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0.7 0.6 0.5 0.4 0.3 0.2 0.1 0 0 1000 2000 3000 Current density, J (A/m2) 7000 8000 Ohmic activation Cathode activation Anode activation Figure 6.2: Variations of electrolyzer overpotentials at various current densities. Table 6.3 lists the thermodynamic specifications of the multigeneration system, including heating and cooling loads, electricity generated by the turbines, COP of the absorption chiller, combustion chamber mass flow rate, hydrogen production rate, hot water mass flow rate and cost of environmental impact. Table 6.3 : Parameter values resulting from energy and exergy analyses of the system. Parameter Value 0.64 5788 1219 43 10000 786 252 61 59 1.25 3.58 0.44 132 7 67.65 1090 19.6 1.73 4000 5000 6000 ̇ ̇ ̇ ̇ ̇ ̇ ̇ Ψmulti (%) ̇ (kg/h) ̇ (kg/s) Absorption chiller COP CO2 emissions (kg/kWh) CO emissions (kg/kWh) ̇ ($/h) Total costa rate ($/h) Total exergy destruction rate (MW) Sustainability index (kg/s) (kW) (kW) (kW) (kW) (kW) (kW) ηmulti (%) 118 Overpotential (V)PDF Image | Energy Systems for Multigeneration Purposes
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