US1379077A - Process and apparatus for generating explosive gases - Google Patents
Process and apparatus for generating explosive gases Download PDFInfo
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- US1379077A US1379077A US388180A US38818020A US1379077A US 1379077 A US1379077 A US 1379077A US 388180 A US388180 A US 388180A US 38818020 A US38818020 A US 38818020A US 1379077 A US1379077 A US 1379077A
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- fuel
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- hydrogen
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- 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
- C10L3/00—Gaseous fuels; Natural gas; Synthetic natural gas obtained by processes not covered by subclass C10G, C10K; Liquefied petroleum gas
-
- 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
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S123/00—Internal-combustion engines
- Y10S123/12—Hydrogen
Definitions
- My invention relates to a process and apparatus for generating combustible gases especially adapted for internal combustion en ines.
- ttempts have been made to use the heavier grades of hydrocarbon fuel, such as engine distillate, kerosene, and the like, but their use is invariably accompanied by the excessive deposit of carbon in the engine. Furthermore, varying amounts of the heavy hydrocarbon fuels are condensed in the explosive chamber and find their way into the lubricating oil in the crank case, which is objectionable.
- hydrocarbon fuel such as engine distillate, kerosene, and the like
- heavy hydrocarbon fuels such as distillate, kerosene, and the like
- My invention consists in the steps of the process and the apparatus for carrying out my process hereinafter described and claimed.
- Fi ure 1 is a sectional view of an automobile aving parts broken away to show the application of my invention to the fuel gaseous vapor producing apparatus of the engine.
- Fig. 2 is a cross sectional view of the apparatus proper for treating the heavy hy drocarbon fuel, shown connected to the carbureter and other parts of the engine.
- 1 indicates a carbureter of any suitable type connected with a pipe line 2 leading to a heavy fuel tank, shown in dotted lines at 3; 3 and 6 are valves in pipe line 2; 4 is a closed vessel for the reception of a heavy hydrocarbon 'fuel 5 such as engine distillate or kerosene.
- a heavy hydrocarbon 'fuel 5 such as engine distillate or kerosene.
- the filllng pipe 7 is used for introducing a suitable quantity of an electrolyte such as a solution 8, either acid, alkaline or neutral.
- an electrolyte such as a solution 8
- the electrolyte employed may be ammonium nitrate.
- the electrolyte is for use in generating hydrogen and oxygen which passes through the supernatant layer 5 of the heavy fuel.
- Electrodes 9 and 10 horizontally disposed and slightly spaced from each other within the electrolyte 8 are connected to the positive and negative poles 11 and 12, respectively, which, in turn, are connected to a storage battery 13, or any other source of electric energy, by means of conductors 35.
- the current from the storage battery leading to the electrodes 9 and 10 may be controlled by a switch conveniently arranged on the dash board 15 within reach of the operator.
- 16 and 17 are supports for the outer ends of the electrodes 9 and 10, respectively.
- a pi e 18 leads from the upper part of the vesse 4 to the intake manifold 19 conducting the gaseous fuel to the explosion chambers.
- The'pipe 18 is controlled by means of a valve 20 operated by a rod 21 passin through the dash board 15 and provided wit an operating handle 22.
- Another pipe 23 leads from the layer of heavy fuel to the pipe line 2, joining the same between valves 3 and 6, and is provided with a valve 34.
- a suitable electrolyte as above referred to, is in troduced through the funnel-shaped pipe 7 of a quantity suflicient to cover the electrodes 9 and 10, then the heavy fuel as above referred to is introduced, and being lighter than the electrolyte will form a supernatant layer thereon.
- he valve 3 in pipe line 2 is closed.
- the switch 14 current is passed between the electrodes 9 and 10, the upper electrode 10 being shown as provided with perforations 10 to evenly distribute the gases enerated, which will pass upwardly througl i should be noted that the gases thus generated are in statu nascendz' and are therefore especially active in effecting chemical reactions.
