Patent Application
20050013772
This invention relates to the field of hydrogen fuel systems. More specifically, this invention relates to a system and a method for breaking down hydrocarbon fuels. Further, the invention relates to a system and a method for breaking down hydrocarbon fuels to produce a hydrogen gas and solid particles without oxidizing the hydrocarbon fuel. Moreover, this invention relates to a system and method for separating the hydrogen gas from the solid particles from a gaseous and non-gaseous fuel source.
Typical hydrocarbon fuel reformers on the market today are used to produce hydrogen for fuel cell applications. An example of hydrocarbon fuel reformers is the use of fuel cells that have a general use in automotive technology. The prior art fuel reformers use a partial oxidation process to produce hydrogen and a mixture of carbon monoxide and carbon dioxide. See for example, United States Patents to: Lomax et al. U.S. Pat. No. 6,623,719; Struthers et al., U.S. Pat. No. 6,620,537; Kiryu et al., U.S. Pat. No. 6,565,817. These prior art fuel reformers produce hydrogen and a mixture of carbon monoxide and carbon dioxide because the production of solid carbon in a reformer usually results in “coking” of the reformer. More specifically, “coking” occurs wherein the gas flow passages become clogged with the solid carbon particulate that has been separated from the hydrocarbon mixture. “Coking” and/or clogging of the gas flow passages greatly diminishes the effectiveness of fuel cell use, because the gas flows are lower and not constant. However, there are situations where a gaseous hydrogen and a particulate byproduct would be advantageous. Such a situation arises when the particulate can be used in a different type of fuel cell application, such as, for example direct carbon-air fuel cells. Therefore if both the hydrogen and the carbon from the hydrocarbons could be used as fuel in a fuel cell application, the overall efficiency of the resulting electrical generator would be greatly increased.
A need therefore exists for a reformer that may provide the ability to separate the fuel into droplets small enough to be reformed. A need also exists for a means of separating the fuel into a gaseous hydrogen and solid particles. Further, a need exists for a means that may remove the solid particles from the flowing stream of hydrogen gas.
The present invention provides a system and a method for separating hydrocarbon fuels into smaller droplets such that the hydrogen and the solid particulate may be separated. More specifically, the present invention provides a system and a method for splitting hydrocarbon fuels into hydrogen gas and solid particulate.
To this end, in an embodiment of the present invention, a system for reforming non-gaseous hydrocarbon fuels is provided. The system has a dispensing means for dividing the hydrocarbon fuel into small droplets. Moreover, the system has a dissociating means for dissociating the hydrocarbon fuel into hydrogen gas and solid particles. Further, the system has a separating means for separating said solid particles from said hydrogen gas.
In another embodiment, the system has a dispensing means for separating the hydrocarbon fuel wherein said dispensing means is a nozzle.
In another embodiment, the system has a dispensing means for separating the hydrocarbon fuel wherein said dispensing means is a injector, grinder, atomizer or other means of dividing into very small particles or droplets.
In another embodiment, the system has a dissociating means wherein said dissociating mean converts the hydrocarbon fuel into gaseous hydrogen and solid particles by using a radio frequency discharge plasma that efficiently dissociates the Carbon-Hydrogen bond.
In another embodiment, the system has a dissociating means wherein said dissociating means converts the hydrocarbon fuel into gaseous hydrogen and solid carbon by using radio frequency plasma discharge tuned to a frequency or frequencies that most efficiently dissociates the carbon-hydrogen bond.
In another embodiment, the system has a separating means for separating said solid particles from said hydrogen gas wherein said separating means is acoustic flocculation.
In another embodiment, the system has a separating means for separating said solid particles from said hydrogen gas wherein said separating means is filter membranes, electromagnetic separating techniques, the use of a bias voltage on a substrate in the bottom of the separation means, or use of other small particles separation techniques.
In another embodiment, the system has a separating means for separating said solid particles from said hydrogen gas wherein said separating means is acoustic flocculation further wherein said acoustic flocculation agglomerates the solid carbon particulate to increase the mass of each particle to the point that the force of gravity will separate the agglomerated particles from the flowing hydrogen stream.
