WO2008029898A1 - Procédé de production de carburant en émulsion et appareil de production du carburant - Google Patents

Procédé de production de carburant en émulsion et appareil de production du carburant Download PDF

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Publication number
WO2008029898A1
WO2008029898A1 PCT/JP2007/067451 JP2007067451W WO2008029898A1 WO 2008029898 A1 WO2008029898 A1 WO 2008029898A1 JP 2007067451 W JP2007067451 W JP 2007067451W WO 2008029898 A1 WO2008029898 A1 WO 2008029898A1
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WO
WIPO (PCT)
Prior art keywords
water
oil
emulsion fuel
combustible
producing
Prior art date
Application number
PCT/JP2007/067451
Other languages
English (en)
Japanese (ja)
Inventor
Saburo Ishiguro
Tomihisa Naito
Original Assignee
Nanomizer Inc.
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 Nanomizer Inc. filed Critical Nanomizer Inc.
Priority to CN2007800407567A priority Critical patent/CN101535718B/zh
Priority to EP07806892A priority patent/EP2068080A1/fr
Priority to US12/439,436 priority patent/US20100186288A1/en
Publication of WO2008029898A1 publication Critical patent/WO2008029898A1/fr

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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
    • F23K5/02—Liquid fuel
    • F23K5/08—Preparation of fuel
    • F23K5/10—Mixing with other fluids
    • F23K5/12—Preparing emulsions
    • 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
    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/32—Liquid carbonaceous fuels consisting of coal-oil suspensions or aqueous emulsions or oil emulsions
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/40—Mixing liquids with liquids; Emulsifying
    • 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
    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/32—Liquid carbonaceous fuels consisting of coal-oil suspensions or aqueous emulsions or oil emulsions
    • C10L1/328—Oil emulsions containing water or any other hydrophilic phase

