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WO2013038393A2 - Centrale domestique multifonctions, dispositif pour l'alimenter en énergie au moyen de l'hydrogène et procédé de fonctionnement correspondant - Google Patents

Centrale domestique multifonctions, dispositif pour l'alimenter en énergie au moyen de l'hydrogène et procédé de fonctionnement correspondant Download PDF

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Publication number
WO2013038393A2
WO2013038393A2 PCT/IB2012/054902 IB2012054902W WO2013038393A2 WO 2013038393 A2 WO2013038393 A2 WO 2013038393A2 IB 2012054902 W IB2012054902 W IB 2012054902W WO 2013038393 A2 WO2013038393 A2 WO 2013038393A2
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WO
WIPO (PCT)
Prior art keywords
reaction
fuel
hydrogen
station
chamber
Prior art date
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Ceased
Application number
PCT/IB2012/054902
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English (en)
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WO2013038393A3 (fr
Inventor
Guido U. Parisi
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Individual
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Individual
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Application filed by Individual filed Critical Individual
Priority to EP12799602.3A priority Critical patent/EP2756230A2/fr
Priority to CN201280055996.5A priority patent/CN103930720A/zh
Priority to US14/344,997 priority patent/US20140373539A1/en
Publication of WO2013038393A2 publication Critical patent/WO2013038393A2/fr
Publication of WO2013038393A3 publication Critical patent/WO2013038393A3/fr
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K13/00—General layout or general methods of operation of complete plants
    • F01K13/006—Auxiliaries or details not otherwise provided for
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23L—SUPPLYING AIR OR NON-COMBUSTIBLE LIQUIDS OR GASES TO COMBUSTION APPARATUS IN GENERAL ; VALVES OR DAMPERS SPECIALLY ADAPTED FOR CONTROLLING AIR SUPPLY OR DRAUGHT IN COMBUSTION APPARATUS; INDUCING DRAUGHT IN COMBUSTION APPARATUS; TOPS FOR CHIMNEYS OR VENTILATING SHAFTS; TERMINALS FOR FLUES
    • F23L7/00—Supplying non-combustible liquids or gases, other than air, to the fire, e.g. oxygen, steam
    • F23L7/002—Supplying water
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B1/00—Electrolytic production of inorganic compounds or non-metals
    • C25B1/01—Products
    • C25B1/02—Hydrogen or oxygen
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B15/00—Operating or servicing cells
    • C25B15/02—Process control or regulation
    • 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 
    • F23C99/00—Subject-matter not provided for in other groups of this subclass
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G7/00—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
    • F23G7/05—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste oils
    • 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
    • F23C2900/99009—Combustion process using vegetable derived fuels, e.g. from rapes
    • 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
    • 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
    • Y02E20/00—Combustion technologies with mitigation potential
    • Y02E20/12—Heat utilisation in combustion or incineration of waste

