WO1995027849A1 - Dispositif de traitement de combustibles - Google Patents
Dispositif de traitement de combustibles Download PDFInfo
- Publication number
- WO1995027849A1 WO1995027849A1 PCT/JP1995/000684 JP9500684W WO9527849A1 WO 1995027849 A1 WO1995027849 A1 WO 1995027849A1 JP 9500684 W JP9500684 W JP 9500684W WO 9527849 A1 WO9527849 A1 WO 9527849A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- fuel
- fuel processing
- aqueous solution
- ceramic
- activated
- Prior art date
Links
- 239000000446 fuel Substances 0.000 title claims abstract description 204
- 239000000463 material Substances 0.000 claims abstract description 64
- 239000000919 ceramic Substances 0.000 claims description 54
- 239000007787 solid Substances 0.000 claims description 38
- 239000007864 aqueous solution Substances 0.000 claims description 27
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 20
- 239000013078 crystal Substances 0.000 claims description 19
- 239000000243 solution Substances 0.000 claims description 8
- 229910021578 Iron(III) chloride Inorganic materials 0.000 claims description 7
- RBTARNINKXHZNM-UHFFFAOYSA-K iron trichloride Chemical compound Cl[Fe](Cl)Cl RBTARNINKXHZNM-UHFFFAOYSA-K 0.000 claims description 7
- 235000003891 ferrous sulphate Nutrition 0.000 claims description 6
- 239000011790 ferrous sulphate Substances 0.000 claims description 6
- BAUYGSIQEAFULO-UHFFFAOYSA-L iron(2+) sulfate (anhydrous) Chemical compound [Fe+2].[O-]S([O-])(=O)=O BAUYGSIQEAFULO-UHFFFAOYSA-L 0.000 claims description 6
- 229910000359 iron(II) sulfate Inorganic materials 0.000 claims description 6
- 238000011144 upstream manufacturing Methods 0.000 claims description 4
- 239000011343 solid material Substances 0.000 claims description 2
- 230000003472 neutralizing effect Effects 0.000 claims 1
- 239000012530 fluid Substances 0.000 abstract description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 11
- 239000002245 particle Substances 0.000 description 8
- 239000004372 Polyvinyl alcohol Substances 0.000 description 7
- NMCUIPGRVMDVDB-UHFFFAOYSA-L iron dichloride Chemical class Cl[Fe]Cl NMCUIPGRVMDVDB-UHFFFAOYSA-L 0.000 description 7
- 229920002451 polyvinyl alcohol Polymers 0.000 description 7
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 6
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 6
- 230000000052 comparative effect Effects 0.000 description 6
- 239000011812 mixed powder Substances 0.000 description 6
- 230000000694 effects Effects 0.000 description 5
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 description 5
- 239000012798 spherical particle Substances 0.000 description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 4
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 4
- 229910052799 carbon Inorganic materials 0.000 description 4
- 238000012856 packing Methods 0.000 description 4
- 238000002360 preparation method Methods 0.000 description 4
- 229910052582 BN Inorganic materials 0.000 description 3
- PZNSFCLAULLKQX-UHFFFAOYSA-N Boron nitride Chemical compound N#B PZNSFCLAULLKQX-UHFFFAOYSA-N 0.000 description 3
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 3
- 150000002505 iron Chemical class 0.000 description 3
- 229910052742 iron Inorganic materials 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 150000004767 nitrides Chemical class 0.000 description 3
- RVTZCBVAJQQJTK-UHFFFAOYSA-N oxygen(2-);zirconium(4+) Chemical compound [O-2].[O-2].[Zr+4] RVTZCBVAJQQJTK-UHFFFAOYSA-N 0.000 description 3
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 description 3
- 229910001928 zirconium oxide Inorganic materials 0.000 description 3
- 229910021536 Zeolite Inorganic materials 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 2
- 239000012153 distilled water Substances 0.000 description 2
- 238000011049 filling Methods 0.000 description 2
- 239000008187 granular material Substances 0.000 description 2
- 239000012046 mixed solvent Substances 0.000 description 2
- 238000005096 rolling process Methods 0.000 description 2
- 235000011121 sodium hydroxide Nutrition 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 239000010457 zeolite Substances 0.000 description 2
- 229910052796 boron Inorganic materials 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000010981 drying operation Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000003350 kerosene Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000011259 mixed solution Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- XTUSEBKMEQERQV-UHFFFAOYSA-N propan-2-ol;hydrate Chemical compound O.CC(C)O XTUSEBKMEQERQV-UHFFFAOYSA-N 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000002407 reforming Methods 0.000 description 1
