WO2011022761A1 - Method and apparatus for plasma decomposition of methane and other hydrocarbons - Google Patents
Method and apparatus for plasma decomposition of methane and other hydrocarbons Download PDFInfo
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- WO2011022761A1 WO2011022761A1 PCT/AU2010/001076 AU2010001076W WO2011022761A1 WO 2011022761 A1 WO2011022761 A1 WO 2011022761A1 AU 2010001076 W AU2010001076 W AU 2010001076W WO 2011022761 A1 WO2011022761 A1 WO 2011022761A1
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- WIPO (PCT)
- Prior art keywords
- cell
- plasma
- hydrocarbon material
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- cathode
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/08—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor
- B01J19/087—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor employing electric or magnetic energy
- B01J19/088—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor employing electric or magnetic energy giving rise to electric discharges
-
- 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
- H05H1/48—Generating plasma using an arc
-
- 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
- C01B3/22—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by decomposition of gaseous or liquid organic compounds
- C01B3/24—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by decomposition of gaseous or liquid organic compounds of hydrocarbons
-
- 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
- H05H1/48—Generating plasma using an arc
- H05H1/50—Generating plasma using an arc and using applied magnetic fields, e.g. for focusing or rotating the arc
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/08—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor
- B01J2219/0873—Materials to be treated
- B01J2219/0875—Gas
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/08—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor
- B01J2219/0873—Materials to be treated
- B01J2219/0877—Liquid
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/02—Processes for making hydrogen or synthesis gas
- C01B2203/0266—Processes for making hydrogen or synthesis gas containing a decomposition step
- C01B2203/0272—Processes for making hydrogen or synthesis gas containing a decomposition step containing a non-catalytic decomposition step
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/08—Methods of heating or cooling
- C01B2203/0805—Methods of heating the process for making hydrogen or synthesis gas
- C01B2203/0861—Methods of heating the process for making hydrogen or synthesis gas by plasma
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/12—Feeding the process for making hydrogen or synthesis gas
- C01B2203/1205—Composition of the feed
- C01B2203/1211—Organic compounds or organic mixtures used in the process for making hydrogen or synthesis gas
- C01B2203/1235—Hydrocarbons
- C01B2203/1241—Natural gas or methane
Definitions
- the present invention relates to plasma decomposition of methane and other hydrocarbons for producing hydrogen and synthetic carbon-free gas through plasma reforming process
- Hydrocarbon fuels are the most commonly used as energy sources . Each molecule of those fuels contains hydrogen and carbon as the major components. Other elements or molecules in those fuels depend of the fuel type - from simplest methane or propane gases to more complicated molecules of crude oil . Fossil fuels developed over geological time represent the world' s energy capital . Many renewable forms of energy-those derived from wind, solar or marine (tidal, wave) sources, must be used as they are produced;
- renewable energy may have some energy storage potential such as: hydro energy is contained in potential energy of stored water in lakes or rivers and geothermal energy is retained underground until required. Decarbonisation of economies is occurring as the shift is progressively made from using coal to using oil and, most recently, to natural gas, i.e. to hydrocarbons containing less carbon. This shift follows technology progress on energy efficiency and lower scale polluting solutions in rising demand for energy. Hydrocarbons are predominantly used in thermodynamic conversion of energy. Hydrogen as a component of hydrocarbon fuel is a major carrier and source of energy. It has universal usage as the source such as thermodynamic in combustion , electric conversion in fuel cells, nuclear in fission and lately developing possibility for fusion experiments .
- Hydrogen is the most efficient when it comes to conversion to useful energy forms such as thermal; mechanical and electrical. Hydrogen is some 39% more efficient than fossil fuels, without the pollution. It can be considered as the most effective energy storage in any scale . When fire hazards and toxicity are taken in to account, hydrogen is the safest due to highest buoyancy - evaporation of all gases and being base of most of biological matter.
- hydrocarbons decomposition will play a major role as the commonly accepted source and storage of H 2 hydrogen and other synthetic carbon-free gases .
- Major consumption of hydrogen so far has been in the petroleum industry for the refining and upgrading of crude petroleum and in chemical industry for the manufacture of fertilizers, methanol and a variety of organic chemicals.
- Hydrogen basic physical properties ensure future wide usage as an energy source and carrier of high caloric value .
- Wide variety of applications can be adapted to hydrogen use as the source or medium of energy.
