Abstract: A hydrogen generating apparatus having a fuel feeding part, a water feeding part for fuel reforming, an oxidant gas feeding part, a reforming catalyst body, a heating part for the reforming catalyst, a CO shifting catalyst body and a CO purification catalyst body is provided wherein the reforming catalyst body, the CO shifting catalyst body and the CO purification catalyst body are sequentially ordered from the fuel feeding part toward the downstream side, and wherein a shifting catalyst of the shifting catalyst body contains as one component at least a platinum group-type catalyst.

Abstract: There is provided a reforming apparatus which shows high efficiency and excellent operation-starting performance, in spite of its compact body and simple structure.

Abstract: An apparatus and method to create a substantially pure hydrogen product stream before any subsequent purification steps. The apparatus provides a generally enclosed reaction vessel so as to reduce any extraneous exhaust materials from escaping. In addition, the apparatus includes a primary and a secondary reaction chamber which are generally held at equivalent or equal pressures while at substantially different temperatures. In addition, a reaction aid or cooperator is used to increase the production of the hydrogen product stream and to also increase the purity of the hydrogen product stream. The method includes using a two chamber apparatus along with the reaction cooperator to increase the hydrogen production and purity and recycling the reaction cooperator.

Abstract: Process and apparatus for the preparation of synthesis gas by catalytic steam and/or CO2 reforming of a hydrocarbon feedstock comprising the following steps:

Abstract: A reforming and hydrogen purification system operating with minimal pressure drop for producing free hydrogen from different hydrogen rich fuels includes a hydrogen reforming catalyst bed in a vessel in communication with a core unit containing a hydrogen permeable selective membrane. The vessel is located within an insulated enclosure which forms an air inlet passageway and an exhaust passageway on opposite sides of the vessel. Air and raffinate pass through a burner within the air inlet passageway, providing a heated flue gas to heat the catalyst to the reaction temperature needed to generate free hydrogen from the feedstock. The burner flue gas flows laterally over and along the length of the bed between the input and output ends of the bed. Hydrogen is recovered from the core for use by a hydrogen-consuming device such as a fuel cell. The remaining unrecovered hydrogen in the reformed gases is contained in raffinate and is used to supply process heat via the burner.

Abstract: A compact steam reformer produces hydrogen to power a fuel cell, such as can be used in a vehicle. The steam reformer includes a first channel, at least partly coated with a steam reforming catalyst, and a second channel, at least partly coated with a combustion catalyst, the channels being in thermal contact with each other. Heat from the combustion is used in the steam reforming reaction. The steam reformer may be provided as a stack of strips defining steam reforming channels which alternate with combustion channels. The reformer may also include a set of modules, connected in series, each module including a stack of strips as described above. The steam reformer preferably also includes a channel wherein a water-gas shift reaction occurs, to convert carbon monoxide, produced by the reformer, into carbon dioxide.

Abstract: Process and apparatus for the preparation of synthesis gas by catalytic steam and/or CO2 reforming of a hydrocarbon feedstock comprising the following steps:

Abstract: A fuel cell power plant (110) has a fuel cell stack assembly (CSA) (16) including an anode (18), and a fuel processing system (FPS) (120) providing a hydrogen-rich reformate/fuel stream (34, 134, 62) for the anode (18) of the CSA (16). A relatively active metal catalyst is associated with one or both of the anode (18) and the FPS (120), and is subject to degradation by the presence of even low levels, e.g. 100 ppb to 5 ppb-wt. reformate, of sulfur in the fuel stream. A guard bed (70) containing a guard material (72) is provided in the FPS (120) for protecting the relatively active metal catalysts by adsorbing, and further reducing the level of, sulfur in the fuel stream. The guard material (72) is a metal or metal oxide capable of forming a stable sulfide in the presence of low levels of H2S in the fuel stream (34), and is preferably selected from the group consisting of: ZnO, CuO on CeO2-based support, NiO on CeO2-based support, and Cu/ZnO.