- Kerosene for instance will absorb as much as 65 volumes of hydrogen to 100 volumes of kerosene at ordinar temperatures.
- the excess of hydrogen will pass through pipe 18 to the manifold 19 and will give an exceedingly explosive gaseous mixture excellent for starting in the coldest weather.
- the gaseous mixture of ox gen and hydrogen will contain vapors 0 light hydrocarbons which are formed by the reaction of the hydrogen durin its passage through the heavy fuel 5.
- the physical qualities of the heavy fuel are changed, due to the absorption of large volumes of hydrogen, lowering its specific gravity and making the same more volatile within the carbureter. Furthermore, chemical changes take place, the hydrogen reacting with the hydrocarbons and producing the lower more volatile members of the hydrocarbon series.
- valve 6 When it is desired to replenish the supply of heavy fuel the valve 6 is closed and valve 3 is opened, allowing the fuel from the supply tank (not shown) to flow into the vessel 4, and by closing the valve 3 and opening the valve 6 the apparatus is again in normal working condition, the electrolyte being from time to time replenished through the filler pipe 7.
- electrolyte may be introduced by other convenient means or provision ma be made for keeping the vessel 4 filled with electrolyte and heavy fuel by means of float chamber devices, as will be understood.
- a process of producing a gaseous fuel mixture comprising treating heavy hydrocarbons with hydrogen by passing a mixture of hydrogen and oxygen electrolytically generated through the body of the heavy hydrocarbons.
- An apparatus for producing a gaseous fuel vapor comprising a closed tank, means at the bottom of the tank for generating electrolytically evolved hydrogen and oxygen, means under the control of the operator for controlling said electrolytic means, a passage leading from said tank to the manifold of an internal combustion engine, means under the control of the operator for controlling said passage, and another passage leading from said tank for conducting hydrocarbons to the carbureter.
- An apparatus for producing a gaseous fuel vapor comprising a closed tank; a pair of horizontally disposed electrodes in the bottom of said tank, the upper of said electrodes being perforated, a source of electricity connected to said electrodes, means for controlling said source of electricity, a. conduit leading from the upper part of said tank for conducting off the gases and vapors a conduit leading from a point intermediate the top and bottom of said tank to conduct liquid fuel, means for supplying a hydrocarbon to said tank, and means for supplying an electrolyte to cover sald electrodes.
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- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Output Control And Ontrol Of Special Type Engine (AREA)
Description
H. BLUMENBERG, JR.
PROCESS AND APPARATUS FOR GENERATING E XPLOSIVE GASES.
APPLICATION FILED JUNE 11. 1920.
l ,37 9 ,077. Patented May 24, 1921.
I N VEN TOR. Hen ry B/umenb erg J71 UNITED STATES HENRY BLUMENBERG, JR.,
OF DAGGETT, CALIFORNIA.
PROCESS AND APPARATUS FOR GE1 T ERATING EXPLOSIVIl GASES.
Specification of Letters Patent.
Patented May 24, 1921.
Application filed June 11, 1920. Serial No. 388,180;
To all whom it may concern):
Be it known that I, HENRY BLUMENBERG, Jr., a citizen of the United States, residing at Daggett, in the county of San Bernardino and State of California, have invented new and useful Improvements in Processes and Apparatus for Generating Explosive Gases, of which the following is a specification.
My invention relates to a process and apparatus for generating combustible gases especially adapted for internal combustion en ines.
ttempts have been made to use the heavier grades of hydrocarbon fuel, such as engine distillate, kerosene, and the like, but their use is invariably accompanied by the excessive deposit of carbon in the engine. Furthermore, varying amounts of the heavy hydrocarbon fuels are condensed in the explosive chamber and find their way into the lubricating oil in the crank case, which is objectionable.