- Hydrogen is very reactive element and does not exist in elementary form in natural environment of the Earth. It always comes in molecular arrangement of clusters. Stability of those clusters depends of stability of all elements included. Hydrogen is bonded with other elements not only as single molecule bond but rather as oscillating clusters of molecules bonded together.
- the substantial cooperative strengthening of the hydrogen bond is dependent on long range interactions and strength of each bond in the cluster encourages larger clusters formation for the same average bond density and potential.
- carbon release can be achieved by exposing clusters to high temperatures .
- Unstable hydrogen in a cluster which bond with carbon has been broken when exposed to high temperatures, will tend to react with predominantly electrically opposite element in its proximity. In a vacuum environment it will form hydrogen molecule cluster H 2 . Breaking one bond through exposing hydrocarbon to heat generally weakens those around. If exposed to the oxygen environment, exposed hydrogen will violently react in combining with oxygen through combustion. Exothermic reaction further breaks the hydrogen-carbon bond in hydrocarbon and exposes more hydrogen to run off
- Plasma can essentially improve situation .
- Plasma is a high-density source of energy, which can cover process enthalpy and provide optimal temperature range to eliminate kinetic limitations .
- Hydrocarbon decomposition through plasma discharge demonstrates a high specific productivity of decomposition rate comparing with steam reforming or partial oxidation processes .
- the object of the invention is to provide an improved apparatus and method for providing stable and controllable plasma for the purpose of generating hydrogen via plasma decomposition of hydrocarbon materials.
- Plasma electrical charge ionises hydrocarbons and enables lower temperatures of hydrocarbon decomposition through resonating bonds in the cluster with a highly energetic rate and resulting in more effective breakage of hydrogen-carbon bond.
- electrical conductivity of input hydrocarbon gas can be converted through plasma discharge in to high conductivity physical properties.
- hydrocarbon compounds can be used in plasma decomposition according to this invention where carbon, as the by-product is released in solid soot state and is easily removable and ready for usage in different applications or safe storage.
- characteristics of the process are simplification of the decomposition, no need for catalyst so no catalyst deactivation, scalable size, on demand usage, mobile equipment friendly and low cost applications .
- hydrogen gas is generated at a cathode with much of the space between the cathode and an ion charge screen layer being formed as double layer . Ions of hydrogen migrate through the screen to discharge on the cathode and produce hydrogen gas.
- the high localised voltage can result in spot temperatures greater than 3000 0 C. Such heating results in instant decarbonisation on a wide scale of hydrocarbons.
- the invention provides a process for producing hydrogen from hydrocarbon material by plasma treatment, the process comprising:
- plasma generated at the electrodes can be stabilised, rather than occurring in short bursts, by controlling the location of the plasma with electrical and magnetic fields.
- the structure of the ion screen layers surrounding the cathode is maintained with largely hydrogen gas filling the gap between the cathode and the ion screen layers .
- Hydrogen ions continue to migrate through the screen to form hydrogen gas and plasma is constantly initiated at the cathode for stabilisation on the further electrodes. Ions and other components of the hydrocarbon migrate to the anode and form carbon soot and additional impurities removed in further processes .
- Plasma can be initiated and maintained through capacitive discharge between electrodes , laser breakage of dielectric gas and maintained through lower voltage capacitive discharge or magnetron or radio frequency applied pulses .
- the relocated plasma is maintained between the further electrodes without an ion screen layers and, therefore , without a dielectric surrounding the
- the hydrocarbon material treated by plasma are ionised and the ions produce carbon soot, other impurities found in particular hydrocarbons and hydrogen or synthetic carbon-free gas at respective electrodes .
- the location of the plasma may be controlled by applying a second electrical potential between each further electrode and the anode.
- the location of the plasma may also be controlled by magnetic fields and, preferably, the magnetic fields are produced by permanent magnets .
- the cathode comprises the cell body in contact with the ion screen layers and the anode comprises a metal and is electrically isolated from the cathode.
- the cathode As a body of a decomposing cell , the plasma generated between the cathode and anode is encouraged to spatially disperse away from the points of closest geometrical proximity between the anode and the cathode, thereby assisting to spatially distribute the plasma around the decomposing cell.
- the first electrical potential may be in the range of 120 to 400 volts, but preferably is 160 to 380 volts with capacitor bank of 60 to 160 ⁇ F.
