WO2001070914A1 - Gazole utilisable dans les moteurs thermiques et dans les piles a combustible - Google Patents
Gazole utilisable dans les moteurs thermiques et dans les piles a combustible Download PDFInfo
- Publication number
- WO2001070914A1 WO2001070914A1 PCT/JP2001/002331 JP0102331W WO0170914A1 WO 2001070914 A1 WO2001070914 A1 WO 2001070914A1 JP 0102331 W JP0102331 W JP 0102331W WO 0170914 A1 WO0170914 A1 WO 0170914A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- fuel oil
- volume
- fuel
- internal combustion
- vol
- Prior art date
Links
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/06—Combination of fuel cells with means for production of reactants or for treatment of residues
- H01M8/0606—Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants
- H01M8/0612—Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants from carbon-containing material
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, 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
- C10L1/02—Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only
-
- 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
- C10L1/02—Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only
- C10L1/023—Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only for spark ignition
-
- 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
- C10L1/04—Liquid carbonaceous fuels essentially based on blends of hydrocarbons
- C10L1/06—Liquid carbonaceous fuels essentially based on blends of hydrocarbons for spark ignition
-
- 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
- Y02E60/50—Fuel cells
Definitions
- the present invention relates to a fuel oil that can be used for both an internal combustion engine and a fuel cell, and more particularly to a fuel oil that is made of a petroleum hydrocarbon fraction such as a gasoline fraction and can be used for an internal combustion engine and a fuel cell.
- a fuel oil that is made of a petroleum hydrocarbon fraction such as a gasoline fraction and can be used for an internal combustion engine and a fuel cell.
- hydrogen is used as fuel for fuel cells.
- examples of such hydrogen include those using hydrogen gas as it is and those using hydrogen obtained by reforming or decomposing methanol or the like.
- the present invention has been made to solve the above problems.
- the present invention provides a fuel oil for a fuel cell that can efficiently produce hydrogen and has little deterioration of the reforming catalyst and the like without adversely affecting the reforming catalyst and the fuel cell electrode.
- the fuel oil for internal combustion engines and fuel cells which has a high octane number and can be used effectively without knocking, etc. It is intended to provide.
- the present inventors have conducted intensive studies in view of the above problems, and have found that a specific composition It has been found that the above object of the present invention can be achieved by using a gasoline fraction in the form of a fuel as a fuel oil.
- the present invention has been completed based on such findings. That is, the present invention
- the present invention first, but relates to the alkylene rate Togaso Li down 5 0 volume 0/0 or more content to that for the internal combustion engine and a fuel cell combined fuel oil (fuel oil 1),
- Arukire Togaso Li ting is Generally, it refers to an alkylated gasoline obtained by an alkylation reaction, which is rich in high octane-valued isoparaffins and does not contain an aromatic polyolefin fraction.
- an alkylated gasoline having an octane value of 90 to 100, preferably about 96 is used.
- Such an alkylated gasoline is obtained, for example, by introducing an alkyl group into a hydrocarbon fraction such as isoparaffin and an aromatic fraction, and the catalyst used in this case is sulfuric acid.
- acid catalysts such as hydrofluoric acid, synthetic zeolite, and solid acid catalysts such as solid phosphoric acid.
- the fuel oil 1 of the present invention contains the above alkylated gasoline in an amount of 50% by volume or more, preferably 50-95% by volume, more preferably 50-90% by volume, particularly preferably 5% by volume. It contains 0 to 80% by volume.
- Alkyle Togaso When the amount of the phosphorus is less than 50% by volume, the octane value is low and knocking may occur when used as a fuel for an internal combustion engine, which is not preferable. On the other hand, if it exceeds 95% by volume, startability may be deteriorated when used as a fuel for an internal combustion engine.
- the fuel oil 1 of the present invention preferably contains 1 to 50% by volume of isobentan in addition to the above-mentioned alkylated gasoline. If the amount of isopentane is less than 1% by volume, the effect of the addition may not be exhibited, and if it exceeds 50% by volume, the octane may not be used when used as a fuel for internal combustion engines. In some cases, knocking may occur due to low fuel pressure, or vapor locking may occur due to too high a vapor pressure. Such isopentane can be separated by distilling a hydrocarbon oil under normal pressure, and in the present invention, the octane value is 85 to 95, preferably 90 to 90. And a vapor pressure of about 130 to 170 kPa, preferably about 150 kPa, is preferably used.
