Title: Primary Energy, Transmission and Infrastructure
1Primary Energy, Transmission and Infrastructure
2Primary Energy Alternatives
- Nuclear
- Fossil
- Renewables
- Solar
3Nuclear Energy in the US
- 104 Operating Units
- 69 PWRs
- 35 BWRs
- 20 of the Electricity
- Operating Conditions
- PWR 325oC, 14 MPa
- BWR 290oC, 7 Mpa
- Fuel Enriched uranium
4Nuclear Energy in US
Source Energy Information Agency
5Current Nuclear Reactors and Hydrogen
- Temperatures too low
- For thermochemical cycles
- For high temperature electrolysis
- Power generation coupled to conventional alkaline
electrolysis - Efficiencies
- Power generation 32-34
- Electrolysis 80
6Nuclear Reactors Other Configurations
- Advanced BWRs, ESBWRs, AP1000
- No change in temperature/pressure
- Safety/operational features
- EPR European PW
- Standard design in France
- Fast Breeder Reactor
- Liquid metal (sodium) cooled
- Temperature 500oC
7Generation IV Reactors
- VHTR (Very High Temperature Reactor)
- GFR (Gas-cooled Fast Reactor)
- LFR (Lead-cooled Fast Reactor)
- MSR (Molten Salt Reactor)
- SFR (Sodium-cooled Fast Reactor)
- SCWR (Supercritical Water-cooled Reactor)
8VHTR
- Pebble bed modular reactor
- Prismatic modular reactor
- Helium cooled, graphite moderated, thermal
reactor - Outlet temperature 850-950oC
- High pressure coolant 5 MPa
9AHTR
- High temperature reactor like VHTR
- Molten salt (fluorides) coolant
- Li-Be fluoride
- Na-Zr fluoride
- Li-Na-K fluoride
- Atmospheric pressure
- Larger size (2400 MW) compared to VHTR (600 MW)
10Energy Transfer from Nuclear Reactor
- Electricity
- Thermal Energy
- Heat loss
- Safety aspects
11Expansion of Nuclear Energy Industry
- Needed if it is to be the primary energy source
- Global primary energy supply from nuclear energy
624 Mtoe/yr (2004 data) - Estimated need for hydrogen transport
applications in 2050 6800-15000 Mtoe/yr - Proven reserves 45000-195000 Mtoe
12Assumptions
- Annual Hydrogen transportation demand 1 Gton
- All vehicles use fuel cell engine, efficiency 50
- How long will the reserves last if all
applications use nuclear as the primary energy
source?
13Fossil Energy
- Coal, natural gas, oil
- Proven reserves (in Mtoe)
- Coal 448,000
- Natural gas 161,000
- Oil 162,000
- Hydrogen for transportation (2050)
- 6250, 3250, and 3900 respectively (in Mtoe)
14Coal Technologies
- Co-generation of hydrogen and electricity in coal
gasifiers - With carbon capture and sequestration systems
- Fossil energy will play a significant part for a
few decades
15Renewables
- Hydropower
- Wind Energy
- Geothermal
- Solar
- Photovoltaic
- Thermal
- Biomass
- Hydrogen primarily through electricity
16Capacity Increase Needed
- Solar Photovoltaic 21,000
- Geothermal 1250
- Wind 900
- Solar thermal 500
- Hydropower 25
- Biomass 10
17Biomass
- Clean and available
- Carbon neutral
- Sources
- Energy Crops
- Corn, sugarcane (bioethanol)
- Sunflower, rapeseed (biodiesel)
- Lignocellulosic
- Organic wastes domestic, industrial, agricultural
18Biomass Utilization
- Transformation into bioethanol or biodiesel
- USA Corn
- Brazil Sugarcane
- Gasification to syngas and biomethanol/hydrogen
19Biomass Availability
- Diversion of crops from alimentary purposes to
energy production - Cultivable land area
- Lignocellulosic biomass conversion
- Cellulose-to-bioethanol
20Can we afford biofuels?
- Resource requirements
- Land
- Water
- Other
- Greenhouse emissions spike
- Loss of tropical forests
- Draining of swamps
21Solar Energy
- Incident solar energy 178,000 TW/y
- Global energy demand 13 TW/y (2000)
- Relatively evenly distributed, in comparison to
geothermal, wind and hydroelectric energy - Average surface irradiation 300 W/sq.m. in
temperate climes, 650 W/sq.m. in desert
22Area Requirements
- 400,000 sq. km. for 13 TW/y
- High irradiance
- Capture efficiency 12
- Approximately 400 x 400 miles
- Only 4.4 of Sahara desert
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24Hydrogen Transmission and Distribution
- Pipelines
- Compressed Gas
- Liquid Hydrogen
- Chemical Compounds
- Container Transport
- Tankers
- Railroad tank cars
- Air Transport
- Sea Transport
25Hydrogen Pipelines in World
26Hydrogen Pipelines
- Gaseous hydrogen
- Leakage through joints, fittings, valves etc. of
concern - Natural gas vs. Hydrogen Pipelines
- Reciprocal compressors preferred for hydrogen
service - Larger diameter and more compression power needed
for hydrogen for equivalent energy transfer - Large Scale Hydrogen transmission 50-80 more
expensive than the natural gas
27Hydrogen Compression
- Centrifugal compressors not as effective as
reciprocal compressors - Recirculation of hydrogen within the compressor
- Natural Gas Centrifugal Compressors not useful
for hydrogen - Lower compression ratio
- Larger number of stages
28Reciprocal Compressors
- Natural Gas compressors can be used for hydrogen
- Seals need to be improved
- Material should be adapted to hydrogen
29Hydrogen vs. Natural Gas Transmission
- 1000 MW Thermal Output
- Hydrogen
- 330,000 Nm3/h
- 500 mm diameter pipeline
- Natural Gas
- 92,000 Nm3/h
- 400 mm diameter pipeline
- More compression power needed for hydrogen
30Liquid Hydrogen Pipelines
- Energy needed for liquefaction
- Hydrogen should be transferred as para-hydrogen
- Cryogenic lines, super-efficient vacuum
insulation required - Minimize the heat leakage
- Single phase flow regime should be maintained
- Supersonic conditions may be reached in two-phase
flow leading to increased flow resistance and
line vibration
31Liquid Hydrogen Pipeline
- Concentric Pipes
- Outer tube diameter up to 2.5 times in the inner
tube diameter - High Vacuum (10-6 torr) in the annular space
- Low emissivity of the materials to minimize
radiative heat transfer - Activated carbon adsorbent in the annular space
to adsorb residual gas - Structural material commonly used Cr18Ni9Ti
32Chemical Energy Transmission Systems (CETS)
33CETS
- Steam reforming
- CO2 reforming
- Methanol
- Methyl Cyclohexane-Toluene
- Cyclohexane-Benzene
- Ammonia
- Others?
