WO2009128735A2 - Procédé et dispositif permettant de dissocier de l'eau destinée à des chauffe-eau - Google Patents

Procédé et dispositif permettant de dissocier de l'eau destinée à des chauffe-eau Download PDF

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Publication number
WO2009128735A2
WO2009128735A2 PCT/PH2009/000004 PH2009000004W WO2009128735A2 WO 2009128735 A2 WO2009128735 A2 WO 2009128735A2 PH 2009000004 W PH2009000004 W PH 2009000004W WO 2009128735 A2 WO2009128735 A2 WO 2009128735A2
Authority
WO
WIPO (PCT)
Prior art keywords
fuel
boiler
hydrogen
tubing
fire tube
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/PH2009/000004
Other languages
English (en)
Other versions
WO2009128735A3 (fr
Inventor
Roberto V. Celis
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
Publication of WO2009128735A2 publication Critical patent/WO2009128735A2/fr
Publication of WO2009128735A3 publication Critical patent/WO2009128735A3/fr
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23K—FEEDING FUEL TO COMBUSTION APPARATUS
    • F23K5/00—Feeding or distributing other fuel to combustion apparatus
    • F23K5/002—Gaseous fuel
    • F23K5/007—Details
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B13/00—Oxygen; Ozone; Oxides or hydroxides in general
    • C01B13/02—Preparation of oxygen
    • C01B13/0203—Preparation of oxygen from inorganic compounds
    • C01B13/0207—Water
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen; Reversible storage of hydrogen
    • C01B3/02—Production of hydrogen; Production of gaseous mixtures containing hydrogen
    • C01B3/04—Production of hydrogen; Production of gaseous mixtures containing hydrogen by decomposition of inorganic compounds
    • C01B3/042—Decomposition of water
    • C01B3/045—Decomposition of water in gaseous phase
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24—HEATING; RANGES; VENTILATING
    • F24D—DOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
    • F24D12/00—Other central heating systems
    • F24D12/02—Other central heating systems having more than one heat source
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23C—METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
    • F23C2900/00—Special features of, or arrangements for combustion apparatus using fluid fuels or solid fuels suspended in air; Combustion processes therefor
    • F23C2900/9901—Combustion process using hydrogen, hydrogen peroxide water or brown gas as fuel
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23K—FEEDING FUEL TO COMBUSTION APPARATUS
    • F23K2400/00—Pretreatment and supply of gaseous fuel
    • F23K2400/10—Pretreatment
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24—HEATING; RANGES; VENTILATING
    • F24D—DOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
    • F24D2200/00—Heat sources or energy sources
    • F24D2200/16—Waste heat
    • F24D2200/18—Flue gas recuperation
    • 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
    • Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
    • 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
    • Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30—Hydrogen technology
    • Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
    • 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
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/10—Process efficiency
    • 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
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/10—Process efficiency
    • Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines

Definitions

  • the present invention relates to a fuel saving method and device and more particularly to a method and device for dissociating water between 710' F and 120 ' F into its constituents hydrogen gases to be used as supplemental fuel and fuel enhancer for boilers to cause complete combustion, save fuel, near zero emission to prevent global warming, greatly reduce maintenance cost due to clean combustion and exhaust system and release oxygen that will contribute to a healthier environment.
  • the method consists of passing pressurized water in controlled flow through a coiled stainless economizer tubing around the inner wall of the chimney of said boiler in order to recover waste heat to preheat the water.
  • the forward end of the coil is connected in fluid communication with the straight stainless super heater tubing that passes concentrically through the larger outer fire tube of the boiler, makes a U-turn and inters the larger straight inner fire tube of the boiler to super heat and exit at the open end of said fire tube and connects in fluid communication with a larger coiled stainless dissociation tube in the combustion chamber of the boiler to discharge the super heated steam in order to dissociate into hydrogen and oxygen gases between 710' F and 1200' F therein.
  • the dissociated hydrogen and oxygen gases are released at the outlet port of the coiled dissociation tube and directed at the base of the burning fuel in the combustion chamber of said boiler in order to burn as supplemental fuel and enhance combustion of the fossil fuel.
  • the primary objective of this invention is to save fuel by utilizing dissociated hydrogen and oxygen gases from water as supplemental fuel and as fuel enhancer for any type of boiler, using any kind of fuel.
  • Another objective of this invention is to use dissociated hydrogen and oxygen gases from water between 710' F and 1200' F as fuel enhancer for boilers in order to cause complete combustion of the fuel to prevent carbon emission that causes global warming.
  • Still another objective is to reduce maintenance expenses that results from cleaner combustion system and exhaust system due to complete fuel combustion.
  • Fig. 1 is the right side cut-away view of the method and device for dissociating water into its constituents hydrogen and oxygen gases between 710 ' F and 1200' F for use as fuel supplement and fuel enhancer for boilers is shown to include an elevated water reservoir tank 1 , water supply pipe with valve 2, overflow pipe with valve 3, pressure regulator 4, pressure gauge 5, compressed air supply pipe 6, water reservoir columnar glass tube 7, water outlet pipe with valve 8, columnar glass tube 9 that indicates the water level in the stainless economizer coil tube 12, water flow meter 10 that indicates the water flow rate of the pressurized water that is fed into the device; water feed control valve 1 1, top of the economizer coil 13, chimney temperature gauge 15, outer straight stainless steel super heater tubing 16 that is in fluid communication with downward tube 14 that inters the larger outer fire tube 20 concentrically, stainless super heater tube 16 makes a U-turn and is in fluid communication with the expanded spiral dissociation pipe 18, where the super heated steam inters, expands and dissociates into hydrogen and oxygen gases in combustion chamber 22.
  • the dissociated hydrogen and oxygen gases are released at outlet port 19 of the dissociation pipe and directed at the base of the burning fuel in the combustion chamber of the said boiler in order to burn with the fuel. Since hydrogen burns 7-times faster than fossil fuels, it therefore causes the fuel to burn completely that results in saving fuel, prevent carbon emission that causes global warming, cleanses the combustion and exhaust systems of the boiler of carbon and soot and save on maintenance expenses and release oxygen from the chimney to make the environment healthier.
  • water reservoir 1 is first filled with water to 90% of its capacity with the outlet valve being closed.
  • the device can be operated by allowing the pressurized water from the reservoir to flow into the device in regulated rate into the piping system of said device.
  • the device consists of the stainless steel economizer tubing that is coiled around the inner wall of the chimney of said boiler in order to recover waste heat to preheat the water.
  • the forward end of the stainless super heater tubing that inters concentrically through the larger outer fire tube of said boiler, makes a U-turn and inters concentrically through the straight inner fire tube to superheat and exits at the open end of said of inner fire tube of the boiler.
  • the forward end of the stainless super heater tubing connects in fluid communication with the larger stainless expansion chamber that is coiled inside the combustion chamber of said boiler oxygen gases between 710' F and 1200' F.
  • the dissociated hydrogen and oxygen gases are released at the outlet port coiled expansion chamber and directed at the base of the burning fuel in the combustion chamber of the said boiler in order to burn with the fuel. Since hydrogen burns 7-times faster that fossil fuels and release high amount of heat energy upon combustion, it therefore causes the fuel to burn completely that results in saving fuel, near zero carbon emission to prevent global warming, cleanses the inner linings of combustion chamber, the inner linings of the fire tubes and the exhaust system that redounds to reduced maintenance expenses and release oxygen to make environment healthier.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Combustion & Propulsion (AREA)
  • Inorganic Chemistry (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Air Supply (AREA)

