SYSTEM AND METHOD FOR THE HYDROTHERMAL OXIDATION OF WATER-INSOLUBLE ORGANIC RESIDUES
The invention relates to a system and method for the hydrothermal oxidation of water-insoluble organic residues. The plant comprises two independent liquid phase feed lines, namely an aqueous phase (1) and a non-water-soluble phase (9). The supercritical conditions in the entrance to the first react...
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| creator | SANCHEZ ONETO JEZABEL NEBOT SANZ ENRIQUE MARTINEZ DE LA OSSA FERNANDEZ ENRIQUE PORTELA MIGUELEZ JUAN RAMON |
| description | The invention relates to a system and method for the hydrothermal oxidation of water-insoluble organic residues. The plant comprises two independent liquid phase feed lines, namely an aqueous phase (1) and a non-water-soluble phase (9). The supercritical conditions in the entrance to the first reactor (10) enable a homogeneous phase to be obtained, in which there are no solubilization problems, thereby enabling the treatment of industrial residues that cannot be treated with standard systems. The inventive system comprises two reactor sections (14 and 18) such that it is possible to inject streams of hydrogen peroxide (11 and 15) in the connections between sections (13 and 17), in order to potentiate the oxidation reaction. The plant is equipped with a heat exchange system (5) in order to make use of the energy generated during the oxidation process, such that the plant operates in autothermal conditions.
Sistema y procedimiento para la oxidación hidrotérmica de residuos orgánicos insolubles en agua. La planta dispone de dos líneas independientes de alimentación de fases líquidas, una acuosa (1) y otra no soluble en agua (9). En la entrada al primer reactor (10) existen condiciones supercríticas, por lo que se obtiene una fase homogénea en la cual no existen problemas de solubilización, permitiendo abordar el tratamiento de residuos industriales para los que los sistemas convencionales no son válidos. El sistema consta de dos tramos más de reactor (14 y 18) de tal manera que en las conexiones entre tramos (13 y 17) es posible la inyección de corrientes de peróxido de hidrógeno (11 y 15) para potenciar la reacción de oxidación. La planta dispone de un sistema intercambiador de calor (5) para aprovechar la energía generada durante el proceso de oxidación, de modo que la planta opere en régimen autotérmico. |
| format | Patent |
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Sistema y procedimiento para la oxidación hidrotérmica de residuos orgánicos insolubles en agua. La planta dispone de dos líneas independientes de alimentación de fases líquidas, una acuosa (1) y otra no soluble en agua (9). En la entrada al primer reactor (10) existen condiciones supercríticas, por lo que se obtiene una fase homogénea en la cual no existen problemas de solubilización, permitiendo abordar el tratamiento de residuos industriales para los que los sistemas convencionales no son válidos. El sistema consta de dos tramos más de reactor (14 y 18) de tal manera que en las conexiones entre tramos (13 y 17) es posible la inyección de corrientes de peróxido de hidrógeno (11 y 15) para potenciar la reacción de oxidación. La planta dispone de un sistema intercambiador de calor (5) para aprovechar la energía generada durante el proceso de oxidación, de modo que la planta opere en régimen autotérmico.</description><language>eng ; spa</language><subject>CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOIDCHEMISTRY ; CHEMISTRY ; METALLURGY ; PERFORMING OPERATIONS ; PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL ; THEIR RELEVANT APPARATUS ; TRANSPORTING ; TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE</subject><creationdate>2006</creationdate><oa>free_for_read</oa><woscitedreferencessubscribed>false</woscitedreferencessubscribed></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&date=20060616&DB=EPODOC&CC=ES&NR=2255443A1$$EHTML$$P50$$Gepo$$Hfree_for_read</linktohtml><link.rule.ids>230,308,776,881,25542,76289</link.rule.ids><linktorsrc>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&date=20060616&DB=EPODOC&CC=ES&NR=2255443A1$$EView_record_in_European_Patent_Office$$FView_record_in_$$GEuropean_Patent_Office$$Hfree_for_read</linktorsrc></links><search><creatorcontrib>SANCHEZ ONETO JEZABEL</creatorcontrib><creatorcontrib>NEBOT SANZ ENRIQUE</creatorcontrib><creatorcontrib>MARTINEZ DE LA OSSA FERNANDEZ ENRIQUE</creatorcontrib><creatorcontrib>PORTELA MIGUELEZ JUAN RAMON</creatorcontrib><title>SYSTEM AND METHOD FOR THE HYDROTHERMAL OXIDATION OF WATER-INSOLUBLE ORGANIC RESIDUES</title><description>The invention relates to a system and method for the hydrothermal oxidation of water-insoluble organic residues. The plant comprises two independent liquid phase feed lines, namely an aqueous phase (1) and a non-water-soluble phase (9). The supercritical conditions in the entrance to the first reactor (10) enable a homogeneous phase to be obtained, in which there are no solubilization problems, thereby enabling the treatment of industrial residues that cannot be treated with standard systems. The inventive system comprises two reactor sections (14 and 18) such that it is possible to inject streams of hydrogen peroxide (11 and 15) in the connections between sections (13 and 17), in order to potentiate the oxidation reaction. The plant is equipped with a heat exchange system (5) in order to make use of the energy generated during the oxidation process, such that the plant operates in autothermal conditions.
