WO1995005665A1 - Process for reducing pollution in energy production - Google Patents
Process for reducing pollution in energy production Download PDFInfo
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- WO1995005665A1 WO1995005665A1 PCT/US1994/009125 US9409125W WO9505665A1 WO 1995005665 A1 WO1995005665 A1 WO 1995005665A1 US 9409125 W US9409125 W US 9409125W WO 9505665 A1 WO9505665 A1 WO 9505665A1
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- Prior art keywords
- lithium
- fuel
- energy
- approximately
- hydrogen
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- G—PHYSICS
- G21—NUCLEAR PHYSICS; NUCLEAR ENGINEERING
- G21B—FUSION REACTORS
- G21B3/00—Low temperature nuclear fusion reactors, e.g. alleged cold fusion reactors
-
- 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
- Y02E30/00—Energy generation of nuclear origin
- Y02E30/10—Nuclear fusion reactors
Definitions
- Natural-occurring lithium is comprised of approximately 8% Li 6 and 92% li 7 .
- compositions are not likely to be simple catalysts since they are consumed in the reaction. However, a complex set of reactions may be occurring as is typical of high temperature combustion processes whereby catalytic and other mechanisms may be involved.
- Additives comprising as a major species organometallic lithium, lithium acetate, or lithium nitrate have been formulated for use in liquid fuels. Any form of lithium or other alkali metal which can be dispersed into a flame or vapor may be effective.
- the subject invention provides for a process for producing energy which comprises contacting an H- containing substance which is in a fluid phase with a Li- containing substance under conditions such that the reaction
- the subject invention also provides a continuous process for producing energy which comprises continuously introducing into a reaction zone an H-containing substance which is in a fluid phase and a Li-containing substance under conditions such that the H-containing substance contacts the Li-containing substance and the reaction
- Li + H ⁇ 2He * + Energy occurs, and continuously removing from the reaction zone helium and the products of any reactions involving the H- containing substance or Li-containing substance, or both.
- the subject invention further provides a composition which comprises a Li-containing substance and an H- containing substance, wherein the lithium in the Li- containing substance is present in molar excess to the hydrogen in the H-containing substance.
- the subject invention also provides a composition which comprises a Li-containing substance and an H-containing substance, wherein the hydrogen in the H-containing substance is present in molar excess to the lithium in the Li- containing substance.
- the subject invention provides a method of increasing the energy output of a process which comprises contacting an H-containing substance which is in a fluid phase with a Li-containing substance under conditions such that the reaction
- Li + H ⁇ 2He * + Energy occurs in conjunction with the process, thereby increasing the energy output of the process.
- the subject invention additionally provides a method of increasing the efficiency of a process which comprises contacting an H-containing substance which is in the fluid phase with a Li-containing substance under conditions such that the reaction
- Li + H ⁇ 2He * + Energy occurs in conjunction with the process, thereby increasing the efficiency of the process.
- the subject invention provides a method for reducing emissions of CO or C0 2 from, while maintaining the amount of energy produced by, a continuous process for producing energy which normally emits CO or CO 2 which comprises continuously introducing into a reaction zone in which such a continuous process is being carried out an H- containing substance which is in the fluid phase and a Li-containing substance under conditions such that the H- containing substance contacts the Li-containing substance and the reaction Li + H ⁇ 2He * + Energy occurs, and continuously removing from the reaction zone helium and the products of any reactions involving the H- containing substance or Li-containing substance, or both, thereby reducing the emissions of CO or C0 2 from such process while maintaining the amount of energy produced thereby.
- the subject invention provides a process for reducing pollution in fuel combustion, which comprises forming a reaction zone containing the fuel in vapor phase, contacting the fuel with a lithium salt in vapor phase and oxygen, and imparting energy to the reaction zone sufficient to initiate the energy-producing process by means of an electrical spark possessing electrostatic energy of at least about 13,000 eV, a thermal energy source, or particles from a source of radioactive decay.
- the subject invention further provides a process for reducing pollution in fuel combustion, which comprises forming a reaction zone comprising the fuel in vapor phase, contacting the fuel with an organolithium compound in vapor phase and oxygen, and imparting energy to the reaction zone sufficient to initiate the energy-producing process by means of an electrical spark possessing electrostatic energy of at least about 13,000 eV, a thermal energy source, or particles from a source of radioactive decay.
- the subject invention further provides a process for reducing pollution in fuel combustion, which comprises forming a reaction zone comprising the fuel in vapor phase, contacting the fuel with an organolithium compound in vapor phase and oxygen, and imparting energy to the reaction zone sufficient to initiate the energy-producing process by means of an electrical spark possessing elec ⁇ trostatic energy of at least about 13,000 eV, a thermal energy source, or particles from a source of radioactive decay, wherein the fuel contains a polar substance.
- the invention also provides a composition useful for reducing pollution and increasing fuel efficiency in fuel combustion which comprises a mixture of a lithium salt and isopropyl alcohol.
- This invention further provides a process for reducing pollution in fuel combustion, which comprises forming a reaction zone containing a composition comprising indolene, ethanol and a mixture of lithium salt and isopropyl alcohol, and imparting energy to the reaction zone sufficient to initiate the energy-producing process by means of an electrical spark possessing electrostatic energy of at least about 13,000 eV, a thermal energy source, or particles from a source of radioactive decay.
- the invention provides a process for increasing fuel efficiency in fuel combustion, which comprises forming a reaction zone containing a composition comprising indolene, ethanol and a mixture of lithium salt and isopropyl alcohol, and imparting energy to the reaction zone sufficient to initiate the energy-producing process by means of an electrical spark possessing electrostatic energy of at least about 13,000 eV, a thermal energy source, or particles from a source of radioactive decay.
- Fig. 1 is a top view of a burner and electrode apparatus used in the combustion process.
- Fig. 2 is a graph of the normal clean Input-Output and Heat-Loss Efficiencies for the boiler used to activate and measure energy production levels.
- Fig. 3 shows the effect of a lithium acetate composition on energy output in boiler combustion.
- Fig. 4 shows the effect of a lithium nitrate composition on energy output in boiler combustion.
- Fig. 5 shows the effect of a lithium stearate composition on energy output in boiler combustion.
- Fig. 6 shows the effect of residual lithium compositions on energy output in boiler combustion.
- Fig. 7 shows the effect of introducing lithium compositions into the combustion process on nitrogen oxides levels in boiler exhausts.
