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Types voltaic cell
Conversion electrical energy to chemical energy
Electrochemistry
Electrolytic cell Voltaic cell
NH4CI and ZnCI2
Chemical and electrical energy
Redox rxn (Oxidation/reduction) Movement electron Produce electricity
Conversion chemical energy to electrical energy
Electrodes – different metal (Half cell) Electrodes – same metal (Half cell)
Chemical rxn
Electric current
Daniell cell Alkaline cell Dry cell Nickel cadmium cell
Primary cell (Non rechargeable)
MnO2 and KOH
Secondary cell (Rechargeable)
Conversion electrical to chemical energy
Electrochemistry
Electrolytic cell Voltaic cell
Conversion chemical to electrical energy
Cathode (+ve) - Reduction Cathode (-ve) - Reduction
Vs
Electron flow from anode (-ve) to cathode (+ve) electrode Electron flow from anode (+ve) to cathode (-ve) electrode
Anode
(-ve)
Spontaneous rxn Non Spontaneous rxn
Anode (-ve) – Oxidation Anode (+ve) – Oxidation
+ +
О
О
О О - -
Zn → Zn 2+ + 2e (oxidized)
Cu2+ + 2e → Cu (reduced)
Zn2+
Zn2+
Zn2+
Zn2+ - - - - → +
+ +
Cu2+
Cu2+
Cu2+
-e
-e + +
+ - - -
X-→ X + -e (oxidized)
X- X-
X-
Anode
(+ve)
Cathode
(-ve) Cathode
(+ve)
-e
-e
Y+ + e- → Y (reduced)
Y+
Y+
Y+ -e
-e
-e
-e
Anode Cathode
Voltaic Cell Electrolytic Cell
Anode Oxidation Negative (-ve) Oxidation Positive (+ve)
Cathode Reduction Positive (+ve) Reduction Negative (-ve)
Cation (+ve ion) to cathode (-ve) Anion (-ve ion) to anode (+ve)
Current – measured in Amperes or Coulombs per second 1A = 1 Coulomb charge pass through a point in 1 second = 1C/s 1 Coulomb charge (electron) = 6.28 x 10 18 electrons passing in 1 second 1 electron/proton carry charge of – 1.6 x 10 -19 C ( very small) 6.28 x 10 18 electron carry charge of - 1 C
Electric current
Flow electric charges (electron, -ve) From High electric potential – low potential Due to Potential Difference – measure with ammeter
ond
electron
ond
CoulombA
sec.1
.1028.6
sec1
11
18
Click here current/voltage
Current Electric Current – moving charges in solid wire or solution
Flow of
charges
-
-
-
Solid/Wire Solution/Electrolyte
Electron move in random
No current flow cause
No potential difference
Electrons & Protons
-
- +
+ 1A = 6.28 x 1018 e 1 second
Video on current/voltage
Potential Difference across wire
Electron move in one direction
Current flow
+ve ions -ve ions (cations) (anions)
Potential Difference applied/Battery used
ItQ t = Time/ s
Find amt charges pass through a sol if Current is 2.ooA, time is 15 mins
ItQ
Current flow
Q = Amt Charges/ C I = Current/ A
CQ 1800601500.2
Electric Potential
C
JVolt
11
Potential Diff/Voltage
-Measured in Volt with Voltmeter - 1 V = 1 Joule energy released when 1 Coulomb charge pass through 1 point - 1 V = 1 J/C
6V battery - 6J energy for every Coulomb moved bet its terminals.
V = Potential Diff
I = Current
R = Resistance
Potential diff bet 2 points is 1 V ↓ 1 J energy released when 1 C charge passes through
Voltmeter across
1Volt
1 V
Potential Diff/Voltage/Potential Energy
+ -
1 Ω 2 Ω
Charges (-ve)
flow down
AR
VI
RIV
23
6
VV
RIV
212
-
+ -
+
VV
RIV
422
Total current
Potential Diff(PD) vs Current PD = Water Pressure PD = 1.5V – 1.5J energy released 1C charge flow down PD – cause charge flow- charge flow = Called CURRENT
Potential Diff(PD) vs Current
1.5V = 1.5J/C A
D Electric potential/PD/Voltage = Electric Pressure = Volt Electric Current/Current = Charge flow = Amp Electric Potential Energy = Work done to bring a charge to a point = Joule Voltage NOT same as energy, Voltage = energy/charge Battery lift charges, Q to higher potential Potential Energy bet 2 terminals in battery stored as chemical energy
2A 2A
EMF vs PD
V = Potential Diff
I = Current
R = Resistance
Max potential diff bet two electrodes of battery source.
+ -
1 Ω 2 Ω
AR
VI
RIV
23
6
VV
RIV
212
VV
RIV
422
Total current
Current flow Circuit complete
Circuit complete ↓
Current flow ↓
Internal resistance (battery - 1Ω)
↓ Terminal PD = 8V
(Voltage drop)
Potential Diff/Voltage in Volt
Symbol for EMF = E or ℰ
Click here voltage drop
internal resistance
No Current flow in circuit
EMF (Electromotive Force) in Volt Battery = EMF = 9V
9 Volt
).(9 currentnoVEMFV
IRV
EMF Internal resistance Ir
Place voltmeter across – EMF= 9V No current flow.
ArR
EI
rRIE
IrIREMFE
19
9
)18(
9
)(
)(
)(
VV
RIV
881
VV
RIV
111
EMF = 8V+1V
8 Volt
1 Volt
Voltage measured across terminal = 8V Click here EMF notes Click here PD, PE and I
EMF (6V) = 2V + 4V
4 Volt 2 Volt
Charges passing through wire
Current flow Circuit complete
Series vs Parallel Circuit
3 Ω
AR
VI
RIV
5.018
9
VV
V
RIV
5.2
55.0
VV
V
RIV
5
105.0
Total Resistance
3 + 10 + 5 = 18Ω
Parallel Circuit Series Circuit
EMF (9V) = 2.5V + 5V + 1.5V
R = 0.625Ω
Voltage same across all component. VT = V1 = V2 = V3 Total current = sum of current in each branch. IT = I1 + I2 + I3 Total equi resistance < value of any individual resistor
Total Current
Current same in circuit
Total voltage = sum of component in series
5 Ω
10 Ω 0.5 A
VV
V
RIV
5.1
35.0
Voltage across all component
Same = 9V
Total Current = sum of all current in each branch
Total Resistance
10Ω 2Ω 1Ω
AI
R
VI
9.010
9
AI
R
VI
5.42
9
AI
R
VI
91
9
Total current (14.4A) = 0.9A + 4.5A + 9A
Ohm’s Law
Sum voltage drop equal to voltage source (EMF). VT = V1 + V2 + V3 Current same in all components in series. Total resistance = sum of individual resistances. RT = R1 + R2 + R3
Click here voltage drop
Series Circuit Parallel Circuit
• Voltage do not flow
• Charges/Current flow
• Voltage cause current to flow
• Voltage ≠ Energy
• Battery do not supply electron
• Wire contain electron, they flow
Electron in wire repel by -ve terminal move in circuit
Electron move slowly, drift velocity, electric field move at speed of light
Electric signal travel speed of light, bulb light up instantaneously,
Electric signal/field travel faster than movement of electron
Movement e – cause electric field – travel speed of light – bulb light up
Voltage Diff – Pressure diff across
Voltage Diff – Cause water/current to flow
14.4A 4.5A 0.9A 9A
Potential Diff bet Zn/Zn2+
Electrode potential Zn/Zn2+ = -ve
-
Electrode Potential
Redox Equilibrium
Zn2+
Zn → Zn 2+ + 2e (Oxidation)
Zn 2+ + 2e → Zn
(Reduction) Zn 2+ + 2e ↔ Zn
(At equilibrium)
Metal Zn placed in its sol Zn2+ ion
Equilibrium bet Zn/Zn2+
Zn metal reactive lose e form Zn2+
Equilibrium shift to right ←
Potential Diff form bet Zn/Zn2+
Potential Diff Electrode potential = -ve
Zn2+
Zn2+
Zn
Zn2+
Zn
Zn2+
Zn2+ Zn2+
Zn 2+ + 2e ↔ Zn Equi shift to ←
-
- -
Zn
- - -
-
+
+
+
+ + +
+ +
+
Voltage of Zn/Zn2+ can’t be measured. Abs electrode potential can’t measured. Only Diff in electrode potential can be measured.
Cannot measure
Abs Potential
Metal Cu placed in its sol Cu2+ ion
Equilibrium bet Cu/Cu2+
Cu2+ ion gain -2e form Cu
Equilibrium shift to left ←
Potential Diff form bet Cu/Cu2+
Potential Diff Electrode potential = +ve
Cu
Cu2+
Cu2+
Cu2+
Cu2+
Cu → Cu2+ + 2e (Oxidation)
Cu2+ + 2e → Cu
(Reduction) Cu2+ + 2e ↔ Cu
(At equilibrium)
Cu
-e
-e
-e
Cu2+
Cu2+
Cu2+
Cu2+ + 2e ↔ Cu Equi shift to →
Zn Half Cell
+
+ +
Cu
+ +
+
- - -
-
- - - - - - -
- -
Potential Diff bet Cu/Cu2+
Electrode potential Cu/Cu2+ = +ve
Cannot measure
Abs Potential
Voltage of Cu/Cu 2+ can’t be measured. Abs electrode potential can’t measured. Only Diff in electrode potential can be measured.
