surface of 15 m z g "1 and a total pore volume of 0.20 cm 3- g " 1 of which 0.15 cm 3- g "1 corresponds to the volume occupied by the macropores.
- the filling density of the product is 0.58 g cm 3 and its water adsorption capacity is 0.18 g of water per gram of product.
- Example 3 A first product in accordance with what is described in Example 3, which is a heat treatment at temperature of 500 0 C for four hours in air is prepared. Thus, a second product similar to that described in Example 3 is prepared, although the heat treatment is carried out at 400 0 C for 4 hours. Finally, a third product is prepared with thermal treatment at 300 0 C for 4 hours. The products are mixed in the ratio 1: 1: 1 by weight for use as fertilizer in a soybean plantation in the proportion of 300-350 Kg / Ha. obtaining an average productivity, measured in Tm / Ha. greater than 10% by weight with respect to the planting area used as a reference.
- the size classification - micro, meso and macro - used in this document is the one adopted by the IUPAC "Manual of Symbols and Terminology of Physicochemical Quantities and Units "E. Butterworths. London (1972).
- the values of the pore volumes and specific surface area of the materials were determined by mercury intrusion and by nitrogen adsorption following the BET procedure.
- the wet sawdust provides the environment suitable for the proliferation of microorganisms such as bacteria, fungi and mites that negatively interfere with the health of the birds.
- the new technology developed consists of replacing the coatings made with sawdust by the use of a product with a "macaroni" format, produced by the extrusion of natural mineral products.
- the nails of the legs develop much more since the animal has a tendency to dig in the hard soil and at this time the friction of the nails in the macaroni absorbs a very important amount of calcium carbonate and minerals, for this reason, the fingers they develop much more due to the size of the nails and the calcification of the entire structure of the animal's legs.
- macaroni as an embodiment of the floor covering of farms, directly provides the following benefits for birds:
- the birds feed on the macaroni that carries carbonates and minerals in its composition.
- the birds tend to bite and ingest the macaroni that, due to its composition in carbonates and minerals, accelerate the activation of the stomach of the animal, reducing the ammonia content that at the same time modifies the composition of the waste and decreasing their liquid content.
- This complementary feeding activity will cause the significant decrease in the ammonium content that is generated in the digestion process to occur in the stomach of birds. This reduction of the ammonium content takes place due to the neutralization of the ammonium with the carbonates and minerals present in the macaroni, which favors the digestion process and modifies the composition of the feces, making them drier.
- the reduction of the moisture content in the feces of the birds contributes directly to the reduction of the humidity of the farm floor.
- the humidity of the farm floor is also reduced due to the absorption of this moisture by the macaroni formation structure.
- thermophilic reactions that occur inside the macaroni transform the ammonia present in the environment into ammonium carbonate, which is a natural sanitation agent.
- the generation of ammonium carbonate together with the reduction of moisture content in the farm floor are conditions that do not favor the growth of bacteria, fungi and mites, providing a healthier environment for the growth of birds.
- the properties of the materials according to the invention are mentioned: Contribution of Ca-Mineralization NH 3 adsorbents and water Odor adsorbents Relative humidity regulators
- the paste-transformed material due to the adsorption of the droppings and footsteps of the birds has a high content of N, P, K, carbonates, trace elements and organic matter and thus becomes a nutrient contribution for soils in agriculture as fertilizer.
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Abstract
Description
COMPOSICIÓN DE UN MATERIAL CON ESTRUCTURA POROSA, PROCEDIMIENTO PARA PREPARAR UNA COMPOSICIÓN Y USO DE COMPOSITION OF A MATERIAL WITH POROUS STRUCTURE, PROCEDURE TO PREPARE A COMPOSITION AND USE OF
UNA COMPOSICIÓNA COMPOSITION
SECTOR DE LA TÉCNICASECTOR OF THE TECHNIQUE
La invención se refiere a nuevos materiales con estructura porosa y a su utilización industrial en Ia eliminación de gases y vapores ácidos y a su empleo en Ia agricultura como fertilizantes de suelos.The invention relates to new materials with porous structure and their industrial use in the elimination of acid gases and vapors and their use in agriculture as soil fertilizers.
ESTADO DE LA TÉCNICASTATE OF THE TECHNIQUE
La eliminación de compuestos indeseables presentes en los efluentes industriales ha sido objeto de numerosos estudios y desarrollos tecnológicos con el fin de evitar su emisión a Ia atmósfera.The elimination of undesirable compounds present in industrial effluents has been the subject of numerous studies and technological developments in order to avoid their emission into the atmosphere.
El anhídrido sulfuroso y los óxidos de nitrógeno, que son los compuestos junto con el amoniaco que más contribuyen a Ia formación de lluvia acida, se generan principalmente en las unidades que incineran combustibles fósiles o sus derivados.The sulphurous anhydride and nitrogen oxides, which are the compounds together with the ammonia that contribute most to the formation of acid rain, are generated mainly in the units that incinerate fossil fuels or their derivatives.
Entre las tecnologías desarrolladas para Ia eliminación de gases y vapores ácidos, el tratamiento con suspensiones acuosas de carbonatos, hidróxidos y óxido de elementos alcalinos y alcalinotérreos o sus mezclas es el proceso utilizado en Ia mayoría de las instalaciones de desulfuración.Among the technologies developed for the elimination of gases and acid vapors, the treatment with aqueous suspensions of carbonates, hydroxides and oxide of alkaline and alkaline earth elements or their mixtures is the process used in most desulfurization facilities.
En estos procesos el SO2 es absorbido en el agua y el ácido formado debe neutralizarse para que pueda continuar Ia absorción del SO2. La velocidad a Ia que se produce esta neutralización condiciona Ia rapidez con Ia que el SO2 es absorbido en el líquido. Generalmente, este proceso utiliza carbonato calcico. La escasa solubilidad de este compuesto limita Ia concentración de cationes de calcio en el agua y, con ello, Ia velocidad de neutralización del SO2 absorbido; consecuentemente esta reacción es Ia etapa de control del proceso global. En estos procesos, por vía húmeda, es necesario utilizar relaciones elevadas de líquido/sólido, largos tiempos de contacto y Ia adición eventual de aditivos para mantener el pH del sistema.In these processes the SO2 is absorbed in water and the acid formed must be neutralized in order to continue the absorption of SO2. The speed at which this neutralization occurs determines the speed with which SO 2 is absorbed in the liquid. Generally, this process uses calcium carbonate. The low solubility of this compound limits the concentration of calcium cations in the water and, thus, the neutralization rate of the absorbed SO2; consequently this reaction is the stage of control of the global process. In these processes, by wet route, it is necessary to use high liquid / solid ratios, long contact times and the possible addition of additives to maintain the pH of the system.