- Fig. 8 shows the effect of introducing lithium compositions into the combustion process on carbon monoxide levels in boiler exhausts.
- Fig. 9 is a side view of the bench apparatus used to produce and measure high energy particles produced by combustion in the presence of lithium salts in a flame front.
- Fig. 9a is a top view of the apparatus used to produce and measure high energy particle produced by combustion in the presence of lithium salts in a flame front.
- Fig. 10 is a diagram of an apparatus incorporating a computerized detection and measurement system used to produce and measure high energy particle produced in a flame front.
- Fig. 11 is a diagram of an apparatus incorporating a computerized system used to produce and measure high energy alpha particles produced by the process of the invention in a vapor cloud.
- Fig. 12 shows the effect of shielding with a sheet of paper on the production of alpha particles in the process of the invention.
- Fig. 13 shows the effect of a composition of lithium nitrate on levels of carbon monoxide, hydrocarbons and nitrogen oxides during a dynamometer test of a 4-cylinder internal combustion engine.
- Fig. 14 shows the effect of a composition of lithium nitrate on the amount of fuel needed to maintain a constant power output during a dynamometer test of a 4- cylinder internal combustion engine.
- Fig. 15 shows measurements of oxygen in the exhaust gases during a dynamometer test of a 4-cylinder internal combustion engine using a composition of lithium nitrate.
- Fig. 16 shows measurements of nitrogen oxides in exhaust gases during a dynamometer test of a 4-cylinder internal combustion engine using a composition of lithium nitrate.
- Fig. 17 shows the effect of various alkali metals on carbon monoxide levels in exhaust gases.
- Fig. 18 shows the percent change from baseline fuel of non-methane hydrocarbons in automobiles with and without emission control devices.
- Fig. 19 shows the percent change from baseline fuel of carbon monoxide emissions in automobiles with and without emission control devices.
- Fig. 20 shows the percent change from baseline fuel of nitrogen oxide emissions in automobiles with and without emission control devices.
- Fig. 21 shows the percent change from baseline fuel in fuel efficiency (in miles per gallon) in automobiles with and without emission control devices.
- the subject invention provides for a process for producing energy which comprises contacting an H- containing substance which is in a fluid phase with a Li- containing substance under conditions such that the reaction
- the exited helium nuclei carry the released energy as kinetic energy and lose it to other species in the flame zone by collision processes. At atmospheric pressures, this occurs within a few centimeters of the original reaction. Most transfers are of the order of a few hundred electron volts, but a direct impact on a lithium or hydrogen atom can transfer sufficient energy to initiate another reaction.
- the H-containing substance may be any H-containing substance useful in an energy producing process.
- the H-containing substance may be any H- containing substance useful in an energy producing process.
- H- containing substance is a fuel, such as, for example, methane ethane, propane, butane, kerosene, crude oil, methanol, ethanol, peat or hydrogen.
- Tables 1-4 fuel and species tables for augmented combustion, are the start of the necessary theory development to define the augmented combustion reaction envelope for application. There are approximations used and values are representative.
- the base includes gases, liquids, and solids. Included are hydrogen, methane through butane, kerosene, distillates No. 2 and 5/6, an a variety of coals from anthracite to peat.
- coals are representative.
- listing of these particular fuels are in no way meant to limit the scope of the application.
- Any compound containing hydrogen or deuterium is contemplated for use in this invention.
- Hydrogen can be used as a fuel.
- the lighter alkanes make good fuels. With some special considerations, alcohols are good fuels. Lighter oil fractions and heavier oil fractions also work well. Solid fuels such as coal and solid waste in most applications require gasification for proper use. This is in part due to ash problems, and in part due to the problems of controlling the composition of the gas phase in the reaction zone.
- the H-containing substance is in a fluid phase, such as a liquid phase or a vapor phase.
- a fluid phase such as a liquid phase or a vapor phase.
- useful vapor phases include flame fronts or rarified vapor phases.
- the H-containing substances may occur naturally in a liquid phase and be converted to the vapor phase.
- both lithium and hydrogen are present in a highly divided form. This permits secondary reactions. While the reaction rates of the basic reaction are of the order of 10 "13 to 10 "12 reactions per energetic hydrogen nucleus, in the vapor phase, by means of secondary reaction, this can be increased by orders of magnitude.
- the Li- containing substance may be a Li 7 -containing substance, such as elemental Li 7 , or a Li 6 -containing substance, or an admixture of a Li 6 -containing, substance and a Li 7 substance, such as a naturally occurring admixture of elemental Li 6 and Li.
- Lithium is the seventh most common element on earth and is in abundant supply. Naturally-occurring lithium is comprised of approximately 92% Li 7 and 8% Li 6 .
- the Li-containing substance may be in the form of a liquid, solid or gas.
- the Li-containing substance may be any Li-containing substance useful in an energy producing process.
- the Li-containing substances is lithium stearate, lithium acetate, lithium nitrate, or lithium amide.
- the lithium in the Li-containing substance may be present in molar excess to the hydrogen in the H-containing substance.
- the molar ratio of hydrogen in the H- containing substance to lithium in the Li-containing substance is less than about 1:10. In another embodiment, the molar ratio of hydrogen in the H- containing substance to lithium in the Li-containing substance is less than about 1:100. In a further embodiment, the molar ratio of hydrogen in the H- containing substance to lithium in the Li-containing substance is between about 1:6,000 and about 1:100.
- the hydrogen in the H-containing substance may be present in molar excess to the lithium in the Li-containing substance.
- the molar ratio of lithium in the Li-containing substance to hydrogen in the H-containing substance is less than about 1:10. In another embodiment, the molar ratio of lithium in the Li- containing substance to hydrogen in the H-containing substance is less than about 1:100. In a further embodiment, the molar ratio of lithium in the Li- containing substance to hydrogen in the H-containing substance is between about 1:6,000 and about 1:100.
- the molar ratio of lithium in the Li-containing substance to hydrogen in the H- containing substance may approach 1:1.
- the lithium-containing material may be intimately mixed with the burner fuel, or introduced in a separate stream in a carrier fluid and atomized into the flame zone.
- reaction may occur under any conditions such that the reaction
- the contacting of the H- containing substance and the Li-containing substance may be effected under conditions such that the kinetic energy of a sufficient amount of the H-containing substance or the Li-containing substance, or both, exceeds about 13,000 eV and thus, the reaction
- These conditions may comprise imparting one or more types of energy to the H-containing substance or the Li- containing substance, or both.
