WO2005044952A1 - Environmentally-friendly machine for the treatment of organic and inorganic waste - Google Patents
Environmentally-friendly machine for the treatment of organic and inorganic waste Download PDFInfo
- Publication number
- WO2005044952A1 WO2005044952A1 PCT/MX2003/000097 MX0300097W WO2005044952A1 WO 2005044952 A1 WO2005044952 A1 WO 2005044952A1 MX 0300097 W MX0300097 W MX 0300097W WO 2005044952 A1 WO2005044952 A1 WO 2005044952A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- organic
- chamber
- inorganic waste
- waste
- vacuum chamber
- 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.)
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Classifications
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B7/00—Coke ovens with mechanical conveying means for the raw material inside the oven
- C10B7/10—Coke ovens with mechanical conveying means for the raw material inside the oven with conveyor-screws
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
Definitions
- the present invention refers to the technical field of ecology, since it provides an ecological machine to process organic and inorganic waste and obtain reusable products from them, such as liquid and gaseous hydrocarbons.
- US Patent 4740270 describes a process for treating rubber in used tires by vacuum pyrolysis, to produce liquid and solid hydrocarbons; which consists of depositing the crushed rubber in a reactor, where the pyrolysis is carried out between 360 to 415 ° C, at a pressure of less than 35 mm Hg, so that the gases and vapors produced remain a few seconds, with which that the production of liquid hydrocarbon is increased and that of gaseous and solid hydrocarbons is decreased.
- US Patent 4,613,408 1984 deals with a fuel-producing apparatus from wastes of the type that is capable of forming flammable oil and gas.
- the apparatus and method are useful in that vehicle tire debris is available to produce gas capable of operating engines and heaters: the system uses a closed cooking pot and a cooling apparatus to condense the gas formed in the cooking container; It should be noted that the discharge of pollution into the atmosphere is negligible.
- a disadvantage of this apparatus is that the pot is removed to be cleaned of the slag at regular periods. In addition, the production capacity of this apparatus is low, since the waste is not crushed or moved or stirred inside the pot, thus delaying this processing.
- patent US 5836524 describes an apparatus and process for treating organic and inorganic waste, which produces recyclable fuel, by liquefaction with oil and pyrolysis.
- the apparatus has an inclined liquefaction and pyrolysis reactor, which in turn has a main body and an endless screw, where the waste will be processed; and an oil heater is responsible for providing a temperature of 200 to 400 ° C.
- Liquefaction and pyrolysis of the waste emit organic gases, which are sent to condensers for better processing and the light oil is sent to a separator , to remove ferrous and non-ferrous materials; while the dense oil is again sent to the heater to start the cycle again, until it turns into light oil. Therefore, one of the disadvantages of this process is the use of oil, which must be preheated and transferred to the inclined reactor, making this process more expensive.
- WO 03/045595 2001 describes a tire smelting machine, which includes a vacuum oven to make the smelting, a condenser, and a tank for liquids, thus applying a temperature of 350 ° C, and a pressure of 10 to 20 mm Hg, for 2 to 2:30 h, hydrocarbon gas and oil are obtained without contaminating the environment.
- the disadvantage of this machine is that due to its configuration it can only treat tires.
- Figure 1 is a front view of the ecological organic and inorganic waste processing machine of the present invention.
- Figure 2 is a right side view of the ecological machine of the present invention.
- Figure 3 is a left side view of the ecological machine of the present invention
- Figure 4 is a rear view of the ecological machine of the present invention.
- Figure 5 is a longitudinal section showing in detail the interior of the vacuum chamber of the ecological machine of the present invention.
- the ecological organic and inorganic waste processing machine basically consists of a rectangular metal base 38, on which a cylindrical vacuum chamber 1 is mounted, to process organic and inorganic waste, previously crushed 29 , by pyrolysis at a range of 250 to 410 ° C and a pressure of 10 to 35 mm Hg; at one end of which it has a discharge gate 13 and 40 of the resulting waste; inside there is horizontally a worm screw 2 that gives movement to the waste 29, for a better and faster cooking; and is powered by a motor 14 and a reducer 37.
- Chamber 1 has a hood 39 that dissipates excess heat into the atmosphere.
