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ES2258383A1 - Dissolution system for unuseable tires, has heat carrying fluid supplied into reactor tank storing discarded tires to gradually come into contact with surface of tires and soften tires until tires are dissolved - Google Patents

Dissolution system for unuseable tires, has heat carrying fluid supplied into reactor tank storing discarded tires to gradually come into contact with surface of tires and soften tires until tires are dissolved

Info

Publication number
ES2258383A1
ES2258383A1 ES200401717A ES200401717A ES2258383A1 ES 2258383 A1 ES2258383 A1 ES 2258383A1 ES 200401717 A ES200401717 A ES 200401717A ES 200401717 A ES200401717 A ES 200401717A ES 2258383 A1 ES2258383 A1 ES 2258383A1
Authority
ES
Spain
Prior art keywords
tires
tank
dissolving
steel
heaters
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
ES200401717A
Other languages
Spanish (es)
Other versions
ES2258383B1 (en
Inventor
Eduardo Perez Lebeña
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Bio Watt Iberica S L
BIO WATT IBERICA SL
Original Assignee
Bio Watt Iberica S L
BIO WATT IBERICA SL
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Bio Watt Iberica S L, BIO WATT IBERICA SL filed Critical Bio Watt Iberica S L
Priority to EP20040380257 priority Critical patent/EP1544236A1/en
Publication of ES2258383A1 publication Critical patent/ES2258383A1/en
Application granted granted Critical
Publication of ES2258383B1 publication Critical patent/ES2258383B1/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J11/00Recovery or working-up of waste materials
    • C08J11/04Recovery or working-up of waste materials of polymers
    • C08J11/06Recovery or working-up of waste materials of polymers without chemical reactions
    • C08J11/08Recovery or working-up of waste materials of polymers without chemical reactions using selective solvents for polymer components
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10BDESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B53/00Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
    • C10B53/07Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form of solid raw materials consisting of synthetic polymeric materials, e.g. tyres
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G1/00Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
    • C10G1/10Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal from rubber or rubber waste
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/141Feedstock
    • Y02P20/143Feedstock the feedstock being recycled material, e.g. plastics
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/62Plastics recycling; Rubber recycling

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Sustainable Development (AREA)
  • Health & Medical Sciences (AREA)
  • Wood Science & Technology (AREA)
  • Polymers & Plastics (AREA)
  • Materials Engineering (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)

Abstract

A heat carrying fluid (2) is supplied into a reactor tank (8) storing discarded tires (1) to gradually come into contact with surface of tires and soften the tires until tires are dissolved. The fluid is heated to 275-350[deg]C by external heaters (3) arranged at the tank bottom for heating the tank. A preheating unit such as a heat exchanger heats the fluid before fluid supply into tank to temperature of 350-450[deg]C. The external heaters are selected from electric, gas, gas oil, fuel heaters, or heaters connected to the exhaust pipes of cogeneration engines. The fluid is selected from used car oil, commercial gas oil used in diesel engines and burners, oil derived from petroleum with a viscosity range similar to that of commercial gas oil, oil obtained by dissolving tires, and oils derived from petroleum which is stable at the temperature of 275-350[deg]C. A tube (6) supplies oil to the tank. The product resulting from the dissolving of the tires is removed from an overflow pipe (5) located in the top portion of the tank which is held at atmospheric pressure. The metal structure of the tire is stacked in the tank after dissolving the tire. The metal structure and the pieces of steel of the tire are removed for recycling.

Description

Mejoras en la Patente nº 200401058, por: "Sistema de disolución de neumáticos fuera de uso par obtención de aceites, carbón y acero".Improvements in Patent No. 200401058, for: "Tire dissolution system out of use to obtain oils, coal and steel. "

Objeto de la invenciónObject of the invention

La presente invención, tal y como se expresa en el enunciado de esta memoria descriptiva, consiste en mejoras introducidas en la Patente principal nº 200401058 en la que se describe un sistema para la transformación parcial en combustible de los neumáticos que se encuentran al final de su vida útil, y que además permite realizar la descomposición de los neumáticos residuales en cada uno de los componentes que lo forman para su reutilización en diversas aplicaciones.The present invention, as expressed in The statement of this specification consists of improvements introduced in main Patent No. 200401058 in which describes a system for the partial transformation into fuel of the tires that are at the end of their useful life, and that It also allows to decompose the tires residuals in each of the components that form it for its reuse in various applications.

