ES2339081A1 - Procedure for the treatment and degradation of toxic gases of organic origin through photocatalytic techniques. (Machine-translation by Google Translate, not legally binding) - Google Patents

Procedure for the treatment and degradation of toxic gases of organic origin through photocatalytic techniques. (Machine-translation by Google Translate, not legally binding) Download PDF

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ES2339081A1
ES2339081A1 ES200701090A ES200701090A ES2339081A1 ES 2339081 A1 ES2339081 A1 ES 2339081A1 ES 200701090 A ES200701090 A ES 200701090A ES 200701090 A ES200701090 A ES 200701090A ES 2339081 A1 ES2339081 A1 ES 2339081A1
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organic
catalyst
toxic
degradation
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ES2339081B1 (en
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Francisco J. Araña Mesa
Jose Miguel Doña Rodriguez
Jesus Perez Peña
Oscar Manuel Gonzalez Diaz
Jose Alberto Herrera Melian
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Universidad de las Palmas de Gran Canaria
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Universidad de las Palmas de Gran Canaria
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    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61LMETHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
    • A61L9/00Disinfection, sterilisation or deodorisation of air
    • A61L9/16Disinfection, sterilisation or deodorisation of air using physical phenomena
    • A61L9/18Radiation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation 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
    • B01D53/007Separation 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 irradiation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation 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
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/74General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/86Catalytic processes
    • B01D53/8668Removing organic compounds not provided for in B01D53/8603 - B01D53/8665

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Environmental & Geological Engineering (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Epidemiology (AREA)
  • Toxicology (AREA)
  • Biomedical Technology (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Animal Behavior & Ethology (AREA)
  • General Health & Medical Sciences (AREA)
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Abstract

Procedure for the treatment and degradation of toxic gases of organic origin by photocatalytic techniques. The present invention refers to a method of treatment and degradation of toxic gases of organic origin that allows to transform and mineralize gases of organic origin, decontaminating in this way the emission of gases. It is a continuous process that involves passing an air flow containing vapors of toxic organic gas to demineralize through a reactor (3) in whose inner walls a catalyst has been impregnated and applying a source of radiation (2), by means of photocatalytic techniques, the flow of air in contact with the catalyst is obtained as a final result of the process the mineralization of the toxic gas of organic origin through the oxidation of organic compounds up to co 2 or less toxic species. (Machine-translation by Google Translate, not legally binding)

Description

Procedimiento para el tratamiento y degradación de gases tóxicos de origen orgánico mediante técnicas fotocatalíticas.Procedure for treatment and degradation of toxic gases of organic origin using techniques Photocatalytic

Sector de la técnicaTechnical sector

La presente invención hace referencia a un procedimiento para el tratamiento y degradación de gases tóxicos de origen orgánico mediante técnicas fotocatalíticas.The present invention refers to a procedure for the treatment and degradation of toxic gases of Organic origin through photocatalytic techniques.

Estado de la técnicaState of the art

En las últimas décadas ha habido una preocupación creciente por controlar y tratar las emisiones gaseosas producidas en los distintos procesos industriales o cotidianos debidos a la actividad del hombre. Así en 1997 los gobiernos de 55 naciones acordaron mediante el Protocolo de Kyoto reducir un 5,2% las emisiones de gases de efecto invernadero responsables del cambio climático. Entre estos gases se encuentran principalmente el dióxido de carbono (CO_{2}), metano (CH_{4}), óxido nitroso (N_{2}O), hidrofluorados (HFC), perfluorocarbonos (PFC) y hexafluoruro de azufre. Sin embargo, además de estos gases existen otros compuestos volátiles de uso más cotidiano cuyo efecto tóxico, en la salud del hombre, es más inmediato. Entre estos compuestos se encuentra el metil-terbutil éter (MTBE), un ingrediente de la gasolina formado a partir de gas natural.In the last decades there has been a growing concern to control and treat the gaseous emissions produced in the different industrial or daily processes due to the activity of man. Thus, in 1997, the governments of 55 nations agreed through the Kyoto Protocol to reduce the emissions of greenhouse gases responsible for climate change by 5.2%. Among these gases are mainly carbon dioxide (CO2), methane (CH4), nitrous oxide (N2O), hydrofluorinated (HFC), perfluorocarbons (PFC) and sulfur hexafluoride. However, in addition to these gases there are other volatile compounds for everyday use whose toxic effect, on the health of man, is more immediate. Among these compounds is methyl-terbutyl ether (MTBE), a gasoline ingredient formed from natural gas.

