EP2068080A1 - 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 PDFInfo
- Publication number
- EP2068080A1 EP2068080A1 EP07806892A EP07806892A EP2068080A1 EP 2068080 A1 EP2068080 A1 EP 2068080A1 EP 07806892 A EP07806892 A EP 07806892A EP 07806892 A EP07806892 A EP 07806892A EP 2068080 A1 EP2068080 A1 EP 2068080A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- water
- oil
- emulsion fuel
- finely
- combustible oil
- 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.)
- Withdrawn
Links
- 239000000446 fuel Substances 0.000 title claims abstract description 149
- 239000000839 emulsion Substances 0.000 title claims abstract description 117
- 238000004519 manufacturing process Methods 0.000 title claims description 32
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 105
- 238000002156 mixing Methods 0.000 claims abstract description 56
- 230000000694 effects Effects 0.000 claims abstract description 14
- 239000003921 oil Substances 0.000 claims description 114
- 235000019198 oils Nutrition 0.000 claims description 113
- 239000007788 liquid Substances 0.000 claims description 41
- 239000000203 mixture Substances 0.000 claims description 41
- 239000000295 fuel oil Substances 0.000 claims description 29
- 239000010419 fine particle Substances 0.000 claims description 6
- 150000003071 polychlorinated biphenyls Chemical class 0.000 claims description 6
- 150000002013 dioxins Chemical class 0.000 claims description 4
- 239000011148 porous material Substances 0.000 claims description 4
- 239000008399 tap water Substances 0.000 claims description 3
- 235000020679 tap water Nutrition 0.000 claims description 3
- 239000008162 cooking oil Substances 0.000 claims description 2
- 239000010840 domestic wastewater Substances 0.000 claims description 2
- 230000035622 drinking Effects 0.000 claims description 2
- 239000002440 industrial waste Substances 0.000 claims description 2
- 239000010842 industrial wastewater Substances 0.000 claims description 2
- 239000010815 organic waste Substances 0.000 claims description 2
- 239000003208 petroleum Substances 0.000 claims description 2
- 239000008159 sesame oil Substances 0.000 claims description 2
- 235000011803 sesame oil Nutrition 0.000 claims description 2
- 239000003549 soybean oil Substances 0.000 claims description 2
- 235000012424 soybean oil Nutrition 0.000 claims description 2
- 239000000341 volatile oil Substances 0.000 claims description 2
- 239000002351 wastewater Substances 0.000 claims description 2
- 238000002485 combustion reaction Methods 0.000 abstract description 20
- 238000012360 testing method Methods 0.000 description 15
- 239000007789 gas Substances 0.000 description 13
- 238000000034 method Methods 0.000 description 10
- 239000003995 emulsifying agent Substances 0.000 description 9
- 238000010248 power generation Methods 0.000 description 9
- 230000000052 comparative effect Effects 0.000 description 8
- 239000002245 particle Substances 0.000 description 8
- 238000005259 measurement Methods 0.000 description 6
- 206010001497 Agitation Diseases 0.000 description 5
- 238000013019 agitation Methods 0.000 description 5
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 5
- 239000001301 oxygen Substances 0.000 description 5
- 229910052760 oxygen Inorganic materials 0.000 description 5
- 239000011882 ultra-fine particle Substances 0.000 description 5
- 239000012190 activator Substances 0.000 description 4
- 238000004458 analytical method Methods 0.000 description 4
- 238000005868 electrolysis reaction Methods 0.000 description 4
- 239000000779 smoke Substances 0.000 description 4
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 3
- KVGZZAHHUNAVKZ-UHFFFAOYSA-N 1,4-Dioxin Chemical compound O1C=COC=C1 KVGZZAHHUNAVKZ-UHFFFAOYSA-N 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000000691 measurement method Methods 0.000 description 2
- 239000011369 resultant mixture Substances 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000004071 soot Substances 0.000 description 2
- 238000005507 spraying Methods 0.000 description 2
- 239000003981 vehicle Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 238000004364 calculation method Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 239000010779 crude oil Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 239000002828 fuel tank Substances 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 230000033116 oxidation-reduction process Effects 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000002569 water oil cream Substances 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
Images
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
- C10L1/00—Liquid carbonaceous fuels
- C10L1/32—Liquid carbonaceous fuels consisting of coal-oil suspensions or aqueous emulsions or oil emulsions
-
- 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
-
- 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 emulsion fuel, and more particularly, to an invention capable of contributing to energy saving and pollution control in a case where particles constituting an emulsion of water and a combustible oil are formed into ultrafine particles, and an obtained emulsion fuel is used as a fuel for various power engines or combustion furnaces.