- the further electrodes may be located in close proximity to the cathode so the second electrical potential applied to the two or more further electrodes encourages plasma generated between the cathode and the anode to transfer to between the further electrodes and the anode .
- step (c) involves applying a second electrical potential to the further electrodes in contact with the ion screen layers and in close proximity to the first electrodes, the second electrical potential
- the second electrical potential 40 40 to 200 volts and, more preferably, is 55 to 100 volts.
- the process may further involve removing oxygen- containing gas from the plasma treatment cell prior to step (a) . This may be achieved by purging with an inert gas, or with the hydrocarbon fluid or by applying a vacuum to the cell.
- the present invention also provides an apparatus for producing hydrogen gas from hydrocarbon material comprising:
- hydrocarbon material the cell comprising an electrically conductive material
- hydrocarbon material input means for supplying the hydrocarbon material to the volume and required pressure
- gas collection means for conveying hydrogen gas and other decomposed elements away from the cell;
- cathodes positioned within the cell for immersion within hydrocarbon contained within the cell and for fast switching initiation plasma;
- the further electrodes may define a planar surface area for spatially distributing plasma between the surface area and the cell.
- the further electrodes may include an array of apertures for increasing the surface area of the electrode to enhance spatial distribution of plasma.
- the cell may comprise an anode for forming plasma in conjunction with the cathode , the cathode being
- the apparatus may include a hydrocarbon material flow member for reducing the effect of turbulence caused by moving around the further electrodes and pre-heating.
- the hydrocarbon material flow member may define a first channel within the cell for enabling temperature directing of hydrocarbon material when passing through the plasma when contained within the cell .
- the hydrocarbon material flow member may be formed as a sleeve for location within the cell volume between the further electrodes and adjacent cell wall, the sleeve may be open at one end and define a volume between the ends that comprises the channel and defines the second channel between the sleeve and the adjacent cell wall such that hydrocarbon material is able to flow from the channel around an end of the sleeve and into the plasma filled area.
- the sleeve may be formed from magnetically conductive material and, in situ within the cell, is connected to the cell.
- the hydrocarbon material is a gas and/or liquid containing hydrocarbons .
- the hydrocarbon material may be natural gas , methane , propane , butane or a refined oil product .
- Figure 1 is a schematic diagram of an apparatus in accordance with an embodiment of the invention .
- FIG. 2 is a schematic isometric view of an embodiment of a plasma hydrocarbon decomposing cell for use with the apparatus of Figure 1. Detailed Description of an Embodiment
- a hydrocarbon material decomposition process in accordance with an embodiment of the present invention may be performed with an apparatus in accordance with an embodiment illustrated in Figure 1.
- the apparatus comprises an hydrocarbon
- decomposing cell 100 linked to gas separators 50 by conduits 40 and off-gas lines 16.
- the separators 50 are linked to an reservoir 60 by a further conduit 40 to ensure that the separators remain filled.
- Thermocouples and pressure sensors 70 are located respectively in the cell 100 and in a separator 50 to monitor the temperature and pressure of the process .
- two separate power sources provide electrical energy for the hydrocarbon decomposition process.
- the cell 100 comprises two stacked upper and lower parts 11IA and 11IB.
- Each part 11IA and 11IB has a cylindrical body 112 with outwardly extending end flanges 114 at each end of the body 112.
- the parts HlA and HlB are formed of stainless steel 316L.
- the stacked parts HlA and HlB are fastened together to form a substantially continuous cylindrical volume within the cylindrical bodies 112. Respective ends of the parts IHA and HlB are closed by covers 113 such that the volume is fluid-tight.
- a disc 115 of virgin Teflon® having the same diameter as the flanges 114, is disposed between the covers 113 and the flanges 114.
- the cell 10 is formed of electrically conductive material to form an electrode.
- a plasma electrode 120 extends into a volume defined by the cylindrical body 112 through the cover 113.
- the plasma electrode 120 is electrically isolated from the cover 113 by an isolator 122 to prevent short circuiting between the cell 10 and the plasma electrode 120.
- Plasma relocating electrodes are provided in the form of plasma relocating cathodes 130 and plasma
- anodes 132 are formed of STAVAX® stainless steel with magnetic properties.
- One or more cathodes 130 and one or more anodes 132 may be alternately supported along two generally parallel support rods 140.
- the support rods 140 are electrically conductive and the cathodes 130 are electrically connected to one of the support rods 140, but electrically isolated from the other support rod 140.
