ES2296521A1 - Clay monoliths for the treatment of contaminant gaseous effluents - Google Patents
Clay monoliths for the treatment of contaminant gaseous effluents Download PDFInfo
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- ES2296521A1 ES2296521A1 ES200601272A ES200601272A ES2296521A1 ES 2296521 A1 ES2296521 A1 ES 2296521A1 ES 200601272 A ES200601272 A ES 200601272A ES 200601272 A ES200601272 A ES 200601272A ES 2296521 A1 ES2296521 A1 ES 2296521A1
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- monoliths
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- treatment
- clays
- effluents
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- 239000004927 clay Substances 0.000 title claims description 22
- 239000000356 contaminant Substances 0.000 title abstract description 4
- 230000007613 environmental effect Effects 0.000 claims abstract description 7
- 239000000654 additive Substances 0.000 claims abstract description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 4
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical group CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 claims description 14
- 239000000203 mixture Substances 0.000 claims description 8
- 229940078552 o-xylene Drugs 0.000 claims description 7
- 238000001179 sorption measurement Methods 0.000 claims description 7
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 6
- 239000000126 substance Substances 0.000 claims description 6
- 239000003344 environmental pollutant Substances 0.000 claims description 4
- 229910052500 inorganic mineral Inorganic materials 0.000 claims description 4
- 239000011707 mineral Substances 0.000 claims description 4
- 231100000719 pollutant Toxicity 0.000 claims description 4
- 239000010453 quartz Substances 0.000 claims description 4
- YGANSGVIUGARFR-UHFFFAOYSA-N dipotassium dioxosilane oxo(oxoalumanyloxy)alumane oxygen(2-) Chemical compound [O--].[K+].[K+].O=[Si]=O.O=[Al]O[Al]=O YGANSGVIUGARFR-UHFFFAOYSA-N 0.000 claims description 3
- 229910052627 muscovite Inorganic materials 0.000 claims description 3
- 229910021532 Calcite Inorganic materials 0.000 claims description 2
- 229910052656 albite Inorganic materials 0.000 claims description 2
- 238000006555 catalytic reaction Methods 0.000 claims description 2
- 150000001875 compounds Chemical class 0.000 claims description 2
- NLYAJNPCOHFWQQ-UHFFFAOYSA-N kaolin Chemical compound O.O.O=[Al]O[Si](=O)O[Si](=O)O[Al]=O NLYAJNPCOHFWQQ-UHFFFAOYSA-N 0.000 claims description 2
- 229910052622 kaolinite Inorganic materials 0.000 claims description 2
- 229910052902 vermiculite Inorganic materials 0.000 claims description 2
- 239000010455 vermiculite Substances 0.000 claims description 2
- 235000019354 vermiculite Nutrition 0.000 claims description 2
- 229910052784 alkaline earth metal Inorganic materials 0.000 claims 2
- 239000012072 active phase Substances 0.000 claims 1
- 239000003513 alkali Substances 0.000 claims 1
- 150000001342 alkaline earth metals Chemical class 0.000 claims 1
- 238000000034 method Methods 0.000 abstract description 10
- 239000000463 material Substances 0.000 abstract description 9
- 238000005516 engineering process Methods 0.000 abstract description 7
- 239000012855 volatile organic compound Substances 0.000 abstract description 7
- 230000008569 process Effects 0.000 abstract description 6
- 238000004519 manufacturing process Methods 0.000 abstract description 4
- 239000000843 powder Substances 0.000 abstract description 3
- 238000013461 design Methods 0.000 abstract description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 6
- 239000003463 adsorbent Substances 0.000 description 6
- 238000012360 testing method Methods 0.000 description 6
- 238000001125 extrusion Methods 0.000 description 5
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- 229910052799 carbon Inorganic materials 0.000 description 4
- 238000003915 air pollution Methods 0.000 description 3
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 3
- 229910052782 aluminium Inorganic materials 0.000 description 3
- 238000004458 analytical method Methods 0.000 description 3
- 239000011777 magnesium Substances 0.000 description 3
- 239000012229 microporous material Substances 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 238000005033 Fourier transform infrared spectroscopy Methods 0.000 description 2
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 2
- 230000003197 catalytic effect Effects 0.000 description 2
- 239000000919 ceramic Substances 0.000 description 2
- 230000002860 competitive effect Effects 0.000 description 2
- 238000003795 desorption Methods 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 230000018109 developmental process Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- 229910052710 silicon Inorganic materials 0.000 description 2
- 239000010703 silicon Substances 0.000 description 2