It is an object of this invention to use heavy hydrocarbon fuels such as distillate, kerosene, and the like, but to modify the same in a manner to avoid the deposit of carbon within the engine, at the same time generating a gaseous fuel which is easily exploded and compares Well with the fuel produced by the best grade of gasolene.
I have attained this object by passing electrolytically generated gases, hydrogen and oxygen, through a heavy fuel, whereby the heavy fuel is physically modified by the solution of a large volume of hydrogen, which subsequently facilitates the vaporlzation and adds to the explosive qualities of the gaseous vapor and also directly modifies the chemical composition of the heavy fuel itself by the chemical reaction taking place between the fuel and the electrolytically generated gases.
My invention consists in the steps of the process and the apparatus for carrying out my process hereinafter described and claimed.
In the accompanying drawings which form a part of this specification,
Fi ure 1 is a sectional view of an automobile aving parts broken away to show the application of my invention to the fuel gaseous vapor producing apparatus of the engine.
Fig. 2 is a cross sectional view of the apparatus proper for treating the heavy hy drocarbon fuel, shown connected to the carbureter and other parts of the engine.
Referring to the drawings, 1 indicates a carbureter of any suitable type connected with a pipe line 2 leading to a heavy fuel tank, shown in dotted lines at 3; 3 and 6 are valves in pipe line 2; 4 is a closed vessel for the reception of a heavy hydrocarbon 'fuel 5 such as engine distillate or kerosene.
7 is a funnel-shaped fillin pi e passin through the top of the vessel 1, the lowe f end of said filling pipe 7 being spaced from the bottom thereof. The filllng pipe 7 is used for introducing a suitable quantity of an electrolyte such as a solution 8, either acid, alkaline or neutral. In practice the electrolyte employed may be ammonium nitrate. The electrolyte is for use in generating hydrogen and oxygen which passes through the supernatant layer 5 of the heavy fuel. Electrodes 9 and 10 horizontally disposed and slightly spaced from each other within the electrolyte 8 are connected to the positive and negative poles 11 and 12, respectively, which, in turn, are connected to a storage battery 13, or any other source of electric energy, by means of conductors 35. The current from the storage battery leading to the electrodes 9 and 10 may be controlled by a switch conveniently arranged on the dash board 15 within reach of the operator. 16 and 17 are supports for the outer ends of the electrodes 9 and 10, respectively. A pi e 18 leads from the upper part of the vesse 4 to the intake manifold 19 conducting the gaseous fuel to the explosion chambers. The'pipe 18 is controlled by means of a valve 20 operated by a rod 21 passin through the dash board 15 and provided wit an operating handle 22. Another pipe 23 leads from the layer of heavy fuel to the pipe line 2, joining the same between valves 3 and 6, and is provided with a valve 34.
In the operation of my apparatus a suitable electrolyte, as above referred to, is in troduced through the funnel-shaped pipe 7 of a quantity suflicient to cover the electrodes 9 and 10, then the heavy fuel as above referred to is introduced, and being lighter than the electrolyte will form a supernatant layer thereon. he valve 3 in pipe line 2 is closed. By closing the switch 14 current is passed between the electrodes 9 and 10, the upper electrode 10 being shown as provided with perforations 10 to evenly distribute the gases enerated, which will pass upwardly througl i should be noted that the gases thus generated are in statu nascendz' and are therefore especially active in effecting chemical reactions.
The heavy fuel will dissolve large quantities of hydrogen and varying quantities of oxygen. Kerosene for instance will absorb as much as 65 volumes of hydrogen to 100 volumes of kerosene at ordinar temperatures. The excess of hydrogen will pass through pipe 18 to the manifold 19 and will give an exceedingly explosive gaseous mixture excellent for starting in the coldest weather.
The gaseous mixture of ox gen and hydrogen will contain vapors 0 light hydrocarbons which are formed by the reaction of the hydrogen durin its passage through the heavy fuel 5. The physical qualities of the heavy fuel are changed, due to the absorption of large volumes of hydrogen, lowering its specific gravity and making the same more volatile within the carbureter. Furthermore, chemical changes take place, the hydrogen reacting with the hydrocarbons and producing the lower more volatile members of the hydrocarbon series.