- the inventors of the present invention have sought the stability, which being identified as the shortcomings of the emulsion-type water-mixed fuel, and have pursued their intensive studies, based on an idea that there needs a mixing thereof under a ultrafine particle state (nano level), in order to stably combust the emulsion of water and the combustion oil.
- combustion with high efficiency which could not be attained by the conventional emulsion fuel, may be realized by reducing an average particle diameter of respective particles in the emulsion fuel into 1,000 nm or less.
- the inventors of the present invention found that, in order to stabilize the emulsion of water and the combustion oil so as not to cause separation therein, it is preferred to form a mixture of ultrafine particle state (nano level).
- the present invention has been made based on the above-mentioned findings, and relates to a method and an apparatus for production of an emulsion fuel having the following constructions.
- an oil and a water are mixed together under ultra fine states to produce an emulsion fuel, thereby being capable of contributing to improve fuel consumption and to make combustion exhaust gas clean.
- a finely-dividing and mixing means used for producing the emulsion fuel of the present invention for example, there may be given an apparatus, which pressurizes a primary mixture liquid including a water and a combustible oil to finely divides and mixes through a cavitation effect due to turbulence generated at one or two or more of orifices.
- the finely-dividing and mixing means there may be given an apparatus, which pressurizes a primary mixture liquid including a water and a combustible oil to cause to flow within a pump at a flow rate of 50 m/s or more; accelerates the primary mixture liquid to pass into holes of a wall member having multiple holes each having a diameter of 500 ⁇ m or less formed therein; and finely divides and mixes through a cavitation effect due to turbulence generated between flows of the liquid.
- a preferred method for the production of an emulsion fuel includes using: a water-combustible oil primary mixing means for primarily mixing a water and a combustible oil, while adding 10.0 to 150.0 parts by volume of the water (more preferably, 25.0 to 120.0 parts by volume of the water) with respect to 100 parts by volume of the combustible oil; and a finely-dividing and mixing means for finely-dividing and mixing the water-combustible oil-based primary mixture liquid obtained by the primary mixing means into a fine particle state, to thereby form an emulsion fuel in which an average diameter of the water or the combustible oil is 1,000 nm or less.
- the mixture liquid is introduced into Nanomizer (Product Name; apparatus for finely-dividing and mixing a primary mixture liquid dispersed within a liquid sample, which is manufactured by Yoshida Kikai Co., Ltd.), and the primary mixture liquid including the water and the combustible oil is finely-divided and mixed, thereby forming an emulsion fuel of a mixture including a ultra fine diameter particles of the water and the combustible oil.
- Nanomizer Provide; apparatus for finely-dividing and mixing a primary mixture liquid dispersed within a liquid sample, which is manufactured by Yoshida Kikai Co., Ltd.
- the primary mixture liquid is subject to a pressure with a plunger within Nanomiser to cause to flow within a pump at a flow rate of 100 m/s or more, and then the accelerated primary mixture liquid passes through a groove(s) (pore(s)) of two pieces of disks, each having the groove (s) (pore(s)) of about 100 ⁇ m at right angle, to cause flows of the liquid to collide with each other, thereby finely-dividing and mixing the liquid.
- the water-combustible oil mixture liquid is caused to pass through orifice holes of 200 ⁇ m or less of Nanomizer with a high pressure for several stages.