- 239000002689 soil Substances 0.000 description 2
- 229910004261 CaF 2 Inorganic materials 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- JLVVSXFLKOJNIY-UHFFFAOYSA-N Magnesium ion Chemical compound [Mg+2] JLVVSXFLKOJNIY-UHFFFAOYSA-N 0.000 description 1
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 description 1
- 241001448434 Pirex Species 0.000 description 1
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical class [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 1
- 238000002441 X-ray diffraction Methods 0.000 description 1
- -1 active carbons Substances 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 229910000323 aluminium silicate Inorganic materials 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 239000012159 carrier gas Substances 0.000 description 1
- 150000001768 cations Chemical class 0.000 description 1
- 238000003889 chemical engineering Methods 0.000 description 1
- 239000002734 clay mineral Substances 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 238000012669 compression test Methods 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000005202 decontamination Methods 0.000 description 1
- 230000003588 decontaminative effect Effects 0.000 description 1
- 238000002845 discoloration Methods 0.000 description 1
- 239000002270 dispersing agent Substances 0.000 description 1
- 230000008030 elimination Effects 0.000 description 1
- 238000003379 elimination reaction Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 230000009931 harmful effect Effects 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 238000011065 in-situ storage Methods 0.000 description 1
- 239000010423 industrial mineral Substances 0.000 description 1
- 238000002329 infrared spectrum Methods 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 239000003014 ion exchange membrane Substances 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 229910001425 magnesium ion Inorganic materials 0.000 description 1
- 239000011572 manganese Substances 0.000 description 1
- 229910052748 manganese Inorganic materials 0.000 description 1
- 239000013335 mesoporous material Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000003973 paint Substances 0.000 description 1
- 238000010422 painting Methods 0.000 description 1
- 239000000123 paper Substances 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000004014 plasticizer Substances 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000004445 quantitative analysis Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000007420 reactivation Effects 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 230000002441 reversible effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000007493 shaping process Methods 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 241000894007 species Species 0.000 description 1
- 238000004611 spectroscopical analysis Methods 0.000 description 1
- 230000001988 toxicity Effects 0.000 description 1
- 231100000419 toxicity Toxicity 0.000 description 1
- 239000010457 zeolite Substances 0.000 description 1
Classifications
-
- 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
- B01D53/02—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 by adsorption, e.g. preparative gas chromatography
-
- 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
-
- 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
- B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
- B01J21/16—Clays or other mineral silicates
-
- B01J35/56—
-
- 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
- C04B33/00—Clay-wares
- C04B33/02—Preparing or treating the raw materials individually or as batches
- C04B33/04—Clay; Kaolin
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2253/00—Adsorbents used in seperation treatment of gases and vapours
- B01D2253/10—Inorganic adsorbents
- B01D2253/106—Silica or silicates
- B01D2253/11—Clays
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2253/00—Adsorbents used in seperation treatment of gases and vapours
- B01D2253/30—Physical properties of adsorbents
- B01D2253/34—Specific shapes
- B01D2253/342—Monoliths
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/70—Organic compounds not provided for in groups B01D2257/00 - B01D2257/602
- B01D2257/708—Volatile organic compounds V.O.C.'s
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Dispersion Chemistry (AREA)
- Materials Engineering (AREA)
- Ceramic Engineering (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Health & Medical Sciences (AREA)
- Biomedical Technology (AREA)
- Environmental & Geological Engineering (AREA)
- Structural Engineering (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Abstract
Description
Monolitos de arcilla para el tratamiento de efluentes gaseosos contaminantes.Clay monoliths for the treatment of gaseous pollutant effluents.