34Steam Reforming Loop
- EVA Einzelspaltrohr-VersuchsAnlage
- Steam reforming of methane
- CH4 H2O ? CO 3H2
- CO H2O ? CO2 H2
35Steam Reforming Loop
- ADAM Anlage mit Drei Adiabaten
Methanisierungsreaktoren - Synthesis Gas ? Methane Water
- Transported Power
- EVA/ADAM 300 kW
- EVA-II/ADAM-II 5 MW
36EVA-ADAM System
37Other CETS
- Transfer as (primarily) hydrogenated liquid
- Extract hydrogen via dehydrogenation at the
delivery point - Cyclohexane-Benzene System
- 3H2 C6H6 ? C6H12
- High density of hydrogen
- Hydrogenation/Dehydrogenation reaction steps at
origin and destination
38Cyclohexane-Benzene System
39CETS
- Methylcyclohexane-Toluene System
- 3H2 C7H8 ? C7H14
- Methanol
- CH3OH H2O ? CO2 3H2
- Ammonia
- 2NH3 ? N2 3H2
- CO2 Reforming
- CH4 CO2 ? 2CO 2H2
40Comparison CETS and other Modes
Cacciola et al, Int. J. Hydrogen Energy 1985,
10325-31
41CETS and Other Modes Efficiency Comparison
42Container Transport
- Liquid Hydrogen Containers
- Cryogenic double hull tanks
- Capacity up to 60 m3
- Boil-off losses
- Emptying through controlled heating rather than
discharge pumps - Suitable for medium-scale installations (a few
thousand m3 per day)
43Containerized Gas Transport
- Pressurized cylindrical vessels
- 200 bar pressure
- Arranged in frames adapted to road transport
- Frame capacity up to 3000 m3
- Strict regulations for public safety
44Rail Transport
- Similar to road transport of gaseous or liquid
hydrogen - Large load hauled per trip due to the size of
tank car - Fewer trips and fillings
- Smaller evaporation losses
45Liquid Hydrogen Transport at Sea
- Sea Transport of LNG common
- Sea Transport of Liquid Hydrogen in Cryogenic
Tanks for Supply to the French Space Station in
Guiana - Euro-Quebec Hydro-Hydrogen Pilot Project
Transport of liquid hydrogen in five 3000 m3
tanks on a ship - Storage/Transportation accounting for 40 of the
cost of hydrogen
46Liquid Hydrogen Transport by Air
- Avoid boil-off losses in sea transport
- Low density of hydrogen compatible with air
transport - Reduced heat leakage into air container during
flight - Delivery time significantly reduced
- Negligible pressure and temperature rise during
the transport - Large air transport system needs to be developed
47Container Transport
- Railway tank cars possibly more efficient than
road transport - Gaseous/liquid tankers for localized
distribution Pipelines more efficient for long
distances - Potential air transport using superjumbo jets
48Hydrogen vs. Electricity
- Electricity
- versatile,
- superior energy carrier
- High exergy
- Electricity Transmission
- Underground/overhead
- DC/AC
- 40-765 kVAC lines
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50Transmission Comparison
- Hydrogen Pipelines
- Compression energy needed
- Diffusion leakage losses
- Frictional losses
- Electrical Transmission
- Power conversion losses at sending and receiving
ends - Transmission line losses
51Best Mode of Transmitting Energy (?)
52Transmission Penalty
53Infrastructure Requirements
- Hydrogen Storage
- Ability to manage the mismatch between production
(supply) and consumption (demand) - Easy for solid-liquid fuels
- Underground/intermediate storage containers used
for natural gas - Limited capacity for storage of electrical energy
54Hydrogen Storage
- Most likely as compressed gas
- Energy penalty in liquefaction
- Chemical storage (hydrides, etc.) uneconomical
- Cheap storage options needed
- Underground storage
- Lower pressure storage of hydrogen (compared to
natural gas)
55Decentralized Storage of Hydrogen
- Industrial Use
- Experience in petrochemical/chemical industry
- Commercial/Residential
- Safety considerations
- High pressure or cryogenic storage may be
undesirable - Metal hydride/Adsorbed hydrogen?
56Transmission Infrastructure
- Use of natural gas pipeline network for hydrogen
transmission - Pipes would be usable
- Capacity will be lower
- Fittings, valves, auxiliary equipment
(compressors) need replacement - Loading up to10 hydrogen in natural gas has no
detrimental economic impact - Simultaneous use of natural gas and hydrogen?
57Distribution Infrastructure
- Distribution through existing local natural gas
lines? - Residential use of hydrogen?
- Hydrogen filling stations
- Number of stations
- Vehicle range?