- the turbulence is generated when the mixture liquid passes through the narrow orifices, and a strong nano level agitation effect is generated owing to the turbulence effect.
- the water (or oil) is finely divided into a nano level (for example, average diameter of water is 200 to 700 nm), and the resultants are dispersed within the oil (to form W/O type emulsion) thereby attaining stabilization.
- a nano level for example, average diameter of water is 200 to 700 nm
- the reduction method for the water is not particularly limited, but a method using electrolysis is industrially preferred.
- a method using a chemical, or a method using an ore such as tourmarine there may be given a method using a chemical, or a method using an ore such as tourmarine.
- hydrogen generates at a cathode and oxygen generates at an anode during the electrolysis.
- the oxygen is unnecessary, and hence the oxygen is discharged by using a barrier, or is fixed by allowing the oxygen to react with an anode plate.
- an electrode at that time zinc, magnesium, or an alloy thereof may be used.
- the reduction potential of the water is preferably -100 mv or less, and -300 mv or less is preferred, if possible.
- the water and the oil are hard to be mixed with each other, because a surface tension of the water is large. If the reduction potential is lowered, the surface tension decreases, resulting in being easily mixed together.
- an emulsion fuel of the present invention was produced.
- the obtained emulsion fuel is a W/O type emulsion, and average diameter of the water in the emulsion was 300 to 500 nm.
- the thus obtained emulsion fuel of the present invention was set to be Sample 2.
- the mixture liquid produced in the same way as in Sample 2 was caused to pass through Nanomizer with 8 MP to obtain an emulsion fuel of the present invention, which was set to be Sample 3.
- Sample 1 is a A heavy oil as a comparative example
- Sample 4 is a light oil as a comparative example
- Samples 5 and 6 each are obtained by the same processing as in Samples 2 and 3, and are emulsion fuels of the present invention in which the light oil is used in place of the A heavy oil.
- Sample 5 and Sample 6 were caused to pass through Nanomizer with pressures of 3 MP and 8 MP, respectively, to be finely-divided and mixed).
- Table 1 is test results of a case in which the number of rotation of the engine is 1, 000 rpm
- Table 2 is test results of a case in which the number of rotation of the engine is 1,400 to 2,200 rpm
- Table 3 is test results of a case in which the number of rotation of the engine is 2,700 rpm.
- Fig. 1 is graphs showing engine test results in which Sample 1 (comparative example fuel) and Sample 2 (emulsion fuel of the present invention) were used
- Fig. 2 is graphs showing engine test results in which Sample 1 (comparative example fuel) and Sample 3 (emulsion fuel of the present invention) were used
- Fig. 3 is graphs showing engine test results in which Sample 4 (comparative example fuel) and Sample 5 (emulsion fuel of the present invention) were used
- Fig. 4 is graphs showing engine test results in which Sample 4 (comparative example fuel) and Sample 6 (emulsion fuel of the present invention) were used.
- a diesel generator of 13ES-type manufactured by Denyo Co. , Ltd. was used to successively measure the concentrations of nitrogen oxides and oxygen within an exhaust gas together with a power generation amount per unit heavy oil, whereby the power generation efficiency of the emulsion fuel of the present invention was measured.
- an emulsion fuel having a composition including 75 wt% of a Special A heavy oil, 24.7 wt% of a water, and 0.3 wt% of an emulsifier was produced and used.
- the emulsion fuel of the present invention and sole A heavy oil are used as the fuels to successively operate the above-mentioned diesel generator, NOx concentration within the exhaust gas and the power generation amount were measured. The concentrations of NOx and O 2 within the exhaust gas were measured successively at an exit smoke-flue of the generator.
- the measurement results of the exhaust gas which was generated by the use of the emulsion fuel of the present invention, are shown in Table 4, and the measurement results of the exhaust gas when the Special A heavy oil was solely used as fuel are shown in Table 5.
- an average NOx concentration within the exhaust gas was 193 ppm.
- the average value of the NOx concentration was 369 ppm.