A pesar de su extensa implementación, esta tecnología por vía húmeda presenta importantes problemas tecnológicos. Son especialmente graves Ia fijación indeseable de sólidos en las paredes de los depósitos o tubos y las frecuentes obturaciones de las tuberías y conductos; ambos fenómenos indeseables se causan por Ia transformación de sulfito de calcio en sulfato de calcio (yeso) por Ia acción del oxígeno presente en los gases a tratar. De este modo, los materiales de construcción de estas unidades están expuestos a los efectos de fenómenos de corrosión, erosión y abrasión, especialmente en zonas de contacto con las suspensiones, fangos o pastas utilizados en el proceso.Despite its extensive implementation, this wet technology presents important technological problems. The undesirable fixing of solids in the walls of the tanks or tubes and the frequent clogging of the pipes and ducts are especially serious; Both undesirable phenomena are caused by the transformation of calcium sulphite into calcium sulfate (gypsum) by the action of oxygen present in the gases to be treated. Thus, the construction materials of these units are exposed to the effects of corrosion, erosion and abrasion phenomena, especially in areas of contact with the suspensions, sludge or pastes used in the process.
Otras dificultades adicionales son Ia gestión y el tratamiento de los fangos y del agua excedentes del proceso, que deben cumplir las reglamentaciones vigentes en cada país para su descarga.Other additional difficulties are the management and treatment of excess sludge and water from the process, which must comply with the regulations in force in each country for discharge.
Para solucionar estas dificultades se han propuesto numerosos procedimientos. Por ejemplo, en las patentes US 4.690.807, US 5.362.458 y US 6.221.325 están sustituidas las suspensiones acuosas de compuestos sólidos por una solución de sulfato de amonio, en Ia que el sulfito y bisulfito de amonio formados se oxidan a sulfato y bisulfato de amonio que, mediante tratamiento con amoniaco, se transforman en sulfato de amonio en dos etapas de reacción; en Ia patente US 4.035.470, se utilizan compuestos de cobre o hierro para inhibir Ia oxidación de sulfito a sulfato. La mayoría de las propuestas registradas mejoran aspectos del proceso aunque, en muchos casos, aumentan Ia complejidad del sistema y su dificultad operativa.To solve these difficulties, numerous procedures have been proposed. For example, in US patents 4,690,807, US 5,362,458 and US 6,221,325 the aqueous suspensions of solid compounds are substituted by a solution of ammonium sulfate, in which the sulphite and ammonium bisulfite formed are oxidized to sulfate and ammonium bisulfate which, by treatment with ammonia, is transformed into ammonium sulfate in two reaction stages; in US 4,035,470, copper or iron compounds are used to inhibit the oxidation of sulphite to sulfate. Most of the registered proposals improve aspects of the process although, in many cases, they increase the complexity of the system and its operational difficulty.
Por otra parte, son conocidas ciertas arcillas que presentan propiedades plásticas, es decir, suficientemente húmedas, son deformables cuando se aplica una leve presión manteniendo Ia forma, y que se vuelven rígidas al secarse y vitreas cuando se someten a altas temperaturas. En general son filosilicatos naturales compuestos por pequeñas partículas o cristales, generalmente de tamaño coloidal, que dan lugar a materiales de gran desarrollo superficial con capacidad tanto de adsorción física como de interacción química.On the other hand, certain clays are known that have plastic properties, that is, sufficiently moist, they are deformable when a slight pressure is applied while maintaining the shape, and they become rigid when dried and vitreous when subjected to high temperatures. In general they are natural phyllosilicates composed of small particles or crystals, generally of colloidal size, which give rise to materials of great surface development with capacity for both physical adsorption and chemical interaction.
La mayoría de las arcillas plásticas puede incorporar como carga otros materiales en forma de polvo. Por ejemplo, Larsson B. K. y col. (J. Amer, OiI Chem. Soc. 64365-70, 1987) describen Ia preparación de mezclas de montmorillonita calcica con carbono activado para Ia eliminación de benzopireno presente como impureza en aceites comestibles. Con este mismo objetivo, en Ia patente US 5.218.112 se utiliza una esmectita que contiene dentro de su textura carbono activado formado por carbonización de aceite previamente adsorbido. De este modo, Yates M. y col. (Studies in Surface Science and Catalysis, 160, pp. 233-240, 2007) estudian Ia incorporación de dióxido de titanio en Ia estructura de bentonita como posible soporte de catalizadores.Most plastic clays can incorporate other materials in powder form as fillers. For example, Larsson B. K. et al. (J. Amer, OiI Chem. Soc. 64365-70, 1987) describe the preparation of mixtures of calcium montmorillonite with activated carbon for the elimination of benzopyrene present as an impurity in edible oils. With this same objective, in the US patent 5,218,112 a smectite is used that contains within its texture activated carbon formed by carbonization of previously adsorbed oil. Thus, Yates M. et al. (Studies in Surface Science and Catalysis, 160, pp. 233-240, 2007) study the incorporation of titanium dioxide in the structure of bentonite as a possible catalyst support.
La bentonita es una arcilla de grano muy fino del tipo de Ia montmorillonita y presenta una estructura y composición química que Ie confiere una alta superficie específica, alta capacidad de intercambio catiónico, gran plasticidad y facilidad de moldeo. El material conformado de bentonita puede incorporar como carga cantidades importantes de diferentes materiales entre los que se encuentran los carbonatos de calcio o de magnesio; este hecho supone una vía de gran interés para Ia preparación de compuestos adsorbentes/reactivos de gases ácidos con geometría adecuada para su utilización industrial.Bentonite is a very fine grain clay of the montmorillonite type and has a chemical structure and composition that confers a high specific surface area, high cation exchange capacity, great plasticity and ease of molding. The bentonite shaped material may incorporate as a load significant amounts of different materials, including calcium carbonates or magnesium; This fact is a way of great interest for the preparation of adsorbent / reactive compounds of acid gases with geometry suitable for industrial use.