Definitions

  • the present invention relates to a water-oil type emulsion fuel family, and in particular, the constituent particles of water and flammable oil emulsion are made into an ultrafine particle state, and the obtained emulsion fuel is used as fuel for various power engines or combustion furnaces.
  • This invention relates to an invention that can contribute to energy saving and pollution prevention.
  • Patent Document Japanese Patent Laid-Open No. 2003-1 1 3385
  • various emulsion-type hydrofuels have been proposed, but they still lack the stability of combustion and are in practical use. Absent.
  • the particle diameters of these emulsions are several ⁇ m to several tens m.
  • the present inventors have pursued the stability that is regarded as a disadvantage of the emulsion-type water-added fuel, and in order to stably burn the emulsion of flammable oil and water, it is necessary to mix in an ultrafine particle state (nano level). Based on this idea, we have conducted earnest research.
  • the present invention has been made on the basis of the above knowledge, and is a method and an apparatus for manufacturing an emulsion fuel having the following configuration.
  • the combustible oil is one or more kinds selected from oils such as heavy oil, light oil, kerosene and volatile oil, industrial waste oil, tempura oil, soybean oil and sesame oil.
  • oils such as heavy oil, light oil, kerosene and volatile oil, industrial waste oil, tempura oil, soybean oil and sesame oil.
  • Miniaturization ' is a device that pressurizes the primary mixture of water and combustible oil and refines and mixes it by the cavitation effect caused by turbulent flow generated in one or more orifices.
  • the mixing means pressurizes the primary mixture of water and combustible oil and flows it through the pump at a flow rate of 50 mZs or more, and this wall has many holes with a diameter of 500 ⁇ m or less.
  • the device according to any one of (1) to (7) above, wherein the device is a device that accelerates through a hole in a body and refines and mixes by a cavity effect caused by turbulent flow between liquids Manufacturing method of emulsion fuel.
  • Refinement ⁇ Mixing means refines and mixes the water-flammable oil primary mixture obtained by the primary mixing means into a fine particle state, and the average particle size of water or combustible oil is 200 to 700 nm.
  • the mixing means pressurizes the water-combustible oil-based primary mixture and passes it through one or more small holes, and refines and mixes it by the cavitation effect caused by the turbulent flow generated at the orifice.
  • the emulsion fuel manufacturing apparatus according to any one of the preceding items (9) to (: 11), characterized by comprising an apparatus.
  • the refinement 'mixing means pressurizes the water-combustible oil-based primary mixture and flows it through the pump at a flow rate of 50 m / s or more, and there are many holes with a diameter of 200 ⁇ m or less.
  • Any one of (9) to (11) above, characterized in that it consists of a device that accelerates through the hole in the wall to be crushed and causes cavitation by the turbulent flow by the orifices of the same liquid flow to refine and mix The apparatus for producing the emulsion fuel according to claim 1.
  • Combustible oil 100 parts by volume of water 10. 0-150.0 parts by volume (more preferably 25.0 parts by volume of water for 100 parts by volume of combustible oil)
  • a method for operating an internal combustion engine characterized in that an emulsion fuel having an average particle size of lOOOOri m or less is used, and the obtained emulsion fuel is sprayed into a reciprocating engine to operate the internal combustion engine.
  • a method for operating an internal combustion engine characterized by comprising an emulsion fuel having an average particle size of 200 to 7 OOnm and spraying the obtained emulsion fuel into a reciprocating engine to operate the internal combustion engine.
  • FIG. 1 is a graph showing the results of a power engine fuel test using an emulsion fuel and other fuels according to the present invention.
  • FIG. 2 is a graph showing engine oil test results for power using the emulsion fuel and other fuels according to the present invention.
  • FIG. 3 is a graph showing the engine fuel test results for power using the emulsion fuel and other fuels according to the present invention.
  • FIG. 4 is a graph showing engine oil test results for power using the emulsion fuel and other fuels according to the present invention.
  • BEST MODE FOR CARRYING OUT THE INVENTION In the present invention, an emulsion fuel is produced by mixing oil and water in an ultra-fine state, which can contribute to improvement of fuel consumption and cleaner exhaust gas.
  • a turbulent flow generated by one or more orifices by pressurizing a primary mixture of water and combustible oil is used.