- results of power generation of this example are shown in Table 6.
- the power generation amount per unit heavy oil of the diesel generator was 3.33 KWH/Kg when the emulsion fuel of the present invention was used, and was 2.73 KWH/Kg when the sole heavy oil was used as fuel.
- the power generation amount was increased by about 22%, whereby it was shown that the power generation efficiency of the emulsion fuel of the present invention was improved.
- the emulsion fuel of the present invention in which 24.5% of the water was added to the A-heavy oil or the light oil, exhibited almost the same characteristics as 100% A-heavy oil or 100% light oil up to 2,200 rpm. This is astonishingly excellent performance.
- the emulsion fuel of the present invention is used for a ship, for instance, it is considered to be good to use a light oil in a harbor, and then to switch to use the emulsion fuel outside the harbor.
- the mixture liquid including a water and a combustible oil is, for example, subjected to a pressure to cause to pass through one or a plurality of small holes, thereby producing the emulsion fuel by finely-diving and mixing the mixture through the cavitation effect due to the turbulence generated when passing through orifices.
- the emulsion fuel containing about 25% of the finely-divided and mixed water does not cause engine troubles, if being burned within the engine, and exhibits substantially the same output and torque with the A-heavy oil or the light oil.
- the fuel consumption amount is also the same even though 25% of the water is contained therein (by simple calculation, 25% of energy saving is attained).
- the generations of soot and dioxin are reduced into 1/2 to 1/5 (theoretically no generation), and NO X was also reduced into about 1/2 to 1/3.
- the emulsion fuel of the present invention has a further energy saving effect as a fuel for combustion furnace, and attains 25 to 35% energy saving.
- the waste oil may also be used as a raw material.
- the emulsion fuel (water-oil-based emulsion-type water-mixed fuel) is obtained by adding 0.5 to 5% of the emulsifier to the water and oil, and by agitating and mixing the mixture into emulsion, and generally contains particles having an average diameter of several ⁇ m to several tens ⁇ m. Even if the emulsion fuel is produced using a particularly excellent emulsifier, the average particle diameter was about several ⁇ m (about 1 to 3 ⁇ m), which is a so-called water-mixed fuel of an emulsified-state liquid (emulsion fuel).
- the emulsion fuel of the emulsified-state liquid has a tendency of separating with elapse of time, and, even if the separation does not occur, has a nature in which the viscosity thereof becomes higher (dilatancy) with the elapse of time, which is opposite to thixotropy, thereby causing an accident such as clogging of a pipe or a nozzle.
- the emulsion fuel obtained by the present invention constitutes an emulsion fuel in which the oil and the water are mixed under a ultra fine particle state (nano level), and the average particle diameter constituting the water or the combustible oil is 1, 000 nm, preferably 200 to 700 nm.
- the stability thereof is extremely excellent, and has high combustion efficiency, whereby the emulsion fuel of the present invention may be used for all the purposes such as for an engine, a combustion furnace, an incinerator, a boiler, and a generator.
- the emulsion fuel of the present invention is used for an engine fuel for a vehicle and a ship, 15 to 25% of energy saving may be achieved. Further, soot and dioxin may be reduced into 1/2 to 1/5, and NO X may be reduced about 1/2 to 1/3, thereby attaining low pollution and excellent stability. As a result, it becomes possible to produce the fine particle mixture liquid at a gas station, and to refuel the liquid into a fuel tank of the vehicle as currently carried out.
