ANNUAL REPORT 2011 - Connacher Oil and Gas
ANNUAL REPORT 2011 - Connacher Oil and Gas
ANNUAL REPORT 2011 - Connacher Oil and Gas
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AR <strong>2011</strong><br />
PG 25<br />
OPERATING COSTS (1)<br />
Three months ended December 31 <strong>2011</strong> 2010<br />
($000 except per unit amounts) <strong>Oil</strong> s<strong>and</strong>s Crude oil Natural gas Total <strong>Oil</strong> s<strong>and</strong>s Crude oil Natural gas Total<br />
Operating costs $ 23,923 $ 781 $ 560 $ 25,264 $ 22,447 $ 1,331 $ 1,145 $ 24,923<br />
Operating costs ($ per bbl / Mcf / boe) (2) $ 19.62 $ 20.35 $ 2.07 $ 19.39 $ 18.96 $ 16.57 $ 1.50 $ 17.91<br />
Year ended December 31 <strong>2011</strong> 2010<br />
($000 except per unit amounts) <strong>Oil</strong> s<strong>and</strong>s Crude oil Natural gas Total <strong>Oil</strong> s<strong>and</strong>s Crude oil Natural gas Total<br />
Operating costs $ 97,295 $ 2,929 $ 2,912 $ 103,136 $ 60,344 $ 4,407 $ 5,403 $ 70,154<br />
Operating costs ($ per bbl / Mcf / boe) (2) $ 20.08 $ 18.80 $ 1.93 $ 19.64 $ 20.15 $ 13.67 $ 1.63 $ 18.12<br />
(1) Effective October 1, 2010, the capitalized costs relating to the company’s second oil s<strong>and</strong>s project, Algar, were subjected to depletion <strong>and</strong> the revenues, expenses <strong>and</strong> finance charges associated with<br />
the project were reported in the statement of operations. Prior thereto, Algar was considered a major development project under construction <strong>and</strong> all costs, including related financing costs <strong>and</strong> operating<br />
expenses net of revenue were capitalized. Accordingly, the above table does not include operating results for Algar prior to October 1, 2010.<br />
(2) Per unit costs are calculated using operating costs divided by bitumen, crude oil <strong>and</strong> natural gas actual volumes sold.<br />
Total oil s<strong>and</strong>s operating costs increased by 7 percent in Q4 <strong>2011</strong> compared to Q4 2010, reflecting general industry cost conditions <strong>and</strong> increased by<br />
61 percent in YTD <strong>2011</strong> compared to YTD 2010 due to the incremental production at Algar. Operating costs in <strong>2011</strong> also include incremental costs<br />
related to our SAGD+ pilot project.<br />
The table below summarizes information related to our oil s<strong>and</strong>s operating costs:<br />
Three months ended December 31 Year ended December 31<br />
<strong>2011</strong> 2010 <strong>2011</strong> 2010<br />
($000) ($ per bbl) ($000) ($ per bbl) ($000) ($ per bbl) ($000) ($ per bbl)<br />
Natural gas costs (1) $ 6,696 5.49 $ 7,187 6.07 $ 29,263 6.04 $ 18,142 6.06<br />
Other operating costs 17,227 14.13 15,260 12.89 68,032 14.04 42,202 14.09<br />
Total oil s<strong>and</strong>s operating costs $ 23,923 $ 19.62 $ 22,447 $ 18.96 $ 97,295 $ 20.08 $ 60,344 $ 20.15<br />
(1) Excluding risk management contract gains <strong>and</strong> losses. Includes natural gas consumed by boilers at the cogeneration facility <strong>and</strong> by other vessels at Great Divide.<br />
We utilize natural gas primarily for our boilers at both plants <strong>and</strong> our cogeneration facility at Algar. In Q4 <strong>2011</strong>, the combined steam: oil ratio (“SOR”)<br />
from Pod One <strong>and</strong> Algar was 4.1 compared to 3.8 in Q4 2010. On a YTD basis, SOR was 4.0 in <strong>2011</strong> compared to 4.3 in 2010. The company had<br />
been producing high levels of steam at Algar to test the reservoir performance while in ramp-up, but recently reduced steam production without any<br />
attendant reduction of bitumen production. At Pod One, the higher SORs reflect the impact of underperforming wells on the north pad. The drilling of<br />
new wells <strong>and</strong> new technologies such as SAGD+ are anticipated to lower SORs <strong>and</strong> improve individual well <strong>and</strong> overall productivity.<br />
We commissioned our 13 megawatt cogeneration plant at Algar in 2010 <strong>and</strong> as a consequence have experienced the benefits of improved power<br />
stability in our oil s<strong>and</strong>s operations. Although this has resulted in higher natural gas utilization <strong>and</strong> related costs, it has reduced our reliance on third<br />
party power suppliers <strong>and</strong> has improved operational reliability at both Pod One <strong>and</strong> Algar.<br />
The company also recorded risk management contract losses of $1.9 million in Q4 <strong>2011</strong> <strong>and</strong> $2.5 million in YTD <strong>2011</strong> relating to AECO natural<br />
gas purchase contracts. These losses are not included in the calculation of operating costs noted in the table above. Currently, the company has the<br />
following AECO natural gas price risk management contracts:<br />
• January 1, 2012 – December 31, 2012 – 5,000 GJ/d at a minimum of AECO CAD$3.70/GJ <strong>and</strong> a maximum of AECO CAD$4.30/GJ;<br />
• January 1, 2012 – December 31, 2012 – 5,000 GJ/d at a minimum of AECO CAD$2.80/GJ <strong>and</strong> a maximum of AECO CAD$4.00/GJ;<br />
• March 1, 2012 – June 30, 2012 – 2,500 GJ/d at a minimum of AECO $1.85/GJ <strong>and</strong> a maximum of AECO $2.90/GJ; <strong>and</strong><br />
• July 1, 2012 – September 30, 2012 – 2,500 GJ/d at a minimum of AECO $1.85/GJ <strong>and</strong> a maximum of AECO $3.20/GJ.<br />
SAGD+<br />
<strong>Connacher</strong> completed a steam with solvent (SAGD+) field trial on two of its wells located on Pad 203 at Algar in <strong>2011</strong>, as a pilot project designed<br />
to enhance reservoir recovery <strong>and</strong> bitumen production, while lowering steam injection volumes. Results were encouraging, with an approximate<br />
29 percent increase in base-line bitumen production <strong>and</strong> a reduction in SOR by approximately 17 percent. The company is currently completing a<br />
commercial front-end engineering design study on this project. While solvent recoveries <strong>and</strong> related production impact have exceeded expectations,<br />
facility modifications will have to be implemented to fully capture <strong>and</strong> recycle the recovered solvent.