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Nuclear Production of Hydrogen, Fourth Information Exchange ...

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NUCLEAR H 2 PRODUCTION – A UTILITY PERSPECTIVE<br />

Oil shale<br />

The United States has sufficient oil shale deposits to meet our current oil demands for approximately<br />

100 years. Many oil shale deposits are thick (200 to 700 m) and can yield up to 2.5 million barrels <strong>of</strong> oil<br />

per acre, or about $125 million/acre (with oil at $50/barrel). Methods for low-cost in situ recovery <strong>of</strong><br />

shale oil are being developed by Shell Oil and others. The leading option involves drilling wells into oil<br />

shale and using electric heaters to raise the bulk temperature <strong>of</strong> the oil shale deposit to ~370°C to<br />

initiate chemical reactions that produce light crude oil, and then pumping the oil to the surface. (Note:<br />

shale oil contains no oil, the heating <strong>of</strong> the oil shale causes chemical reactions to yield oil.)<br />

Approximately 250 to 300 kW-hr <strong>of</strong> electricity are required for down-hole heating per barrel <strong>of</strong> oil.<br />

An alternative method being considered is the use <strong>of</strong> HTGR to provide high temperature heat to<br />

replace the electricity. Direct use <strong>of</strong> high temperature heat avoids the factor-<strong>of</strong>-2 loss in converting high<br />

temperature heat to electricity (which is then used to heat oil shale). The concentrated characteristics<br />

<strong>of</strong> United States oil-shale deposits make it practical to transfer high temperature heat over limited<br />

distances from a reactor to the oil shale deposits while operating the reactor for 40 to 60 years.<br />

Commercial feasibility<br />

Our evaluations on the production <strong>of</strong> hydrogen from nuclear energy have included a wide spectrum <strong>of</strong><br />

processes and techniques from conventional electrolysis using existing nuclear technologies to<br />

thermochemical water-splitting and high temperature electrolysis using advanced high temperature<br />

gas-cooled reactors. Since hydrogen production from nuclear energy will likely be a merchant operation,<br />

economic viability will depend on the competitiveness <strong>of</strong> nuclear produced hydrogen with the more<br />

traditional SMR process. Unless and until advancements are made in conventional electrolysis, it is<br />

unlikely that existing nuclear technologies and conventional electrolysis will be competitive with SMR<br />

in the bulk hydrogen markets. We believe that HTGR coupled with compatible advanced hydrogen<br />

production processes do, however, have the potential to be competitive with SMR.<br />

While the potential market for the advanced HTGR and nuclear hydrogen production technologies<br />

is substantial, key considerations such as: i) economic competitiveness with the alternatives;<br />

ii) feasibility <strong>of</strong> licensing and permitting; iii) the acceptability <strong>of</strong> the operating risks and <strong>of</strong>f-take<br />

contracts, must be assessed and deemed satisfactory before this commercial market becomes viable.<br />

Economic competitiveness<br />

Although we have a basic understanding <strong>of</strong> the advanced hydrogen production processes being<br />

considered for incorporation with the NGNP project, our assessment as to their commercial viability is<br />

very limited due to the developmental nature <strong>of</strong> the technologies and the lack <strong>of</strong> sufficient design<br />

maturity. Over the past several years, we have participated in several studies with the DOE and the<br />

Idaho National Laboratory that have resulted in what we believe to be the best available projections<br />

for cost and economics for hydrogen production using an HTGR. As depicted in Figure 5, these studies<br />

indicate a H 2 production cost in the range <strong>of</strong> $2/kg-$4/kg. In this range nuclear production <strong>of</strong> hydrogen<br />

is competitive with SMR when natural gas is above $8/MMBTU and perhaps as high as $16/MMBTU.<br />

An NGNP study currently underway suggests that the cost <strong>of</strong> hydrogen is actually in the higher<br />

end <strong>of</strong> this range. At face value, these price ranges are clearly not competitive with hydrogen<br />

produced by SMR at today’s natural gas prices. In assessing economic competitiveness, however,<br />

consideration must be given to the volatility in natural gas prices, the security <strong>of</strong> supply and the<br />

potential cost consequences <strong>of</strong> carbon legislation – all <strong>of</strong> which may influence the economics and the<br />

commercial viability discussion. Given the uncertainty in the basic cost assumptions, the fluctuation<br />

in natural gas prices seen over the past several years, and the possibility <strong>of</strong> carbon emissions legislation,<br />

it seems logical that further technology development and design work be done to more accurately<br />

estimate costs and hopefully improve economic competitiveness.<br />

Licensing and permitting<br />

There will no doubt be challenges to overcome in licensing a nuclear facility co-located or in the<br />

proximity <strong>of</strong> a major industrial complex and coupling its output to the industrial facility processes.<br />

NUCLEAR PRODUCTION OF HYDROGEN – © OECD/NEA 2010 295

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