  • a device that refines and mixes by the cavity effect of the above can be mentioned.
  • a primary mixture of water and combustible oil is pressurized and flowed through the pump at a flow rate of 5 Om / s or more, and there are many holes with a diameter of 500 ⁇ m or less.
  • a preferable method for producing the emulsion fuel 100 parts by volume of the flammable oil, 10.0 to 15.0 parts by volume of water, more preferably 25.0 to 12.0 parts by volume of water) is preferable.
  • Force S et al. Water-flammable oil primary mixing means for primary mixing of water and combustible oil, and water-flammable oil-based primary mixture obtained by the primary mixing means are refined and mixed to form fine particles, It is to use a refining / mixing means to make an emulsion fuel with an average particle size of water or combustible oil of lOOOnm or less.
  • flammable oil Preferably, add 100 parts by volume of flammable oil, and add 25 to 120 parts by volume of water while adding “Nano-Mizer 1” (trade name, Yoshida Kikai Kogyo Co., Ltd.
  • the mixture of water and combustible oil is refined and mixed to produce an emulsion fuel consisting of a mixture containing ultrafine particles of water and combustible oil.
  • the For example, in the Nanomizer pressurize the primary mixture with a plunger and let it flow through the pump at a flow rate of 1 O OmZ s or higher.
  • the accelerated primary liquid mixture passes through the grooves (pores) of the disk, and the liquid streams collide with each other to refine and mix.
  • water and flammable oil mixture is passed through orifice holes of 200 ⁇ or less in the nanomizer at high pressure to generate turbulent flow when passing through a narrow orifice. A powerful stirring action of level level occurs.
  • water or oil
  • nano-levels for example, the average particle size of water is 200 to 700 nm
  • the average particle size of water is 200 to 700 nm
  • the method for reducing water is not particularly limited, but an industrial method by electrolysis is preferred. In addition, there are methods using chemicals and ores such as tourmaline.
  • electrolysis hydrogen is generated at the cathode and oxygen is generated at the anode.
  • oxygen is not required, so oxygen is not required, so it is removed by a diaphragm or reacted with the anode plate and fixed.
  • the electrode plate at that time is made of zinc, magnesium, or an alloy thereof.
  • the reduction potential of water is preferably 1 l OOmv or less, preferably 1 300mv or less.
  • Example 1 One by one Example 1 An example of the present invention and a comparative example will be described.
  • the reduced water 1. 96 liters of ⁇ -heavy oil 5. 88 liters After the primary stirring of the Li-Isumi IJl60cc by manual stirring, it was refined and mixed through a nanomizer at a pressure of 3MP to produce an emulsion fuel according to the present invention.
  • Each obtained emulsion was a W / O type emulsion, and the average particle size of water in the emulsion was 300 to 500 mn.
  • the obtained emulsion fuel according to the present invention was sample 2, and sample 3 was an emulsion fuel according to the present invention obtained by passing a mixed solution produced in the same manner as sample 2 at 8 MP through a nanomizer.
  • Sample 1 is treated with A-heavy oil in the comparative example
  • Sample 4 is treated with the light oil in the comparative example
  • Samples 5 and 6 are treated in the same manner as in Samples 2 and 3, but the present invention uses light oil instead of A-heavy oil.
  • Example 5 was finely mixed through a nanomizer at a pressure of 3MP and sample 6 at a pressure of 8MP).
  • Sample 2 A—heavy oil 73.5%, reduced water 24.5%, activator 2% Nanomizer 3MP treatment (emulsion fuel)
  • Sample 3 A—heavy oil 73.5%, reduced water 24.5%, activator 2% Nanomizer 8MP treatment (emulsion fuel)
  • Sample 5 Light oil 73.5%, reduced water 24.5%, activator 2% Nanomizer 3MP treatment (emulsion fuel)
  • Sample 6 Light oil 73.5%, reduced water 24.5%, activator 2% Nanomizer 8MP treatment (emulsion fuel)
  • Tables 1 to 3 and Figs. 1 to 4 show the results of combustion tests using the above samples in the engine.
  • Table 1 shows the test results when the engine speed is lOOOrpm
  • Table 2 shows the test results when the engine speed is 1400 to 2200rpm
  • Table 3 shows that the engine speed is 2700rpm. It is a test result in the case.
  • Fig. 1 shows the results of an engine test using Sample 1 (Comparative fuel) and Sample 2 (Emulsion fuel of the present invention).
  • Fig. 2 shows Sample 1 (Comparative fuel) and Sample 3 (Invention of the present invention).
  • Fig. 3 shows the results of an engine test using sample 4 (comparative fuel) and sample 5 (the emulsion fuel of the present invention).
  • Fig. 4 shows sample 4 (sample fuel).