Los compuestos orgánicos volátiles (COV) son liberados a la atmósfera, principalmente, en diferentes procesos industriales mediante la combustión de gasolina, madera, carbón o gas natural. También muchos de ellos son emitidos cuando se usan como disolventes industriales como el tolueno, xileno o percloroetileno. Estos compuestos liberados a la atmósfera contribuyen a la formación de ozono troposférico (ozono en la atmósfera inferior, a nivel del suelo). En grandes cantidades este ozono empobrece la calidad del aire, resultando nocivo para el medio ambiente y cancerígeno y tóxico para la salud humana. También, la exposición a largo plazo a los compuestos orgánicos volátiles puede causar lesiones del hígado, riñones y sistema nervioso.Volatile organic compounds (VOCs) are released into the atmosphere, mainly in different processes industrial through the combustion of gasoline, wood, coal or natural gas. Also many of them are emitted when used as industrial solvents such as toluene, xylene or perchlorethylene. These compounds released into the atmosphere contribute to tropospheric ozone formation (ozone in the lower atmosphere, at ground level). In large quantities this ozone impoverishes air quality, proving harmful to the environment environment and carcinogen and toxic to human health. Also, the Long-term exposure to volatile organic compounds may cause lesions of the liver, kidneys and nervous system.

Por ello se han desarrollado distintas normativas, entre ellas la Directiva 13/1999 de la Comunidad Europea, que establece las medidas y limitaciones de las emisiones de COV.That is why they have developed different regulations, including Community Directive 13/1999 European, which establishes emission measures and limitations of VOC.

En la actualidad las técnicas fotocatalíticas para el tratamiento de contaminantes han sido aplicadas únicamente en aguas residuales. Por lo tanto la presente invención propone una forma novedosa de aplicación de las técnicas fotocatalíticas para la eliminación y mineralización de contaminantes gaseosos en un sistema en continuo.Currently photocatalytic techniques for the treatment of contaminants they have been applied only in sewage Therefore the present invention proposes a novel way of applying photocatalytic techniques for removal and mineralization of gaseous pollutants in a system in continuous.

Explicación de la invenciónExplanation of the invention.

La presente invención hace referencia a un procedimiento de tratamiento y degradación de gases tóxicos de origen orgánico que permite transformar y mineralizar gases de origen orgánico, descontaminando de esta forma la emisión de gases. Se trata de un procedimiento en continuo que consiste en hacer pasar un flujo de aire que contiene vapores del gas tóxico de origen orgánico a desmineralizar a través de un reactor en cuyas paredes interiores se ha impregnado un catalizador y aplicando una fuente de radiación, mediante técnicas fotocatalíticas, al flujo de aire en contacto con el catalizador se obtiene como resultado final del proceso la mineralización del gas tóxico de origen orgánico mediante la oxidación de los compuestos orgánicos hasta CO_{2} o especies menos tóxicas.The present invention refers to a procedure of treatment and degradation of toxic gases of organic origin that allows to transform and mineralize gases of organic origin, thus decontaminating the emission of gases. It is a continuous procedure that involves passing an air flow containing vapors of the toxic gas of origin organic to demineralize through a reactor in whose walls interiors has been impregnated a catalyst and applying a source of radiation, by photocatalytic techniques, to the air flow in contact with the catalyst is obtained as a final result of mineralization process of toxic gas of organic origin by the oxidation of organic compounds to CO2 or species less toxic

Descripción de las figurasDescription of the figures

La figura 1 representa un esquema donde se pueden apreciar todas las etapas del procedimiento de tratamiento y degradación de gases tóxicos de origen orgánico.Figure 1 represents a scheme where they can appreciate all the stages of the treatment procedure and degradation of toxic gases of organic origin.