When it is desired to replenish the supply of heavy fuel the valve 6 is closed and valve 3 is opened, allowing the fuel from the supply tank (not shown) to flow into the vessel 4, and by closing the valve 3 and opening the valve 6 the apparatus is again in normal working condition, the electrolyte being from time to time replenished through the filler pipe 7. It will be understood that electrolyte may be introduced by other convenient means or provision ma be made for keeping the vessel 4 filled with electrolyte and heavy fuel by means of float chamber devices, as will be understood.
By my treatment of the heavy fuel, as explained above, I may utilize t e grades of fuel which at the present time are unsuitthe heavy fuel 5. Itv
able for internal combustion engines for motor vehicles, by producin a gaseous fuel mixture which is highly exp osive and which does not deposit carbon in the combustion chamber.
Various changes may be made without departing from the spirit of the invention as claimed.
What is claimed is:
1. A process of producing a gaseous fuel mixture, comprising treating heavy hydrocarbons with hydrogen by passing a mixture of hydrogen and oxygen electrolytically generated through the body of the heavy hydrocarbons.
2. An apparatus for producing a gaseous fuel vapor, comprising a closed tank, means at the bottom of the tank for generating electrolytically evolved hydrogen and oxygen, means under the control of the operator for controlling said electrolytic means, a passage leading from said tank to the manifold of an internal combustion engine, means under the control of the operator for controlling said passage, and another passage leading from said tank for conducting hydrocarbons to the carbureter.
3. An apparatus for producing a gaseous fuel vapor, comprising a closed tank; a pair of horizontally disposed electrodes in the bottom of said tank, the upper of said electrodes being perforated, a source of electricity connected to said electrodes, means for controlling said source of electricity, a. conduit leading from the upper part of said tank for conducting off the gases and vapors a conduit leading from a point intermediate the top and bottom of said tank to conduct liquid fuel, means for supplying a hydrocarbon to said tank, and means for supplying an electrolyte to cover sald electrodes.
In testimony whereof I have signed my name to this specification.
HENRY BLUMENBERG, JR.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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US388180A US1379077A (en) | 1920-06-11 | 1920-06-11 | Process and apparatus for generating explosive gases |
Applications Claiming Priority (1)
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US388180A US1379077A (en) | 1920-06-11 | 1920-06-11 | Process and apparatus for generating explosive gases |
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Cited By (25)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2509498A (en) * | 1944-11-28 | 1950-05-30 | Heyl George Edward | Electrolytic charge forming device |
US2686153A (en) * | 1952-06-30 | 1954-08-10 | Harry S Hoenes | Apparatus for generating hydrogen and oxygen |
US4011843A (en) * | 1975-02-27 | 1977-03-15 | Feuerman Arnold I | Vaporized fuel for internal combustion engine and method and apparatus for producing same |
US4017268A (en) * | 1975-02-12 | 1977-04-12 | Gilley E Gene | Hydrocarbon fuel containing dispersed hydrogen and method of use thereof |