Click here chem database (std electrode potential)
Click here chem database (std electrode potential)
Click here interactive ECS Click here pdf version ECS
Cu Half Cell
Potential Diff Cu/Cu2+
Electrode potential Cu/Cu2+ = +ve
Potential Diff Zn/Zn2+
Electrode potential Zn/Zn2+ = -ve
Zn2+
Zn → Zn 2+ + 2e
(Oxidation)
Zn 2+ + 2e → Zn
(Reduction)
Zn 2+ + 2e ↔ Zn
(At equilibrium)
Zn2+
Zn2+
Zn
Zn2+
Zn
Zn2+
Zn2+ Zn2+
Zn 2+ + 2e ↔ Zn
Equi shift to ←
- -
-
Zn
- - -
- +
+ +
+
+ +
+ +
+
Can’t measure
Abs Potential
Cu
Cu2+
Cu2+
Cu2+
Cu2+
Cu → Cu2+ + 2e
(Oxidation)
Cu2+ + 2e → Cu
(Reduction)
Cu2+ + 2e ↔ Cu
(At equilibrium)
Cu
-e
-e -e
Cu2+
Cu2+
Cu2+
Cu2+ + 2e ↔ Cu
Equi shift to →
Zn Half Cell
+ +
+
Cu
+ + +
-
Cu Half Cell
Zn/Cu Voltaic Cell
External circuit – flow of electrons Complete circuit
- - -
- - -
- - - - - - - -
Connect 2 Half Cell with wire/ salt bridge
Zn half cell (-ve) Oxidation
Cu half cell (+ve) Reduction
Salt Bridge – flow of ions Complete the circuit
Cu2+ + 2e → Cu Zn → Zn 2+ + 2e
Zn + Cu2+ → Zn2+ + Cu
Anode Cathode
Maintain electrical neutrality
Salt bridge – saturated KNO3
Zn2+ increase ↑
NO3- flow in to balance excess Zn2+
Cu2+ decrease ↓, excess –ve ion ↑
K+ flow in to balance loss of Cu2+
Zn Cu
- - - -
Zn2+ Zn2+
Zn2+
Excess of Zn2+ ion
+ +
+ +
- - -
-
- - - - - -
- -
Excess of –ve ion
+ + +
+ + +
+
Without Salt Bridge
- + +
+
+
With Salt Bridge
(electron unable to flow due to ESF)
NO3-
NO3-
NO3-
NO3-
+
+
+ K+
K+
K+
-
- -
K+ flow in to balance
excess of – ion
NO3- flow in to balance
excess of + ion
2 Half Cell to make a Voltaic Cell
-e -e
-
-
-
-
+
+
+
+
Potential Diff Cu/Cu2+
Electrode potential Cu/Cu2+ = +ve
Potential Diff Zn/Zn2+
Electrode potential Zn/Zn2+ = -ve
Zn2+
Zn → Zn 2+ + 2e
(Oxidation)
Zn 2+ + 2e → Zn
(Reduction)
Zn 2+ + 2e ↔ Zn
(At equilibrium)
Zn2+
Zn2+
Zn
Zn2+
Zn
Zn2+
Zn2+ Zn2+
Zn 2+ + 2e ↔ Zn
Equi shift to ←
- -
-
Zn
- - -
- +
+ +
+
+ +
+ +
+
Can’t measure
Abs Potential
Cu
Cu2+
Cu2+
Cu2+
Cu2+
Cu → Cu2+ + 2e
(Oxidation)
Cu2+ + 2e → Cu
(Reduction)
Cu2+ + 2e ↔ Cu
(At equilibrium)
Cu
-e
-e -e
Cu2+
Cu2+
Cu2+
Cu2+ + 2e ↔ Cu
Equi shift to →
+ +
+
Cu
+ + +
-
External circuit – flow of electrons Complete circuit
- - -
- - -
- - - - - - - -
Connect 2 Half Cell with wire/ salt bridge
Zn half cell (-ve) Oxidation
Cu half cell (+ve) Reduction
Voltmeter – High resistance (No current flow) Salt Bridge – flow of ions
Complete the circuit
Cu2+ + 2e → Cu Zn → Zn 2+ + 2e
1.10Volt Potential diff can be measured.
Voltmeter across – EMF
1.10 Volt
Zn + Cu2+ → Zn2+ + Cu
Anode Cathode
Zn(s) | Zn2+(aq) || Cu2+
(aq)| Cu (s)
Cell diagram
Anode Cathode
Half Cell Half Cell (Oxidation) (Reduction)
Phase boundary Salt Bridge Flow
electrons
Maintain electrical neutrality
Salt bridge – saturated KNO3
Zn2+ increase ↑
NO3- flow in to balance excess Zn2+
Cu2+ decrease ↓
K+ flow in to balance loss of Cu2+
Zn/Cu Voltaic Cell 2 Half Cell to make a Voltaic Cell
Zn Half Cell Cu Half Cell
-e -e
-
-
-
-
+
+
+
+
Potential Diff Ag/Ag2+
Electrode potential Ag/Ag2+ = +ve
Potential Diff Zn/Zn2+
Electrode potential Zn/Zn2+ = -ve
Zn2+
Zn → Zn 2+ + 2e
(Oxidation)
Zn 2+ + 2e → Zn
(Reduction)
Zn 2+ + 2e ↔ Zn
(At equilibrium)
Zn2+
Zn2+
Zn
Zn2+
Zn
Zn2+
Zn2+ Zn2+
Zn 2+ + 2e ↔ Zn
Equi shift to ←
- -
-
Zn
- - -
- +
+ +
+
+ +
+ +
+
Can’t measure
Abs Potential
Ag
Ag+
Ag+
Ag+
Ag+
Ag → Ag+ + e
(Oxidation)
Ag+ + e → Ag
(Reduction)
Ag+ + e ↔ Ag
(At equilibrium)
Ag
-e
-e -e
Ag+
Ag+
Ag+
Ag+ + e ↔ Ag
Equi shift to →
+ +
+
Ag
+ + +
-
External circuit – flow of electrons Complete circuit
- - -
- - -
- - - - - - - -
Connect 2 Half Cell with wire/ salt bridge
Zn half cell (-ve) Oxidation
Ag half cell (+ve) Reduction
Voltmeter – High resistance (No current flow) Salt Bridge – flow of ions
Complete the circuit
Ag+ + e → Ag Zn → Zn 2+ + 2e
1.56Volt Potential diff can be measured.
Voltmeter across – EMF
1.56 Volt
Zn + 2Ag+ → Zn2+ + 2Ag
Anode Cathode
Zn(s) | Zn2+(aq) || Ag+
(aq)| Ag (s)
Cell diagram
Anode Cathode
Half Cell Half Cell (Oxidation) (Reduction)
Phase boundary Salt Bridge Flow
electrons
Maintain electrical neutrality
Salt bridge – saturated KNO3
Zn2+ increase ↑
NO3- flow in to balance excess Zn2+
Ag+ decrease ↓
K+ flow in to balance loss of Ag+
Zn/Ag Voltaic Cell 2 Half Cell to make a Voltaic Cell
Zn Half Cell Ag Half Cell
Ag
Ag+
-e -e
-
-
-
-
+
+
+
+
Potential Diff Ag/Ag2+
Electrode potential Ag/Ag2+ = +ve
Potential Diff Cu/Cu2+
Electrode potential Cu/Cu2+ = -ve
Cu2+
Cu → Cu 2+ + 2e
(Oxidation)
Cu 2+ + 2e → Cu
(Reduction)
Cu 2+ + 2e ↔ Cu
(At equilibrium)
Cu2+
Cu2+
Cu
Cu2+
Cu
Cu2+
Cu2+ Cu2+
Cu 2+ + 2e ↔ Cu
Equi shift to ←
- -
-
Cu
- - -
- +
+ +
+
+ +
+ +
+
Can’t measure
Abs Potential
Ag
Ag+
Ag+
Ag+
Ag+
Ag → Ag+ + e
(Oxidation)
Ag+ + e → Ag
(Reduction)
Ag+ + e ↔ Ag
(At equilibrium)
Ag
-e
-e -e
Ag+
Ag+
Ag+
Ag+ + e ↔ Ag
Equi shift to →
+ +
+
Ag
+ + +
-
External circuit – flow of electrons Complete circuit
- - -
- - -
- - - - - - - -
Connect 2 Half Cell with wire/ salt bridge
Cu half cell (-ve) Oxidation
Ag half cell (+ve) Reduction
Voltmeter – High resistance (No current flow) Salt Bridge – flow of ions
Complete the circuit
Ag+ + e → Ag Cu → Cu 2+ + 2e
0.46Volt Potential diff can be measured.
