Classifications

• • C—CHEMISTRY; METALLURGY
  • C01—INORGANIC CHEMISTRY
  • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
  • C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
  • C01B3/50—Separation of hydrogen or hydrogen containing gases from gaseous mixtures, e.g. purification
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01J—ELECTRIC DISCHARGE TUBES OR DISCHARGE LAMPS
  • H01J37/00—Discharge tubes with provision for introducing objects or material to be exposed to the discharge, e.g. for the purpose of examination or processing thereof
  • H01J37/32—Gas-filled discharge tubes
• • C—CHEMISTRY; METALLURGY
  • C01—INORGANIC CHEMISTRY
  • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
  • C01B13/00—Oxygen; Ozone; Oxides or hydroxides in general
  • C01B13/02—Preparation of oxygen
• • C—CHEMISTRY; METALLURGY
  • C01—INORGANIC CHEMISTRY
  • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
  • C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
  • C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
• • H—ELECTRICITY
  • H05—ELECTRIC TECHNIQUES NOT OTHERWISE PROVIDED FOR
  • H05H—PLASMA TECHNIQUE; PRODUCTION OF ACCELERATED ELECTRICALLY-CHARGED PARTICLES OR OF NEUTRONS; PRODUCTION OR ACCELERATION OF NEUTRAL MOLECULAR OR ATOMIC BEAMS
  • H05H1/00—Generating plasma; Handling plasma
  • H05H1/24—Generating plasma
  • H05H1/26—Plasma torches
  • H05H1/32—Plasma torches using an arc
  • H05H1/34—Details, e.g. electrodes, nozzles
• • H—ELECTRICITY
  • H05—ELECTRIC TECHNIQUES NOT OTHERWISE PROVIDED FOR
  • H05H—PLASMA TECHNIQUE; PRODUCTION OF ACCELERATED ELECTRICALLY-CHARGED PARTICLES OR OF NEUTRONS; PRODUCTION OR ACCELERATION OF NEUTRAL MOLECULAR OR ATOMIC BEAMS
  • H05H1/00—Generating plasma; Handling plasma
  • H05H1/24—Generating plasma
  • H05H1/47—Generating plasma using corona discharges
  • H05H1/475—Filamentary electrodes
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
  • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
  • Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
  • Y02E60/30—Hydrogen technology
  • Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
• • 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
  • Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
  • Y02W10/00—Technologies for wastewater treatment
  • Y02W10/30—Wastewater or sewage treatment systems using renewable energies
  • Y02W10/37—Wastewater or sewage treatment systems using renewable energies using solar energy

Definitions

• Water splitting is the general term for a chemical reaction in which water is separated into oxygen and hydrogen. Efficient and economical water splitting is a key technological component of a hydrogen economy.
• Various techniques for water splitting have been described in water splitting patents issued in the United States. In photosynthesis, water splitting donates electrons to the electron transport chain in photosystem II and separately donates protons in the proton membrane process.
• Huge energy requirements, the expected shortage of petroleum in the future and quick rise in pollution are the problems that need to be addressed by putting more efforts into investigating clean and sustainable energy resources. In pursuit of such energy sources, efforts are being put into 'light driven' splitting of water into 0 2 and H 2 in an attempt to convert solar energy into fuel.
• Water oxidation (2H 2 0 ⁇ 4H + +4e ⁇ +0 2 ) is the first important step in providing the necessary electrons and protons for the next step (proton reduction) in which hydrogen production takes place in a catalysis reaction by a proton reduction catalyst.
• the water oxidation step has been considered the bottleneck of this process, so the designing of highly active and robust water oxidation catalysts (WOCs) is an important step in the development of light- driven water splitting.
• WOCs water oxidation catalysts minimize the overpotential and increase the reaction rate.
• An ideal WOC is required to possess low overpotential, high stability, high
• Hydrogen is locked up in enormous quantities in water, hydrocarbons, and other organic matter.
• One of the challenges of using hydrogen as a fuel comes from being able to efficiently extract hydrogen from these compounds.