Definitions

  • the present invention relates to a multifunction domestic station, to a device for powering the same with hydrogen and to a method of operating the same.
  • the invention relates to a domestic station having the functions of electric generator, heat generator and device for the disposal of domestic wastes.
  • a method and a device using a reaction chamber or combustor using water and heated oil for generating energy is disclosed in patent publication WO 95/23942.
  • the prior art device includes a combustor arranged to generate a flame which is horizontally deflected into a conventional boiler trough a connection.
  • the flame of the combustor being deflected so as to act in the horizontally arranged boiler, is arranged to heat the connection outside the boiler to a greater extent than the boiler interior, thereby causing a high loss of heat that could otherwise be exploited.
  • connection between the combustor and the boiler is a possible source of danger for the operators, who can burn themselves in case of contact with the connection, which is incandescent in use.
  • the station comprises a structure including a combustor in which an endothermic reaction of at least one fuel with water is exploited in order to generate high temperature thermal energy.
  • the combustor is configured so as to directly direct the thermal energy, for instance a vertical flame, towards utilisation devices, such as a boiler external to the combustor and/or a boiler internal to the combustor.
  • the combustor or reaction chamber is connected to a source of a pressurised mixture of water and air and at least to a source of a first fuel capable of endothermically reacting with the mixture.
  • the domestic station further includes heating devices for heating the first fuel to a combustion temperature in order to prime the reaction.
  • the source of the first fuel which is a vegetal or mineral oil, preferably exhausted, is connected to the reaction chamber both during a reaction priming phase and during a reaction maintaining phase, so that a reaction between the exhausted oil and the water - air mixture takes place in both phases.
  • the station also includes a source of a hydrogen-containing second fuel, which source is connectable to the reaction chamber, during the reaction maintaining phase, in the alternative or in addition to the source of the first fuel.
  • the station includes a hydrogen generator utilisable as the source of the second fuel.
  • the generator comprises one or more units, each including:
  • a chamber for the electrolytic decomposition of water the chamber being internally equipped with a plurality of elements of conductive material, which are electrically connected in series with one another and with a pulsed voltage generator;
  • a pressurised container connected on the one side to the decomposition chamber for receiving therefrom water, hydrogen and other products of the electrolytic decomposition and for introducing again pressurised water into the chamber, and connected on another side to the reaction chamber of the station in order to feed the chamber with hydrogen and the other products of the electrolytic decomposition.
  • the pulsed voltage generator includes a d.c. voltage source, such as a battery or an accumulator, connected to a generator of a sawtooth voltage.
  • a d.c. voltage source such as a battery or an accumulator
  • a method of operating the station comprises bringing a pressurised mixture of water and air into contact with a fuel capable of endothermically reacting with the mixture, after the fuel has been heated to a combustion temperature in order to prime the reaction between the fuel and the mixture.
  • the fuel In a reaction priming phase the fuel is a vegetal or mineral oil, preferably exhausted, and in a reaction maintaining phase the fuel either can be the oil or it is hydrogen (more precisely, a hydrogen-containing fuel) or an oil - hydrogen mixture.
  • FIG. 1 is a principle diagram of a station according to the invention.
  • Fig. 2a is a principle diagram of a variant
  • FIG. 2b is a schematic representation of the station shown in Fig. 2a;
  • FIG. 3 is a diagram of a hydrogen generator utilisable in the invention.
  • the multifunction domestic station includes a reaction chamber or combustor 11 equipped with an exhaust terminal 11a at an upper end of the chamber.
  • a strongly endothermic reaction takes place in chamber 11 between water, preferably source water at ambient temperature, and a preheated fuel.
  • the fuel is an oil (either a vegetal oil, for instance seed oil, olive oil and so on, or a mineral oil, for instance oil for engines or hydraulic oil), which is preferably exhausted so as to limit its cost.
  • Chamber 11 is preferably shaped as a frustum of a cone or a pyramid with square base and has exhaust terminal 1 la at its top end.
  • Such a structure assists in maintaining the water - fuel reaction within the chamber upon multiple reflections, thanks to the kinetic energy generated, so as to create a rotating fire ball which does not leave immediately the chamber through exhaust terminal 11a and therefore has the necessary time to burn possible residuals of the endothermic reaction, thereby drastically reducing or eliminating them and/or raising at the same time the operating temperature of the chamber.
  • the chamber might also be prismatic, without thereby departing from the scope of the invention as described and claimed, and it may preferably have a base size in the range 15 x 15 cm to 200 x 200 cm and a height in the range 15 cm to 200 cm.
  • the endothermic reaction preferably generates a flame that, in all embodiments, vertically leaves the chamber through exhaust terminal 11a.
  • the fuel is contained in a tank 12, for instance a gravity tank with an electrically operated valve 12a, and is preferably sent to reaction chamber 11 by means of a pump 13.
  • Tank 12 is moreover associated in conventional manner with level detectors 22, arranged to monitor the filling level of tank 12 and to operate an external pump (not shown) when it is necessary to supply again the tank with fuel.
  • level detectors 23 are advantageously associated with reaction chamber 1 1 and are arranged to act on pump 13 so as to keep the fuel level within chamber 11 between a minimum and a maximum ensuring the optimum station operation. Taking into account that the reaction generates very high temperatures, as it will be better disclosed below, detectors 23 can for instance include a laser device arranged outside chamber 11 , or they may be detectors immersed in the fuel.
  • Reaction chamber 11 is further associated with two burners 14, 15.
  • the first burner 14 (priming burner) is a conventional burner, for instance an oil or gas burner, and is to preheat the oil at such a temperature as to cause combustion thereof.
  • the second burner 15 (reaction maintaining burner) is instead to send a pressurised water - air mixture, typically at a pressure of the order of 0.5 - 1 bars, into reaction chamber 11 after oil firing.
  • burner 15 may be replaced by a compressed air ejector, operating at a pressure of a few bars, for instance 3 - 4 bars, and it is associated with a Venturi for air suction.
  • first phase oil is brought to a combustion temperature that will depend on the particular kind of oil being used and, generally, will be in the range of about 350°C to 450°C.
  • second phase reaction maintaining phase
  • the water - air mixture is introduced into chamber 1 1.
  • a strong reaction at very high temperature occurs, resulting in water dissociation and consequent development of atomic and molecular hydrogen, oxygen and H + and OH " ions, as experimentally verified by the inventor.
  • Devices for utilising the thermal energy are directly connected to exhaust 11a of combustion chamber 11, said devices being configured so as to exploit the thermal energy produced by the reaction.
  • devices 16 may include a steam producing device (boiler) 17, followed by a conventional turbine 18 (in this case, a steam turbine) made to rotate by the steam produced in boiler 17.
  • Turbine 18 is in turn connected for instance to one or more alternators 19 for generating electric power for domestic use, for instance at 3 to 5 kW/h per generator.
  • a second boiler 17a is located inside reaction chamber 1 1. Such an embodiment allows a double exploitation of the energy generated by the endothermic reaction.