- valve 3 In the upper part of said chamber 1 it is joined to a throat 99 which is a space where the gases rise to start their exit to valves 3 and 36.
- valve 3 there are two pipes 33 and 34, which conduct the steam from water and hydrocarbon gases, respectively, towards condensers.
- the water vapor is cooled in the condenser 9 and transported to a filter 98 to be released into the environment.
- the hydrocarbon gases While the hydrocarbon gases are cooled in a condenser 4 to be later deposited in liquid form in a separator 5, subsequently, the hydrocarbon vapor is extracted by the compressor vacuum pump 7 to be compressed in a tank 8. relief 36 is useful in case of over pressure, thus avoiding accidents.
- To feed the waste chamber 1, it has a loading gate 12 and a further armored observation window 11, located externally in the throat 99.
- the vacuum chamber 1 is heated by a burner 35 located on one of its sides, which in turn comprises a feeder 66 that provides it with energy.
- Condensers 4 and 9 are cooled by a fan 18 which allows the circulation of cold water, using a pump 10 for this.
- the machine has a 97 control panel where vacuum meter, manometers and thermometers are located to control and monitor its operation. It also has a dividing wall 31 to separate the control panel from the vacuum chamber 1. The latter may have a jacket as an additional accessory to recover the heat that it radiates. Operation of the ecological organic and inorganic waste processing machine
- line 33 is closed, and line 34 is opened to conduct the hydrocarbon gases to condenser 4, passing to separator 5, where the liquid hydrocarbons are deposited and the gaseous ones are extracted by the vacuum compressor 7 and compresses them into a reservoir tank 8.
- the condensers are cooled by water and a fan 18.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Processing Of Solid Wastes (AREA)
- Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
Description
AQUINA ECOLÓGICA PROCESADORA DE DESECHOS ORGÁNICOS E INORGÁNICOS ORGANIC AND INORGANIC WASTE PROCESSING ECOLOGICAL AQUINE
CAMPO TÉCNICO DE LA INVENCIÓNTECHNICAL FIELD OF THE INVENTION
La presente invención se refiere al campo técnico de la ecología, ya que proporciona un maquina ecológica para procesar desechos orgánicos e inorgánicos y obtener de ellos productos reutilizables, tales como hidrocarbonos líquidos y gaseosos.The present invention refers to the technical field of ecology, since it provides an ecological machine to process organic and inorganic waste and obtain reusable products from them, such as liquid and gaseous hydrocarbons.
ANTECEDENTES DE LA INVENCIÓNBACKGROUND OF THE INVENTION
Los desechos sólidos orgánicos e inorgánicos, en su mayoría son confinados a rellenos sanitarios y en menor escala se reciclan aprovechando los metales, el papel, ciertos plásticos, vidrio, etc. El inconveniente de los rellenos sanitarios es que deben estar lejos de las zonas urbanas, otra opción es incinerarlos a alta temperatura para utilizarlos como combustible o para generar electricidad, pero contaminan considerablemente.Organic and inorganic solid wastes are mostly confined to sanitary landfills and on a smaller scale are recycled using metals, paper, certain plastics, glass, etc. The drawback of sanitary landfills is that they must be far from urban areas, another option is to incinerate them at high temperatures to use them as fuel or to generate electricity, but they pollute considerably.
