0581.5271 electrochemistry for engineers lecture 2 lecturer: dr. brian rosen office: 128 wolfson...
TRANSCRIPT
0581.5271 Electrochemistry for Engineers
LECTURE 2
Lecturer: Dr. Brian Rosen Office: 128 Wolfson
Office Hours: Sun 16:00
The Electrochemical CellPart II
Lower Stability of Water
Starting withH+(aq) + e- ½H2(g)
we write the Nernst equation
We set pH2 = 1 atm. Also, Gr° = 0, so E0 = 0. Thus,
we have
pHE 0592.0
H
H
a
pEE
21
2log1
0592.00
Upper Stability of Water
½O2(g) + 2e- + 2H+ H2O
but now we employ the Nernst eq.
2
0
21
2
1log
0592.0
HO apn
EE
We assume that pO2 = 1 atm. This results in
This yields a line with slope of -0.0592.
221
2log0296.023.1
HO apE
pHpE O 0592.0log0148.023.12
volts23.1)42.96)(2(
)1.237(00
n
GE r
pHE 0592.023.1
Upper Stability of Water
Recall pH = -log (aH+)
The Electrochemical Series
Pourbaix Diagram
Pourbaix Diagram of Water Stability vs. Ag/AgCl?
Recall: A Good Reference is Non-Pol.
0.00V vs. SHE +0.197V vs. SHE+0.00 vs. Ag/AgCl
Pourbaix Diagram vs Ag/AgCl
E = 1.03 V vs. Ag/AgCl
E = -.197 V vs. Ag/AgCl
Reconsider : Galvanic vs. Electrolytic
+ E- E
E° Cu/Cu+
=0.340 V vs. SHE
Cu+2 + 2e- Cu + i
- i
When the electrode is heldat its equilibrium potential,the forward and reverse current cancel and the NET current is zero
Equilibrium (Non-polarized)
+ E- E
E° Cu/Cu+
=0.340 V vs. SHE
Cu+2 + 2e- Cu + i
- i
When the electrode is negative ofits equilibrium potential, reductionis favored and there is a net flow ofelectrons consumed by the electrodefor the reduction reaction.
ΔE
Cathodic Polarization
+ E- E
E° Cu/Cu+
=0.340 V vs. SHE
Cu+2 + 2e- Cu + i
- i
When the electrode is positive ofits equilibrium potential, oxidationis favored and there is a net flow ofelectrons produced for the oxidation reaction.
ΔE
Anodic Polarization
Real Polarization of Electrodes
In reality, I-V curves for electrodestake on a variety of shapes and forms dependent on the kinetic and mass-transport parameters
1M Cd+2 1M Cu+2 CuCd
OPEN CIRCUIT POTENTIAL (OCP)
Cd+2 +2e- Cd Cu+2 +2e- Cu
+ E- E
i
E° Cd/Cd+2
-0.40 vs. SHE
+ E- E
E° Cu/Cu+2
+0.34 vs. SHE
E Cell (OCP) = 0.74 V i
1M Cd+2 1M Cu+2 CuCd
GALVANIC CELL (SPONTANEOUS)
Cd+2 +2e- Cd Cu+2 +2e- Cu
+ E- E
E° Cd/Cd+2
-0.40 vs. SHE
+ E- E
E° Cu/Cu+2
+0.34 vs. SHE
+∆E -∆E
-0.35V
+0.29V
E Cell = 0.64 V
e-
e-
+CATHODE
-ANODE
i i
1M Cd+2 1M Cu+2 CuCd
ELECTROLYTIC CELL
Cd+2 +2e- Cd Cu+2 +2e- Cu
+ E- E
E° Cu/Cu+2
+0.34 vs. SHE
+ E- E
E° Cd/Cd+2
-0.4 vs. SHE
+∆E-∆E
+0.75V
+0.29V
E Applied = 1.5 V
e-
+ANODE
-CATHODE
1.5Ve-
-0.75V ii
Summary • Galvanic (spontaneous cells) operate below their
maximum potential (OCP) due to the electrode polarization required to produce current (anode E is less negative than E°, and cathode E is less positive than E°)
• Electrolytic cells require an external voltage more than the minimum required OCP predicted by thermodynamics (anode E is more positive than E°, cathode E is more negative than E°)
η = (E - E°) = “overpotential”
Electrode Processes
KINETICS
MASS-TRANSFERdiffusion
convection migration
Electrochemical Kinetics
Electrode Processes
KINETICS
MASS-TRANSFERdiffusion
convection migration
(FAST)(SLOW)
In our modeling of kinetics, we will assumethat mass transfer to the electrode is fast
compared to the reaction rate
Our Goal
i = f(E)
How can we model the current at an electrode as a function of its potential assuming the reaction is the rate limiting step? (i.e. mass
transfer to the electrode is FAST)
Surface vs. Bulk Concentration
• Surface concentration of A
CA f(x,t)
..at surface x=0, therefore surface concentration is CA (0,t) or (CA for short here)
CA* is the symbol we will use for “bulk”
concentration
Basic Rate Laws (1st order rxn)
kf
kb
Ox + ne- Red
OxfOx
f Ckdt
dN
dRebdRe
r Ckdt
dN
dRebOxfdReOx
net CkCkdt
)NN(d
NOTE Cox is really Cox(0,t), the surface concentration of “Ox”!