- the emulsion fuel of the present invention may be applied for the boiler, the generator, the combustion furnace and the incinerator, and utilization of the waste oil is possible. Such a result was obtained that, if the emulsion fuel of the present invention is used for the combustion furnace, the energy saving effect may be increased by 30 to 40%.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Liquid Carbonaceous Fuels (AREA)
- Feeding And Controlling Fuel (AREA)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2006238131 | 2006-09-01 | ||
PCT/JP2007/067451 WO2008029898A1 (fr) | 2006-09-01 | 2007-08-31 | Procédé de production de carburant en émulsion et appareil de production du carburant |
Publications (1)
Publication Number | Publication Date |
---|---|
EP2068080A1 true EP2068080A1 (fr) | 2009-06-10 |
Family
ID=39157324
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP07806892A Withdrawn EP2068080A1 (fr) | 2006-09-01 | 2007-08-31 | Procédé de production de carburant en émulsion et appareil de production du carburant |
Country Status (7)
Country | Link |
---|---|
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) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
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 |
Families Citing this family (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPWO2011083877A1 (ja) * | 2010-01-07 | 2013-05-16 | 石黒 三郎 | 燃料と有機化合物水溶液を使用する高温燃焼方法及び装置 |
EP2691496A2 (fr) | 2011-03-29 | 2014-02-05 | Fuelina, Inc. | Combustible hydride et son procédé de fabrication |
RU2704822C2 (ru) * | 2014-03-28 | 2019-10-31 | Роял Корпорэйшн Ко., Лтд. | Процесс и устройство для производства топливного углеводородного масла |
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 |
US10308885B2 (en) | 2014-12-03 | 2019-06-04 | Drexel University | Direct incorporation of natural gas into hydrocarbon liquid fuels |
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 |
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 |
Family Cites Families (20)
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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 |
EP0312641A1 (fr) * | 1987-10-23 | 1989-04-26 | "Harrier" Gmbh Gesellschaft Für Den Vertrieb Medizinischer Und Technischer Geräte | Procédé pour mélanger du carburant et de l'eau, dispositif pour mettre en oeuvre ce procédé et mélange carburant-eau |
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 |
US6368366B1 (en) * | 1999-07-07 | 2002-04-09 | The Lubrizol Corporation | Process and apparatus for making aqueous hydrocarbon fuel compositions, and aqueous hydrocarbon fuel composition |
ATE261336T1 (de) * | 1998-12-07 | 2004-03-15 | Hoffmann La Roche | Verfahren und vorrichtung zum mischen oder dispergieren von flüssigkeiten |
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 |
KR20030017889A (ko) | 2001-08-25 | 2003-03-04 | 이엔이테크(주) | 에멀젼 연료유의 제조방법 |
JP3839385B2 (ja) | 2002-10-03 | 2006-11-01 | 三洋化成工業株式会社 | エマルジョン燃料用乳化剤 |
US6802639B2 (en) * | 2002-10-15 | 2004-10-12 | Five Star Technologies, Inc. | Homogenization device and method of using same |
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 |
JP3877078B2 (ja) | 2005-05-23 | 2007-02-07 | 株式会社エヌ・エフ・ジー | 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 |
-
2007
- 2007-08-31 US US12/439,436 patent/US20100186288A1/en not_active Abandoned
- 2007-08-31 SG SG2011060373A patent/SG174732A1/en unknown
- 2007-08-31 EP EP07806892A patent/EP2068080A1/fr not_active Withdrawn
- 2007-08-31 RU RU2009111851/05A patent/RU2440403C2/ru not_active IP Right Cessation
- 2007-08-31 CN CN2007800407567A patent/CN101535718B/zh not_active Expired - Fee Related
- 2007-08-31 KR KR1020097006588A patent/KR20090049085A/ko not_active Application Discontinuation
- 2007-08-31 WO PCT/JP2007/067451 patent/WO2008029898A1/fr active Application Filing
Non-Patent Citations (1)
Title |
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See references of WO2008029898A1 * |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
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 |
Also Published As
Publication number | Publication date |
---|---|
US20100186288A1 (en) | 2010-07-29 |
SG174732A1 (en) | 2011-10-28 |
WO2008029898A1 (fr) | 2008-03-13 |
RU2440403C2 (ru) | 2012-01-20 |
CN101535718A (zh) | 2009-09-16 |
CN101535718B (zh) | 2012-02-29 |
KR20090049085A (ko) | 2009-05-15 |
RU2009111851A (ru) | 2010-10-10 |
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