Modo preferente de realización de la invenciónPreferred embodiment of the invention

Aunque la invención se describe en términos de una realización específica preferida, será fácilmente evidente para los expertos en esta técnica que se pueden hacer diversas modificaciones, redisposiciones y reemplazos. El alcance de la invención está definido por las reivindicaciones adjuntas a la misma.Although the invention is described in terms of a specific preferred embodiment will be readily apparent to the experts in this technique that can be made diverse modifications, redispositions and replacements. The scope of the invention is defined by the claims appended to the same.

Para explicar detalladamente el modo de realización preferente de la invención se ha escogido el metil-terbutil eter (MTBE) como compuesto orgánico volátil.To explain in detail the mode of preferred embodiment of the invention the methyl terbutyl ether (MTBE) as an organic compound volatile.

En primer lugar se procedió a preparar el catalizador a partir de la mezcla de TiO_{2} con una solución acuosa de CuSO_{4}, removiendo la mezcla durante 48 horas.First we proceeded to prepare the catalyst from the mixture of TiO2 with a solution aqueous of CuSO4, stirring the mixture for 48 hours.

Para impregnar el catalizador en las paredes interiores del reactor (3) en primer lugar se evaporó el agua de la mezcla mediante el calentamiento de la misma, a 100ºC y durante 24 horas, posteriormente se calcinó el CuTiO_{2} resultante a 400ºC y durante aproximadamente 5 horas.To impregnate the catalyst in the walls reactor interiors (3) first the water was evaporated from the mixture by heating it, at 100 ° C and for 24 hours, then the resulting CuTiO2 was calcined at 400 ° C and for about 5 hours.

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Una vez preparado el catalizador e impregnado en las paredes del reactor (3) el procedimiento de tratamiento y degradación de gases tóxicos de origen orgánico continuó tal y como se representa en la figura 1.Once the catalyst is prepared and impregnated in the reactor walls (3) the treatment procedure and degradation of toxic gases of organic origin continued as It is represented in figure 1.

En un recipiente (1) era calentado continuamente, a 40ºC, una solución acuosa donde se encontraba el MTBE en una relación de volumen 2:1, siendo el pH de la solución de 5. A este recipiente se le inyectó de forma continua un flujo de aire (4) de 150 cm^{3}/min. El flujo de aire resultante, que contenía vapores de agua y MTBE, fue introducido en un reactor (3) de vidrio cilíndrico en espiral de 2 mm de diámetro interno.In a bowl (1) it was heated continuously, at 40 ° C, an aqueous solution where the MTBE in a 2: 1 volume ratio, the pH of the solution being 5. This vessel was continuously injected with a flow of air (4) of 150 cm3 / min. The resulting air flow, which it contained water vapors and MTBE, it was introduced in a reactor (3) of spiral cylindrical glass of 2 mm internal diameter.

A continuación se le aplicó una fuente de radiación (2), utilizando como fuente de energía lámparas comunes de radiación ultravioleta, al flujo de aire que contenía vapores de agua y MTBE.A source of radiation (2), using common lamps as energy source ultraviolet radiation, to the air flow that contained vapors of water and MTBE.

Los gases de salida de estos sistemas fueron continuamente analizados mediante un cromatógrafo de gases (5) (GC Varían Star 3600) equipado con una válvula de inyección de gases. Este cromatógrafo (5) está dotado de un detector FED para el seguimiento y detección del MTBE e intermedios de reacción tales como alcoholes o ácidos carboxílicos y un detector TCD para el seguimiento y detección del CO_{2}. También una cámara catalítica fue utilizada para el seguimiento mediante espectroscopia FTIR de los intermedios de reacción en la superficie del catalizador.The exhaust gases of these systems were continuously analyzed by a gas chromatograph (5) (GC They vary Star 3600) equipped with a gas injection valve. This chromatograph (5) is equipped with an EDF detector for the MTBE monitoring and detection and reaction intermediates such as alcohols or carboxylic acids and a TCD detector for monitoring and detection of CO2. Also a catalytic chamber It was used for monitoring by FTIR spectroscopy of reaction intermediates on the catalyst surface.