La invención es de aplicación en el desarrollo comercial de filtros, tanto en forma de tamices como monolíticos, constituidos por arcillas como tecnología de protección medioambiental, fundamentalmente en el tratamiento de efluentes gaseosos contaminados.The invention is applicable in development commercial filters, both in the form of sieves and monolithic, constituted by clays as protection technology environmental, mainly in the treatment of effluents contaminated soda
Es bien conocido que las arcillas naturales son minerales constituidos por partículas cristalinas pequeñas cuya estructura consiste en capas de tetraedros formados por iones silicio coordinados con cuatro oxígenos, alternadas con otras capas en las que iones aluminio o magnesio están coordinados octaédricamente con seis oxígenos o grupos hidroxilo. Durante el proceso de formación de una arcilla el aluminio puede reemplazar al silicio en las capas de tetraedros, mientras que hierro, magnesio, manganeso y otros cationes de tamaño similar pueden sustituir al aluminio en las capas octaédricas (ver, por ejemplo, Grim, R.E. en Clay Mineralogy, Mc Graw Hill, New York, 1968). Estos aluminosilicatos son muy abundantes en la naturaleza al ser el resultado de los múltiples procesos de envejecimiento, en su mayoría con participación del agua, que sufren los constituyentes primigenios del suelo (ver, por ejemplo, Sposito, G. en The Chemistry of Soils, Oxford University Press, New York, 1989). Su abundancia asociada a un coste relativamente bajo y a sus interesantes propiedades físico-químicas justifican su uso tradicional en cerámica, papel, pinturas, plásticos, como soporte químico, en membranas de intercambio iónico, en decoloración de fluidos, etc., e incluso, de manera más reciente, en otras aplicaciones más avanzadas como la catálisis (ver, por ejemplo, Ciullo, P.A. en Industrial Minerals and their uses: a handbook and formulary; William Andrew Inc., New Jersey, 1996). A pesar de todo este bagaje de experiencia y conocimiento en torno a las arcillas, todavía se anuncian mejoras en las técnicas que se emplean para su extracción y procesado (ver, por ejemplo, Murray, H. en Applied Clay Science; vol. 17, pág. 207-221, 2000).It is well known that natural clays are minerals consisting of small crystalline particles whose structure consists of layers of tetrahedra formed by ions silicon coordinated with four oxygen, alternated with other layers in which aluminum or magnesium ions are coordinated octahedrally with six oxygens or hydroxyl groups. During the process of forming a clay the aluminum can replace the silicon in the layers of tetrahedra, while iron, magnesium, manganese and other cations of similar size may replace the aluminum in the octahedral layers (see, for example, Grim, R.E. in Clay Mineralogy, Mc Graw Hill, New York, 1968). These aluminosilicates are very abundant in nature to be the result of multiple aging processes, mostly with the participation of water, which the constituents suffer soil primitives (see, for example, Sposito, G. in The Chemistry of Soils, Oxford University Press, New York, 1989). its abundance associated with a relatively low cost and its interesting physicochemical properties justify its traditional use in ceramics, paper, paints, plastics, as chemical support, in ion exchange membranes, in fluid discoloration, etc., and even more recently, in other more advanced applications such as catalysis (see, for example, Ciullo, P.A. in Industrial Minerals and their uses: a handbook and formulary; William Andrew Inc., New Jersey, 1996). TO in spite of all this background of experience and knowledge around the clays are still announced improvements in the techniques that are used for extraction and processing (see, for example, Murray, H. in Applied Clay Science; vol. 17, p. 207-221, 2000).
El norte de Marruecos es una zona geográfica en la que abundan los minerales de naturaleza arcillosa, lo que representa un potencial enorme para el desarrollo de la economía local. Sin embargo, es de destacar que hasta el presente estas arcillas sólo están siendo utilizadas como materia prima para la fabricación de objetos de cerámica tradicional, de escaso valor en el mercado y nulo interés tecnológico.The north of Morocco is a geographical area in the abundant minerals of clay nature, which It represents a huge potential for the development of the economy local. However, it is noteworthy that until now you are clays are only being used as raw material for manufacture of traditional ceramic objects, of low value in the market and zero technological interest.
Esta situación contrasta con la existencia en la
zona o en sus alrededores de diferentes industrias que emiten al
aire diversos contaminantes, entre ellos Compuestos Orgánicos
Volátiles (COVs), sustancias de procedencia muy variada y
reconocida toxicidad y que, por ello, han sido seleccionadas en este
estudio para chequear el rendimiento del material elaborado a
escala de laboratorio. La emisión de COVs a partir de industrias
químicas y petroquímicas se ha convertido desde hace años, no sólo
en Marruecos sino a nivel mundial, en una de las formas más
preocupantes de contaminación atmosférica debido a los múltiples
efectos nocivos que provocan tanto en los seres humanos como en el
medio ambiente (ver, por ejemplo, Heck, R.M. et al. en
Catalytic air pollution control: Commercial technology; pág.
