International Fuel Cells, LLC

Francis A Kocum

Richard A Sederquist

Glenn W Scheffler

Thomas J Corrigan

Peter F Foley

Stanley P Bonk

William E Romanowski

A compact and efficient fuel reformer which is operable to produce a hydrogen-enriched process fuel from a raw fuel such as natural gas, or the like includes a compact array of catalyst tubes which are contained in a heat-insulated housing. The catalyst tube array preferably includes a multitude of catalyst tubes that are arranged in a hexagonal array. The housing includes internal hexagonal thermal insulation so as to ensure even heating of the catalyst tubes. The diameter of the tubes is sized so that spacing between adjacent tubes in the array can be minimized for efficient heat transfer. The interior of each of the catalyst tubes includes a hollow dead-ended central tube which serves as a fines trap for collecting catalyst fines that may become entrained in the fuel stream. The catalyst tubes are also provided with an upper frusto-conical portion which serves to extend the catalyst bed and provide a catalyst reserve. The assembly includes a side-fired startup burner which allows for an improved diffusion burner orifice array at the top of the reformer. The catalyst tubes are supported by side walls of the assembly in a manner that stabilizes the tubes in the assembly. In the assembly, the internal transverse manifold plates are tied together by portions of the tube assemblies so as to form a composite beam that supports the weight of the catalyst tube array.

Hydrocarbon fuel gas reformer assembly for a fuel cell power plant

The temperature of the end cells in a fuel cell stack is controlled by means of auxiliary coolant plates. Outwardly of the end cells in the fuel cell stack there are disposed thermal and electrical insulating plates, and outwardly of the insulating plates there are disposed metal pressure plates. The temperature of the end cells of the stack is controlled by means of auxiliary coolant plates which are connected to the main coolant circulation lines and which are sandwiched between the insulating plates and the pressure plates at each end of the stack. In this way, the outer surface of the insulating plates is kept at substantially the same temperature as the inner surface thereof thus minimizing heat loss across the insulating plates from the end cells in the stack.

Temperature regulation system for endmost fuel cells in a fuel cell stack

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Glastonbury, CT, United States of America

Francis A Kocum