WO2015111993A1 - Fire-lighter using highly porous carbonised cellulose impregnated with biofuel - Google Patents

Fire-lighter using highly porous carbonised cellulose impregnated with biofuel Download PDF

Info

Publication number
WO2015111993A1
WO2015111993A1 PCT/MX2014/000019 MX2014000019W WO2015111993A1 WO 2015111993 A1 WO2015111993 A1 WO 2015111993A1 MX 2014000019 W MX2014000019 W MX 2014000019W WO 2015111993 A1 WO2015111993 A1 WO 2015111993A1
Authority
WO
WIPO (PCT)
Prior art keywords
fibro
carbonized
cavernous
fire
degrees celsius
Prior art date
Application number
PCT/MX2014/000019
Other languages
Spanish (es)
French (fr)
Inventor
José Martín VELEZ DE LA ROCHA
Felipe CARO RAMOS
Dino Alenjandro PARDO GUZMAN
Gerardo Trinidad PAREDES QUIJADA
Original Assignee
Velez De La Rocha José Martín
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 Velez De La Rocha José Martín filed Critical Velez De La Rocha José Martín
Priority to PCT/MX2014/000019 priority Critical patent/WO2015111993A1/en
Publication of WO2015111993A1 publication Critical patent/WO2015111993A1/en

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L5/00—Solid fuels
    • C10L5/40—Solid fuels essentially based on materials of non-mineral origin
    • C10L5/44—Solid fuels essentially based on materials of non-mineral origin on vegetable substances
    • C10L5/447—Carbonized vegetable substances, e.g. charcoal, or produced by hydrothermal carbonization of biomass
    • 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
    • C10B53/02—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form of cellulose-containing material
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L11/00—Manufacture of firelighters
    • C10L11/04—Manufacture of firelighters consisting of combustible material
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L2200/00—Components of fuel compositions
    • C10L2200/04—Organic compounds
    • C10L2200/0461—Fractions defined by their origin
    • C10L2200/0469—Renewables or materials of biological origin
    • C10L2200/0476—Biodiesel, i.e. defined lower alkyl esters of fatty acids first generation biodiesel
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
    • C10L2290/02—Combustion or pyrolysis
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
    • C10L2290/08—Drying or removing water
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
    • C10L2290/22—Impregnation or immersion of a fuel component or a fuel as a whole
    • Y—GENERAL 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
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00—Technologies for the production of fuel of non-fossil origin
    • Y02E50/10—Biofuels, e.g. bio-diesel
    • Y—GENERAL 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
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00—Technologies for the production of fuel of non-fossil origin
    • Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel

Definitions

  • the present invention is applied in the safe preparation of food with heat supply by means of natural coal.
  • Combustion materials normally, even if they have been dried, have a humidity level resulting from the environmental contact and the absorption process, increasing the energy required to remove this water which has a maximum evaporation point around 100 9 C, after elimination. of water the main material increases the temperature to start its own combustion which happens in these materials at a temperature higher than 260 9 C and in its final exothermic phase temperatures are reached in the range of 400-700 9 C.
  • the objective of the invention is to manufacture a body capable of providing the initial heat that allows the ignition of these materials. Therefore this ignition body must have a low flash point, have prolonged and self-controlled combustion to give constant energy at the beginning of the combustion of the main material.
  • Figure 1 is a schematic diagram of the manufacturing process of the solid fire starter of the present invention.
  • the present invention describes a method of manufacturing a carbonized body of rapid ignition and slow combustion (16) characterized by: a) a fibro-cavernous body (1), with more than 60% cellulose is carbonized by exposure to more than 380 degrees Celsius in an oven (15) until its radiation absorption in the visible spectrum is less than 5% (3); b) the carbonized fibrocavernous body is transported by a band (4) to a cooling chamber (5) until a temperature of 50 to 60 degrees Celsius is reached as indicated by an ambient temperature sensor (6); c) the fibro-cavernous body is impregnated with methyl esters derived from fatty acids (7); d) the body is transported by drying bands (8) to collect excess fluid in the body and reach room temperature; e) the excess liquid is captured for recirculation in a container (9) and returned to the impregnation container (10).
  • cavernous fibro body is spun natural cotton fiber (1), with a very low density screen, at least 40% of air;
  • the fibrous solid body before being carbonized has a density of between 0.3-0.5 weight over volume (g / cm3).
  • the virgin natural cellulose fiber is molded according to the purpose or use that is required, in this case it was spherically molded and the material was 100% carbonized at a temperature of 400 9 C. Once carbonized it was impregnated with fuel at the rate 45-55% volume of fuel over total body volume of previously carbonized fiber.
  • the impregnation fuel with calorific value of 35-40 mega joules / liter, 0.88 g / cm3 density contains fast combustion fuel of 3-5% weight fraction.
  • This fuel has a flash point above 130 9 C and is biodegradable non-toxic and immiscible with water.
  • the solid transport body ⁇ fuel support is previously carbonized for the elimination of nitrogen and hydrogen oxygen which increases the carbon content achieving a high level of porosity and adhesion surface that is complemented by the polar absorption capacity of coal and fuel .
  • the combustion occurs gradually and self-controlled on the external surface of the body where the total fuel flows by capillarity through the carbonized internal fibers and naturally mixes with the ambient air allowing temperatures to reach more than 400 0 C sufficient to propagate and accelerate the ignition of other materials.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Materials Engineering (AREA)
  • Combustion & Propulsion (AREA)
  • Manufacturing & Machinery (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Sustainable Development (AREA)
  • Solid Fuels And Fuel-Associated Substances (AREA)

Abstract

The invention relates to a ball of cotton fibre with a white tow which is highly impregnated with biodiesel in order to be able to ignite a sustainable fire which allows, in turn, the ignition of other materials such as charcoal in a simple and practical manner, without smoke.