In an embodiment of the present invention, a system for reforming gaseous hydrocarbon fuels is provided. The system has a dissociating means for dissociating the hydrocarbon fuel into hydrogen gas and solid particles. Moreover, the system has a separating means for separating said solid particles from said hydrogen gas.
In another embodiment, the system has a dissociating means wherein said dissociating means converts the hydrocarbon fuel into gaseous hydrogen and solid particles by using a radio frequency discharge plasma that efficiently dissociates the carbon-hydrogen bond.
In another embodiment, the system has a dissociating means wherein said dissociating means converts the hydrocarbon fuel into gaseous hydrogen and solid particles by using radio frequency plasma discharge tuned to a frequency or frequencies that most efficiently dissociates the carbon-hydrogen bond or the carbon-carbon bond.
In another embodiment, the system has a separating means for separating the dissociated hydrocarbon into solid particles and gas wherein said separating means is acoustic flocculation and further wherein said acoustic flocculation agglomerates the solid particles to increase the mass of each particles to the point that the force of gravity will separate the agglomerated particles from the flowing hydrogen stream.
In another embodiment, the system has a separating means for separating the dissociated hydrocarbon into solid particles and gas wherein said dispensing means is filter membranes, electromagnetic separating techniques, the use of a bias voltage on a substrate in the bottom of the separating means, or use of other small particles separation techniques.
In an embodiment of the present invention, a method for producing gaseous hydrogen and solid particles from non-gaseous hydrocarbon fuels is provided. The method comprising the steps of: dividing the fuel into very small particles; dissociating the hydrocarbon fuel particles into gaseous hydrogen and solid particles; separating the dissociated solid particles from the gaseous hydrogen.
In another embodiment, the method includes the step of: providing a means of dividing hydrocarbon fuel into particles wherein hydrogen-carbon bonds that exist in the hydrocarbon fuel may be broken wherein said means of dividing hydrocarbon fuel is a nozzle, injector, grinder, atomizer, or other means to divide the hydrocarbon fuels into small particles or droplets.
In another embodiment, the method includes the step of: providing a means of dissociating the solid particles from the hydrogen and producing gaseous hydrogen and solid particulate wherein said dissociating means is a radio frequency plasma discharge.
In another embodiment, the method includes the step of: providing a means of dissociating the solid particles carbon from the hydrogen and producing gaseous hydrogen and solid particulate wherein said dissociating means is plasma discharge created by a capacitive or inductive coil discharge device.
In another embodiment, the method includes the step of: providing a means of separating the gaseous hydrogen from the solid particles such that the gaseous hydrogen and the solid particles can then be used in their natural state wherein said separating means is acoustic flocculation to agglomerate the solid particles to increase the mass of each particle to the point that the force of gravity separates the agglomerated particles from a hydrogen stream.
In another embodiment, the method includes the step of: providing a means of separating the gaseous hydrogen from the solid particles such that the gaseous hydrogen and the solid particles can then be used in their natural state wherein said separating means is electromagnetic separation techniques, bias voltage on a substrate in the bottom of the separation means that will attract the solid particulate and cause the solid particulate to settle and be removed, or any small particle separating technique to remove the solid particle from the divided hydrocarbon fuel.
In another embodiment, the method includes the step of: reforming hydrocarbon fuels for a fuel cell which does not oxidize the hydrocarbon fuel.
In another embodiment, the method includes the step of: producing a solid particle fuel in addition to the gaseous hydrogen.
In another embodiment, the method includes the step of: removing the solid particulate from the gaseous hydrogen.
In another embodiment, the method includes the step of: utilizing the solid particles in a carbon fuel cell and utilizing the gaseous hydrogen in a hydrogen fuel cell.
In an embodiment of the present invention, a method for producing gaseous hydrogen and solid particles from gaseous hydrocarbon fuels is provided. The method comprising the steps of: dissociating the hydrocarbon fuel into gaseous hydrogen and solid particles; separating the dissociated solid particles from the gaseous hydrogen.
In another embodiment, the method includes the step of: providing a means of dissociating the solid particles from the hydrogen and producing gaseous hydrogen and solid particulate wherein said dissociating means is a radio frequency plasma discharge.
