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Instructions for a laboratory experiment aimed at investigating the electrochemical behavior of Fe(CN)6 and Co(NH3)6 using cyclic voltammetry. It explains the concept of electrode capacitance, the role of redox couples in electrochemical systems, and the impact of electrode contamination on the experiment. It also discusses the calculation of charging current and the analysis of cyclic voltammograms to determine the formal potential and diffusion coefficient of Fe(CN)6.
Typology: Lecture notes
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Objectives
Introduction
Electrode Reactions and Electrode Capacitance
Figure 1 describes the process that occurs in simple electrode reactions. In the case of reduction, a species (O) capable of receiving an electron from the electrode diffuses to the surface, receives an electron and diffuses away from the surface. Current at the surface is generated by the transfer of electrons from the electrode to the redox species. In solution current is carried by migration of ions. You already studied this in your measurements of conductivity.
One can ask whether a current can occur if there is no species in the solution that can transfer electrons to the surface at the potential of interest. The answer is that a transient current can flow because the electrode-solution interface will behave as a capacitor. As the potential of the electrode is varied, ions move to the surface to form a double-layer as show in Figure 2.
Although strictly speaking an electrode-solution interface in the absence of a redox couple is not a pure parallel-plate capacitor, it behaves rather like one and a parallel-plate capacitor model is often adequate to describe electrochemical systems. Use of this model allows us to learn about the behavior of electrodes in the absence of a redox couple.
For a simple parallel plate capacitor, charge on the capacitor, Q , is proportional to the voltage drop across the capacitor, E :
electrode
ne-
O
R
diffusion Bulk
O*
R*
double layer C (^) dl
R (^) ct Z (^) D
R (^) soln
Figure 1. Electrochemical system that includes electron transfer along with its equivalent circuit.
E l e c t r o d e
Figure 2. Schematic diagram Q = CE (1) of an^ electrical double^ layer.
The proportionality constant C is the capacitance of the medium. The simplest description of electrochemical capacitance is the Helmholtz model given by:
where ε is the dielectric constant of the material separating the parallel plates, εo is the permittivity of free space, l is the separation between the plates, and A is the area of the electrode. This model does not adequately describe all electrochemical interfaces as the capacitance can depend on both potential and the supporting electrolyte. Still it is a helpful construct.
Capacitance is a crucial factor in electrochemical experiments because it gives rise to current during the charging of the capacitor. Rather logically (and without imagination), we term this charging current. To calculate the magnitude of this current, we differentiate equation (1) with respect to t and assume that capacitance is constant:
Recognizing that dQ/dt is an expression for current and dE/dt is the potential scan rate ν, we obtain:
From this very simple derivation, we have an expression for the charging current at steady state when applying a ramping voltage. Thus by measuring the charging current at a given scan rate, you can determine the capacitance of the system. If there is no possibility for electron transfer between the solution and the electrode (we don’t add a redox couple) this is the only current that we will observe.
Let’s now consider the very simple cyclic voltammetry (no active redox couple present) experiment shown in Figure 3. We apply the potential form shown in the figure. Initially, we have a sharp rise in current because of a sharp change in the scan rate ν. The current then reaches steady state as we are constantly varying the voltage. At reversal of the scan rate, the current
Figure 3. Schematic explanation of a cyclic voltammetry experiment in the absence of a redox couple.
A l
dt
dE C dt
dQ = (3)
i = Cv (4)
without proof. (The details of CV simulations can be found in Anal. Chem. , 1964 , 36, 706 and Anal. Chem. 1965 , 37 , 1351.)
First we give the qualitative, pictorial explanation. If we assume that concentrations at the surface are governed by the Nernst equation, the concentration of the oxidized species at the surface will decrease as the potential becomes more negative. Assuming that the electron transfer rate is very rapid, the current i that is measured as the potential is decreased will be directly related to diffusion rate of oxidized species to the electrode surface:
where n is the number of electrons, F is Faraday’s constant, A is the area of the electrode surface and J is the flux of the oxidized species to that surface. The flux is governed by Fick’s law:
where, D is the diffusion coefficient of the species, x is the distance from the electrode surface, (dC/dx)x=0 is the concentration gradient at the surface, C* is the concentration of the oxidized species in the bulk solution, and C (^) x=0 is its concentration at the surface. As you can see, the greater the concentration gradient, the greater the flux J and therefore by equation (6), the greater the cathodic current.