Description

INICIADOR DE FUEGO POR CELULOSA CARBONIZADA DE ALTA POROSIDAD IMPREGNADA CON  FIRE INITIATOR BY CARBONIZED CELLULOSE OF HIGH POROSITY IMPREGNATED WITH
BIOCOMBUSTIBLES  BIOFUELS
CAMPO TÉCNICO DE LA INVENCIÓN La presente invención se aplica en la preparación segura de alimentos con suministro de calor por medio de carbón natural. TECHNICAL FIELD OF THE INVENTION The present invention is applied in the safe preparation of food with heat supply by means of natural coal.
ANTECEDENTES DE LA INVENCIÓN BACKGROUND OF THE INVENTION
En la combustión de materiales para diferentes fines siempre se requiere una cantidad mayor de energía calorífica para aumentar la temperatura e iniciar la combustión del material. Este proceso es laborioso y puede hacerse haciendo combustión de un líquido más volátil y de menor punto de inflamación o incluso con un material gaseoso e inyección de aire; los líquidos volátiles de punto de inflamación bajo son generalmente difíciles de manejar por su peligrosidad y. toxicidad al igual que los gases de combustión conocidos ihdustrialmente. También se suele iniciar la combustión del material principal con materiales más ligeros o menos densos en su estructura para favorecer la combustión inicial, estos materiales son productos a base de celulosa tales como astilla de madera, paja, corteza pequeña que se consumen con mayor rapidez generando la energía calorífica para iniciar la combustión del material principal y existen algunos a base de alcohol sólido para el mismo fin. En la combustión se da un proceso de oxidación química liberándose calor y luz manifestándose como fuego es necesario alcanzar una temperatura de ignición donde los vapores del material arden espontáneamente alcanzando después la temperatura de inflamación donde los propios vapores continúan ardiendo sin necesidad de alimentar calor externo. In the combustion of materials for different purposes, a greater amount of heat energy is always required to increase the temperature and initiate the combustion of the material. This process is laborious and can be done by burning a more volatile liquid with a lower flash point or even with a gaseous material and air injection; volatile low flash point liquids are generally difficult to handle due to their danger and . toxicity as well as industrially known combustion gases. Combustion of the main material is also usually initiated with lighter or less dense materials in its structure to favor initial combustion, these materials are cellulose-based products such as wood chips, straw, small bark that are consumed more quickly generating the heat energy to start the combustion of the main material and there are some based on solid alcohol for the same purpose. In combustion there is a process of chemical oxidation releasing heat and light manifesting itself as fire, it is necessary to reach an ignition temperature where the vapors of the material burn spontaneously after reaching the flash point where the vapors themselves continue to burn without the need to feed external heat.
Los materiales de combustión normalmente aunque hayan sido secados presentan un nivel de humedad producto del contacto ambiental y del proceso de absorción aumentando la energía requerida para eliminar esta agua la cual tiene un punto de evaporación máxima alrededor de los 100 9C, posterior a la eliminación del agua el material principal aumenta la temperatura para iniciar su propia combustión lo cual sucede en estos materiales a la temperatura superior a los 260 9C y en su fase final exotérmica se alcanzan temperaturas del rango de 400-700 9C. El objetivo de la invención es fabricar un cuerpo capaz de aportar el calor inicial que permita el encendido de estos materiales. Por lo tanto este cuerpo de ignición debe de tener un punto de inflamación bajo, presentar combustión prolongada y autocontrolada para dar energía constante al inicio de la combustión del material principal. Combustion materials normally, even if they have been dried, have a humidity level resulting from the environmental contact and the absorption process, increasing the energy required to remove this water which has a maximum evaporation point around 100 9 C, after elimination. of water the main material increases the temperature to start its own combustion which happens in these materials at a temperature higher than 260 9 C and in its final exothermic phase temperatures are reached in the range of 400-700 9 C. The objective of the invention is to manufacture a body capable of providing the initial heat that allows the ignition of these materials. Therefore this ignition body must have a low flash point, have prolonged and self-controlled combustion to give constant energy at the beginning of the combustion of the main material.
DESCRIPCION DETALLADA DE LA INVENCIÓN DETAILED DESCRIPTION OF THE INVENTION
Los detalles característicos de la presente invención se muestran en la siguiente descripción y figuras y que se acompañan para la presente invención. The characteristic details of the present invention are shown in the following description and figures and which are attached for the present invention.
Breve descripción de las figuras: Brief description of the figures:
La figura 1 es un diagrama esquemático del proceso de fabricación del arrancador sólido de fuego de la presente invención. Figure 1 is a schematic diagram of the manufacturing process of the solid fire starter of the present invention.
DESCRIPCIÓN DESCRIPTION
