Electrochemical Properties of Materials for Electrical Energy Storage Applications

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1 Electrochemical Properties of Materials for Electrical Energy Storage Applications Lecture Note 3 October 11, 2013 Kwang Kim Yonsei Univ., KOREA kbkim@yonsei.ac.kr 39 Y O N Se I 126.9

2 Nernst Equation Nernst equation for an electrode reaction of O + ne = R as: G = G 0 + RT ln ((a (Reductant) /a (Oxidant) ) -G = zfe, -G 0 = zfe 0 E = E 0 -(RT/nF) ln (a (Reductant) /a (Oxidant) ) Other thermodynamic quantities can be derived from electrochemical measurement. G = H- TS, dg = VdP S dt S = -(G/T) p S = nf (E cell /T) p H = G + TS = nf [T(E cell /T) p -E cell ] RT ln K rxn = -G 0 = zfe 0

3 Reversibility Thermodynamics : system at equilibrium : reversibility Chemical reversibility : Pt/H 2 /H +, Cl - /AgCl/Ag Overall H 2 + 2AgCl 2Ag + 2H + + 2Cl - One can overcome the cell voltage by opposing it with the external dc source, then the current flow through the cell will reverse. The new cell reaction is 2Ag + 2H + + 2Cl - H 2 + 2AgCl Thermodynamic reversibility A process is thermodynamic reversible when an infinitesimal reversal in the driving force causes it to reverse direction. Obviously, this cannot happen unless the system feels only an infinitesimal driving force at any time. Hence, the system essentially be always at equilibrium.

4 Reversibility Thermodynamics : system at equilibrium : reversibility Practical reversibility : Reversible process : infinitely slow process Since all actual processes occur at finite rates, they cannot proceed with strictly thermodynamic reversibility. However, a process may be in practice be carried out in such a manner that thermodynamic equations apply to a desired accuracy. Example; Removal of a large weight from a spring balance Reversible removal of a weight requires continuous equilibrium of Kx = mg. The spring is never prone to contract more than an infinitesimal distance because the weight is removed progressively in infinitesimal portions.

5 Reversibility Practical reversibility (continued) O + ne = R E = E o - (RT/nF) (a R /a O ), E o =? If the system follows the Nernst equation, the electrode reaction is often said to be thermodynamically or electrochemically reversible (or nernstian). Reversibility of a process ; one s ability to detect the signs of disequilibrium Rate of change of force driving the observed process vs. speed with which the system can reestablish equilibrium If the perturbation applied to the system is small enough, or if the system can attain equilibrium rapidly enough compared to the measuring time, thermodynamic relation will apply.

6 Reaction at each electrode (half cell reaction) Differing reactivities of metals of Mg and Cu: When metals react, they give away electrons and form positive ions. This particular topic sets about comparing the ease with which a metal does this to form hydrated ions in solution for example, Mg 2+ (aq) or Cu2+ (aq).

7 Electrode/Solution Interface :Electric Double Layer Capacitance Electrode: Electronic conductor Charge transported by electron Solution: Ionic conductor Charge transported by ion : Charge Transfer Resistance (a) Non Faradaic Process :Double Layer Charge/Discharge (b) Faradaic Process : Charge Transfer Reaction, Redox reaction

9 Ideal Polarizable Electrode (interface) :Electric Double Layer Capacitance X : Charge Transfer Resistance R F : infinite resistance

10 Ideal Non Polarizable Electrode (Interface) X :Electric Double Layer Capacitance : Charge Transfer Resistance R F : Zero

11 Electrical double layer Diffuse Layer Bulk Electrolyte Solid Aqueous Solution The charged surface and the diffuse ion layer of counterions form a double-layer (diffuse) capacitor.

12 From Coulomb s Law, F c q 1 q 2 4D 0 r 2 By integration we can estimate the energy to separate a charge q1 from q2. In water W~1.9x10-20 J, In Air W~1.5x10-18 J Clearly it is the high dielectric constant or polar nature of water which causes dissociation. In air or hexane (D~2), no dissociation is expected. This is why NaCl dissolves in water but not in oil.