- these types of energy may include, for example, thermal, electromagnetic, radiation or c-radiation energy.
- imparting thermal energy comprises heating the H-containing substance and the Li-containing substance to a temperature of 2700°F.
- imparting electromagnetic energy may comprise subjecting the H-containing substance and the Li- containing substance to an alternating current spark.
- imparting ⁇ -radiation comprises subjecting the H-containing substance and the Li- containing substance to a material containing trace amounts of a substance which emits a-radiation, such as, for example, thorium.
- the a-radiation may be a product of a different transmutation reaction, which said reaction may or may not require the kinetic energy present in the conditions for the reaction of the subject invention.
- different transmutation reactions have been known since the early twentieth century. These additional transmutation reactions may contribute ⁇ _- radiation and high-energy protons during the process, thereby increasing the energy of the system sufficient to initiate the process of the invention.
- the H- containing substance may be in any form useful in an energy producing process.
- the subject invention also provides a continuous process for producing energy which comprises continuously introducing into a reaction zone an H-containing substance which the fluid phase and a Li-containing substance under conditions such that the h-containing substance contacts the Li-containing substance and the reaction
- Li + H — > 2He* + Energy occurs, and continuously removing from the reaction zone helium and the products of any reactions involving the H- containing substance or Li-containing substance.
- the products may be the products of any reactions involving the H- containing substance or the Li-containing substance, or both.
- these products may include CO, C0 2 , H 2 0. or any combination thereof.
- the subject invention further provides a composition which comprises a Li-containing substance and an H- containing substance, wherein the lithium in the Li- containing substance is present in molar excess to the hydrogen in the H-containing substance.
- the molar ratio of the hydrogen in the H- containing substance to lithium in the Li-containing substance is less than about 1:10.
- the molar ratio of hydrogen in the H- containing substance to lithium in the Li-containing substance is less than about 1:100.
- the molar ratio of hydrogen in the H- containing substance to lithium in the Li-containing substance is between about 1:6,000 and about 1:100.
- the subject invention also provides a composition which comprises a Li-containing substance and an H-containing substance, wherein the hydrogen in the H-containing substance is present in molar excess to the lithium in the Li-containing substance.
- the molar ratio of lithium in the Li-containing substance to hydrogen in the H-containing substance is less than about 1:10. In another embodiment, the molar ratio of the H- containing substance is less than about 1:100. In a further embodiment, the molar ratio of lithium in the Li- containing substance to hydrogen in the H-containing substance is between 1:6,000 and about 1:100.
- the H- containing substance of the composition may be a fuel, such as, for example, methane, ethane, propane, butane, kerosene, crude oil, methanol, peat or hydrogen.
- the Li- containing substance may be in the form of a liquid, a solid or a gas. Examples of particular Li-containing substances include lithium stearate, lithium acetate, lithium nitrate, or lithium amide.
- the subject invention provides for a method of increasing the energy output of a process which comprises contacting the H-containing substance which is in a fluid phase with a Li-containing substance under conditions such that the reaction
- the process may be any energy-producing process, such as, for example, a combustion process wherein the H-containing substance is a fuel, or process for the generation of electricity.
- the subject invention additionally provides a method of increasing the efficiency of a process which comprises contacting an H-containing substance which is in a fluid phase with a Li-containing substance under
- Li + H —> 2He* + Energy occurs in conjunction with the process / thereby increasing the efficiency of the process.
- the subject invention provides a method for reducing emissions of CO or C0 2 from, while maintaining the amount of energy produced by, a continuous process for producing energy which normally emits CO or CO- which comprises continuously introducing into a reaction zone in which such a continuous process is being carried out an H-containing substance which is in the fluid phase and a Li-containing substance under conditions such that the H-containing substance contacts the Li- containing substance and the reaction Li + H —> 2He* + Energy occurs, and continuously removing from the reaction zone helium and the products of any reactions involving the H-containing substance or Li-containing substance, or both, thereby reducing the emissions of CO or CO. from such process while maintaining the amount of energy produced thereby.
- the subject invention also provides an apparatus for carrying out a process for producing energy, which process is carried out in a reaction zone, the improvement comprising means for i-. ⁇ Producing into the reaction zone an H-containing substance and a Li- containing substance and means for imparting to the H- containing substance or the Li-containing substance, or both, within the reaction zone, sufficient kinetic energy so that the resulting kinetic energy of the substance or substances exceeds 13,000 eV.
- the apparatus may be any apparatus for the production of energy. Specific examples of an apparatus include a furnce, electric utility, power station, commercial home heating unit, or marine boiler.
- the reaction zone may comprise a composition which comprises a Li- containing substance and an H-containing substance, wherein the lithium in the Li-containing substance is present in molar excess to the hydrogen in the H- containing substance.
- the molar ratio of hydrogen in the H-containing substance to lithium in the Li-containing substance is less than about 1:10. In another embodiment, the molar ratio of hydrogen in the H-containing substance to lithium in the Li-containing substance is less than about 1:100. In a further embodiment, the molar ratio of hydrogen in the H-containing substance to lithium in the Li- containing substance is between about 1:6,000 and about 1:100.
- the reaction zone may comprise a composition which comprises a Li- containing substance and an H-containing substance, wherein the hydrogen in the H-containing substance is present in molar excess to the lithium in the Li- containing substance.
- the molar ratio of lithium in the Li-containing substance to hydrogen in the H-containing substance is less than about 1:10. In another embodiment, the molar ratio of lithium in the Li-containing substance to hydrogen in the H-containing substance is less than about 1:100. In a further embodiment, the molar ratio of lithium in the Li-containing substance to hydrogen in the H- containing substance is between about 1:6,000 and about 1:100.
- the H- containing substance in the reaction zone of the apparatus may be a fuel, such as, for example, methane, ethane, propane, butane, kerosene, crude oil, methanol, ethanol, peat or hydrogen.
- a fuel such as, for example, methane, ethane, propane, butane, kerosene, crude oil, methanol, ethanol, peat or hydrogen.
- the Li- containing substance may be in the form of a liquid, a solid or a gas.
- Li-containing substances include lithium stearate, lithium acetate, lithium nitrate, or lithium amide.