Se han desarrollado máquinas, aparatos y procesos para solucionar a los problemas antes mencionados. Por ejemplo, en la patente US 4740270 se describe un proceso para el tratamiento del caucho de los neumáticos usados mediante pirólisis al vacío, para producir hidrocarbonos líquidos y sólidos; el cual consiste en depositar el caucho triturado en un reactor, donde la pirólisis se lleva a acabo entre 360 a 415° C, a presión inferior a los 35 mm Hg, de tal forma que los gases y vapores producidos permanecen pocos segundos, con lo que se incrementa la producción de hidrocarbono líquido y se disminuye la de los hidrocarbonos gaseosos y sólidos. Sin embargo, se requieren de varias etapas para realizar este proceso, haciéndolo más complicado, lo que repercute en el uso de una mayor área de trabajo; además, la configuración de cómo está dispuesto el reactor, dividido en secciones, obliga a utilizar temperaturas altas para calentar las secciones inferiores, y cabe agregar que su tolva de abastecimiento es poco accesible por estar situada en la parte mas alta de la maquina. Otra de las desventajas de que adolece este proceso, es que en la etapa de condensación necesita alcanzar temperaturas de - 20 a - 80 ° C aproximadamente lo que implica el uso de una mezcla de acetona y dióxido de carbono y una solución refrigerante como el etilen glicol.Machines, apparatus and processes have been developed to solve the aforementioned problems. For example, US Patent 4740270 describes a process for treating rubber in used tires by vacuum pyrolysis, to produce liquid and solid hydrocarbons; which consists of depositing the crushed rubber in a reactor, where the pyrolysis is carried out between 360 to 415 ° C, at a pressure of less than 35 mm Hg, so that the gases and vapors produced remain a few seconds, with which that the production of liquid hydrocarbon is increased and that of gaseous and solid hydrocarbons is decreased. However, several stages are required to carry out this process, making it more complicated, which affects the use of a larger work area; In addition, the configuration of how the reactor is arranged, divided into sections, requires the use of high temperatures to heat the lower sections, and it should be added that its supply hopper is not very accessible because it is located in the most remote part. high of the machine. Another disadvantage of this process is that in the condensation stage it needs to reach temperatures of approximately -20 to -80 ° C, which implies the use of a mixture of acetone and carbon dioxide and a cooling solution such as ethylene. glycol.
La patente US 4,613,408 1984 trata de un aparato productor de combustible a partir de desperdicios del tipo que es capaz de formar aceite flamable y gas. El aparato y método son útiles por que se dispone de desechos de llanta de vehículos para producir gas capaz de operar motores y calentadores: el sistema utiliza un pote cocinador que está cerrado y un aparato enfriador para condensar el gas formado en el recipiente cocinador; cabe señalar que la descarga de contaminación a la atmósfera es despreciable. Una desventaja de este aparato es que el pote es removido para ser limpiado de la escoria en periodos regulares. A demás la capacidad de producción de este aparato es baja, pues los desperdicios no son triturados ni son movidos o agitados dentro del pote, retardando así este procesamiento.US Patent 4,613,408 1984 deals with a fuel-producing apparatus from wastes of the type that is capable of forming flammable oil and gas. The apparatus and method are useful in that vehicle tire debris is available to produce gas capable of operating engines and heaters: the system uses a closed cooking pot and a cooling apparatus to condense the gas formed in the cooking container; It should be noted that the discharge of pollution into the atmosphere is negligible. A disadvantage of this apparatus is that the pot is removed to be cleaned of the slag at regular periods. In addition, the production capacity of this apparatus is low, since the waste is not crushed or moved or stirred inside the pot, thus delaying this processing.
Por su parte, la patente US 5836524 describe un aparato y proceso para tratar basura orgánica e inorgánica, que produce combustible reciclable, mediante liquefacción con aceite y pirólisis. El aparato cuenta con un reactor de licuefacción y pirólisis inclinado, el cual a su vez tiene un cuerpo principal y un tornillo sin fin, lugar donde la basura se procesará; y un calentador de aceite se encarga de proporcionarle una temperatura de 200 a 400° C. De la licuefacción y pirólisis de la basura se desprenden gases orgánicos, los cuales son enviados a condensadores para un mejor procesamiento y el aceite ligero es enviado a un separador, para eliminar materiales ferrosos y no ferrosos; mientras que el aceite denso es nuevamente enviado al calentador para iniciar el ciclo otra vez, hasta que se convierta en aceite ligero. Por lo tanto, uno de los inconvenientes de este proceso es el uso de aceite, el cual debe ser precalentado y trasladado al reactor inclinado, encareciendo a dicho proceso.For its part, patent US 5836524 describes an apparatus and process for treating organic and inorganic waste, which produces recyclable fuel, by liquefaction with oil and pyrolysis. The apparatus has an inclined liquefaction and pyrolysis reactor, which in turn has a main body and an endless screw, where the waste will be processed; and an oil heater is responsible for providing a temperature of 200 to 400 ° C. Liquefaction and pyrolysis of the waste emit organic gases, which are sent to condensers for better processing and the light oil is sent to a separator , to remove ferrous and non-ferrous materials; while the dense oil is again sent to the heater to start the cycle again, until it turns into light oil. Therefore, one of the disadvantages of this process is the use of oil, which must be preheated and transferred to the inclined reactor, making this process more expensive.