La bentonita se utiliza en numerosos productos y procesos (Kendall,Bentonite is used in numerous products and processes (Kendall,
T., 1996 Industrial Minerals, mayo, pp. 25-37); su utilización es conocida para Ia mejora de suelos arenosos o ácidos cuyo efecto podría potenciarse por Ia incorporación en su estructura de compuestos que no solo contengan elementos de interés en Ia preparación del suelo sino que introduzcan, a diferencia de los fertilizantes sólidos convencionales, Ia macroporosidad necesaria para facilitar los procesos biológicos deseables, como es el caso de Ia mayoría de las algas.T., 1996 Industrial Minerals, May, pp. 25-37); Its use is known for the improvement of sandy or acidic soils whose effect could be enhanced by the incorporation into its structure of compounds that not only contain elements of interest in soil preparation but also introduce macroporosity, unlike conventional solid fertilizers. necessary to facilitate desirable biological processes, as is the case with most algae.
DESCRIPCIÓN DE LA INVENCIÓNDESCRIPTION OF THE INVENTION
La presente invención se refiere a nuevos materiales, con estructura porosa, conformados preferentemente como cilindros huecos, a su utilización industrial en Ia eliminación de gases y vapores ácidos y a su empleo en Ia agricultura como fertilizantes de suelos.The present invention relates to new materials, with porous structure, preferably formed as hollow cylinders, their industrial use in the elimination of acid gases and vapors and their use in agriculture as soil fertilizers.
La presente invención se refiere a una composición de material adsorbente/reactivo caracterizada porque incluye bentonita junto con carbonatos de elementos alcalinotérreos de origen mineral u orgánico, en este caso procedente de algas calcáreas.The present invention relates to a composition of adsorbent / reagent material characterized in that it includes bentonite together with carbonates of alkaline earth elements of mineral or organic origin, in this case from calcareous algae.
Para Ia preparación de los materiales objeto de esta invención se mezclan, en seco y de forma homogénea, polvos de bentonita y de los carbonatos seleccionados; posteriormente, Ia mezcla se amasa con agua en una amasadora de alto cizallamiento. Cuando las partículas de bentonita se amasan de manera adecuada en un medio acuoso (o en cualquier otro disolvente polar), se produce una masa pseudoplástica que incorpora con gran facilidad las partículas del carbonato. La masa obtenida tras el amasado se moldea o extruye para obtener Ia forma deseada y se seca después preferiblemente a temperatura ambiente durante al menos 2 horas y a 80-150° C durante al menos cuatro horas; posteriormente el material se trata térmicamente entre 300°C y 900°C durante al menos 2 horas en aire.For the preparation of the materials object of this invention, bentonite powders and selected carbonates are mixed dry and homogeneously; subsequently, the mixture is kneaded with water in a high shear kneader. When the bentonite particles are adequately kneaded in an aqueous medium (or in any other polar solvent), a pseudoplastic mass is produced that easily incorporates the carbonate particles. The mass obtained after kneading is molded or extruded to obtain the desired shape and then preferably dried at room temperature for at least 2 hours and at 80-150 ° C for at least four hours; subsequently the material is heat treated between 300 ° C and 900 ° C for at least 2 hours in air.
Cuando Ia masa húmeda obtenida con estos materiales se conforma en estructuras de cilindros huecos de dimensiones adecuadas, se pueden obtener materiales adsorbentes con importantes ventajas operativas para Ia depuración de fluidos en régimen dinámico o para su incorporación al suelo como fertilizante o potencializador de fertilizantes convencionales.When the wet mass obtained with these materials is formed in hollow cylinder structures of suitable dimensions, adsorbent materials can be obtained with important operational advantages for the purification of fluids in dynamic regime or for incorporation into the soil as a fertilizer or fertilizer potentializer of conventional fertilizers.
Estos cilindros huecos pueden ser del tipo "macarrón" liso, estriado, recto, curvo, de corte regular o irregular, de cualquier forma y tamaño. En su aplicación para Ia eliminación de gases y vapores ácidos, el paso del fluido a depurar a través del material adsorbente dispuesto en esta forma geométrica, da lugar a una dinámica de fluido que combina un régimen turbulento provocado por el flujo que pasa entre los cilindros con un régimen laminar que tiene lugar en el paso del fluido por el interior de los cilindros huecos. Esta situación da lugar a un comportamiento singular que mejora de modo significativo Ia eficacia del fenómeno de adsorción si se compara con las unidades conformadas en colmena donde el fluido pasa a través de ella según un régimen laminar. En su aplicación como fertilizante, el material ofrece mayor superficie de contacto por unidad de volumen que los sistemas que contienen pellas o materiales macizos y su estructura macroporosa facilita el espacio adecuado para un mejor desarrollo de los procesos biológicos deseables.These hollow cylinders can be of the "macaroni" type smooth, striated, straight, curved, regular or irregular cut, of any shape and size. In its application for the elimination of acid gases and vapors, the passage of the fluid to be purified through the adsorbent material arranged in this geometric form, gives rise to a fluid dynamic that combines a turbulent regime caused by the flow that passes between the cylinders with a laminar regime that takes place in the passage of the fluid inside the hollow cylinders. This situation gives rise to a unique behavior that significantly improves the effectiveness of the adsorption phenomenon when compared to the units formed in a hive where the fluid passes through it according to a laminar regime. In its application as a fertilizer, the material offers greater contact area per unit volume than systems containing pellets or solid materials and its macroporous structure provides adequate space for a better development of desirable biological processes.