- the anodes 132 are electrically connected to the other support rod 140, but electrically isolated from the support rod 140 to which the cathodes 130 are
- insulating mounts that comprise respective silicone gaskets and 0-rings .
- the plasma relocating cathodes 130 and anodes 132 are generally disc-shaped to fill a substantial cross- sectional area of the cylindrical body 112. However, the plasma relocating cathode 130 in closest proximity to plasma initiating anode electrode 120 is formed with hole, approximately 4 millimetres in diameter, adjacent to the plasma initiating anode 120.
- plasma relocating cathode 130 and plasma relocating anode 132 and permanent magnets 138 ensures that the electrical field generated by the cathodes 130 and the anodes 132 and the magnetic field generated by the
- permanent magnets 138 causes relocation of plasma from the plasma initiation electrode 120 to the plasma relocating electrodes 130, 132.
- the cell 100 includes a conductive sleeve 142 that is positioned in a lower part 11IB between the plasma relocating anodes and cathodes 130 and 132 and the cell body 112.
- the sleeve 142 has a cylindrical form with top end attached to body 11IB forming part of body and, at bottom end, four tabs 144 that project outwardly from the sleeve 142.
- the tabs 144 are located at 90 degree intervals around the rim of the sleeve 142 and diverge outwardly from the sleeve 142 such that the distance between free ends of opposed tabs 144 is slightly greater than the inner diameter of the cell body 112.
- the sleeve 142 acts as an electrode; it forms a path for magnetic flux with anodes and cathodes 130 and 132 and mounted permanent magnets 138, such that plasma extends between the sleeve 142 and the anodes and cathodes 130 and 132.
- Significant quantities of hydrogen gas are produced in the course of operating the cell .
- decomposed hydrogen manifests as gas mixed with carbon soot that rise from the anodes and cathodes 130 and 132 and require further cooling and filtering through wet and dry filtration outside the cell.
- the sleeve 142 aids circulation of hydrocarbon material within the cell 100. Specifically, hydrocarbon circulation through the volume defined by the sleeve 142, force moving hydrocarbon downwardly in a channel 146 between the sleeve 142 and the cell body 112 and around the lower rim 148 of the sleeve 142 and back upwardly through the sleeve 142 volume.
- a top cover (not shown) of the cell 10 includes two apertures to which off-gas conduit lines 16 are connected for removing hydrogen gas and carbon soot mixture from the cell.
- the off-gas conduit lines 16 extend respectively into the separators 50 so that the cell off-gas bubbles through a liquid solution contained within the separators 50. After removing oxygen-containing gas from the cell 100, the cell 10 is filled with hydrocarbon,
- plasma discharge is performed by applying an electrical potential between the electrodes 160 and 380V and is supported by capacitor bank .
- the electrical potential is applied by a typical power supply with a MOSFET transistor control such that an electrical
- the current supplied to the apparatus will vary depending on the scale of the apparatus .
- the current applied to the apparatus shown in Figures 1 and 2 may range from 40 to 200A.
- the current is 50 to 85A.
- Direct electrical potential is applied between the plasma electrodes 120 and the cell body 112.
- An electrical potential in the range 120 to 400V may be applied, but an electrical potential in the range 160 to
- 380V is suitable to initiate plasma formation.
- the charge application of an electrical potential to the plasma electrodes 120 and the cell body 112 continues and increases the amount of hydrogen gas and carbon soot mixture generated. Hydrogen ions are formed and migrate to the cell body 112, and C- ions migrate to the electrode 120.
- This ionic flux allows current to pass through the hydrocarbon material and produces hydrogen at the plasma discharge surface.
- This mechanism is characterized by low activation energy and high reaction rate .
- Non- equilibrium plasma is obtained in arc discharges via fast mixing of plasma jet and reactants in the high temperature zone of discharge.
- Proposed mechanism of the plasma effect on CH 4 decomposition follows - thermal acceleration related with local preheating on to entry of the hydrocarbon material in the cell through channel 146 between body 112 and sleeve 142 cause radical acceleration.
- thermal acceleration is provided and directly related to local overheating into ions CH 3 , H , CH 2 generated by plasma from supply gas , autocatalytic methane decomposition on the surface of carbon soot particles generated in plasma zone, ion acceleration caused by ion-molecular chain reaction of methane decomposition.