• steam reforming, or combining high-temperature steam with natural gas accounts for the majority of hydrogen produced.
• Hydrogen can also be produced from water through electrolysis, but this method is much more energy intensive which also limits its' productivity (Myers, 1987).
• hydrogen is an energy carrier (i.e. a store for energy first generated by other means).
• the energy can be delivered to fuel cells and generate electricity and heat or burned to run a combustion engine.
• hydrogen is combined with oxygen to form water.
• the heat in a hydrogen flame is a radiant emission from the newly formed water molecules.
• the water molecules are in an excited state on initial formation and then transition to a ground state; the transition unleashing thermal radiation.
• the temperature is roughly 2000 °C.
• Materials used in photocatalytic water splitting fulfill the band requirements outlined previously and typically have dopants and/or co-catalysts added to optimize their performance.
• a sample semiconductor with the proper band structure is titanium dioxide (TiO).
• TiO titanium dioxide
• Pt platinum
• CdS cadmium sulfide
• sulfide-based photocatalysts are not viable without sacrificial reagents such as sodium sulfide to replenish any sulfur lost, which effectively changes the main reaction to one of hydrogen evolution as opposed to water splitting. Recombination of the electron-hole pairs needed for photocatalysis can occur with any catalyst and is dependent on the defects and surface area of the catalyst; thus, a high degree of crystallinity is required to avoid recombination at the defects.
• Orange County California leads the world in recycling and purifying raw sewage and converting it back to usable/potable drinking water.
• the process works by re-routing a proportion of the 1.3 billion gallons of waste water generated in Southern California each day into a three-step treatment.
• the first is microfiltration of the treated waste water to remove solids, oils and bacteria, before the resulting liquid goes through reverse osmosis, pushing it through a fine plastic membrane that filters out viruses and pharmaceuticals.
• the water is then treated with UV light to remove any remaining organic compounds, before joining the main groundwater supply, which must pass strict quality controls to meet legal standards, and distribution to households.
• Texas (parts of which are also severely affected by drought), plans to generate 10% of all new water supplies through reclaimed water by 2060.
• a facility in Big Spring has introduced the first "Direct Potable Re- use” scheme in the United States by sending recycled water to the final treatment plant without passing it through groundwater reserves.
• the present invention utilizes waste water or raw sewage to create hydrogen and oxygen gasses from waste, thereby preserving the usage of potable water for drinking, to produce hydrogen and oxygen as a fuel source.
• the dirty water is thereby purified, and the bacteria therein is eliminated.
• the byproduct (if any) is potable water.
• the required solution is to use materials capable of storing large amounts of hydrogen in a compact form.
• Metals and compounds such as magnesium and sodium borohydride can absorb a lot of hydrogen (up to 10% of their own weight) like a sponge would absorb water.
• the beauty of this concept is that once the hydrogen is absorbed by the material it is indefinitely stored in a totally safe manner. Controlling the temperature of the materials will allow fully reversible uptake and release of hydrogen.
• Hydrogen must be liquefied at temperature of 20.28 K (-423.17 °F/-252.87°C) and maintained at this temperature so it does not turn into gas form by means of nitrogen.
• Liquid hydrogen in maintenance of a liquid state and the devices in order to do this requires an industrial MAZMAT type licensing and certification. This can only be acquired if undersigned by corporate entity with over-sight.
• Liquid hydrogen requires cryogenic storage technology such as special thermally insulated containers and requires special handling common to all cryogenic fuels. Liquid hydrogen is in all purposes considered an explosive in liquid form or gas form and certifications are not for public use.
• Plasma acceleration is a technique for accelerating charged particles, such as electrons, positrons and ions, using an electric field associated with electron plasma wave or other high-gradient plasma structures (like shock and sheath fields).
• the plasma acceleration structures are created either using ultra-short laser pulses or energetic particle beams that are matched to the plasma parameters. These techniques offer a way to build high performance particle accelerators of much smaller size than conventional devices.