Voltmeter across – EMF
0.46 Volt
Cu + 2Ag+ → Cu2+ + 2Ag
Anode Cathode
Cu(s) | Cu2+(aq) || Ag+
(aq)| Ag (s)
Cell diagram
Anode Cathode
Half Cell Half Cell (Oxidation) (Reduction)
Phase boundary Salt Bridge Flow
electrons
Maintain electrical neutrality
Salt bridge – saturated KNO3
Cu2+ increase ↑
NO3- flow in to balance excess Cu2+
Ag+ decrease ↓
K+ flow in to balance loss of Ag+
Cu/Ag Voltaic Cell 2 Half Cell to make a Voltaic Cell
Cu Half Cell Ag Half Cell
Ag
Ag+
Cu
Cu2+
-e -e
-
-
-
-
+
+
+
+
Standard Electrode Potential
Standard Hydrogen Electrode (SHE)
Platinum coat with Platinum oxide/black – increase surface area for adsorption H2 - catalyze equilibrium bet H2 /H+
- H2 ↔ 2H+ + 2e-
Eθ
Standard Reference electrode All Cell Potential are measured against
• Conc ( 1M) • Pressure (1 atm) • Temp (298K) • Platinum- inert electrode (sys without metal)
Standard
condition
H2 at 1 atm
Platinum
H2 gas
Pt wire
Platinum
2H+ + 2e ↔ H2
Eθ = 0V
Types of Half Cells
Metal/ Ion (M/M+)
Gas/ Ion (M/M-)
Ion/ Ion (Fe3+/Fe2+)
• Pure Zn metal • Conc (1M Zn2+) • Pressure (1 atm) • Temp (298K)
Condition Std Zn/Zn2+
Condition Std CI2/CI-
• CI2 gas • Platinum electrode • Conc (1M CI-) • Pressure (1 atm) • Temp (298K)
• Platinum electrode • Conc (1M Fe3+/Fe2+) • Pressure (1 atm) • Temp (298K)
Condition Std Fe3+/ Fe2+
Zn2+
Zn
Fe3+/Fe2+
CI-
Condition for Standard C
A
N
T
M
E
A
S
U
R
E
A
B
S
P
O
T
E
N
T
I
A
L
1
2
3
How to measure
electrode
potential ?
Pt
1M H+
Measure
Difference?
Standard Electrode Potential
Std Hydrogen Electrode (SHE)
Eθ = 0V
Types of Half Cells
Metal/ Ion (M/M+)
Gas/ Ion (M/M+)
Ion/ Ion (Fe3+/Fe2+)
• Pure Zn metal • Conc (1M Zn2+) • Pressure (1 atm) • Temp (298K)
Condition Std Zn/Zn2+
Condition Std CI2/CI-
• CI2 gas • Platinum electrode • Conc (1M CI-) • Pressure (1 atm) • Temp (298K)
• Platinum electrode • Conc (1M Fe3+/Fe2+) • Pressure (1 atm) • Temp (298K)
Condition Std Fe3+/ Fe2+
Zn2+
Zn
Fe3+/Fe2+
1
2
3
Connect to SHE
Connect to SHE
Connect to SHE
Eθ = 0V
Eθ = 0V
Eθ = -0.76V
Standard electrode potential Zn/Zn2+ = -0.76V
Eθ cell = -0.76V
Eθ = +0.77V
Eθ = +1.35V
Standard electrode potential Fe3+/Fe2+ = +0.77V
Eθ cell = +0.77V
Standard electrode potential CI2 /CI- = +1.35V
Eθ cell = +1.35V
Eθ= -0.76V
Eθ= +0.77V
Eθ= +1.35V
2 Half Cell with SHE as reference electrode
CI-
Pt
+
+
+
Pt
Standard Electrode Potential
Std Electrode Potential diff systems
Eθ = 0V
Eθ = 0V
Eθ = 0V
Eθ = -0.76V
Standard electrode potential Zn/Zn2+ = -0.76V
Eθ cell = -0.76V
Eθ = +0.77V
Eθ = +1.35V
Standard electrode potential Fe3+/Fe2+ = +0.77V
Eθ cell = +0.77V
Standard electrode potential CI2 /CI- = +1.35V
Eθ cell = +1.35V
Eθ= -0.76V
Eθ= +0.77V
Eθ= +1.35V
STANDARD Reduction potential – Hydrogen as std
Oxidized sp ↔ Reduced sp Eθ/V
Li+ + e- ↔ Li -3.04 K+ + e- ↔ K -2.93 Ca2+ + 2e- ↔ Ca -2.87 Na+ + e- ↔ Na -2.71 Mg 2+ + 2e- ↔ Mg -2.37 Al3+ + 3e- ↔ AI -1.66 Mn2+ + 2e- ↔ Mn -1.19 H2O + e- ↔ 1/2H2 + OH- -0.83 Zn2+ + 2e- ↔ Zn -0.76 Fe2+ + 2e- ↔ Fe -0.45 Ni2+ + 2e- ↔ Ni -0.26 Sn2+ + 2e- ↔ Sn -0.14 Pb2+ + 2e- ↔ Pb -0.13 H+ + e- ↔ 1/2H2 0.00 Cu2+ + e- ↔ Cu+ +0.15 SO4
2- + 4H+ + 2e- ↔ H2SO3 + H2O +0.17 Cu2+ + 2e- ↔ Cu +0.34 1/2O2 + H2O +2e- ↔ 2OH- +0.40 Cu+ + e- ↔ Cu +0.52 1/2I2 + e- ↔ I- +0.54 Fe3+ + e- ↔ Fe2+ +0.77 Ag+ + e- ↔ Ag +0.80 1/2Br2 + e- ↔ Br- +1.07 1/2O2 + 2H+ +2e- ↔ H2O +1.23 Cr2O7
2-+14H+ +6e- ↔ 2Cr3+ + 7H2O +1.33 1/2CI2 + e- ↔ CI- +1.35 MnO4
- + 8H+ + 5e- ↔ Mn2+ + 4H2O +1.51 1/2F2 + e- ↔ F +2.87
-ve reduction
potential
+ve reduction
potential
Click here std analogy video
Click here std analogy
Click here chem database (std electrode potential)
Compared to
H2 as std
Eθ cell/Cell Potential = EMF in volt EMF prod when half cell connect to SHE at std condition Std electrode potential written as std reduction potential
Zn half cell (-ve) Oxidation
H2 half cell (+ve) Reduction
Anode Cathode
Zn(s) | Zn2+(aq) || H
+(aq) , H2(g) | Pt (s)
Cell diagram
Anode Cathode
Half Cell Half Cell
(Oxidation) (Reduction)
Salt Bridge Flow
electrons
Eθcell = Eθ
(cathode) – Eθ (anode)
Eθcell = 0.00 – ( Eθ Zn )
0.76 = 0.00 - Eθ Zn Eθ Zn = -0.76V
Zn2+ + 2e ↔ Zn Eθ = ? 2H+ + 2e ↔ H2 E
θ = 0.00V
Std electrode potential as std reduction potential
Find Eθcell (use formula)
Eθcell = Eθ
(cathode) – Eθ(anode)
Oxidized sp ↔ Reduced sp Eθ/V
Li+ + e- ↔ Li -3.04 K+ + e- ↔ K -2.93 Ca2+ + 2e- ↔ Ca -2.87 Na+ + e- ↔ Na -2.71 Mg 2+ + 2e- ↔ Mg -2.37 Al3+ + 3e- ↔ AI -1.66 Mn2+ + 2e- ↔ Mn -1.19 H2O + e- ↔ 1/2H2 + OH- -0.83
Zn2+ + 2e- ↔ Zn ????