  • devices 16 could include a heat exchanger 20, for instance a coil surrounding reaction chamber 11, for heating water to be used in a heating plant, as sanitary hot water for domestic use etc.
  • the steam generated in the boiler for instance the steam generated in the first boiler 17 and used to drive turbine(s) 18, upon being condensed into water and before being sent to a collecting container, is used for being applied in heating plants, for instance plants with radiators, or for producing hot water, and then is cooled through a heat exchanger before entering the water supply container for boiler 17.
  • a drawer or other container 21 is inserted between reaction chamber 11 and boiler 17, said container (of course made of a material resistant to the high temperatures mentioned above) being arranged to contain domestic wastes, in particular wastes that cannot be subjected to differentiated collection and hence recycled,.
  • the drawer is arranged inclined towards a grate exposed to the flame so that the wastes, exposed to the high temperatures generated by the reaction, burn substantially without emitting polluting and poisonous substances, such as dioxin, and with a negligible emission of the above-mentioned C0 2 and NO x .
  • the station can therefore also be used as a domestic waste-to-energy plant.
  • Figs. 2a and 2b show a second embodiment of the invention, denoted 1A.
  • the elements already disclosed with reference to Fig. 1 are denoted by the same reference numerals.
  • oil coming from tank 12 is still used as the fuel in the reaction priming phase, whereas oil, or an oil - hydrogen mixture, containing for instance 70% oil and 30% hydrogen, or yet only hydrogen can be used as fuel in the reaction maintaining phase.
  • Hydrogen is produced for instance by at least one hydrogen generator 25.
  • At least a pair of identical generators 25 is provided, as shown in Fig. 2a.
  • one of them can be a stand-by generator, arranged to intervene in case of failure of the other generator.
  • the generators can however be used in alternating manner, according to a suitable timing, or jointly, for instance to meet peaks of power demand.
  • devices arranged to detect the value of the flame temperature in reaction chamber 1 1 can be preferably provided. Such devices can be connected to means for automatically turning off the station in case of anomalous operation.
  • the station comprises a control panel including, for instance, instruments for measuring temperature and pressure values in the various components of the station.
  • non-return valves, pressure switches and other safety devices might also be provided in the station.
  • generator 25 The structure of generator 25 is shown in greater detail in Fig. 3.
  • the generator comprises a chamber 30 for the electrolytic decomposition of demineralised water, with a duct 21 for supplying the demineralised water, made conductive preferably by the addition of alkaline metal compounds, preferably hydroxides of such metals, in particular sodium hydroxide or, in the alternative, potassium hydroxide.
  • alkaline metal compounds preferably hydroxides of such metals, in particular sodium hydroxide or, in the alternative, potassium hydroxide.
  • the water might also contain concentrated hydrogen peroxide added in a percentage of up to 50%, for instance 10 to 50%>.
  • the addition of hydrogen peroxide allows increasing the amount of hydrogen produced for a given size of chamber 30.
  • Elements 32 for instance discs or plates
  • discs are coaxially mounted on one or more rods 33 (for instance a central rod, as shown in the Figure, or a plurality of rods distributed along the periphery of discs 32) and are separated by spacers 34, for instance a few millimetres thick (e.g. 1 - 2 mm thick).
  • Discs 32 have a slightly smaller size than chamber 30 and define with the side walls of the chamber a substantially serpentine path for water.
  • the serpentine path for water is obtained by inserting, at the end of each disc 32, suitable sealing rings or components 32a of plastic material, e.g. Teflon, fastened to decomposition chamber 30, and by providing one or more throughholes 52 on each disc
  • Discs 32 are electrically connected in series with one another and with a generator of d.c. voltage, for instance a battery or accumulator 41 (typically, a motor-car battery with 12 V nominal voltage or an industrial vehicle battery with 24 V nominal voltage), and a wall of chamber 30, in particular roof 30a, serves as the ground.
  • the voltage source is such as to establish a same voltage difference, in particular a voltage difference of about 2
  • V and preferably in the range 2.1 to 2.35 V, between a first disc 32 in the plurality and ground 30a and between adjacent discs 32.
  • at least six discs 32 are provided, since a nominal voltage lower than 12 V does not allow a good operation of the generator.
  • the actual number of the discs will depend on the voltage generated by battery 41.
  • Means 42 are arranged between battery 41 and the set of discs 32 for converting the d.c. voltage generated by battery 41 into a pulsed voltage, for instance a sawtooth voltage having a maximum value corresponding to the nominal voltage of the battery, whereas the minimum value can preferably be in the range 40% to 50%, and preferably is about 50%, of such a nominal voltage.
  • Such a pulsed voltage causes the formation on the surface of discs 32, due to water decomposition, of small hydrogen bubbles the sizes of which increase as the voltage applied to the individual discs increase (and hence as water proceeds within chamber 30 by following the serpentine path).
  • the small hydrogen bubbles attain, due to the surface tension, such sizes that they can detach themselves from the surface of the same disc.
  • the above-mentioned voltage difference of about 2 V between adjacent discs is the optimum value for creating those bubbles.
  • Water and the products of electrolytic decomposition leave chamber 30 through a duct 35 and are fed to a pressurised container 37 (for instance at 2 - 3 bars), possibly through a radiator 38 arranged to cool the products of electrolytic decomposition.
  • cooling can be performed by means of d.c. powered cooling fans, for instance of the kind used in personal computers.
  • a proton accelerator for instance of the kind disclosed in patent publication WO 2007/119141 A in the name of the inventor, is located at the exit from top duct 39 leading the hydrogen compound from the generator to combustion chamber 1 1.
  • Said accelerator is capable of increasing the yield of generator 25, as experimentally verified by the inventor,
  • the gases are heated before being introduced into reaction chamber 11 (for instance by using coil 20 mentioned above), thereby creating a pressure and volume increase and a stronger suction of the same gases.
  • duct 39 will have to be associated with a non-return valve (not shown), for preventing hydrogen and the other products of electrolytic decomposition, which have undergone the pressure and volume increase due to the heating, from going back into container 37.
  • reaction chamber 1 1 Sending the products of electrolytic decomposition into reaction chamber 1 1 facilitates the high temperature reaction.
  • hydrogen denotes, more generally, the whole of the products of the electrolytic decomposition of water.
  • the basic reagents are cheap (essentially water, alkaline compounds and exhausted oils) and hence the whole process and the station can be carried out/manufactured and managed in economical manner.
  • exhausted oils as fuel at least in the reaction priming phase also contributes to the disposal of such oils.
  • the possibility of using the station as waste-to-energy plant assists in eliminating wastes that cannot be recycled.
  • the station can be configured so as to allow, for instance, heat production, electric power production and waste disposal.
  • a domestic station In synthesis, a domestic station is provided that can be installed in every house as a one-family plant or as a central plant, for instance a condominium plant, in order to provide a plurality of services at very low cost.
  • the station of the invention is actually a completely autonomous and stand-alone equipment and not only a component of a more complex system.