El objeto del presente certificado de adición se centra en simplificar el sistema, reduciendo con ello el coste de la recuperación de residuos.The purpose of this certificate of addition is It focuses on simplifying the system, thereby reducing the cost of Waste recovery

Antecedentes de la invenciónBackground of the invention

El antecedente más próximo al presente certificado de adición lo constituye su Patente principal nº 200401058 en la que se describe un sistema que comprende un depósito reactor en el que se preveía la descomposición de los neumáticos mediante la aplicación de un fluido caloportador que entra paulatinamente en contacto con la superficie de los neumáticos que lo absorben y se reblandece hasta su disolución, para lo que es necesario calentar el fluido caloportador, que al aplicarse principalmente mediante un sistema a modo de ducha, se requería su calentamiento previo mediante un serpentín. Al aplicarse la ducha del fluido caloportador caliente, éste tiende a enfriarse mientras cae, por lo que requiere un mayor calentamiento. En dicha Patente principal no se describe la posibilidad de realizar la descomposición de los neumáticos mediante el baño de los mismos para lo que el fluido caloportador se calienta directamente en el depósito reactor, mediante el calentamiento de dicho depósito reactor, lo que requiere una menor temperatura de calentamiento, simplifica el sistema y reduce el coste de recuperación de residuos.The history closest to the present Certificate of Addition is its main Patent No. 200401058 in which a system comprising a tank is described   reactor in which tire breakdown was anticipated by applying a heat transfer fluid that enters gradually in contact with the surface of the tires that they absorb it and it softens until it dissolves, for what it is it is necessary to heat the heat transfer fluid, which when applied mainly through a shower-like system, its required preheating by means of a coil. When applying the shower of the hot heat transfer fluid, it tends to cool while falls, so it requires more warming. In said patent main does not describe the possibility of performing the tire breakdown by bathing them for which the heat transfer fluid is heated directly in the reactor tank, by heating said tank reactor, which requires a lower heating temperature, simplifies the system and reduces the recovery cost of waste.

Descripción de la invenciónDescription of the invention

Para resolver los inconvenientes anteriormente indicados, la invención, al igual que su Patente principal, comprende un depósito reactor en el que se depositan los neumáticos desechados, que además comprenden medios de aplicación de un fluido caloportador que entra paulatinamente en contacto con la superficie de los neumáticos que lo absorben y se reblandecen hasta su disolución; y se caracteriza porque incorpora la mejora de comprender medios de calentamiento del reactor para calentar por contacto directo el fluido caloportador que se encuentra en su interior.To solve the problems above indicated, the invention, like its main patent, it comprises a reactor tank in which the tires are deposited discarded, which also include means for applying a fluid heat carrier that gradually comes into contact with the surface of the tires that absorb it and soften until its dissolution; and it is characterized because it incorporates the improvement of comprise reactor heating means for heating by direct contact the heat transfer fluid that is in your inside.

Los medios de calentamiento del reactor están determinados por calentadores externos que se sitúan en la parte inferior del reactor, y en una realización de la invención se prevé que comprendan una conexión a tubos de escape de motores de cogeneración, para su calentamiento, comprendiendo además una salida para eliminar los gases aplicados a dichos calentadores procedentes del tubo de escape.The reactor heating means are determined by external heaters that are located in the part bottom of the reactor, and in one embodiment of the invention is provided that comprise a connection to engine exhaust pipes of cogeneration, for its heating, also comprising a outlet to remove gases applied to said heaters coming from the exhaust pipe.