  • FIG. 7 is a graph showing engine test results using Comparative Example Fuel) and Sample 6 (Emulsion Fuel of the present invention).
  • Example 2 In this example, a diesel generator manufactured by Denyo Co., Ltd. 1 3E S type was used to continuously measure the nitrogen oxide concentration and oxygen concentration in the exhaust gas, and the amount of power generation per unit heavy oil. And the power generation efficiency of the emulsion fuel of the present invention was measured.
  • emulsion fuel of the present invention a fuel having a composition of 75% by weight of special heavy oil A, 24.7% by weight of water and 0.3% by weight of emulsifier was used.
  • This Emulsion fuel is made up of 8.33 liters of A-heavy oil and 2.50 liters of water and 0.04 liters of emulsifier (100 parts by volume of heavy oil: 29.7 parts by volume of water: 0.5 parts by volume of emulsifier). The mixture was stirred temporarily by manual stirring, and then refined and mixed through a nanomizer at a pressure of 3MP. The average particle size of water in the emulsion fuel was about 300-5 OOiim.
  • the diesel generator was continuously operated using the emulsion fuel of the present invention and A heavy oil alone (comparative example) as fuels, and the NOx concentration and power generation amount in the exhaust gas were measured.
  • the NOx concentration and ⁇ 2 concentration in the exhaust gas were measured continuously at the generator outlet flue.
  • the measurement results of exhaust gas using the emulsion fuel of the present invention are shown in Table 4, and the measurement results of exhaust gas using special A heavy oil alone as fuel are shown in Table 5.
  • the average value of NOx concentration in the exhaust gas is 193 ppm, whereas heavy oil alone is used.
  • the average value of NOx concentration is 369 P pm, and it has been found that the concentration of NOx in exhaust gas can be greatly reduced by the fuel of the present invention.
  • Emulsion Combustion results of Emulsion (special A heavy oil 75 ⁇ 1 ⁇ 2, ⁇ 2 ⁇ 24.7%, emulsifier 0.3%)
  • Table 6 shows the results of power generation in this example.
  • the amount of power generated by diesel generator per unit heavy oil is 3.33KWH / Kg when using the emulsion fuel of the present invention, and 2.73KWH / Kg when using the heavy oil alone as the fuel. It has been demonstrated that the power generation efficiency of the emulsion fuel of the present invention has been improved.
  • the generator is DENYO TLG-1 3ESY type
  • the consumption (use amount) of the flammable oil can be reduced by about 25%.
  • misfire seems to occur at 2,600 rpm or higher. Therefore, for example, when using the emulsion fuel of the present invention for a ship, it is better to use light oil at the port and switch to the emulsion fuel outside the port. It is done.
  • a cavity effect caused by turbulent flow when a liquid mixture of water and combustible oil is pressurized and passed through one or more small holes and passes through an orifice In order to produce an emulsion fuel, the emulsion fuel containing about 25% water that has been refined and mixed does not cause engine trouble even if it is burned in the engine. It showed the same output and torque, and the fuel consumption was the same despite containing 25% water (simply calculating 25% energy saving).
  • the emulsion fuel water-one emulsion emulsion fuel
  • water-one emulsion emulsion fuel is made by adding 0.5 to 5% of an emulsifier to water and oil and stirring and mixing to form an emulsion, usually several ⁇ ⁇ to several Although it contains an average particle size of 10 ⁇ , it is a so-called emulsified liquid with an average particle size of about several ⁇ (about 1 to 3 ⁇ ) even when manufactured using a particularly excellent emulsifier.
  • Water fuel emulsion fuel
  • the emulsion fuel in this emulsified liquid tends to separate over time, and even if it does not separate, it has the property of increasing in viscosity (dilatancy) over time, contrary to wrinkle denaturation (titatropy), and clogging pipes and nozzles. There was an accident.
  • the emulsion fuel obtained by the present invention is a mixture of oil and water in an ultrafine state (nano level), and the average particle size of the constituent particles of water or combustible oil is 1,000 nm, preferably 200 to 700 nrn. Because it is an emulsion fuel, it has excellent stability, high combustion efficiency, and can be used for engines, combustion furnaces, incinerators, boilers, and power generation.
  • the present invention is used for engine fuel of a car or a ship, it will save 15 to 25%, and ⁇ , dioxin will be 1/2 to 1 ⁇ 5, ⁇ will be about 1/2 to 1/3 and low pollution. Since it is obtained and has good stability, it is possible to produce this liquid mixture at a gas station and replenish it to the fuel tank of the car as in the present situation.