Fe2+ + 2e- ↔ Fe -0.45 Ni2+ + 2e- ↔ Ni -0.26 Sn2+ + 2e- ↔ Sn -0.14 Pb2+ + 2e- ↔ Pb -0.13
H+ + e- ↔ 1/2H2 0.00 Cu2+ + e- ↔ Cu+ +0.15 SO4
2- + 4H+ + 2e- ↔ H2SO3 + H2O +0.17 Cu2+ + 2e- ↔ Cu +0.34 1/2O2 + H2O +2e- ↔ 2OH- +0.40 Cu+ + e- ↔ Cu +0.52 1/2I2 + e- ↔ I- +0.54 Fe3+ + e- ↔ Fe2+ + 0.77 Ag+ + e- ↔ Ag +0.80 1/2Br2 + e- ↔ Br- +1.07 1/2O2 + 2H+ +2e- ↔ H2O +1.23 Cr2O7
2-+14H+ +6e- ↔ 2Cr3+ + 7H2O +1.33 1/2CI2 + e- ↔ CI- +1.35 MnO4
- + 8H+ + 5e- ↔ Mn2+ + 4H2O +1.51 1/2F2 + e- ↔ F +2.87
-0.76V
+ve/high electrode potential is cathode (+) -ve/ low electrode potential is anode (-) Electrons flow from anode (- ) to cathode (+ )
Eθ Zn/H2 = 0.76V
Zn/H2
Eθ value DO NOT depend on stoichiometric coefficient (Independent of stoichiometric eqn)
Zn
Zn2+
H+
Pt
H2
-
-
- +
-e
Zn/H2 Cell Determine Eθ cell Zn/Zn2+
Zn2+ + 2e →Zn Eθ = -0.76V
H2 half cell (-ve) Oxidation
Fe3+/2+ half cell (+ve) Reduction
Anode Cathode
Pt(s) | H2, H+
(aq) || Fe3+ Fe2+
| Pt (s)
Cell diagram
Anode Cathode
Half Cell Half Cell
(Oxidation) (Reduction)
Salt Bridge Flow
electrons
Std electrode potential as std reduction potential
Find Eθcell (use formula)
Eθcell = Eθ
(cathode) – Eθ(anode)
Oxidized sp ↔ Reduced sp Eθ/V
Li+ + e- ↔ Li -3.04 K+ + e- ↔ K -2.93 Ca2+ + 2e- ↔ Ca -2.87 Na+ + e- ↔ Na -2.71 Mg 2+ + 2e- ↔ Mg -2.37 Al3+ + 3e- ↔ AI -1.66 Mn2+ + 2e- ↔ Mn -1.19 H2O + e- ↔ 1/2H2 + OH- -0.83 Zn2+ + 2e- ↔ Zn -0.76 Fe2+ + 2e- ↔ Fe -0.45 Ni2+ + 2e- ↔ Ni -0.26 Sn2+ + 2e- ↔ Sn -0.14 Pb2+ + 2e- ↔ Pb -0.13
H+ + e- ↔ 1/2H2 0.00 Cu2+ + e- ↔ Cu+ +0.15 SO4
2- + 4H+ + 2e- ↔ H2SO3 + H2O +0.17 Cu2+ + 2e- ↔ Cu +0.34 1/2O2 + H2O +2e- ↔ 2OH- +0.40 Cu+ + e- ↔ Cu +0.52 1/2I2 + e- ↔ I- +0.54 Fe3+ + e- ↔ Fe2+ ????? Ag+ + e- ↔ Ag +0.80 1/2Br2 + e- ↔ Br- +1.07 1/2O2 + 2H+ +2e- ↔ H2O +1.23 Cr2O7
2-+14H+ +6e- ↔ 2Cr3+ + 7H2O +1.33 1/2CI2 + e- ↔ CI- +1.35 MnO4
- + 8H+ + 5e- ↔ Mn2+ + 4H2O +1.51 1/2F2 + e- ↔ F +2.87
+0.77V
+ve/high electrode potential is cathode (+) -ve/ low electrode potential is anode (-) Electrons flow from anode (- ) to cathode (+ )
Pt
Fe3+
H+
Pt
H2
+
+
+ - -
-e
H2 /Fe3+,Fe2+ Cell
H2 /Fe3+,Fe2+
2H+ + 2e ↔ H2 Eθ = 0.00V
Fe3+ + e ↔ Fe2+ Eθ = ????
Eθcell = Eθ
(cathode) – Eθ (anode)
Eθcell = Eθ Fe3+ – (-0.00)
0.77 = Eθ Fe3+
Determine Eθ cell Fe 3+/Fe2+
Eθ H2 /Fe3+ = 0.77V
Fe3+ + e →Fe2+ Eθ = +0.77V
Eθ value DO NOT depend on stoichiometric coefficient (Independent of stoichiometric eqn)
H2 half cell (-ve) Oxidation
CI2 half cell (+ve) Reduction
Anode
Pt(s) | H2, H+
(aq) || CI2 ,CI- | Pt (s)
Cell diagram
Anode Cathode
Half Cell Half Cell
(Oxidation) (Reduction)
Salt Bridge Flow
electrons
Std electrode potential as std reduction potential
Find Eθcell (use formula)
Eθcell = Eθ
(cathode) – Eθ(anode)
Oxidized sp ↔ Reduced sp Eθ/V
Li+ + e- ↔ Li -3.04 K+ + e- ↔ K -2.93 Ca2+ + 2e- ↔ Ca -2.87 Na+ + e- ↔ Na -2.71 Mg 2+ + 2e- ↔ Mg -2.37 Al3+ + 3e- ↔ AI -1.66 Mn2+ + 2e- ↔ Mn -1.19 H2O + e- ↔ 1/2H2 + OH- -0.83 Zn2+ + 2e- ↔ Zn -0.76 Fe2+ + 2e- ↔ Fe -0.45 Ni2+ + 2e- ↔ Ni -0.26 Sn2+ + 2e- ↔ Sn -0.14 Pb2+ + 2e- ↔ Pb -0.13
H+ + e- ↔ 1/2H2 0.00 Cu2+ + e- ↔ Cu+ +0.15 SO4
2- + 4H+ + 2e- ↔ H2SO3 + H2O +0.17 Cu2+ + 2e- ↔ Cu +0.34 1/2O2 + H2O +2e- ↔ 2OH- +0.40 Cu+ + e- ↔ Cu +0.52 1/2I2 + e- ↔ I- +0.54 Fe3+ + e- ↔ Fe2+ + 0.77 Ag+ + e- ↔ Ag +0.80 1/2Br2 + e- ↔ Br- +1.07 1/2O2 + 2H+ +2e- ↔ H2O +1.23 Cr2O7
2-+14H+ +6e- ↔ 2Cr3+ + 7H2O +1.33 1/2CI2 + e- ↔ CI- ????? MnO4
- + 8H+ + 5e- ↔ Mn2+ + 4H2O +1.51 1/2F2 + e- ↔ F +2.87
+1.35V
+ve/high electrode potential is cathode (+) -ve/ low electrode potential is anode (-) Electrons flow from anode (- ) to cathode (+ )
H+
Pt
H2 - -
-e
H2 /CI2 Cell
2H+ + 2e ↔ H2 Eθ = 0.00V
CI + e ↔ CI- Eθ = ?????
Eθcell = Eθ
(cathode) – Eθ (anode)
Eθcell = Eθ CI2 – (-0.00)
1.35 = Eθ CI2
H2 /CI2 Cell
+ Pt
CI - CI2
Determine Eθ cell H2 /CI2
Eθ H2 /CI2
= 1.35V
1/2CI- + e →CI- Eθ = +1.35V
Eθ value DO NOT depend on stoichiometric coefficient (Independent of stoichiometric eqn)
Zn half cell (-ve) Oxidation
Cu half cell (+ve) Reduction
Anode Cathode
Zn(s) | Zn2+(aq) || Cu2+
(aq) | Cu (s)
Cell diagram
Anode Cathode
Half Cell Half Cell
(Oxidation) (Reduction)
Salt Bridge Flow
electrons
Zn/Cu Voltaic Cell
-e -e
Zn/Cu half cell
Eθcell = Eθ
(cathode) – Eθ (anode)
Eθcell = +0.34 – (-0.76) = +1.10V
Zn 2+ + 2e ↔ Zn (anode) Eθ = -0.76V Cu2+ + 2e ↔ Cu (cathode) Eθ = +0.34V
Std electrode potential as std reduction potential
Find Eθcell (use reduction potential) Find Eθ
cell (use formula)
Zn + Cu2+ → Zn2+ + Cu Eθ = ?????
Eθcell = Eθ
(cathode) – Eθ(anode)
Zn 2+ + 2e ↔ Zn Eθ = -0.76V Cu2+ + 2e ↔ Cu Eθ = +0.34V
Zn ↔ Zn2+ + 2e Eθ = +0.76V Cu2+ + 2e ↔ Cu Eθ = +0.34V Zn + Cu2+ → Zn 2+ + Cu Eθ = +1.10V
Oxidized sp ↔ Reduced sp Eθ/V
Li+ + e- ↔ Li -3.04 K+ + e- ↔ K -2.93 Ca2+ + 2e- ↔ Ca -2.87 Na+ + e- ↔ Na -2.71 Mg 2+ + 2e- ↔ Mg -2.37 Al3+ + 3e- ↔ AI -1.66 Mn2+ + 2e- ↔ Mn -1.19 H2O + e- ↔ 1/2H2 + OH- -0.83
Zn2+ + 2e- ↔ Zn - 0.76
Fe2+ + 2e- ↔ Fe -0.45 Ni2+ + 2e- ↔ Ni -0.26 Sn2+ + 2e- ↔ Sn -0.14 Pb2+ + 2e- ↔ Pb -0.13 H+ + e- ↔ 1/2H2 0.00 Cu2+ + e- ↔ Cu+ +0.15 SO4
2- + 4H+ + 2e- ↔ H2SO3 + H2O +0.17
Cu2+ + 2e- ↔ Cu + 0.34 1/2O2 + H2O +2e- ↔ 2OH- +0.40 Cu+ + e- ↔ Cu +0.52 1/2I2 + e- ↔ I- +0.54 Fe3+ + e- ↔ Fe2+ +0.77 Ag+ + e- ↔ Ag +0.80 1/2Br2 + e- ↔ Br- +1.07 1/2O2 + 2H+ +2e- ↔ H2O +1.23 Cr2O7
2-+14H+ +6e- ↔ 2Cr3+ + 7H2O +1.33 1/2CI2 + e- ↔ CI- +1.35 MnO4
- + 8H+ + 5e- ↔ Mn2+ + 4H2O +1.51 1/2F2 + e- ↔ F +2.87
+
+1.10 V
Eθ Zn/Cu = 1.10V
Cu2+
+ve/high electrode potential is cathode (+) -ve/ low electrode potential is anode (-) Electrons flow from anode (- ) to cathode (+ )
-
-
-
-
Zn Cu
+
+
+
+
Eθ value DO NOT depend on stoichiometric coefficient (Independent of stoichiometric eqn)
Zn half cell (-ve) Oxidation
Ag half cell (+ve) Reduction
Anode Cathode
Zn(s) | Zn2+(aq) || Ag+
(aq) | Ag (s)
Cell diagram
Anode Cathode
Half Cell Half Cell
(Oxidation) (Reduction)
Salt Bridge Flow
electrons
Zn/Ag Voltaic Cell
-e -e
Zn/Ag half cell
Eθcell = Eθ
(cathode) – Eθ (anode)
Eθcell = +0.80 – (-0.76) = +1.56V
Zn 2+ + 2e ↔ Zn (anode) Eθ = -0.76V Ag + + e ↔ Ag(cathode) Eθ = +0.80V
Std electrode potential as std reduction potential
Find Eθcell (use reduction potential) Find Eθ
cell (use formula)
Zn + Ag+ → Zn2+ + Ag Eθ = ?????