En la patente WO 03/045595; 2001 se describe una máquina fundidora de llantas, que comprende un horno al vacío para hacer la fundición, un condensador, y un deposito para líquidos, así aplicando temperatura de 350° C, y presión de 10 a 20 mm de Hg, durante 2 a 2:30 h, se obtienen gas y aceite de hidrocarbonos sin contaminar el medio ambiente. La desventaja de esta máquina es que por su configuración solo puede tratar neumáticos.In WO 03/045595; 2001 describes a tire smelting machine, which includes a vacuum oven to make the smelting, a condenser, and a tank for liquids, thus applying a temperature of 350 ° C, and a pressure of 10 to 20 mm Hg, for 2 to 2:30 h, hydrocarbon gas and oil are obtained without contaminating the environment. The disadvantage of this machine is that due to its configuration it can only treat tires.
DESCRIPCIÓN DETALLADA DE LA INVENCIÓN.DETAILED DESCRIPTION OF THE INVENTION.
Los detalles característicos de este maquina ecológica procesadora de desechos orgánicos e inorgánicos se muestran claramente en la siguiente descripción y en las figuras que se acompañan, las cuales se mencionan a manera de ejemplos y no deben considerarse como limitativas.The characteristic details of this ecological organic and inorganic waste processing machine are clearly shown in the following description and in the accompanying figures, which are mentioned as examples and should not be considered as limiting.
Breve descripción de las figuras;Brief description of the figures;
La figura 1 es una vista frontal de la máquina ecológica procesadora de desechos orgánicos e inorgánicos de la presente invención. La figura 2 es una vista lateral derecha de la máquina ecológica de la presente invención. La figura 3 es una vista lateral izquierda de la máquina ecológica de la presente invenciónFigure 1 is a front view of the ecological organic and inorganic waste processing machine of the present invention. Figure 2 is a right side view of the ecological machine of the present invention. Figure 3 is a left side view of the ecological machine of the present invention
La figura 4 es una vista posterior de la máquina ecológica de la presente invención La figura 5 es un corte longitudinal que muestra en detalle el interior de la cámara de vacío de la maquina ecológica de la presente invenciónFigure 4 is a rear view of the ecological machine of the present invention. Figure 5 is a longitudinal section showing in detail the interior of the vacuum chamber of the ecological machine of the present invention.
Con referencia a dichas figuras, la máquina ecológica procesadora de desechos orgánicos e inorgánicos se constituye básicamente de, una base rectangular metálica 38, sobre la cual va montada una cámara cilindrica de vacío 1 , para procesar a los desperdicios orgánicos e inorgánicos, previamente triturados 29, mediante pirólisis a un rango de 250 a 410° C y una presión de 10 a 35 mm Hg; en un cuyos extremos tiene una compuerta de descarga 13 y 40 de los residuos resultantes; en su interior hay horizontalmente un tornillo sin fin 2 que da movimiento a los desperdicios 29, para una mejor y rápida cocción; y es accionado por un motor 14 y un reductor 37. La cámara 1 posee una campana 39 que disipa el exceso de calor a la atmósfera. En la parte superior de dicha cámara 1 se une a un garganta 99 que es un espacio donde se elevan los gases para iniciar su salida a las válvulas 3 y 36. En la válvula 3 existen dos tuberías 33 y 34, que conducen el vapor de agua y gases hidrocarbonos, respectivamente, hacia unos condensadores. El vapor de agua es enfriado en el condensador 9 y transportado a un filtro 98 para ser liberado al ambiente. Mientras que los gases hidrocarbonos son enfriados en un condensador 4 para después ser depositado en forma líquida en un separador 5, posteriormente, el vapor hidrocarbono es extraído por la bomba de vacío compresor 7 para ser comprimido en un tanque de deposito 8. La válvula de alivio 36 es útil en caso de sobre presión, con lo que se evitan accidentes. Para alimentar a la cámara 1 de desechos, ésta cuenta con una compuerta de carga 12 y a demás una ventana blindada de observación 11 , ubicadas externamente en la garganta 99.With reference to these figures, the ecological organic and inorganic waste processing machine basically consists of a rectangular metal base 38, on which a cylindrical vacuum chamber 1 is mounted, to process organic and inorganic waste, previously crushed 29 , by pyrolysis at a range of 250 to 410 ° C and a pressure