Abstract: A method is provided for maintaining low concentration of carbon monoxide in a fuel processor product hydrogen stream during transient operation with a residential fuel cell, particularly during increases in load demand (turn-up). Algorithms have been developed for controlling the air flow to a preferential oxidation reactor and for controlling the rate of direct water injection for rapid steam generation in a water gas shift reactor.

Abstract: A compact steam reformer produces hydrogen to power a fuel cell, such as can be used in a vehicle. The steam reformer includes a first channel, at least partly coated with a steam reforming catalyst, and a second channel, at least partly coated with a combustion catalyst, the channels being in thermal contact with each other. Heat from the combustion is used in the steam reforming reaction. In another embodiment, the gas streams feeding the reforming and combustion channels pass through a valve which reverses the gas streams periodically. The combustion channel becomes the reforming channel, and vice versa, so that carbon deposits in the former reforming channel are burned off. This arrangement enables the reforming reaction to continue indefinitely at peak efficiency.

Abstract: An arrangement for generating a hydrogen-containing gas from a hydrocarbon-containing medium includes a multi-stage reforming unit that is connected to a multi-stage carbon monoxide removal unit by a heat-conducting separating medium. The stages of the reforming unit, in an ascending order relative to the gas flow direction in the reforming unit, are in a thermal contact with stages of the carbon monoxide removal unit, in a descending order relative to the gas flow direction in the carbon monoxide removal unit.

Abstract: A fast start-up catalytic reformer for producing hydrogen-rich reformate from hydrocarbon fuel includes a reactor having an inlet for receiving a flow of fuel and a flow of air, a reforming catalyst disposed within a reforming chamber in the reactor, and an outlet for discharging the produced reformate stream. An ignition device within the reactor tube ignites a first lean mixture in combustion mode to generate exhaust gases to warm the catalyst which also warms the wall of the reactor adjacent the catalyst. The reactor then switches over to a rich fuel/air mixture during reforming mode. A jacket concentrically surrounds the reactor, defining a mixing chamber therebetween which communicates with the reforming chamber via openings in the wall of the reactor. Fuel entering the reformer in combustion mode is injected directly into the reforming chamber to provide rapid warming of the catalyst.

Abstract: Process and reaction unit for isothermal shift conversion of a carbon monoxide containing feed gas, the process comprising the steps of

Abstract: An apparatus and a method of generating a carburizing atmosphere are provided which can stably generate a reformed gas containing carbon monoxide of high concentration that is suitably used as a carburizing atmosphere.

Abstract: Improved method for recovering hydrogen and carbon monoxide from hydrocarbon conversion processes are disclosed. A monolith catalyst reactor means is utilized in treating the waste gas stream from the hydrocarbon conversion process to assist in recovering hydrogen and carbon monoxide from the waste gas stream. The present invention also provides a method for improving the yield of hydrogen and carbon monoxide from a hydrocarbon conversion process utilizing a monolith catalyst reactor means.

Abstract: A method and apparatus for processing a hydrocarbon fuel comprises: a primary fuel processing reactor for converting a feed stream to a first reformate stream comprising hydrogen; a first hydrogen separator located downstream of the primary fuel processing reactor and fluidly connected thereto for receiving the first reformate stream, the first separator comprising a first membrane for separating the first reformate stream into a first hydrogen-rich stream and a first retentate stream; and a secondary fuel processing reactor fluidly connected to the first separator for receiving and converting the first retentate stream to a second reformate stream comprising hydrogen. A fuel cell power generation system includes the present apparatus and a fuel cell stack fluidly connected thereto for receiving hydrogen-rich streams therefrom.

Abstract: An autothermal reformer according to the principles of the present invention comprises a first stage that selectively receives a fuel flow, a first oxidant flow, and a steam flow. The first stage has a first portion of a catalyst bed. The fluids within the first stage are routed through the first portion of the catalyst bed and react. There is a second stage downstream from and communicating with the first stage. The second stage receives the fluids from the first stage and also selectively receives a second oxidant flow. The second oxidant flow and the fluids received from the first stage flow through a second portion of a catalyst bed and further react.