• the basic concepts of plasma acceleration and its possibilities were originally conceived by Toshiki Tinima and Prof. John M. Dawson of UCLA in 1979. Initial designs of experiment for "wakefield" were conceived at UCLA by the group of Prof. Chan Joshi. Current experimental devices show accelerating gradients several orders of magnitude better than current particle accelerators.
• Plasma accelerators have immense promise for innovation of affordable and compact accelerators for various applications ranging from high energy physics to medical and industrial applications. Medical applications include betatron and free-electron light sources for diagnostics or radiation therapy and protons sources for hadron therapy. Plasma accelerators generally use
• plasma accelerators can operate in many different regimes depending upon the characteristics of the plasmas used.
• the present invention relates generally to creating hydrogen gas as well as oxygen in the same crucible with bladderless separation due to the use of a plasma arc created by dissimilar metals reacting with Perforated Nickel Plates.
• the 'plasma effect' acts to free massive amounts of hydrogen molecules and oxygen molecules on the hydrogen emitting side of the crucible and the ionized oxygen molecules combine with the fragmented metal particles from the tungsten electrode which consumes the tungsten in part, which thereby captures the oxygen molecules almost completely. This then releases relatively pure hydrogen on the hydrogen side of the crucible.
• the 'plasma effect acts to free massive amounts of hydrogen molecules and oxygen molecules on the Oxygen emitting side of the crucible and the ionized hydrogen molecules combine with the fragmented metal particles from the Nickel electrode which consumes the nickel in part, which thereby captures the hydrogen molecules almost completely. This then releases relatively pure oxygen on the oxygen side of the crucible.
• the process begins when a 600 - 800 pulsed VDC is applied to the anode and cathode side of the hydrogen side of the crucible.
• the Cathode is comprised of a filament wire of Tungsten which is electronically fed, as needed, by an automatic feeder assembly and a stepper motor attached to a control module, monitored by a p/c at a control console and monitor.
• the Anode side is comprised of two perforated solid nickel plates affixed on either side of the Tungsten filament at close range and separated from the filament by two glass, or ceramic, or Teflon insulators that keep the filament from touching the nickel plates and shorting out.
• the seeded water in the crucible tank acts as a short circuit between the Anode and Cathode creating high heat because of the high voltage/high amperage VDC applied across the field.
• the high heat ionizes the hydrogen and oxygen molecules in the solution and millions of highly charged ions (electrons and protons) are freed from the H20 solution instantaneously.
• the freed electrons are guided, in one embodiment, by magnetics to a spot where a vacuum pump evacuates the free hydrogen and the resulting freed oxygen molecules are trapped by the particles and fragmented Tungsten metal that is melted off in the process whereby the oxygen atoms become bonded to the tungsten atoms and the oxygen atoms are trapped in the bottom of the crucible in the water bath solution.
• the opposite side of the crucible begins to emit pure oxygen atoms because of a similar reaction between the Cathode comprised of perforated solid nickel plates identical to the plates and plate configuration on the hydrogen inside of the crucible with the exception that the Anode is now comprised of solid nickel wire that is again sandwiched between the two solid nickel plates and insulated by glass, ceramic, or Teflon insulators.
• the water solution creates a short between the Anode and Cathode and results in high heat being generated between the plates and the wire which fragments the nickel wire into small nickel particles which act to trap any hydrogen released in the plasma process and once the hydrogen atoms and the nickel atoms are bonded, the pure oxygen is released and then guided and accelerated by the magnetic guidance system to a place in the crucible where the freed oxygen atoms can be vacuumed off and stored as is the teachings of the present invention.
• the aqueous solution in the bottom of the crucible is constantly stirred by a recycle water pump that acts to reconstitute the catalytic or seeding element in the water bath and at the same time cool and clean the water chamber of larger particles and debris through a water filter located within the pump assembly.
• a recycle water pump that acts to reconstitute the catalytic or seeding element in the water bath and at the same time cool and clean the water chamber of larger particles and debris through a water filter located within the pump assembly.