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Combustion & Propulsion (AREA)
  • Environmental & Geological Engineering (AREA)
  • Electrochemistry (AREA)
  • Organic Chemistry (AREA)
  • Metallurgy (AREA)
  • Materials Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Automation & Control Theory (AREA)
  • Inorganic Chemistry (AREA)
  • Engine Equipment That Uses Special Cycles (AREA)
  • Hydrogen, Water And Hydrids (AREA)
  • Fuel Cell (AREA)
  • Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

Selon l'invention, une centrale domestique multifonctions (1) comprend une chambre de réaction (11) connectée à une source (15) de mélange pressurisé d'eau et d'air, à une première source (12) de premier combustible capable d'une réaction endothermique avec le mélange et à une deuxième source (25) d'un deuxième combustible. La centrale comprend aussi des dispositifs de chauffage (14) capables de réchauffer le premier combustible à une température de combustion afin d'initier la réaction entre le combustible et le mélange, et des dispositifs (16) pour utiliser l'énergie thermique générée par la réaction afin de faire fonctionner la centrale comme une génératrice d'énergie électrique, un générateur de chaleur et un dispositif d'élimination de déchets ménagers. L'invention concerne également un dispositif pour alimenter la centrale en un deuxième combustible et un procédé pour faire fonctionner la centrale (1).
PCT/IB2012/054902 2011-09-15 2012-09-17 Centrale domestique multifonctions, dispositif pour l'alimenter en énergie au moyen de l'hydrogène et procédé de fonctionnement correspondant Ceased WO2013038393A2 (fr)