- 239000011435 rock Substances 0.000 description 1
- 150000003384 small molecules Chemical class 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02M—SUPPLYING COMBUSTION ENGINES IN GENERAL WITH COMBUSTIBLE MIXTURES OR CONSTITUENTS THEREOF
- F02M27/00—Apparatus for treating combustion-air, fuel, or fuel-air mixture, by catalysts, electric means, magnetism, rays, sound waves, or the like
- F02M27/06—Apparatus for treating combustion-air, fuel, or fuel-air mixture, by catalysts, electric means, magnetism, rays, sound waves, or the like by rays, e.g. infrared and ultraviolet
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02M—SUPPLYING COMBUSTION ENGINES IN GENERAL WITH COMBUSTIBLE MIXTURES OR CONSTITUENTS THEREOF
- F02M27/00—Apparatus for treating combustion-air, fuel, or fuel-air mixture, by catalysts, electric means, magnetism, rays, sound waves, or the like
- F02M27/02—Apparatus for treating combustion-air, fuel, or fuel-air mixture, by catalysts, electric means, magnetism, rays, sound waves, or the like by catalysts
-
- 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
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T137/00—Fluid handling
- Y10T137/5109—Convertible
-
- 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
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T137/00—Fluid handling
- Y10T137/5327—Hydrant type
- Y10T137/5333—Water crane type
- Y10T137/5339—Spout operated valve
Definitions
- the present invention relates to a fuel processing device used for processing fuel.
- Conventional technology is a fuel processing device used for processing fuel.
- this type of fuel processing has a fuel plate (2) with a fuel inlet (3) at one end and a fuel outlet (4) at the other end.
- a fuel treatment device (1) is provided in which a granulated fuel treatment material (7) such as activated carbon, zeolite, ceramic or the like is filled between the perforated plates (5, 6). I have.
- the fuel processing material in the fuel processing vessel (2) is used to improve the contact efficiency between the fuel and the fuel processing material (7) in order to completely perform the fuel processing. It is necessary to increase the packing density of the fuel treatment material (7). If the packing density of the fuel treatment material (7) is increased in this way, the pressure loss due to the resistance of the fuel treatment material (7) packed bed increases, and the fuel Had to be introduced into the fuel processor (1) at high pressure.
- the present invention provides a fuel processing container (12) having a fuel inlet (14, 24, 34) at one end and a fuel outlet (15, 25, 35) at the other end. , 22, 32) to provide a fuel treatment device (11, 21, 31, 31) in which a fuel treatment material (16, 26, 36) is movably moved by the fuel flow.
- a fuel treatment material (16, 26, 36) is movably moved by the fuel flow.
- light oil, gasoline, kerosene, etc. and the arrangement state of the fuel processing material (16, 26, 36) in the fuel processing container (12, 22, 32) includes the fuel processing material (16).
- the fuel processing vessel (11) in an open state, or roughly fill the granulated fuel processing material (26) to such an extent that it can be moved by the fuel flow.
- a plurality of the perforated small containers (27) are filled in the fuel processing container (22), or the fuel processing material (36) is formed into a blade shape, and Others to place the fuel processing vessel (32) in towards the plurality upstream direction desired.
- the fuel processing material (16, 26, 36) is preferably a ceramic solid, and as the ceramic solid, ferric chloride is dissolved in a large amount of aqueous caustic soda, and then neutralized with hydrochloric acid.
- the crystals obtained by concentration and Z or ferrous sulfate are dissolved in a large amount of hydrochloric acid aqueous solution and then immersed in an aqueous solution of crystals obtained by concentration and / or passed through the aqueous solution. It is desirable to use activated ceramics that have been contacted with air.
- fuel is introduced into the fuel processing vessel (12, 22, 32) from the inlet (14, 24, 34).
- the fuel is processed by contacting the fuel processing material (16, 26, 36).
- the fuel processing material (16, 26, 36) moves in the fuel processing vessel (12, 22, 32) due to the fluid pressure of the fuel, and moves due to the movement of the fuel processing material (16, 26, 36).