Abstract: A steam reformer that produces hydrogen gas from water and a carbon-containing feedstock, such as an alcohol or a hydrocarbon. The steam reformer includes a hydrogen-producing region, in which a mixed gas stream containing hydrogen gas and other gases is produced from water and a carbon-containing feedstock. The steam reformer includes a separation region, in which the mixed gas stream is separated into a hydrogen-rich stream containing at least substantially pure hydrogen gas, and a byproduct stream containing at least a substantial portion of the other gases. In some embodiments, the steam reformer is a vertically oriented fuel processor. In some embodiments, the separation region includes at least one hydrogen-selective membrane. In some embodiments, the steam reformer further includes a polishing region, in which the hydrogen-rich stream produced in the separation region is further purified. In some embodiments, the reformer includes an external metal or sealed ceramic shell.

Abstract: The present invention provides a method of steam reforming a hydrocarbon over a spinel-containing catalyst at short residence times or short contact times. The present invention also provides spinel-containing catalysts. Surprisingly superior results and properties obtained in methods and catalysts of the present invention are also described.

Abstract: A method for generating a hydrogen-containing product gas from liquid or gaseous hydrocarbons includes providing a reformer installation having a combustion space, a mixing chamber and a reformer unit. Partial oxidation of a first hydrocarbon stream with a first oxygen-containing gas stream is performed and a first product-gas stream containing hydrogen is formed, in the combustion space. A second hydrocarbon stream is reformed with water and a second product gas stream containing hydrogen is formed, in the reformer unit. The first product-gas stream and the second product-gas stream are mixed in the mixing chamber to form a third product-gas stream. The reformer unit is heated with the third product-gas stream.

Abstract: A reactor/purifier for generating pure hydrogen in a stack or array of pairs of alternatingly connected high and low pressure reactor chambers wherein a gas-porous turbulence-promoting screen structure washcoated with a steam-reforming catalyst is sandwiched between a planar hydrogen-selective palladium alloy membrane and a planar gas-impermeable heat-conducting metal plate within the high pressure reactor chamber of each high pressure reactor chamber; and wherein the catalyst-coated structure in each high pressure chamber is reacted with steam and hydrocarbon fuel, such as methane or syn/gas, and/or carbon monoxide at an appropriately controlled temperature of between about 200° C. to 650° C.

Abstract: There is provided is a process for preparation of synthesis gas, i.e. mixtures containing dihydrogen and oxides of carbon, from feedstocks containing methane and/or higher hydrocarbons having from about 2 to about 12 carbon atoms by an initial catalytic treatment of feedstock to provide a methane-containing gaseous mixture substantially free of compounds having 2 or more carbon atoms, and reforming the gaseous mixture at elevated temperatures using nickel-containing catalytic materials that are unusually active under mild conditions of conversion and resistant to deactivation. The process consists fundamentally in converting the higher hydrocarbon compounds to form a methane-containing gaseous mixture substantially free of compounds having 2 or more carbon atoms in an initial conversion zone containing a catalyst while controlling temperatures within the initial conversion zone to temperatures in a range of temperature downward from about 500° C. to about 300° C.

Abstract: A process for converting carbon monoxide and water in a reformate stream into carbon dioxide and hydrogen comprising: generating a reformate by reacting a hydrocarbon via partial oxidation, steam reforming, or both, including autothermal reforming; and promoting a water gas shift in the reformate in the presence of a platinum group metal selected from the group consisting of platinum, palladium, iridium, osmium, rhodium and mixtures thereof, supported on zirconium oxide. The platinum group metal advantageously may be supported directly on a monolithic substrate composed of zirconium oxide.