- the subject invention provides a process for reducing pollution in fuel combustion, which comprises forming a reaction zone containing the fuel in vapor phase, contacting the fuel with a lithium salt in vapor phase and oxygen, and imparting energy to the reaction zone sufficient to initiate the energy-producing process by means of an electrical spark possessing electrostatic energy of at least about 13,000 eV, a thermal energy source, or particles from a source of radioactive decay.
- the subject invention provides a process wherein the energy imparted to the reaction zone is an electrical spark possessing electrostatic energy of greater than about 13,000 eV.
- the subject invention provi ⁇ es a process wherein the particles from a source of radioactive decay are ⁇ -particles.
- the subject invention provides a process wherein the energy produced is in excess of that obtainable upon combustion of a hydrogen-containing fuel.
- the subject invention further provides a process wherein the fuel is gasoline, diesel fuel, or coal.
- the subject invention also provides a process wherein the pollution reduced includes carbon monoxide, carbon dioxide, aldehydes, aromatic hydrocarbons, olefinic hydrocarbons, branched and linear chain alkyl hydrocarbons, nitrogen oxides, and sulfur oxides.
- the subject invention provides a process wherein the lithium salt is lithium nitrate, lithium acetate, or lithium amide.
- the subject invention provides a process wherein the energy is produced by means of the reaction
- the subject invention provides a process wherein the lithium in the lithium salt and the hydrogen in the fuel are in a concentration ratio of between about 1:6,000 and about 1:100. In a certain other embodiment, the subject invention provides a process wherein the hydrogen in the fuel is present in molar excess to the lithium in the lithium salt. In another embodiment, the lithium in the lithium salt and the hydrogen in the fuel are in a concentration ratio of less than about 1:10. In yet another embodiment, the subject invention provides a process wherein the lithium in the lithium salt and the hydrogen in the fuel are in a concentration ratio of less than about 1:100. Within the scope of the subject invention is a process wherein the combustion occurs in an internal-combustion or external-combustion engine.
- the subject invention further provides a process for reducing pollution in fuel combustion, which comprises forming a reaction zone comprising the fuel in vapor phase, contacting the fuel with an organolithium compound in vapor phase and oxygen, and imparting energy to the reaction zone sufficient to initiate the energy-producing process by means of an electrical spark possessing electrostatic energy of at least about 13,000 eV, a thermal energy source, or particles from a source of radioactive decay.
- the subject invention provides a process wherein the energy imparted to the reaction zone is an electrical spark.
- the subject invention provides a process wherein the electrical spark possesses electrostatic energies of greater than about 13,000 eV.
- the subject invention provides a process wherein the energy produced is in excess of that obtainable upon combustion of a hydrogen-containing fuel.
- the subject invention also provides a process wherein the fuel is gasoline, diesel fuel, or coal.
- the subject invention provides a process wherein the organolithium compound is liposoluble.
- the organolithium compound is selected from a group comprising lithium stearate, lithium oleate, lithium butyrate, or lithium benzoate.
- the subject invention provides a process wherein the energy is produced by means of the reaction:
- the subject invention provides a process wherein the vapor phase is a flame front.
- the subject invention provides a process wherein wherein the lithium in the lithium salt and the hydrogen in the fuel are in a concentration ratio of between about 1:6,000 and about 1:100.
- the hydrogen in the fuel is present in molar excess relative to the lithium in the organolithium compound.
- the lithium in the lithium salt and the hydrogen in the fuel are in a concentration ratio of less than about 1:10.
- the lithium in the lithium salt and the hydrogen in the fuel are in a concentration ratio of less than about 1:100.
- the combustion occurs in an internal combustion or external combustion engine.
- the subject invention provides a process for reducing pollution in fuel combustion, which comprises forming a reaction zone comprising the fuel in vapor phase, contacting the fuel with an organolithium compound in vapor phase and oxygen, and imparting energy to the reaction zone sufficient to initiate the energy-producing process by means of an electrical spark possessing electrostatic energy of at least about 13,000 eV, a thermal energy source, or particles from a source of radioactive decay, wherein the fuel contains a polar substance.
- the subject invention provides a process wherein the energy imparted to the reaction zone is an electrical spark.
- the subject invention provides a process wherein the electrical spark possesses electrostatic energies of greater than about 13,000 eV.
- the subject invention provides a process wherein the energy produced is in excess of that obtainable upon combustion of a hydrogen-containing fuel.
- the subject invention provides a process wherein the fuel is gasoline, diesel fuel, or coal.
- the subject invention provides a process wherein the pollution reduced includes carbon monoxide, carbon dioxide, aldehydes, aromatic hydrocarbons, olefinic hydrocarbons, branched and linear chain alkyl hydrocarbons, nitrogen oxides, and sulfur oxides.
- the subject invention provides a process wherein the organolithium compound is liposoluble.
- the subject invention provides a process wherein the organolithium compound is selected from a group comprising lithium stearate, lithium oleate, lithium butyrate, or lithium benzoate.
- the subject invention provides a process wherein the energy is produced by means of the reaction: Li + H ⁇ 2He * + Energy.
- the subject invention provides a process wherein the vapor phase is a flame front.
- the subject invention provides a process wherein the lithium in the lithium salt and the hydrogen in the fuel are in a concentration ratio of between about 1:6,000 and about 1:100.
- the hydrogen in the fuel is present in molar excess relative to the lithium in the lithium salt.
- the lithium in the lithium salt and the hydrogen in the fuel are in a concentration ratio of less than about 1:10.
- the lithium in the lithium salt and the hydrogen in the fuel are in a concentration ratio of less than about 1:100.
- the polar substance is an alcohol or ether.
- the alcohol is selected from a group comprising methanol, ethanol, isopropanol, n-butanol, sec-butanol, tert- butanol, and benzyl alcohol.
- the ether is methyl t-butyl ether.
- the invention also provides a composition useful for reducing pollution and increasing fuel effciency in fuel combustion which comprises a mixture of a lithium salt and isopropyl alcohol.
- the lithium salt of the composition is lithium nitrate.
- Other lithium salts which may also be useful in the practice of this invention are known to those skilled in the art and it is anticipated that they are within the coverage of the claims.
- the composition described above comprises approximately 0.1-2.0 g of lithium nitrate and approximately 8-20 g of isopropyl alcohol.
- the composition comprises approximately 0.5-1.5 g of lithium nitrate and approximately 10-15 g of isopropyl alcohol.