- the fuel is agitated, and as a result, the contact efficiency between the fuel processing material (16, 26,) and the fuel is greatly improved.
- the fuel processing material (16) is moved by the fluid pressure of the fuel. Rolling or moving within (12), the fuel is agitated by rolling or moving the fuel processing material (16), and as a result, the contact efficiency between the fuel processing material (16) and the fuel is reduced. Improve greatly.
- the far-infrared effect of the ceramic causes the molecules of the fuel to become small molecules, or the clusters of the molecules to become small, resulting in a decrease in the fuel cluster.
- the processing fluid is modified.
- the activated iron chloride aqueous solution When the ceramic is immersed or the air passing through the aqueous solution is brought into contact with the ceramic, the above-described effect of the ceramic is amplified.
- Examples of the ceramic used in the present invention include well-known ceramics such as, for example, gay oxide, aluminum oxide, zirconium oxide, titanium oxide, gay nitride, boron nitride, and gay carbide, and these are two types.
- the mixture may be mixed as described above, and a desirable combination is a mixed ceramic of a gay oxide and an aluminum oxide.
- 1 and 2 relate to a first embodiment of the present invention.
- FIG. 1 is a longitudinal sectional view.
- FIG. 2 is a cross-sectional view.
- FIG. 3 and FIG. 4 relate to a second embodiment of the present invention.
- FIG. 3 is a longitudinal sectional view.
- FIG. 4 is a perspective view of the perforated small container in an opened state.
- FIGS. 5 and 6 relate to a third embodiment of the present invention.
- FIG. 5 is a longitudinal sectional view.
- FIG. 6 is a sectional view taken along line AA in FIG.
- FIG. 7 is an explanatory sectional view of a conventional example. Detailed description of the invention
- FIG. 1 and FIG. 2 show a first embodiment of the present invention.
- a fuel reformer (11) which is a fuel processor shown in the figure, includes a disc-shaped fuel processing vessel (12), a flow path (13) formed on the periphery of the fuel processing vessel (12), A fuel inlet (14) obliquely connected to the flow path (13), a fuel outlet (15) connected to the flow path (13) from above, and an open filling in the flow path (13) And a plurality of granular ceramic solids (16).
- the ceramic solid (16) is usually formed into granules having a particle size of about 3 to 10 particles, preferably 5 to 7 mm.
- the fuel F is stirred in the flow path (13) by the movement of the ceramic solid (16), makes efficient contact with the ceramic solid, and is radiated from the ceramic solid (16). Is decomposed and degraded to lower molecular weight by energy. So low Molecularized fuel F has very good combustion efficiency, and almost no C or C0 is generated during combustion.
- the porous small container (27) is spherical and comprises a pair of net cages (27B, 27C) divided so as to be openable and closable via a hinge (27A).
- the basket (27B, 27C) is closed by superimposing the flanges (27D, 27E) on the periphery and fitting a rock band (27F)
- the ceramic solid (26) filled in the small porous container (27) is usually formed into granules having a particle size of about 3 to about 10 and preferably 5 to 7 mm, so that the closest packing can be achieved. If it is set to 100%, the packing density is usually about 60 to 90%, so that the fuel processing material (26) can move in the small porous container (27).
- FIGS. 5 and 6 show a third embodiment of the present invention.
- a fuel reformer (31) which is a fuel processor of the present embodiment, is connected to a cylindrical fuel processor (32) having a flow path (33) formed therein and one end of the fuel processor (32).
- the number of blades of the blade-shaped ceramic solid material is not particularly limited, but it is preferable that the blades are arranged as densely as possible unless the fluid resistance is significantly increased. It is preferable that the diameter of the blade of the blade-shaped ceramic solid is set slightly smaller than the inner diameter of the fuel processing container (32). Although two blades are used in this embodiment, three blades, four blades, or more blades may be used.
- the ceramic solid (36) is changed by the fluid pressure of the fuel F.
- the fuel F rotates, and the fuel F is stirred by the rotation of the ceramic solid (36), and efficiently comes into contact with the ceramic solid (36) to be depolymerized. .
- the fuel F thus treated is discharged from the fuel outlet (35).