La presente invención se refiere además a un procedimiento para preparar las composiciones indicadas anteriormente. Según una realización preferente del procedimiento, esta incluye las siguientes etapas:The present invention further relates to a process for preparing the compositions indicated above. According to a preferred embodiment of the process, this includes the following steps:
a) mezclar polvos de bentonita y carbonato calcico hasta obtener una mezcla de polvos homogénea, b) amasar Ia mezcla homogénea de polvos obtenida con adición de agua para obtener una pasta húmeda, c) conformar Ia pasta húmeda en forma de cilindros huecos, d) secar las piezas conformadas al aire y a temperatura ambiente al menos durante 2 horas y entre 80 y 15O0C al menos durante 4 horas, preferentemente durante 24 horas. e) tratar térmicamente las piezas a temperaturas comprendidas entre 65O0C y 9000C, preferentemente entre 7000C y 8000C, durante al menos 2 horas, preferiblemente durante al menos 4 horas.a) mix bentonite and calcium carbonate powders until a homogeneous powder mixture, b) kneading the homogeneous powder mixture obtained with the addition of water to obtain a wet paste, c) forming the wet paste in the form of hollow cylinders, d) drying the shaped pieces in the air and at room temperature for at least during 2 hours and between 80 and 15O 0 C for at least 4 hours, preferably for 24 hours. e) heat treating the parts at temperatures between 65O 0 C and 900 0 C, preferably between 700 0 C and 800 0 C, for at least 2 hours, preferably for at least 4 hours.
Según esta realización y, preferiblemente en Ia etapa a), se mezcla exclusivamente bentonita y carbonato calcico con una proporción de bentonita entre 20 y 30% en peso.According to this embodiment and, preferably in step a), bentonite and calcium carbonate are mixed exclusively with a proportion of bentonite between 20 and 30% by weight.
Tratamientos térmicos del material preparado con bentonita y carbonato calcico a temperaturas inferiores a 4000C dan lugar a piezas demasiado sensibles a Ia abrasión y al desmoronamiento de Ia estructura física por efecto del agua. Estas limitaciones desaparecen prácticamente cuando el material se trata durante tiempos superiores a 2 horas a temperaturas comprendidas entre 5000C y 8000C. A partir de 6000C, el carbonato se transforma en óxido de calcio con desprendimiento de CO2. A temperaturas de 7000C durante un tiempo no inferior a 2 horas, todos los carbonatas se descomponen.Heat treatments of the material prepared with bentonite and calcium carbonate at temperatures below 400 0 C give rise to pieces that are too sensitive to abrasion and the collapse of the physical structure due to water. These limitations practically disappear when the material is treated for times greater than 2 hours at temperatures between 500 0 C and 800 0 C. From 600 0 C, the carbonate is transformed into calcium oxide with CO2 evolution. At temperatures of 700 0 C for a time not less than 2 hours, all carbonates break down.
Las piezas conformadas y estabilizadas térmicamente a 7000C presentan un alto contendido en macroporos nuevos, originados principalmente por los huecos o espacios que se originan por el desprendimiento del anhídrido carbónico. En consecuencia, se observa un aumento en el valor del volumen total de poros con Ia temperatura y el tiempo de tratamiento; para Ia composición inicial carbonato cálcico/bentonita de 70:30, las piezas tratadas a 600°C/2 h presentan un volumen total de poros de 0,27 ml g~1, para 700°C/2 h el valor aumenta a 0,76 mi g"1, y para 800°C/2h pasa a 0,79 mi g"1.The pieces formed and thermally stabilized at 700 0 C have a high content of new macropores, mainly caused by the gaps or spaces that are caused by the evolution of carbon dioxide. Consequently, an increase in the value of the total pore volume is observed with the temperature and the treatment time; for the initial composition calcium carbonate / bentonite of 70:30, the pieces treated at 600 ° C / 2 h have a total pore volume of 0.27 ml g ~ 1 , for 700 ° C / 2 h the value increases to 0.76 mi g "1 , and for 800 ° C / 2h it goes to 0.79 mi g " 1 .
La presente invención se refiere también al uso de una composición realizada tal como se ha descrito anteriormente, como material adsorbente/reactivo para eliminación de gases y vapores ácidos en régimen dinámico. Cuando los gases contaminados con dióxidos de azufre, ácido clorhídrico o ácido fluorhídrico o sus mezclas se hacen pasar a través de este material en forma de cilindro hueco, se produce Ia reacción de estos gases ácidos con el óxido de calcio que contiene, formándose con eficacia extraordinaria el sulfito, sulfato, cloruros y fluoruros de calcio que quedan depositados rellenando los poros del material. El material saturado, dispuesto en un lecho móvil, puede sustituirse con facilidad (por ejemplo, mediante un sistema neumático) por el material fresco sin problemas de corrosión, depósitos, o tratamiento de lodos.The present invention also relates to the use of a composition made as described above, as an adsorbent / reagent material for the elimination of acid gases and vapors in a dynamic regime. When gases contaminated with sulfur dioxides, hydrochloric acid or hydrofluoric acid or mixtures thereof are passed through this material in the form of a hollow cylinder, the reaction of these acid gases with the calcium oxide it contains occurs, effectively forming extraordinary sulfite, sulfate, chlorides and calcium fluorides that are deposited filling the pores of the material. The saturated material, arranged in a moving bed, can easily be replaced (for example, by a pneumatic system) by the fresh material without problems of corrosion, deposits, or sludge treatment.
El carbonato calcico utilizado puede ser de origen mineral o pueden emplearse también algas calcáreas de alto contenido en dicha sal con rendimientos semejantes.The calcium carbonate used may be of mineral origin or high-calcareous algae can also be used in said salt with similar yields.
De este modo, estos materiales cuando son tratados en Ia etapa e) a temperaturas entre 5000C y 6000C durante al menos 2 horas, pueden utilizarse como agentes neutralizantes o remineralizantes para tratamiento de aguas, bajando su contenido en CO2 y proporcionando los iones carbonato y bicarbonato necesarios.Thus, when these materials are treated in stage e) at temperatures between 500 0 C and 600 0 C for at least 2 hours, they can be used as neutralizing or remineralizing agents for water treatment, lowering their CO 2 content and providing the necessary carbonate and bicarbonate ions.
Según otra realización particular preferente del procedimiento, éste incluye las siguientes etapas:According to another particular preferred embodiment of the process, this includes the following steps:
a) mezclar polvos de bentonita y alga calcárea hasta obtener una mezcla de polvos homogénea, b) amasar Ia mezcla homogénea de polvos obtenida con adición de agua para obtener una pasta húmeda, c) conformar Ia pasta húmeda en forma de cilindros huecos, d) secar las piezas conformadas al aire y a temperatura ambiente por Io menos durante 2 horas y entre 80 y 15O0C al menos durante 4 horas, preferentemente durante 24 horas, e) tratar térmicamente las piezas a temperaturas comprendidas entre 3000C y 6000C, preferentemente entre 4000C y 5000C, durante al menos 2 horas, preferiblemente durante al menos 4 horas en aire.a) mixing bentonite and calcareous algae powders until a homogeneous powder mixture is obtained, b) kneading the homogeneous powder mixture obtained with the addition of water to obtain a wet paste, c) form the wet paste in the form of hollow cylinders, d) dry the shaped parts in air and at room temperature for at least 2 hours and between 80 and 15 ° C at least for 4 hours, preferably for 24 hours, e) heat treating the parts at temperatures between 300 0 C and 600 0 C, preferably between 400 0 C and 500 0 C, for at least 2 hours, preferably for at least 4 hours in air.