of 10 to 35 mm Hg; at one end of which it has a discharge gate 13 and 40 of the resulting waste; inside there is horizontally a worm screw 2 that gives movement to the waste 29, for a better and faster cooking; and is powered by a motor 14 and a reducer 37. Chamber 1 has a hood 39 that dissipates excess heat into the atmosphere. In the upper part of said chamber 1 it is joined to a throat 99 which is a space where the gases rise to start their exit to valves 3 and 36. In valve 3 there are two pipes 33 and 34, which conduct the steam from water and hydrocarbon gases, respectively, towards condensers. The water vapor is cooled in the condenser 9 and transported to a filter 98 to be released into the environment. While the hydrocarbon gases are cooled in a condenser 4 to be later deposited in liquid form in a separator 5, subsequently, the hydrocarbon vapor is extracted by the compressor vacuum pump 7 to be compressed in a tank 8. relief 36 is useful in case of over pressure, thus avoiding accidents. To feed the waste chamber 1, it has a loading gate 12 and a further armored observation window 11, located externally in the throat 99.
La cámara de vacío 1 es calentada por un quemador 35 ubicado en uno de sus costados, el cual a su vez comprende un alimentador 66 que lo provee de energía.The vacuum chamber 1 is heated by a burner 35 located on one of its sides, which in turn comprises a feeder 66 that provides it with energy.
Los condensadores 4 y 9 son enfriados por un ventilador 18 el cual permite la circulación de agua fría, valiéndose para ello de una bomba 10.Condensers 4 and 9 are cooled by a fan 18 which allows the circulation of cold water, using a pump 10 for this.
La máquina cuenta con un panel de control 97 donde están situados vacuo metro, manómetros y termómetros para controlar y monitorear su funcionamiento. Además cuenta con una pared divisora 31 para separar al panel de control de la cámara de vacío 1. Esta última puede llevar como accesorio adicional una chaqueta para recuperar el calor que ésta irradie. Funcionamiento de la máquina ecológica procesadora de desechos orgánicos e inorgánicosThe machine has a 97 control panel where vacuum meter, manometers and thermometers are located to control and monitor its operation. It also has a dividing wall 31 to separate the control panel from the vacuum chamber 1. The latter may have a jacket as an additional accessory to recover the heat that it radiates. Operation of the ecological organic and inorganic waste processing machine
Para el funcionamiento de la máquina ecológica procesadora de desechos orgánicos e inorgánicos, estos son previamente triturados y secados, son depositados a la cámara de vacío 1 por la compuerta de carga 12; esta se cierra herméticamente; posteriormente se enciende el quemador 35 y la bomba de vacío compresor 7 extraer el aire de la cámara, procurando tener una presión entre 10 a 35 mm Hg y una temperatura de 250 a 410° C. De esta forma se inicia una pirólisis, donde los primeros gases emanados son vapor de agua, el cual es conducido por la tubería 33 hasta un condensador 9, pasando por un filtro 98 para ser disipado a la atmósfera. Una vez eliminado todo el vapor de agua, se cierra la tubería 33, y se abre la tubería 34 para conducir los gases hidrocarbonos al condensador 4, pasando al separador 5, donde quedan depositados los hidrocarburos líquidos y los gaseosos son extraídos por la bomba de vacío compresor 7 y los comprime en un tanque de depósito 8. Los condensadores son enfriados por agua y un ventilador 18.For the operation of the ecological machine for processing organic and inorganic waste, these are previously crushed and dried, they are deposited in the vacuum chamber 1 by the loading gate 12; it closes hermetically; Subsequently, the burner 35 is ignited and the compressor vacuum pump 7 extracts the air from the chamber, trying to have a pressure between 10 to 35 mm Hg and a temperature of 250 to 410 ° C. In this way a pyrolysis begins, where the The first gases emanating are water vapor, which is conducted through line 33 to a condenser 9, passing through a filter 98 to be dissipated into the atmosphere. Once all the water vapor has been removed, line 33 is closed, and line 34 is opened to conduct the hydrocarbon gases to condenser 4, passing to separator 5, where the liquid hydrocarbons are deposited and the gaseous ones are extracted by the vacuum compressor 7 and compresses them into a reservoir tank 8. The condensers are cooled by water and a fan 18.