• a low voltage pulse of 0 to 200Hz is applied to the anode and cathode simultaneously which is caused to resonate at a specific frequency relevant to the hydrogen atoms on the one side and the oxygen atoms on the other side.
• the monitoring system senses any irregularities in the system such as high heat, high pressure, leaking gasses on either side, loss of power, loss of pulsed modulation, low water level, low catalytic levels or any other such abnormality, the entire system will be powered down and the gasses exhausted first on the oxygen side and then on the hydrogen side. Since the entire system is comprised of base metals, water, ceramics, glass, and other non-flammables, the system is very unlikely to experience any fire or explosions.
• metals described here in the Specifications are not limited to Nickel and Tungsten.
• Several other combinations of metals in a similar configuration can produce similar reactions to a greater or lesser degree of desired results.
• Figure 28 there are a set of possible combinations which can achieve desired results and at the same time create byproducts of great value and desirability such as Titanium Dioxide (Ti02) for example, as may be used in paint, food coloring, sunscreen, cosmetics and various industrial uses.
• Ti02 Titanium Dioxide
• the output product of each can be stored under low pressure in designated tanks, one for the hydrogen gas storage, and one for the oxygen gas storage.
• the storage tanks are loaded with special materials to allow for maximum volume storage for each type of gas.
• the materials in each storage tank compliment the storage by compacting the H2 and 02 gasses respectively.
• the storage of the gasses is in small quantities for safety and is required only to get the vehicle going from a dead start in the morning, if and when no gas generation has been undertaken overnight. This completes the production and storage phase of operations for vehicles powered by hydrogen or hydrogen and oxygen or as combined with other gases or fuels.
• the gasses can be stored under pressure on demand for a specific period such as hourly, daily, or weekly. In this case, the amount of gasses, actually stored for any given period, are minimized, as a safety factor, and the gasses are completely consumed by the. end of the designated period of use or demand.
• any vehicle can be powered by both a combination of hydrogen and oxygen or other combustible materials created on demand, on an as needed basis.
• the use of non-potable water, or sea water greatly enhances the process, such that water reservoirs located within the vehicle can be replenished at the seashore or just about anywhere with any form of water, potable or not.
• the fail-safe mechanical monitoring system indicates the gas pressure, temperature, flow-rate, water level, and output volumes, which may be automatically or manually controlled.
• the non-potable water is seeded with sodium chloride and other base salts to eliminate bacteria and diseases.
• Ultra-Violet light is also used to eliminate bacteria, that may be present and the entire system is sanitized by filtering and straining of the aqueous solution on a continuous basis.
• Figure 1 Depicts the oxygen and hydrogen generator crucible as might be depicted in the preferred embodiment of the present invention for example.
• the drawing depicts the two the invention's usage of nickel wire on the one side and the use of tungsten wire on the other side, each wire sandwiched between a pair of perforated solid nickel plates.
• Figure 2 Depicts the oxygen or Cathode side of the gas generator and the component configuration of the cathode as might be found in the preferred embodiment of the present invention for example.
• Figure 3 Depicts the hydrogen or Anode side of the gas generator and the component configuration as might be found in the preferred embodiment of the present invention for example.
• Figure 4 Depicts the Dual Power Supply and Pulse Modulator for the present invention as might be found in the preferred embodiment for example.
• Figure 5 Depicts the hydrogen and oxygen gasses under storage after creation including the recirculation pump, the vacuum pumps for each side of the crucible and the catalytic water feed as be found in the preferred embodiment of the present invention for example.
• Figure 6 Depicts the hydrogen and oxygen storage tanks as depicted in Figure 5 with the addition of the H2 and 02 combiner chamber resulting in the burnable gas mixture as might be found in the preferred embodiment of the present invention for example.
• Figure 7 Depicts the pressure pumps as might be found in the preferred embodiment of the present invention for example.
• Figure 8 Depicts the flash guard or flash back suppressor as might be found in the preferred embodiment of the present invention for example.
