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 PDFInfo
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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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- 238000000034 method Methods 0.000 title claims abstract description 28
- 239000002341 toxic gas Substances 0.000 title claims abstract description 15
- 230000015556 catabolic process Effects 0.000 title claims abstract description 10
- 238000006731 degradation reaction Methods 0.000 title claims abstract description 10
- 230000001699 photocatalysis Effects 0.000 title claims abstract description 9
- 239000003054 catalyst Substances 0.000 claims abstract description 17
- 230000005855 radiation Effects 0.000 claims abstract description 7
- 150000002894 organic compounds Chemical class 0.000 claims abstract description 5
- 231100001231 less toxic Toxicity 0.000 claims abstract description 4
- 230000003647 oxidation Effects 0.000 claims abstract description 3
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 3
- 239000000203 mixture Substances 0.000 claims description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 4
- 230000003197 catalytic effect Effects 0.000 claims description 2
- 238000010438 heat treatment Methods 0.000 claims description 2
- 238000001354 calcination Methods 0.000 claims 1
- 230000008020 evaporation Effects 0.000 claims 1
- 238000001704 evaporation Methods 0.000 claims 1
- 238000005470 impregnation Methods 0.000 claims 1
- 239000007789 gas Substances 0.000 abstract description 11
- 230000008569 process Effects 0.000 abstract description 6
- 230000033558 biomineral tissue development Effects 0.000 abstract description 3
- 231100000331 toxic Toxicity 0.000 abstract description 3
- 230000002588 toxic effect Effects 0.000 abstract description 3
- 238000010924 continuous production Methods 0.000 abstract 1
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 10
- BZLVMXJERCGZMT-UHFFFAOYSA-N Methyl tert-butyl ether Chemical compound COC(C)(C)C BZLVMXJERCGZMT-UHFFFAOYSA-N 0.000 description 8
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 7
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 6
- 229910002092 carbon dioxide Inorganic materials 0.000 description 5
- 239000001569 carbon dioxide Substances 0.000 description 5
- GQPLMRYTRLFLPF-UHFFFAOYSA-N Nitrous Oxide Chemical compound [O-][N+]#N GQPLMRYTRLFLPF-UHFFFAOYSA-N 0.000 description 4
- 150000001875 compounds Chemical class 0.000 description 4
- 239000012855 volatile organic compound Substances 0.000 description 4
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 238000012544 monitoring process Methods 0.000 description 3
- 230000001590 oxidative effect Effects 0.000 description 3
- 150000001722 carbon compounds Chemical class 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000007806 chemical reaction intermediate Substances 0.000 description 2
- 238000001514 detection method Methods 0.000 description 2
- 239000003502 gasoline Substances 0.000 description 2
- 230000036541 health Effects 0.000 description 2
- 239000003345 natural gas Substances 0.000 description 2
- 239000001272 nitrous oxide Substances 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 241000894007 species Species 0.000 description 2
- 238000005033 Fourier transform infrared spectroscopy Methods 0.000 description 1
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 1
- CYTYCFOTNPOANT-UHFFFAOYSA-N Perchloroethylene Chemical group ClC(Cl)=C(Cl)Cl CYTYCFOTNPOANT-UHFFFAOYSA-N 0.000 description 1
- 229910018503 SF6 Inorganic materials 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000000711 cancerogenic effect Effects 0.000 description 1
- 150000001735 carboxylic acids Chemical class 0.000 description 1
- 231100000357 carcinogen Toxicity 0.000 description 1
- 239000003183 carcinogenic agent Substances 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000003034 coal gas Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- ARUVKPQLZAKDPS-UHFFFAOYSA-L copper(II) sulfate Chemical compound [Cu+2].[O-][S+2]([O-])([O-])[O-] ARUVKPQLZAKDPS-UHFFFAOYSA-L 0.000 description 1
- 229910000366 copper(II) sulfate Inorganic materials 0.000 description 1
- 230000002354 daily effect Effects 0.000 description 1
- 230000009849 deactivation Effects 0.000 description 1
- 230000000593 degrading effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- DQYBDCGIPTYXML-UHFFFAOYSA-N ethoxyethane;hydrate Chemical compound O.CCOCC DQYBDCGIPTYXML-UHFFFAOYSA-N 0.000 description 1
- 230000003203 everyday effect Effects 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 239000005431 greenhouse gas Substances 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 239000004434 industrial solvent Substances 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 210000003734 kidney Anatomy 0.000 description 1
- 230000003902 lesion Effects 0.000 description 1
- 210000004185 liver Anatomy 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 210000000653 nervous system Anatomy 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 239000004065 semiconductor Substances 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- SFZCNBIFKDRMGX-UHFFFAOYSA-N sulfur hexafluoride Chemical compound FS(F)(F)(F)(F)F SFZCNBIFKDRMGX-UHFFFAOYSA-N 0.000 description 1
- 229960000909 sulfur hexafluoride Drugs 0.000 description 1
- 229950011008 tetrachloroethylene Drugs 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
- 239000008096 xylene Substances 0.000 description 1
Classifications
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61L—METHODS 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
- A61L9/00—Disinfection, sterilisation or deodorisation of air
- A61L9/16—Disinfection, sterilisation or deodorisation of air using physical phenomena
- A61L9/18—Radiation
-
- 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
- B01D53/007—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 irradiation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/86—Catalytic processes
- B01D53/8668—Removing 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)
- Public Health (AREA)
- Veterinary Medicine (AREA)
- Catalysts (AREA)
Abstract
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
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.
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.
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
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.
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:
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.
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)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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ES200701090A ES2339081B1 (en) | 2007-04-13 | 2007-04-13 | PROCEDURE FOR THE TREATMENT AND DEGRADATION OF TOXIC GASES OF ORGANIC ORIGIN THROUGH PHOTOCATALITICAL TECHNIQUES. |
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ES200701090A ES2339081B1 (en) | 2007-04-13 | 2007-04-13 | PROCEDURE FOR THE TREATMENT AND DEGRADATION OF TOXIC GASES OF ORGANIC ORIGIN THROUGH PHOTOCATALITICAL TECHNIQUES. |
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ES2339081A1 true ES2339081A1 (en) | 2010-05-14 |
ES2339081B1 ES2339081B1 (en) | 2011-02-18 |
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Citations (6)
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 |
-
2007
- 2007-04-13 ES ES200701090A patent/ES2339081B1/en active Active
Patent Citations (6)
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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