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Lawrence Kok
Tutorial on Secondary Cells, Hydrogen and Microbial
Fuel Cell, Thermodynamic Efficiency.
Lithium ion
Types voltaic cell
NH4CI and ZnCI2
Alkaline cellDry cell Nickel cadmium cell
Primary cell (Non rechargeable)
MnO2 and KOH
Secondary cell (Rechargeable)
Lead acid battery
Fuel cell
H2 fuel cell- alkaline electrolyte H2 fuel cell- acidic electrolyte Direct Methanol fuel cell Microbial fuel cell (MFC)
H2H2 O2
O2
H2O
CH3OH O2
CO2 H2O
C6H12O6
O2
- No pollution
- Fuel is constantly supply
- Convert fuel H2 /organic fuel to electricity
Longer life time
Rechargeable
Diff rechargeable vs fuel cell
Rechargeable battery are reversible
fuel cell irreversible – need supply fuel
Similarity rechargeable vs fuel cell
Both convert chemical
to electrical – redox rxn (spontaneous)
vs
Battery/Fuel cell Advantage Disadvantage
Lead acid High amt charge
High energy density
Cheap
Heavy
Lead/H2SO4 pollution
Nickel cadmium Longer lifetime
Quick recharge time
Low resistance
Cadmium toxic
Expensive
Memory effect
Lithium ion Low density
High voltage – 3.7V
Longer lifetime
High recharge cycle
Non toxic
Expensive
Explosive expose to heat
Fuel Cell More efficient
High energy density
No pollution
Low density
H2 explosive
Diff to store/transport gas
Expensive
Low storage density
Microbial Fuel Cell Safe and renewable
Treatment waste
Low energy
Battery/Fuel cell Energy
density
/MJdm-1
Specific
energy
/MJkg-1
H2 fuel cell 2 120
Methanol fuel cell 16 20
Liquid natural gas 21 50
Liquid propane 27 46
Gasoline 32 46
H2 highest specific energy
( ratio energy to mass)
1 mol H2 – 2g
1 mol methanol – 32g
1 mol propane - 44 g
1 mol octane/gasoline – 114g
Comparison in terms of energy density/specific energy Advantage/disadvantage of battery/fuel cell
H2 lowest energy density
(ratio energy to vol)
1 mol H2 – 24000 cm3
1 mol methanol – 40.4 cm3
1 mol propane - 76 cm3
1 mol octane/gasoline – 162 cm3
Comparison in terms of energy density/specific energy
Zinc carbon alkaline nickel/cad Li/Fe Li/Mn nickel/MH Li/ion Li/polymer fuel cell Zinc air
Types voltaic cell
Discharging
Pb + PbO2 + 2H2SO4 2PbSO→ 4 + 2H2O
Lead acid battery
(-ve) (Anode) - Oxidation
Pb + SO4
2-
PbSO→ 4 + 2e−
+ ve (Cathode)- Reduction
PbO2 + 4H+
+ SO4
2-
+ 2e−
PbSO→ 4 + 2H2O
(-ve) (Cathode)- Reduction
PbSO4 + 2e Pb + SO→ 4
2−
+ ve (Anode)- Oxidation
PbSO4 + 2H2O PbO→ 2 + 4H+
+ SO4
2-
2e−
Charging
Electrolyte
H2SO4
Nickel cadmium battery
Discharging
(-ve) (Anode) - Oxidation
Cd + 2OH-
Cd(OH)→ 2 + 2e−
+ ve (Cathode)- Reduction
2NiO(OH) + 2H2O+ 2e−
2Ni(OH)→ 2 + 2OH-
Charging
nickel (III)
oxide hydroxide
(-ve) (Cathode) - Reduction
Cd(OH)2 + 2e−
Cd + 2OH→ -
+ ve (Anode)- Oxidation
2Ni(OH)2 + 2OH-
2NiO(OH)+ 2H→ 2O+ 2e−
net eqn
2NiO(OH)+ Cd + 2H2O+ 2Ni(OH)→ 2 + Cd(OH)2
net eqn
NiO(OH) Cd
Electrolyte
KOH
Lithium ion battery
(-ve) (Anode) - Oxidation
Li Li→ +
+ e−
+ ve (Cathode)- Reduction