- the fuel oil 1 of the present invention preferably contains a hydrocarbon compound having 4 carbon atoms in an amount of 1 to 12% by volume.
- the hydrocarbon compound having 4 carbon atoms in the present invention include butane, n-butene, iso-butene and the like, and those appropriately obtained by a method common in the art are used. You can do this. If the amount of the above hydrocarbon compound is less than 1% by volume, the effect of the addition may not be exhibited. If it exceeds 12% by volume, the vapor pressure may be reduced when used as a fuel for internal combustion engines. May be too high to cause the vapor locking phenomenon.
- the fuel oil 1 of the present invention preferably further contains an oxygen-containing compound at 7% by volume or less.
- the oxygenates include MTBE (methyl-t-butyl ether), ETBE (ethyl-t-butyl ether), TAME (t-amyl methyl ether), etc. Preferred from the aspect.
- MTBE methyl-t-butyl ether
- ETBE ethyl-t-butyl ether
- TAME t-amyl methyl ether
- the fuel oil 1 of the present invention contains the oxygen-containing compound in an amount of 1 to 7% by volume.
- the fuel oil 1 of the present invention preferably further contains 1 to 30% by volume of desulfurized light naphtha.
- the desulfurized light naphtha normal para Fi emission of C 4 ⁇ C 7, Lee sono.
- crude oil is fractionated as light naphtha by a normal pressure distillation unit and crude oil is fractionated as light naphtha by a naphtha desulfurization unit, or crude oil is separated as full range naphtha by a normal pressure distillation unit. This is obtained by fractionating and distilling light naphtha after desulfurization with a naphtha desulfurization unit.
- the sulfur content of the above desulfurized light naphtha is usually 5 wt ppm or less, preferably 1 wt ppm or less, more preferably 0.1 wt ppm or less.
- an isomerized desulfurized light naphtha having a ratio of isoparaffin to normal paraffin of 1 or more, preferably 1.5 or more, and more preferably 2.5 or more is used. Is preferred.
- Such isomerized desulfurized light naphtha is commonly used in the industry.
- One that is isomerized by a commonly used method for example, by passing desulfurized light naphtha through a platinum catalyst such as a platinum-supported alumina catalyst, a platinum-supported zeolite catalyst, or a platinum-supported strongly acidic carrier catalyst. Can be used.
- desulfurized light naphtha is 10 to 60% by volume, debenzen reformed.
- the desulfurized light naphtha and the hydrocarbon compound having 4 carbon atoms those similar to the desulfurized light naphtha and the hydrocarbon having 4 carbon atoms used in the fuel oil 1 are used.
- the content of desulfurized light naphtha in fuel oil 2 is less than 10% by volume, the aromatic content increases, and the reforming reaction is disadvantageous when used as a fuel for a fuel cell. If it exceeds 60% by volume, the octane number will be low and knocking may occur when used as a fuel for internal combustion engines.
- the effect of increasing the vapor pressure when used as a fuel for an internal combustion engine and improving the startability of the engine can be obtained. If the amount is more than 10% by volume, the vapor pressure may be too high, causing a vapor lock phenomenon.
- the aforementioned fuel oils 2, de base benzene reformed gasoline Li down 4 0-9 0 volume 0/0 contains.
- the modified gasoline generally refers to gasoline obtained by subjecting a straight-running gasoline having a low octane number to thermal reforming or catalytic reforming treatment, and in the present invention, octane Those having a value of 95 to 100 are preferably used.
- the catalyst used in the above catalytic reforming treatment examples thereof include a platinum-based catalyst.
- Debenzene-modified gasoline refers to gasoline obtained by removing benzene from reformed gasoline by distillation or the like.
- the first fractionation column of the reformed gasoline is used to separate a low-boiling fraction mainly composed of a saturated hydrocarbon having 5 carbon atoms from the top of the column. (Tower temperature 73 to 83 ° C, overhead pressure 3 to 4 kg / cm 2 G)
- benzene which is usually contained in the reformed gasoline at 4 to 10% by volume, can be reduced to 0 to 0.5% by volume, which is advantageous not only for the reforming reaction but also for the medium boiling point. Since a fraction having a low octane number is removed together with benzene as a fraction, the octane number can be increased, which is a more preferable mode when used as an internal combustion engine. Become.