Eθcell = Eθ
(cathode) – Eθ(anode)
Zn 2+ + 2e ↔ Zn Eθ = -0.76V Ag+ + e ↔ Ag Eθ = +0.80V
Zn ↔ Zn2+ + 2e Eθ = +0.76V Ag+ + e ↔ Ag Eθ = +0.80V Zn + Ag+ → Zn 2+ + Ag Eθ = +1.56V
Oxidized sp ↔ Reduced sp Eθ/V
Li+ + e- ↔ Li -3.04 K+ + e- ↔ K -2.93 Ca2+ + 2e- ↔ Ca -2.87 Na+ + e- ↔ Na -2.71 Mg 2+ + 2e- ↔ Mg -2.37 Al3+ + 3e- ↔ AI -1.66 Mn2+ + 2e- ↔ Mn -1.19 H2O + e- ↔ 1/2H2 + OH- -0.83
Zn2+ + 2e- ↔ Zn - 0.76
Fe2+ + 2e- ↔ Fe -0.45 Ni2+ + 2e- ↔ Ni -0.26 Sn2+ + 2e- ↔ Sn -0.14 Pb2+ + 2e- ↔ Pb -0.13 H+ + e- ↔ 1/2H2 0.00 Cu2+ + e- ↔ Cu+ +0.15 SO4
2- + 4H+ + 2e- ↔ H2SO3 + H2O +0.17 Cu2+ + 2e- ↔ Cu +0.34 1/2O2 + H2O +2e- ↔ 2OH- +0.40 Cu+ + e- ↔ Cu +0.52 1/2I2 + e- ↔ I- +0.54 Fe3+ + e- ↔ Fe2+ +0.77
Ag+ + e- ↔ Ag + 0.80 1/2Br2 + e- ↔ Br- +1.07 1/2O2 + 2H+ +2e- ↔ H2O +1.23 Cr2O7
2-+14H+ +6e- ↔ 2Cr3+ + 7H2O +1.33 1/2CI2 + e- ↔ CI- +1.36 MnO4
- + 8H+ + 5e- ↔ Mn2+ + 4H2O +1.51 1/2F2 + e- ↔ F +2.87
+
+1.56 V
Ag
Eθ Zn/Ag = 1.56V
Ag+
+ve/high electrode potential is cathode (+) -ve/ low electrode potential is anode (-) Electrons flow from anode (- ) to cathode (+ )
-
-
-
-
+
+
+
+
Zn
Eθ value DO NOT depend on stoichiometric coefficient (Independent of stoichiometric eqn)
Cu half cell (-ve) Oxidation
Ag half cell (+ve) Reduction
Anode Cathode
Cu(s) | Cu2+(aq) || Ag+
(aq) | Ag (s)
Cell diagram
Anode Cathode
Half Cell Half Cell
(Oxidation) (Reduction)
Salt Bridge Flow
electrons
Cu/Ag Voltaic Cell
-e -e
Cu/Ag half cell
Eθcell = Eθ
(cathode) – Eθ (anode)
Eθcell = +0.80 – (+0.34) = +0.46V
Cu 2+ + 2e ↔ Cu (anode) Eθ = +0.34V Ag + + e ↔ Ag(cathode) Eθ = +0.80V
Std electrode potential as std reduction potential
Find Eθcell (use reduction potential) Find Eθ
cell (use formula)
Cu + 2Ag+ → Cu2+ + 2Ag Eθ = ?????
Eθcell = Eθ
(cathode) – Eθ(anode)
Cu 2+ + 2e ↔ Cu Eθ = +0.34V Ag+ + e ↔ Ag Eθ = +0.80V
Cu ↔ Cu2+ + 2e Eθ = -0.34V 2Ag+ + e ↔ 2Ag Eθ = +0.80V Cu + 2Ag+→ Cu 2+ + 2Ag Eθ = +0.46V
Oxidized sp ↔ Reduced sp Eθ/V
Li+ + e- ↔ Li -3.04 K+ + e- ↔ K -2.93 Ca2+ + 2e- ↔ Ca -2.87 Na+ + e- ↔ Na -2.71 Mg 2+ + 2e- ↔ Mg -2.37 Al3+ + 3e- ↔ AI -1.66 Mn2+ + 2e- ↔ Mn -1.19 H2O + e- ↔ 1/2H2 + OH- -0.83 Zn2+ + 2e- ↔ Zn -0.76 Fe2+ + 2e- ↔ Fe -0.45 Ni2+ + 2e- ↔ Ni -0.26 Sn2+ + 2e- ↔ Sn -0.14 Pb2+ + 2e- ↔ Pb -0.13 H+ + e- ↔ 1/2H2 0.00 Cu2+ + e- ↔ Cu+ +0.15 SO4
2- + 4H+ + 2e- ↔ H2SO3 + H2O +0.17
Cu2+ + 2e- ↔ Cu +0.34 1/2O2 + H2O +2e- ↔ 2OH- +0.40 Cu+ + e- ↔ Cu +0.52 1/2I2 + e- ↔ I- +0.54 Fe3+ + e- ↔ Fe2+ +0.77
Ag+ + e- ↔ Ag +0.80 1/2Br2 + e- ↔ Br- +1.07 1/2O2 + 2H+ +2e- ↔ H2O +1.23 Cr2O7
2-+14H+ +6e- ↔ 2Cr3+ + 7H2O +1.33 1/2CI2 + e- ↔ CI- +1.36 MnO4
- + 8H+ + 5e- ↔ Mn2+ + 4H2O +1.51 1/2F2 + e- ↔ F +2.87
+
+0.46V
Ag Cu
Cu2+
Half cell- high electrode potential is cathode (+) Half cell - low electrode potential is anode (-) Electrons flow from anode (- ) to cathode (+ )
Eθ Cu/Ag = 0.46V
Ag+
-
-
-
-
+
+
+
+
Eθ value DO NOT depend on stoichiometric coefficient (Independent of stoichiometric eqn)
Mn half cell (-ve) Oxidation
Ni half cell (+ve) Reduction
Anode Cathode
Mn(s) | Mn2+(aq) || Ni2+
(aq) | Ni (s)
Cell diagram
Anode Cathode
Half Cell Half Cell
(Oxidation) (Reduction)
Salt Bridge Flow
electrons
Mn/Ni Voltaic Cell
-e -e
Mn/Ni half cells
Eθcell = Eθ
(cathode) – Eθ (anode)
Eθcell = -0.26 – (-1.19) = +0.93V
Mn 2+ + 2e ↔ Mn (anode) Eθ = -1.19V Ni2+ + 2e ↔ Ni (cathode) Eθ = -0.26V
Std electrode potential as std reduction potential
Find Eθcell (use reduction potential) Find Eθ
cell (use formula)
Mn + Ni2+ → Mn2+ + Ni Eθ = ?????
Eθcell = Eθ
(cathode) – Eθ(anode)
Mn 2+ + 2e ↔ Mn Eθ = -1.19V Ni2+ + 2e ↔ Ni Eθ = -0.26V
Mn ↔ Mn2+ + 2e Eθ = +1.19V Ni2+ + 2e ↔ Ni Eθ = -0.26V Mn + Ni2+ → Mn2+ + Ni Eθ = +0.93V
Oxidized sp ↔ Reduced sp Eθ/V
Li+ + e- ↔ Li -3.04 K+ + e- ↔ K -2.93 Ca2+ + 2e- ↔ Ca -2.87 Na+ + e- ↔ Na -2.71 Mg 2+ + 2e- ↔ Mg -2.37 Al3+ + 3e- ↔ AI -1.66 Mn2+ + 2e- ↔ Mn -1.19
H2O + e- ↔ 1/2H2 + OH- -0.83 Zn2+ + 2e- ↔ Zn -0.76 Fe2+ + 2e- ↔ Fe -0.45
Ni2+ + 2e- ↔ Ni - 0.26
Sn2+ + 2e- ↔ Sn -0.14 Pb2+ + 2e- ↔ Pb -0.13 H+ + e- ↔ 1/2H2 0.00 Cu2+ + e- ↔ Cu+ +0.15 SO4
2- + 4H+ + 2e- ↔ H2SO3 + H2O +0.17 Cu2+ + 2e- ↔ Cu +0.34 1/2O2 + H2O +2e- ↔ 2OH- +0.40 Cu+ + e- ↔ Cu +0.52 1/2I2 + e- ↔ I- +0.54 Fe3+ + e- ↔ Fe2+ +0.77 Ag+ + e- ↔ Ag +0.80 1/2Br2 + e- ↔ Br- +1.07 1/2O2 + 2H+ +2e- ↔ H2O +1.23 Cr2O7
2-+14H+ +6e- ↔ 2Cr3+ + 7H2O +1.33 1/2CI2 + e- ↔ CI- +1.36 MnO4
- + 8H+ + 5e- ↔ Mn2+ + 4H2O +1.51 1/2F2 + e- ↔ F +2.87
+
+0.93 V
Eθ Mn/Ni = 0.93V
Ni2+
+ve/high electrode potential is cathode (+) -ve/ low electrode potential is anode (-) Electrons flow from anode (- ) to cathode (+ )
-
-
-
-
Ni Mn
+
+
+
+ Mn2+
Eθ value DO NOT depend on stoichiometric coefficient (Independent of stoichiometric eqn)
Fe half cell (-ve) Oxidation
MnO4- half cell (+ve) Reduction
Anode Cathode
Fe(s) | Fe2+(aq) || MnO4
- ,H+, Mn2+ | Pt (s)
Cell diagram
Anode Cathode
Half Cell Half Cell
(Oxidation) (Reduction)
Salt Bridge Flow
electrons
Fe/MnO4- Voltaic Cell
-e -e
Fe/MnO4- half cells
Eθcell = Eθ
(cathode) – Eθ (anode)
Eθcell = +1.51 – (-0.45) = +1.96V
Fe2+ + 2e ↔ Fe Eθ = -0.45V MnO4
- + 5e ↔ Mn2+ + 4H2O E θ = +1.51V
Std electrode potential as std reduction potential
Find Eθcell (use reduction potential) Find Eθ
cell (use formula)
5Fe + 2MnO4- + 16H+→5Fe2+ +2Mn2+ + 8H2O Eθ = ?