Abstract: A fuel cell system including a fuel reforming processor having a catalyst therein constructed and arranged to produce a reformate stream including hydrogen and carbon monoxide, a water gas shift reactor downstream of the fuel reforming processor and wherein the water gas shift reactor includes a catalyst therein constructed and arranged to reduce the amount of carbon monoxide in the reformate stream, a preferential oxidation reactor downstream of the water gas shift reactor and wherein the preferential oxidation reactor includes a catalyst therein constructed and arranged to preferentially oxidize carbon monoxide into carbon dioxide and to produce a hydrogen-rich stream, and a fuel cell stack downstream of the preferential oxidation reactor constructed and arranged to produce electricity from the hydrogen-rich stream, a first direct water vaporizing combustor constructed and arranged to combust fuel producing a high-temperature fuel combustion byproducts exhaust and to produce steam from water sprayed into th

Abstract: A fuel reforming method includes the step of supplying carbon-containing fuel and steam to a reactor filled with a fuel reforming catalyst and a CO2 absorbent and discharging CO2, and setting the absorbent at an absorption temperature, thereby converting the carbon-containing fuel into reformed fuel, and separating CO2 from the reformed fuel, the step of obtaining a product gas by oxidizing a portion of the reformed fuel and/or the carbon-containing fuel with an oxidizer, and heating the absorbent with this product gas to a regeneration temperature, thereby regenerating the absorbent and storing heat in this absorbent, and the step of supplying the carbon-containing fuel and steam to the reactor, thereby cooling, to the absorption temperature, the absorbent heated to the regeneration temperature, and converting the carbon-containing fuel into reformed fuel by heat energy stored in the CO2 absorbent. An apparatus for the method is also disclosed.

Abstract: A compact fuel processor for converting a hydro-carbonaceous fuel into hydrogen and carbon dioxide comprising in series a hydrocarbon converstion zone (5) for converting the hydro-carbonaceous fuel into a product gas comprising carbon monoxide and hydrogen, a water-gas shift reaction zone (6) containing a catalyst suitable for the water-gas shift conversion reaction, an auxiliary water-gas shift reaction zone (7) containing a catalyst suitable for the water-gas shift conversion reaction, and a carbon monoxide removal zone (8). The invention further relates to a fuel cell system comprising such a fuel processor and a fuel cell and to the use of such a fuel processor or such a fuel cell system.

Abstract: The invention is directed to a method of fueling gas turbines from natural gas reserves with relatively low methane concentrations. The invention permits the use of such reserves to be used to fuel gas turbines to generate electric power. The method of the invention includes providing a natural gas comprising not more than about 40 percent methane on a volume basis and mixing the methane of the natural gas with hydrogen gas to provide a hydrogen enhanced methane/hydrogen gas blend which has sufficient hydrogen to provide flame stability during burning. Thereafter, if required, the hydrogen enhanced methane/hydrogen gas blend is dehydrated to remove a sufficient amount of water to provide a flame stable hydrogen enhanced dehydrated methane/hydrogen gas blend. The hydrogen enhanced natural gas blend is used to fuel gas turbine generators.

Abstract: A reactor for autothermal reforming of hydrocarbons that allows a reduction of excess-air factor &phgr; during the reforming without resulting in a reduced conversion of the hydrocarbons in an end region of the reaction zone. The reactor includes at least one reaction zone in which is arranged at least one catalyst structure for the reformation so that the educts involved in the reformation are converted while flowing through the reaction zone. A heating device is included for heating the end region of the reaction zone to accelerate the conversion of the hydrocarbons.

Abstract: The present invention provides a CO2-selective membrane process that is useful for the purification and/or water gas shift reaction of a reformed gas, generated from on-board reforming of a fuel, e.g., hydrocarbon, gasoline, diesel, methanol or natural gas, to hydrogen for fuel cell vehicles. Another embodiment of the present invention is directed toward a composition comprising a hydrophylic polymer and at least one ammonium halide salt, the ammonium halide salt being present in an amount ranging from about 10 to 80 wt % based on the total weight of the composition. The composition is suitable in formation of a membrane useful for separating CO2 from a CO2-containing gas, particularly from an on-board reformed gas for the CO2-selective membrane process.