En otra realización de la invención los calentadores externos están seleccionados entre calentadores eléctricos, de gas, gasóleo, fuel o combinación de los mismos. También cabría combinarlo con los calentadores dotados de una conexión a tubos de escape si así se requiriera.In another embodiment of the invention the External heaters are selected among heaters electric, gas, diesel, fuel or combination thereof. It could also be combined with heaters equipped with a connection to exhaust pipes if required.

El depósito reactor de la invención comprende un rebosadero situado en su parte superior por el que sale la materia resultante de la disolución de los neumáticos, de manera que la estructura metálica del neumático, tras su disolución, queda apilada en el reactor, del que se extrae para su reciclado.The reactor tank of the invention comprises a overflow located at the top where the matter comes out resulting from the dissolution of the tires, so that the metallic structure of the tire, after its dissolution, remains stacked in the reactor, from which it is extracted for recycling.

El margen de temperaturas al que se calienta el fluido caloportador, según las mejoras de la invención, es de alrededor de 300ºC (275ºC-350ºC), que es una temperatura inferior a la que se requería en la Patente principal en la que al margen de temperaturas de calentamiento estaba comprendido entre 350ºC y 450ºC, ya que al aplicar el fluido caloportador en forma de ducha se producía un enfriamiento del mismo al caer sobre los neumáticos. Por consiguiente las mejoras de la invención representan un ahorro energético al realizar el calentamiento del fluido caloportador a menor temperatura.The temperature range at which the heat transfer fluid, according to the improvements of the invention, is of around 300ºC (275ºC-350ºC), which is a temperature lower than that required in the main patent in which regardless of heating temperatures was between 350ºC and 450ºC, since when applying the fluid heat transfer in the form of a shower cooling of the same when falling on the tires. Therefore the improvements of the invention represents an energy saving when performing the heating of the heat transfer fluid at a lower temperature.

El fluido caloportador se compone de aceites derivados del petróleo y estables en el rango de temperaturas 275ºC-350ºC, o bien se puede utilizar directamente fuel.The heat transfer fluid is composed of oils petroleum derivatives and stable in the temperature range 275ºC-350ºC, or it can be used directly fuel

La invención prevé que las mejoras descritas puedan ser aplicadas para realizar la disolución de cualquier producto derivado del petróleo, como por ejemplo pueden ser plásticos, hidrocarburos, etc., por lo que se obtiene un sistema versátil, que no sólo permite realizar la disolución de los neumáticos en los componentes que lo constituyen, sino que también permite realizar esta disolución de cualquier producto derivado del petróleo.The invention provides that the improvements described can be applied to dissolve any petroleum product, such as for example plastics, hydrocarbons, etc., so that a system is obtained versatile, which not only allows the dissolution of tires in the components that constitute it, but also allows this dissolution of any product derived from Petroleum.

A continuación para facilitar una mejor comprensión de esta memoria descriptiva y formando parte integrante de la misma, se acompañan una serie de figuras en las que con carácter ilustrativo y no limitativo se ha representado el objeto de la invención.Next to facilitate a better understanding of this specification and being part member of the same, a series of figures are accompanied in the that for illustrative and non-limiting purposes the object of the invention.

Breve enunciado de las figurasBrief statement of the figures

Figura 1.- Muestra una representación esquemática del sistema de la invención con las mejoras. Representa el comienzo del proceso de disolución de los neumáticos depositados en el interior del depósito reactor.Figure 1.- Shows a schematic representation of the system of the invention with the improvements. Represents the beginning of the dissolution process of the tires deposited in the inside of the reactor tank.

Figura 2.- Muestra una vista equivalente a la figura anterior, en la que ha finalizado el proceso de disolución de los neumáticos, quedando por tanto únicamente su estructura metálica que posteriormente se retira para su reciclado.Figure 2.- Shows a view equivalent to the previous figure, in which the dissolution process has ended of the tires, leaving therefore only its structure metal that is subsequently removed for recycling.

Descripción de la forma de realización preferidaDescription of the preferred embodiment

A continuación se realiza una descripción de la invención basada en las figuras anteriormente comentadas.Below is a description of the invention based on the figures discussed above.