The change in the concentration gradient for the cathodic portion of the cyclic voltammogram is shown in Figure
Concetration of Oxidized Species
C*
Distance From Electrode
t=
time
Figure 5. Crude concentration profiles at different time in a CV experiment (only the negative scan is shown). The equations are
i = nFAJ (6)
x
dx
dC J D x x ∆
=
0
As we reverse the voltage scan (not shown in Figure 5), we still have a layer depleted of the oxidized species, but the surface concentration begins to rise so current decreases further. Finally, we reach a region where anodic current begins to dominate (Figure 6). Then we begin to go through similar concentration profiles for the reduced species. We will achieve a peak negative current and then the current will decrease in magnitude as the depletion layer for the reduced species increases.
That was a very qualitative description of CV. Nicholson and Shain performed quantitative simulations of CV in 1964 and the field of electrochemistry changed in a major way. All reversible voltammograms look the same and the typical shape is that shown in Figure 6. The quantitative simulations show several things for a Nernstian system. The peak current in a cyclic voltammogram containing only one species is described by:
at 25 °C where i (^) p is the peak current, n is the number of electrons transferred, A is the electrode area, D is the diffusion coefficient of the species, v is the scan rate and C* is the bulk concentration of the species. The difference between Ep and the point where current is half that at Ep , Ep/2 , is 56.5/ n mV at 25 °C, where n is the number of electrons transferred. Note that for a Nernstian system, Ep should be independent of scan rate, but i (^) p will depend on the square root of scan rate. Another useful piece of information is that the separation of anodic and cathodic peaks is about (59/ n ) mV at 25 °C. It is very difficult to achieve a 59/ n mV splitting at most solid electrodes. (If you can achieve 70 mV, you will be doing well. This is a function of electrode preparation as well as scan rate.) If the diffusion constants for the oxidized and reduced species are similar, the value of Eo^ ’ can be estimated from the average of Epa and Epc , where E (^) pa is the potential of the anodic peak current and E (^) pc is the potential of the cathodic current. Thus, in your experiments you will use CV to estimate the value of Eo’ for the Fe(CN) 6 3-/4-^ couple. You will also use the peak current to estimate the diffusion coefficient for Fe(CN) 6 3-. One other characteristic of a reversible system is that i (^) pa and i (^) pc are the same, but i (^) pc has to be determined as shown in Figure 6.
Current (arbitrary units)
0
switching point
i (^) pc
i (^) pa
≈E o’
E (^) p/
Figure 6. Shape of a cyclic voltammogram for a Nernstian electrochemical reaction.
i (^) p = ( 2. 69 × 105 ) n^3 /^2 AD^1 /^2 v^1 /^2 C * (8)
Procedure
(1) Write an introductory paragraph including the objectives of this experiment.
(2) Determine the diffusion coefficient of Fe(CN) 6 3-^ from your cyclic voltammograms at clean gold electrodes. Do this for the three different scan rates. What assumptions are you making when you do this calculation? Do the CV’s justify this assumption? Why wouldn’t you do this calculation at a monolayer-coated electrode. Which one of the scan rates would you expect to give you the most accurate value of the diffusion coefficient?
(3) Approximate the formal potential of Fe(CN) 6 3-^ from its CV at bare gold. Convert this value to versus NHE and compare it with literature values.
(4) Using the voltammograms in just Na 2 SO 4 , calculate the capacitance/area of the bare gold system. Does the capacitance vary with scan rate? The diameter of the electrode is 3 mm.
(5) From your capacitance, determine the dielectric constant at the interface. Assume a parallel plate capacitor with a separation between the plates of 3 Å.
(6) Determine the capacitance/area of the electrode coated with the self-assembled monolayer. Determine a dielectric constant for the monolayer assuming that it is 25 Å thick. Does this value of dielectric constant seem reasonable?
(7) Why does hexaamine(cobalt(III)) have an irreversible CV? You may need to consult an inorganic textbook to study the relative lability of cobalt(III) and cobalt(II) complexes.
(8) Explain why the monolayer changed the CV of Fe(CN) 6 3-.
(9) Write a short paragraph stating your conclusions from this lab.