281-305; John Wiley, New York, 2002). En muchos
casos, estas emisiones proceden de procesos industriales que
utilizan disolventes, polímeros y resinas tales como los implicados
en operaciones de pintura y recubrimiento (ver, por ejemplo, Kiely,
G. en Environmental Engineering, McGraw Hill, Berkshire, UK, 1997).
Entre las muy diversas tecnologías desarrolladas para eliminar COVs
en aire contaminado, la adsorción es quizás una de las más
utilizadas (ver, por ejemplo, Hocking, M.B. en Handbook of chemical
technology and pollution control; Academia Press, San Diego, 1998;
y Khan, F.I. y Ghoshal, A.K. en Journal of Loss prevention in the
Process Industries, vol. 13, pág.
527-545,
2000).This situation contrasts with the existence in the area or in its surroundings of different industries that emit various pollutants into the air, among them Volatile Organic Compounds (VOCs), substances of very varied origin and recognized toxicity and that, therefore, have been selected in this study to check the performance of the material elaborated on a laboratory scale. The emission of VOCs from chemical and petrochemical industries has become for years, not only in Morocco but worldwide, in one of the most worrisome forms of air pollution due to the multiple harmful effects they cause both in humans as in the environment (see, for example, Heck, RM et al . in Catalytic air pollution control: Commercial technology; p. 281-305; John Wiley, New York, 2002). In many cases, these emissions come from industrial processes that use solvents, polymers and resins such as those involved in painting and coating operations (see, for example, Kiely, G. in Environmental Engineering, McGraw Hill, Berkshire, UK, 1997) . Among the very diverse technologies developed to eliminate VOCs in polluted air, adsorption is perhaps one of the most used (see, for example, Hocking, MB in Handbook of chemical technology and pollution control; Academia Press, San Diego, 1998; and Khan , FI and Ghoshal, AK in Journal of Loss prevention in the Process Industries, vol. 13, p.
527-545, 2000).
En este sentido, se han probado con éxito muchos materiales diversos tales como carbones activos, zeolitas, alúminas, sílices e incluso polímeros (ver, por ejemplo, Ruthven, D.M. en Principles of adsorption processes; John Wiley, New York, 1984; Gélin et al. en Microporous Materials; vol. 4, pág. 283-290, 1995; Takeuchi et al. en Separations Technology; vol. 5, pág. 23-24, 1995; Carsten et al. en Microporous and Mesoporous Materials; vol. 35, pág. 349-365, 2000; y Marsh, H. en Activated carbon compendium; Elsevier, Amsterdam, 2001). Sin embargo, aún hay un continuo esfuerzo por encontrar adsorbentes que asocien eficiencia con bajo coste, como lo demuestran nuestras propias investigaciones recientes en las que hemos comparado el rendimiento de tierras de diatomeas con el de sílice comercial (ver, por ejemplo, Zaitan, H. y Chafik, T. en Comptes Rendus Chimie; vol. 8, pág. 1701-1709, 2005), o estudiado las posibilidades como adsorbentes de COVs tanto de monolitos a base de carbón natural activados tras la extrusión (ver, por ejemplo, Gatica, J.M. et al. en Comptes Rendus Chimie; en prensa) como de diversos minerales arcillosos procedentes de Marruecos en forma de polvo (ver, por ejemplo, Harti, S. et al. en Applied Clay Science; enviado).In this sense, many diverse materials such as active carbons, zeolites, aluminas, silicas and even polymers have been successfully tested (see, for example, Ruthven, DM in Principles of adsorption processes; John Wiley, New York, 1984; Gélin et al . in Microporous Materials; vol. 4, p. 283-290, 1995; Takeuchi et al . in Separations Technology; vol. 5, p. 23-24, 1995; Carsten et al . in Microporous and Mesoporous Materials; vol. 35, pp. 349-365, 2000; and Marsh, H. in Activated carbon compendium; Elsevier, Amsterdam, 2001). However, there is still a continuous effort to find adsorbents that associate efficiency with low cost, as evidenced by our own recent research in which we have compared the yield of diatomaceous earths with that of commercial silica (see, for example, Zaitan, H and Chafik, T. in Comptes Rendus Chimie; vol. 8, p. 1701-1709, 2005), or studied the possibilities as adsorbents of VOCs of both natural carbon-based monoliths activated after extrusion (see, for example, Gatica, JM et al . In Comptes Rendus Chimie; in press) as various clay minerals from Morocco in powder form (see, for example, Harti, S. et al . In Applied Clay Science; sent).