El sistema de la invención comprende un depósito reactor (8) donde se almacenan los neumáticos (1) y se llena mediante un fluido caloportador (2), de modo que éste baña a los neumáticos (1) depositados en el depósito reactor (8). El llenado del depósito reactor (8) con el fluido caloportador (2), se efectúa mediante unos medios de llenado (6), que están determinados por una conducción de dicho fluido (2), que tal y como describe la Patente principal está seleccionado entre aceite usado de coche, gasóleo de locomoción o calefacción, aceites derivados del petróleo en un rango de viscosidad similar al del gasóleo comercial y que por sus propiedades están indicados como disolventes, o bien por el propio aceite del neumático obtenido al realizar su descomposición según la invención.The system of the invention comprises a reservoir reactor (8) where the tires (1) are stored and filled by means of a heat transfer fluid (2), so that it bathes the tires (1) deposited in the reactor tank (8). Filling of the reactor tank (8) with the heat transfer fluid (2), is carried out by means of filling (6), which are determined by a conduction of said fluid (2), which as described in the Patent Main is selected from used car oil, diesel locomotion or heating, petroleum derived oils in a viscosity range similar to that of commercial diesel and that due to its properties are indicated as solvents, or by itself tire oil obtained by decomposing according to the invention.

Para favorecer la disolución de los neumáticos la invención prevé la incorporación de calentadores extremos (3) que realizan el calentamiento del depósito reactor (8), y en consecuencia producen el calentamiento del fluido caloportador (2) lo que provoca la paulatina disolución de los neumáticos (1), obteniéndose los distintos productos que lo componen, como son el aceite que se obtiene al realizar su descomposición y el carbón en polvo que se disuelve en el fluido caloportador (2).To favor the dissolution of the tires the  The invention provides for the incorporation of extreme heaters (3) that perform the heating of the reactor tank (8), and in consequently they produce the heating of the heat transfer fluid (2) which causes the gradual dissolution of the tires (1), obtaining the different products that compose it, such as the oil obtained when decomposing and carbon in powder that dissolves in the heat transfer fluid (2).

Una vez realizada la descomposición del neumático el aceite flota y el carbón en polvo queda disuelto, y se recuperan mediante un rebosadero (5) por donde se expulsan al exterior para su recuperación. Para expulsarlos por el rebosadero (5) se añade más cantidad de fluido caloportador (2) al interior del depósito reactor 8 hasta que rebosa.Once the tire decomposition the oil floats and the coal powder is dissolved, and it recovered by an overflow (5) where they are expelled to exterior for recovery. To expel them over the overflow (5) more heat transfer fluid (2) is added to the interior from reactor tank 8 until it overflows.

Como resultado de todo el proceso en el interior del depósito reactor (8) queda depositada la estructura metálica la de los neumáticos, que se extrae por la parte superior del reactor (8) para su reutilización.As a result of the entire process inside the metal structure is deposited from the reactor tank (8) that of the tires, which is extracted from the top of the reactor (8) for reuse.

Para realizar el calentamiento del depósito reactor (8), y en consecuencia del fluido caloportador (2); en una realización de la invención se prevé que los calentadores (3) sean eléctricos, o tal y como ya fue comentado de gas.To heat the tank reactor (8), and consequently the heat transfer fluid (2); in a Embodiment of the invention is provided that the heaters (3) are electrical, or as already commented on gas.

En otra realización de la invención se prevé que los calentadores estén dotados de una entrada (7) de conexión a los tubos de escape de motores de cogeneración para a partir de éstos proporcionar la energía que provoca el calentamiento de los calentadores. En este caso los calentadores 3 están dotados de una salida (9) por la que se eliminan los gases procedentes del tubo de escape del vehículo.In another embodiment of the invention it is envisioned that the heaters are provided with an input (7) for connection to the exhaust pipes of cogeneration engines for from these provide the energy that causes heating of the heaters In this case the heaters 3 are provided with a outlet (9) by which gases from the tube are removed vehicle exhaust.