- This invention also provides a process for reducing pollution in fuel combustion, which comprises forming a reaction zone containing a composition comprising indolene, ethanol and a mixture of lithium salt and isopropyl alcohol, and imparting energy to the reaction zone sufficient to initiate the energy-producing process by means of an electrical spark possessing electrostatic energy of at least about 13,000 eV, a thermal energy source, or particles from a source of radioactive decay.
- the lithium salt is lithium nitrate.
- Other lithium salts which may also be useful in the practice of this invention are known to those skilled in the art and it is anticipated that they are within the coverage of the claims.
- ethanol is present in an amount of approximately 1-20% by weight of the composition, the mixture contains approximately 0.1-2.0 g of lithium nitrate and 8-20 g of isopropyl alcohol and the mixture is present at a concentration of approximately 1-20 mL/gal of the composition.
- ethanol is present in an amount of approximately 2.5-10% by weight of the composition, the mixture contains approximately 0.5-1.5 g of lithium nitrate and 10-15 g of isopropyl alcohol and the mixture is present at a concentration of approximately 2.5-12 mL/gal of the composition.
- ethanol is present in an amount of approximately 5% by weight of the composition, the mixture contains approximately 1 g of lithium nitrate and approximately 12 g of isopropyl alcohol and the mixture is present at a concentration of approximately 5 mL/gal of the composition.
- the invention provides a process for increasing fuel efficiency in fuel combustion, which comprises forming a reaction zone containing a composition comprising indolene, ethanol and a mixture of lithium salt and isopropyl alcohol, and imparting energy to the reaction zone sufficient to initiate the energy-producing process by means of an electrical spark possessing electrostatic energy of at least about 13,000 eV, a thermal energy source, or particles from a source of radioactive decay.
- the lithium salt is lithium nitrate.
- Other lithium salts which may also be useful in the practice of this invention are known to those skilled in the art and it is anticipated that they are within the coverage of the claims.
- ethanol is present in an amount of approximately 1-20% by weight of the composition, the mixture contains approximately 0.1-2.0 g of lithium nitrate and 8-20 g of isopropyl alcohol and the mixture is present at a concentration of approximately 1-20 mL/gal of the composition.
- ethanol is present in an amount of approximately 2.5-10% by weight of the composition, the mixture contains approximately 0.5-1.5 g of lithium nitrate and 10-15 g of isopropyl alcohol and the mixture is present at a concentration of approximately 2.5-12 mL/gal of the composition.
- ethanol is present in an amount of approximately 5% by weight of the composition, the mixture contains approximately 1 g of lithium nitrate and approximately 12 g of isopropyl alcohol and the mixture is present at a concentration of approximately 5 mL/gal of the composition.
- compositions and processes of increasing fuel efficeincy and for reducing pollution in fuel combustion can be practiced in any type of engine including but not limited to internal combustion, external combustion and jet engines.
- Fig. 1 shows the burner tip and high voltage excitation electrodes used for ignition of the combustion process and excitation voltage for the reaction.
- the inlet/outlet temperatures of the heat exchange section of the boiler were measured with calibrated thermocouple systems.
- the liquid fuel was measured volumetrically, using scientific grade graduated cylinders. Many other parameters such as fuel temperature, ambient air temperature, and combustion zone temperature were measured to assure stable conditions existed.
- the flow of water through the boiler, fuel to the burner, and additive delivery rates were all cross checked using a comput'erized system to insure test conditions were stable and constant.
- the turbine type water flow meter, with a totalizing register, suitable for billing applications, was tested for accuracy, which was better than ⁇ 1%.
- the Higher Heating Values for the fuel was tested by a University engineering department under strict quality assurance procedures.
- I. CLEAN BOILER CALIBRATION Fig. 2 shows the input-output efficiency and the heat loss efficiency for 12 15-minute test runs with absolutely no lithium additive present. The boiler had been thoroughly cleaned and rebuilt with new parts for the cleaning process. For most of the runs the Input- Output efficiency and Heat-Loss efficiency agree within 0.2% except for the first two runs when efficiencies were within ⁇ 0.5%. This test establishes the expected degree of stability and the agreement between the two methods used to measure efficiency, the input-output and -heat loss methods.
- the Input- Output efficiency is of paramount importance and shows efficiency and energy changes caused by the reactions of the present invention.
- the heat loss efficiency is shown on the graphs for comparison, showing where the efficiency should be under normal conditions.
- Fig. 2 shows that the Input-Output efficiency and Heat Loss Efficiency should be in very close agreement, certainly not more than +1% apart for this test apparatus.
- Fig. 3 shows the results of one of the Lithium Acetate tests; the test was 5.2 hours long with 16 data runs.
- the fuel was kerosene and the fuel pressure was steady at 60 psig.
- No additive was used during the first two runs; a positive displacement chemical injection pump injected a lithium acetate-ethanol solution into the fuel suction hose for the next eight test runs only.
- a saturated solution of lithium acetate in commercial grade ethanol was used in concentrations varying from 5xl0 "4 to lxlO "3 by volume. Shortly after the additive injection started, input-output efficiency climbed from 84.6% to 105.9% and stayed above 100% for 5 runs (105 minutes) and above 90% for 12 runs (243 minutes or 4 hr) . This was one of several lithium acetate based tests with similar results.
- Fig. 4 shows the results of one of the lithium nitrate tests, the test was 5.4 hours long with 25 test runs.
- the fuel was diesel and the fuel pressure was steady at 90 psig.
- a saturated solution of lithium nitrate in commercial grade ethanol was used in concentrations varying from .05 to .28 by volume.
- No additive was injected during the first three and the last five runs, a rotary positive displacement pump was used for injection of the composition.
- the efficiency increased significantly during this test with one input-output efficiency test run reaching 99.6%.
- sets of test data were timed to the second, the dashed line in the graph is a running average to eliminate errors due to any possible inconsistencies in recording and observing test data sets. Levels of gamma radiation were also measured and found to be typical for the reaction under study.
- Fig. 5 shows the results on one of the lithium stearate tests; the test was 8.5 hours long with 52 ten minute test runs.
- the fuel was diesel and the lithium stearate was premixed with the fuel, a concentration of 6.7 x 10 "4 to 2 x 10 "3 by volume was used.
- no additive was used with the fuel.
- the efficiency climbed from 81.2% to an average of 87.26% for 6.5 hours, returning to 80.1% for the last 5 runs (50 minutes) .