La presente invención describe un método de fabricación de un cuerpo carbonizado de rápida ignición y lenta combustión (16) caracterizado por: a) un cuerpo fibro-cavernoso (1), con más de 60% de celulosa es carbonizado mediante exposición a más de 380 grados Celsius en un horno (15) hasta que su absorción de radiación en el espectro visible es menor de 5% (3); b) el cuerpo fibro- cavernoso carbonizado es transportado por una banda (4) a una cámara de enfriamiento (5) hasta alcanzar una temperatura de 50 a 60 grados Celsius según indica un sensor de temperatura ambiental (6); c) el cuerpo fibro-cavernoso es impregnado con métil ésteres derivado de ácidos grasos (7); d) el cuerpo es transportado por bandas de secado (8) para colectar el exceso de líquido en el cuerpo y alcanzar la temperatura ambiente; e) el exceso de liquido es capturado para su recirculación en un contenedor (9) y retornado al contenedor de impregnación (10). The present invention describes a method of manufacturing a carbonized body of rapid ignition and slow combustion (16) characterized by: a) a fibro-cavernous body (1), with more than 60% cellulose is carbonized by exposure to more than 380 degrees Celsius in an oven (15) until its radiation absorption in the visible spectrum is less than 5% (3); b) the carbonized fibrocavernous body is transported by a band (4) to a cooling chamber (5) until a temperature of 50 to 60 degrees Celsius is reached as indicated by an ambient temperature sensor (6); c) the fibro-cavernous body is impregnated with methyl esters derived from fatty acids (7); d) the body is transported by drying bands (8) to collect excess fluid in the body and reach room temperature; e) the excess liquid is captured for recirculation in a container (9) and returned to the impregnation container (10).
El método descrito anteriormente, donde el cuerpo fibro-cavernoso (1) una vez moldeado y porcionado (2) es expuesto al fuego en un horno (15) y el contenido de oxígeno en el horno es monitoreádo por un sensor químico (11) y controlado por un procesador de datos (12) para mantener la temperatura a menos de 700 grados Celsius; dicho cuerpo es modificado por calor y combustión controlada (3). El mismo método antes descrito, donde el control de oxígeno en el horno es alcanzado mediante flujo de aire suministrado desde el medio ambiente (14) a través de una válvula de control manual o electrónico (13); The method described above, where the fibro-cavernous body (1) once molded and portioned (2) is exposed to fire in an oven (15) and the oxygen content in the oven is monitored by a chemical sensor (11) and controlled by a data processor (12) to keep the temperature below 700 degrees Celsius; said body is modified by heat and controlled combustion (3). The same method described above, where the control of oxygen in the oven is achieved by the flow of air supplied from the environment (14) through a manual or electronic control valve (13);
El mismo método descrito anteriormente, donde el cuerpo fibro cavernoso es fibra de algodón natural hilada (1), con tramado de muy baja densidad, al menos 40% de aire; The same method described above, where the cavernous fibro body is spun natural cotton fiber (1), with a very low density screen, at least 40% of air;
MODO PREFERENTE DE IMPLEMENTACION PREFERRED IMPLEMENTATION MODE
Arrancador sólido de fuego a base de fibra de celulosa mayor del 90 % carbonizada y con alta superficie de contacto que permite aireación y combustión superficial del combustible alternativo proveniente de esterificación y transesterificación de aceites vegeta les y/o animales. Solid fire starter based on cellulose fiber greater than 90% carbonized and with high contact surface that allows aeration and superficial combustion of the alternative fuel from esterification and transesterification of vegetable and / or animal oils.
El cuerpo sólido fibroso antes de ser carbonizado tiene una densidad de entre 0.3-0.5 de peso sobre volumen (g/cm3). The fibrous solid body before being carbonized has a density of between 0.3-0.5 weight over volume (g / cm3).
La fibra virgen de celulosa natural es moldeada de acuerdo a la finalidad o uso que se requiera, en este caso se moldeó esféricamente y se carbonizó al 100% el material a una temperatura de 400 9C. Una vez carbonizado se impregnó de combustible a razón de 45-55 % volumen de combustible sobre volumen total del cuerpo de fibra previamente carbonizada. The virgin natural cellulose fiber is molded according to the purpose or use that is required, in this case it was spherically molded and the material was 100% carbonized at a temperature of 400 9 C. Once carbonized it was impregnated with fuel at the rate 45-55% volume of fuel over total body volume of previously carbonized fiber.
El combustible de impregnación con poder calorífico de 35-40 mega julios / litro, 0.88 g/cm3 de densidad contiene combustible de rápida combustión del 3-5 % fracción peso. The impregnation fuel with calorific value of 35-40 mega joules / liter, 0.88 g / cm3 density contains fast combustion fuel of 3-5% weight fraction.
Este combustible tiene un punto de inflamación arriba de 130 9C y es biodegradable no tóxico e inmiscible con el agua. This fuel has a flash point above 130 9 C and is biodegradable non-toxic and immiscible with water.
El cuerpo sólido de transporte γ soporte de combustible previamente es carbonizado para la eliminación de oxigeno nitrógeno e hidrógeno lo cual aumenta el contenido carbónico lográndose un alto nivel de porosidad y superficie de adherencia que se complementa con la capacidad de absorción polar del carbón y el combustible. La combustión se da de manera gradual y auto controlada en la superficie externa del cuerpo donde el combustible total fluye por capilaridad a través de las fibras internas carbonizadas y se mezcla naturalmente con el aire ambiental permitiendo alcanzar temperaturas de más de 400 0 C suficientes para propagar y acelerar el encendido de otros materiales. The solid transport body γ fuel support is previously carbonized for the elimination of nitrogen and hydrogen oxygen which increases the carbon content achieving a high level of porosity and adhesion surface that is complemented by the polar absorption capacity of coal and fuel . The combustion occurs gradually and self-controlled on the external surface of the body where the total fuel flows by capillarity through the carbonized internal fibers and naturally mixes with the ambient air allowing temperatures to reach more than 400 0 C sufficient to propagate and accelerate the ignition of other materials.