Abstract

La présente invention concerne un carburant mélangé à de l'eau de type en émulsion qui ne cause aucune séparation entre une phase huileuse et une phase aqueuse et présente donc une excellente stabilité, un rendement de combustion élevé et un effet d'économie d'énergie extrêmement élevé. La présente invention concerne plus spécifiquement un carburant en émulsion dans lequel une phase aqueuse ou une phase huileuse a un diamètre moyen de particules inférieur ou égal à 1000 nm (plus préférablement de 200 à 700 nm), qui peut être produit en divisant finement et mélangeant 100 parties en volume d'huile combustible à 10,0 à 150,0 parties en volume (plus préférablement de 25,0 à 120,0 parties en volume) d'eau au moyen d'un dispositif de division fine/mélange tout en ajoutant l'eau à l'huile combustible. L'eau a de préférence un potentiel de réduction inférieur ou égal à -100 mV, de préférence inférieur ou égal à -300 mV.
PCT/JP2007/067451 2006-09-01 2007-08-31 Procédé de production de carburant en émulsion et appareil de production du carburant WO2008029898A1 (fr)

Priority Applications (3)

Application Number Priority Date Filing Date Title
CN2007800407567A CN101535718B (zh) 2006-09-01 2007-08-31 乳化燃料的制造方法及该燃料的制造装置
EP07806892A EP2068080A1 (fr) 2006-09-01 2007-08-31 Procédé de production de carburant en émulsion et appareil de production du carburant
US12/439,436 US20100186288A1 (en) 2006-09-01 2007-08-31 Method for production of emulsion fuel and apparatus for production of the fuel

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP2006-238131 2006-09-01
JP2006238131 2006-09-01

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WO2008029898A1 true WO2008029898A1 (fr) 2008-03-13

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US (1) US20100186288A1 (fr)
EP (1) EP2068080A1 (fr)
KR (1) KR20090049085A (fr)
CN (1) CN101535718B (fr)
RU (1) RU2440403C2 (fr)
SG (1) SG174732A1 (fr)
WO (1) WO2008029898A1 (fr)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2420313A2 (fr) * 2009-02-10 2012-02-22 Maschenko, Viktor Viktorovich Procédé de fabrication d'une émulsion eau-combustible et combustible composé à composants multiples
JP2020176231A (ja) * 2019-04-22 2020-10-29 真二 長谷川 加水燃料製造方法及び加水燃料製造装置

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102893087B (zh) * 2010-01-07 2015-09-30 株式会社Kcs 使用燃料和有机化合物水溶液的高温燃烧方法及装置
CA2831839A1 (fr) 2011-03-29 2012-10-04 Fuelina Technologies, Llc Combustible hydride et son procede de fabrication
MX2016011721A (es) * 2014-03-28 2017-04-25 Royal Corp Co Ltd Proceso y dispositivo para producir aceite de hidrocarburo combustible.
RU2596625C2 (ru) * 2014-11-06 2016-09-10 Федеральное государственное унитарное предприятие "Ордена Ленина и ордена Трудового Красного Знамени научно-исследовательский институт синтетического каучука имени академика С.В. Лебедева" Способ повышения удельной эффективности жидких углеводородных топлив и устройство для осуществления способа
EP3227411B1 (fr) 2014-12-03 2019-09-04 Drexel University Incorporation directe de gaz naturel dans des combustibles liquides hydrocarbonés
CN106582458A (zh) * 2015-10-16 2017-04-26 世能华奇（北京）科技发展有限公司 一种混合柴油的制造方法、由该方法制造的混合柴油及其制造装置
KR102155265B1 (ko) * 2019-03-13 2020-09-11 김영욱 물을 포함하는 석탄연소용 연료조성물

Citations (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01198691A (ja) * 1987-10-23 1989-08-10 Harrier Inc 液体燃料と水との混合物，並びにその製造方法及び製造装置
JP2001019983A (ja) * 1999-07-06 2001-01-23 Shigemi Sawada 水と油との混合物であるエマルジョンの製造装置およびエマルジョンの製造方法
JP2001329274A (ja) * 2000-05-19 2001-11-27 Zenshin Denryoku Engineering:Kk 含油水ガス燃料の製造方法および製造装置
JP2002147733A (ja) * 2000-11-13 2002-05-22 Katsumitsu Uehara 可燃性廃棄物の焼却方法及び装置
JP2003504486A (ja) * 1999-07-07 2003-02-04 ザ ルブリゾル コーポレイション 水性炭化水素燃料組成物を作製するためのプロセスおよび装置、ならびに水性炭化水素燃料組成物
JP2003113385A (ja) 2001-08-25 2003-04-18 Enetekku Co Ltd エマルジョン燃料油の製造方法及び製造装置
JP2004123947A (ja) 2002-10-03 2004-04-22 Sanyo Chem Ind Ltd エマルジョン燃料用乳化剤
JP2005306964A (ja) * 2004-04-20 2005-11-04 Lion Corp 液状燃料用乳化分散剤
JP2005344088A (ja) 2004-06-07 2005-12-15 Kagoshima Tlo Co Ltd バイオディーゼル燃料を用いたエマルジョン燃料及びその製法
JP2006052884A (ja) * 2004-08-11 2006-02-23 Toray Ind Inc エマルジョンの燃焼処理方法
JP2006188616A (ja) 2005-01-07 2006-07-20 Koichi Hanada エマルジョン燃料の製造方法
JP2006329438A (ja) 2005-05-23 2006-12-07 Nfg:Kk エマルジョン燃料製造装置
JP2006348157A (ja) * 2005-06-15 2006-12-28 Spg Techno Kk 多孔質体を用いた乳化型燃料生成方法とその製造装置

