Examples of oil spills
Combustion engine by-products:
1 Gallon of gas is equivalent to…
20 lbs CO2
‘Hydrogen Economy’
Potentially the future of energy in a system where hydrogen is used as the primary energy carrier and used for a wide range of applications.
It has the potential to significantly reduce greenhouse gas emissions.
There are many technical, infrastructural, and economic challenges to overcome.
Advantages of the ‘Hydrogen Economy’
Where does the hydrogen come from?
Hydrogen must be derived from renewable sources
Current uses of Hydrogen
Ways to create electricity
Safety aspect of hydrogen as a fuel
However, hydrogen is less flammable than gasoline and other fossil fuels
Liquid hydrogen: spilling –> Burns, explosions
Safety factors to be considered for hydrogen as a fuel
How to prevent accidents involving hydrogen:
Methods for producing hydrogen:
Steam Reforming (most common)
(1) CH4 + H2O ==> CO + 3H2 (+ 206.4 kJ/mol)
Catalyst : Ni , highly endothermic, T = 700 - 1100
(2) CO + H2O ==> CO2 + H2 (-41, kJ/mol)
Catalyst: Fe, Cr Oxides, mildly exothermic, water gas-shift reaction
Heat needed in (1) is provided by
(3) CH4 + 2O2 ==> CO2 + 2H2O (-880 Kj/mol)
Combining (1) and (2)
(4) CH4 + 2H2O (+165 kJ/mol) ==> CO2 + H2
Efficiency: 65% - 75%
CO (traces) and CO2 are removed using adsorption processes “pressure swing adsorption”
Disadvantage of steam reforming to produce hydrogen
Costs: still 2-3 times higher than producing gasoline from
crude oil Improving
Steam (methane) reforming not to be confused with catalytic reforming of naphta (octane gasoline and H2 as a by product)
Methane Cracking
CH4 + 74.9 KJ/mol ==> C + 2H
(Excess of steam is effective in preventing coke formation)
2CO ==> C + CO2 + 172.4 KJ/mol
Carbon Contamination
Current natural gas steam reforming is not aimed at fuel cell use of
H2 produced, so CO is not eliminated
Commonly in SMR: CO: 0.3-3%
CO: in the range of 10-50 ppm
Partial Oxidation Reforming
(6) reactions
CH4 + 2O2 ==> CO2 + 2H2O (liq) (-880 KJ/mol)
Exothermic, Methane Combustion
CO + 1/2 O2 ==> CO2 (-283.4 KJ/mol)
Exothermic, CO combustion
H2 + 1/2 O2 ==> H2O (liq) (-286 KJ/mol)
Exothermic, H2 combustion
Complete combustion: CO2 , H2O; no H2 , CO, O2 or fuel
Incomplete combustion: H2 , CO (in the presence of a catalyst)
Example of combustion: Conservation of mass
The number of moles of H, C, and O must be equal on both sides of the equation.
Stochiometry
Autothermal Reforming
It is a combination of:
- Steam reforming reaction
- Partial oxidation reaction
- The water gas-shift reaction
(1) in the same chemical reactor
(2) The heat required by the (endothermic) SR and WGS reaction is exactly provided by the (exothermic) POX reaction
(3) Steam (for SR) as a reactant
(4) Substoichiometric amount of O2 for (POX)
Autothermal Reforming: Reaction
CxHy + zH2O (l) + (x-0.5z)O2 <===> xCO2 + (z+0.5y)H2
z/x = steam to carbon ratio
It should be chosen such that the reaction is energy neutral
(neither exothermic nor endothermic)
Coal Gasification : Reaction
C + aO2 + bH2O <===> cCO2 + dCO + eH2 + “other species”
Coal Gasification: Devolatilisation
From carbon to complex gaseous mixture and porous solid char residue
Coal Gasification: gaseous mixture
Combination of partial oxidation, SR, and WGS reactions
Coal Gasification: Char Particles
Gasified to CO through partial oxidation of C
Absorption force and Adsorption force:
Weakest: Hydrogen/Helium, Oxygen
Strongest: Water
CO cleanup
Reformative stream: CO = 0.2% (2000 ppm)
Fuel cell catalyst tolerance: CO = 1-10 ppm
Goal: Reduce CO yield to extremely low level
Physical separation: Pressure swing adsorption, Palladium membrane separation
Chemical reaction: Selective methanation of CO
Selective oxidation of CO