En relación con el diseño de estos adsorbentes, frente a los más convencionales como los basados en lechos de partículas, las estructuras monolíticas en forma de panal de abeja ofrecen probadas ventajas tales como baja caída de presión en caudales gaseosos con alta velocidad espacial, así como menores requerimientos de peso y espacio, lo que las vuelve especialmente atractivas en aplicaciones medioambientales (ver, por ejemplo, Heck, R.M. en Catalytic air pollution control: Commercial technology; pág. 11-24, John Wiley, New York, 2002). Sin embargo, para que una pasta sea extruible debe poseer unas propiedades reológicas muy específicas que le permitan ser conformada con una estructura rígida como la de un monolito (ver, por ejemplo, Avila, P. et al. en Chemical Engineering Journal, vol. 109, pág. 11-36, 2005). Esto hace que el proceso de extrusión sea a menudo tedioso y requiera un gran número de ensayos empleando diversos aditivos que mejoren la plasticidad (ver, por ejemplo Gatica, J.M. et al. en Carbon; vol. 42, pag. 3251-3254, 2004; y Mohino, F. et al. en Applied Clay Science; vol. 29, pag. 125-136, 2005). En este sentido, la utilización de diferentes aditivos que aportan propiedades aglomerantes, plastificantes, lubricantes y dispersantes a los materiales de base (ver, por ejemplo, Gatica, J.M. et al. en Carbon; vol. 42, pág. 3251-3254) comporta un evidente coste económico tanto por su uso como por el tratamiento térmico posterior que debe realizarse para su eliminación y la necesaria reactivación de la capacidad de adsorción. Además puede inducir efectos negativos en las propiedades químico-estructurales del material de base tanto por la interacción directa como por el posterior tratamiento indicado (ver, por ejemplo, Velde, B. en Origin and Mineralogy of Clays: Clays and Environment; Springer, Berlin, 1995).In relation to the design of these adsorbents, compared to the more conventional ones such as those based on particle beds, monolithic structures in the form of honeycomb offer proven advantages such as low pressure drop in gaseous flows with high spatial velocity, as well as lower weight and space requirements, which makes them especially attractive in environmental applications (see, for example, Heck, RM in Catalytic air pollution control: Commercial technology; p. 11-24, John Wiley, New York, 2002). However, for a paste to be extrudable, it must have very specific rheological properties that allow it to be shaped with a rigid structure such as that of a monolith (see, for example, Avila, P. et al . In Chemical Engineering Journal, vol. 109, p. 11-36, 2005). This makes the extrusion process often tedious and requires a large number of tests using various additives that improve plasticity (see, for example, Gatica, JM et al . In Carbon; vol. 42, page 3251-3254, 2004 ; and Mohino, F. et al . in Applied Clay Science; vol. 29, p. 125-136, 2005). In this sense, the use of different additives that provide binder, plasticizer, lubricant and dispersant properties to the base materials (see, for example, Gatica, JM et al . In Carbon; vol. 42, p. 3251-3254) entails an obvious economic cost both for its use and for the subsequent heat treatment that must be carried out for its elimination and the necessary reactivation of the adsorption capacity. It can also induce negative effects on the chemical-structural properties of the base material both by direct interaction and by the subsequent treatment indicated (see, for example, Velde, B. in Origin and Mineralogy of Clays: Clays and Environment; Springer, Berlin , nineteen ninety five).
