Chapter 2 Echem Thermodynamics

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Chapter 2: ELECTROCHEMICAL THERMODYNAMICS APPLICATION TO FUEL CELLS CHG8300F Electrochemical Engineering Elena Baranova, University of Ottawa
2 • The fuel cell was invented over 170 years ago (1839). At the time, problems with the materials, along with the invention of the combustion engine and the electric generator conspired to prevent a rollout of fuel cell technology. • Not until the 1960s was the technology rediscovered by astronautics, where cost and lavish research programs don't matter. • Due to increasing environmental pollution and our limited reserves of fossil sources of energy, new environmentally friendly fuels and efficient energy converters are in great demand. This serves to drive the research and development of fuel cells. Fuel cells
3 • The way a fuel cell works is basically the opposite of the principle of an electrolysis cell. • In a fuel cell, chemical energy from hydrogen and oxygen (or air) is directly converted to electrical energy, i.e. without a combustion process. All fuel cells essentially consist of two electrodes (cathode and anode) and an electrolyte (medium for transporting the ions), which separates the two electrodes from each other. • Fuel cells are usually classified by the type of electrolyte used. Other traits they may differ in include Service Temperature, Efficiency, and Field of application. Fuel cells
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4 In a fuel cell, chemical energy from hydrogen and oxygen (or air) is directly converted to electrical energy, i.e. without a combustion process. Fuel cells
5 Fuel cells CHG8191- Dr. Elena Baranova
6 Renewable energy Solar hydrogen technology makes it possible. Using electrolysis, available solar or wind energy is used to produce hydrogen. This is temporarily stored and used for generating power via the fuel cell anytime is needed. A clean solution indeed!
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7 What really is new ? "Yes, my friends, I believe that water will one day be employed as fuel, that hydrogen and oxygen which constitute it…will furnish an inexhaustible source of heat and light…and …as long as the earth is inhabited, it will supply the wants of its inhabitants…“ - Jules Verne, The Mysterious Island 1874
8 Hydrogen Vision….
9 PEM fuel cell PEM fuel cells use a thin, proton-conducting polymer membrane as an electrolyte. Both sides of the membrane are coated with a layer of catalyst material. The catalytic effects of the electrode (e.g. platinum) cause the hydrogen gas at the anode to break down into protons and electrons even at room temperature. The H + ions (protons) traverse the proton-conducting membrane to get to the cathode side and the electrons travel to the cathode, thereby doing electrical work. As a result, water is produced at the cathode side. Individual fuel cells, summarized into a unit and connected with each other in series, result in a "stack" of cells. The stacks' output can be varied as desired by adjusting the number of individual cells. CHG8191- Dr. Elena Baranova
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10 PEM fuel cell "stack" of cells one cell element
11 PEM fuel cell
12 Thermodynamic efficiency ( h th ) in the conversion of chemical energy to electric energy H 2 (g) 2H + + 2e - 1/2O 2 (g) + 2e - + 2 H + H 2 O(l) (Anode) (Cathode) D r G o = –237.13 kJ/mol D r H o = –285.83 kJ/mol D r S o = –163.4 J/K·mol Standard state of reactants and products (1 atm ; 298 K) H 2 (g) + 1/2O 2 (g) H 2 O(l) Oxygen Energy (+) Hydrogen Energy (–) Fuel Cell Electricity Energy = V·I·t Heat Water
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13 D r G o = –237.13 kJ/mol D r H o = –285.83 kJ/mol D r S o = –163.4 J/K·mol Thermodynamic efficiency ( h th ) in the conversion of chemical energy to electric energy (298 K ; 1 atm) H 2 (g) + 1/2O 2 (g) H 2 O(l) D r G o (total reversible electrical work obtained) = – z F E o = – 2 F E eq o 3 r eq Δ G 237.13 10 E = = 1.23 V 2F 2 96500 - × = × o r th o r Useful energy Δ G 237.13 η = = 0.83 Total available energy 285.83 Δ H - = = - Note : h th depends strongly on the working temperature and on the state (g or l) of the formed water. In a reversible operation of the fuel cell only part of the available chemical energy is converted into electric work (total available: D r H o ; useful: D r G o ).