Li+
+ MnO2 + e−
LiMnO→ 2
Discharging
Lithium in Graphite layer – prevent lithium
for oxidizing to oxide (reactive)
LiMnO2 Li
-+
Charging
(-ve) (Cathode) - Reduction
Li+
+ e−
Li→
+ ve (Anode)- Oxidation
LiMnO2 Li→ +
+ MnO2 + e−
Li + MnO2 LiMnO→ 2
net eqn
Discharging/Charging possible
- insoluble PbSO4/PbO reversible
Discharging/Charging possible
- insoluble Cd(OH)2/Ni(OH)2 reversible
Lithium in MnO2 lattice – prevent lithium
for oxidizing to oxide (reactive)
2H2 + O2 2H→ 2O
H2 fuel cell- alkaline electrolyte
(-ve) (Anode) - Oxidation
2H2 + 4OH-
4H→ 2O + 4e−
+ ve (Cathode)- Reduction
2H2O + O2 + 4e−
4OH→ -
net eqn
net eqn
CH3OH + 1.5O2 CO→ 2 + 2H2O
net eqn
Fuel cell
Electrolyte
KOH
O2H2
H2 fuel cell- acidic electrolyte
(-ve) (Anode) - Oxidation
2H2 4H→ +
+ 4e−
+ ve (Cathode)- Reduction
4H+
+ O2 + 4e−
4H→ 2O
2H2 + O2 2H→ 2O O2H2
PEM – made of Teflon
allow H+
ion to flow
Proton Exchange Membrane
Electron flow in external circuit
Direct Methanol fuel cell
H2O
H2O
(-ve) (Anode) - Oxidation
CH3OH + H2O CO→ 2 + 6H+
+ 6e−
+ ve (Cathode)- Reduction
6H+
+ 1.5O2 + 6e−
3H→ 2O
O2
H2OCO2
CH3OH
Proton Exchange Membrane
PEM – made of Teflon
allow H+
ion to flow
Carbon oxidized to CO2 - C (-2) to C (+4)
Catalyst – platinum used anode/cathode
Catalyst – platinum used anode/cathode
Catalyst – platinum used anode/cathode
CH3COOH
Microbial fuel cell (MFC)
(-ve) (Anode) - Oxidation
C6H12O6 + 6H2O 6CO→ 2 + 24H+
+ 24e−
+ ve (Cathode)- Reduction
24H+
+ 6O2 + 24e−
12H→ 2O
net eqn
net eqn
net eqn
Fuel cell
O2CO2
CH3COOH + 2O2 2CO→ 2 + 2H2O
CH3COOH
Electron flow in external circuit
C6H12O6
O2CO2
Proton Exchange Membrane
PEM – made of Teflon
allow H+
ion to flow
C6H12O6 + 6O2 6CO→ 2 + 6H2O
Microbial/bacteria in anode, anaerobic
oxidized organic/fatty acid/ alcohol to CO2/H2O
Elec and H+
produced when oxidized
(-ve) (Anode) - Oxidation
CH3COOH + 2H2O 2CO→ 2 + 8H+
+ 8e−
+ ve (Cathode)- Reduction
8H+
+ 2O2 + 8e−
4H→ 2O
Microbial fuel cell (MFC) – Ethanoic acid
O2CO2
Electron flow in external circuit
Bacteria GEOBACTER in anode, anaerobic
oxidized ethanoic acid to CO2/H2O
Elec and H+
produced when oxidized
Microbial fuel cell (MFC) – Ethanoic acid
(-ve) (Anode) - Oxidation
CH3COOH + 2H2O 2CO→ 2 + 8H+
+ 8e−
+ ve (Cathode)- Reduction
8H+
+ 2O2 + 8e−
4H→ 2O
CH3COOH + 2O2 2CO→ 2 + 2H2O
Bioremediation to break down oil spill/organic waste
H2 fuel cell- acidic electrolyte
2H2 + O2 2H→ 2O
net eqn
Fuel cell
(-ve) (Anode) - Oxidation
2H2 4H→ +
+ 4e−
+ ve (Cathode)- Reduction
4H+
+ O2 + 4e−
4H→ 2O
O2
H2
PEM – made of Teflon
allow H+
ion to flow
Proton Exchange Membrane
H2O
Catalyst – platinum used anode/cathode
Thermodynamic Efficiency fuel cell
%100
..
..
. ×=
energyinputtotal
energyoutputuseful
efficiencyMax
%100. ×
∆−
∆−
=
sys
sys
H
G
efficiencyMax
Ratio of Gibbs Free energy to Enthalpy change of rxn 2H2 (g) + O2 (g) 2H→ 2O (l)
∆Hf = -285.8kJ mol-1
∆Gf = -237.1 kJ mol-1
%83%100
8.285
1.237
.