Abstract

L'invention porte sur un dispositif et un procédé qui permettent de dissocier de l'eau en ses composants hydrogène et oxygène gazeux afin d'économiser le combustible nécessaire aux chauffe-eau. Le procédé précité fait appel à la chaleur résiduelle des chauffe-eau pour préchauffer de l'eau pressurisée en un flux contrôlé à travers un tube économiseur en acier inoxydable enroulé autour de la paroi interne de la cheminée. L'extrémité avant de l'enroulement précité est reliée en communication fluidique à un tube surchauffeur droit en acier inoxydable qui passe de manière concentrique à travers le tube de fumée externe plus grand, effectue un demi-tour vers le tube de fumée interne du chauffe-eau, sort à l'extrémité ouverte avant dudit tube de fumée, et vient se raccorder en communication fluidique au tube d'expansion enroulé dans la chambre de combustion, où la vapeur surchauffée se dilate et se dissocie en hydrogène et en oxygène gazeux entre 710° F et 1200° F. Les gaz dissociés sont relâchés par l'orifice de sortie de la chambre d'expansion et dirigés vers la base de la flamme du combustible en train de brûler afin de s'enflammer et entraîner une combustion complète du combustible fossile.
PCT/PH2009/000004 2008-04-14 2009-04-14 Procédé et dispositif permettant de dissocier de l'eau destinée à des chauffe-eau Ceased WO2009128735A2 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
PH12008000117 2008-04-14
PH12008000117 2008-04-14

Publications (2)

Publication Number Publication Date
WO2009128735A2 true WO2009128735A2 (fr) 2009-10-22
WO2009128735A3 WO2009128735A3 (fr) 2010-02-18

Family

ID=41199605

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/PH2009/000004 Ceased WO2009128735A2 (fr) 2008-04-14 2009-04-14 Procédé et dispositif permettant de dissocier de l'eau destinée à des chauffe-eau

Country Status (1)

Country Link
WO (1) WO2009128735A2 (fr)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2012161600A3 (fr) * 2011-05-24 2013-01-17 Celis Roberto V Procédé et dispositif de dissociation d'eau pour chaudières
WO2018217109A3 (fr) * 2017-05-25 2019-01-10 Celis Roberto V Dispositif et procédé de dissociation de l'eau dans une centrale électrique

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100556119B1 (ko) * 2004-01-31 2006-03-03 김태경 물을 연료로 이용하는 연소시스템 및 연소방법
KR20060007494A (ko) * 2004-07-20 2006-01-26 최동민 물을 연소보조재로 이용하는 연소시스템
JP2006046765A (ja) * 2004-08-03 2006-02-16 Benten:Kk 燃焼装置
KR20060113169A (ko) * 2005-04-29 2006-11-02 김태경 담수를 이용하여 연소 효율을 향상시킨 연소시스템

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2012161600A3 (fr) * 2011-05-24 2013-01-17 Celis Roberto V Procédé et dispositif de dissociation d'eau pour chaudières
WO2018217109A3 (fr) * 2017-05-25 2019-01-10 Celis Roberto V Dispositif et procédé de dissociation de l'eau dans une centrale électrique
PH12017000155A1 (en) * 2017-05-25 2019-01-21 V Celis Roberto Device and method of dissociating water in a power plant

Also Published As

Publication number Publication date
WO2009128735A3 (fr) 2010-02-18

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