14 Hydrogen fuel cell (298 K ; 1 atm) H 2 (g) + ½O 2 (g) H 2 O(l) = (298x0.1634) o o o 1 r r r kJ mol G H T S ( ) 237.13 285.83 298( 0.1634) 237.13 285.83 48.7 - D = D - D - = - - - - = - + H 2 (g) O 2 (g) H 2 O(l)
15 Reverse process : Electrolysis of water (298 K ; 1 atm) 1.23 V 1.23 V o o o r r r o r o 1 r G H T S G 285.83 298(0.1634) G 237.13 kJ mol - D = D - D D = - D = = (101.3x10 3 Pa)(1.5 mol)(22.4x10 -3 m 3 /mol)(298 K/273 K) o o r r o r o 1 r U H P V U 285.83 3.72 U 282.11 kJ mol - D = D - D D = - D = H 2 O(l) H 2 (g) + ½O 2 (g) Change in internal energy
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16 Comparison of electrolysis and fuel cell process The fuel cell process is the reverse reaction of water electrolysis. The Gibbs free energy change ( D r G o ) is that which you actually have to supply if you want to drive a reaction (electrolysis) or the amount that you can actually get out if the reaction is working for you (fuel cell). In electrolysis where the enthalpy change is 285.8 kJ ( D r H o ) you have to supply 237 kJ ( D r G o ) of energy to drive electrolysis and the heat from the environment 48.7 kJ (T D r S o ) will contribute to help you. In the fuel cell you can get out the 237 kJ ( D r G o ) as electric energy, but have to dump 48.7 kJ (T D r S o ) to the environment. H 2 O(l) H 2 (g) + ½O 2 (g) Electrolysis Fuel cell
17 Influence of temperature on the thermodynamic efficiency ( h th ) State of water product T/°C D r G o /kJ mol -1 E eq /V h th Liquid 25 - 237.2 1.23 83 Liquid 80 - 228.2 1.18 80 Gas 100 - 225.2 1.17 79 Gas 200 - 220.4 1.14 77 Gas 400 - 210.3 1.09 74 Gas 600 - 199.6 1.04 70 Gas 800 - 188.6 0.98 66 Gas 1000 - 177.4 0.92 62
18 Thermodynamic efficiency ( h th ) in the conversion of chemical energy to electric energy o o o o r r r r th o o o r r r Δ G Δ H TΔ S Δ S η = 1 T Δ H Δ H Δ H - = = H 2 (g) + 1/2O 2 (g) H 2 O(l) D S for this reaction is negative then T D S is the amount of heat dissipated into the environment (even in a reversible operating fuel cell). We can define a characteristic temperature at which the fuel cell delivers only heat (entropic heat). It is the temperature where D r G=0 (T D r G=0 ). r r r th G=0 r r G=0 r Δ S T η 1 T 1 T Δ H Δ H with T Δ S D D = - = - = G 0 r T 5000 K D = = For the overall reaction of hydrogen oxidation
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19 Electrochemical efficiency ( h el ), conversion efficiency ( h c ) and actual efficiency ( h o ) of a fuel cell As soon as the cell drives a current through the external circuit, the cell potential falls from the equilibrium value E eq to E (with E eq >E). The electrochemical efficiency depends on the operating current and is given by the relation: el eq E η = E The conversion efficiency takes into account the incomplete conversion of reactant (H 2 ) into products. 2 c 2 mass of fuel (H ) reacted in the cell η = mass of fuel (H ) input to the cell The actual efficiency ( h o ) of an electrochemical energy converter : o th el c η = η η η × ×
20 Derivation of the Carnot efficiency (CE) The derivation of the Carnot efficiency is based on the first and second law of thermodynamics: According to the first law : the energy is conserved Q 1 = Q 2 + W According to the second law : in any isolated and spontaneous process the entropy change of the system is positive (or zero in case of a reversible process) 1 2 2 2 1 1 1 1 Q Q Q T W CE = = 1 1 Q Q Q T - = - = - Conversion of heat into work 2 1 2 1 Q Q 0 T T - = 1 W CE = Q The Carnot efficiency (CE) is given by Combining the above three equations we obtain 2 2 1 1 Q T Q T =
21 Heat produced by the combustion reaction (Q 1 ) at T 1 : H 2 (g) + 1/2O 2 (g) H 2 O (l) Waste heat (Q 2 ) at T 2 Efficiency of heat engine (Carnot’s theorem) 1 2 2 2 1 1 1 1 Q Q Q T W CE = = 1 1 Q Q Q T - = - = -