%100.
=×=
×
∆−
∆−
=
efficiencyMax
H
G
efficiencyMax
sys
sys
2H2 (g) + O2 (g) 2H→ 2O (g)
∆Hf = -241.8kJ mol-1
∆Gf = -228.6 kJ mol-1
%95%100
8.241
6.228
.
%100.
=×=
×
∆−
∆−
=
efficiencyMax
H
G
efficiencyMax
sys
sys
STHG ∆−∆=∆
Liquid water – Entropy lower (order)
∆S sys = ∆S(product – reactant) is higher
∆G = ∆H - T∆S
∆G = less negative
Efficiency = Less
Gas produced–Entropy gas high (disorder)
∆S sys = ∆S(product – reactant) is lower
∆G = ∆H - T∆S
∆G = more negative
Efficiency = More
STHG ∆−∆=∆
H2 fuel cell- acidic electrolyte
Click here making H2 fuel cell
H2 fuel cell- acidic electrolyte
2H2 + O2 2H→ 2O
net eqn
Fuel cell
(-ve) (Anode) - Oxidation
2H2 4H→ +
+ 4e−
+ ve (Cathode)- Reduction
4H+
+ O2 + 4e−
4H→ 2O
O2
H2
PEM – made of Teflon
allow H+
ion to flow
Proton Exchange Membrane
H2O
Catalyst – platinum used anode/cathode
Thermodynamic Efficiency
CH3OH+ 1.5O2 CO→ 2 + 2H2O
∆Hf = -726 kJ mol-1
∆Gf = - 685 kJ mol-1
%94%100
726
685
.
%100.
=×=
×
∆−
∆−
=
efficiencyMax
H
G
efficiencyMax
sys
sys
Sucrose, C12H22O11 used as substrate in MFC
i. Where do the bacteria live in fuel cell
ii. Oxi number carbon in –ve electrode
iii. Oxi number oxygen in + ve electrode
iv. Overall redox rxn
Direct Methanol fuel cell
CH3OH
CO2
O2
H2O
C12H22O11 + 12O2 12CO→ 2 + 11H2O
Oxi C = 0 Oxi C = +4Oxi O = 0
Oxi C = 0 to +4 (oxidized)
48 electron lost
(-ve) electrode
C12H22O11 + 13H2O 12CO→ 2 + 48H+
+ 48e–
Oxi O = -2
Oxi O = 0 to -2 (reduced)
48 electron gain
(+ve ) electrode
48H+
+ 12O2 + 48e– 24H→ 2O
Microbial fuel cell (MFC)
Bacteria in anode (-ve) –oxidation of substrate
- +
C12H22O11 + 12O2 12CO→ 2 + 11H2O
Eθ
value DO NOT depend surface area of metal electrode.
E cell = Energy per unit charge. (Joule)/C
E cell- 10v = 10J energy released by 1C of charge
= 100J energy released by 10C of charge
Eθ – intensive property– independent of amt – Ratio energy/charge
Increasing surface area metal will NOT increase E cell
Total Energy increase ↑
Total Charge increase ↑
Current increase ↑
BUT E cell remain SAME
E cell = (Energy/charge)
t
Q
I
tIQ
=
×=
Q up ↑ – I up ↑
i. Nature of material, further apart oxidising / reducing in std electrode potential, more
voltage produce
ii. Quantity material, surface area and total number of elec moving
iii. Large thick plates increase surface area- quantity of material (work/energy) increase,
current/charges increase BUT NO VOLTAGE CHANGE
Placing in series increase voltage
i. State factors that determine voltage of battery
ii. Outline what determine , total energy/work/current a battery can do
iii. Explain the effect of large surface area, battery have on voltage and work
Surface area increase ↑
E/Voltage remain SAME
Reactive lithium form oxide layer on metal
which decrease the contact with electrolyte
How lithium ion battery overcome this problem
Mixing lithium with graphite at anode.
and lithium with MnO2 lattice at cathode,
prevent oxidation of lithium metal
LiMnO2
Li - graphite
Oxi Li = +1, deduce oxi number of Mn in mixed
oxide LiMnO2, and show Mn has been reduced
Li +(polymer) + MnO2 + e- LiMnO→ 2
Oxi Mn = +4
Oxi Li = +1 Oxi O = -2
Oxi Mn in LiMnO2
+1 + Mn + 2(-2) = 0
Oxi Mn = +3
Oxi Mn = +4 to +3 ( reduced )
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
Check out more video tutorials from my site and hope you enjoy this tutorial
http://lawrencekok.blogspot.com

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Option C Secondary Cell, Hydrogen Microbial Fuel Cell and Thermodynamic Efficiency

  • 1. http://lawrencekok.blogspot.com Prepared by Lawrence Kok Tutorial on Secondary Cells, Hydrogen and Microbial Fuel Cell, Thermodynamic Efficiency.