Eθcell = Eθ
(cathode) – Eθ(anode)
Fe 2+ + 2e ↔ Fe Eθ = -0.45V MnO4
- + 5e ↔ Mn2+ + 4H2O Eθ = +1.51V
Fe ↔ Fe2+ + 2e Eθ = +0.45V MnO4
- +5e ↔ Mn2+ + 4H2O Eθ = +1.51V Fe + MnO4
- → Mn2+ + Fe2+ Eθ = +1.96V
Oxidized sp ↔ Reduced sp Eθ/V
Li+ + e- ↔ Li -3.04 K+ + e- ↔ K -2.93 Ca2+ + 2e- ↔ Ca -2.87 Na+ + e- ↔ Na -2.71 Mg 2+ + 2e- ↔ Mg -2.37 Al3+ + 3e- ↔ AI -1.66 Mn2+ + 2e- ↔ Mn -1.19 H2O + e- ↔ 1/2H2 + OH- -0.83 Zn2+ + 2e- ↔ Zn -0.76
Fe2+ + 2e- ↔ Fe -0.45
Ni2+ + 2e- ↔ Ni -0.26 Sn2+ + 2e- ↔ Sn -0.14 Pb2+ + 2e- ↔ Pb -0.13 H+ + e- ↔ 1/2H2 0.00 Cu2+ + e- ↔ Cu+ +0.15 SO4
2- + 4H+ + 2e- ↔ H2SO3 + H2O +0.17 Cu2+ + 2e- ↔ Cu +0.34 1/2O2 + H2O +2e- ↔ 2OH- +0.40 Cu+ + e- ↔ Cu +0.52 1/2I2 + e- ↔ I- +0.54 Fe3+ + e- ↔ Fe2+ +0.77 Ag+ + e- ↔ Ag +0.80 1/2Br2 + e- ↔ Br- +1.07 1/2O2 + 2H+ +2e- ↔ H2O +1.23 Cr2O7
2-+14H+ +6e- ↔ 2Cr3+ + 7H2O +1.33 1/2CI2 + e- ↔ CI- +1.36
MnO4- + 8H+ + 5e- ↔ Mn2+ + 4H2O +1.51
1/2F2 + e- ↔ F +2.87
+
+1.96V
Pt Fe
Fe2+
Eθ Fe/MnO4- = 1.96V
MnO4-
Mn2+
Using platinum electrode
+ve/high electrode potential is cathode (+) -ve/ low electrode potential is anode (-) Electrons flow from anode (- ) to cathode (+ )
-
-
-
-
+
+
+
+
Eθ value DO NOT depend on stoichiometric coefficient (Independent of stoichiometric eqn)
Zn half cell (-ve) Oxidation
Fe3+/2+ half cell (+ve) Reduction
Anode Cathode
Zn(s) | Zn2+(aq) || Fe3+ , Fe2+
(aq) | Pt (s)
Cell diagram
Anode Cathode
Half Cell Half Cell
(Oxidation) (Reduction)
Salt Bridge Flow
electrons
Zn/Fe3+,Fe2+ Cell
-e -e
Eθcell = Eθ
(cathode) – Eθ (anode)
Eθcell = +0.77 – (-0.76) = +1.53V
Zn2+ + 2e ↔ Zn Eθ = -0.76V Fe3+ + e ↔ Fe2+ Eθ = +0.77V
Std electrode potential as std reduction potential
Find Eθcell (use reduction potential) Find Eθ
cell (use formula)
Zn + 2Fe3+→ Zn2+ +2Fe2+ Eθ = ?
Eθcell = Eθ
(cathode) – Eθ(anode)
Zn 2+ + 2e ↔ Zn Eθ = -0.76V Fe3+ + e ↔ Fe2+ Eθ = +0.77V
Zn ↔ Zn2+ + 2e Eθ = +0.76V Fe3+ +e ↔ Fe2+ Eθ = +0.77V Zn + 2Fe3+ → Zn2+ + 2Fe2+ Eθ = +1.53V
Oxidized sp ↔ Reduced sp Eθ/V
Li+ + e- ↔ Li -3.04 K+ + e- ↔ K -2.93 Ca2+ + 2e- ↔ Ca -2.87 Na+ + e- ↔ Na -2.71 Mg 2+ + 2e- ↔ Mg -2.37 Al3+ + 3e- ↔ AI -1.66 Mn2+ + 2e- ↔ Mn -1.19 H2O + e- ↔ 1/2H2 + OH- -0.83
Zn2+ + 2e- ↔ Zn -0.76
Fe2+ + 2e- ↔ Fe -0.45 Ni2+ + 2e- ↔ Ni -0.26 Sn2+ + 2e- ↔ Sn -0.14 Pb2+ + 2e- ↔ Pb -0.13 H+ + e- ↔ 1/2H2 0.00 Cu2+ + e- ↔ Cu+ +0.15 SO4
2- + 4H+ + 2e- ↔ H2SO3 + H2O +0.17 Cu2+ + 2e- ↔ Cu +0.34 1/2O2 + H2O +2e- ↔ 2OH- +0.40 Cu+ + e- ↔ Cu +0.52 1/2I2 + e- ↔ I- +0.54
Fe3+ + e- ↔ Fe2+ + 0.77 Ag+ + e- ↔ Ag +0.80 1/2Br2 + e- ↔ Br- +1.07 1/2O2 + 2H+ +2e- ↔ H2O +1.23 Cr2O7
2-+14H+ +6e- ↔ 2Cr3+ + 7H2O +1.33 1/2CI2 + e- ↔ CI- +1.36 MnO4
- + 8H+ + 5e- ↔ Mn2+ + 4H2O +1.51 1/2F2 + e- ↔ F +2.87
+
+1.53V
Pt Zn
Zn2+
+ve/high electrode potential is cathode (+) -ve/ low electrode potential is anode (-) Electrons flow from anode (- ) to cathode (+ )
Eθ Zn/Fe3+ = 1.53V
Fe3+-
Fe2+
Using platinum electrode
Zn/Fe3+,Fe2+
-
-
-
-
+
+
+
+
Eθ value DO NOT depend on stoichiometric coefficient (Independent of stoichiometric eqn)
Zn half cell (-ve) Oxidation
I2 half cell (+ve) Reduction
Anode Cathode
Zn(s) | Zn2+(aq) || I2 , I
-(aq) | Pt (s)
Cell diagram
Anode Cathode
Half Cell Half Cell
(Oxidation) (Reduction)
Salt Bridge Flow
electrons
Zn/I2 , I- Cell
-e -e
Eθcell = Eθ
(cathode) – Eθ (anode)
Eθcell = +0.54 – (-0.76) = +1.30V
Zn2+ + 2e ↔ Zn Eθ = -0.76V I2
+ 2e ↔ 2I- Eθ = +0.54V
Std electrode potential as std reduction potential
Find Eθcell (use reduction potential) Find Eθ
cell (use formula)
Zn + I2 → Zn2+ +2I- Eθ = ?