De esta manera se obtiene una máquina ecológica capaz de procesar varios tipos de desechos orgánicos e inorgánicos y obtener a partir de ellos, productos reutilizables, tales como hidrocarbonos líquidos, sólidos y gaseosos. Además de ser construcción sencilla y compacta por estar conformada por pocos elementos. Es ahorradora de energía, ya que las distintas etapas del proceso se llevan a cabo en una sola sección. Para su funcionamiento de requiere de gas y electricidad, lo que no sucede en la patente US 5836524, que requiere de aceite. Para el enfriado de los gases sólo se requiere de agua y aire ambiental, mientras que en la patente US 4740270, se necesita de acetona, C02 y etilen glicol. In this way, an ecological machine is obtained capable of processing various types of organic and inorganic waste and obtaining reusable products from them, such as liquid, solid and gaseous hydrocarbons. In addition to being simple and compact construction for being made up of few elements. It is energy saving, since the different stages of the process are carried out in a single section. For its operation it requires gas and electricity, which does not happen in US patent 5836524, which requires oil. For gas cooling, only water and ambient air are required, whereas in US patent 4740270, acetone, C02 and ethylene glycol are required.
Claims
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| PCT/MX2003/000097 WO2005044952A1 (en) | 2003-11-10 | 2003-11-10 | Environmentally-friendly machine for the treatment of organic and inorganic waste |
| AU2003279593A AU2003279593A1 (en) | 2003-11-10 | 2003-11-10 | Environmentally-friendly machine for the treatment of organic and inorganic waste |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| PCT/MX2003/000097 WO2005044952A1 (en) | 2003-11-10 | 2003-11-10 | Environmentally-friendly machine for the treatment of organic and inorganic waste |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO2005044952A1 true WO2005044952A1 (en) | 2005-05-19 |
Family
ID=34567895
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/MX2003/000097 Ceased WO2005044952A1 (en) | 2003-11-10 | 2003-11-10 | Environmentally-friendly machine for the treatment of organic and inorganic waste |
Country Status (2)
| Country | Link |
|---|---|
| AU (1) | AU2003279593A1 (en) |
| WO (1) | WO2005044952A1 (en) |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| ES444715A1 (en) * | 1975-02-10 | 1977-09-01 | Deco Ind | A method of obtaining hydrocarbon products. (Machine-translation by Google Translate, not legally binding) |
| US4098649A (en) * | 1974-05-06 | 1978-07-04 | Redker-Young Processes, Inc. | Conversion of organic waste material |
| US5720232A (en) * | 1996-07-10 | 1998-02-24 | Meador; William R. | Method and apparatus for recovering constituents from discarded tires |
| WO2003045595A1 (en) * | 2001-10-25 | 2003-06-05 | Rodriguez Mancilla Jose De Jes | Tyre-melting machine |
-
2003
- 2003-11-10 WO PCT/MX2003/000097 patent/WO2005044952A1/en not_active Ceased
- 2003-11-10 AU AU2003279593A patent/AU2003279593A1/en not_active Abandoned
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4098649A (en) * | 1974-05-06 | 1978-07-04 | Redker-Young Processes, Inc. | Conversion of organic waste material |
| ES444715A1 (en) * | 1975-02-10 | 1977-09-01 | Deco Ind | A method of obtaining hydrocarbon products. (Machine-translation by Google Translate, not legally binding) |
| US5720232A (en) * | 1996-07-10 | 1998-02-24 | Meador; William R. | Method and apparatus for recovering constituents from discarded tires |
| WO2003045595A1 (en) * | 2001-10-25 | 2003-06-05 | Rodriguez Mancilla Jose De Jes | Tyre-melting machine |
Also Published As
| Publication number | Publication date |
|---|---|
| AU2003279593A1 (en) | 2005-05-26 |
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