Esta técnica se basa en la iluminación de un semiconductor, TiO_{2} dopado con Cu en este caso, que actúa como catalizador y que en presencia de radiación ultravioleta genera radicales altamente oxidantes capaces de degradar la materia orgánica. Las reacciones que tienen lugar en este proceso son las siguientes:This technique is based on the lighting of a semiconductor, TiO2 doped with Cu in this case, which acts as catalyst and that in the presence of ultraviolet radiation generates highly oxidizing radicals capable of degrading matter organic The reactions that take place in this process are the following:

1one

Así el TiO_{2} en presencia de radiación ultravioleta con suficiente energía es capaz de excitar un electrón (e^{-}) a niveles más altos de energía generando a su vez un hueco (h^{+}). Estos huecos fotogenerados pueden reaccionar directamente con los compuestos orgánicos oxidándolos hasta CO_{2} o especies orgánicas menos tóxicas. Los grupos hidroxilos (OH^{-}) presentes en la superficie del catalizador pueden reaccionar con los huecos generando radicales (OH) altamente oxidantes que degradan la materia orgánica. Del mismo modo, el oxígeno adsorbido en la superficie del catalizador puede reaccionar con los electrones fotogenerados para producir radicales (O_{2}^{-}).Thus the TiO2 in the presence of radiation ultraviolet with enough energy is able to excite an electron (e ^ -) at higher levels of energy while generating a gap (h +). These photogenerated holes can react directly with the organic compounds oxidizing them to CO2 or species less toxic organic. The hydroxyl groups (OH -) present on the surface of the catalyst can react with the gaps generating highly oxidizing radicals (OH) that degrade matter organic Similarly, oxygen adsorbed on the surface of the catalyst can react with photogenerated electrons to produce radicals (O 2 -).

En este sistema no se han observado procesos de desactivación dado que el Cu^{+} generado por su reacción con los electrones fotogenerados es nuevamente oxidado a Cu^{2+} mediante el oxígeno.In this system no processes of deactivation since the Cu + generated by its reaction with the Photogenerated electrons are again oxidized to Cu 2+ by the Oxigen.

Aplicación industrialIndustrial application

La principal aplicación industrial es la instalación de este sistema en las chimeneas o campanas extractoras de las industrias donde se generan estos gases evitando así la emisión de estos compuestos. Algunas de las ventajas que presenta este sistema es su bajo coste y el escaso mantenimiento que presenta.The main industrial application is the installation of this system in chimneys or extractor hoods of the industries where these gases are generated thus avoiding emission of these compounds. Some of the advantages it presents This system is its low cost and the low maintenance that presents.

Claims (2)