Abstract: A method of producing hydrogen by reforming a hydrocarbon or an aliphatic alcohol efficiently is disclosed together with an apparatus for implementing the method.

Abstract: A steam reformer for producing H2 from a low pressure hydrocarbon gas (preferably propane) using an improved gaseous hydrocarbon fuel and steam delivery system comprising two coaxial tubes, an outer tube for delivery of steam which is gradually reduced in diameter to form a truncated conical tip for the outflow of steam around the end of an inner tube for the outflow of gaseous hydrocarbon. The outflow ends of both tubes are positioned in the same plane perpendicular to their axis. The outflow end of the second tube is preferably also gradually reduced in diameter in order to provide higher velocity of gaseous hydrocarbon to be mixed with the steam entering the reformer for optimized yield of hydrogen by optimizing the mixing of the steam and gaseous hydrocarbon in order to optimize the yield of hydrogen for the optimized generation of wattage for the same fuel-cell power generating system.

Abstract: Preferred embodiments of the present invention generate a synthesis gas with a molar ratio of hydrogen to carbon monoxide of approximately 2:1 required for Fischer-Tropsch synthesis. Additional hydrogen produced in the steam reforming of methane beyond the requirements for the Fischer-Tropsch reaction is separated from the product gases of the reformer by the use of a hydrogen permeable membrane. Air is passed over the outside of the tube. As the hydrogen contacts the air, it is combusted with oxygen in the air to form water and release the heat necessary to drive the steam reforming reaction.

Abstract: An apparatus for steam reforming of hydrocarbons, the apparatus comprising a vessel defining a combustion chamber. The combustion chamber has a burner device for combustion of a fuel and a flue gas outlet for exhausting flue gas resulting from the combustion. A second chamber is integrally formed with the vessel. The second chamber comprises a first inlet conduit adapted for receiving water therein and an outlet conduit for exhausting steam. A reformer tube in the combustion chamber is filled with a catalyst and is connected to a second inlet conduit for having a steam and hydrocarbon mixture flow therethrough, and to a second outlet conduit for exhausting a process gas resulting from a steam reforming process in the reformer tube. The reformer tube is disposed in the combustion chamber so as to transfer heat from the combustion to the steam reforming process.

Abstract: An apparatus for carrying out a multi-step process of converting hydrocarbon fuel to a substantially pure hydrogen gas feed includes a plurality of modules stacked end-to-end along a common axis. Each module includes a shell having an interior space defining a passageway for the flow of gas from a first end of the shell to a second end of the shell opposite the first end, and a processing core being contained within the interior space for effecting a chemical, thermal, or physical change to a gas stream passing axially through the module. The multi-step process includes: providing a fuel processor having a plurality of modules stacked end-to-end along a common axis; and feeding the hydrocarbon fuel successively through each of the modules in an axial direction through the tubular reactor to produce the hydrogen rich gas.

Abstract: An auto-oxidation and internal heating type reforming method and apparatus for hydrogen production are disclosed for use in a process in which a gaseous mixture of a hydrocarbon or an aliphatic alcohol with water vapor is fed into contact with a mass of a reforming catalyst to bring about a reforming reaction of the gaseous mixture to produce hydrogen, wherein a small amount of an oxidizing catalyst is admixed with the reforming catalyst in that mass; and a small amount of oxygen is admixed with the gaseous mixture, whereby a portion of the hydrocarbon or aliphatic alcohol is exothermally oxidized to generate a quantity of heat required to reform the gaseous mixture of the hydrocarbon or aliphatic alcohol with water vapor.

Abstract: A combustion/reforming catalyst 15 is composed of a plurality of catalyst layers 15a, 15b, 15c arranged in series with intervals between them, and when a fuel reforming apparatus is started from a low temperature, while the supply of the fuel gas is stopped, air preheated in a preheater is supplied in parallel to a point upstream of each catalyst layer, thereby the catalyst in each catalyst layer is self-heated at the same time so that the entire catalyst is heated. After the whole catalyst is heated up to a temperature at which a combustion/reforming reaction can take place, the feed of air is temporarily stopped, the supply of fuel gas is started, next air is supplied while controlling the flow rate thereof so that temperatures in the catalyst do not exceed the temperature that the catalyst can withstand.

