Abstract:
A hydrogen generation apparatus is constituted of a treated-substance container, which has a hydrogen discharge port for activating a treated substance; and at least one plate-form activation structural body, which is provided within the treated-substance container vertically thereto. The plate-form activation structural body is a structural body that arranges particles composed of any of a single constituent element, which is selected from a group comprising silicon, titanium, nickel, and samarium, and fluorocarbon at positions that amplify unique wave energy in each the element and the fluorocarbon, and which structural body has an energy concentration field between the particles within the treated-substance container, wherein gases containing hydrogen are generated by any of the treated substance within the treated-substance container staying in and passing through the energy concentration field. The hydrogen generation apparatus can generate hydrogen with less energy and achieve space saving.
Abstract:
An arrangement for generating hydrogen gas utilizes differential pressure to transport fuel and spent fuel components without requiring an electrically powered fuel delivery pump.
Abstract:
A fuel reformer which can easily achieve high weight energy density and high volume energy density, and a method for producing the fuel reformer with ease and high efficiency as well as an electrode for electrochemical device, such as a fuel cell, and an electrochemical device are provided. The present invention is to feed hydrogen obtained from a fuel reformer (1) having a catalyst layer (4) containing Pt for taking out hydrogen from a liquid fuel, such as methanol, and a hydrogen permeable layer (5), such as a Pd thin film, which is impermeable to liquid and permeable to hydrogen to an electrochemical device such as a fuel cell (40), which comprises a negative electrode (19), a positive electrode (23) and a proton conductive film (14) sandwiched therebetween. The present invention provides a method of producing the hydrogen permeable layer (5) in the reformer 1 by forming the hydrogen permeable layer (5) and the catalyst layer (4) on a base layer (51) comprising Al or the like, and removing the base layer (51) by dissolution.
Abstract:
A process for contacting reactants with a particulate catalyst while indirectly contacting the reactants with a heat exchange medium amid simultaneous exchange of catalyst particles by an operation that sequentially restricts reactant flow while moving catalyst through reaction stacks in which the reactant flow has been restricted. The process permits a change out of catalyst in a channel type reactor arrangement that would normally restrict catalyst flow during operation. Moving catalyst through a heat exchange type reactor having reactant and heat exchange channels permits control of catalyst activity as well as temperatures.
Abstract:
The present invention provides methods and apparatus for decomposing toxic compounds so that reaction by-products produced thereby are selectively reduced. A method generally comprises: introducing a carrier gas, having a toxic compound entrained therein, into a packed-bed of ferroelectric pellets; and polarizing the pellets to produce a plasma which decomposes the toxic compound. The pellets are coated with a catalyst selected to react with by-products of the decomposition of the toxic compound and thereby produce non-toxic compounds. An apparatus for decomposing toxic compounds and selectively reducing by-products, according to the present invention, comprises: a vessel having an internal passageway therethrough; a packed-bed of pellets coated with at least one catalyst; means for producing a plasma within the packed-bed of pellets; and carrier gas flow means in fluid communication with the internal passageway for causing a carrier gas entrained with toxic compounds to flow through the packed-bed of pellets. The present invention also discloses methods and apparatus wherein a pulsed corona reactor having a catalyst coating on a portion thereof is utilized to decompose toxic compounds.
Abstract:
The present invention provides methods and apparatus for decomposing toxic compounds so that reaction by-products produced thereby are selectively reduced. A method generally comprises: introducing a carrier gas, having a toxic compound entrained therein, into a packed-bed of ferroelectric pellets; and polarizing the pellets to produce a plasma which decomposes the toxic compound. The pellets are coated with a catalyst selected to react with by-products of the decomposition of the toxic compound and thereby produce non-toxic compounds. An apparatus for decomposing toxic compounds and selectively reducing by-products, according to the present invention, comprises: a vessel having an internal passageway therethrough; a packed-bed of pellets coated with at least one catalyst; means for producing a plasma within the packed-bed of pellets; and carrier gas flow means in fluid communication with the internal passageway for causing a carrier gas entrained with toxic compounds to flow through the packed-bed of pellets. The present invention also discloses methods and apparatus wherein a pulsed corona reactor having a catalyst coating on a portion thereof is utilized to decompose toxic compounds.
Abstract:
An isothermal reactor design uses interleaved layers of plate heat exchange elements to improve heat transfer in a radial flow arrangement that offers a simple and compact design for fluid flow and catalyst transfer.
Abstract:
A plate type shift converter comprises a stack of alternately piled shift reactor plates and cooling plates and various gas intake and exhaust manifolds mounted on lateral faces of the stack. Each shift reactor plate includes a plate member, a masking frame provided along the periphery of the plate member, a gas entrance formed in the masking frame, a gas exit formed at a location opposite the gas entrance in the masking frame and a shift catalyst located in the masking frame. Each cooling plate includes a plate member, a masking frame provided along the periphery of the plate member, a gas entrance formed in the masking frame, a gas exit formed at a location opposite the second gas entrance in the masking frame and a fin plate located in the masking frame. When gases are introduced to the shift reactor plate, the gases undergo the CO shift reaction (exothermic reaction) as they flow contacting the shift catalyst. At the same time, the gases are cooled by the cooling plates which sandwich the flow of the gases or sandwich the shift reactor plate.
Abstract:
Void blowing by gas flow through a bed of particulate material is avoided by the use of a cover plate that eliminates void spaces at the top of the bed and a vertical duct that allows a head of particulate material to be maintained above the cover plate. The particle bed is arranged in the usual fashion using inner and outer screens to hold particulate material in a vertically extended bed into which particulate material is intermittently added and withdrawn. The top of the particulate bed is contacted by an imperforate cover plate that is sloped up to an inlet opening that has a smaller cross-sectional area than the area of the bed. The cover plate has a slope which is greater than the angle of the repose of the particles so that particles filling the top section of the bed will be free of void spaces. The cover plate also has a relatively small inlet opening so that a small volume of catalyst particles can provide a head of particles above the inlet opening to resist upward pressure that otherwise forms voids at the inlet screen surface. This cover plate arrangement also minimizes bed heights and overall reactor height necessary to provide the head of particles for resisting upward pressure.
Abstract:
In a furnace which allows a feed powder or granules in a stack of trays on a base plate to be reacted with a reactive gas, the improvement wherein each of the trays has a cutout or an opening providing a passage for the reactive gas or the produced gas both at the top of one side wall and in the bottom wall to the opposite side of the tray, the base plate having an opening through which the reactive gas is introduced or the produced gas is discharged.