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Canada’s Oil Sands Overview and Bitumen Blending Primer
US National Academy of Science October 23, 2012
Global Crude Oil Reserves by Country
25 21 203037
4760
92102
143151
174
211
265
0
50
100
150
200
250
300
Saud
i Ara
bia
Vene
zuela
Cana
da Iran
Iraq
Kuwait
Abu D
habi
Russ
iaLib
ya
Nigeria
Kazh
akhs
tanQata
r
United
Stat
esCh
ina
billi
on b
arre
ls
Source: Oil & Gas Journal Dec. 2011
Restricted (80%)
Open to Private Sector
Oil Sands 55%
Other 45%
World Oil Reserves Open to
Private Sector
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Oil Sands Projects in Three Deposits
Peace River
Athabasca
Cold Lake
Edmonton
Calgary
Ft. McMurray Fort
McMurray
Cold Lake
Fort Hills
Horizon
Joslyn Creek
Syncrude
Suncor
Dover
MacKay River
Firebag
Hangingstone
Long Lake
Surmont
Foster Creek
Wolf Lake/Primrose
Tucker Lake
Jackfish
Kearl Lake
Jackpine
• Oil sands production now exceeds 1.6 million barrels per day
• $123 billion
built from 1997-2010
Peace River
Peace River
Seal
Northern Lights
White Sands
In Situ Projects Mining Projects
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Oil Sands production technologies
Source: Canadian Centre for Energy Information
Steam Assisted Gravity Drainage (SAGD)
In-situ operations: • Do not have mines • Or tailings ponds
Mining – 35 billion barrels reserves 20% of the oil sands reserves is less than 200 feet deep
In-Situ – 135 billion barrels reserves 80% of the oil sands reserves is more than 200 feet deep
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Oil Sands - In Situ
● 80% of reserves produced using in-situ recovery technology
● Too deep to mine ● Technologies:
• Cyclic steam • Steam Assisted Gravity
Drainage (SAGD)
Oil Production
SAGD Process
Steam Injection
Reservoir Oil Production
Steam Chamber
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Cold Lake Cyclic Steam Stimulation (CSS)
Steam and condensed water heat the viscous oil
Steam injected into the reservoir
Heated oil and water are pumped to the surface
Stage 1 Steam Injection
Stage 2 Soak Phase
Stage 3 Production
Courtesy Imperial Oil
Mined vs SAGD Growth
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Mined Bitumen production :
• Historically integrated with Alberta Upgraders to produce synthetic crude oils thus this bitumen does not planfully leave the province.
• Future Mined production designs incorporate a process called Paraffinic Froth Treatment (PFT) which yields a bitumen (and subsequent dilbit/synbit blend) of improved coker yield value for Refiners/Upgraders as well as maintaining required Pipeline specifications. This will have some portion leaving the provincial upgrading network.
SAGD Bitumen Production :
• Upgrader feed as well as going to Refinery markets as dilbits/synbits
• high volumetric growth commodity ex Alberta for bitumen blends
Million
bpd
0.0
0.5
1.0
1.5
2.0
2.5
3.0
3.5
2011 2030
Mined
Insitu
Dilbit vs Synbit
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Raw Bitumen has a density of 960-1020 kg/m3. To meet Pipelines specifications for viscosity and density, and to meet Refinery desired heavy crude yields/qualities, a controlled blend with a diluent is produced.
Diluents fall into two categories in general
1) naphtha based diluents – used to produce a DILBIT • 650-750 kg/m3 typical density for diluent
• natural liquids, ultra light sweet crudes, imported condensates, US and Cdn Refinery components
• nominal 30% diluent required with 70% Bitumen
2) sweet synthetic crude oils (SCO) – used to produce a SYNBIT
• 840-870 kg/m3 typical density for SCO
• same as existing SCO from Alberta upgraders to Refiners for 20+ years; residue free, hydrotreated, low sulfur
• nominal 50% Synthetic crude required with 50% Bitumen
• higher refinery value than dilbit (improved yield/value)
Generallly, the market diluent pricing, access to logistics, production technologies, and Producer/Refiner economics dictate a bitumen produced as a dilbit or synbit.
Bitumen Crude Blends
● Heavy Crudes vary blend quality somewhat with seasonal temperature (for bitumen based and conventional heavies).
● Pipeline designs are for 350 cSt viscosity maximum crude and 940 kg/m3 density (one is constraining).
● Bitumen remains constant, with the diluent ratio changing. ● Viscosity limit of 350 cSt is at pipeline reference temperature
§ 7.5 - 18.5 deg C = 45.5 - 65.3 deg F § Changes on planned schedule from winter to summer in 2 week increments
● Density maximums of 940 are approached in the summer and may become the limiting blend constraint for producers then
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Blend Component
Volume (m3)
Density (kg/m³) vol frac wt frac Mass (kg)
Viscosity (cSt @ 15 C)
Bitumen Heavy 7500 1.0100 51.7% 55.6% 7575 760,000 SCO Diluent 7003 0.8650 48.3% 44.4% 6058 5.85
Synbit Total 14503 0.9400 100.0% 100.0% 13633 128
ComponentVolume
(m3)Density (kg/m³) vol frac wt frac Mass (kg)
Viscosity (cSt @ 15 C)
Bitumen Heavy 7500 1.0100 74.6% 80.5% 7575 760,000 "CRW" Diluent 2554 0.7200 25.4% 19.5% 1839 0.63
Dilbit Total 10054 0.9363 100.0% 100.0% 9414 350
Simple blend example for a dilbit and synbit
Bitumen Crude Blends
● Currently there are many Diluted bitumen crudes in the market
● Some produced for 10+ years (CL); many new ones in last 5 years
● Fewer Synbits in the market (due to more costly diluent) ● CrudeMonitor.ca is a public service providing generic crude
quality data for these blends, as well as providing a list of blend names § This program is not exhaustive for all pipelines crudes but is
representative of all commodity classes including dilbits and synbits
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Sweet Synthetic primer
SYN and OSA – legacy known sweet synthetics (20+ years)
new entries into commodity class adding refinery optimization potential for yield
Specifications of quality
generally tightly controlled Residue free (no vacuum
bottoms yield)
generic sweet synthetic yields
5
15
25
35
45
55
65
PSC SPX CNS PAS OSA SYN HSB SSX
wt%
= %
off
NaphthaKeroGasoil
Long Lake Light Synthetic
Shell Premium Synthetic
CNRL Light Sweet Synthetic
Premium Albian Synthetic
Suncor Synthetic A
Syncrude Synthetic
Husky Synthetic Blend
Shell Synthetic Light
(PSC) (SPX) (CNS) (PAS) (OSA) (SYN) (HSB) (SSX)Density (kg/m 3 ) 843.0 ± 17.6 862.4 850.7 ± 1.8 860.5 ± 3.1 860.3 ± 5.8 862.5 ± 5.7 863.9 ± 2.6 863.6 ± 4.0
Gravity ( o API) 36.3 ± 3.5 32.4 34.7 ± 0.3 32.8 ± 0.6 32.8 ± 1.1 32.4 ± 1.1 32.1 ± 0.5 32.2 ± 0.8
Sulphur (wt%) 0.08 ± 0.04 0.04 0.08 ± 0.01 0.05 ± 0.01 0.17 ± 0.02 0.18 ± 0.02 0.10 ± 0.02 0.11 ± 0.04
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