- the results obtained by processing the vehicle fuel using the fuel processor (11, 21, 31) of the present invention and the conventional fuel processor (1) as a comparison and performing an actual vehicle running test are shown below.
- the two types of fuels A, A2, B, B2, C, C2, D, D2, E, E2 and F, F2 used in the fuel processor (11, 21, 31) The treatment material (16, 26, 36) and the fuel treatment material (7) G used in the conventional fuel treatment device (1) were prepared as follows.
- the crystals were collected, dried in a desiccator under reduced pressure overnight, dissolved in 10 ml of a mixed solvent of isopropanol / water at a weight ratio of 80:20, and filtered with filter paper (No. 5C). The solution is filtered, concentrated under reduced pressure to remove the solvent and dried. The above extraction-concentration-drying operation is repeated several times to purify Activated iron chloride crystals are obtained.
- the crystals are dissolved in distilled water to make a 2 ppm aqueous solution.
- Fuel processing materials A, A2 Polyvinyl alcohol and water were mixed in a 1: 1 weight ratio mixed powder of gay oxide and aluminum oxide. The mixture is added and kneaded, and the kneaded material is formed into spherical particles having an average particle diameter of 6 and baked at 1000 ° C. for 3 hours to produce a ceramic solid.
- Fuel treatment material C, C 2 Polyvinyl alcohol and water are added to a 1: 1 weight ratio mixed powder of zirconium oxide and titanium oxide and kneaded, and the kneaded product is formed into spherical particles having an average particle diameter of 6 Then, it is baked at 1000 ° C for 3 hours to produce a ceramic solid.
- Fuel processing materials E, E 2 Polyvinyl alcohol and water are added to a powder mixture of 1: 1 by weight of gay nitride and boron nitride and kneaded, and the kneaded product is formed into a blade shape as shown in the third embodiment. Then, it is baked at 1000 ° C. for 3 hours to produce a ceramic solid.
- the above-mentioned ceramic solids A, C, and E are immersed in the aqueous solution, left for 2 hours, collected, and dried at 100 ° C. for 2 hours to obtain an activated ceramic solid.
- the aqueous solution was added to the ceramic solids A2, C2 and E2.
- the activated air is passed through at a flow rate of 51 / min for 3 hours to obtain activated ceramic solids.
- the crystals were collected and dried under reduced pressure overnight in a desiccator, dissolved in 10 ml of a mixed solvent of isopropanol-water at a weight ratio of 80:20, and filtered with filter paper (No. 5C). The solution is filtered, concentrated under reduced pressure to remove the solvent and dried. The above operation of extraction, concentration and drying is repeated several times to obtain purified activated iron chloride crystals.
- the crystals are dissolved in distilled water to make a 2 ppm aqueous solution.
- Fuel treatment materials B, B2 Polyvinyl alcohol and water were added to a 1: 1 weight ratio mixed powder of gay oxide and aluminum oxide. Is added and kneaded, and the kneaded material is formed into spherical particles having an average particle size of 6 and baked at 1000 ° C. for 3 hours to produce a ceramic solid.
- Fuel treatment materials D, D 2 zirconium oxide and titanium oxide
- Polyvinyl alcohol and water were added to the 1: 1 weight ratio mixed powder and kneaded, and the kneaded product was formed into spherical particles having an average particle diameter of 6 cm, and baked at 1000 for 3 hours. Make a solid compact.
- Fuel treatment materials F, F 2 Polyvinyl alcohol and water are added to a 1: 1 weight ratio mixed powder of gay nitride and boron nitride and kneaded, and the kneaded product is shaped into a blade shape as shown in the third embodiment. Then, it is baked at 1000 for 3 hours to produce a ceramic solid.
- Each of the above-mentioned ceramic solids is immersed in the aqueous solution, left for 2 hours, collected and dried for 100 hours to obtain an activated ceramic solid.
- the above-mentioned ceramic solids B, D, and F are immersed in the aqueous solution, left to stand for 2 hours, collected, dried for 100 hours and dried for 2 hours to obtain an activated ceramic solid.
- activated ceramic solids are obtained by passing the air passing through the aqueous solution through the ceramic solids B2, D2, and F2 at a flow rate of 51 / min for 3 hours.
- Polyvinyl alcohol and water are added to a 1: 1 weight ratio mixed powder of gay oxide and aluminum oxide and kneaded, and the kneaded product is formed into spherical particles having an average particle diameter of 6 Bake for 3 hours at ° C to produce a ceramic solid.