  • 2. Lithium ion Types voltaic cell NH4CI and ZnCI2 Alkaline cellDry cell Nickel cadmium cell Primary cell (Non rechargeable) MnO2 and KOH Secondary cell (Rechargeable) Lead acid battery Fuel cell H2 fuel cell- alkaline electrolyte H2 fuel cell- acidic electrolyte Direct Methanol fuel cell Microbial fuel cell (MFC) H2H2 O2 O2 H2O CH3OH O2 CO2 H2O C6H12O6 O2 - No pollution - Fuel is constantly supply - Convert fuel H2 /organic fuel to electricity Longer life time Rechargeable Diff rechargeable vs fuel cell Rechargeable battery are reversible fuel cell irreversible – need supply fuel Similarity rechargeable vs fuel cell Both convert chemical to electrical – redox rxn (spontaneous) vs
  • 3. Battery/Fuel cell Advantage Disadvantage Lead acid High amt charge High energy density Cheap Heavy Lead/H2SO4 pollution Nickel cadmium Longer lifetime Quick recharge time Low resistance Cadmium toxic Expensive Memory effect Lithium ion Low density High voltage – 3.7V Longer lifetime High recharge cycle Non toxic Expensive Explosive expose to heat Fuel Cell More efficient High energy density No pollution Low density H2 explosive Diff to store/transport gas Expensive Low storage density Microbial Fuel Cell Safe and renewable Treatment waste Low energy Battery/Fuel cell Energy density /MJdm-1 Specific energy /MJkg-1 H2 fuel cell 2 120 Methanol fuel cell 16 20 Liquid natural gas 21 50 Liquid propane 27 46 Gasoline 32 46 H2 highest specific energy ( ratio energy to mass) 1 mol H2 – 2g 1 mol methanol – 32g 1 mol propane - 44 g 1 mol octane/gasoline – 114g Comparison in terms of energy density/specific energy Advantage/disadvantage of battery/fuel cell H2 lowest energy density (ratio energy to vol) 1 mol H2 – 24000 cm3 1 mol methanol – 40.4 cm3 1 mol propane - 76 cm3 1 mol octane/gasoline – 162 cm3 Comparison in terms of energy density/specific energy Zinc carbon alkaline nickel/cad Li/Fe Li/Mn nickel/MH Li/ion Li/polymer fuel cell Zinc air
  • 4. Types voltaic cell Discharging Pb + PbO2 + 2H2SO4 2PbSO→ 4 + 2H2O Lead acid battery (-ve) (Anode) - Oxidation Pb + SO4 2- PbSO→ 4 + 2e− + ve (Cathode)- Reduction PbO2 + 4H+ + SO4 2- + 2e− PbSO→ 4 + 2H2O (-ve) (Cathode)- Reduction PbSO4 + 2e Pb + SO→ 4 2− + ve (Anode)- Oxidation PbSO4 + 2H2O PbO→ 2 + 4H+ + SO4 2- 2e− Charging Electrolyte H2SO4 Nickel cadmium battery Discharging (-ve) (Anode) - Oxidation Cd + 2OH- Cd(OH)→ 2 + 2e− + ve (Cathode)- Reduction 2NiO(OH) + 2H2O+ 2e− 2Ni(OH)→ 2 + 2OH- Charging nickel (III) oxide hydroxide (-ve) (Cathode) - Reduction Cd(OH)2 + 2e− Cd + 2OH→ - + ve (Anode)- Oxidation 2Ni(OH)2 + 2OH- 2NiO(OH)+ 2H→ 2O+ 2e− net eqn 2NiO(OH)+ Cd + 2H2O+ 2Ni(OH)→ 2 + Cd(OH)2 net eqn NiO(OH) Cd Electrolyte KOH Lithium ion battery (-ve) (Anode) - Oxidation Li Li→ + + e− + ve (Cathode)- Reduction Li+ + MnO2 + e− LiMnO→ 2 Discharging Lithium in Graphite layer – prevent lithium for oxidizing to oxide (reactive) LiMnO2 Li -+ Charging (-ve) (Cathode) - Reduction Li+ + e− Li→ + ve (Anode)- Oxidation LiMnO2 Li→ + + MnO2 + e− Li + MnO2 LiMnO→ 2 net eqn Discharging/Charging possible - insoluble PbSO4/PbO reversible Discharging/Charging possible - insoluble Cd(OH)2/Ni(OH)2 reversible Lithium in MnO2 lattice – prevent lithium for oxidizing to oxide (reactive)