FR2383315A1 (en) * | 1977-03-07 | 1978-10-06 | Feuerman Arnold | Vaporised fuel for IC engine - has source of electrolytically conductive water hydrocarbon emulsion and of electric current |
US4133847A (en) * | 1975-02-27 | 1979-01-09 | Feuerman Arnold I | Vaporized fuel for internal combustion engine and method and apparatus for producing same |
US4233132A (en) * | 1979-03-19 | 1980-11-11 | Randall Carr | Method and apparatus for producing hydrogen |
US4246082A (en) * | 1975-02-27 | 1981-01-20 | Feuerman Arnold I | Method for producing vaporized fuel for internal combustion engine |
US4361474A (en) * | 1981-01-12 | 1982-11-30 | George Shoaf | Electrolysis chamber for hybrid fuel system |
US4442801A (en) * | 1981-12-16 | 1984-04-17 | Glynn John D | Electrolysis fuel supplementation apparatus for combustion engines |
US5139002A (en) * | 1990-10-30 | 1992-08-18 | Hydrogen Consultants, Inc. | Special purpose blends of hydrogen and natural gas |
USRE35237E (en) * | 1989-11-22 | 1996-05-14 | Gunnerman Rudolf W | Aqueous fuel for internal combustion engine and method of combustion |
US6302929B1 (en) | 1994-04-04 | 2001-10-16 | Rudolf W. Gunnerman | Aqueous fuel for internal combustion engine and method of preparing |
US20070080070A1 (en) * | 2001-04-04 | 2007-04-12 | Klein Dennis J | Apparatus and method for the conversion of water into a new gaseous and combustible form and the combustible gas formed thereby |
US7357102B1 (en) * | 2006-11-02 | 2008-04-15 | Wen-Chang Lin | System for generating hybrid fuel for a combustion engine |
DE202008002304U1 (en) | 2008-02-20 | 2008-07-17 | Lin, Wen Chang, Lin-Yuan Hsiang | Engine device for a hydrogen vehicle |
US20080190383A1 (en) * | 2007-02-09 | 2008-08-14 | Wen-Chang Lin | Engine device for an oxyhydrogen vehicle |
US20080296173A1 (en) * | 2007-05-29 | 2008-12-04 | Transphorm, Inc. | Electrolysis transistor |
US20090145771A1 (en) * | 2007-08-28 | 2009-06-11 | Transphorm, Inc. | Compact electric appliance for providing gas for combustion |
US20090288947A1 (en) * | 2008-05-22 | 2009-11-26 | Ostgaard John T | Hydrogen generator system |
US20100132634A1 (en) * | 2008-12-01 | 2010-06-03 | Jeff Selano | Electronic System for an Internal Combustion Engine |
US20100206646A1 (en) * | 2009-02-13 | 2010-08-19 | Yu Chuan Technology Enterprise Co., Ltd. | Oxyhydrogen vehicle |
WO2011124872A1 (en) * | 2010-04-08 | 2011-10-13 | Advanced Fuel Technologies Uk Limited | Fuel enrichment method and device |
US20120111734A1 (en) * | 2012-01-19 | 2012-05-10 | Edward Kramer | Water Electrolyzer System and Method |
US20120199472A1 (en) * | 2011-02-03 | 2012-08-09 | Dan Curfew | System and method for electrolyzing water |
-
1920
- 1920-06-11 US US388180A patent/US1379077A/en not_active Expired - Lifetime
Cited By (32)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2509498A (en) * | 1944-11-28 | 1950-05-30 | Heyl George Edward | Electrolytic charge forming device |
US2686153A (en) * | 1952-06-30 | 1954-08-10 | Harry S Hoenes | Apparatus for generating hydrogen and oxygen |
US4017268A (en) * | 1975-02-12 | 1977-04-12 | Gilley E Gene | Hydrocarbon fuel containing dispersed hydrogen and method of use thereof |
US4011843A (en) * | 1975-02-27 | 1977-03-15 | Feuerman Arnold I | Vaporized fuel for internal combustion engine and method and apparatus for producing same |
US4133847A (en) * | 1975-02-27 | 1979-01-09 | Feuerman Arnold I | Vaporized fuel for internal combustion engine and method and apparatus for producing same |