Priority Applications (3)

Application Number Priority Date Filing Date Title
EP12799602.3A EP2756230A2 (fr) 2011-09-15 2012-09-17 Centrale domestique multifonctions, dispositif pour l'alimenter en énergie au moyen de l'hydrogène et procédé de fonctionnement correspondant
CN201280055996.5A CN103930720A (zh) 2011-09-15 2012-09-17 多功能家用电站，用于利用氢对其供电的设备以及操作其的方法
US14/344,997 US20140373539A1 (en) 2011-09-15 2012-09-17 Multifunction domestic station, device for powering the same with hydrogen and method of operating the same

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
ITTO2011A000826 2011-09-15
IT000826A ITTO20110826A1 (it) 2011-09-15 2011-09-15 Centrale domestica a piu' funzioni, dispositivo per la sua alimentazione con idrogeno e metodo di funzionamento della stessa

Publications (2)

Publication Number Publication Date
WO2013038393A2 true WO2013038393A2 (fr) 2013-03-21
WO2013038393A3 WO2013038393A3 (fr) 2013-07-04

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ID=44993774

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Application Number Title Priority Date Filing Date
PCT/IB2012/054902 Ceased WO2013038393A2 (fr) 2011-09-15 2012-09-17 Centrale domestique multifonctions, dispositif pour l'alimenter en énergie au moyen de l'hydrogène et procédé de fonctionnement correspondant

Country Status (5)

Country Link
US (1) US20140373539A1 (fr)
EP (1) EP2756230A2 (fr)
CN (1) CN103930720A (fr)
IT (1) ITTO20110826A1 (fr)
WO (1) WO2013038393A2 (fr)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ES2522817A1 (es) * 2013-05-17 2014-11-18 Universidade De Vigo Sistema generador de calor

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR3026315B1 (fr) * 2014-09-26 2018-01-26 Centre National De La Recherche Scientifique Procede de controle d'au moins une bulle de gaz produite de maniere localisee

Citations (2)

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Publication number Priority date Publication date Assignee Title
WO1995023942A1 (fr) 1994-03-03 1995-09-08 Pendolo Corporation N.V. Procede et dispositif de production d'energie
WO2007119141A2 (fr) 2006-04-14 2007-10-25 Guido Parisi Appareil de polarisation destiné a améliorer la combustion de combustibles liquides ou gazeux

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CH585874A5 (fr) * 1975-07-04 1977-03-15 Demoiseau Bernard
US6053725A (en) * 1995-03-03 2000-04-25 Selany Corporation N.V. Method of and device for producing energy
DE19749688A1 (de) * 1997-11-10 1999-05-12 Gourmeli International N V Verfahren zur Verbrennung organischer Brennstoffe und Brenner hierfür
JP2002115812A (ja) * 2000-10-12 2002-04-19 Zenshin Denryoku Engineering:Kk 水−化石燃料混合エマルジョンの燃焼方法及び燃焼装置
US8070480B2 (en) * 2003-11-21 2011-12-06 Associated Physics Of America, Llc Method and device for combusting liquid fuels using hydrogen
US20110091824A1 (en) * 2009-10-20 2011-04-21 Vinayak Barve Method of operating a multi-fuel combustion system
CN201531887U (zh) * 2009-10-30 2010-07-21 上海煜工环保科技有限公司 垃圾与有机废液联烧的处理装置

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1995023942A1 (fr) 1994-03-03 1995-09-08 Pendolo Corporation N.V. Procede et dispositif de production d'energie
WO2007119141A2 (fr) 2006-04-14 2007-10-25 Guido Parisi Appareil de polarisation destiné a améliorer la combustion de combustibles liquides ou gazeux

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ES2522817A1 (es) * 2013-05-17 2014-11-18 Universidade De Vigo Sistema generador de calor

Also Published As

Publication number Publication date
ITTO20110826A1 (it) 2013-03-16
CN103930720A (zh) 2014-07-16
US20140373539A1 (en) 2014-12-25
EP2756230A2 (fr) 2014-07-23
WO2013038393A3 (fr) 2013-07-04

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