Likewise Nox is the number of molsOf “Ox” on the surface
Therefore v is in units of mols/(time*area)
Measured Current
i [=] Coulombs / s
F is the “molecular weight equivalentof electrons in Coulombs / mol
dRebOxfdReOx
net CkCkdt
)NN(d
)( RedbOxfanocathnet CkCkFAiii
FA
i
dt
NNd netdOxnet
)( Rev [=] mol/(sec*cm2)
#mols Ox on surface
Hg
Na+
Mercury Drop Electrode
Na+ + 2e- Na E° = - 2.71 V vs. SHE
Na+ + 2e- Na(Hg) E° = - 2.71 V vs. SHE
Dangerous!
Solid Na is NOT stable, hence the VERY negative E°Reacts exothermically with moisture
The Energy Barrier
1. Reconfiguration of atomic position2. Repulsion forces3. Desolvation of ions in solution
Even though the reaction is favorable according to THERMODYNAMICS, it must overcome anenergy barrier.
LARGER BARRIER = SLOWER REACTION
Reasons for Energy Barriers
AB + CGib
bs F
ree
Ener
gy
+
- Energy increasesas we bring the sodium ioncloser to the Na(Hg) surfacedue to repulsion forces.Vice-versa also true for energy of amalgamated sodium atom
Changing the potential changes the energy of the participating electron
Na+ +e- Na (Hg)
The Hg drop electrode is ANODICALLY polarized by ΔE = E - E°The energy of the electrode changes by F ΔE
Na+ +e- Na (Hg)
+
-
Charge x Voltage = Energy
Na+ +e- Na (Hg)+
-
How do the anodic and cathodic activation barriers change with overpotential (η = E-E°)?
Symmetry Factor, α
• The symmetry factor, α, describes what fraction of the overpotential goes towards changing the CATHODIC barrier.
• (1-α) , same for ANODIC barrier
• For multistep/multi-electron reactions, the symmetry factor is called the transfer coefficient
+
-
Na+ +e- Na (Hg)
(1-α)F Δ E
αFΔE
R+
-
Cathodic barrier goes up by the same amount that the anodic
barrier goes downCathodic barrier goes up by less than the anodic barrier
goes downCathodic barrier goes up by
more than the anodic barrier goes down
Defining the Rate Constant
Substituting our expression for how ΔG changes with η we get
defining a standard rate constant )exp(0
0
RT
GAk
Where f = F/RTWe assume Af = Ab
Butler-Volmer Equation
)CkCk(nFAiii dRebOxfanocath
Inserting our expression for the rate constants into our expression for total current
We get:
RT
EEF
dRT
EEF
Ox eCeCFAki)()1(
Re
)(0
00
We now have our relationship for how the current at an electrode varies with overpotential!
At Equilibrium kf
Recall that at equilibrium, the kinetic model and the thermodynamic model
must match!!!
kb
Ox + ne- Red
At Equilibrium
0CkCkdt
)NN(ddRebOxf
dReOxnet
Ox
dReeq
b
f
C
CK
k
k
but….. νf and νr are NOT ZERO, rather, they cancel!
kf
kb
Ox + ne- Red
Equilibrium
At equilibrium, the surface concentration C(0,t) equals the bulk concentration in solution C*
Which is just an exponential form of the Nernst equation
Kinetic model breaks down into thermodynamic model at equilibrium
Exchange Current Density • Although the NET current is zero, the anodic and cathodic
currents still have equal but opposite values known as the exchange current density
Raise both sides to -α
Substitute into
to get
Note i0 is dependent only on kinetic parameters!
Current-Overpotential Equation
• Divide the Butler-Volmer Equation by i0 to get:
Simplifies to :
..where f = F/RT
i0 Visualized
Effect of i0 on Polarization
Effect of Symmetry Factor on Polarization
Tafel Plot
at large η either the left or the right side becomes negligible.
..where f = F/RT
What happens when we account for mass transport?
Fig.1.1 Schematic j/E plot for the electrolysis of 1.0 M solution
of KI in H2SO4, employing two Pt electrodes. The minimum
potential for dc current flow is 0.56 V.