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22 Carnot efficiency (CE) and thermodynamic fuel cell efficiency ( h th ) 2 T Carnot efficiency CE 1 T Þ = The Carnot efficiency (CE) is a monotone increasing function approaching unity (100% efficiency) at very high temperature The thermodynamic fuel cell efficiency ( h th ) is a linear decreasing function approaching unity (100% efficiency) at low temperature There is a break-event point at the temperature (T BE ) where CE = h th o BE BE G 0 r BE o G 0 r T T 1 1 T T T T T D = D = - = - = × with T o =298 K and T BE = 1200 K G 0 r T 5000 K D = = T BE CE h th r th G=0 T Thermodynamic fuel cell efficiency η 1 T D Þ = -
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23 The theoretical (reversible) cell potential is a function of operating temperature and pressure: where, a stands for activity or the ratio between the partial pressures of reactants (H 2 and O 2 ) or product (H 2 O) and atmospheric pressure (for liquid water product a H2O = 1). E o is a standard equilibrium potential E o eq = 1.229 V H 2 (g) + 1/2O 2 (g) H 2 O(l) Nernst equation for PEM fuel cell
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24 Theoretical cell potential at different temperatures and pressures Actual cell potentials are always smaller than the theoretical ones due to irreversible losses. Voltage losses in an operational fuel cell are caused by several factors such as: kinetics of the electrochemical reactions (activation polarization), internal electrical and ionic resistance, difficulties in getting the reactants to reaction sites (mass transport limitations), internal (stray) currents, crossover of reactants T(K) Atm. 200 kPa 300 kPa 298.15 1.230 1.243 1.251 333.15 1.200 1.215 1.223 353.15 1.184 1.200 1.209
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25 Electrochemical Thermodynamics Application to fuel cells Exercices https://www.youtube.com/watch?v=8rofx6Gaz40 https://www.youtube.com/watch?v=LDwS31OE7ak
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26 General If no other indication is given, consider the following numerical data when solving problems in Chapter 1 : Standard (1 atm, 298 K) equilibrium potential : =1.229V o eq E D H f o S o C p o kJ / mol J / mol K J / mol K C 0 5.73 8.52 H 2 0 130.5 28.8 O 2 0 204.8 29.3 CH 4 -74.6 186.3 35.3 CO -110.5 197.7 29.1 H 2 O (l) -285.8 69.9 75.2 H 2 O (g) -241.8 188.8 33.5 Water vapor pressure (at 40°C £ T £ 60°C) : p H 2 O (mbar)=1.286×10 -5 e 0.04966T(K) Consider : 1 atm ≈ 1 bar valid for H 2 (g)+½O 2 (g) H 2 O(l)
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27 Problem 1.1 A PEM fuel cell is working with pure H 2 as fuel at the cathode and with (a) pure O 2 or (b) air at the anode. 1) Calculate for both cases the open circuit potential (E eq ) at T=40 and 60°C and at different operating pressures of 1, 3 and 5 bar. For simplicity, neglect the temperature dependence of the standard potential. 2) Explain the opposite temperature dependence of cell voltage at atmospheric and high gas pressures.
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28 Problem 1.2 In a solid electrolyte fuel cell utilizing YSZ as the solid electrolyte, H 2 and O 2 are consumed at the anode and cathode, respectively, according to the reactions: H 2 (g) + O 2- H 2 O(g) + 2e - O 2 (g) + 4e - 2 O 2- The cell is working at 800 ° C with p H2 =80 kPa and p H2O =20 kPa at the anode and p O2 =100 kPa at the cathode. Calculate 1) the open-circuit potential of the cell, 2) the thermodynamic efficiency of the cell.
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29 Problem 1.3 Consider the following overall reaction taking place in a solid oxide fuel cell (SOFC) at 800 ° C : CH 4 (g) + 1/2O 2 (g) CO(g) + 2H 2 (g) 1) Estimate the thermodynamic efficiency of this fuel cell. 2)Analyze this fuel cell from the point of view of the first and second law of thermodynamics. 3) Does the cell produce or absorb heat?
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30 Problem 1.4 A PEM fuel cell working at 25°C produces a power of 10 W at 0.75 V from a single cell. 1) Calculate the amount of hydrogen and air (Nm 3 /h) needed to operate the stack consisted of 20 cells. 2) What is the electrochemical and the actual efficiency of the cell? Assume 100% utilization of reactants (100% conversion efficiency).
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