- Fig. 6 shows the results of one of the many tests to learn the effect of residual lithium in the combustion system, the test was 4.6 hours long with 28, 10 minute test runs. The fuel was diesel and no additive was used. This was the third similar test of a series of blank runs to measure the effects of residual lithium in the boiler. During previous testing, blank runs had been used at the beginning and at the end of each test to establish base line efficiency conditions for the day in question. Often, the base line values disagreed with expected efficiencies and the efficiency would rise during testing and not return to the expected baseline value after the additive injection stopped. The ideal efficiency for this test should be about 78%, but for 10 runs (100 minutes) the efficiency is above 90%; six runs have an efficiency 15% higher than normal. Only straight fuel was used, precluding any error from higher heating values of additives being tested.
- Fig. 7 shows the results of a 3.8 hour test to determine the effect of lithium additives on the level of nitrogen oxides found in the boiler exhaust. Three consecutive runs with lithium averaged 104 parts per million, after the lithium additive was stopped the average NOx level increased by 300% to 320 PPM.
- Fig. 8 shows the results of an experiment to measure the change in carbon dioxide during a test with a standard oil burner mounted on steel oil drums. This method was used to eliminate the possibility of residual deposits of lithium from influencing the results. A 33% drop in carbon monoxide was produced with a starting value of 45 PPM dropping to 30 PPM over a series of tests.
- Fig. 2 shows that the test bed was accurate enough to indicate 1% changes in efficiency.
- Figures 3 through 6 show that significant efficiency increases can be achieved with compositions of lithium in normal fuels. This included energy output increases of 20% and a most unusual condition, efficiencies over 105%.
- a cause- effect relationship between lithium compositions and efficiency is shown in Fig. 5.
- Fig. 6 shows that even minute amounts of residual lithium can cause efficiency increases if the combustion apparatus is not absolutely clean. More than 8 hours of blank runs preceded this blank run of 4.6 hours which continued to produce very high levels of efficiency.
- the clean run of Fig. 2 shows that efficiencies can be normal with the test apparatus when it is thoroughly clean with no lithium present.
- Fig. 7 shows a significant decrease in nitrogen oxide emissions
- Fig. 8 shows a significant reduction in carbon monoxide. Carbon dioxide is reduced because less fuel is required for a comparable energy output by virtue of the energy producing reactions of this invention.
- Figures 9, 9a, 10 and 11 show an experimental apparatus designed for radiation measurements for alpha, proton and other particles and radiation from the reaction. It is designed to enclose a flame source or reaction envelope, in this case a propane flame with a lithium-ethanol feeder tube attached. A water cooled radiation detector, in this case a proportional counter, is close to the flame and a low grade water cooled alpha source is near the flame for particle initiation. By taking counts from a continuing reaction, changes in the particle population could be measured.
- a flame source or reaction envelope in this case a propane flame with a lithium-ethanol feeder tube attached.
- a water cooled radiation detector in this case a proportional counter, is close to the flame and a low grade water cooled alpha source is near the flame for particle initiation.
- Fig. 12 depicts the results typical of a long series of tests using the apparatus in Figures 9, 9a, and 10. The experiment was conducted to prove the production of alphas using the reactions cited hereinabove. Fig. 12 only shows part of the results; Table 6 has the complete information recorded from a Multi-Channel Analyzer. In this particular experiment, a high voltage source was used as an excitation means for the reaction. Calibration runs using the flame and high voltage excitation system recorded only expected background radiation of just a few counts in a three minute period. When the lithium containing composition was introduced to the flame envelope and the plasma zone created by the intense voltage discharge, the "open path" readings were obtained. A piece of paper was used as shielding, and counts were taken with this shielding in place.
- Fig. 13 depicts a typical result for reductions in carbon monoxide, hydrocarbons, and nitrogen oxides, when the composition contains optimized proportions of lithium to hydrocarbon.
- 2.5 ml of lithium nitrate in a solution of isopropyl alcohol was mixed with each gallon of gasoline.
- the automotive engine being tested had a high voltage spark ignition system.
- Fig. 14 demonstrates the reduction in fuel consumption during the same test.
- Fig. 15 shows the unexpected increase in oxygen during another similar test. This large increase of oxygen in engine exhaust gases is typical for those occasions when the Li/H reaction is thought to be proceeding. Table 6
- Fig. 17 shows experimental results when magnesium nitrate and sodium nitrate compositions were added to the fuel .
- the magnesium composition produced a 22% reduction in carbon monoxide and the sodium compositions produced 20% and 14% reductions.
- compositions useful for reducing pollution in fuel combustion and increasing fuel efficiency were tested as follows.
- test compositions were a) indoline alone, i.e., "pure” gasoline; b) indoline plus 5% ethanol by weight; and c) indoline plus 5% ethanol by weight plus varying amounts of a mixture of lithium nitrate and isopropyl, hereinafter refered to as the "additive.”
- the additive mixture was mixed by weight, 1 gram of lithium nitrate in 12 grams of isopropyl.
- the amount of the additive combined with the indoline / 5% ethanol fuel composition varied from 1ml of additive per gallon of fuel composition to 10 ml of additive per gallon of fuel composition.
- the experimental design was based on established testing regimens.
- the sample of vehicles was weighted to more comprehensively test the most current technology. However, it was also determined that at least several of the vehicles should be older models representing earlier generation emission control systems, or none at all.
- the sample composition was ultimately determined by which vehicles could be obtained for the project.
- the variables in design included age of vehicle, emission control technology, levels of oxygen in the fuel and concentrations of additive. Ethanol was selected as the oxygenate for testing in large part due to its ability to blend easily an thoroughly with the additive.
- FTP Federal Test Protocol
- Each of the vehicles was tested using the Federal Test Protocol (FTP) described in Code of Federal Regulations 40 CFR Part 86 and 40 CFR Part 600. Exhaust emissions were measured under three regimens: cold transient, stabilized and hot transient.
- ETC Environmental Testing Corporation
- AAA Automobile Club of Southern California
- CARB commercially available oxygenated test fuel approved by CARB.
- the second step was to add ethanol to the indolene test fuel and establish a second base line condition. Again, two test were conducted in accordance with specific ⁇ ations. For the four vehicles tested both pre and post emission controls, ethanol was added to provide 1.8% oxygen by weight. The three remaining vehicles at ETC were tested with ethanol providing 2.7% oxygen by weight. The base fuel at AAA contained a negligible percentage of oxygen by weight. The base fuels were provided by the testing facilities. The neat ethanol was laboratory grade and purchased commercially.
