Viktória B. Kovács| Fuel cells| © 2015 BMEGEENAG51 | D218 | 2015-16-1 | 1 FUEL CELLS Viktória Barbara KOVÁCS
Jan 20, 2016
Viktória B. Kovács| Fuel cells| © 2015 BMEGEENAG51 | D218 | 2015-16-1 | 1
FUEL CELLS
Viktória Barbara KOVÁCS
Viktória B. Kovács| Fuel cells| © 2015 BMEGEENAG51 | D218 | 2015-16-1 | 2
INTRODUCTION
Fuel cell is a device which use hydrogen or hydrogen rich fuel and oxygen to produce electricity through electrochemical process.
Byproducts: water and heat Present use: vehicles, energy supply of
buildings, PC.
Viktória B. Kovács| Fuel cells| © 2015 BMEGEENAG51 | D218 | 2015-16-1 | 3
WHY FUEL CELLS?
Decrease pollution Decrease fossil energy source dependence Slowing down global warming Prevent energy crisis
Viktória B. Kovács| Fuel cells| © 2015 BMEGEENAG51 | D218 | 2015-16-1 | 4
FUEL CELLSAdvantages
High and size independent efficiency (40..70%).
The heat (byproduct) can be used in cogeneration.
Low specific mass: 1 kg/kW. No moving parts → long
lifetime, silent, reliable. Very low GHG emission. No toxic /harmful pollutants for
health or for the environment In case of pure hydrogen
operation only water and heat emission.
Disadvantages
New technology → averseness in the beginning.
High costs in the beginning of market introduction → high risk
Missing or undeveloped hydrogen infrastructure.
Viktória B. Kovács| Fuel cells| © 2015 BMEGEENAG51 | D218 | 2015-16-1 | 5
PRINCIPLE OF OPERATION The fuel cell produces electric power from hydrogen and
oxygen through electrochemical process. An ordinary fuel cell consists of two fine and porous
electrode (anode and cathode) and the electrolyte between the electrodes. The hydrogen or hydrogen rich
fuel dissociates to e- and p+ on the anode by the help of the catalyst.
The oxygen with the electrons and protons (or other ions) form water (or something else) on the cathode.
The electrons are not allowed to penetrate through the membrane, they are forced to the cathode through the current circuit.
The drift of the electrons produces electrical direct current.
an
od
e cath
od
e
Viktória B. Kovács| Fuel cells| © 2015 BMEGEENAG51 | D218 | 2015-16-1 | 6
PRINCIPLE OF OPERATION
oxygen
protons
electrons
membrane
DC
ee
water
heat
H2 2H+ + 2e- 1/2O2 + 2e- 1/2O2 2 -
~1,23 Volt
ee e
e
an
od
e
cath
od
e
Viktória B. Kovács| Fuel cells| © 2015 BMEGEENAG51 | D218 | 2015-16-1 | 7
FUEL CELL SYSTEM
1. Fuel reforming unit (cleaner) 2. Energy conversation unit (fuel cell) 3. Transformer (DC/AC converter) 4. Heat recovery (mainly in case of high temperature)
3. INVERTER
H2-rich gasfuel
4. Heat recoveryfuel reforming
2.Fuel CELL
1. thermal reformer
oxygen (air)
ACDC
water
cogeneration
heat
Viktória B. Kovács| Fuel cells| © 2015 BMEGEENAG51 | D218 | 2015-16-1 | 8
1. FUEL REFORMING UNIT
Fuel reforming and cleaning. If the fuel is hydrogen only cleaning is
needed. Liquid fuel (methanol, ethanol, gasoline...)
are changed by thermal reforming to gaseous hydrocarbons.
Viktória B. Kovács| Fuel cells| © 2015 BMEGEENAG51 | D218 | 2015-16-1 | 9
2. ENERGY CONVERSATION UNIT (FUEL CELL)
Chemical energy → electrical power. DC is produced through chemical reaction.
Viktória B. Kovács| Fuel cells| © 2015 BMEGEENAG51 | D218 | 2015-16-1 | 10
3. TRANSFORMER AND REGULATOR
Keep regulated and constant electrical connection between the fuel cell and network (consumer).
Transform DC to AC. Regulates the current intensity, potential,
frequency, and other parameters according to the demands.
Viktória B. Kovács| Fuel cells| © 2015 BMEGEENAG51 | D218 | 2015-16-1 | 11
4. HEAT RECOVERY UNIT
Not always added, because heat is not the main product.
In case of high temperature:– steam production for combined power
generation – direct use in steam turbine.
The overall efficiency is higher with heat recovery.
