摘要:
In various aspects, systems and methods are provided for integration of molten carbonate fuel cells with a Fischer-Tropsch synthesis process. The molten carbonate fuel cells can be integrated with a Fischer-Tropsch synthesis process in various manners, including providing synthesis gas for use in producing hydrocarbonaceous carbons. Additionally, integration of molten carbonate fuel cells with a Fischer-Tropsch synthesis process can facilitate further processing of vent streams or secondary product streams generated during the synthesis process.
摘要:
In various aspects, systems and methods are provided for integration of molten carbonate fuel cells with a Fischer-Tropsch synthesis process. The molten carbonate fuel cells can be integrated with a Fischer-Tropsch synthesis process in various manners, including providing synthesis gas for use in producing hydrocarbonaceous carbons. Additionally, integration of molten carbonate fuel cells with a Fischer-Tropsch synthesis process can facilitate further processing of vent streams or secondary product streams generated during the synthesis process.
摘要:
In various aspects, systems and methods are provided for integration of molten carbonate fuel cells with a Fischer-Tropsch synthesis process. The molten carbonate fuel cells can be integrated with a Fischer-Tropsch synthesis process in various manners, including providing synthesis gas for use in producing hydrocarbonaceous carbons. Additionally, integration of molten carbonate fuel cells with a Fischer-Tropsch synthesis process can facilitate further processing of vent streams or secondary product streams generated during the synthesis process.
摘要:
In various aspects, systems and methods are provided for integration of molten carbonate fuel cells with a Fischer-Tropsch synthesis process. The molten carbonate fuel cells can be integrated with a Fischer-Tropsch synthesis process in various manners, including providing synthesis gas for use in producing hydrocarbonaceous carbons. Additionally, integration of molten carbonate fuel cells with a Fischer-Tropsch synthesis process can facilitate further processing of vent streams or secondary product streams generated during the synthesis process.
摘要:
A hydrogen generator includes: a hydro-desulfurizer configured to remove a sulfur compound in a raw material and including a tubular first wall; a reformer configured to generate a hydrogen-containing gas by using the raw material supplied from the hydro-desulfurizer; a tubular second wall provided coaxially with the first wall so as to be opposed to the first wall; and an electric heater annularly provided in a gap between the first wall and the second wall so as to turn back in the axial direction of the first wall and including a portion extending in an axial direction of the first wall.
摘要:
A SOFC module (100) includes a SOFC (20) including a power generation section for generating electric power through a power generation reaction by utilizing a fuel gas and air; and a reformer (40) for generating a reformed gas as the fuel gas, by using a fluid supplied to the reformer, the reformed gas being generated from the fluid. The fluid heated by heat owned by the SOFC (20) is supplied to the reformer (40).
摘要:
The invention concerns a high temperature fuel cell with mixed anionic and protonic conduction comprising a protonic conduction reforming membrane directly coupled to a solid oxide fuel cell with conduction by oxygen ions, enabling use of a gradually reforming anode generating carbon deposits to be avoided. The reverse operation of the present invention outside the reforming stage forms a high water temperature electrolyzer to produce hydrogen efficiently without having to separate it from water as is the case with current systems.
摘要:
A fuel cell system has at least one fuel cell (3) with a high-temperature polymer electrolyte membrane (9). The fuel cell (3) is supplied with liquid gas from a liquid gas supply (1). The liquid gas is introduced directly - without complex reformation - in an anode reaction area (7) of the fuel cell (3). Water vapour is mixed with the liquid gas before entry to the anode reaction area (7).