- a method for reducing the benzene content in the reformed gasoline Li down if example embodiment, (1) contacting changing operating conditions of the reformer, (2) C 6 fraction of the desulfurized heavy naphtha ingredients (3) A method of removing the benzene fraction from the reformed gasoline by distillation, and (4) A hydrogenation treatment of the benzene component in the reformed gasoline by catalytic reaction. Cyclohexane Etc., which are then led to an isomerizer to be isomerized to high octane number isomers. (5) The benzene component in the reformed gasoline is alkylated by catalytic reaction.
- the octane value will be low and knocking may occur when used as a fuel for internal combustion engines. If it exceeds 90% by volume, the aromatic content increases, and the reforming reaction may be disadvantageous when used as a fuel for a fuel cell.
- both the fuel oils 1 and 2 for internal combustion engines and fuel cells of the present invention have an octane number of 89 or more according to the research method. If the research method octane value is less than 89, knocking may occur when used as a fuel for internal combustion engines.
- the fuel oils 1 and 2 for the internal combustion engine and the fuel cell of the present invention have a vapor pressure of 44 to 93 kPa. If the vapor pressure is lower than 44 kPa, the engine may have poor startability when used as a fuel for internal combustion engines. If the vapor pressure is higher than 93 kPa, the steam Pressure may be too high, causing vapor locking.
- the fuel oil of the present invention can be used for both internal combustion engines and fuel cells.
- the octane value when used for an internal combustion engine, the octane value is high, and it can be used effectively without knocking, etc., and when used for a fuel cell, hydrogen is efficiently produced. You can do The deterioration of the reforming catalyst can be reduced without adversely affecting the quality catalyst and the fuel cell electrode.
- the fuel oil of the present invention has characteristics such as high purity of hydrogen produced by the method and a small decrease in hydrogen partial pressure. Therefore, the fuel oil is suitable for producing hydrogen for a fuel cell.
- the fuel oil is first desulfurized as necessary.
- a hydrodesulfurization method usually, a hydrodesulfurization method is used, and the method uses a hydrodesulfurization catalyst such as Co—Mo / alumina or Ni—Mo / alumina and a hydrogen sulfide adsorption such as Zn—.
- the test is carried out at a pressure of normal pressure to 5 MPa and a temperature of 200 to 400 ° C.
- steam reforming and / or partial oxidation is performed on the desulfurized fuel oil.
- ADVANTAGE OF THE INVENTION According to this invention, the fuel oil which can produce hydrogen efficiently without carbon deposition on a steam reforming catalyst etc. can be obtained.
- the method of steam reforming is not particularly limited, but is usually performed by the following method.
- the steam reforming catalyst used in this hydrogen production method is not particularly limited, but the supported metals include Ni, zirconium or ruthenium (Ru), rhodium (Rh), and platinum (Pt). And others using precious metals. These supported metals may be used alone or in combination of two or more.
- Ru is particularly desirable, and has a large effect of suppressing carbon deposition during the steam reforming reaction.
- the loading amount of Ru is preferably 0.05 to 20% by weight, more preferably 0.05 to 15% by weight, based on the carrier. If the supported amount is less than 0.05% by weight, the activity of the steam reforming reaction may be extremely reduced, and even if it exceeds 20% by weight, a remarkable increase in the activity is hardly obtained.
- a combination supporting Ru and zirconium can be given. Ru and zirconium may be supported simultaneously or separately.
- the zirconium content is preferably 0.5 to 20% by weight, more preferably 0.5 to 15% by weight, based on the carrier, in terms of Zr02.
- the content of lute is in the atomic ratio of Kurt / luteum, preferably from 0.11 to 30 and more preferably from 0.1 to 30.
- the content of magnesium is preferably magnesia.
- the content is preferably 0.5 to 20% by weight, more preferably 0.5 to 15% by weight in terms of (Mg0).