- the third step was to test the additive at various concentrations ranging from 1 to 10 milliliters per gallon.
- the test on the Ford Taurus was conducted using the additive only with no oxygenate.
- the only instrumentation needed apart from the testing facility FTP apparatus was a precision scale for measuring fuel.
- test data addresses (1) a determination of any trends in that data, (2) a determination of statistical significance of the results and (3) a determination of the impact of the additive itself on the results.
- Older non-catalyst vehicles run typically lean. The addition of oxygenates in the fuel would further enlean the air-fuel mixture which would result in some carbon monoxide reductions. But the further enleanment of the air-fuel mixture could produce higher VOC emissions because of poor combustion.
- Open-loop vehicles are usually calibrated to run richer than stoichiometric and enleanment resulting from the presence of oxygenates in the fuel would result in VOC and CO emissions reductions accompanied with possible increases in NO x emissions. Closed-loop vehicles are expected to be affected by the presence of oxygenates only when they are operated at open- loop, warm-up, and full power modes.
- the determination of trends is based on three analyses. First, a comparison is made between the results of the indolene test fuel and the ethanol runs to determine the net benefits derived from use of the oxygenate, alone. Second, a comparison is made of the oxygenate and fuel additive together to the indolene test fuel to determine the extent of performance enhancements derived from the combination of additives. Third, a comparison is made between the additive runs and those of ethanol to test the levels of improvement in pollution reduction or fuel efficiency explained by the additive working with the ethanol.
- the first based on the averages of readings for each test, is a comparison of the percentage changes from the indolene baseline figures to the results of (1) the ethanol runs alone and (2) the runs combining ethanol with the proprietary fuel additive.
- the second measurement is a test for the statistical significance of any variances produced by the various runs .
- the tests for statistical significance were structured to test not the overall composite result of each test but rather to look at the significance of each of three phases making up each test. In this regard, the statistical standard is a conservative one.
- Each of the following sections addresses carbon monoxide, non-methane hydrocarbons, nitrogen oxides and miles per gallon, as a measure of fuel efficiency, with and without emissions controls.
- Figure 18 shows a comparison of the percentage change of test results for ethanol alone (open squares) and for ethanol plus the additive (closed squares) from the indolene base line figures. This chart shows the results for non-methane hydrocarbons (NMHC) .
- This comparison is intended to illustrate the basic trends in the test data for the total population of vehicles tested.
- test results indicate that the additive has a statistically significant impact on NMHC production and generally enhances ethanol performance with a few exceptions, the types of emission control devices notwithstanding.
- the results for each test series shows the ranges of data from which the averages were derived.
- the graphical presentation indicates the unit measures for each vehicle. As expected, the pollution levels for the vehicles without emission control devices are substantially more than those for the vehicles with controls.
- Figure 19 shows the similar percentage changes for CO as described above for NMHC.
- the data indicate that for all vehicles without emission controls, there is a substantial reduction in carbon monoxide with the additive compared to use of ethanol alone. All four of the additive data series and one data series of ethanol are statistically significant. The average CO reduction with the additive is 15.9% for these four vehicles and 11.2% excluding the Grand Safari. The average CO reduction for ethanol is 5.4% including the Grand Safari and 4% without.
- Figure 21 shows a trend in the data for miles per gallon for vehicles without emission controls. In all instances there is an increase in MPG. The average increase is .7% for ethanol alone and 1.5% for the oxygenate/additive combination. The figure shows the additive improving four vehicle runs with emission control, leaving two unchanged, eliminating a benefit for the Safari, and further reducing mileage loss for the Cavalier.
- the additive increases the average fuel efficiency by 75% greater than with ethanol alone.
- the statistical significance of three analyses is reviewed for vehicles without emission controls.
- the first comparison shows the impact of ethanol on indolene thereby identifying the benefits derived from use of ethanol alone.
- the second comparison shows the impact of the use of the additive/ethanol combination on indolene.
- the third comparison identifies the statistically significance of the additive no ethanol.
- the top comparison shows the effects of introducing ethanol a base fuel which has no other oxygenate. Eleven of the sixteen entries are statistically significant. The results show the anomalous behavior of the Safari, the beneficial impact of non-methane hydrocarbons and the anticipated increased levels of N0 X .
- the second comparison of the ethanol/additive combination shows how introducing the additive fills in the matrix with significant results, particularly with CO and MPG.
- the third comparison shows how the additive specifically accounted for a change in the performance of the oxygenate or may have increased the magnitude of that change.
- the synergistic effects are notable.
- the introduction of the additive reverses the statistically significant increase in pollution for the Sunbird and Cavalier and provides a statistically significant reduction in both of those two instances.
- the ethanol/additive combination creates statistically significant benefits for the Achieva and Cutlass. The combination provides a benefit in the instance of the Cutlass for hydrocarbons and for the Sunbird with MPG. The additive contributed to a degradation in MPG for the Safari.
- the fuel additive disclosed hereinabove has demonstrated statistically significant reductions in carbon monoxide and hydrocarbons in vehicles without emission control devices and without materially increasing nitrogen oxide levels.
- the average reduction in carbon monoxide for vehicles without emission control devices is 15% with the fuel additive compared to 4.7% for ethanol alone.
- the fuel additive has demonstrated a trend in the reduction of hydrocarbons in vehicles with emission control devices .
- Several data points were statistically significant. There is no apparent trend in the carbon monoxide data but a trend toward increased nitrogen oxide levels is suggested.
- the average reduction in hydrocarbons for the vehicles with emissions controls is 8.4% with the fuel additive compared to less than 1% for ethanol alone.
- the effects of the fuel additive on carbon monoxide levels are reduced when emission controls are used (1) because the levels of pollutants from the tailpipe are substantially less and (2) the oxygen sensor (the on- board computer with an oxygen feedback loop) compensates for and mitigates the impact of the catalytic reaction. This result is consistent with CARB determinations that the benefits of oxygenates in vehicles with emission controls are not as pronounced as those without controls.
- the catalytic reaction also appears to raise combustion zone oxygen levels which, in turn, activate control devices and dampen the effect of the reaction.
- the average increase in NO x is 3% with ethanol alone and 5.3% with the oxygenate/additive combination.
- Fuel efficiency for the whole sample is increased an average of .75% over indolene or ethanol alone. For those vehicles without emission controls the increase is 1.5% with the additive and .7% for the ethanol alone.