Con los antecedentes expuestos, es evidente que seria muy interesante conseguir que un material abundante y barato como lo son las arcillas naturales que abundan en el norte de Marruecos pudieran también utilizarse como adsorbente de compuestos orgánicos volátiles, sin prejuicio de que esta aplicación pudiera extrapolarse a la depuración de otros contaminantes que habitualmente están presentes en los efluentes gaseosos generados por cualquier tipo de actividad humana. Esto daría un valor añadido al producto ya existente a la vez que aportaría un nuevo material competitivo frente a los que ya se vienen empleando en aplicaciones de descontaminación ambiental. Asimismo, sería de gran interés conseguir que a partir de estas arcillas se pudieran obtener filtros o soportes monolíticos y, aún más si cabe, que la metodología de fabricación no implicase el uso de aditivos para facilitar el proceso de extrusión.With the background exposed, it is clear that it would be very interesting to get an abundant and cheap material as are the natural clays that abound in the north of Morocco could also be used as an adsorbent of compounds volatile organic, without prejudice that this application could extrapolate to the clearance of other contaminants that they are usually present in the gaseous effluents generated for any type of human activity. This would give added value. to the existing product while contributing a new material competitive compared to those already used in applications of environmental decontamination. It would also be of great interest get that from these clays filters could be obtained or monolithic supports and, even more so, that the methodology of manufacturing does not involve the use of additives to facilitate the extrusion process
Se proponen dos arcillas procedentes específicamente de depósitos localizados en el área de Tetuán, aunque son muy abundantes en todo el norte de Marruecos. La arcilla denominada FERA contiene diversos minerales de acuerdo con el análisis de difracción de rayos X: cuarzo, moscovita, vermiculita, caolinita y albita. Por su parte, el análisis de la otra arcilla, denominada TEFA, indica que está compuesta de cuarzo, calcita, moscovita y clinocloro. Desde el punto de vista elemental, el análisis químico mediante Espectroscopia de Energía Dispersiva (EDS) revela que la composición media de las arcillas (% en peso) es, en el caso de la arcilla FERA, 0 (39,3%), Si (23,4%), Fe (16,3%), Al (13,2%), K (5,3%), Mg (0,8%), Ca (0,6%), C (0,4%), Ti (0,4%) y Na (0,3%); y en el caso de la arcilla TEFA: 0 (44,4%), Si (21,3%), Al (9,2%), Fe (8,9%), Ca (5,8%), C (5,1%), K (2,8%), Mg (1,9%), Ti (0,2%), Cl (0,2%) y S (0,2%).Two clays are proposed specifically from deposits located in the Tetouan area, although they are very abundant in all the north of Morocco. Clay called FERA contains various minerals according to the X-ray diffraction analysis: quartz, muscovite, vermiculite, kaolinite and albite. For its part, the analysis of the other clay, called TEFA, it indicates that it is composed of quartz, calcite, Muscovite and Clinochlor. From the elementary point of view, the Chemical analysis using Dispersive Energy Spectroscopy (EDS) reveals that the average clay composition (% by weight) is, in the case of clay FERA, 0 (39.3%), Si (23.4%), Fe (16.3%), Al (13.2%), K (5.3%), Mg (0.8%), Ca (0.6%), C (0.4%), Ti (0.4%) and Na (0.3%); and in the case of TEFA clay: 0 (44.4%), Si (21.3%), Al (9.2%), Fe (8.9%), Ca (5.8%), C (5.1%), K (2.8%), Mg (1.9%), Ti (0.2%), Cl (0.2%) and S (0.2%).
Antes de cualquier uso, las arcillas en forma de polvo han sido molidas y tamizadas a un tamaño medio de grano de 180 micras.Before any use, clays in the form of powder have been ground and sieved to an average grain size of 180 microns
Para probar su potencial de aplicación en el tratamiento de efluentes gaseosos contaminados se ha estudiado su capacidad de adsorción de compuestos orgánicos volátiles y, en particular, se ha elegido o-xileno como modelo por ser uno de los más habituales en las emisiones de muchas industrias de la zona. Los ensayos se han realizado en condiciones dinámicas a presión atmosférica en un dispositivo instrumental ya descrito en la bibliografía (ver, por ejemplo, Zaitan, H. y Chafik, T. en Comptes Rendus Chimie; vol. 8, pág. 1701-1709). Se ha utilizado nitrógeno como gas portador de vapores de o-xileno, preparando una mezcla que contiene 3600 ppm de contaminante mediante un saturador asociado a un condensador que está inmerso en un baño termostático para mantener la temperatura a 10\pm0,5ºC. El flujo total de la mezcla durante los ensayos fue de 100 cm^{3} min^{-1}. Los tests de adsorción se han llevado a cabo a 27ºC en un reactor de cuarzo con 1 gramo de la arcilla, que previamente se ha sometido a un tratamiento in situ en flujo de 100 cm^{3} min^{-1} de N_{2} a 210ºC durante 30 minutos para limpiar su superficie de especies previamente adsorbidas. Una vez que se alcanza la saturación de la muestra, se hace pasar por ella un flujo de N_{2} puro (100 cm^{3} min^{-1}) para inducir la desorción térmica a 27ºC hasta que la concentración de o-xileno a la salida del reactor se haga cero. A continuación se realiza un experimento de Desorción Térmica Programada (DTP) usando una velocidad de calentamiento de la muestra de 5ºC min^{-1}. La composición de la mezcla gaseosa a la salida del reactor se ha monitorizado