• Figure 9 Depicts the Combiner Chamber that is used to recombine the H2 and 02 in the preferred embodiment of the present invention for example.
• Figure 10 Depicts the System Control Console Hardware as might be found in the preferred embodiment of the present invention for example.
• Figure 11 Depicts the Flow Chart of the Fail-Safe monitoring system as might be found in the preferred embodiment of the present invention for example.
• FIG. 12 Depicts the Tungsten Feed Assembly that might be found in the preferred embodiment of the present invention for example.
• Figure 13 Depicts the Automated Metal Wire Feed Assembly that might be found in the preferred embodiment of the present invention for example.
• Figure 14 Depicts the Magnetic Steering and Ionic Mass Guidance System that might be in the preferred embodiment of the present invention for example.
• Figure 15 Depicts the System Flow Chart as might be found in the preferred embodiment of the present invention for example.
• Figure 16 Depicts the Gas Storage System that might be found in the preferred embodiment of the present invention for example.
• Figure 17 Depicts the Seeded Water Catalytic Feed System as might be found in the preferred embodiment of the present invention for example.
• Figure 18 Depicts the Magnetic Ionic Alignment System as might ' be found in the preferred embodiment of the present invention for example.
• Figure 19 Depicts the Vacuum Pump Example that might be found in the preferred embodiment of the present invention for example.
• Figure 20 Depicts the Computer Monitor Screen that can control operations and failsafe shut downs from a remote location as might be found in the preferred embodiment of the present invention for example.
• Figure 21 Depicts the Remote Monitoring Station Console as might be found in the preferred embodiment of the present invention for example.
• Figure 22 Depicts a simple Plasma Generated Chemical Accelerator as might be found in the preferred embodiment of the present invention for example.
• Figure 23 Depicts the Effective Ratios of H2 and 02 when bonded by various metals, as might be found in the preferred embodiment of the present invention for example.
• Figure 24 Depicts the revised Periodic Table identifying combining of Various Metals under the Arno Vigen Scrunched Cube Model as might be found in the preferred embodiment of the present invention for example.
• Figure 25 Depicts the Invention Accelerator Example as might be found in the preferred embodiment of the present invention for example.
• Figure 26 Depicts the Arno Vigen Scrunched Cube - Hydrogen Bonding Examples of the preferred embodiment of the present invention for example.
• Figure 27 Depicts the Chemical Formulas suggesting the reactions found on the Anode Side and the Cathode Side as might be found in the preferred embodiment of the present invention for example.
• Figure 28 Depicts the combining of elements found in the Arno Vigen Scrunched Cube Example of the redrawn Periodic Table as might be found in the preferred embodiment of the present invention for example.
• Figure 29 Depicts the Summary of the Invention as might be found in the preferred embodiment of the present invention for example.
• Figure 1 depicts (101) the Cathode (02) side of the (102) Crucible (ceramic container) comprising said (103) Ceramic Insulators, (104) Perforated Nickel Plates, (105) the Nickel wire, comprising (106) an open filament, and (107) the Anode Side of the (102) Crucible (ceramic container), comprising said (108) Ceramic Insulators, (108) Tungsten Wire, (109) a closed filament, and (1 10) Perforated Nickel Plates, all submerged in (111) an aqueous solution comprising H20 and KOH.
• Figure 2 depicts (201) a Detailed image of the Cathode Side - Oxygen Side (O) of the Ceramic Crucible, comprising (202) the Ceramic Insulators, (203) the Mesh Nickel Plate (connected to the Anode Side of the Power Supply), (204) the Nickel Wire (connected to the Cathode Side of the Power Supply).
• Figure 3 depicts (301) a Detailed image of the Anode Side - Hydrogen Side (H2) of the Ceramic Crucible, comprising (302) the Ceramic Insulators, (303) the Mesh Nickel Plate (Closed Filament), (304) the Tungsten Wire (connected to the Anode Side of the Power Supply).