Eθcell = Eθ
(cathode) – Eθ(anode)
Zn ↔ Zn2+ + 2e Eθ = +0.76V I2
+ 2e ↔ 2I- Eθ = +0.54V Zn + I2
→ Zn2+ + 2I- Eθ = +1.30V
Oxidized sp ↔ Reduced sp Eθ/V
Li+ + e- ↔ Li -3.04 K+ + e- ↔ K -2.93 Ca2+ + 2e- ↔ Ca -2.87 Na+ + e- ↔ Na -2.71 Mg 2+ + 2e- ↔ Mg -2.37 Al3+ + 3e- ↔ AI -1.66 Mn2+ + 2e- ↔ Mn -1.19 H2O + e- ↔ 1/2H2 + OH- -0.83
Zn2+ + 2e- ↔ Zn -0.76
Fe2+ + 2e- ↔ Fe -0.45 Ni2+ + 2e- ↔ Ni -0.26 Sn2+ + 2e- ↔ Sn -0.14 Pb2+ + 2e- ↔ Pb -0.13 H+ + e- ↔ 1/2H2 0.00 Cu2+ + e- ↔ Cu+ +0.15 SO4
2- + 4H+ + 2e- ↔ H2SO3 + H2O +0.17 Cu2+ + 2e- ↔ Cu +0.34 1/2O2 + H2O +2e- ↔ 2OH- +0.40 Cu+ + e- ↔ Cu +0.52
1/2I2 + e- ↔ I- +0.54 Fe3+ + e- ↔ Fe2+ + 0.77
Ag+ + e- ↔ Ag +0.80 1/2Br2 + e- ↔ Br- +1.07 1/2O2 + 2H+ +2e- ↔ H2O +1.23 Cr2O7
2-+14H+ +6e- ↔ 2Cr3+ + 7H2O +1.33 1/2CI2 + e- ↔ CI- +1.36 MnO4
- + 8H+ + 5e- ↔ Mn2+ + 4H2O +1.51 1/2F2 + e- ↔ F +2.87
+
+1.30V
Pt Zn
Zn2+
+ve/high electrode potential is cathode (+) -ve/ low electrode potential is anode (-) Electrons flow from anode (- ) to cathode (+ )
Eθ Zn/I2 = 1.30V
I--
I2
Using platinum electrode
-
-
-
-
+
+
+
+
Zn/I2 , I-
Zn2+ + 2e ↔ Zn Eθ = -0.76V I2
+ 2e ↔ 2I- Eθ = +0.54V
Eθ value DO NOT depend on stoichiometric coefficient (Independent of stoichiometric eqn)
Zn half cell (-ve) Oxidation
H2 half cell (+ve) Reduction
Anode Cathode
Zn(s) | Zn2+(aq) || H
+(aq) , H2(g) | Pt (s)
Cell diagram
Anode Cathode
Half Cell Half Cell
(Oxidation) (Reduction)
Salt Bridge Flow
electrons
Eθcell = Eθ
(cathode) – Eθ (anode)
Eθcell = 0.00 – (-0.76) = +0.76V
Zn2+ + 2e ↔ Zn Eθ = -0.76V 2H+ + 2e ↔ H2 E
θ = 0.00V
Std electrode potential as std reduction potential
Find Eθcell (use reduction potential) Find Eθ
cell (use formula)
Zn + 2H+→ Zn2+ + H2 Eθ = ?
Eθcell = Eθ
(cathode) – Eθ(anode)
Zn 2+ + 2e ↔ Zn Eθ = -0.76V 2H+ + 2e ↔ H2 E
θ = 0.00V
Zn ↔ Zn2+ + 2e Eθ = +0.76V 2H+ +2e ↔ H2
Eθ = 0.00V Zn + 2H+ → Zn2+ + H2 Eθ = +0.76V
Oxidized sp ↔ Reduced sp Eθ/V
Li+ + e- ↔ Li -3.04 K+ + e- ↔ K -2.93 Ca2+ + 2e- ↔ Ca -2.87 Na+ + e- ↔ Na -2.71 Mg 2+ + 2e- ↔ Mg -2.37 Al3+ + 3e- ↔ AI -1.66 Mn2+ + 2e- ↔ Mn -1.19 H2O + e- ↔ 1/2H2 + OH- -0.83
Zn2+ + 2e- ↔ Zn -0.76
Fe2+ + 2e- ↔ Fe -0.45 Ni2+ + 2e- ↔ Ni -0.26 Sn2+ + 2e- ↔ Sn -0.14 Pb2+ + 2e- ↔ Pb -0.13
H+ + e- ↔ 1/2H2 0.00 Cu2+ + e- ↔ Cu+ +0.15 SO4
2- + 4H+ + 2e- ↔ H2SO3 + H2O +0.17 Cu2+ + 2e- ↔ Cu +0.34 1/2O2 + H2O +2e- ↔ 2OH- +0.40 Cu+ + e- ↔ Cu +0.52 1/2I2 + e- ↔ I- +0.54 Fe3+ + e- ↔ Fe2+ + 0.77 Ag+ + e- ↔ Ag +0.80 1/2Br2 + e- ↔ Br- +1.07 1/2O2 + 2H+ +2e- ↔ H2O +1.23 Cr2O7
2-+14H+ +6e- ↔ 2Cr3+ + 7H2O +1.33 1/2CI2 + e- ↔ CI- +1.36 MnO4
- + 8H+ + 5e- ↔ Mn2+ + 4H2O +1.51 1/2F2 + e- ↔ F +2.87
+
+0.76V
+ve/high electrode potential is cathode (+) -ve/ low electrode potential is anode (-) Electrons flow from anode (- ) to cathode (+ )
Eθ Zn/H2 = 0.76V
Using platinum electrode/H2
Zn/H2
Zn
Zn2+
H+
Pt
H2
-
-
- +
-e
Zn/H2 Cell
Eθ value DO NOT depend on stoichiometric coefficient (Independent of stoichiometric eqn)
H2 half cell (-ve) Oxidation
Ag half cell (+ve) Reduction
Anode Cathode
Pt(s) | H2, H+
(aq) || Ag+(aq) | Ag (s)
Cell diagram
Anode Cathode
Half Cell Half Cell
(Oxidation) (Reduction)
Salt Bridge Flow
electrons
H2/Ag Cell
Eθcell = Eθ
(cathode) – Eθ (anode)
Eθcell = +0.80 – (-0.00) = +0.80V
2H+ + 2e ↔ H2 Eθ = 0.00V
Ag+ + e ↔ Ag Eθ = +0.80V
Std electrode potential as std reduction potential
Find Eθcell (use reduction potential) Find Eθ
cell (use formula)
H2 + 2Ag+ → 2H+ + 2Ag Eθ = ?
Eθcell = Eθ
(cathode) – Eθ(anode)
H2 ↔ 2H+ + 2e Eθ = +0.00V 2Ag+ +2e ↔ 2Ag Eθ = +0.80V H2 + 2Ag+ → 2H+ + 2Ag Eθ = +0.80V
Oxidized sp ↔ Reduced sp Eθ/V
Li+ + e- ↔ Li -3.04 K+ + e- ↔ K -2.93 Ca2+ + 2e- ↔ Ca -2.87 Na+ + e- ↔ Na -2.71 Mg 2+ + 2e- ↔ Mg -2.37 Al3+ + 3e- ↔ AI -1.66 Mn2+ + 2e- ↔ Mn -1.19 H2O + e- ↔ 1/2H2 + OH- -0.83
Zn2+ + 2e- ↔ Zn -0.76
Fe2+ + 2e- ↔ Fe -0.45 Ni2+ + 2e- ↔ Ni -0.26 Sn2+ + 2e- ↔ Sn -0.14 Pb2+ + 2e- ↔ Pb -0.13
H+ + e- ↔ 1/2H2 0.00 Cu2+ + e- ↔ Cu+ +0.15 SO4
2- + 4H+ + 2e- ↔ H2SO3 + H2O +0.17 Cu2+ + 2e- ↔ Cu +0.34 1/2O2 + H2O +2e- ↔ 2OH- +0.40 Cu+ + e- ↔ Cu +0.52 1/2I2 + e- ↔ I- +0.54 Fe3+ + e- ↔ Fe2+ + 0.77
Ag+ + e- ↔ Ag +0.80 1/2Br2 + e- ↔ Br- +1.07 1/2O2 + 2H+ +2e- ↔ H2O +1.23 Cr2O7
2-+14H+ +6e- ↔ 2Cr3+ + 7H2O +1.33 1/2CI2 + e- ↔ CI- +1.36 MnO4
- + 8H+ + 5e- ↔ Mn2+ + 4H2O +1.51 1/2F2 + e- ↔ F +2.87
+
+0.80V
+ve/high electrode potential is cathode (+) -ve/ low electrode potential is anode (-) Electrons flow from anode (- ) to cathode (+ )
Eθ H2 /Ag = 0.80V
Using platinum electrode/H2
H2/Ag
Ag
Ag+
H+
Pt
H2
2H+ + 2e ↔ H2 Eθ = 0.00V
Ag+ + e ↔ Ag Eθ = +0.80V
+
+
+ - -
-e
Eθ value DO NOT depend on stoichiometric coefficient (Independent of stoichiometric eqn)
H2 half cell (-ve) Oxidation
Fe3+/2+ half cell (+ve) Reduction
Anode Cathode
Pt(s) | H2, H+
(aq) || Fe3+ Fe2+
| Pt (s)
Cell diagram
Anode Cathode
Half Cell Half Cell
(Oxidation) (Reduction)
Salt Bridge Flow
electrons
Std electrode potential as std reduction potential
Find Eθcell (use reduction potential) Find Eθ
cell (use formula)
H2 + 2Fe3+ → 2H+ + 2Fe Eθ = ?
