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World Energy Outlook 2006

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important factors. Higher differentials over the past few years have made the<br />

option of adding local upgrading capacity more attractive. As a result, most<br />

planned in situ projects now also include upgrading of the raw bitumen. For<br />

integrated mining and upgrading projects, the cost of building upgrading<br />

units is a critical factor. Capital costs have risen sharply in recent years as prices<br />

of steel, cement and equipment have soared (Box 3.1). Rapid development<br />

of the oil-sands industry has also led to a shortage of skilled labour and a fall<br />

in productivity.<br />

Chapter 3 - Oil Market <strong>Outlook</strong><br />

Box 3.1: Canadian Oil-Sands Production Costs<br />

Overall production costs – including capital, operating and maintenance,<br />

but excluding taxes – are typically lower for in situ projects. The cost<br />

of producing bitumen from greenfield projects is currently about<br />

US$ 16 per barrel. It is highly sensitive to the steam-to-oil ratio (SOR),<br />

a measure of how much energy must be applied to the reservoir to induce<br />

bitumen to flow into the producing-well bore. For pure steam, an<br />

increase of 0.5 in SOR translates into an additional 6 cubic metres of<br />

natural gas consumption per barrel of bitumen, as well as increased water<br />

handling costs. At current gas prices, this equates to nearly $2 per barrel.<br />

For integrated mining, the current cost of producing synthetic crude is<br />

about $33 per barrel. Each 10% increase in capital costs is estimated to<br />

increase the per-barrel production cost by $1.50 for in situ projects and<br />

$2 for integrated projects.<br />

The energy efficiency of both in situ and integrated projects is expected to<br />

improve over the projection period. New technologies, such as bitumen or coke<br />

gasification, which are assumed to be introduced after 2012, contribute to a<br />

significant reduction in average gas intensity. Some new projects are expected<br />

to use only natural gas, but others will use gasification or a combination of the<br />

two. However, the fall in gas intensity may be partially offset by more intensive<br />

upgrading to produce higher-quality synthetic crude, which requires more<br />

hydrogen. Currently, about 60% of crude bitumen is transformed into various<br />

grades of synthetic crude or upgraded products. Although this percentage is<br />

expected to decline, we believe it will still be higher than 50% by 2015. Overall<br />

natural gas consumption for oil-sands production, including on-site gas-fired<br />

power production, is projected to rise from 10 bcm per year now to 21 bcm in<br />

2015 and 29 bcm in 2030 (Figure 3.8). These projections assume that no<br />

financial penalty for carbon-dioxide emissions is introduced. As oil-sands<br />

production is very carbon-intensive, such a move could have a major impact on<br />

prospects for new investment.<br />

99<br />

© OECD/IEA, 2007<br />

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