Según esta realización y, preferiblemente en Ia etapa a), se mezclan bentonita y alga calcárea con una proporción de bentonita de 10 y 15% en peso.According to this embodiment and, preferably in step a), bentonite and calcareous algae are mixed with a proportion of bentonite of 10 and 15% by weight.
El material preparado con bentonita y alga calcárea con contenido en bentonita de 10% y tratado a 5000C durante 4 horas en aire presenta una superficie específica de 7 m2g"1 y un volumen total de poros de 0,28 mi g"1.The material prepared with bentonite and calcareous algae with a 10% bentonite content and treated at 500 0 C for 4 hours in air has a specific surface area of 7 m 2 g "1 and a total pore volume of 0.28 mi g " 1 .
La presente invención se refiere también al uso de una composición realizada tal como se ha descrito anteriormente, como material fertilizante y de mejora de suelos ácidos o arenosos, introduciendo los numerosos elementos nutrientes presentes en el alga calcárea y ofreciendo una forma de cilindro hueco con paredes macroporosas que favorecen de manera extraordinaria los fenómenos biológicos que intervienen en el crecimiento de las plantas.The present invention also relates to the use of a composition made as described above, as a fertilizer and acidic or sandy soil improvement material, introducing the numerous nutrient elements present in the calcareous algae and offering a hollow cylinder shape with walls. macroporous that favor in an extraordinary way the biological phenomena that take part in the growth of the plants.
En otra aplicación, los cilindros preparados de este modo se utilizan como lechos (recubrimiento temporal del suelo) en granjas de aves que mejoran Ia salubridad de Ia instalación, favorecen el engorde de los animales e incrementan Ia calidad del producto.In another application, the cylinders prepared in this way are used as beds (temporary covering of the soil) in poultry farms that improve the health of the installation, favor the fattening of the animals and increase the quality of the product.
La bentonita utilizada como materia prima en esta invención fue suministrada por Tolsa S.A. con Ia denominación Atox, con una superficie específica BET de 130 m2 g"1 y un tamaño de partícula de 75% inferior a 45 μm. De este modo, se utilizó una bentonita natural suministrada por Oil-Dry Corporation denominada Bentonita del Paraná con una superficie específica BET de 95 m2 g"1 y un tamaño de partícula de 82% inferior a 44 μm.The bentonite used as raw material in this invention was supplied by Tolsa SA under the name Atox, with a surface BET specific of 130 m 2 g "1 and a particle size of 75% less than 45 μm. Thus, a natural bentonite supplied by Oil-Dry Corporation called Bentonite of Paraná with a specific BET surface of 95 m 2 was used g "1 and a particle size of 82% less than 44 μm.
El carbonato calcico precipitado utilizado en esta invención denominado SOCAL P2V fue suministrado por el Grupo Solvay con una pureza de 98,8%, un tamaño de partícula medio de 1 ,5 μm y una superficie específica de 7 m2 g"1.The precipitated calcium carbonate used in this invention called SOCAL P2V was supplied by the Solvay Group with a purity of 98.8%, an average particle size of 1.5 μm and a specific surface area of 7 m 2 g "1 .
El alga calcárea fue suministrada por Algarea Mineragáo Industria e Comercio Ltda. (Brasil) y corresponde particularmente a Ia especie Lithothamnium spp. El valor medio de su composición ponderal es de 90,9% de carbonato calcico, 3% de magnesio como Mg y 0,75 de sílice como SiO2. El resto corresponde a compuestos de más de 20 elementos existentes en pequeñas cantidades. El 90% de las partículas disgregadas de este material seco tiene un tamaño inferior a 5,2 μm. La textura porosa de este material presenta una superficie específica media de 6 m2 g"1 con desarrollo textural centrado en Ia macroporosidad (poros de diámetro 50-10.000 nm) y ausencia de microporos.The calcareous algae was supplied by Algarea Mineragáo Industria e Comercio Ltda. (Brazil) and corresponds particularly to the species Lithothamnium spp. The average value of its weight composition is 90.9% calcium carbonate, 3% magnesium as Mg and 0.75 silica as SiO 2 . The rest corresponds to compounds of more than 20 existing elements in small quantities. 90% of the disintegrated particles of this dry material are less than 5.2 μm in size. The porous texture of this material has an average specific surface area of 6 m 2 g "1 with textural development centered on macroporosity (pores with a diameter of 50-10,000 nm) and absence of micropores.
EJEMPLOS DE REALIZACIÓN DE LA INVENCIÓNEXAMPLES OF EMBODIMENT OF THE INVENTION
Los siguientes ejemplos, no limitativos, ilustran adicionalmente Ia presente invención.The following non-limiting examples further illustrate the present invention.
Ejemplo 1Example 1
Como materias primas, se utilizan carbonato calcico Socal P2V suministrado por Solvay y Bentonita del Paraná suministrada por Oil-Dry Corporation; ambos materiales en forma de polvo. Se mezclan 332,6 g. de bentonita, con una humedad del 7%, con 705 g. de carbonato calcico, con una humedad del 0,7%. Tras obtener una mezcla homogénea, esta se lleva a una amasadora de doble sigma y se inicia el amasado añadiendo lentamente agua desionizada; una vez terminada Ia adición de agua, se mantiene el amasado durante 4 horas. La masa así obtenida se conforma mediante una extrusora obteniendo cilindros huecos de 10 mm de longitud, 4,5 mm de diámetro exterior y 2,5 mm de diámetro interior. Las piezas conformadas, se secan al aire a temperatura ambiente durante 24 horas y posteriormente se tratan a 15O0C durante 24 horas en atmósfera de aire y a 7000C durante 2 horas en atmósfera de aire.As raw materials, Socal P2V calcium carbonate supplied by Solvay and Bentonite del Paraná supplied by Oil-Dry Corporation is used; both materials in powder form. 332.6 g are mixed. of bentonite, with a humidity of 7%, with 705 g. of calcium carbonate, with a humidity of 0.7%. After obtaining a homogeneous mixture, it is taken to a double sigma kneader and kneading is started by slowly adding deionized water; once the addition of water is finished, kneading is maintained for 4 hours. The mass thus obtained is formed by an extruder obtaining hollow cylinders 10 mm long, 4.5 mm outside diameter and 2.5 mm inside diameter. Shaped parts, air dried at room temperature for 24 hours and subsequently treated at 15O 0 C for 24 hours in air and 700 0 C for 2 hours in air.
