Full exam for Electrochemical Energy Conversion and Storage in the Energy Engineering degree programme at Politecnico di Milano. The document covers: EECS – Prof. A. Casalegno – 14th January 2022 1 Basic Part (4.5 points per questions, minimum score 12) 1. Write the Nernst-Plank equation for mass transport in a generic electrolyte 2. Define the efficiency for a battery following a complex operation profile 3. Write Faraday’s
Full exam for Electrochemical Energy Conversion and Storage in the Energy Engineering degree programme at Politecnico di Milano. The document covers: EECS – Prof. A. Casalegno – 14th January 2022 1 Basic Part (4.5 points per questions, minimum score 12) 1. Write the Nernst-Plank equation for mass transport in a generic electrolyte 2. Define the efficiency for a battery following a complex operation profile 3. Write Faraday’s
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EECS – Prof. A. Casalegno – 14th January 2022 1 Basic Part (4.5 points per questions, minimum score 12) 1. Write the Nernst-Plank equation for mass transport in a generic electrolyte 2. Define the efficiency for a battery following a complex operation profile 3. Write Faraday’s law applied to products in an alkaline electrolyser 4. Exercise A PEM electrolyser stack consumes at full load 400 A at 360 V with an efficiency equal to 67% (LHV=120 MJ/kg). Assuming that 3% of H 2 is wasted and its performance follows the reported polarization curve, estimate the number of cell, cell area and efficiency at 20% current load. Intermediate Part (3 points per theory questions and 3.5 for the exercise) 1. Is the overpotential negative when O2 reduction occurs? Demonstrate analyzing 𝐺̃ 2. Show how voltage limits in batteries could reduce the available capacity during discharge at high C-rate 3. Exercise A PEM fuel cell operates at 80°C with pure H2 and air at 2.5 atm pressure and supplies at 0. 65 V a current density equal to 1.8 A/cm2 and related impedance is reported in the figure. Assuming that: 1. anode behaves as an ideal H 2 electrode (𝐸− + 𝜂−=0) 2. ion and mass transport effects in catalyst layers are negligible 3. the average O 2 chemical activity in the cathode channel is equal to 0.25 4. diffusion layer diffusivity is equal to 0.03 cm2/s (at 2.5 atm) and its thickness is 200 μm 5. cost of the fuel cell stack is 80 €/kW if operated at 1.8 A/cm2. Design a 90 kW stack with a maximum current density of 1.5 A/cm2, assuming a cell area of 200 cm2 and a fuel utilization of 98%, providing: minimum efficiency, number of cells and cost per kW. 𝑅𝑒(𝑍) −𝐼𝑚(𝑍) 0.1 𝛺 𝑐𝑚2 −0.0165 𝛺 𝑐𝑚2 0.14 𝛺 𝑐𝑚2 ∆𝑉 0 𝑗 1.5 V 1.8 V 0.4 A cm -2 2 A cm -2 EECS – Prof. A. Casalegno – 14th January 2022 2…
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