  • 5. 2H2 + O2 2H→ 2O H2 fuel cell- alkaline electrolyte (-ve) (Anode) - Oxidation 2H2 + 4OH- 4H→ 2O + 4e− + ve (Cathode)- Reduction 2H2O + O2 + 4e− 4OH→ - net eqn net eqn CH3OH + 1.5O2 CO→ 2 + 2H2O net eqn Fuel cell Electrolyte KOH O2H2 H2 fuel cell- acidic electrolyte (-ve) (Anode) - Oxidation 2H2 4H→ + + 4e− + ve (Cathode)- Reduction 4H+ + O2 + 4e− 4H→ 2O 2H2 + O2 2H→ 2O O2H2 PEM – made of Teflon allow H+ ion to flow Proton Exchange Membrane Electron flow in external circuit Direct Methanol fuel cell H2O H2O (-ve) (Anode) - Oxidation CH3OH + H2O CO→ 2 + 6H+ + 6e− + ve (Cathode)- Reduction 6H+ + 1.5O2 + 6e− 3H→ 2O O2 H2OCO2 CH3OH Proton Exchange Membrane PEM – made of Teflon allow H+ ion to flow Carbon oxidized to CO2 - C (-2) to C (+4) Catalyst – platinum used anode/cathode Catalyst – platinum used anode/cathode Catalyst – platinum used anode/cathode
  • 6. CH3COOH Microbial fuel cell (MFC) (-ve) (Anode) - Oxidation C6H12O6 + 6H2O 6CO→ 2 + 24H+ + 24e− + ve (Cathode)- Reduction 24H+ + 6O2 + 24e− 12H→ 2O net eqn net eqn net eqn Fuel cell O2CO2 CH3COOH + 2O2 2CO→ 2 + 2H2O CH3COOH Electron flow in external circuit C6H12O6 O2CO2 Proton Exchange Membrane PEM – made of Teflon allow H+ ion to flow C6H12O6 + 6O2 6CO→ 2 + 6H2O Microbial/bacteria in anode, anaerobic oxidized organic/fatty acid/ alcohol to CO2/H2O Elec and H+ produced when oxidized (-ve) (Anode) - Oxidation CH3COOH + 2H2O 2CO→ 2 + 8H+ + 8e− + ve (Cathode)- Reduction 8H+ + 2O2 + 8e− 4H→ 2O Microbial fuel cell (MFC) – Ethanoic acid O2CO2 Electron flow in external circuit Bacteria GEOBACTER in anode, anaerobic oxidized ethanoic acid to CO2/H2O Elec and H+ produced when oxidized Microbial fuel cell (MFC) – Ethanoic acid (-ve) (Anode) - Oxidation CH3COOH + 2H2O 2CO→ 2 + 8H+ + 8e− + ve (Cathode)- Reduction 8H+ + 2O2 + 8e− 4H→ 2O CH3COOH + 2O2 2CO→ 2 + 2H2O Bioremediation to break down oil spill/organic waste
  • 7. H2 fuel cell- acidic electrolyte 2H2 + O2 2H→ 2O net eqn Fuel cell (-ve) (Anode) - Oxidation 2H2 4H→ + + 4e− + ve (Cathode)- Reduction 4H+ + O2 + 4e− 4H→ 2O O2 H2 PEM – made of Teflon allow H+ ion to flow Proton Exchange Membrane H2O Catalyst – platinum used anode/cathode Thermodynamic Efficiency fuel cell %100 .. .. . ×= energyinputtotal energyoutputuseful efficiencyMax %100. × ∆− ∆− = sys sys H G efficiencyMax Ratio of Gibbs Free energy to Enthalpy change of rxn 2H2 (g) + O2 (g) 2H→ 2O (l) ∆Hf = -285.8kJ mol-1 ∆Gf = -237.1 kJ mol-1 %83%100 8.285 1.237 . %100. =×= × ∆− ∆− = efficiencyMax H G efficiencyMax sys sys 2H2 (g) + O2 (g) 2H→ 2O (g) ∆Hf = -241.8kJ mol-1 ∆Gf = -228.6 kJ mol-1 %95%100 8.241 6.228 . %100. =×= × ∆− ∆− = efficiencyMax H G efficiencyMax sys sys STHG ∆−∆=∆ Liquid water – Entropy lower (order) ∆S sys = ∆S(product – reactant) is higher ∆G = ∆H - T∆S ∆G = less negative Efficiency = Less Gas produced–Entropy gas high (disorder) ∆S sys = ∆S(product – reactant) is lower ∆G = ∆H - T∆S ∆G = more negative Efficiency = More STHG ∆−∆=∆ H2 fuel cell- acidic electrolyte Click here making H2 fuel cell