Sistema y procedimiento para la oxidación hidrotérmica de residuos orgánicos insolubles en agua. La planta dispone de dos líneas independientes de alimentación de fases líquidas, una acuosa (1) y otra no soluble en agua (9). En la entrada al primer reactor (10) existen condiciones supercríticas, por lo que se obtiene una fase homogénea en la cual no existen problemas de solubilización, permitiendo abordar el tratamiento de residuos industriales para los que los sistemas convencionales no son válidos. El sistema consta de dos tramos más de reactor (14 y 18) de tal manera que en las conexiones entre tramos (13 y 17) es posible la inyección de corrientes de peróxido de hidrógeno (11 y 15) para potenciar la reacción de oxidación. La planta dispone de un sistema intercambiador de calor (5) para aprovechar la energía generada durante el proceso de oxidación, de modo que la planta opere en régimen autotérmico.</description><subject>CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOIDCHEMISTRY</subject><subject>CHEMISTRY</subject><subject>METALLURGY</subject><subject>PERFORMING OPERATIONS</subject><subject>PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL</subject><subject>THEIR RELEVANT APPARATUS</subject><subject>TRANSPORTING</subject><subject>TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE</subject><fulltext>true</fulltext><rsrctype>patent</rsrctype><creationdate>2006</creationdate><recordtype>patent</recordtype><sourceid>EVB</sourceid><recordid>eNqNyj0OwjAMQOEsDAi4gy_Qgf4cIDQOiZTEUuwKOlUVChOCSuX-goEDML1veFslPLJgBJ0MRBRHBixlEIfgRpPpixx1ALp6o8VTArJw0YK58okpDKeAQPmsk-8hI3szIO_V5j4_1nL4dafAovSuKstrKusy38qzvCfkuu66tm30sflj-QDqdC_3</recordid><startdate>20060616</startdate><enddate>20060616</enddate><creator>SANCHEZ ONETO JEZABEL</creator><creator>NEBOT SANZ ENRIQUE</creator><creator>MARTINEZ DE LA OSSA FERNANDEZ ENRIQUE</creator><creator>PORTELA MIGUELEZ JUAN RAMON</creator><scope>EVB</scope></search><sort><creationdate>20060616</creationdate><title>SYSTEM AND METHOD FOR THE HYDROTHERMAL OXIDATION OF WATER-INSOLUBLE ORGANIC RESIDUES</title><author>SANCHEZ ONETO JEZABEL ; NEBOT SANZ ENRIQUE ; MARTINEZ DE LA OSSA FERNANDEZ ENRIQUE ; PORTELA MIGUELEZ JUAN RAMON</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-epo_espacenet_ES2255443A13</frbrgroupid><rsrctype>patents</rsrctype><prefilter>patents</prefilter><language>eng ; spa</language><creationdate>2006</creationdate><topic>CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOIDCHEMISTRY</topic><topic>CHEMISTRY</topic><topic>METALLURGY</topic><topic>PERFORMING OPERATIONS</topic><topic>PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL</topic><topic>THEIR RELEVANT APPARATUS</topic><topic>TRANSPORTING</topic><topic>TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE</topic><toplevel>online_resources</toplevel><creatorcontrib>SANCHEZ ONETO JEZABEL</creatorcontrib><creatorcontrib>NEBOT SANZ ENRIQUE</creatorcontrib><creatorcontrib>MARTINEZ DE LA OSSA FERNANDEZ ENRIQUE</creatorcontrib><creatorcontrib>PORTELA MIGUELEZ JUAN RAMON</creatorcontrib><collection>esp@cenet</collection></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext_linktorsrc</fulltext></delivery><addata><au>SANCHEZ ONETO JEZABEL</au><au>NEBOT SANZ ENRIQUE</au><au>MARTINEZ DE LA OSSA FERNANDEZ ENRIQUE</au><au>PORTELA MIGUELEZ JUAN RAMON</au><format>patent</format><genre>patent</genre><ristype>GEN</ristype><title>SYSTEM AND METHOD FOR THE HYDROTHERMAL OXIDATION OF WATER-INSOLUBLE ORGANIC RESIDUES</title><date>2006-06-16</date><risdate>2006</risdate><abstract>The invention relates to a system and method for the hydrothermal oxidation of water-insoluble organic residues. The plant comprises two independent liquid phase feed lines, namely an aqueous phase (1) and a non-water-soluble phase (9). The supercritical conditions in the entrance to the first reactor (10) enable a homogeneous phase to be obtained, in which there are no solubilization problems, thereby enabling the treatment of industrial residues that cannot be treated with standard systems. The inventive system comprises two reactor sections (14 and 18) such that it is possible to inject streams of hydrogen peroxide (11 and 15) in the connections between sections (13 and 17), in order to potentiate the oxidation reaction. The plant is equipped with a heat exchange system (5) in order to make use of the energy generated during the oxidation process, such that the plant operates in autothermal conditions.
Sistema y procedimiento para la oxidación hidrotérmica de residuos orgánicos insolubles en agua. La planta dispone de dos líneas independientes de alimentación de fases líquidas, una acuosa (1) y otra no soluble en agua (9). En la entrada al primer reactor (10) existen condiciones supercríticas, por lo que se obtiene una fase homogénea en la cual no existen problemas de solubilización, permitiendo abordar el tratamiento de residuos industriales para los que los sistemas convencionales no son válidos. El sistema consta de dos tramos más de reactor (14 y 18) de tal manera que en las conexiones entre tramos (13 y 17) es posible la inyección de corrientes de peróxido de hidrógeno (11 y 15) para potenciar la reacción de oxidación. La planta dispone de un sistema intercambiador de calor (5) para aprovechar la energía generada durante el proceso de oxidación, de modo que la planta opere en régimen autotérmico.</abstract><oa>free_for_read</oa></addata></record> |
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| title | SYSTEM AND METHOD FOR THE HYDROTHERMAL OXIDATION OF WATER-INSOLUBLE ORGANIC RESIDUES |
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