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STEAM REFORMATION FUEL CELL WITH WASTE HEAT COGENERATION TURBINE HEAT TO ENERGY PYROELECTRIC CRYSTALS AND/OR THERMO-COUPLING ANY AND ALL WASTE HEAT TO ENERGY TECHNOLOGIES AND/OR NEW MACRO-MICROS FUEL CELL POWER PLANT DESIGN
STEAM REFORMATION FUEL CELL WITH WASTE HEAT COGENERATION TURBINE HEAT TO ENERGY PYROELECTRIC CRYSTALS AND/OR THERMO-COUPLING ANY AND ALL WASTE HEAT TO ENERGY TECHNOLOGIES AND/OR NEW MACRO-MICROS FUEL CELL POWER PLANT DESIGN
Any all technologies including... MCFC and SOFC...Note our bio fuels to energy Super Fuel Cell do not use any combustionprocesses and therefore do notproduce any green house gases.SUPER FUEL CELL Methane, Ethanol, Butane, Hydrogen...Any and all fuels.Macro Upper Large Scale Fast and Mass Production per time. Probably Cheaper.1. The nozzles that injects new unreacted fuel in the direction of the anode.Heat produced from thereaction can be used for turbine co-generation.2. The direction of the fuel down the channels.3. The Anode Electrode.4. The Cathode (where oxygen enters and reacts).5. The Electrolyte.Multiple Micro Scale Higher Yield per concentration of fuel left in themixture ie. biogas is oftencontaminated with other gases present, therefore concentration per bulk/volumeof the rest of the gasesvaries. By using multiple Micro Fuel Cells we 1. Maintain the same speed ofthroughput as the Macro part ofthe Super Fuel Cell Above so there is no backing up 2. Micro Fuel Cells aremore efficient at reacting with thereactable fuels since the channel is thinner and therefore less fuel isexposed to more electrodes...meaningmore of the reactable fuel molecules pass over the surface of the electrodesallowing for more fuelmolecules access to the surface of the electrode(s) such that there is lessdead space between the electrodeand the outer walls of the channel...to capture the most fuel conversion, fromthe total mixture.6. Cathode Outer Wall and Cathode Channel.7. Cathode Electrode.8. The Anode Electrode.9. The Anode Outer Wall and Anode Channel. The bottom channel is narrowed tothe optimal size for viablefuel cell stationary power plant capacity, then they feed into Multiple Microfuel cells (possibly ProtonExchange Membrane - which are cheaper) the hot (high temperature) is runthrough waste heat to enenergy (such as co-generation, pyroelectric crystals, thermo-coupling and anyand all Heat to EnergyTechnologies) whereas the materials for MCFC and SOFC are expensive to replaceand heavy. We mighteven use circular outer walls in the Multiple Micro technologies to redirectthe secondary processed fueland/or use smaller jets/sprays to get higher concentration of fuel into thedepleted side facing the anode toreplenish the side facing the electrode that has been depleted/spent fromreacting with the anode.We do the opposite with the cathode side of the fuel cell.Additionally Biogas/Methane/CH4 are also steam reformed directly inside theAnode Channel by the heatproduced by the reaction.Excess heat can be used for:1. Co-Generation.2. Pyroelectric Crystals.3. Thermo-Coupling.4. Any and All Heat Waste to Energy Technologies.To deal with the problem of carbon deposits we could scrub biogas to removethe tar before entering thefuel cell, use cleanable electrodes and/or replaceable electrodes; we couldalso configure the each of theanode and cathode each in layers, an outer shield (made of less expensivematerials) to allow deposit ofcarbon on its surface, and thick back (inner) anode that could produce astronger current to increaseefficiency (perhaps made of a more conductive material).
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