Viktória B. Kovács| Fuel cells| © 2015 BMEGEENAG51 | D218 | 2015-16-1 | 12
CLASSIFICATION OF FUEL CELLS
By Fuel
Direct: hydrogen to anode Indirect: Hydrogen rich fuel
reformatted to anode Regenerative: products are
decomposed and reused
By Electrolyte
polymer electrolyte membrane (PEMFC) ~80 °C
phosphoric acid (PAFC) ~200 °C alkaline (AFC) 80..100 °C molten carbonate (MCFC) ~650
°C solid oxide (SOFC)
– tubular (TSOFC) 800 °C– intermediate temperature (ITSOFC)
1000 °C
Viktória B. Kovács| Fuel cells| © 2015 BMEGEENAG51 | D218 | 2015-16-1 | 13
POLYMER ELECTROLYTE MEMBRANE- PEMFC
Other name: SPEFC (Solid Polymer Electrolyte Fuel Cells)
Electrolyte: proton exchange membrane
Low temperature (85..105 °C) Nafion® membrane (DuPont
development) which is bed in poli-tetra-fluorethilen (PTFE, Teflon) based composition
Anode: H2 → 2H+ + 2e-
Cathode: 1/2O2+ 2H+ + 2e- → H2O High power density (Power/mass) Fast stand-up Mainly in vehicles disadvantage: low CO tolerance (Pt
poison)
Viktória B. Kovács| Fuel cells| © 2015 BMEGEENAG51 | D218 | 2015-16-1 | 14
POLYMER ELECTROLYTE MEMBRANE - PEMFC
Fuel cell stack explained.mp4:https://www.youtube.com/watch?v=w5E_MAZdO-k
anode cathode
Viktória B. Kovács| Fuel cells| © 2015 BMEGEENAG51 | D218 | 2015-16-1 | 15
PHOSPHORIC ACID ELECTROLYTE - PAFC
100% concentration of H3PO4 in SiC matrix with Pt catalyst
Anode: H2 → 2H+ + 2e-
Cathode: 1/2O2+ 2H+ + 2e- → H2O High temperature is needed,
because H3PO4 is bad conductor CO<3..5 vol% or Pt is poisoned
Viktória B. Kovács| Fuel cells| © 2015 BMEGEENAG51 | D218 | 2015-16-1 | 16
ALKALINE ELECTROLYTE - AFC
high concentration KOH (35..85 m%) in asbestos matrix Anode: H2 + 2OH- → 2H2O + e- Cathode: 1/2O2 + H2O + 2e- →
2OH- CO2 is poison: CO2 + KOH →
K2CO3
because the electrolyte changes High efficiency (~60%) Disadvantage: expensive
Viktória B. Kovács| Fuel cells| © 2015 BMEGEENAG51 | D218 | 2015-16-1 | 17
MOLTEN CARBONATE ELECTROLYTE - MCFC
Mixture of alkali carbonates LiAlO2 in ceramic matrix,
High temperature (600..800 °C) Anode: H2 + CO3
2- → H2O + CO2 + 2e-
CO + CO32- → 2CO2 +
2e-
Cathode: 1/2O2+ CO2 + 2e- → CO3
2-
Ni (anode) and NiO (cathode) High efficiency (70..80% !!!!!) fuel: H2, CO, NG, propane and
even diesel oil
Viktória B. Kovács| Fuel cells| © 2015 BMEGEENAG51 | D218 | 2015-16-1 | 18
SOLID OXIDE ELECTROLYTE - SOFC
solid ceramic: ZrO2 stabilized by Y2O3
Anode: H2 + O2- → H2O + 2e-
CO + O2- → CO2 + 2e-
CH4 + 4O2- → 2H2O + CO2 + 8e-
Cathode: 1/2O2 + 2e- → O2-
Co-ZrO2 or Ni-ZrO2 (anode) and LaMnO3 mixed with Strontium (cathode)
two types:– tubular (1 m tube bundles)– laminated plates
high power: (electricity supply)SOFC Brennstoffzelle.mp4:https://www.youtube.com/watch?v=Itz2hJPP9l4
Viktória B. Kovács| Fuel cells| © 2015 BMEGEENAG51 | D218 | 2015-16-1 | 19
COMPARISON - REACTION I.