- an inorganic oxide is used, and specific examples thereof include alumina, silica, zirconia, magnesia, and a mixture thereof. Of these, alumina and zirconia are particularly preferred.
- a preferred embodiment of the steam reforming catalyst is a catalyst in which Ru is supported on zirconium.
- This zirconia may be a simple zirconia (Zr02) or a stabilized zirconia containing a stabilizing component such as magnesia.
- a stabilizing component such as magnesia.
- the stabilized zirconia those containing magnesia, yttria, celia, and the like are preferable.
- a catalyst in which Ru and zirconium, or Ru and zirconium, and additionally a root and / or magnesium are supported on an alumina carrier is used.
- alumina ⁇ .1-alumina, which is particularly excellent in heat resistance and mechanical strength, is preferred.
- the ratio S / C (molar ratio) of water vapor (S) to carbon (C) derived from fuel oil is 2-5, and even 2-4.
- the preferred method is to perform steam reforming in a state. If steam reforming is performed at a high S / C (molar ratio) of 5 or more, excess steam must be produced, resulting in large heat loss and reduced efficiency of hydrogen production. If the S / C is less than 2, the amount of generated hydrogen may decrease.
- a method of performing steam reforming while maintaining the inlet temperature of the steam reforming catalyst layer at 63 ° C. or lower is preferable.
- the temperature at the inlet of the steam reforming catalyst layer tends to rise due to the addition of oxygen, it is necessary to control the temperature. If the inlet temperature exceeds 630 t, thermal decomposition of the raw material hydrocarbons is accelerated, and carbon may precipitate on the catalyst or the reaction tube wall via the generated radicals, which may make operation difficult.
- the temperature at the outlet of the catalyst layer is not particularly limited, but is preferably in the range of 650 to 800 ° C. If the outlet temperature of the catalyst layer is lower than 650 ° C, the amount of generated hydrogen is not sufficient.In order to react at a temperature exceeding 800 ° C, the reactor may need to be made of a heat-resistant material in particular. This is because it is not economically favorable.
- the reaction pressure is preferably normal pressure to 3 MPa, and more preferably normal pressure to IMPa.
- the flow rate of fuel oil is 0.1 to 100 h- 1 in LHSV.
- the partial oxidation reaction is preferably carried out under a catalyst in which a noble metal such as ruthenium or the like is supported on a heat-resistant oxide, at a reaction pressure of normal pressure to 5 MPa, a reaction temperature of 400 to 1,100 ° (: oxygen / carbon ratio 0. 2 ⁇ 0. 8, LHSVO. carried out in 1 ⁇ 1 0 0 h 1. also, the field of adding steam In this case, the S / C ratio is 0.4 to 4.
- hydrogen can be efficiently produced, and the reforming catalyst and the like can be deteriorated without adversely affecting the reforming catalyst and the fuel cell electrode.
- Low-cost fuel oil for fuel cells and when used as fuel oil for engines of internal combustion engines for automobiles, an internal combustion engine that has a high octane value and can be used without knocking etc. It is possible to provide a dual-use fuel oil for fuel cells and fuel cells.
- a fuel oil having the composition and properties shown in Table 1 was prepared, and the respective resiroctane number and vapor pressure of each were measured according to JISK 280 and JISK 258, respectively.
- a hydrogen production experiment was performed as shown below, and a coking test was performed on the catalyst after the reaction. The results are shown in Table 1.
- Desulfurization catalyst C 0- ⁇ 0 (first stage) / ⁇ ⁇ 0 (second stage)
- (2nd stage) Reforming catalyst 20% by weight of water was added to ⁇ -alumina powder, mixed with a kneader and compression-molded to obtain a cylindrical molded body having a diameter of 5 mm and a length of 5 mm. After drying at 200 ° C for 3 hours, it was calcined at 128 ° C for 26 hours to obtain an alumina carrier. Zirconium O carboxymethyl chloride (Z r 0 (0 H) C 1) in an aqueous solution of (Z r ⁇ 2 in 2 equivalent.
- Carbon deposition rate (%) length of carbon deposited part / total catalyst length
- the fuel oil of the present invention is suitable for a fuel oil that can also be used for an internal combustion engine and a fuel cell. More specifically, the fuel oil is composed of a petroleum hydrocarbon fraction such as a gasoline fraction. Suitable for such fuel oils.