- the fuel processing materials A, A 2, B and B 2 are filled in the fuel processing container (12) of the first embodiment in an open state as shown in FIGS. 1 and 2, and the fuel processing materials C, C As shown in Figs. 3 and 4, 2, D and D2 are filled in the porous small container (27) of the second embodiment at a filling density of 80%, and then the fuel treatment container (22) is filled.
- the fuel processing materials E, E 2, F and F 2 are arranged in the fuel processing container (32) of the third embodiment as shown in FIGS. 5 and 6.
- Comparative Example 1 The fuel processing container (2) of the conventional example in which the fuel processing material G is densely filled as shown in Fig. 7 is referred to as Comparative Example 1, and the fuel processing material A treated with an aqueous solution containing activated iron is referred to as Comparative Example 1. As shown in Fig. 7, the conventional fuel processing container (2), which was densely packed, was used as Comparative Example 2.
- Comparative Example 2 in which the fuel treatment material A treated with the activated iron-containing aqueous solution was densely packed, the fuel efficiency was improved as compared with Comparative Example 1, but the fuel efficiency improvement effect of each embodiment of the present invention. Did not reach.
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Compounds Of Iron (AREA)
- Liquid Carbonaceous Fuels (AREA)
Description
Claims
Priority Applications (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE69529449T DE69529449T2 (de) | 1994-04-06 | 1995-04-06 | Brennstoffbehandlungsvorrichtung |
AU21480/95A AU2148095A (en) | 1994-04-06 | 1995-04-06 | Fuel treatment device |
EP95914537A EP0708237B1 (en) | 1994-04-06 | 1995-04-06 | Fuel treatment device |
US08/556,975 US5695531A (en) | 1994-04-06 | 1995-04-06 | Fuel treating device |
KR1019950705498A KR960702887A (ko) | 1994-04-06 | 1995-04-06 | 연료처리장치(fuel treatment device) |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9366594A JPH07224730A (ja) | 1993-12-15 | 1994-04-06 | 燃料処理装置 |
JP6/93665 | 1994-04-06 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1995027849A1 true WO1995027849A1 (fr) | 1995-10-19 |
Family
ID=14088703
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/JP1995/000684 WO1995027849A1 (fr) | 1994-04-06 | 1995-04-06 | Dispositif de traitement de combustibles |
Country Status (7)
Country | Link |
---|---|
US (1) | US5695531A (ja) |
EP (1) | EP0708237B1 (ja) |
KR (1) | KR960702887A (ja) |
AU (1) | AU2148095A (ja) |
DE (1) | DE69529449T2 (ja) |
TW (1) | TW314573B (ja) |
WO (1) | WO1995027849A1 (ja) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0791745A1 (en) * | 1996-02-23 | 1997-08-27 | Nobuyoshi Nishikawa | Method of reforming fuel, fuel-reforming apparatus and thermal engine |
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JP3582709B2 (ja) * | 2000-02-16 | 2004-10-27 | 基成 小山 | 燃焼促進装置 |
US6203586B1 (en) * | 2000-01-12 | 2001-03-20 | John W. Davis | Fire enhancement system |
US6623636B2 (en) * | 2000-05-08 | 2003-09-23 | Honeywell International Inc. | Staged oil filter incorporating timed release oil conditioner |
CA2408880A1 (en) | 2000-05-08 | 2001-11-15 | Ronald P. Rohrbach | Staged oil filter incorporating pelletized basic conditioner |
US6827750B2 (en) * | 2001-08-24 | 2004-12-07 | Dober Chemical Corp | Controlled release additives in fuel systems |
US6835218B1 (en) | 2001-08-24 | 2004-12-28 | Dober Chemical Corp. | Fuel additive compositions |
AU2002323231B2 (en) | 2001-08-24 | 2008-01-31 | Cummins Filtration Inc. | Controlled release of additives in fluid systems |