Abstract: The invention concerns a method for producing a gas mixture containing hydrogen and carbon monoxide, and optionally nitrogen, from at least a hydrocarbon such as methane, propane, butane or LPG or natural gas, which consists in performing a partial catalytic oxidation (1) of one or several hydrocarbons, at a temperature of 500° C., at a pressure of 3 to 20 bars, in the pre of oxygen or a gas containing oxygen, such as air, to produce hydrogen and carbon monoxide; then in recuperating the gas mixture which can subsequently be purified or separated, by pressure swing adsorption, temperature swing adsorption of by permeation (3), to produce hydrogen having a purity of at least 80% and a residue gas capable of supplying a cogeneration unit In another embodiment, the gas mixture can subsequently be purified of its water vapour impurities and carbon dioxide to obtain a thermal treatment atmosphere containing hydrogen, carbon monoxide and nitrogen.

Abstract: A method for starting a fast light-off catalytic reformer for producing hydrogen-rich reformate fuel from hydrocarbon fuel and air, the reformer having means for receiving flows of fuel and air, a reforming catalyst for reforming the fuel and air mixture, and an ignition device. A control system selects fuel and air flow rates to form a lean fuel/air mixture and operates the ignition device to ignite the lean mixture to produce hot exhaust gases that flow over and heat the reforming catalyst for a first length of time. Fuel flow is then stopped temporarily for a second length of time, and further ignition is terminated. Fuel flow is then restarted and adjusted to provide a rich fuel/air mixture which is directed to the heated catalyst for reforming into reformate fuel. Air flow may also be adjusted in setting the lean and/or rich fuel/air mixtures.

Abstract: A method of generating a H2 rich gas from a fuel includes supplying a mixture of molecular oxygen, fuel, and water to a fuel processor, and converting the mixture of molecular oxygen, fuel, and water in the fuel processor to the H2 rich gas. The fuel has the formula CnHmOp where n has a value ranging from 1 to 20 and is the average number of carbon atoms per mole of the fuel; m has a value ranging from 2 to 42 and is the average number of hydrogen atoms per mole of the fuel; and p has a value ranging from 0 to 12 and is the average number of oxygen atoms per mole of the fuel. The molar ratio of molecular oxygen supplied to the fuel processor per mole of fuel is a value ranging from about 0.5x0 to about 1.5x0, and the value of x0 is equal to 0.312n−0.5p+0.5(&Dgr;Hf, fuel/&Dgr;Hf, water) where n and p have the values described above, &Dgr;Hf, fuel is the heat of formation of the fuel, and &Dgr;Hf, water is the heat of formation of water.

Abstract: Disclosed is a compact steam reformer which integrally comprises a housing; a reforming reactor having an upper mixing compartment for mixing natural gas and steam and a lower compartment for accommodating a catalyst bed; a natural gas feeding coiled pipe through which natural gas is introduced while being heated; a steam generating coiled pipe in which pure water is converted to steam by the exhaust; a metal fiber burner for heating the reforming reactor; a high-temperature converter for primarily removing carbon monoxide from a synthetic gas; a low-temperature converter for secondarily reducing the carbon monoxide level of the synthetic gas; and a heat exchanger, provided between the high-temperature converter and the low-temperature converter, for cooling the gas effluent from the high-temperature converter. The steam reformer enjoys the advantage of being easy to install in situ and being fabricated at low cost.