• H2 Anode Side - Hydrogen Side
• Figure 3 depicts (301) a Detailed image of the Anode Side - Hydrogen Side (H2) of the Ceramic Crucible, comprising (302) the Ceramic Insulators, (303) the Mesh Nickel Plate (Closed Filament), (304) the Tungsten Wire (connected to the Anode Side of the Power Supply).
• Figure 4 depicts (401) the -24VDC Pulse Modulated Power Supply Comprising an Anode Side and a Cathode Side, AND (402) the Dual 200-800VDC Pulsed Arc Voltage Power Supply comprising a + Cathode Side individual Power Supply, and a - Anode Side individual Power Supply.
• Figure 5 depicts (501) Cathode Side (02) Gas Pump, comprising a (502) Flash Suppressor, a (503) outlet hose, a (504) Oxygen Storage Tank, a (505) submerged Filtration Unit, a (506) Anode Side (H2) Gas Pump, further comprising a (507) Flash Suppressor, a (508) outlet hose, a (509) Hydrogen Storage Tank, a (510) submerged Filtration Unit, a (51 1) Water Bath Chamber comprising H20 and a Catalytic, a (512) Circulation Pump, as well as a (513) Water Supply for the Fuel Stock.
• Figure 6 depicts the same component part as Figure 5 herein and further comprises (600) the H2 + 02 Combiner to supply fuel to an external device such as a car, truck, or other form of vehicular transportation.
• Figure 7 depicts a commercially made Hydrogen Diaphragm Compressor for example.
• Figure 8 depicts a commercially available Flash Guard for example that might be found in the preferred embodiment of the present invention for example.
• Figure 9 depicts the detailed drawing of the Combiner depicted in Figure 6 herein above as (600).
• the Combiner Chamber is comprised of (901) the H2 Input Port, (902) the 02 Input Port, (903) the Exhaust, (904) the Bladder, (905) the Flashback Suppressor, (906) a Flow Control on the 02 Input Side and (907) the Output Port with the Combined H2 + 02 product ready to combust.
• Figure 10 depicts (1001) the System Control Console, comprising (1002) the Date, (1003) the Time of Day, (1004) the Water Level in the Crucible, (1005) the Water Temperature in the Crucible, (1006) the H2 Temp, (1007) the H2 Pressure, (1008) the 02 Temp, (1009) the 02 Pressure, and (1010) the
• the console can be remotely monitored and controlled by a Smart Phone or Hand-Held Device.
• Figure 1 1 depicts the Overall System Fail Safe Flow Chart Diagram. After initialization the systems routinely checks the H2 Gas Sensor for Leaks, the 02 Gas Sensor for leaks, the H2 Chamber
• FIG. 12 depicts the (1201) Ceramic Tungsten Feeder Assembly, comprising (1202) a Copper Sleeve, (1203) a series of Tungsten (or other preselected) Metal Tips for use as an alternative for the Anode Side of the System, as opposed to the Tungsten Wire and Feeder Assembly. This configuration is for high heat and maximum output capacity.
• Figure 13 depicts (1301) the Metal Filament Feeder Assembly as opposed to the Tip Feder Assembly depicted in Figure 12 above, comprising (1302) the Ceramic Container (one side), (1303) the Water Level, (1304) the Filament Wire itself, (1305) a Guide Wheel and Post, (1306) the Feedstock Spool, (1307) the Drive Belt or Chain Drive Assembly, (1308) the Stepper Motor.
• Figure 14 depicts (1401) the Magnetic Steering Assembly, comprising (1402) a Ceramic Encapsulated Circular Neodymium Magnet, (1403) an Encapsulated Stepper Motor, (1404) a non-metallic Drive Belt Assembly, (1405) a Fine-Tuning Bar Magnet (with Swivel), (1406) a Ceramic Casing Enclosure, and (1407) a Mounting Assembly.
• Figure 15 depicts the System Flow Chart indicating a Go-No Go condition during normal operations.
• Figure 16 depicts two hydrogen storage tanks found in the current model of the Honda FCX hybrid car.