- the overall cathode reaction is strongly enhanced by the hydrogen ions H + . Accordingly, the cathode reaction will last until all the hydrogen disappears from the solution. Simultaneously, the carbon will collect around the electrode, without depositing on it, to form a sleeve or screen with a negative potential that holds itself few nanometers from the surface of the plasma electrode . In this situation , the space between the screen of carbon ions and the plasma electrode becomes filled with H + and H 2 + which acts as a dielectric. In spite of this screen of carbon ions, ions of hydrogen, being much smaller, will continue to work through the screen of carbon ions without difficulty to move towards and deposit on the plasma cathode 112 and generate gaseous hydrogen.
- the amount of the hydrogen generation increases significantly, so much that it blocks further hydrogen ions from reaching the plasma electrode 112.
- the plasma causes the potential to drop locally as the electrical current in the plasma bridges the space between the plasma electrode 120 and the carbon ion screen.
- the plasma is stabilised by applying an electrical field that attracts plasma away from the plasma initiating electrode 120.
- the electrical field is applied by applying an electrical potential to the plasma
- relocating electrodes 130 and 132 e.g. 12 to 300V DC.
- the new path relocates and scatters the plasma from between the plasma electrodes 120 and the cell body 112 to between the plasma relocating electrodes 130 and 132 and the cell body 112.
- the plasma is spatially distributed through a many times greater volume of the cell 100, thereby forming a bigger decomposition effect of passing through hydrocarbon material .
- Control of plasma and output of generated gases is achieved through varying the current applied to the plasma relocating electrodes 130 and 132.
- This volume of solution also assists to maintain a stable cell 100 temperatures by circulating solution through the cell 100 and applied current of plasma relocating electrodes .
- Associated equipment is electrically isolated from the cell 100 and the ground connection is protected by a metal enclosure in which the apparatus is installed.
Abstract
Description
Claims
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AU2010286322A AU2010286322B2 (en) | 2008-05-16 | 2010-08-23 | Method and apparatus for plasma decomposition of Methane and other hydrocarbons |
US13/769,405 US8911596B2 (en) | 2007-05-18 | 2013-02-18 | Method and apparatus for plasma decomposition of methane and other hydrocarbons |
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AU2009904061 | 2009-08-25 | ||
AU2009904061A AU2009904061A0 (en) | 2009-08-25 | Method and apparatus for plasma decomposing of methane and other hydrocarbons | |
AU2009905592 | 2009-11-13 | ||
AU2009905592A AU2009905592A0 (en) | 2009-11-13 | Method and apparatus for generating hydrogen gas |
Related Parent Applications (3)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US12/992,928 Continuation-In-Part US8409422B2 (en) | 2007-05-18 | 2008-05-16 | Method and apparatus for producing hydrogen and oxygen gas |
PCT/AU2008/000693 Continuation-In-Part WO2008141369A1 (en) | 2007-05-18 | 2008-05-16 | Method and apparatus for producing hydrogen and oxygen gas |
US99292810A Continuation-In-Part | 2007-05-18 | 2010-12-29 |
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US13/769,405 Continuation-In-Part US8911596B2 (en) | 2007-05-18 | 2013-02-18 | Method and apparatus for plasma decomposition of methane and other hydrocarbons |
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WO2011022761A1 true WO2011022761A1 (en) | 2011-03-03 |
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PCT/AU2010/001076 WO2011022761A1 (en) | 2007-05-18 | 2010-08-23 | Method and apparatus for plasma decomposition of methane and other hydrocarbons |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2020121287A1 (en) | 2018-12-14 | 2020-06-18 | Pixel Voltaic Lda | Catalytic methane decomposition and catalyst regeneration, methods and uses thereof |
GB2590083A (en) * | 2019-12-04 | 2021-06-23 | Ananda Shakti Tech Ltd | Plasma generator |
US11701632B2 (en) | 2018-12-10 | 2023-07-18 | Ekona Power Inc. | Method and reactor for producing one or more products |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US11701632B2 (en) | 2018-12-10 | 2023-07-18 | Ekona Power Inc. | Method and reactor for producing one or more products |
WO2020121287A1 (en) | 2018-12-14 | 2020-06-18 | Pixel Voltaic Lda | Catalytic methane decomposition and catalyst regeneration, methods and uses thereof |
GB2590083A (en) * | 2019-12-04 | 2021-06-23 | Ananda Shakti Tech Ltd | Plasma generator |
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