US7938277B2 (en) | 2001-08-24 | 2011-05-10 | Dober Chemical Corporation | Controlled release of microbiocides |
US7384896B2 (en) * | 2002-07-16 | 2008-06-10 | The Lubrizol Corporation | Controlled release of additive gel(s) for functional fluids |
US6843916B2 (en) * | 2002-07-16 | 2005-01-18 | The Lubrizol Corporation | Slow release lubricant additives gel |
PL373253A1 (en) * | 2002-08-01 | 2005-08-22 | Briggs & Stratton Corporation | Drip feed apparatus for a fuel container |
US6981532B2 (en) * | 2002-08-01 | 2006-01-03 | Briggs & Stratton Corporation | Drip feed apparatus for a fuel container |
US7534747B2 (en) * | 2003-06-25 | 2009-05-19 | The Lubrizol Corporation | Gels that reduce soot and/or emissions from engines |
US7563368B2 (en) | 2006-12-12 | 2009-07-21 | Cummins Filtration Ip Inc. | Filtration device with releasable additive |
US8022021B2 (en) * | 2007-02-05 | 2011-09-20 | The Lubrizol Corporation | Low ash controlled release gels |
US8591747B2 (en) | 2008-05-27 | 2013-11-26 | Dober Chemical Corp. | Devices and methods for controlled release of additive compositions |
US7883638B2 (en) | 2008-05-27 | 2011-02-08 | Dober Chemical Corporation | Controlled release cooling additive compositions |
US8702995B2 (en) | 2008-05-27 | 2014-04-22 | Dober Chemical Corp. | Controlled release of microbiocides |
US20090294379A1 (en) * | 2008-05-27 | 2009-12-03 | Dober Chemical Corporation | Controlled release of additive compositions |
MX2019013783A (es) * | 2019-11-19 | 2021-05-20 | Carey Gipson | Dispositivo para el tratamiento de combustible. |
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US5059217A (en) * | 1990-10-10 | 1991-10-22 | Arroyo Melvin L | Fluid treating device |
DE4129408C1 (ja) * | 1991-09-04 | 1992-10-22 | Chemische Betriebe Pluto Gmbh, 4690 Herne, De | |
US5305725A (en) * | 1992-09-11 | 1994-04-26 | Marlow John R | Method and apparatus for treating fuel |
-
1995
- 1995-04-06 EP EP95914537A patent/EP0708237B1/en not_active Expired - Lifetime
- 1995-04-06 DE DE69529449T patent/DE69529449T2/de not_active Expired - Fee Related
- 1995-04-06 KR KR1019950705498A patent/KR960702887A/ko not_active Application Discontinuation
- 1995-04-06 US US08/556,975 patent/US5695531A/en not_active Expired - Fee Related
- 1995-04-06 AU AU21480/95A patent/AU2148095A/en not_active Abandoned
- 1995-04-06 WO PCT/JP1995/000684 patent/WO1995027849A1/ja active IP Right Grant
- 1995-05-19 TW TW084104967A patent/TW314573B/zh active
Patent Citations (5)
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JPS59160847U (ja) * | 1983-04-14 | 1984-10-27 | 弘保 亘 | 燃料油の磁化装置 |
JPH01116275A (ja) * | 1987-10-28 | 1989-05-09 | Kenji Yakura | 燃料処理方法およびその燃料処理装置 |
JPH03213653A (ja) * | 1990-01-19 | 1991-09-19 | Nissho Rajiekoo Kk | 燃焼機関の燃費向上方法 |
JPH0499289A (ja) * | 1990-08-08 | 1992-03-31 | Sumitomo Metal Ind Ltd | エッチング方法 |
JPH062622A (ja) * | 1992-06-18 | 1994-01-11 | Mamoru Miyano | 炭化水素系燃料の高燃焼化処理装置 |
Non-Patent Citations (1)
Title |
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See also references of EP0708237A4 * |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0791745A1 (en) * | 1996-02-23 | 1997-08-27 | Nobuyoshi Nishikawa | Method of reforming fuel, fuel-reforming apparatus and thermal engine |
Also Published As
Publication number | Publication date |
---|---|
US5695531A (en) | 1997-12-09 |
EP0708237A1 (en) | 1996-04-24 |
KR960702887A (ko) | 1996-05-23 |
TW314573B (ja) | 1997-09-01 |
AU2148095A (en) | 1995-10-30 |
DE69529449D1 (de) | 2003-02-27 |
EP0708237B1 (en) | 2003-01-22 |
DE69529449T2 (de) | 2003-10-23 |
EP0708237A4 (en) | 1997-12-29 |
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