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Figure 6-4 Figure 6-5 Figure 6-6 Figure 6-7 Figure 6-8 Figure 6-9 Figure 6-10 Figure 6-11 Figure 6-12 Figure 6-13 Figure 6-14 Figure 6-15 Figure 6-16 Figure 6-17 Figure 7-1 Figure 7-2 Figure 7-3 Figure 7-4 Figure 7-5 Figure 7-6 Figure 7-7 Figure 7-8 Effect of Oxidant Gas Composition on MCFC Cathode Performance at 650°C, (Curve 1, 12.6 percent O2/18.4 percent CO2/69.0 percent N2; Curve 2, 33 percent O2/67 percent CO2) (49, Figure 3, Pg. 2711) .................... 6-14 Voltage and Power Output of a 1.0/m2 19 cell MCFC Stack after 960 Hours at 965 °C and 1 atm, Fuel Utilization, 75 percent (50) ...................................... 6-15 Influence of Cell Pressure on the Performance of a 70.5 cm2 MCFC at 650 °C (anode gas, not specified; cathode gases, 23.2 percent O2/3.2 percent CO2/66.3 percent N2/7.3 percent H2O and 9.2 percent O2/18.2 percent CO2/65.3 percent N2/7.3 percent H2O; 50 percent CO2, utilization at 215 mA/cm2) (53, Figure 4, Pg. 395) ................................................................. 6-18 Influence of Pressure on Voltage Gain (55) ...................................................... 6-19 Effect of CO2/O2 Ratio on Cathode Performance in an MCFC, Oxygen Pressure is 0.15 atm (22, Figure 5-10, Pgs. 5-20)............................................... 6-22 Influence of Reactant Gas Utilization on the Average Cell Voltage of an MCFC Stack (67, Figure 4-21, Pgs. 4-24) ......................................................... 6-23 Dependence of Cell Voltage on Fuel Utilization (69) ....................................... 6-25 Influence of 5 ppm H2S on the Performance of a Bench Scale MCFC (10 cm x 10 cm) at 650 °C, Fuel Gas (10 percent H2/5 percent CO2/ 10 percent H2O/75 percent He) at 25 percent H2 Utilization (78, Figure 4, Pg. 443) .............................................................................................................. 6-29 IIR/DIR Operating Concept, Molten Carbonate Fuel Cell Design (29) ............ 6-31 CH4 Conversion as a Function of Fuel Utilization in a DIR Fuel Cell (MCFC at 650 oC and 1 atm, steam/carbon ratio = 2.0, >99 percent methane conversion achieved with fuel utilization > 65 percent (93).............................. 6-33 Voltage Current Characteristics of a 3kW, Five Cell DIR Stack with 5,016 cm2 Cells Operating on280/20 percent H2/CO2 and Methane (85)........... 6-33 Performance Data of a 0.37m 2 kW Internally Reformed MCFC Stack at 650 °C and 1 atm (13) ........................................................................................ 6-34 Average Cell Voltage of a 0.37m2 2 kW Internally Reformed MCFC Stack at 650 °C and 1 atm. Fuel, 100 percent CH4, Oxidant, 12 percent CO2/9 percent O2/77 percent N2 .................................................................................. 6-35 Model Predicted and Constant Flow Polarization Data Comparison (98)......... 6-37 Electrolyte Conductivity as a Function of Temperature (4, 5, 6) ........................ 7-3 (a) Sulfur Tolerance of Ni-YSZ Anodes (16, 17) and (b) Relationship between Fuel Sulfur and Anode Sulfur Concentration. ....................................... 7-5 Impact of Chromia Poisoning on the Performance of Cells with Different Electrolytes (From (21)) ...................................................................................... 7-6 Stability of Metal Oxides in Stainless Steels (26,27) .......................................... 7-8 Impact of LSCM Contact Layer on Contact Resistance in Cell with Metal Interconnect (from (28)). ..................................................................................... 7-8 Possible Seal Types in a Planar SOFC (from (29)) ........................................... 7-10 Expansion of Typical Cell Components in a 10 cm x 10 cm Planar SOFC with Ni-YSZ anode, YSZ Electrolyte, LSM Cathode, and Ferritic Steel Interconnect........................................................................................................ 7-11 Structure of Mica and Mica-Glass Hybrid Seals and Performance of Hybrid Seals (29) ............................................................................................... 7-13 xPDF Image | Fuel Cell Handbook (Seventh Edition)
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