Abstract:
Sulfur and sulfur compounds are removed from a gas stream, such as a hydrocarbon fuel gas stream so as to render the gas stream suitable for use in a fuel cell power plant. Natural gas and recycled hydrogen enters the hydrodesulfurizer assembly at a temperature of about 120 DEG F. The gas stream is heated to a temperature of about 625 DEG F whereupon it enters a desulfurizing bed (44) formed from a mixture of platinum catalyst deposited on alumina pellets (46) and a pelletized zinc oxide hydrogen sulfide absorbent (48). The gas is cooled to an exit temperature of about 525 DEG F as it passes through the desulfurizer bed. The desulfurizer bed is combined with a shift converter (6) which reduces carbon monoxide in the desulfurized gas stream after the latter has passed through a steam reformer bed.
Abstract:
A fuel cell system, generally, has a fuel processing apparatus for steam reforming a hydrocarbon fuel and steam into a product gas, and a fuel cell stack for converting the product gas into electricity. The fuel processing apparatus is a catalytic reaction apparatus (36) having a furnace (10) and a catalytic reactor. In an effort to increase the efficiency of the catalytic reaction apparatus and decrease the size and/or number of catalytic reactors, the present invention relates to a furnace that utilizes air and fuel preheat chambers (12, 14) to increase the flame temperature within the furnace.
Abstract:
A fuel cell has a current collector plate (22) located between an electrode (20) and a separator plate (25). The collector plate has a plurality of arches (26, 28) deformed from a single flat plate in a checkerboard pattern. The arches are of sufficient height (30) to provide sufficient reactant flow area. Each arch is formed with sufficient stiffness to accept compressive load and sufficient resiliently to distribute the load and maintain electrical contact.