Claims

REIVINDICACIONES
1. Un método de fabricación de un cuerpo carbonizado de rápida ignición y lenta combustión caracterizado porque comprende los siguientes pasos: a) un cuerpo fibro-cavernoso, con más de 60% de celulosa es carbonizado mediante exposición a más de 380 grados Celsius en un horno hasta que su absorción de radiación en el espectro visible es menor de 5%; b) el cuerpo fibro-cavernoso carbonizado es transportado a una cámara de enfriamiento hasta 50 grados Celsius; c) el cuerpo fibro-cavernoso es impregnado con métil ésteres derivado de ácidos grasos; y d) el cuerpo es transportado por bandas de secado para colectar el exceso de líquido en el cuerpo y alcanzar la temperatura ambiente. 1. A method of manufacturing a carbonized body of rapid ignition and slow combustion characterized in that it comprises the following steps: a) a fibro-cavernous body with more than 60% cellulose is carbonized by exposure to more than 380 degrees Celsius in a oven until its absorption of radiation in the visible spectrum is less than 5%; b) the carbonized fibro-cavernous body is transported to a cooling chamber up to 50 degrees Celsius; c) the fibro-cavernous body is impregnated with methyl esters derived from fatty acids; and d) the body is transported by drying bands to collect excess fluid in the body and reach room temperature.
Un método como el descrito en reivindicación número 1, donde el cuerpo fibro-cavernoso es expuesto al fuego, y el contenido de oxígeno en el horno es controlado para mantener la temperatura a menos de 700 grados Celsius. A method as described in claim number 1, wherein the fibro-cavernous body is exposed to fire, and the oxygen content in the oven is controlled to maintain the temperature at less than 700 degrees Celsius.
Un método como el descrito en reivindicación número 2, donde el control de oxígeno en el horno es alcanzado mediante flujo de aire suministrado desde el medio ambiente a través de una válvula de control manual o electrónico. A method as described in claim number 2, wherein the control of oxygen in the oven is achieved by flow of air supplied from the environment through a manual or electronic control valve.
Un método como el descrito en reivindicación número 1, donde el cuerpo fibro cavernoso es fibra de algodón natural hilada, con tramado de muy baja densidad, al menos 40% de aire. A method as described in claim number 1, wherein the cavernous fibro body is spun natural cotton fiber, with a very low density screen, at least 40% air.
PCT/MX2014/000019 2014-01-23 2014-01-23 Fire-lighter using highly porous carbonised cellulose impregnated with biofuel WO2015111993A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
PCT/MX2014/000019 WO2015111993A1 (en) 2014-01-23 2014-01-23 Fire-lighter using highly porous carbonised cellulose impregnated with biofuel

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/MX2014/000019 WO2015111993A1 (en) 2014-01-23 2014-01-23 Fire-lighter using highly porous carbonised cellulose impregnated with biofuel

Publications (1)

Publication Number Publication Date
WO2015111993A1 true WO2015111993A1 (en) 2015-07-30

Family

ID=53681710

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/MX2014/000019 WO2015111993A1 (en) 2014-01-23 2014-01-23 Fire-lighter using highly porous carbonised cellulose impregnated with biofuel