Type of fuel cell
Name Electrolytetoperation
(°C)Fuel
OxidizerAnode and cathode
reaction
alkaline AFC30% KOH,
Liquid or gel60-90
- pure H2
- O2
A: H2+2OH- 2H2O +2e-
C: 1/2O2+H2O+2e-2OH-
solid polymer
SPFC, PEMFC
Proton exchange membrane
70-90- pure H2- O2, air
A: H2 2H+ +2e-
C: 1/2O2+2H++2e-2H2O
direct methanol
DMFCProton
exchange membrane
60-120- methanol- O2, air
A: CH3OH + H2OCO2++6H+ +6e-
C: 3/2O2+6H++6e-3H2O
phosphoric acid
PAFCundiluted
phosphoric acid
~220- pure H2- O2, air
A: H2 2H+ +2e-
C: 1/2O2+2H++2e-2H2O
molten carbonate
MCFC
lithium-carbonate,potassium- carbonate
~650- H2, NG, biogas, coal-gas- air, O2
A: H2+CO32- H2O +CO2+2e-
C: 1/2O2+CO2+2e-CO32-
Solid oxide
SOFCyttrium-Zircon cheramic oxid
~1000- H2, NG, biogas, coal-gas- air, O2
A: H2+O2- H2O +2e-
C: 1/2O2+2e-O2-
Viktória B. Kovács| Fuel cells| © 2015 BMEGEENAG51 | D218 | 2015-16-1 | 20
COMPARISON - REACTION II.
Not used fuel
fuel O2 / air
not used O2 / air
SOFC
MCFC
PAFC
DMFC
PEMFC
AFC
H2/CO
H2/CO
H2
CH3OH
H2
H2
O2
O2
O2
O2
O2
O2
H+
H+
H+
OH-
CO32-
O2-solid oxide
molten carbonatephosphoric acid
direct methanol
polymer electrolyte
alkaline
hig
h
tem
pera
ture
low
tem
pera
tire
>800°C
650°C
200°C
60 – 120°C
< 90°C
< 80°C
Viktória B. Kovács| Fuel cells| © 2015 BMEGEENAG51 | D218 | 2015-16-1 | 21
COMPARISON - ENERGY
Type of fuel cellOperation
temp., °C
Pressure,kPa
Current density, A/cm2
Potential, V
alkaline 70 1 (101) 0,2 0,8
Phosphoric acid 190 1 (101) 0,324 0,62
Phosphoric acid 205 8 (808) 0,216 0,73
molten carbonate 650 1 (101) 0,16 0,78
solid oxide 1000 1 (101) 0,2 0,66
Viktória B. Kovács| Fuel cells| © 2015 BMEGEENAG51 | D218 | 2015-16-1 | 22
USE, POWER, EFFICIENCY
Type of fuel cell Use PowerEfficiency
actual (theoretical)
AFC (alkaline)
vehiclesSpace program
Military purposesEnergy storage
low power 5..150 kW
62% (70%)
PEMFC (polymer electrolyte)
low power 5..250 kW
50% (68%)
DMFC (direct methanol)
low power 5 kW
26% (30%)
PAFC (phosphoric acid)
Combined cycle power plant
Low - medium power
50 kW..11 MW60% (65%)
MCFC (molten carbonate)
Combined cycle power plantAnd traffic
(railway, ship, …)
low power 100 kW..2 MW
62% (65%)
SOFC (solid oxide)
low power 100..250 kW
62% (65%)
Viktória B. Kovács| Fuel cells| © 2015 BMEGEENAG51 | D218 | 2015-16-1 | 23
EFFICIENCY OF A FUEL CELL
H2 52,5 kW (100%) Net Power
25,1 kW (47,8%)
System loss 4,5 kW (8,6%)
H2 loss 0,5 kW
(1%)
Gross power
29,6 kW (56,4%)
Heat loss
22,4 kW (42,6%)
25 kW PEMFC efficiencies in case of DC production
Viktória B. Kovács| Fuel cells| © 2015 BMEGEENAG51 | D218 | 2015-16-1 | 24
USE AND POWER RANGES
Methanol Alkaline Molten carbonate
Phosphoric acid
Solid oxide
Polymer electrolyte / Proton exchange
Portable devices,
high energy density
Mobile, home use
zero emission
Industrial use,
higher efficiency
silent, environmental
friendly operation
Viktória B. Kovács| Fuel cells| © 2015 BMEGEENAG51 | D218 | 2015-16-1 | 25
USE
Energy storage
Road transport
Small scale power plants
Analytics
Viktória B. Kovács| Fuel cells| © 2015 BMEGEENAG51 | D218 | 2015-16-1 | 26
PEMFC IN VEHICLES
Viktória B. Kovács| Fuel cells| © 2015 BMEGEENAG51 | D218 | 2015-16-1 | 27
QUESTIONS
What is the working principle of fuel cells (PEMFC)?
What are the advantages and disadvantages of fuel cells?
Describe fuel cell system for power generation!
What type of fuel cells do you know? Describe one of them in detail: type of electrolyte, fuel, operating temperature, efficiency!
Viktória B. Kovács| Fuel cells| © 2015 BMEGEENAG51 | D218 | 2015-16-1 | 28
THANK YOU FOR YOUR ATTENTION!
Viktória Barbara KOVÁCS
Build. D room 207B06 1 463 2592