Abstract: A process and apparatus are disclosed for the operation of a fuel cell to generate electric power from a feed stream comprising a hydrocarbon or an alcohol. The fuel cell comprises a proton exchange membrane which produces electric power from a hydrogen product stream which comprises essentially no carbon monoxide. The hydrogen product stream is produced from the feed stream in a novel steam reforming zone containing a steam reforming catalyst disposed in a bell-shaped catalyst zone. The bell-shaped catalyst zone is disposed over a combustion zone such that the exhaust gas from the combustion flows around the bell-shaped catalyst zone to heat the catalyst from the inside and the outside of the catalyst zone. Furthermore, the bell-shaped catalyst zone maintains a high inlet and a high outlet temperature to avoid methane slippage in the steam reforming zone. Heat for the steam reforming zone is provided by a fuel stream and at least a portion of the anode waste gas stream from the fuel cell.

Abstract: A tubular fuel gas-steam reformer assembly, preferably an autothermal reformer assembly, for use in a fuel cell power plant, includes a fuel-steam vaporizer, a fuel-steam and air mixing station, and a catalyst bed. The catalyst bed can include catalyzed alumina pellets, or a monolith such as a foam or honeycomb body which is preferably formed from a high temperature material such as a steel alloy, or from a ceramic material. The fuel-steam mixture is vaporized in the vaporizer and then passes into the mixing station. The mixing station comprises a plurality of mixing tubes which open into the catalyst bed. The mixing tubes extend through a manifold and include openings which interconnect the interior of the tubes with the manifold. The openings have axes which are perpendicular to the axis of each of the mixing tubes, and are positioned on the tubes at locations which are dictated by the diameter of the mixing tubes and which will ensure thorough mixing of the air and fuel-steam streams.

Abstract: An apparatus for carrying out a process of converting hydrocarbon fuel to a hydrogen rich gas including a first heat exchanger for heating the hydrocarbon fuel to produce a heated hydrocarbon fuel, a first desulfurization reactor for reacting the heated hydrocarbon fuel to produce a substantially desulfurized hydrocarbon fuel, a manifold for mixing the substantially desulfurized hydrocarbon fuel with an oxygen containing gas to produce a fuel mixture, a second heat exchanger for heating the fuel mixture to produce a heated fuel mixture, an autothermal reactor including a catalyst for reacting the heated fuel mixture to produce a first hydrogen containing gaseous mixture, a second desulfurization reactor for reacting the first hydrogen containing gaseous mixture to produce a second hydrogen containing gaseous mixture that is substantially desulfurized, a water gas shift reactor for reacting the second hydrogen containing gaseous mixture to produce a third hydrogen containing gaseous mixture with a substantiall

Abstract: A method of generating hydrogen and hydrocarbons utilizing superadiabatic combustion is disclosed.

Abstract: A method is disclosed for converting light hydrocarbons to synthesis gas employing a reduced nickel alloy monolith catalyst which catalyzes a net partial oxidation reaction to produce an effluent stream comprising carbon monoxide and hydrogen in a ratio of about 2:1 H2/CO. Preferred catalyst beds comprise a compositionally graded axial array, or stack, of Ni—Cr, Ni—Co—Cr, or Ni—Rh monoliths, and their manner of making is disclosed. The Ni alloy monolith catalysts are mechanically strong and retain high activity and selectivity to carbon monoxide and hydrogen products under syngas production conditions of high gas space velocity, elevated pressure and high temperature.

Abstract: A process for catalytic conversion of methane or natural gas to syngas using a supported catalyst containing oxides of nickel and cobalt with of without noble metals. Efficiency of the catalytic process is increased by simultaneously carrying out an exothermic oxidation reaction and an endothermic steam and carbon dioxide reforming reaction over the supported catalyst. The catalyst is prepared by depositing oxides of nickel and cobalt, with or without noble metals, on a sintered low surface area porous inert support. Surface of the support is precoated with an oxide of Be, Mg, Ca or a mixture thereof so that a protective layer of alkaline earth oxide is formed between the oxides of nickel and cobalt and the support, and hence, direct chemical interactions between the oxides of nickel and cobalt and reactive components of the support, which leads to formation of catalytically inactive binary oxide phases, are avoided.