Eθcell = Eθ
(cathode) – Eθ(anode)
H2 ↔ 2H+ + 2e Eθ = +0.00V 2Fe3+ +2e ↔ 2Fe2+ Eθ = +0.77V H2 + 2Ag+ → 2H+ + 2Ag Eθ = +0.77V
Oxidized sp ↔ Reduced sp Eθ/V
Li+ + e- ↔ Li -3.04 K+ + e- ↔ K -2.93 Ca2+ + 2e- ↔ Ca -2.87 Na+ + e- ↔ Na -2.71 Mg 2+ + 2e- ↔ Mg -2.37 Al3+ + 3e- ↔ AI -1.66 Mn2+ + 2e- ↔ Mn -1.19 H2O + e- ↔ 1/2H2 + OH- -0.83 Zn2+ + 2e- ↔ Zn -0.76 Fe2+ + 2e- ↔ Fe -0.45 Ni2+ + 2e- ↔ Ni -0.26 Sn2+ + 2e- ↔ Sn -0.14 Pb2+ + 2e- ↔ Pb -0.13
H+ + e- ↔ 1/2H2 0.00 Cu2+ + e- ↔ Cu+ +0.15 SO4
2- + 4H+ + 2e- ↔ H2SO3 + H2O +0.17 Cu2+ + 2e- ↔ Cu +0.34 1/2O2 + H2O +2e- ↔ 2OH- +0.40 Cu+ + e- ↔ Cu +0.52 1/2I2 + e- ↔ I- +0.54 Fe3+ + e- ↔ Fe2+ + 0.77 Ag+ + e- ↔ Ag +0.80 1/2Br2 + e- ↔ Br- +1.07 1/2O2 + 2H+ +2e- ↔ H2O +1.23 Cr2O7
2-+14H+ +6e- ↔ 2Cr3+ + 7H2O +1.33 1/2CI2 + e- ↔ CI- +1.36 MnO4
- + 8H+ + 5e- ↔ Mn2+ + 4H2O +1.51 1/2F2 + e- ↔ F +2.87
+
+0.77V
+ve/high electrode potential is cathode (+) -ve/ low electrode potential is anode (-) Electrons flow from anode (- ) to cathode (+ )
Eθ H2 /Fe3+ = 0.77V
Using platinum electrode/H2
Pt
Fe3+
H+
Pt
H2
+
+
+ - -
-e
H2 /Fe3+,Fe2+ Cell
H2 /Fe3+,Fe2+
2H+ + 2e ↔ H2 Eθ = 0.00V
Fe3+ + e ↔ Fe2+ Eθ = +0.77V 2H+ + 2e ↔ H2 E
θ = 0.00V Fe3+ + e ↔ Fe2+ Eθ = +0.77V
Eθcell = Eθ
(cathode) – Eθ (anode)
Eθcell = +0.77– (-0.00) = +0.77V
Eθ value DO NOT depend on stoichiometric coefficient (Independent of stoichiometric eqn)
H2 half cell (-ve) Oxidation
CI2 half cell (+ve) Reduction
Anode Cathode
Pt(s) | H2, H+
(aq) || CI2 ,CI- | Pt (s)
Cell diagram
Anode Cathode
Half Cell Half Cell
(Oxidation) (Reduction)
Salt Bridge Flow
electrons
Std electrode potential as std reduction potential
Find Eθcell (use reduction potential) Find Eθ
cell (use formula)
CI2 + H2 → 2CI- + 2H+ Eθ = ?
Eθcell = Eθ
(cathode) – Eθ(anode)
H2 ↔ 2H+ + 2e Eθ = +0.00V CI2
+2e ↔ 2CI- Eθ = +1.35V H2 + CI2
→ 2H+ + 2CI- Eθ = +1.35V
Oxidized sp ↔ Reduced sp Eθ/V
Li+ + e- ↔ Li -3.04 K+ + e- ↔ K -2.93 Ca2+ + 2e- ↔ Ca -2.87 Na+ + e- ↔ Na -2.71 Mg 2+ + 2e- ↔ Mg -2.37 Al3+ + 3e- ↔ AI -1.66 Mn2+ + 2e- ↔ Mn -1.19 H2O + e- ↔ 1/2H2 + OH- -0.83 Zn2+ + 2e- ↔ Zn -0.76 Fe2+ + 2e- ↔ Fe -0.45 Ni2+ + 2e- ↔ Ni -0.26 Sn2+ + 2e- ↔ Sn -0.14 Pb2+ + 2e- ↔ Pb -0.13
H+ + e- ↔ 1/2H2 0.00 Cu2+ + e- ↔ Cu+ +0.15 SO4
2- + 4H+ + 2e- ↔ H2SO3 + H2O +0.17 Cu2+ + 2e- ↔ Cu +0.34 1/2O2 + H2O +2e- ↔ 2OH- +0.40 Cu+ + e- ↔ Cu +0.52 1/2I2 + e- ↔ I- +0.54 Fe3+ + e- ↔ Fe2+ + 0.77 Ag+ + e- ↔ Ag +0.80 1/2Br2 + e- ↔ Br- +1.07 1/2O2 + 2H+ +2e- ↔ H2O +1.23 Cr2O7
2-+14H+ +6e- ↔ 2Cr3+ + 7H2O +1.33
1/2CI2 + e- ↔ CI- +1.35 MnO4
- + 8H+ + 5e- ↔ Mn2+ + 4H2O +1.51 1/2F2 + e- ↔ F +2.87
+
+1.35V
+ve/high electrode potential is cathode (+) -ve/ low electrode potential is anode (-) Electrons flow from anode (- ) to cathode (+ )
Eθ H2 /CI2
= 1.35V
Using platinum electrode/H2
H+
Pt
H2 - -
-e
H2 /CI2 Cell
2H+ + 2e ↔ H2 Eθ = 0.00V
CI + e ↔ CI- Eθ = +1.35V
Eθcell = Eθ
(cathode) – Eθ (anode)
Eθcell = +1.35 – (-0.00) = +1.35V
H2 /CI2 Cell
2H+ + 2e ↔ H2 Eθ = 0.00V
CI + e ↔ CI- Eθ = +1.35V
+ Pt
CI - CI2
Eθ value DO NOT depend on stoichiometric coefficient (Independent of stoichiometric eqn)
Standard Electrode Potential
STANDARD Reduction potential – H2 as std
Oxidized sp ↔ Reduced sp Eθ/V
Li+ + e- ↔ Li -3.04 K+ + e- ↔ K -2.93 Ca2+ + 2e- ↔ Ca -2.87 Na+ + e- ↔ Na -2.71 Mg 2+ + 2e- ↔ Mg -2.37 Al3+ + 3e- ↔ AI -1.66 Mn2+ + 2e- ↔ Mn -1.19 H2O + e- ↔ H2+OH- -0.83 Zn2+ + 2e- ↔ Zn -0.76 Fe2+ + 2e- ↔ Fe -0.45 Ni2+ + 2e- ↔ Ni -0.26 Sn2+ + 2e- ↔ Sn -0.14 Pb2+ + 2e- ↔ Pb -0.13 H+ + e- ↔ 1/2H2 0.00 Cu2+ + e- ↔ Cu+ +0.15 SO4
2- + 4H+ + 2e- ↔ H2SO3 + H2O +0.17 Cu2+ + 2e- ↔ Cu +0.34 1/2O2 + H2O +2e- ↔ 2OH- +0.40 Cu+ + e- ↔ Cu +0.52 1/2I2 + e- ↔ I- +0.54 Fe3+ + e- ↔ Fe2+ +0.77 Ag+ + e- ↔ Ag +0.80 1/2Br2 + e- ↔ Br- +1.07 1/2O2 + 2H+ +2e- ↔ H2O +1.23 Cr2O7
2-+14H+ +6e- ↔ 2Cr3+ +7H2O +1.33 1/2CI2 + e- ↔ CI- +1.36 MnO4
- + 8H+ + 5e- ↔ Mn2+ + 4H2O +1.51 1/2F2 + e- ↔ F +2.87
-ve reduction
potential
+ve reduction
potential
Compared to
H2 as std
Eθ cell/Cell Potential = EMF in volt EMF when half cell connect to SHE std condition Std potential written as std reduction potential
TOP right • High ↑ tendency lose e • Li → Li + + e
• Eθ Li = +3.04V • STRONG reducing Agent •Oxi favourable (Eθ =+ve)
STRONG
Reducing Agent
WEAK
Reducing Agent
BOTTOM right • Low ↓ tendency lose e • F - → 1/2F2 + e
• Eθ F2 = - 2.87V • WEAK reducing Agent •Oxi NOT favourable (Eθ =-ve)
WEAK
Oxidizing Agent
Strong
Oxidizing Agent
TOP left • Low ↓ tendency gain e • Li+ + e → Li
• Eθ Li= - 3.04V • WEAK oxidizing Agent • Red NOT favourable (Eθ =-ve)
BOTTOM left • High ↑ tendency gain e • F2 + 2e → 2F-
• Eθ F2= +2.87V • STRONG oxidizing Agent •Red favourable (Eθ =+ve)
Acknowledgements
Thanks to source of pictures and video used in this presentation
Thanks to Creative Commons for excellent contribution on licenses http://creativecommons.org/licenses/ http://spmchemistry.onlinetuition.com.my/2013/10/electrolytic-cell.html http://www.chemguide.co.uk/physical/redoxeqia/introduction.html http://educationia.tk/reduction-potential-table http://2012books.lardbucket.org/books/principles-of-general-chemistry-v1.0/s23-electrochemistry.html
Prepared by Lawrence Kok
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http://lawrencekok.blogspot.com