Chemistry: electrical current producing apparatus – product – and – With pressure equalizing means for liquid immersion operation
Reexamination Certificate
1999-09-14
2001-07-17
Brouillette, Gabrielle (Department: 1745)
Chemistry: electrical current producing apparatus, product, and
With pressure equalizing means for liquid immersion operation
C429S010000, C429S010000, C429S010000, C429S006000, C429S006000, C429S006000, C429S006000
Reexamination Certificate
active
06261711
ABSTRACT:
This invention relates generally to fuel cells and more specifically to an improved sealing system between the fluid flow plates in such cells.
BACKGROUND OF THE INVENTION
A fuel cell is a device which converts chemical energy of a fuel into electrical energy, typically by oxidizing the fuel. In general a fuel cell includes an anode and a cathode separated by an electrolyte. When fuel is supplied to the anode and oxidant is supplied to the cathode, the electrolyte electrochemically generates a useable electric current which is passed through an external load. The fuel typically supplied is hydrogen and the oxidant typically supplied is oxygen. In such cells, the electrolyte combines the oxygen and hydrogen to form water and to release electrons. The chemical reaction for a fuel cell using hydrogen as the fuel and oxygen as the oxidant is shown in equation (1).
H
2
+½O
2
→H
2
O (1)
This process occurs through two redox or separate half-reactions which occur at the electrodes:
Anode Reaction
H
2
→2H
+
+2
e
−
(2)
Cathode Reaction
½O
2
+2H
+
+2
e
−
→H
2
O (3)
In the anode half-reaction, hydrogen is consumed at the fuel cell anode releasing protons and electrons as shown in equation (2). The protons are injected into the fuel cell electrolyte and migrate to the cathode. The electrons travel from the fuel cell anode to cathode through an external electrical load. In the cathode half-reaction, oxygen, electrons from the load, and protons from the electrolyte combine to form water as shown in equation (3). The directional flow of protons, such as from anode to cathode, serves as a basis for labeling an “anode” side and a “cathode” side of the fuel cell.
Fuel cells are classified into several types according to the electrolyte used to accommodate ion transfer during operation. Examples of electrolytes include aqueous potassium hydroxide, concentrated phosphoric acid, fused alkali carbonate, stabilized zirconium oxide, and solid polymers, e.g., a solid polymer ion exchange membrane.
An example of a solid polymer ion exchange membrane is a Proton Exchange Membrane (hereinafter “PEM”) which is used in fuel cells to convert the chemical energy of hydrogen and oxygen directly into electrical energy. A PEM is a solid polymer electrolyte which when used in a PEM-type fuel cell permits the passage of protons (i.e.,H
+
ions) from the anode side of a fuel cell to the cathode side of the fuel cell while preventing passage of reactant fluids such as hydrogen and oxygen gases.
Typically, a PEM-type cell includes an electrode assembly disposed between an anode fluid flow plate and a cathode fluid flow plate. An electrode assembly usually includes five components: two gas diffusion layers; two catalysts; and an electrolyte. The electrolyte is located in the middle of the five-component electrode assembly. On one side of the electrolyte (the anode side) a gas diffusion layer (the anode gas diffusion layer) is disposed adjacent the anode layer, and a catalyst (the anode catalyst) is disposed between the anode gas diffusion layer and the electrolyte. On the other side of the electrolyte (the cathode side), a gas diffusion layer (the cathode gas diffusion layer) is disposed adjacent the cathode layer, and a catalyst (the cathode catalyst) is disposed between the cathode gas diffusion layer and the electrolyte.
Several PEM-type fuel cells are arranged as a multi-cell assembly or “stack.” In a multi-cell stack, multiple single PEM-type cells are connected together in series. The number and arrangement of single cells within a multi-cell assembly are adjusted to increase the overall power output of the fuel cell. Typically, the cells are connected in series with one side of a fluid flow plate acting as the anode for one cell and the other side of the fluid flow plate acting as the cathode for an adjacent cell.
The anode and cathode fluid flow plates are made of an electrically conductive material, typically metal or compressed carbon, in various sizes and shapes. Fluid flow plates act as current collectors, provide electrode support, provide paths for access of the fuels and oxidants to the electrolyte, and provide a path for removal of waste products formed during operation of the cell.
The cell also includes a catalyst, such as platinum on each side of the electrolyte for promoting the chemical reaction(s) that take place in the electrolyte in the fuel cells. The fluid flow plates include a fluid flow field of open-faced channels for distributing fluids over the surface of the electrolyte within the cell.
Fluid flow plates may be manufactured using any one of a variety of different processes. For example, one technique for plate construction, referred to as “monolithic” style, includes compressing carbon powder into a coherent mass which is subjected to high temperature processes to bind the carbon particles together, and to convert a portion of the mass into graphite for improved electrical conductivity. The mass is then cut into slices, which are formed into the fluid flow plates. Typically, each fluid flow plate is subjected to a sealing process (e.g., resin impregnation) in order to decrease gas permeation therethrough and reduce the risk of uncontrolled reactions.
Fluid flow plates also have holes therethrough which when aligned in a stack form fluid manifolds through which fluids are supplied to and evacuated from the stack. Some of the fluid manifolds distribute fuel (such as hydrogen) and oxidant (such as air or oxygen) to, and remove unused fuel and oxidant as well as product water from, the fluid flow fields of the fluid flow plates. Additionally, other fluid manifolds circulate coolant. Furthermore, other cooling mechanisms such as cooling plates are commonly installed within the stack between adjacent single cells to remove heat generated during fuel cell operation.
Typically, the PEM-type cell is sealed outside the PEM active area by compressing the membrane between an O-ring gasket disposed within a groove on the cathode side and an insulator glued to the anode side.
SUMMARY OF THE INVENTION
In general, in one aspect, the invention is a fluid seal for a fuel cell including a compressible member which conforms to a surface of a gasket to form a seal.
In another aspect, a fluid seal for a fuel cell includes a first fluid flow plate having a gasket at least partially disposed within a groove formed in a first surface and a second fluid flow plate having a compressible member bonded to a first surface of the second fluid flow plate. The first surface of the first fluid flow plate is parallel to the first surface of the second fluid flow plate and the compressible member circumscribes a pattern that mirrors the pattern formed by the groove on the first fluid flow plate. The compressible member conforms to a surface of the gasket.
In another aspect, the invention features a fluid flow plate for a fuel cell includes a plate made at least in part from an electrically conductive material having a front surface with one or more open-faced channels formed therein define a fluid flow region for carrying a reactive gas. The plate further including a supply opening and an exhaust opening, and a compressible material bonded to the plate surface around a perimeter of the fluid flow region, the supply opening, and the exhaust opening.
In yet another aspect, the invention features a method of sealing a fuel cell by compressing a first fluid flow plate towards a second fluid flow plate. The first fluid flow plate includes a gasket at least partially disposed within a groove formed in a surface of the first plate and the second fluid flow plate includes a compressible member bonded to a surface of the second fluid flow plate. The compressible member circumscribes a pattern that mirrors the pattern formed by the groove on the first fluid flow plate, and the compressible member conforms to a surface of the gasket as the fluid flow plates are compressed together.
Embodiments may include one or more of th
Buesing Donald G.
Matlock Richard R.
Brouillette Gabrielle
Fish & Richardson P.C.
Plug Power Inc.
Yuan Dah-Wei
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