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1496858A (en) * 1923-02-17 1924-06-10 Knollenberg Rudolf Mixing liquids
US1975631A (en) * 1929-11-16 1934-10-02 Universal Products Corp Emulsifying apparatus
US2132854A (en) * 1937-07-16 1938-10-11 John Duval Dodge Emulsifier
CN1042552C (zh) * 1993-09-14 1999-03-17 程国柱 一种改质乳化燃料油及其生产方法
US5720551A (en) * 1994-10-28 1998-02-24 Shechter; Tal Forming emulsions
DE69915434T2 (de) * 1998-12-07 2005-03-03 Dsm Ip Assets B.V. Verfahren und Vorrichtung zum Mischen oder Dispergieren von Flüssigkeiten
US6802639B2 (en) * 2002-10-15 2004-10-12 Five Star Technologies, Inc. Homogenization device and method of using same

Patent Citations (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01198691A (ja) * 1987-10-23 1989-08-10 Harrier Inc 液体燃料と水との混合物，並びにその製造方法及び製造装置
JP2001019983A (ja) * 1999-07-06 2001-01-23 Shigemi Sawada 水と油との混合物であるエマルジョンの製造装置およびエマルジョンの製造方法
JP2003504486A (ja) * 1999-07-07 2003-02-04 ザ ルブリゾル コーポレイション 水性炭化水素燃料組成物を作製するためのプロセスおよび装置、ならびに水性炭化水素燃料組成物
JP2001329274A (ja) * 2000-05-19 2001-11-27 Zenshin Denryoku Engineering:Kk 含油水ガス燃料の製造方法および製造装置
JP2002147733A (ja) * 2000-11-13 2002-05-22 Katsumitsu Uehara 可燃性廃棄物の焼却方法及び装置
JP2003113385A (ja) 2001-08-25 2003-04-18 Enetekku Co Ltd エマルジョン燃料油の製造方法及び製造装置
JP2004123947A (ja) 2002-10-03 2004-04-22 Sanyo Chem Ind Ltd エマルジョン燃料用乳化剤
JP2005306964A (ja) * 2004-04-20 2005-11-04 Lion Corp 液状燃料用乳化分散剤
JP2005344088A (ja) 2004-06-07 2005-12-15 Kagoshima Tlo Co Ltd バイオディーゼル燃料を用いたエマルジョン燃料及びその製法
JP2006052884A (ja) * 2004-08-11 2006-02-23 Toray Ind Inc エマルジョンの燃焼処理方法
JP2006188616A (ja) 2005-01-07 2006-07-20 Koichi Hanada エマルジョン燃料の製造方法
JP2006329438A (ja) 2005-05-23 2006-12-07 Nfg:Kk エマルジョン燃料製造装置
JP2006348157A (ja) * 2005-06-15 2006-12-28 Spg Techno Kk 多孔質体を用いた乳化型燃料生成方法とその製造装置

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2420313A2 (fr) * 2009-02-10 2012-02-22 Maschenko, Viktor Viktorovich Procédé de fabrication d'une émulsion eau-combustible et combustible composé à composants multiples
EP2420313A4 (fr) * 2009-02-10 2012-08-15 Maschenko Viktor Viktorovich Procédé de fabrication d'une émulsion eau-combustible et combustible composé à composants multiples
JP2020176231A (ja) * 2019-04-22 2020-10-29 真二 長谷川 加水燃料製造方法及び加水燃料製造装置
JP7265250B2 (ja) 2019-04-22 2023-04-26 真二 長谷川 加水燃料製造方法及び加水燃料製造装置

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RU2009111851A (ru) 2010-10-10
EP2068080A1 (fr) 2009-06-10
SG174732A1 (en) 2011-10-28
CN101535718A (zh) 2009-09-16
RU2440403C2 (ru) 2012-01-20
US20100186288A1 (en) 2010-07-29
KR20090049085A (ko) 2009-05-15

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