Reforming external

A viable electrocatalyst operating with minimal polarization for the direct electrochemical oxidation of methanol at low temperature would strongly enhance the competitive position of fuel ceU systems for transportation appHcations. Fuel ceUs that directiy oxidize CH OH would eliminate the need for an external reformer in fuel ceU systems resulting in a less complex, more lightweight system occupying less volume and having lower cost. Improvement in the performance of PFFCs for transportation appHcations, which operate close to ambient temperatures and utilize steam-reformed CH OH, would be a more CO-tolerant anode electrocatalyst. Such an electrocatalyst would reduce the need to pretreat the steam-reformed CH OH to lower the CO content in the anode fuel gas. Platinum—mthenium alloys show encouraging performance for the direct oxidation of methanol. 

Fuel cells such as the one shown on Fig. 3.4a convert H2 to H20 and produce electrical power with no intermediate combustion cycle. Thus their thermodynamic efficiency compares favorably with thermal power generation which is limited by Carnot-type constraints. One important advantage of solid electrolyte fuel cells is that, due to their high operating temperature (typically 700° to 1100°C), they offer the possibility of "internal reforming" which permits the use of fuels such as methane without a separate external reformer.33 36... 

This reaction is of great technological interest in the area of solid oxide fuel cells (SOFC) since it is catalyzed by the Ni surface of the Ni-stabilized Zr02 cermet used as the anode material in power-producing SOFC units.60,61 The ability of SOFC units to reform methane "internally", i.e. in the anode compartment, permits the direct use of methane or natural gas as the fuel, without a separate external reformer, and thus constitutes a significant advantage of SOFC in relation to low temperature fuel cells. 

Hydrocarbons such as natural gas or methane can be reformed internally in the SOFC, which means that these fuels can be fed to the cells directly. Other types of fuel cells require external reforming. The reforming equipment is size-dependent which reduces the modularity. 

Additionally, nickel is a well established steam-reforming catalyst. An ideal SOFC system operated on natural gas applies internal steam reforming, i.e., the reforming of the methane takes place in the anode compartment of the stack. This type of system is favored for system simplicity and costs (no external reformer), and for system efficiency because the heat generated by the cell reaction is directly used by the reform reaction, and hence the cooling requirements of the stack (by air at the cathode side) are significantly reduced. 

Figure 1-3 External Reforming and Internal Reforming MCFC System Comparison...

The fuel processor efficiency is size dependent therefore, small fuel cell power plants using externally reformed hydrocarbon fuels would have a lower overall system efficiency. 

These issues do not eliminate the possibility of a pressurized MCFC system, but they do favor the selection of more moderate pressures. For external reforming systems sized near 1 MW, the current practice is a pressurization of 3 atmospheres. 

A solid oxide fuel cell (SOFC) consists of two electrodes anode and cathode, with a ceramic electrolyte between that transfers oxygen ions. A SOFC typically operates at a temperature between 700 and 1000 °C. at which temperature the ceramic electrolyte begins to exhibit sufficient ionic conductivity. This high operating temperature also accelerates electrochemical reactions therefore, a SOFC does not require precious metal catalysts to promote the reactions. More abundant materials such as nickel have sufficient catalytic activity to be used as SOFC electrodes. In addition, the SOFC is more fuel-flexible than other types of fuel cells, and reforming of hydrocarbon fuels can be performed inside the cell. This allows use of conventional hydrocarbon fuels in a SOFC without an external reformer. 

Liese E.A., Gemmen R.S. (2005) Performance comparison of internal reforming against external reforming in a solid oxide fuel cell, gas turbine hybrid system. ASME Journal of Engineering for Gas Turbines and Power 127, 86-90. 

Fig. 10.24 The tensile stress profile in the electrolyte for the external-reforming case ( 2) in...

Well-established anode materials are Ni cermets such as Ni/YSZ composites. The presence of the second phase increases the contact area and prevents the catalytically active Ni particles from aggregating. The use of the composite becomes problematic if hydrocarbons are to be directly converted Ni catalyzes cracking, and the resulting carbon deposition deactivates the fuel cells. Therefore either pure H2 has to be used or the fuel has to be externally reformed. A third way is internal conversion of CHV with H20 to synthesis gas. The necessary steam addition, however, reduces the overall efficiency. Another problem of Ni cermets, if they are to be used at lower temperatures, is a potential oxidation of the Ni. Alternatives are Cu/Ce02 cermets in which Cu essentially provides the electronic conductivity and Ce02 the catalytic activity. Note that an efficient current collecting property of the electrode presupposes a metal concentration above the percolation threshold. 

Both the 2000 doe analysis and a 2003 analysis by the Fuel Cell and Hydrogen Research Centre in Berlin suggest that solid oxide fuel cells (sofcs) may be a better candidate for home fuel cells because they have higher electric efficiency, they do not need an expensive external reformer, and they have more usable heat.27 For home use, however, sofcs would have their own limitations. Since they operate at very high temperatures, they take a long time (several hours) to warm up, which is why they operate much better in commercial and industrial applications that require high levels of electricity continuously. 

The indirect internal reformer (HR) is situated within the cell stack in separate reforming channels, where only the reforming reaction takes place. This concept features energetic coupling with the exothermic oxidation process. The main advantage is that no external heat exchanger is required, as the separator plate between HR and anode channel fulfills this function. The HR can be seen as an external reformer operating at fuel cell temperature. 

In 1993 Energy Research Company (ERC) of Danbury and Torrington, CT, made a test of a 120 kW MCFC for 250 h [333], This is a prototype stack for a 2 MW, natural-gas-fueled power plant [358], ERC has announced that after these initial demonstrations it expects its MCFC power plant of about 100 MW to be commercialized at the beginning of the next century. In Japan, Tonen Corp., Sanyo Electric Corp. and Toyo Engineering Corp. are conducting tests on 10 kW external-reforming-type MCFC stacks [338], Likewise, in 1993, Hitachi Ltd. [359] has... 

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