13 Electrical Double Layer The model which gave rise to the term 'electrical double layer' was first put forward in the 1850's by Helmholtz. - No electron transfer reactions occur at the electrode - Interactions between the ions in solution and the electrode surface are assumed to be electrostatic in nature and resulted from the fact that the electrode holds a charge density (q m )which arises from either an excess or deficiency of electrons at the electrode surface. - In order for the interface to remain neutral the charge held on the electrode is balanced by the redistribution of ions (q s )close to the electrode surface. lq m l=lq s l q m q s

14 Helmholtz Electrical Double Layer This theory is a simplest approximation that the surface charge is neutralized by opposite sign counterions placed at an increment of d away from the surface. The overall result is two layers of charge (the double layer) and a linear potential drop which is confined to only this region (termed the outer Helmholtz Plane, OHP) in solution. The result is absolutely analogous to an electrical capacitor which has two plates of charge separated by some distance (d) with the potential drop occurring in a linear manner between the two plates. q m q s lq m l=lq s l

15 Helmholtz model E 0 d Electrode possesses a charge density resulted from excess charge at the electrode surface (q m ), this must be balanced by an excess charge in the electrolyte (-q s )

16 Helmholtz model C A 0 r q V 0 r d A d q charge on electrode (in Coulomb) Helmholtz model Two sheets of charge, having opposite polarity, separated by a distance of molecular order equivalent to a parallel plate capacitor Relation of stored charge density, q, and voltage drop V between the plates q = (εε0/d)v ε :dielectric constant of the medium, ε0 : permittivity of free space, d : spacing Differential capacitance q / V = Cd= εε0/d Weakness of this model: predict Cd is const

17 Surface potential 1) Transfer of charged species e - Cu 2+ Cu 2+ (aq) e - Cu 2+ e - e - Cu 2+ Cu Cu e - e - Cu 2+ e - e - Cu 2+

18 2) Specific adsorption of ions I I I I I I I +

19 3) Orientation of dipole molecules +

20 Gouy-Chappman layer Plane of shear E 0 d Charge on the electrode is confined to surface but same is not true for the solution. Due to interplay between electros tatic forces and thermal randomizing force particularly at low concentrations, it may take a finite thickness to accumulate necessary counter charge in solution.

21 Gouy-Chappman layer Plane of shear E 0 d

22 Gouy-Chappman layer Debye Length * 2nze kt o moles L o C =1/cm C onc Does not belong N z e kt x10 1L 100cm x charge mole 10 cm m charge x10 C m Nm x10 unitless 2 N m cm J K o A C J 298K

23 Gouy-Chappman layer * zf ( 2C ) zf0 C d cosh RT 2RT 1 2 sinh x e x e 2 x Hyperbolic functions 1) Minimum in capacitance at the potential of zero charge 2) dependence of C d on concentration

24 Stern double layer Combination of Helmholtz and Guoy-Chapman Models Now the ions are assumed to be able to move in solution and so the electrostatic interactions are in competition with Brownian motion. The result is still a region close to the electrode surface (100x10-10 m) containing an excess of one type of ion but now the potential drop occurs over the region called the diffuse layer.

25 Stern double layer Combination of Helmholtz and Guoy-Chapman Models The potential drop may be broken into two contributions. ( ) ( ) m s m 2 2 s

26 Stern double layer ( ) ( ) m s m 2 2 s Inner layer + diffuse layer This may be seen as two capacitors in series: M C i C d S 1 C t 1 C i 1 C d C i : inner layer capacitance C d : diffuse layer capacitance-given by Gouy-Chapman

27 Stern double layer M C i C d S 1 C t 1 C i 1 C d Total capacitance (C t ) dominated by the smaller of the two. At low c 0 At high c 0 C d dominant C i dominant C d C t C i C t

29 Reaction Rate Energy Reactants Products Reaction coordinate

30 Activation Energy - Minimum energy to make the reaction happen Energy Reactants Products Reaction coordinate

31 Energy Reactants Overall energy change Products Reaction coordinate

32 Energy Reactants Products Reaction coordinate

34 Catalysts H H Hydrogen bonds to surface of metal. Break H-H bonds H H H H H H Pt surface

35 Energy This reaction takes place in three steps Reaction coordinate

36 E a Energy First step is fast Low activation energy Reaction coordinate

37 E a Energy Second step is slow High activation energy Reaction coordinate

38 E a Energy Third step is fast Low activation energy Reaction coordinate

39 Second step is slow High activation energy Energy Second step is rate determining Reaction coordinate

41 INCREASING TEMPERATURE NUMBER OF MOLECUES WITH A PARTICULAR ENERGY MAXWELL-BOLTZMANN DISTRIBUTION OF MOLECULAR ENERGY MOLECULAR ENERGY Because of the many collisions taking place between molecules, there is a spread of molecular energies and velocities. This has been demonstrated by experiment. It indicated that... no particles have zero energy/velocity. some have very low and some have very high energies/velocities. most have intermediate velocities.