In another embodiment, the method includes the step of: providing a means of dissociating the solid particles carbon from the hydrogen and producing gaseous hydrogen and solid particulate wherein said dissociating means is plasma discharge created by a capacitive or inductive coil discharge device.
In another embodiment, the method includes the step of: providing a means of separating the gaseous hydrogen from the solid particles such that the gaseous hydrogen and the solid particles can then be used in their natural state wherein said separating means is acoustic flocculation to agglomerate the solid particles to increase the mass of each particle to the point that the force of gravity separates the agglomerated particles from a hydrogen stream.
In another embodiment, the method includes the step of: providing a means of separating the gaseous hydrogen from the solid particles such that the gaseous hydrogen and the solid particles can then be used in their natural state wherein said separating means is electromagnetic separation techniques, bias voltage on a substrate in the bottom of the separation means that will attract the solid particulate and cause the solid particulate to settle and be removed, or any small particle separating technique to remove the solid particle from the divided hydrocarbon fuel.
In another embodiment, the method includes the step of: reforming hydrocarbon fuels for a fuel cell which does not oxidize the hydrocarbon fuel.
In another embodiment, the method includes the step of: producing a solid particle fuel in addition to the gaseous hydrogen.
In another embodiment, the method includes the step of: removing the solid particulate from the gaseous hydrogen.
In another embodiment, the method includes the step of: utilizing the solid particles in a carbon fuel cell and utilizing the gaseous hydrogen in a hydrogen fuel cell.
It is, therefore, an advantage of the present invention to provide a system and a method for producing gaseous hydrogen from hydrocarbon fuels.
Another advantage of the present invention is to provide a system and a method for producing solid particulate directly from hydrocarbon fuels.
Still another advantage of the present invention is to provide a system and a method for producing gaseous hydrogen and solid particles at high efficiency.
Another advantage of the present invention is to provide a system and a method for atomizing the fuel through a nozzle.
Yet another advantage of the present invention is to provide a system and a method for dividing the fuel into very small droplets.
An advantage of the present invention is to provide a system and a method for producing gaseous hydrogen and solid particulate by dividing the fuel into droplets small enough to be reformed.
Still another advantage of the present invention is to provide a system and a method for producing gaseous hydrogen and solid particulate that may be highly compact.
Yet another advantage of the present invention is to provide a system and a method for producing gaseous hydrogen and solid particulate that may be a robust fuel reformer.
Another advantage of the present invention is to provide a system and a method for dissociating hydrocarbon fuels wherein the hydrocarbon fuel may be solid.
An advantage of the present invention is to provide a system and a method for dissociating hydrocarbon fuels wherein the fuel may be liquid.
Still another advantage of the present invention is to provide a system and a method for dissociating hydrocarbon fuels wherein the fuel may be a gas.
Yet another advantage of the present invention is to provide a system and a method for dissociating hydrocarbon fuels wherein the hydrocarbon fuel may be gasoline.
Another advantage of the present invention is to provide a system and a method for dissociating hydrocarbon fuels wherein the hydrocarbon fuel may be kerosene.
An advantage of the present invention is to provide a system and a method for dissociating hydrocarbon fuels wherein the hydrocarbon fuel may be diesel.
Still another advantage of the present invention is to provide a system and a method for dissociating hydrocarbon fuels wherein the hydrocarbon fuel may be heating oil.
Yet another advantage of the present invention is to provide a system and a method for dissociating hydrocarbon fuels wherein the hydrocarbon fuel may be bunker fuel.
Another advantage of the present invention is to provide a system and a method for dissociating hydrocarbon fuels wherein the hydrocarbon fuel may be crude oil.
Still another advantage of the present invention is to provide a system and a method for dissociating hydrocarbon fuels wherein the hydrocarbon fuel may be natural gas.
Yet another advantage of the present invention is to provide a system and a method for dissociating hydrocarbon fuels wherein the hydrocarbon fuel may be high hydrogen coals.
Still yet another advantage of the present invention is to provide a system and a method for dissociating hydrocarbon fuels wherein the hydrocarbon fuel may be any petroleum or bio-derived hydrocarbon fuel.
An advantage of the present invention is to provide a system and a method for dissociating hydrocarbon fuels wherein the hydrocarbon fuel may be a solid fuel including high hydrogen coal, oil shale, tar sand, or any hydrocarbon that is in solid form.