Los cilindros huecos así obtenidos presentan una superficie específica de 30 m2 g"1, un volumen de microporos despreciable, un volumen de mesoporos de 0,08 cm3g"1 y un volumen de macroporos de 0,68cm3g"1. Las propiedades mecánicas de los cilindros obtenidos son adecuadas para su utilización industrial; de este modo, su estructura resultó ser perfectamente estable al agua o al vapor de agua.The hollow cylinders thus obtained have a specific surface area of 30 m 2 g "1 , a negligible micropore volume, a mesopore volume of 0.08 cm 3 g " 1 and a macropore volume of 0.68 cm 3 g "1 . The mechanical properties of the cylinders obtained are suitable for industrial use; thus, its structure proved to be perfectly stable to water or water vapor.
Ejemplo 2Example 2
El material preparado en el ejemplo anterior es ensayado para determinar su capacidad de adsorción en régimen dinámico. Los ensayos se realizan a temperaturas de 20-240C y una presión próxima a Ia atmosférica. El aire a tratar contiene 4% de volumen molar de agua y 700 ppm de SO2. Se opera a una velocidad espacial de 2014 h"1 (CN.) y a una velocidad lineal de paso de los gases a través del lecho de 0,2 Nrrrs"1; Ia adsorción de SO2 se mide hasta una concentración en Ia salida de 50 ppm.The material prepared in the previous example is tested to determine its adsorption capacity in a dynamic regime. The tests are carried out at temperatures of 20-24 0 C and a pressure close to atmospheric. The air to be treated contains 4% molar volume of water and 700 ppm of SO2. It operates at a spatial velocity of 2014 h "1 (CN.) And at a linear velocity of passage of gases through the bed of 0.2 Nrrrs "1; The adsorption of SO 2 is measured to a concentration at the output of 50 ppm.
Tras el ensayo de adsorción el material utilizado aumenta su peso en 46% y su resistencia a Ia compresión pasa de 1 ,0 a 2,2 kg'cm"1. Ejemplo 3After the adsorption test, the material used increases its weight by 46% and its resistance to compression increases from 1.0 to 2.2 kg ' cm "1 . Example 3
Siguiendo el procedimiento expuesto en el ejemplo 1 , se preparan cilindros huecos, estriados de 10 mm de largo, 5 mm de diámetro exterior y 3 mm de diámetro interior, utilizando como materias primas bentonita suministrada por Tolsa, S.A. (España) con Ia denominación Atox y alga calcárea suministrada por Algarea Mineragáo Industria e Comercio Ltda. (Brasil). La relación ponderal bentonita/alga es de 20:80. En este ejemplo, el tratamiento térmico de los cilindros huecos conformados y secos se lleva a cabo a 5000C durante 4 horas en atmósfera de aire.Following the procedure set forth in Example 1, hollow, fluted cylinders 10 mm long, 5 mm outside diameter and 3 mm inside diameter are prepared, using as raw materials bentonite supplied by Tolsa, SA (Spain) with the designation Atox and calcareous algae supplied by Algarea Mineragáo Industria e Comercio Ltda. (Brazil). The weight ratio bentonite / seaweed is 20:80. In this example, the thermal treatment of shaped depressions and dried cylinders is carried out at 500 0 C for 4 hours in air.
El producto obtenido presenta una superficie BET de 15 mzg"1 y un volumen total de poros de 0,20 cm3-g"1 de los que 0,15 cm3-g"1 corresponden al volumen ocupado por los macroporos. La densidad de relleno del producto es de 0,58 g cm3 y su capacidad de adsorción de agua es de 0,18 g de agua por gramo de producto.The product obtained has a BET surface of 15 m z g "1 and a total pore volume of 0.20 cm 3- g " 1 of which 0.15 cm 3- g "1 corresponds to the volume occupied by the macropores. The filling density of the product is 0.58 g cm 3 and its water adsorption capacity is 0.18 g of water per gram of product.
Ejemplo 4Example 4
Se prepara un primer producto conforme a Io descrito en el ejemplo 3, que supone un tratamiento térmico a temperatura de 5000C durante cuatro horas en aire. De este modo, se prepara un segundo producto semejante al descrito en el ejemplo 3, aunque el tratamiento térmico se lleva a cabo a 4000C durante 4 horas. Finalmente, se prepara un tercer producto con tratamiento térmico a 3000C durante 4 horas. Los productos se mezclan en Ia relación 1 :1 :1 en peso para su utilización como fertilizante en una plantación de soja en Ia proporción de 300-350 Kg/Ha. obteniendo una productividad media, medida en Tm/Ha. superior al 10% en peso con respecto al área de plantación utilizada como referencia.A first product in accordance with what is described in Example 3, which is a heat treatment at temperature of 500 0 C for four hours in air is prepared. Thus, a second product similar to that described in Example 3 is prepared, although the heat treatment is carried out at 400 0 C for 4 hours. Finally, a third product is prepared with thermal treatment at 300 0 C for 4 hours. The products are mixed in the ratio 1: 1: 1 by weight for use as fertilizer in a soybean plantation in the proportion of 300-350 Kg / Ha. obtaining an average productivity, measured in Tm / Ha. greater than 10% by weight with respect to the planting area used as a reference.