42 INCREASING TEMPERATURE NUMBER OF MOLECUES WITH A PARTICULAR ENERGY T 1 MAXWELL-BOLTZMANN DISTRIBUTION OF MOLECULAR ENERGY T 2 TEMPERATURE T 2 > T 1 MOLECULAR ENERGY Increasing the temperature alters the distribution get a shift to higher energies/velocities. curve gets broader and flatter due to the greater spread of values. area under the curve stays constant - it corresponds to the total number of particles.

43 DECREASING TEMPERATURE NUMBER OF MOLECUES WITH A PARTICULAR ENERGY T 3 T 1 MAXWELL-BOLTZMANN DISTRIBUTION OF MOLECULAR ENERGY TEMPERATURE T 1 > T 3 MOLECULAR ENERGY Decreasing the temperature alters the distribution get a shift to lower energies/velocities. curve gets narrower and more pointed due to the smaller spread of values. area under the curve stays constant - it corresponds to the total number of particles.

44 INCREASING TEMPERATURE NUMBER OF MOLECUES WITH A PARTICULAR ENERGY T 3 T 1 MAXWELL-BOLTZMANN DISTRIBUTION OF MOLECULAR ENERGY T 2 TEMPERATURE T 2 > T 1 > T 3 MOLECULAR ENERGY No particles have zero energy/velocity. Some particles have very low and some have very high energies/velocities. Most have intermediate velocities. As the temperature increases the curves flatten, broaden and shift to higher energies.

45 INCREASING TEMPERATURE NUMBER OF MOLECUES WITH A PARTICULAR ENERGY MAXWELL-BOLTZMANN DISTRIBUTION OF MOLECULAR ENERGY E a NUMBER OF MOLECULES WITH SUFFICIENT ENERGY TO OVERCOME THE ENERGY BARRIER MOLECULAR ENERGY ACTIVATION ENERGY - E a The Activation Energy is the minimum energy required for a reaction to take place. The area under the curve beyond E a corresponds to the number of molecules with sufficient energy to overcome the energy barrier and react.

46 INCREASING TEMPERATURE NUMBER OF MOLECUES WITH A PARTICULAR ENERGY TEMPERATURE T 2 > T 1 T 1 MAXWELL-BOLTZMANN DISTRIBUTION OF MOLECULAR ENERGY T 2 E a EXTRA MOLECULES WITH SUFFICIENT ENERGY TO OVERCOME THE ENERGY BARRIER MOLECULAR ENERGY Increasing the temperature gives more particles an energy greater than E a. More reactants are able to overcome the energy barrier and form products. A small rise in temperature can lead to a large increase in rate.

47 General Chemical Reaction Equation cc + dd = aa + bb v A A v B B v C C v D D v i S i 0 v stoichiometric coefficients v C c v D d v A a v B b

48 Extent of Reaction n i n i0 v i n i n i0 v i extent of reaction (moles reacting) n i = moles of species i present in the system after the reaction occurs n i0 moles of species i present in the system when the reaction starts v i coefficient for species i in the particular chemical reaction equation (moles of species i produced or consumed per moles reacting)

49 Reaction rate 2N 2 O ) 4 NO O 2 If we want to equalize the rates then: Rate = Δ[O 2 ] = 1/4 Δ[NO 2 ] = - 1/2 Δ[N 2 O 5 ] Δt Δt Δt - divide by balancing coefficients when we equalize rates.

50 Reaction rate The problem of having several possibly different rates to describe the same reaction is avoided by defining the unique rate of reaction as the rate of change of the extent of reaction,ξ (small chi ) : Reaction rate = n d dt n 0 v J Because J J,, the change in the extent of reaction is related to the change in the amount of each substance J by, so v d J dn J Reaction rate = 1 v J dn dt J

51 Reaction rate In it s most general representation, we can discuss a reaction rate as a function of the extent of reaction: Rate = dξ/vdt where ξ is the extent of rxn, V is the volume of the system and t is time Normalized to concentration and stoichiometry: rate = dn i /v Vdt i = d[c i ]/v dt i where n is # moles, v is stoichiometric coefficient, and C is molar concentration of species i

Electrochemical Properties of Materials for Electrical Energy Storage Applications

Electrochemical Properties of Materials for Electrical Energy Storage Applications Lecture Note 2 March 4, 2015 Kwang Kim Yonsei Univ., KOREA kbkim@yonsei.ac.kr 39 Y 88.91 8 O 16.00 7 N 14.01 34 Se 78.96