Description
Claims
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AU2001242767A AU2001242767A1 (en) | 2000-03-23 | 2001-03-23 | Fuel oil for use both in internal combustion in engine and fuel cell |
EP01915728A EP1266949A4 (en) | 2000-03-23 | 2001-03-23 | GASOLINE FOR USE IN THERMAL MOTORS AND FUEL CELLS |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2000-81357 | 2000-03-23 | ||
JP2000081357A JP2001262163A (ja) | 2000-03-23 | 2000-03-23 | 内燃機関用及び燃料電池用兼用燃料油 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2001070914A1 true WO2001070914A1 (fr) | 2001-09-27 |
Family
ID=18598307
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/JP2001/002331 WO2001070914A1 (fr) | 2000-03-23 | 2001-03-23 | Gazole utilisable dans les moteurs thermiques et dans les piles a combustible |
Country Status (5)
Country | Link |
---|---|
US (1) | US20030145514A1 (ja) |
EP (1) | EP1266949A4 (ja) |
JP (1) | JP2001262163A (ja) |
AU (1) | AU2001242767A1 (ja) |
WO (1) | WO2001070914A1 (ja) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2846002A1 (fr) * | 2002-10-22 | 2004-04-23 | Totalfinaelf France | Nouveau carburant a indice d'octane eleve et a teneur abaissee en plomb |
FR2846003A1 (fr) * | 2002-10-22 | 2004-04-23 | Total France | Nouveau carburant a indice d'octane eleve et a teneur abaissee en plomb |
Families Citing this family (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AU4688701A (en) * | 2000-04-10 | 2001-10-23 | Nippon Mitsubishi Oil Corporation | Fuel for use in fuel cell system |
EP1273650A4 (en) * | 2000-04-10 | 2004-10-06 | Nippon Oil Corp | FUEL FOR USE IN A FUEL CELL |
AU4688401A (en) * | 2000-04-10 | 2001-10-23 | Nippon Mitsubishi Oil Corporation | Fuel for use in fuel cell system |
EP1346013A1 (en) * | 2000-12-21 | 2003-09-24 | Bp Oil International Limited | Dual use hydrocarbon fuel composition |
GB0121871D0 (en) * | 2001-09-11 | 2001-10-31 | Bp Plc | Hydrogen production |
AU2003301272A1 (en) * | 2002-10-14 | 2004-05-04 | Shell Internationale Research Maatschappij B.V. | A process for the catalytic conversion of a gasoline composition |
US20080134571A1 (en) | 2006-12-12 | 2008-06-12 | Jorg Landschof | Unleaded fuel compositions |
US20100018112A1 (en) * | 2008-07-28 | 2010-01-28 | Joseph Michael Russo | High octane unleaded fuel compositions and methods for increasing the maximum torque output value produced burning same |
JP5439840B2 (ja) * | 2009-02-13 | 2014-03-12 | 日産自動車株式会社 | 燃料改質装置 |
US8679204B2 (en) | 2009-11-17 | 2014-03-25 | Shell Oil Company | Fuel formulations |
CA2797163A1 (en) | 2011-12-01 | 2013-06-01 | Shell Internationale Research Maatschappij B.V. | Balanced unleaded fuel compositions |
CN104531236B (zh) * | 2014-12-29 | 2016-04-20 | 清华大学 | 一种内燃机用宽馏分燃料 |
WO2021206873A1 (en) * | 2020-04-09 | 2021-10-14 | Exxonmobil Research And Engineering Company | Fuel blending component composition and method for reducing criteria emissions |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5031516A (ja) * | 1973-07-24 | 1975-03-28 | ||