US4246082A (en) * | 1975-02-27 | 1981-01-20 | Feuerman Arnold I | Method for producing vaporized fuel for internal combustion engine |
FR2383315A1 (en) * | 1977-03-07 | 1978-10-06 | Feuerman Arnold | Vaporised fuel for IC engine - has source of electrolytically conductive water hydrocarbon emulsion and of electric current |
US4233132A (en) * | 1979-03-19 | 1980-11-11 | Randall Carr | Method and apparatus for producing hydrogen |
US4361474A (en) * | 1981-01-12 | 1982-11-30 | George Shoaf | Electrolysis chamber for hybrid fuel system |
US4442801A (en) * | 1981-12-16 | 1984-04-17 | Glynn John D | Electrolysis fuel supplementation apparatus for combustion engines |
USRE35237E (en) * | 1989-11-22 | 1996-05-14 | Gunnerman Rudolf W | Aqueous fuel for internal combustion engine and method of combustion |
US5139002A (en) * | 1990-10-30 | 1992-08-18 | Hydrogen Consultants, Inc. | Special purpose blends of hydrogen and natural gas |
US6302929B1 (en) | 1994-04-04 | 2001-10-16 | Rudolf W. Gunnerman | Aqueous fuel for internal combustion engine and method of preparing |
US20070080070A1 (en) * | 2001-04-04 | 2007-04-12 | Klein Dennis J | Apparatus and method for the conversion of water into a new gaseous and combustible form and the combustible gas formed thereby |
US7357102B1 (en) * | 2006-11-02 | 2008-04-15 | Wen-Chang Lin | System for generating hybrid fuel for a combustion engine |
US20080105218A1 (en) * | 2006-11-02 | 2008-05-08 | Wen-Chang Lin | System for generating hybrid fuel for a combustion engine |
US7654233B2 (en) | 2007-02-09 | 2010-02-02 | Wen-Chang Lin | Engine device for an oxyhydrogen vehicle |
US20080190383A1 (en) * | 2007-02-09 | 2008-08-14 | Wen-Chang Lin | Engine device for an oxyhydrogen vehicle |
US20080296173A1 (en) * | 2007-05-29 | 2008-12-04 | Transphorm, Inc. | Electrolysis transistor |
US9096939B2 (en) | 2007-05-29 | 2015-08-04 | Transphorm, Inc. | Electrolysis transistor |
US20090145771A1 (en) * | 2007-08-28 | 2009-06-11 | Transphorm, Inc. | Compact electric appliance for providing gas for combustion |
DE202008002304U1 (en) | 2008-02-20 | 2008-07-17 | Lin, Wen Chang, Lin-Yuan Hsiang | Engine device for a hydrogen vehicle |
US20090288947A1 (en) * | 2008-05-22 | 2009-11-26 | Ostgaard John T | Hydrogen generator system |
US20100132634A1 (en) * | 2008-12-01 | 2010-06-03 | Jeff Selano | Electronic System for an Internal Combustion Engine |
US20100206646A1 (en) * | 2009-02-13 | 2010-08-19 | Yu Chuan Technology Enterprise Co., Ltd. | Oxyhydrogen vehicle |
US8109354B2 (en) * | 2009-02-13 | 2012-02-07 | Yu Chuan Technology Enterprise Co., Ltd. | Oxyhydrogen vehicle |
WO2011124872A1 (en) * | 2010-04-08 | 2011-10-13 | Advanced Fuel Technologies Uk Limited | Fuel enrichment method and device |
US10016731B2 (en) | 2010-04-08 | 2018-07-10 | Advanced Fuel Technologies Uk Limited | Fuel enrichment method and device |
EA031847B1 (en) * | 2010-04-08 | 2019-03-29 | ЭДВАНСТ ФЬЮЭЛ ТЕКНОЛОДЖИЗ ЮКей ЛИМИТЕД | Fuel enrichment method and device |
US10695727B2 (en) | 2010-04-08 | 2020-06-30 | Advanced Fuel Technologies Uk Limited | Fuel enrichment method and device |
US20120199472A1 (en) * | 2011-02-03 | 2012-08-09 | Dan Curfew | System and method for electrolyzing water |
US20120111734A1 (en) * | 2012-01-19 | 2012-05-10 | Edward Kramer | Water Electrolyzer System and Method |
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