- the benefits of the fuel additive vary with the make and emission control technology of each automobile. (For example, with the exception of one reading, the fuel additive reduced every pollutant from the 1994 Oldsmobile Achieva with and without emission control devices while there was no effect from the oxygenate or the additive in the instance of the 1988 Ford Bronco.)
- the combination of the additive and ethanol creates statistically significant changes relative to indolene that are not explained by the reaction of the additive with the oxygenate alone, i.e., the combination creates a synergistic effect. That synergistic effect basically creates an additional beneficial result.
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- Physics & Mathematics (AREA)
- Engineering & Computer Science (AREA)
- Plasma & Fusion (AREA)
- General Engineering & Computer Science (AREA)
- High Energy & Nuclear Physics (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Description
Claims
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
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AU78276/94A AU7827694A (en) | 1993-08-12 | 1994-08-12 | Process for reducing pollution in energy production |
EP94929094A EP0719440A1 (en) | 1993-08-12 | 1994-08-12 | Process for reducing pollution in energy production |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
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US10579393A | 1993-08-12 | 1993-08-12 | |
US08/105,793 | 1993-08-12 |
Publications (1)
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WO1995005665A1 true WO1995005665A1 (en) | 1995-02-23 |
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Application Number | Title | Priority Date | Filing Date |
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PCT/US1994/009125 WO1995005665A1 (en) | 1993-08-12 | 1994-08-12 | Process for reducing pollution in energy production |
Country Status (4)
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EP (1) | EP0719440A1 (en) |
AU (1) | AU7827694A (en) |
CA (1) | CA2169359A1 (en) |
WO (1) | WO1995005665A1 (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2408844A (en) * | 2003-11-26 | 2005-06-08 | Ping-Wha Lin | Generating electricity from nuclear reactions |
WO2012003005A3 (en) * | 2010-07-02 | 2013-07-11 | Taplin Harry R Jr | Process for high efficiency, low pollution fuel conversion |
US10718511B2 (en) | 2010-07-02 | 2020-07-21 | Harry R. Taplin, JR. | System for combustion of fuel to provide high efficiency, low pollution energy |
Citations (6)
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US3951613A (en) * | 1971-02-03 | 1976-04-20 | Stewart Hall Chemical Co. | Anti-pollution heating oil products and processes |
US4333796A (en) * | 1978-05-19 | 1982-06-08 | Flynn Hugh G | Method of generating energy by acoustically induced cavitation fusion and reactor therefor |
US4428193A (en) * | 1980-09-04 | 1984-01-31 | Papp International Incorporated | Inert gas fuel, fuel preparation apparatus and system for extracting useful work from the fuel |
US4454850A (en) * | 1978-07-14 | 1984-06-19 | Beeston Company Limited | Apparatus and method for energy conversion |
US4668247A (en) * | 1985-09-25 | 1987-05-26 | Fusion Aided Combustion Technology International Corporation | Hydrogen energy releasing catalyst |
US4973336A (en) * | 1988-06-10 | 1990-11-27 | Gheysens Jean Louis G | Fuel additives |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB458496A (en) * | 1935-03-14 | 1936-07-08 | Neutron S A | Process for the synthesis of chemical elements |
GB459210A (en) * | 1935-11-25 | 1936-08-17 | Neutron S A | Process for the production of power by means of nuclear combinations |
GB508233A (en) * | 1937-02-09 | 1939-06-28 | Degea Ag Auergesellschaft | Method for carrying out nuclear reactions |
DE4041127A1 (en) * | 1990-12-21 | 1992-02-20 | Daimler Benz Ag | METHOD FOR REDUCING POLLUTANT EMISSIONS FROM COMBUSTION EXHAUST GASES FROM DIESEL ENGINES |
-
1994
- 1994-08-12 EP EP94929094A patent/EP0719440A1/en not_active Withdrawn
- 1994-08-12 WO PCT/US1994/009125 patent/WO1995005665A1/en not_active Application Discontinuation
- 1994-08-12 AU AU78276/94A patent/AU7827694A/en not_active Abandoned
- 1994-08-12 CA CA002169359A patent/CA2169359A1/en not_active Abandoned
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3951613A (en) * | 1971-02-03 | 1976-04-20 | Stewart Hall Chemical Co. | Anti-pollution heating oil products and processes |
US4333796A (en) * | 1978-05-19 | 1982-06-08 | Flynn Hugh G | Method of generating energy by acoustically induced cavitation fusion and reactor therefor |
US4454850A (en) * | 1978-07-14 | 1984-06-19 | Beeston Company Limited | Apparatus and method for energy conversion |
US4428193A (en) * | 1980-09-04 | 1984-01-31 | Papp International Incorporated | Inert gas fuel, fuel preparation apparatus and system for extracting useful work from the fuel |
US4668247A (en) * | 1985-09-25 | 1987-05-26 | Fusion Aided Combustion Technology International Corporation | Hydrogen energy releasing catalyst |
US4973336A (en) * | 1988-06-10 | 1990-11-27 | Gheysens Jean Louis G | Fuel additives |
Non-Patent Citations (1)
Title |
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Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2408844A (en) * | 2003-11-26 | 2005-06-08 | Ping-Wha Lin | Generating electricity from nuclear reactions |
GB2408844B (en) * | 2003-11-26 | 2006-11-01 | Ping-Wha Lin | Fuel cells that operate on nuclear reactions produced using rapid temperature changes |
WO2012003005A3 (en) * | 2010-07-02 | 2013-07-11 | Taplin Harry R Jr | Process for high efficiency, low pollution fuel conversion |
US8852300B2 (en) | 2010-07-02 | 2014-10-07 | Harry R. Taplin, JR. | Lithium conditioned engine with reduced carbon oxide emissions |
US9702546B2 (en) | 2010-07-02 | 2017-07-11 | Harry R. Taplin, JR. | Process for high efficiency, low pollution fuel conversion |
US10082288B2 (en) | 2010-07-02 | 2018-09-25 | Harry R. Taplin, JR. | Process for high efficiency, low pollution fuel conversion |
US10718511B2 (en) | 2010-07-02 | 2020-07-21 | Harry R. Taplin, JR. | System for combustion of fuel to provide high efficiency, low pollution energy |
Also Published As
Publication number | Publication date |
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EP0719440A1 (en) | 1996-07-03 |
AU7827694A (en) | 1995-03-14 |
EP0719440A4 (en) | 1996-07-17 |
CA2169359A1 (en) | 1995-02-23 |
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