mediante un espectrofotómetro FTIR (modelo Jasco 410) registrando espectros infrarrojos con una resolución de análisis de 4 cm^{-1}, usando para ello una celda construida en vidrio Pirex con ventanas de CaF_{2} e integrando las bandas FTIR características de o-xileno en la región comprendida entre 2600 y 3200 cm^{-1}. El análisis cuantitativo de estas bandas se ha llevado a cabo en base a un calibrado previo realizado con mezclas de concentración de o-xileno conocida.In order to test its application potential in the treatment of contaminated gaseous effluents, its ability to adsorb volatile organic compounds has been studied and, in particular, o-xylene has been chosen as a model because it is one of the most common emissions in many industries from the area The tests have been carried out under dynamic conditions at atmospheric pressure in an instrumental device already described in the literature (see, for example, Zaitan, H. and Chafik, T. in Comptes Rendus Chimie; vol. 8, p. 1701-1709) . Nitrogen has been used as a carrier gas for o-xylene vapors, preparing a mixture containing 3600 ppm of contaminant by means of a saturator associated with a condenser that is immersed in a thermostatic bath to maintain the temperature at 10 ± 0.5 ° C. The total flow of the mixture during the tests was 100 cm 3 min -1. The adsorption tests have been carried out at 27 ° C in a quartz reactor with 1 gram of the clay, which has previously undergone an in situ flow treatment of 100 cm 3 min -1 of N_ {2} at 210 ° C for 30 minutes to clean its surface of previously adsorbed species. Once the sample saturation is reached, a flow of pure N2 (100 cm3 min -1) is passed through to induce thermal desorption at 27 ° C until the concentration of o-xylene at the outlet of the reactor becomes zero. A Programmed Thermal Desorption (DTP) experiment is then performed using a sample heating rate of 5 ° C min -1. The composition of the gas mixture at the outlet of the reactor has been monitored by an FTIR spectrophotometer (Jasco 410 model) recording infrared spectra with an analysis resolution of 4 cm -1, using a cell built in Pirex glass with CaF 2 windows and integrating the FTIR bands characteristic of o-xylene in the region between 2600 and 3200 cm -1. The quantitative analysis of these bands has been carried out based on a previous calibration performed with mixtures of known o-xylene concentration.
Siguiendo el tratamiento numérico de datos descrito en la bibliografía (ver, por ejemplo, Gatica, J.M. et al. en Comptes Rendus Chimie, en prensa) se ha comprobado que, en las condiciones experimentales indicadas, las arcillas FERA y TEFA tienen una capacidad de adsorción total de o-xileno a 27ºC de 157 y 156 \mumol g^{-1} respectivamente. Estas cantidades, aunque inferiores a las de otros adsorbentes en el mercado, son comparables a las de otros materiales estudiados en la bibliografía (ver por ejemplo, Zaitan, H. y Chafik, T. en Comptes Rendus Chimie; vol. 8, pág. 1701-1709, 2005) y pueden considerarse aceptables si se tiene en cuenta que no se ha realizado ningún esfuerzo por mejorar la textura de las arcillas, que según nuestros estudios previos demostró corresponder en ambos casos a la de un material no microporoso con una superficie en torno a los 40 m^{2} g^{-1}. Además, se ha observado que la mayor parte de la cantidad adsorbida (81% en el caso de FERA y 74% en el de TEFA) corresponde a un tipo de adsorción reversible (eliminable a temperatura ambiente) y que ambas arcillas pueden regenerarse completamente a baja temperatura (65ºC y 100ºC respectivamente) lo que añade un mayor atractivo a los resultados obtenidos. No debe perderse de vista que las arcillas estudiadas son muy económicas si se comparan con otros materiales. Su precio estimado es de 30 euros por tonelada (excluidos los costes de transporte) lo que, unido a los resultados comentados, las convierte en un potencial adsorbente muy competitivo.Following the numerical data treatment described in the literature (see, for example, Gatica, JM et al . In Comptes Rendus Chimie, in press) it has been found that, under the indicated experimental conditions, the FERA and TEFA clays have a capacity to total adsorption of o-xylene at 27 ° C of 157 and 156 µg g -1, respectively. These quantities, although lower than those of other adsorbents in the market, are comparable to those of other materials studied in the literature (see for example, Zaitan, H. and Chafik, T. in Comptes Rendus Chimie; vol. 8, p. 1701-1709, 2005) and can be considered acceptable if one takes into account that no effort has been made to improve the texture of the clays, which according to our previous studies proved to correspond in both cases to that of a non-microporous material with a surface around 40 m 2 g -1. Furthermore, it has been observed that most of the adsorbed amount (81% in the case of FERA and 74% in the case of TEFA) corresponds to a reversible adsorption type (removable at room temperature) and that both clays can be completely regenerated at low temperature (65ºC and 100ºC respectively) which adds more attractiveness to the results obtained. It should not be forgotten that the clays studied are very economical when compared to other materials. Its estimated price is 30 euros per ton (excluding transport costs) which, together with the results mentioned, makes them a very competitive adsorbent potential.
