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Anodic
reaction
cathodic
reaction
Active dissolution
Passivation and conversion
Anodization
Inert
anode
Active
anode
Oxidation of species in
solution
reduction of species in solution
reduction of oxide/conversion layer
Electrolysis
reaction
§7.12 Basic principal and application of electrolysis
For evolution of gas, the overpotential is relatively large,
therefore, the overpotential should be taken into
consideration.
Ag+, Cu2+, H+, and Pb2+ will liberates at 0.799 V; 0.337 V;
0.000 V; -0.126 V, respectively without consideration of
overpotential;
Overpotential of hydrogen liberation on Cu is 0.6 V, on Pb
is 1.56 V
0.337 V
⊖ Cu2+/Cu
-0.126
⊖ Pb2+/Pb
0.799 V
⊖Ag+/Ag
0.000
⊖ H+/H2
For liberation of metal, the overpotential is usually very
low, and the reversible potential can be used in stead of
irreversible potential.
1. Cathode reaction
§7.12 Basic principal and application of electrolysis
a(Ag+) = 1.510-8
0.799 V
a(Cu2+) = 2.210-16
0.337 V
a(Pb2+) = 3.310-49
-0.126 V -1.56 V
The liberation order and the residual concentration of the ions upon negative
shift of potential of cathode
Potential sweep and residual concentration
1. Cathode reaction
§7.12 Basic principal and application of electrolysis
2) Application
1) Separation of metal (Lanthanum)
2) Quantitative and qualitative analysis (polarography)
3) Electroplating of single metal and alloy
4) Electrolytic metallurgy (Al, Ti, Mn)
5) Electrorefining of metal (Cu)
6) Electrosynthesis (Aniline)
1. Cathode reaction
§7.12 Basic principal and application of electrolysis
2. Anode reaction
When inert material such as Platinum and graphite
was used, the species in the solution discharge on
the electrode in the order of liberation potential.
F < Cl < Br < I
Henri Moissan
1906 Noble Prize
France
1852/09/28 ~ 1907/02/20
Investigation and isolation of the element fluorine
1) Reaction on inert anode
§7.12 Basic principal and application of electrolysis
(1) Active dissolution;
(2) Anodic passivation
(3) Anodic oxidation
2) Reaction of active anode
Pourbaix diagram of iron-water system
(1) Active dissolution:
At pH=4 and low current density, active
dissolution occurs.
Fe Fe2+ + 2e
Fe2+
Fe2O3
Fe
pH
/ V
2 4 6 8 10 12 140
Fe3O4
Fe3+
FeO22
We usually judge the reaction based on
Porbaix diagram
2. Anode reaction
§7.12 Basic principal and application of electrolysis
(2) Anodic passivation:
At pH= 12 and high potential, upon polarization,
compact thin layer of Fe3O4 forms and passivation
of iron takes place.
3Fe + 4H2O – 8e Fe3O4 + 8 H+
Passivation curve of iron
Active dissolution
passivation
Trans-passivation
2. Anode reaction
§7.12 Basic principal and application of electrolysis
Anodic oxidation of aluminum at
constant current density(3) Anodic oxidation
t / hE
/ V
Barrier
layer
Porous
layer
Initiation
of pores
2. Anode reaction
§7.12 Basic principal and application of electrolysis
top surface
Cross-section
1) Corrosion:
Destruction of materials due to the
chemical, electrochemical and physical
attack of the media.
White marble of Jinshui Bridge, Beijing
Stone Sculpture before the Capitol, Washington D.C.
1. General introduction
§7.13 Corrosion and protection of metals
metal
Surroundings
(1)Materials:
(2)Environment:
(3)Reaction;
(4)Uniformity;
(5)Other
1. General introduction
§7.13 Corrosion and protection of metals
metal
film
Surroundings
Local corrosion:
1) uniformity of
metal
2) Surface film
3) Solution
2. Theoretical consideration
Zn + 2 HCl ZnCl2 + H2
Why does Zn of 99.5 % purity dissolve in dilute HCl in 1 min, while that of
99.999% purity does not dissolve even after 8 h?
anode reaction:
Zn Zn2+ + 2e
Cathode reaction:
2H+ + 2e H2
Conjugation reaction
§7.13 Corrosion and protection of metals
Conjugation reaction
Corrosion current Corrosion / stable / mixed potential
2H+ + 2e H2
H2 2H+ + 2e
Zn Zn2+ + 2e
Zn2+ + 2e Zn
re Zn2+/Zn
re H+/H2
/
V
lg jlg jcorr
corr
2. Theoretical consideration
§7.13 Corrosion and protection of metals
re Zn2+/Zn
re H+/H2
2H+ + 2e H2
H2 2H+ + 2e
Zn Zn2+ + 2e
Zn2+ + 2e Zn
lg jcorr
/
V
lg j
corr
metal
Surroundings
film
1) metal
2) Surface film
3) Solution
4) Electricity
3. Corrosion protection
§7.13 Corrosion and protection of metals
1. Classification of batteries
1) The way to use
Primary battery: Dry battery
Secondary/rechargeable battery: Lead-acid battery
Fuel cell: direct methanol cell
Liquid-fluid cell:
2) Type of electrolyte
Acidic battery: Lead-acid battery
Neutral battery: Neutral dry battery
Basic battery: Basic dry battery, Cd-Ni battery
§7.14 Chemical power sources
Energy conversion efficiency:
internal combustion: 20%25%
electrical power generation: 35%40%
fuel cells: 50%60% or more, depending on type
Advantages:
1) low noise; 2) high efficiency; 3)
small scale; 4) portable
G H T S
Electric energy Chemical energy Heat
100%G
H
Energy conversion efficiency
§7.14 Chemical power sources
3. Parameters for chemical batteries
Working voltage:
1.2 V for dry battery, 3.0 V for lithium-ion battery
Nominal Capacity:
1200-1500 mAh for AA type nickel-hydride battery
Power density: (Wh/kg, or Wh/L)
lead-acid batter is much lower than lithium battery
Cycle life: for lead-acid battery > 500 charge-discharge cycles required.
Charge-discharge efficiency: the higher, the better
Self-discharge: the less, the better
Environment friendliness: no hazard materials was used.
§7.14 Chemical power sources
Parameters Lithium-ion Ni-Cd Ni-MH
Mass power density (Wh/kg) 90 40 60
Volume power density (Wh/1) 210 100 140
Nominal voltage (V) 3.7 1.2 1.2
Cycle life 1000 1000 800
Self-discharge(%/month) 6 15 20
Parameters for lithium-ion, nickel-cadmium and nickel-metal
hydride batteries
§7.14 Chemical power sources