JPS63317591A (ja) * | 1987-06-19 | 1988-12-26 | Idemitsu Kosan Co Ltd | 高性能燃料油 |
JPH0570780A (ja) * | 1991-09-12 | 1993-03-23 | Sekiyu Sangyo Kasseika Center | 中軽質油の深度脱硫方法 |
JPH0913051A (ja) * | 1995-06-26 | 1997-01-14 | Idemitsu Kosan Co Ltd | ガソリン基材及び該基材を用いた無鉛ガソリン |
JPH0971789A (ja) * | 1995-07-06 | 1997-03-18 | Idemitsu Kosan Co Ltd | 無鉛ガソリン |
JPH11236580A (ja) * | 1997-12-18 | 1999-08-31 | Idemitsu Kosan Co Ltd | 無鉛ガソリン組成物 |
JPH11311136A (ja) * | 1998-04-28 | 1999-11-09 | Hitachi Ltd | ハイブリッド自動車およびその駆動装置 |
Family Cites Families (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB520564A (en) * | 1938-03-11 | 1940-04-26 | Standard Oil Dev Co | An improved manufacture of motor fuel |
US3081255A (en) * | 1959-05-18 | 1963-03-12 | Texaco Inc | Method of treating a petroleum fraction using molecular sieve aluminosilicate selective adsorbents |
US4140622A (en) * | 1977-11-03 | 1979-02-20 | Uop Inc. | Process to reduce the benzene content of gasoline |
CA1306356C (en) * | 1987-05-20 | 1992-08-18 | Takao Nagasawa | High-octane-rating gasolines |
US4812146A (en) * | 1988-06-09 | 1989-03-14 | Union Oil Company Of California | Liquid fuels of high octane values |
US5200059A (en) * | 1991-11-21 | 1993-04-06 | Uop | Reformulated-gasoline production |
JPH06128570A (ja) * | 1992-10-14 | 1994-05-10 | Nippon Oil Co Ltd | 無鉛高オクタン価ガソリン |
US5624548A (en) * | 1994-07-21 | 1997-04-29 | Texaco Inc. | Heavy naphtha hydroconversion process |
JPH0971788A (ja) * | 1995-09-07 | 1997-03-18 | Cosmo Sogo Kenkyusho:Kk | 無鉛高性能ガソリン |
US20020045785A1 (en) * | 1996-11-18 | 2002-04-18 | Bazzani Roberto Vittorio | Fuel composition |
JP4646345B2 (ja) * | 1999-12-27 | 2011-03-09 | Jx日鉱日石エネルギー株式会社 | 燃料油添加剤及び該添加剤を含有してなる燃料油組成物 |
-
2000
- 2000-03-23 JP JP2000081357A patent/JP2001262163A/ja active Pending
-
2001
- 2001-03-23 WO PCT/JP2001/002331 patent/WO2001070914A1/ja not_active Application Discontinuation
- 2001-03-23 EP EP01915728A patent/EP1266949A4/en not_active Withdrawn
- 2001-03-23 US US10/221,786 patent/US20030145514A1/en not_active Abandoned
- 2001-03-23 AU AU2001242767A patent/AU2001242767A1/en not_active Abandoned
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5031516A (ja) * | 1973-07-24 | 1975-03-28 | ||
JPS63317591A (ja) * | 1987-06-19 | 1988-12-26 | Idemitsu Kosan Co Ltd | 高性能燃料油 |
JPH0570780A (ja) * | 1991-09-12 | 1993-03-23 | Sekiyu Sangyo Kasseika Center | 中軽質油の深度脱硫方法 |
JPH0913051A (ja) * | 1995-06-26 | 1997-01-14 | Idemitsu Kosan Co Ltd | ガソリン基材及び該基材を用いた無鉛ガソリン |
JPH0971789A (ja) * | 1995-07-06 | 1997-03-18 | Idemitsu Kosan Co Ltd | 無鉛ガソリン |
JPH11236580A (ja) * | 1997-12-18 | 1999-08-31 | Idemitsu Kosan Co Ltd | 無鉛ガソリン組成物 |
JPH11311136A (ja) * | 1998-04-28 | 1999-11-09 | Hitachi Ltd | ハイブリッド自動車およびその駆動装置 |
Non-Patent Citations (1)
Title |
---|
See also references of EP1266949A4 * |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2846002A1 (fr) * | 2002-10-22 | 2004-04-23 | Totalfinaelf France | Nouveau carburant a indice d'octane eleve et a teneur abaissee en plomb |