Claims (8)

1. Mejoras en la Patente 200401058, por: Sistema de disolución de neumáticos fuera de uso para obtención de aceites, carbón y acero, que comprende un depósito reactor (8) en el que se depositan los neumáticos (1) desechados, y que comprenden medios (6) de aplicación de un fluido caloportador (2) que entra paulatinamente en contacto con la superficie de los neumáticos (1) que lo absorben y se reblandecen hasta su disolución; caracterizadas las mejoras porque comprenden medios (3) de calentamiento del reactor para calentar por contacto directo el fluido caloportador (2) que se encuentra almacenado en su interior.1. Improvements in Patent 200401058, for: System of dissolving tires out of use to obtain oils, coal and steel, comprising a reactor tank (8) in which the discarded tires (1) are deposited, and comprising means (6) for applying a heat transfer fluid (2) that gradually comes into contact with the surface of the tires (1) that absorb it and soften until dissolved; The improvements are characterized in that they comprise means (3) for heating the reactor to directly heat the heat transfer fluid (2) that is stored inside. 2. Mejoras en la Patente 200401058, por: Sistema de disolución de neumáticos fuera de uso para obtención de aceites, carbón y acero, según reivindicación 1, caracterizado porque los medios de calentamiento del reactor están constituidos por calentadores externos (3) que se sitúan en la parte inferior del reactor.2. Improvements in the Patent 200401058, for: System of dissolution of tires out of use for obtaining oils, coal and steel, according to claim 1, characterized in that the reactor heating means are constituted by external heaters (3) that are located at the bottom of the reactor. 3. Mejoras en la Patente 200401058, por: "Sistema de disolución de neumáticos fuera de uso para obtención de aceites, carbón y acero", según reivindicación 2, caracterizado porque los calentadores extremos (3) comprenden una conexión (7) a tubos de escape de motores de cogeneración para su calentamiento, y una salida (9) para eliminar los gases aplicados a dichos calentadores extremos (3), procedentes del tubo de escape.3. Improvements in Patent 200401058, for: "System for dissolving tires out of use for obtaining oils, coal and steel", according to claim 2, characterized in that the extreme heaters (3) comprise a connection (7) to pipes of Exhaust of cogeneration engines for heating, and an outlet (9) to remove the gases applied to said end heaters (3), coming from the exhaust pipe. 4. Mejoras en la Patente 200401058, por: Sistema de disolución de neumáticos fuera de uso para obtención de aceites, carbón y acero, según reivindicación 2, caracterizado porque los calentadores externos (3) están seleccionados entre calentadores eléctricos, de gas, de gasóleo, fuel o combinación de los mismos.4. Improvements in Patent 200401058, for: Dissolving system of tires out of use for obtaining oils, coal and steel, according to claim 2, characterized in that the external heaters (3) are selected from electric, gas, diesel heaters , fuel or combination thereof. 5. Mejoras en la Patente 200401058, por: "Sistema de disolución de neumáticos fuera de uso para obtención de aceites, carbón y acero", según reivindicación 1, caracterizado porque el depósito reactor (8) comprende un rebosadero (5) situado en su parte superior, por el que rebosa la materia resultante de la disolución de los neumáticos (1), quedando la estructura metálica (1a) del neumático (1) apilada en el depósito reactor (8) del que se extrae para su reciclado posterior.5. Improvements in Patent 200401058, for: "Tire dissolution system out of use for obtaining oils, coal and steel", according to claim 1, characterized in that the reactor tank (8) comprises an overflow (5) located in its upper part, through which the material resulting from the dissolution of the tires (1) overflows, leaving the metal structure (1a) of the tire (1) stacked in the reactor tank (8) from which it is extracted for later recycling. 6. Mejoras en la Patente 200401058, por: Sistema de disolución de neumáticos fuera de uso para obtención de aceites, carbón y acero, según reivindicaciones anteriores, caracterizado porque la temperatura de calentamiento del fluido caloportador está comprendida entre 275ºC y 350ºC.6. Improvements in Patent 200401058, for: System of dissolving tires out of use for obtaining oils, coal and steel, according to previous claims, characterized in that the heating temperature of the heat transfer fluid is between 275 ° C and 350 ° C. 7. Mejoras en la Patente 200401058, por: Sistema de disolución de neumáticos fuera de uso para obtención de aceites, carbón y acero, según reivindicación 1, caracterizado porque el fluido caloportador se compone de aceites derivados del petróleo y estables en el rango de temperaturas 275ºC-350ºC, o bien directamente fuel.7. Improvements in Patent 200401058, for: Dissolving system of tires out of use for obtaining oils, coal and steel, according to claim 1, characterized in that the heat transfer fluid is composed of petroleum-derived and stable oils in the temperature range 275ºC-350ºC, or directly fuel. 8. Mejoras en la Patente 200401058, por: Sistema de disolución de neumáticos fuera de uso para obtención de aceites, carbón y acero, según reivindicación 1, caracterizado porque realiza la disolución de otros productos derivados del petróleo, tales como residuos plásticos, gomas y similares.8. Improvements in Patent 200401058, for: Dissolving system of tires out of use for obtaining oils, coal and steel, according to claim 1, characterized in that it dissolves other petroleum products, such as plastic waste, rubber and Similar.
ES200401717A 2003-12-15 2004-07-14 IMPROVEMENTS IN THE PATENT 200401058, BY: TIRE DISSOLUTION SYSTEM OUT OF USE FOR OBTAINING OILS, CARBON AND STEEL. Expired - Fee Related ES2258383B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
EP20040380257 EP1544236A1 (en) 2003-12-15 2004-12-13 System for dissolving unuseable tires to obtain oils, coal and steel