1. Procedimiento para el tratamiento y degradación de gases tóxicos de origen orgánico que comprende las siguientes etapas:1. Procedure for treatment and degradation of toxic gases of organic origin comprising following stages: a) Se prepara un catalizador que comprende al menos un componente seleccionado de una lista de elementos en la que se encuentran el TiO_{2} y el CuSO_{4}.a) A catalyst is prepared comprising the least one component selected from a list of items in which TiO_ {2} and CuSO_ {4} are found. b) Se impregnan las paredes de al menos un reactor con el catalizador anteriormente preparado.b) The walls of at least one are impregnated reactor with the catalyst previously prepared. c) Se calienta, de forma continua, una mezcla acuosa que comprende al menos un componente seleccionado de una lista de elementos en la que se encuentra el gas tóxico de origen orgánico que se desea tratar y degradar.c) A mixture is continuously heated aqueous comprising at least one component selected from a list of elements in which the toxic gas of origin is found organic that you want to treat and degrade. d) Se inyecta un flujo de aire, de forma continua, a la anterior mezcla.d) An air flow is injected, so Continue to the previous mix. e) El flujo de aire resultante, que contiene vapores de la mezcla, se hace pasar por al menos un reactor cuyas paredes están impregnadas del catalizador anteriormente preparado.e) The resulting air flow, which contains vapors of the mixture, it is passed through at least one reactor whose walls are impregnated with the catalyst above prepared. f) Se aplica una fuente de radiación, mediante técnicas fotocatalíticas, al flujo de aire, que contiene vapores de la mezcla, en contacto con el catalizador.f) A radiation source is applied, by photocatalytic techniques, to the air flow, which contains vapors of the mixture, in contact with the catalyst. g) Se mineraliza el gas tóxico de origen orgánico mediante la oxidación de los compuestos orgánicos hasta CO_{2} o especies menos tóxicas.g) Toxic gas of origin is mineralized organic by oxidation of organic compounds until CO2 or less toxic species. 2. Procedimiento para el tratamiento y degradación de gases tóxicos de origen orgánico según reivindicación 1 caracterizado porque la impregnación del catalizador comprende las siguientes etapas:2. Procedure for the treatment and degradation of toxic gases of organic origin according to claim 1 characterized in that the impregnation of the catalyst comprises the following steps: a) Evaporación del agua de la solución catalítica mediante calentamiento a 100ºC durante 15-30 horas.a) Evaporation of the solution water catalytic by heating at 100 ° C for 15-30 hours b) Calcinación del catalizador resultante de la primera etapa a 400ºC durante 3-8 horas.b) Calcination of the catalyst resulting from the First stage at 400 ° C for 3-8 hours.
ES200701090A 2007-04-13 2007-04-13 PROCEDURE FOR THE TREATMENT AND DEGRADATION OF TOXIC GASES OF ORGANIC ORIGIN THROUGH PHOTOCATALITICAL TECHNIQUES. Active ES2339081B1 (en)

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Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0719579A1 (en) * 1994-12-26 1996-07-03 Takeda Chemical Industries, Ltd. Catalytic compositions and a deodorizing method using the same
US5866752A (en) * 1997-09-29 1999-02-02 Goozner; Robert E. Destruction of volatile organic carbons
US20040258581A1 (en) * 2003-06-19 2004-12-23 Di Wei Bifunctional manganese oxide/titanium dioxide photocatalyst/thermocatalyst for improving indoor air quality
US20050069464A1 (en) * 2003-09-25 2005-03-31 Obee Timothy N. Photocatalytic oxidation of contaminants through selective desorption of water utilizing microwaves
ES2238014A1 (en) * 2004-01-30 2005-08-01 Envirocontrol S.A. Photocatalytic procedure for the control of macrobiota in the air in indoor environments
US20050238551A1 (en) * 2003-12-11 2005-10-27 Sharper Image Corporation Electro-kinetic air transporter-conditioner system and method to oxidize volatile organic compounds

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0719579A1 (en) * 1994-12-26 1996-07-03 Takeda Chemical Industries, Ltd. Catalytic compositions and a deodorizing method using the same
US5866752A (en) * 1997-09-29 1999-02-02 Goozner; Robert E. Destruction of volatile organic carbons
US20040258581A1 (en) * 2003-06-19 2004-12-23 Di Wei Bifunctional manganese oxide/titanium dioxide photocatalyst/thermocatalyst for improving indoor air quality
US20050069464A1 (en) * 2003-09-25 2005-03-31 Obee Timothy N. Photocatalytic oxidation of contaminants through selective desorption of water utilizing microwaves
US20050238551A1 (en) * 2003-12-11 2005-10-27 Sharper Image Corporation Electro-kinetic air transporter-conditioner system and method to oxidize volatile organic compounds
ES2238014A1 (en) * 2004-01-30 2005-08-01 Envirocontrol S.A. Photocatalytic procedure for the control of macrobiota in the air in indoor environments

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