Chemistry: electrical current producing apparatus – product – and – With pressure equalizing means for liquid immersion operation
Reexamination Certificate
2000-12-15
2003-12-09
Gulakowski, Randy (Department: 1746)
Chemistry: electrical current producing apparatus, product, and
With pressure equalizing means for liquid immersion operation
C429S006000, C429S006000, C429S047000, C429S047000, C427S115000
Reexamination Certificate
active
06660423
ABSTRACT:
FIELD OF INVENTION
The present invention pertains to fuel cells, and more particularly to a direct methanol fuel cell including a water management system and a method of fabricating the system, in which water is collected and redistributed during the process of generating electrical energy.
BACKGROUND OF THE INVENTION
Fuel cells in general, are “battery replacements”, and like batteries, produce electricity through an electrochemical process without combustion. The electrochemical process utilized provides for the combining of protons with oxygen from air or as a pure gas. The process is accomplished utilizing a proton exchange membrane (PEM) sandwiched between two electrodes, namely an anode and a cathode. Fuel cells, as known, are a perpetual provider of electricity. Hydrogen is typically used as the fuel for producing the electricity and can be processed from methanol, natural gas, petroleum, or stored as pure hydrogen. Direct methanol fuel cells (DMFCs) utilize methanol, in a gaseous or liquid form as fuel, thus eliminating the need for expensive reforming operations. DMFCs provide for a simpler PEM cell system, lower weight, streamlined production, and thus lower costs.
In a standard DMFC, a dilute aqueous solution of methanol is fed as the fuel on the anode side (first electrode), and the cathode side (second electrode) is exposed to forced or ambient air (or O2). A Nafion® type proton conducting membrane typically separates the anode and the cathode sides. Several of these fuel cells can be connected in series or parallel depending on power requirements.
Typically, DMFC designs are large stacks with forced airflow at elevated temperatures. Smaller air breathing DMFC designs are more complicated. In conventional PEM fuel cells, stack connections are made between the fuels cell assemblies with conductive plates, machined with channels or grooves for gas distribution. A typical conventional fuel cell is comprised of an anode (H
2
or methanol side) current collector, anode backing, membrane electrode assembly (MEA) (anode/ion conducting membrane/cathode), cathode backing, and cathode current collector. Each fuel cell is capable of producing approx. 1.0 V. To obtain higher voltages, fuel cells are typically stacked in series (bi-polar manner—positive to negative) one on top of another. Conventional fuel cells can also be stacked in parallel (positive to positive) to obtain higher power, but generally larger fuel cells are simply used instead.
During operation of a direct methanol fuel cell, a dilute aqueous methanol (usually 3-4% methanol) solution is used as the fuel on the anode side. If the methanol concentration is too high, then there is a methanol crossover problem that will reduce the efficiency of the fuel cell. If the methanol concentration is too low then there will not be enough fuel on the anode side for the fuel cell reaction to take place. Current DMFC designs are for larger stacks with forced airflow. The smaller air breathing DMFC designs are difficult to accomplish because of the complexity in miniaturizing the system for portable applications. Carrying the fuel in the form of a very dilute methanol mixture would require carrying a large quantity of fuel which is not practical for the design of a miniature power source for portable applications. Miniaturizing the DMFC system requires having on hand separate sources of methanol and water and mixing them in-situ for the fuel cell reaction. To aid in supplying methanol and water to the anode, it would be beneficial to recirculate the aqueous fuel mixture after the fuel cell reaction, and recycle the water generated at the cathode in the fuel cell reaction, as well as the water arriving at the cathode via diffusion and electro-osmotic drag.
Accordingly, it is a purpose of the present invention to provide for a direct methanol fuel cell system design in which a water management system is integrated into a miniaturized device.
It is a purpose of the present invention to provide for a direct methanol fuel cell including a water management system, comprised of microchannels, cavities, hydrophobic treatments, and microfluidics technology for fuel-bearing fluid mixing, pumping and recirculation of water by-product production.
It is still a further purpose of the present invention to provide for a direct methanol fuel cell including a water management system in which all of the system components are embedded inside a base portion, such as a ceramic base portion.
It is yet a further purpose of the present invention to provide for method of fabricating a direct methanol fuel cell including a water management system, comprised of microchannels, cavities, chemical surface modifications, and microfluidics technology for fuel-bearing fluid mixing, pumping and recirculation of water by-product production.
SUMMARY OF THE INVENTION
The above problems and others are at least partially solved and the above purposes and others are realized in a fuel cell device and method of forming the fuel cell device including a base portion, formed of a singular body, and having a major surface. At least one membrane electrode assembly is formed on the major surface of the base portion. The membrane electrode assembly includes hydrophilic properties for the water management of by-product water. A fluid supply channel is defined in the base portion and communicates with the at least one membrane electrode assembly for supplying a fuel-bearing fluid to the at least one membrane electrode assembly. An exhaust channel is defined in the base portion and communicating with the at least one membrane electrode assembly. The exhaust channel is spaced apart from the fluid supply channel for exhausting by-product fluid, including water, from the at least one membrane electrode assembly. The membrane electrode assembly and the cooperating fluid supply channel and cooperating exhaust channel form a single fuel cell assembly.
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Bostaph Joseph W.
Fisher Allison M.
Neutzler Jay
Crepean Jonathan
Gulakowski Randy
Koch William E.
Motorola Inc.
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