Adicionalmente se ha estudiado la posibilidad de extrusión de las dos arcillas en forma de monolitos de tipo panal de abeja siguiendo la metodología previamente descrita en la bibliografía (ver, por ejemplo, Gatica, J.M. et al. en Carbon; vol. 42, pág. 3251-3254, 2004). El resultado de este estudio ha demostrado que ambas arcillas cumplen con los requisitos necesarios para ser extruidas al poseer un límite líquido (LL) y un índice de plasticidad (IP) adecuado: LL = 49,2% y IP = 28,8% en el caso de la arcilla denominada FERA, y LL = 51,2% y IP = 28,8% en el caso de TEFA.Additionally, the possibility of extrusion of the two clays in the form of honeycomb monoliths has been studied following the methodology previously described in the literature (see, for example, Gatica, JM et al . In Carbon; vol. 42, p. 3251-3254, 2004). The result of this study has shown that both clays meet the necessary requirements to be extruded by having a liquid limit (LL) and an adequate plasticity index (IP): LL = 49.2% and IP = 28.8% in the case of clay called FERA, and LL = 51.2% and IP = 28.8% in the case of TEFA.
Las predicciones han sido confirmadas al conseguir la extrusión en una máquina extrusora capaz de conformar monolitos de sección cuadrada en forma de panal de abeja con una densidad de 4 celdas cm^{-2}, en configuraciones de 2x2 y 4x4, y con un espesor de pared de 1,3 mm. Para preparar la pasta a extruir no se han precisado más aditivos que agua, añadida en cantidades de 0,325 ml y 0,4 ml por gramo empleado de arcilla FERA y TEFA, respectivamente. Tras obtener los monolitos, éstos se secaron en estufa a 90ºC durante una noche, obteniendo muestras como las de la Figura 1.The predictions have been confirmed at achieve extrusion in an extruder machine capable of shaping Honeycomb square section monoliths with a density of 4 cm-2 cells, in 2x2 and 4x4 configurations, and with a wall thickness of 1.3 mm. To prepare the paste to extrude no more additives than water have been required, added in amounts of 0.325 ml and 0.4 ml per gram used of FERA and TEFA clay, respectively. After obtaining the monoliths, they were dried in stove at 90 ° C overnight, obtaining samples such as those from the Figure 1.
La resistencia mecánica de los monolitos se ha determinado mediante ensayos de compresión realizados en una Máquina Universal de Ensayos Mecánicos Shimadzu AG-IS capaz de trabajar a una presión máxima de 100 kN. Este estudio ha revelado que los monolitos de la arcilla FERA y TEFA resisten presiones ejercidas en el sentido de los canales (longitudinal) de 2,53 MPa y 1,62 MPa respectivamente.The mechanical resistance of the monoliths has determined by compression tests performed on a Universal Shimadzu Mechanical Testing Machine AG-IS capable of working at a maximum pressure of 100 kN. This study has revealed that FERA clay monoliths and TEFA resist pressures exerted in the direction of the channels (longitudinal) of 2.53 MPa and 1.62 MPa respectively.
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