초록 ▼

A mass and heat recovery system for a fuel cell power plant includes at least one fuel cell for producing electrical energy, hydrocarbon fuel processing components for producing a hydrogen rich reducing fluid for the fuel cell, and a direct mass and heat transfer device for recovering mass and heat

A mass and heat recovery system for a fuel cell power plant includes at least one fuel cell for producing electrical energy, hydrocarbon fuel processing components for producing a hydrogen rich reducing fluid for the fuel cell, and a direct mass and heat transfer device for recovering mass and heat such as water vapor leaving the plant. The fuel processing components include an auxiliary burner that provides heat to generate steam and a reformer that receives the steam mixed with a hydrocarbon fuel along with a small amount of air and converts the mixture to a hydrogen rich stream appropriate for supplying hydrogen to the anode electrode. The direct mass and heat transfer device passes a process oxidant stream upstream of the plant in mass transfer relationship with a plant exhaust stream that includes both a cathode exhaust stream and an anode exhaust stream wherein the anode exhaust stream has first been burned in the auxiliary burner so that mass and heat such as water vapor in the plant exhaust stream transfer directly through a mass transfer medium of the device to the process oxidant stream entering the plant. The device includes a separator housing for supporting the transfer medium and for preventing bulk mixing of the streams. An exemplary transfer medium such as a liquid water portion of a water saturated polyflourosulfonic ionomer selectively sorbs a fluid substance consisting of polar molecules such as water molecules from a fluid stream containing polar and non-polar molecules.

대표청구항 ▼

[ What is claimed is:] [17.] A method of operating a fuel cell power plant for recovery of mass and heat exiting the plant, the method comprising the steps of:a. providing at least one fuel cell, including;i. an electrolyte having a first major surface and an opposed second major surface; andii. an

[ What is claimed is:] [17.] A method of operating a fuel cell power plant for recovery of mass and heat exiting the plant, the method comprising the steps of:a. providing at least one fuel cell, including;i. an electrolyte having a first major surface and an opposed second major surface; andii. an anode electrode supported by a porous anode support layer in intimate contact with the first major surface of the electrolyte and a cathode electrode supported by a porous cathode support layer in intimate contact with the second major surface of the electrolyte, wherein the porous anode support layer passes a stream of the reducing fluid in contact with the anode electrode and the porous cathode support layer passes a stream of the oxidant fluid in contact with the cathode electrode;b. passing a process oxidant stream through a primary oxidant passage from a supply of oxidant into the porous cathode support layer;c. passing an anode exhaust stream from the anode support layer through an auxiliary burner fuel processing component, burning the anode exhaust stream and directing the burned anode exhaust stream into a plant exhaust passage;d. passing a cathode exhaust stream through a cathode exhaust passage out of the porous cathode support layer into the plant exhaust passage and mixing the burned anode exhaust stream with the cathode exhaust stream into a plant exhaust stream; and,e. directing the process oxidant stream and plant exhaust stream in mass transfer relationship within a direct mass and heat transfer device by passing the process oxidant stream and plant exhaust stream in contact with a transfer medium for sorbing a fluid substance consisting of polar molecules within the plant exhaust stream and for desorbing the fluid substance consisting of polar molecules into the process oxidant stream by further supporting the mass transfer medium within a separator housing so that both streams contact the mass transfer medium and both streams are prevented from bulk mixing together.