La clasificación de tamaños -micro, meso y macro- utilizada en este documento es Ia adoptada por Ia IUPAC "Manual of Symbols and Terminology of Physicochemical Quantities and Units" E. Butterworths. Londres (1972). Los valores de los volúmenes de poros y de superficie específica de los materiales se determinaron por intrusión de mercurio y mediante adsorción de nitrógeno siguiendo el procedimiento BET.The size classification - micro, meso and macro - used in this document is the one adopted by the IUPAC "Manual of Symbols and Terminology of Physicochemical Quantities and Units "E. Butterworths. London (1972). The values of the pore volumes and specific surface area of the materials were determined by mercury intrusion and by nitrogen adsorption following the BET procedure.
Utilización de Ia nueva tecnología de producto (macarrón), en Ia preparación del recubrimiento del suelo (lechos), de las granjas de cría de aves.Use of the new product technology (macaroni), in the preparation of the floor covering (beds), of the poultry breeding farms.
Actualmente, los productores de aves utilizan recortes de maderaCurrently, poultry producers use wood clippings
(virutas de madera) para Ia realización de recubrimiento del suelo de las granjas de cría. La finalidad de esta utilización de recubrimiento es evitar el contacto directo de las aves con el suelo y absorber Ia humedad procedente del piso y las heces de las aves durante el periodo de crecimiento.(wood shavings) for the realization of floor covering of breeding farms. The purpose of this coating use is to avoid direct contact of the birds with the ground and absorb moisture from the floor and the feces of the birds during the growth period.
El movimiento de las aves sobre el serrín humedecido durante el periodo de crecimiento, proporciona Ia compactación del recubrimiento. Debido a esta alteración, el recubrimiento queda con una consistencia más dura, obligando a las aves a caminar con las patas extendidas.The movement of the birds on the moistened sawdust during the period of growth, provides the compaction of the coating. Due to this alteration, the coating is left with a harder consistency, forcing the birds to walk with their legs extended.
Normalmente, el serrín húmedo proporciona el ambiente adecuado para Ia proliferación de microorganismos tales como bacterias, hongos y ácaros que interfieren de modo negativo en Ia salud de las aves.Normally, the wet sawdust provides the environment suitable for the proliferation of microorganisms such as bacteria, fungi and mites that negatively interfere with the health of the birds.
La nueva tecnología desarrollada consiste en Ia sustitución de los recubrimientos realizados con serrín por Ia utilización de un producto con formato "macarrón", producido mediante Ia extrusión de productos minerales naturales.The new technology developed consists of replacing the coatings made with sawdust by the use of a product with a "macaroni" format, produced by the extrusion of natural mineral products.
La utilización de esta nueva tecnología evita el contacto directo de las aves con el suelo y también proporciona el contacto de las patas de las aves con un piso de consistencia más suave que modifica de modo natural Ia característica de movimiento de las aves.The use of this new technology avoids the direct contact of the birds with the ground and also provides the contact of the legs of the birds with a softer consistency floor that naturally modifies the bird movement characteristic.
Contrariamente a Ia situación antes descrita, en Ia que las aves caminan con las patas extendidas, Ia utilización del macarrón facilita el movimiento, puesto que las aves utilizan las patas, los dedos y las uñas de modo más uniforme.Contrary to the situation described above, in which the birds walk with the legs extended, the use of the macaroni facilitates movement, since the birds use the legs, fingers and nails more evenly.
Las uñas de las patas se desarrollan mucho más ya que el animal tiene tendencia a excavar en el suelo duro y en este momento Ia fricción de las uñas en los macarrones absorbe una cantidad de carbonato calcico y minerales muy importante, por este motivo, los dedos se desarrollan mucho más debido al tamaño de las uñas y a Ia calcificación de toda Ia estructura de las patas del animal.The nails of the legs develop much more since the animal has a tendency to dig in the hard soil and at this time the friction of the nails in the macaroni absorbs a very important amount of calcium carbonate and minerals, for this reason, the fingers they develop much more due to the size of the nails and the calcification of the entire structure of the animal's legs.
La utilización del macarrón como material de realización del recubrimiento del piso de las granjas, proporciona directamente los beneficios siguientes para las aves:The use of macaroni as an embodiment of the floor covering of farms, directly provides the following benefits for birds:
1. Mineralización de las uñas y de los picos; 2. Mejor calcificación del esqueleto;1. Mineralization of nails and spikes; 2. Better calcification of the skeleton;
3. Aumento de las dimensiones de las uñas con el consiguiente aumento de las dimensiones de los dedos, de las espuelas y de las tibias;3. Increase in the dimensions of the nails with the consequent increase in the dimensions of the fingers, spurs and tibiae;
4. Aumento de Ia proporción del pecho, debido a Ia facilidad de movimiento.4. Increase in the proportion of the chest, due to the ease of movement.
5. Alteración en Ia consistencia de Ia carne de las aves, generando una carne más tierna y sabrosa; y5. Alteration in the consistency of the meat of the birds, generating a more tender and tasty meat; Y
6. Reducción del tiempo de cría.6. Reduction of breeding time.
Además, durante el periodo de crecimiento, las aves se alimentan del macarrón que lleva en su composición carbonatos y minerales. Adicionalmente, durante el periodo de crecimiento, las aves tienden a picar y a ingerir los macarrones que, por su composición en carbonatos y minerales, aceleran Ia activación del estómago del animal, reduciendo el contenido de amoniaco que al mismo tiempo modifica Ia composición de los residuos y disminuyendo el contenido de líquidos de los mismos. Esta actividad complementaria de alimentación hará que se produzca en el estómago de las aves Ia disminución significativa del contenido de amonio que se genera en el proceso de digestión. Esta reducción del contenido de amonio tiene lugar debido a Ia neutralización del amonio con los carbonatos y minerales presentes en el macarrón, que favorece el proceso de digestión y modifica Ia composición de las heces, haciéndolas más secas.In addition, during the growth period, the birds feed on the macaroni that carries carbonates and minerals in its composition. Additionally, during the growth period, the birds tend to bite and ingest the macaroni that, due to its composition in carbonates and minerals, accelerate the activation of the stomach of the animal, reducing the ammonia content that at the same time modifies the composition of the waste and decreasing their liquid content. This complementary feeding activity will cause the significant decrease in the ammonium content that is generated in the digestion process to occur in the stomach of birds. This reduction of the ammonium content takes place due to the neutralization of the ammonium with the carbonates and minerals present in the macaroni, which favors the digestion process and modifies the composition of the feces, making them drier.