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
ES200401058A ES2249127B1 (en) 2003-12-15 2003-12-15 TIRES DISSOLUTION SYSTEM OUT OF USE FOR OBTAINING OILS, CARBON AND STEEL.

Publications (2)

Publication Number Publication Date
ES2258383A1 true ES2258383A1 (en) 2006-08-16
ES2258383B1 ES2258383B1 (en) 2007-12-16

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Family Applications (3)

Application Number Title Priority Date Filing Date
ES200401058A Expired - Fee Related ES2249127B1 (en) 2003-12-15 2003-12-15 TIRES DISSOLUTION SYSTEM OUT OF USE FOR OBTAINING OILS, CARBON AND STEEL.
ES200401717A Expired - Fee Related ES2258383B1 (en) 2003-12-15 2004-07-14 IMPROVEMENTS IN THE PATENT 200401058, BY: TIRE DISSOLUTION SYSTEM OUT OF USE FOR OBTAINING OILS, CARBON AND STEEL.
ES200501591A Expired - Fee Related ES2277749B1 (en) 2003-12-15 2005-06-29 IMPROVEMENTS INTRODUCED IN THE PATENT OF INVENTION N. P-200401058/4, BY: TIRE DISSOLUTION SYSTEM OUT OF USE FOR OBTAINING OILS, CARBON AND STEEL.

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ES200401058A Expired - Fee Related ES2249127B1 (en) 2003-12-15 2003-12-15 TIRES DISSOLUTION SYSTEM OUT OF USE FOR OBTAINING OILS, CARBON AND STEEL.

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ES200501591A Expired - Fee Related ES2277749B1 (en) 2003-12-15 2005-06-29 IMPROVEMENTS INTRODUCED IN THE PATENT OF INVENTION N. P-200401058/4, BY: TIRE DISSOLUTION SYSTEM OUT OF USE FOR OBTAINING OILS, CARBON AND STEEL.

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ES2335258B1 (en) * 2008-07-11 2010-12-30 Innovacion Y Nuevas Energias, S.A. PROCEDURE FOR RECOVERY OF USED TIRES AND OILS, AND REACTOR FOR THE PRACTICE OF THE SAME.

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WO1999009092A1 (en) * 1997-08-21 1999-02-25 Edsview Belleggings (Proprietary) Limited The reprocessing of polymeric products
WO2003052029A1 (en) * 2001-12-19 2003-06-26 Igor Skworcow Method and installation for production of technological carbon and motor fuel during a processing of worn tires and other polymer waste materials

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