• Figure 17 depicts (1701) a Salt Water Seeding Feed Tank, comprising (1702) Water Inlet Port, (1703) Salt Inlet Port, (1704) a Cube Float Water Shut Off Level Detector, (1705) a Salinity Measuring Instrument.
• Figure 18 depicts (1801) 18-A Ionic Misalignment of the H2 ions as might be found in the preferred embodiment, and (1802) 18-B Ionic Alignment after the ions are subjected to the Magnetic Field generated by the Magnetic Steering Assembly depicted in Figure 14 herein above.
• Figure 19 depicts (1901) the Vacuum Pumps Example as might be found in the preferred embodiment of the present invention for example.
• the Pumps comprise removing gas from the (1 02) Production Chamber, the (1903) Production Egress to H2 or 02 Gas, and (!904) the Initial Egress Removing Air.
• Figure 20 depicts (2001) the Computer Dashboard Image (identical to the one found in Figure 10 above with the exception that the control may be monitored and adjusted by a computer operator from a remote location via a satellite feed or wireless link.
• Figure 21 depicts (2101) a satellite fed control feed from (2102) a regional office of the Operator, comprising (2103) a satellite uplink antenna to an orbiting satellite, (2104) a H2 refueling pump owned by a major gasoline provider such as ARCO for example, comprising (2105) a satellite receiving antenna.
• Figure 22 depicts (2201) a Plasma Chemical Accelerator comprising (2202) a gas inlet port, (2203) a Plasma Source, (2204) a remote transport region, (2205) a gas buffer or flashback suppressor, (2206) a Main Processing Chamber, and (2207) a Vacuum Pump, as might be found in the preferred embodiment of the present invention for example.
• Figure 23 depicts (2301) the Effective Ratios of Hydrogen and Oxygen with a Metalloid or Metal, comprising (2302) Hydrogen Gas, (2303) Metal, and (2304) Oxygen Gas, as might be found in the preferred embodiment of the present invention for example.
• Figure 24 depicts Figure 45 of the Arno Vigen Scrunched Cube Model of the Realignment of the Periodic Table of the Elements incorporated herein by reference thereto as if fully contained herein.
• Motomagnetic Endcap (2402) a Circle around the Groupings EO l , E02, and E03 depicting Equatorial 90 Group with High Electrical Conductivity.
• Figure 25 depicts (2501 ) the Coherent Light Source Model, comprising (2502) the Magnetic Guide,
• the Laser Light Tube acts to accelerate the ions in the preferred embodiment of the present invention for example at a specified wavelength to match the resonant frequency of the ionic mass being affected in this example.
• Figure 26 depicts (2601) the H20 and H202 Electron Settling Positions according to the Arno Vigen Scrunched Cube Model, comprising (2602) the Hydrogen Atom offering a Proton to Bond with an Oxygen Atom to achieve a shared Bond, further comprising (2603) depicting H202 with the Oxygen and Hydrogen sharing a Bond derived from the Magnetic Steering of the Ionic Mass.
• Figure 27 depicts the Chemical Formulae that allows the present invention to release Hydrogen on the one side of the crucible and Oxygen on the opposite side of the same crucible with a result of pure H2 gas being released on the H2 side of the crucible.
• Figure 28 depicts the Arno Vigen Scrunched Cube Example of diverse Cathode and Anode choices with various metals and their counterparts to achieve the desired end results in the preferred embodiment of the present invention for example.
• Figure 29 depicts a summary of the present invention and the advantages of the invention over prior art teachings previously cited on the Background of the Invention Listings pages that are incorporated within the present invention by disclosure herein.

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• Chemical & Material Sciences (AREA)
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• Physics & Mathematics (AREA)
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• Combustion & Propulsion (AREA)
• Spectroscopy & Molecular Physics (AREA)
• Analytical Chemistry (AREA)
• Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
• Engine Equipment That Uses Special Cycles (AREA)
• Plasma Technology (AREA)
• Water Treatment By Electricity Or Magnetism (AREA)

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• 2018
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