FR2846003A1 (fr) * | 2002-10-22 | 2004-04-23 | Total France | Nouveau carburant a indice d'octane eleve et a teneur abaissee en plomb |
WO2004037952A1 (fr) * | 2002-10-22 | 2004-05-06 | Total France | Nouveau carburant a indice d'octane eleve et a teneur abaissee en plomb |
Also Published As
Publication number | Publication date |
---|---|
AU2001242767A1 (en) | 2001-10-03 |
EP1266949A4 (en) | 2005-01-12 |
EP1266949A1 (en) | 2002-12-18 |
JP2001262163A (ja) | 2001-09-26 |
US20030145514A1 (en) | 2003-08-07 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP5114164B2 (ja) | ガソリン組成物の製造方法 | |
WO2001070914A1 (fr) | Gazole utilisable dans les moteurs thermiques et dans les piles a combustible | |
JP4776287B2 (ja) | クリーンガソリン組成物及びその製造方法 | |
WO2001044412A1 (fr) | Carburant pour pile a combustible composition de carburant et systeme de propulsion d'automobile | |
JP5027971B2 (ja) | 燃料油組成物 | |
JP4916743B2 (ja) | 環境対応型ガソリン組成物及びその製造方法 | |
JP4803790B2 (ja) | クリーンガソリン組成物 | |
JP5186183B2 (ja) | ガソリン組成物 | |
JP4490533B2 (ja) | 燃料電池用燃料油 | |
JP4426039B2 (ja) | 燃料電池用燃料油及びその製造方法 | |
JP4213062B2 (ja) | 環境対応型クリーンガソリンおよびその製造方法 | |
JP2001279271A (ja) | 燃料電池用燃料油及び燃料電池用水素の製造方法 | |
JP4916742B2 (ja) | 高オクタン価環境対応型ガソリン組成物及びその製造方法 | |
JP2001262164A (ja) | 燃料電池用燃料油 | |
JP3973191B2 (ja) | 水素発生用炭化水素燃料およびその製造方法 | |
JP4850412B2 (ja) | 環境対応型ガソリン組成物の製造方法 | |
WO2004035468A1 (en) | A process for the catalytic conversion of a gasoline composition | |
JP2006182792A (ja) | 液化石油ガスの製造方法 | |
JPS6116985A (ja) | 無鉛高オクタン価ガソリンの製造方法 | |
JP4832104B2 (ja) | ガソリン基材の製造方法及びガソリン組成物 | |
JP4798649B2 (ja) | 環境対応型ガソリン組成物及びその製造方法 | |
CN1648112A (zh) | 制备含硫的蒸汽裂化器原料的方法 | |
JP2008138186A (ja) | ガソリン組成物 | |
JP2006233033A (ja) | 二酸化炭素低排出ガソリン組成物 | |
JP2001262161A (ja) | 燃料電池用燃料油 |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
AK | Designated states |
Kind code of ref document: A1 Designated state(s): AE AG AL AM AT AU AZ BA BB BG BR BY BZ CA CH CN CR CU CZ DE DK DM DZ EE ES FI GB GD GE GH GM HR HU ID IL IN IS KE KG KP KR KZ LC LK LR LS LT LU LV MA MD MG MK MN MW MX MZ NO NZ PL PT RO RU SD SE SG SI SK SL TJ TM TR TT TZ UA UG US UZ VN YU ZA ZW |
|
AL | Designated countries for regional patents |
Kind code of ref document: A1 Designated state(s): GH GM KE LS MW MZ SD SL SZ TZ UG ZW AM AZ BY KG KZ MD RU TJ TM AT BE CH CY DE DK ES FI FR GB GR IE IT LU MC NL PT SE TR BF BJ CF CG CI CM GA GN GW ML MR NE SN TD TG |
|
DFPE | Request for preliminary examination filed prior to expiration of 19th month from priority date (pct application filed before 20040101) | ||
121 | Ep: the epo has been informed by wipo that ep was designated in this application | ||
WWE | Wipo information: entry into national phase |
Ref document number: 2001915728 Country of ref document: EP |
|
WWE | Wipo information: entry into national phase |
Ref document number: 10221786 Country of ref document: US |
|
WWP | Wipo information: published in national office |
Ref document number: 2001915728 Country of ref document: EP |
|
WWW | Wipo information: withdrawn in national office |
Ref document number: 2001915728 Country of ref document: EP |