Yet another advantage of the present invention is to provide a system and a method for dissociating hydrocarbon fuels wherein the hydrocarbon fuel may be natural gas, propane, LPG, acetylene, or other gaseous hydrocarbon.
Another advantage of the present invention is to provide a system and a method for dissociating hydrocarbon fuels wherein the hydrocarbon fuel may be input into a chamber where the hydrogen and solid particulate dissociate from each other.
An advantage of the present invention is to provide a system and a method for dissociating hydrocarbon fuels wherein the carbon to hydrogen chemical bonds are broken so that hydrogen may form molecular free hydrogen.
An advantage of the present invention is to provide a system and a method for dissociating hydrocarbon fuels wherein the system includes a fuel reformer for separating the fuel into solid and gaseous particles.
Still another advantage of the present invention is to provide a system and a method for dissociating hydrocarbon fuels into a gaseous hydrogen and solid particles wherein the system may reflux some of the dissociated hydrogen back into the system to further facilitate dissociation.
Another advantage of the present invention is to provide a system and a method for dissociation of hydrocarbon fuels without oxidizing the mixture.
An advantage of the present invention is to provide a system and a method for dividing the hydrocarbon fuel into a gaseous hydrogen state and a solid particulate wherein the solid particulate is primarily carbon.
Another advantage of the present invention is to provide a system and a method for providing an output of gaseous hydrogen and solid particulate that may be used in fuel cell technology.
Still another advantage of the present invention is to provide a system and a method for separating the hydrogen gas from the solid particulate.
Another advantage of the present invention is to provide a system and a method for separating the hydrogen gas from the solid particulate using acoustic flocculation.
Another advantage of the present invention is to provide a system and a method to divide hydrocarbon fuels by using fuel atomization.
Yet another advantage of the present invention is to provide a system and a method for separating hydrocarbon fuels by using fuel atomization where the hydrocarbon is fed through a dividing device such as a nozzle to divide the hydrocarbon into small droplets.
Still another advantage of the present invention is to provide a system and a method for dissociating the small droplets of hydrocarbon fuels by using a dissociating means wherein the dissociating means dissociates the gaseous hydrogen from the solid particulate by a means of radio frequency discharge.
An advantage of the present invention is to provide a system and a method for separating the hydrogen gas from the solid particulate using acoustic flocculation in which the solid particles in an aerosol collide with each other and stick together, to become large enough that they will fall out of the aerosol due to the force of gravity.
These and other objects of the invention will become more clear when one reads the following specification. The scope of protection sought by the inventors may be gleaned from a fair reading of the claims that conclude this specification.
Additional features and advantages of the present invention are described in, and will be apparent from the detailed description of the presently preferred embodiments and from the drawings.
Turning now to the drawings wherein elements are identified by numbers and like elements are identified by like numbers throughout the 2 figures, the invention is depicted in
Hydrocarbon fuel 3 may come from a variety of physical forms. For example, the fuel may be solid, liquid and/or gas. However, in an embodiment of the present invention, the hydrocarbon fuel 3 may be in non-gaseous form In another embodiment of the invention, the hydrocarbon fuel 3 may be in gaseous form. The non-gaseous hydrocarbon fuel 3 may be gasoline, kerosene, diesel, heating oil, bunker fuel, or even crude oil, among others. Natural gas may also be used as the initial stock fuel for the reformer, as well as high hydrogen coals.
As illustrated in
As illustrated in
The hydrocarbon fuel 3 may be broken down into small droplets by using atomizers (not shown) or nozzles 7 or injectors (not shown) for liquid fuels. The fuel may also be broken down when dispensed through use of a dust nozzle (not shown), injectors (not shown), grinders (not shown) or other means for dividing solid hydrocarbon fuels 3 and introducing them to the dissociation means 19.
As illustrated in
It should be understood that various changes and modifications to the presently preferred embodiments described herein will be apparent to those skilled in the art. Such changes and modifications may be made without departing from the spirit and scope of the present invention and without diminishing its attendant advantages.
| Number | Date | Country | |
|---|---|---|---|
| 60488515 | Jul 2003 | US |
