WO2015111993A1 - Allume-feu à base de cellulose carbonisée à haute porosité imprégnée de biocombustible - Google Patents

Allume-feu à base de cellulose carbonisée à haute porosité imprégnée de biocombustible Download PDF

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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
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.)
Ceased
Application number
PCT/MX2014/000019
Other languages
English (en)
Spanish (es)
Inventor
José Martín VELEZ DE LA ROCHA
Felipe CARO RAMOS
Dino Alenjandro PARDO GUZMAN
Gerardo Trinidad PAREDES QUIJADA
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to PCT/MX2014/000019 priority Critical patent/WO2015111993A1/fr
Publication of WO2015111993A1 publication Critical patent/WO2015111993A1/fr
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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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 OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • 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 OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L11/00—Fire-lighters
    • C10L11/04—Fire-lighters 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 OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • 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 OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • 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 OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • 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 OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • 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

L'invention concerne une sphère à base de fibre de coton avec étoupe blanche hautement imprégnée de biodiesel pour obtenir un allumage de feu prolongé, permettant à son tour d'allumer d'autres matériaux tels que du charbon de bois de manière simple et pratique et sans fumée.
PCT/MX2014/000019 2014-01-23 2014-01-23 Allume-feu à base de cellulose carbonisée à haute porosité imprégnée de biocombustible Ceased WO2015111993A1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
PCT/MX2014/000019 WO2015111993A1 (fr) 2014-01-23 2014-01-23 Allume-feu à base de cellulose carbonisée à haute porosité imprégnée de biocombustible

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/MX2014/000019 WO2015111993A1 (fr) 2014-01-23 2014-01-23 Allume-feu à base de cellulose carbonisée à haute porosité imprégnée de biocombustible

Publications (1)

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

Family

ID=53681710

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/MX2014/000019 Ceased WO2015111993A1 (fr) 2014-01-23 2014-01-23 Allume-feu à base de cellulose carbonisée à haute porosité imprégnée de biocombustible

Country Status (1)

Country Link
WO (1) WO2015111993A1 (fr)

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 (fr) * 2011-06-10 2012-12-13 Danmarks Tekniske Universitet (Dtu) Torréfaction et pyrolyse partielle pour produire des pastilles combustibles à l'aide d'un flux de goudron à contre-courant
US20130040248A1 (en) * 2011-08-08 2013-02-14 Daniel Perlman Composite fuel for fires
WO2013036694A1 (fr) * 2011-09-06 2013-03-14 Johnston John C Système réacteur de torréfaction et de pyrolyse combinées à conversion thermique et son procédé

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 (fr) * 2011-06-10 2012-12-13 Danmarks Tekniske Universitet (Dtu) Torréfaction et pyrolyse partielle pour produire des pastilles combustibles à l'aide d'un flux de goudron à contre-courant
US20130040248A1 (en) * 2011-08-08 2013-02-14 Daniel Perlman Composite fuel for fires
WO2013036694A1 (fr) * 2011-09-06 2013-03-14 Johnston John C Système réacteur de torréfaction et de pyrolyse combinées à conversion thermique et son procédé

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 *

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