La reducción del contenido de humedad en las heces de las aves contribuye directamente a Ia reducción de Ia humedad del piso de Ia granja.The reduction of the moisture content in the feces of the birds contributes directly to the reduction of the humidity of the farm floor.
La humedad del piso de Ia granja también se reduce debido a Ia absorción de esta humedad por Ia estructura de formación del macarrón. Al mismo tiempo, reacciones termófilas que se producen en el interior del macarrón transforman el amoniaco presente en el ambiente en carbonato de amonio, que es un agente de saneamiento natural.The humidity of the farm floor is also reduced due to the absorption of this moisture by the macaroni formation structure. At the same time, thermophilic reactions that occur inside the macaroni transform the ammonia present in the environment into ammonium carbonate, which is a natural sanitation agent.
La generación del carbonato de amonio junto con Ia reducción del contenido de humedad en el piso de Ia granja, son condiciones que no favorecen el crecimiento de las bacterias, de los hongos y de los ácaros, proporcionando un ambiente más saludable para el crecimiento de las aves. Se citan las propiedades de los materiales según Ia invención: Aporte de Ca-Mineralización Adsorbentes de NH3 y agua Adsorbentes de olores Reguladores de humedad relativaThe generation of ammonium carbonate together with the reduction of moisture content in the farm floor are conditions that do not favor the growth of bacteria, fungi and mites, providing a healthier environment for the growth of birds. The properties of the materials according to the invention are mentioned: Contribution of Ca-Mineralization NH 3 adsorbents and water Odor adsorbents Relative humidity regulators
Tiempo de vida útil superior a los materiales utilizados en Ia actualidad. Los efectos en el crecimiento y desarrollo de las especies pueden resumirse del modo siguiente:Lifetime exceeds the materials used today. The effects on the growth and development of the species can be summarized as follows:
Crecimiento:Increase:
.Disposición postural de las aves que permite un mayor desarrollo de los dedos y patas por contacto directo. Mineralización de los huesosPostural disposition of the birds that allows a greater development of the fingers and legs by direct contact. Bone mineralization
.Incremento de Ia absorción de nutrientes por ingestión..Increase the absorption of nutrients by ingestion.
Desarrollo:Developing:
.Aumento permanente de masa en las patas y en el pecho.Permanent increase in mass in the legs and chest
.Refuerzo del esqueleto .Refuerzo de Ia cascara de los huevosReinforcement of the skeleton. Reinforcement of the eggshell
.Reducción de Ia concentración de amoniaco de las heces.Reduction of the concentration of ammonia in the feces
.Reducción de problemas oculares y respiratorios.Reduction of eye and respiratory problems
.Mejora de Ia calidad del aire.Improvement of air quality
.Mejora del aspecto de las aves. Beneficios:.Improved bird appearance. Benefits:
.Aumento de Ia masa molecular en menos tiempo.Increased molecular mass in less time
.Reducción del periodo de engorde.Reduction of the fattening period
.Reducción de enfermedades infecciosas.Reduction of infectious diseases
.Aumento de Ia productividad .Mayor tiempo de duración del lecho.Increase in productivity. Longer bed time
.Aplicación posterior del material -> abono agrícola..After application of the material -> agricultural fertilizer.
En este caso, el material transformado en pasta por efecto de Ia adsorción de los excrementos y de las pisadas de las aves tiene alto contenido en N, P, K, carbonatos, oligoelementos y materia orgánica y se convierte así en un aporte de nutrientes para suelos en agricultura como abono. In this case, the paste-transformed material due to the adsorption of the droppings and footsteps of the birds has a high content of N, P, K, carbonates, trace elements and organic matter and thus becomes a nutrient contribution for soils in agriculture as fertilizer.
Claims
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| BRPI0803394-3A BRPI0803394A2 (en) | 2008-08-08 | 2008-08-08 | composition of a porous structure material, method for preparing a composition and use of a composition |
| BRPI0803394-3 | 2008-08-08 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO2010015724A1 true WO2010015724A1 (en) | 2010-02-11 |
Family
ID=41663303
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/ES2009/070331 Ceased WO2010015724A1 (en) | 2008-08-08 | 2009-08-03 | Composition of a material having a porous structure, composition preparation method and use of composition |
Country Status (4)
| Country | Link |
|---|---|
| AR (1) | AR073264A1 (en) |
| BR (1) | BRPI0803394A2 (en) |
| UY (1) | UY32039A (en) |
| WO (1) | WO2010015724A1 (en) |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4387653A (en) * | 1980-08-04 | 1983-06-14 | Engelhard Corporation | Limestone-based sorbent agglomerates for removal of sulfur compounds in hot gases and method of making |
| US4671208A (en) * | 1984-12-07 | 1987-06-09 | International Packaging, Inc. | Clay and limestone composition |
| US6752850B1 (en) * | 1999-06-18 | 2004-06-22 | Ultimate Products (Aust) Pty Ltd | Liquid soil conditioner |
| WO2007085672A1 (en) * | 2006-01-27 | 2007-08-02 | Bionatur Biotechnologies S.L. | Adsorbent composition containing enstatite, method for obtaining same and use thereof |
-
2008
- 2008-08-08 BR BRPI0803394-3A patent/BRPI0803394A2/en not_active IP Right Cessation
-
2009
- 2009-08-03 WO PCT/ES2009/070331 patent/WO2010015724A1/en not_active Ceased
- 2009-08-05 AR ARP090103003A patent/AR073264A1/en unknown
- 2009-08-06 UY UY0001032039A patent/UY32039A/en not_active Application Discontinuation
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4387653A (en) * | 1980-08-04 | 1983-06-14 | Engelhard Corporation | Limestone-based sorbent agglomerates for removal of sulfur compounds in hot gases and method of making |
| US4671208A (en) * | 1984-12-07 | 1987-06-09 | International Packaging, Inc. | Clay and limestone composition |
| US6752850B1 (en) * | 1999-06-18 | 2004-06-22 | Ultimate Products (Aust) Pty Ltd | Liquid soil conditioner |
| WO2007085672A1 (en) * | 2006-01-27 | 2007-08-02 | Bionatur Biotechnologies S.L. | Adsorbent composition containing enstatite, method for obtaining same and use thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| AR073264A1 (en) | 2010-10-28 |
| UY32039A (en) | 2010-03-26 |
| BRPI0803394A2 (en) | 2010-08-03 |
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