Country Status (1)

Country Link
WO (1) WO2015111993A1 (en)

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3950143A (en) * 1972-07-14 1976-04-13 The Kingsford Company Process for producing solid industrial fuel
US5244472A (en) * 1987-05-13 1993-09-14 Simmons John J Preparation of chemically dried cellulosic fuel
WO2012167795A1 (en) * 2011-06-10 2012-12-13 Danmarks Tekniske Universitet (Dtu) Torrefaction and partial pyrolysis to produce fuel pellets with counter current flow of tar
US20130040248A1 (en) * 2011-08-08 2013-02-14 Daniel Perlman Composite fuel for fires
WO2013036694A1 (en) * 2011-09-06 2013-03-14 Johnston John C A thermal conversion combined torrefaction and pyrolysis reactor system and method thereof

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3950143A (en) * 1972-07-14 1976-04-13 The Kingsford Company Process for producing solid industrial fuel
US5244472A (en) * 1987-05-13 1993-09-14 Simmons John J Preparation of chemically dried cellulosic fuel
WO2012167795A1 (en) * 2011-06-10 2012-12-13 Danmarks Tekniske Universitet (Dtu) Torrefaction and partial pyrolysis to produce fuel pellets with counter current flow of tar
US20130040248A1 (en) * 2011-08-08 2013-02-14 Daniel Perlman Composite fuel for fires
WO2013036694A1 (en) * 2011-09-06 2013-03-14 Johnston John C A thermal conversion combined torrefaction and pyrolysis reactor system and method thereof

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
ABDULLAH ET AL.: "Bioslurry as a Fuel.4. Preparation of Bioslurry Fuels from Biochar and the Bio-oil-Rich Fractions after Bio-oil/Biodiesel Extraction", ENERGY & FUELS, vol. 25, no. 4, 2011, pages 1759 - 1771, XP055214732 *
KOLOKOLOKOVA ET AL.: "Torrefaction and Pyrolyis of biomass waste on continuous reactors.", CEST2013, ATHENS, GREECE, XP055214734 *

Similar Documents

Publication Publication Date Title
EP0953033B1 (en) Combustible fuel source
US8647399B2 (en) Fire starter
CA2805871A1 (en) Meltable fuel gas generation methods
CN203128520U (en) Composite biomass fuel brick
KR20160147429A (en) The complexing agent for the solid fuel
ATE547460T1 (en) POROUS UNFUELABLE POLYMER PARTS
EP2638132B1 (en) Fire starter
WO2015111993A1 (en) Fire-lighter using highly porous carbonised cellulose impregnated with biofuel
ES2759932T3 (en) Product for the control of insect pests and method for the control of insect pests
RU2522235C1 (en) Ignition device
RU87164U1 (en) WASTE DEVICE
JP2017036883A (en) Woody biomass boiler
Bae et al. An investigation of the evaporation behavior of bioliquid in the pores and its application to hybrid coal combining biomass with coal
ES2402450T3 (en) Fuel to heat a barbecue device
JP5587966B2 (en) Inflammable incense for burning smoke
RU163877U1 (en) FLOWERS
WO2015111992A1 (en) Quick-lighting and slow-burning coal
EP2096159A1 (en) Fire starter composition comprising 2-phenoxyethanol
JP5220498B2 (en) Method for delaying burning of incense for smoke
KR20150117952A (en) Solid fuel use an oak and manufacturing method of the same
RU2393381C1 (en) Flameless solid fuel combustion method
RU2582617C1 (en) Starting agent
KR101655659B1 (en) Smoke cooking apparatus
JP2004269835A (en) Carbonized matter having good ignition and burning properties and used as fuel, and method for producing the same
Abreu et al. Elementary, Chemical and Energy Characterization of “Dendê”(Elaeis guineensis Jacq.) Waste in the State of Pará

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 14879802

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 14879802

Country of ref document: EP

Kind code of ref document: A1