  • 8. H2 fuel cell- acidic electrolyte 2H2 + O2 2H→ 2O net eqn Fuel cell (-ve) (Anode) - Oxidation 2H2 4H→ + + 4e− + ve (Cathode)- Reduction 4H+ + O2 + 4e− 4H→ 2O O2 H2 PEM – made of Teflon allow H+ ion to flow Proton Exchange Membrane H2O Catalyst – platinum used anode/cathode Thermodynamic Efficiency CH3OH+ 1.5O2 CO→ 2 + 2H2O ∆Hf = -726 kJ mol-1 ∆Gf = - 685 kJ mol-1 %94%100 726 685 . %100. =×= × ∆− ∆− = efficiencyMax H G efficiencyMax sys sys Sucrose, C12H22O11 used as substrate in MFC i. Where do the bacteria live in fuel cell ii. Oxi number carbon in –ve electrode iii. Oxi number oxygen in + ve electrode iv. Overall redox rxn Direct Methanol fuel cell CH3OH CO2 O2 H2O C12H22O11 + 12O2 12CO→ 2 + 11H2O Oxi C = 0 Oxi C = +4Oxi O = 0 Oxi C = 0 to +4 (oxidized) 48 electron lost (-ve) electrode C12H22O11 + 13H2O 12CO→ 2 + 48H+ + 48e– Oxi O = -2 Oxi O = 0 to -2 (reduced) 48 electron gain (+ve ) electrode 48H+ + 12O2 + 48e– 24H→ 2O Microbial fuel cell (MFC) Bacteria in anode (-ve) –oxidation of substrate - + C12H22O11 + 12O2 12CO→ 2 + 11H2O
  • 9. Eθ value DO NOT depend surface area of metal electrode. E cell = Energy per unit charge. (Joule)/C E cell- 10v = 10J energy released by 1C of charge = 100J energy released by 10C of charge Eθ – intensive property– independent of amt – Ratio energy/charge Increasing surface area metal will NOT increase E cell Total Energy increase ↑ Total Charge increase ↑ Current increase ↑ BUT E cell remain SAME E cell = (Energy/charge) t Q I tIQ = ×= Q up ↑ – I up ↑ i. Nature of material, further apart oxidising / reducing in std electrode potential, more voltage produce ii. Quantity material, surface area and total number of elec moving iii. Large thick plates increase surface area- quantity of material (work/energy) increase, current/charges increase BUT NO VOLTAGE CHANGE Placing in series increase voltage i. State factors that determine voltage of battery ii. Outline what determine , total energy/work/current a battery can do iii. Explain the effect of large surface area, battery have on voltage and work Surface area increase ↑ E/Voltage remain SAME Reactive lithium form oxide layer on metal which decrease the contact with electrolyte How lithium ion battery overcome this problem Mixing lithium with graphite at anode. and lithium with MnO2 lattice at cathode, prevent oxidation of lithium metal LiMnO2 Li - graphite Oxi Li = +1, deduce oxi number of Mn in mixed oxide LiMnO2, and show Mn has been reduced Li +(polymer) + MnO2 + e- LiMnO→ 2 Oxi Mn = +4 Oxi Li = +1 Oxi O = -2 Oxi Mn in LiMnO2 +1 + Mn + 2(-2) = 0 Oxi Mn = +3 Oxi Mn = +4 to +3 ( reduced )
  • 10. 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 Check out more video tutorials from my site and hope you enjoy this tutorial http://lawrencekok.blogspot.com