ATHABASCA OIL CORPORATION - AER€¦ · ATHABASCA 2015 ARTIFICIAL LIFT 21 ARTIFICIAL LIFT o All...
Transcript of ATHABASCA OIL CORPORATION - AER€¦ · ATHABASCA 2015 ARTIFICIAL LIFT 21 ARTIFICIAL LIFT o All...
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LEISMER D54 PERFORMANCE REPORT
ATHABASCA OIL CORPORATION
April 2019
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ATHABASCA 2015
INTRODUCTION
DEVELOPMENT OVERVIEW
SUBSURFACE
o Geoscience
o 4-D Seismic & Monitoring
o Well Design & Instrumentation
o Scheme Performance
o Pilots
o Future Plans
SURFACE OPERATIONS & COMPLIANCE
o Facilities
o Measurement & Reporting
o Facility Performance
o Water Production, Injection & Uses
o Sulphur Production
o Future Plans
o Compliance
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DEVELOPMENT OVERVIEW
PROJECT DETAILS
o First steam September 2010
o Approved processing capacity 40,000 bbl/d
o 6 producing pads
• 35 horizontal well pairs
• 13 infill wells
o 2 approved drainage areas
• Pad 7 spud Q4 2018, first steam summer 2019
• Pad 8 approval received September 2018
INFRASTRUCTURE
o Fuel gas from TransCanada Pipeline (TCPL)
o Dilbit export to Enbridge Cheecham Terminal
o Diluent supply from Enbridge Cheecham Terminal
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4 AOC Lease AreaDevelopment AreaPad Drainage AreaPad Drainage Area (Not on Production)Planned and Approved Drainage AreaSAGD Well-PairInfill Well
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SUBSURFACEGEOSCIENCE OVERVIEW
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ATHABASCA 2015
Pad 7 Observation WellCored WellImage Log(HMI) Well
4 AOC Lease AreaDevelopment AreaPad Drainage AreaPad Drainage Area (Not on Production)
SURFACE DATA OVERVIEW 5
NO NEW GEOSCIENCE DATA ACQUIRED DURING THE REPORTING PERIOD
o Cores, petrophysics, geomechanical, fracture pressure or caprock integrity tests
Area Area (km2) Cored Wells Image Logs
Lease Area 326 369 621
DevelopmentArea
37.4 144 240
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ATHABASCA 2015
STRATIGRAPHY AND REFERENCE WELL 6
De
pth
(m
SST
VD
)
100/09-33-078-10SEISMIC
PEAK
TROUGH
HIGH
LOW
GR
RESISTIVITY
HIGH
LOW Wabiskaw
McMurray
GBIP Top
GBIP Base
Devonian
Left-Gamma Ray
Right-Resistivity
SandSandy IHSMuddy IHSMudstoneLimestone
FACIES
4 AOC Lease AreaDevelopment AreaPad Drainage AreaPad Drainage Area (Not on Production)Type Well (00/09-33-078-10W4)SAGD Well-PairInfill Well
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ATHABASCA 2015
4 AOC Lease AreaDevelopment AreaPad Drainage AreaPad Drainage Area (Not on Production)Type Well (00/09-33-078-10W4)
BITUMEN PAY CLASSIFICATION: GBIP 7
ELEVATION RANGE
o 202 -241 masl
GROSS BITUMEN IN PLACE (GBIP)
o GBIP represents the total pay interval accessible via SAGD
o Petrophysical criteria:
• Gamma Ray (GR) = 40 ohm-m
• Porosity (DPSS) >= 27%
o Non-Non-reservoir lithofacies (F6–F7) are not included if greater than 2m in thickness
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ATHABASCA 2015
BITUMEN PAY CLASSIFICATION: DBIP 8
ELEVATION RANGE
o 202 -237 masl
4 AOC Lease AreaDevelopment AreaPad Drainage AreaPad Drainage Area (Not on Production)Type Well (00/09-33-078-10W4)
DEVELOPABLE BITUMEN IN PLACE (DBIP)
o DBIP has the same petrophysical properties as GBIP but is restricted to higher quality lithofacies:
• F1: Shale-Clast Breccia (if
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ATHABASCA 2015
27.1m 24.8m 28.2m 24.5m
31.2m 27.3m
A’AWABISKAW
MCMURRAY
GBIP TOP
GBIP BASEBOTTOM
WATER TOP
DEVONIAN
WABISKAW
MCMURRAY
GBIP TOP
GBIP BASEBOTTOM WATER TOP
DEVONIAN
PADS 1-6 STRUCTURAL CROSS SECTION N-S 9
A A’
Wabiskaw
McMurray
GBIP Top
GBIP Base
Devonian
PEAK
TROUGH
Left - Gamma Ray
Right - Resistivity
HIGH
LOW
GRRESISTIVITY
HIGH
LOW
Development AreaPad Drainage AreaPad Drainage Area (Not on Production)
Cross Section WellSAGD Well-PairInfill Well
A
A’
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TOP STRUCTURE MAP 10
Elevation Range 202 -241 masl
4 AOC Lease AreaDevelopment AreaPad Drainage AreaPad Drainage Area (Not on Production)Type Well (00/09-33-078-10W4)
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ATHABASCA 2015
BASE STRUCTURE MAP 11
Elevation Range 193 -231 masl
4 AOC Lease AreaDevelopment AreaPad Drainage AreaPad Drainage Area (Not on Production)Type Well (00/09-33-078-10W4)
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ATHABASCA 2015
BOTTOM WATER THICKNESS MAP 12
Elevation Range 191 -213 masl
4 AOC Lease AreaDevelopment AreaPad Drainage AreaPad Drainage Area (Not on Production)Type Well (00/09-33-078-10W4)
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TOP GAS THICKNESS MAP 13
M. McMurray Gas
Elevation Range 221-253 masl
MINIMAL GAS THICKNESS AND LIMITED DISTRIBUTION WITHIN DEVELOPMENT AREA
4 AOC Lease AreaDevelopment AreaPad Drainage AreaPad Drainage Area (Not on Production)Type Well (00/09-33-078-10W4)
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ATHABASCA 2015
GEOMECHANICS
2018
o No new caprock core, mini-frac or tri-axial testing completed during the reporting period
HISTORICAL
o Caprock defined as the Clearwater Formation
• Includes regionally continuous shale of the Wabiskaw Member
• mini-frac tests completed at two locations (01-04-079-10W4, 01-28-078-10W4)
o Approved maximum operating pressure is 5,500 kPag
o All injectors operating at ~ 3,000 - 3,300 kPag
SURFACE HEAVE MONITORING
o No new data acquired during reporting period
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Development AreaPad Drainage AreaPad Drainage Area (Not on Production)Mini-Frac LocationSAGD Well-PairInfill Well
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ATHABASCA 2015
GBIP RESERVOIR PROPERTIES 15
RESERVOIR PROPERTIES
o Original Reservoir Pressure: 2,300 to 2,600 kPa
o Original Reservoir Temperature: 14⁰C
o Average Horizontal Permeability: 5 to 6 D
o Average Vertical Permeability: 4 to 5 D
o Depth: 410 to 444 m TVD (-230 to -216 m subsea)
4 AOC Lease AreaDevelopment AreaPad Drainage AreaPad Drainage Area (Not on Production)
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SUBSURFACE4D SEISMIC & MONITORING
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SEISMIC ACQUISITION HISTORY 17
2009 4D Seismic (Baseline)2012 4D Seismic2013 4D Seismic
2014 4D Seismic 2015 4D Seismic2016 4D Seismic
4 4
2018
o No new data acquired during the reporting period
HISTORICAL
o Q1 2016: 2.0 km2 first 4D survey for Pad 5
o Q1 2015: 9.0 km2 3D survey
• Third 4D repeat survey (2.2 km2 active SAGD Pads 1 & 2)
• Repeat 3D seismic for higher resolution data
o Q1 2014: 2.1 km2 4D survey (active SAGD Pads 3 & 4)
o Q1 2013: 4.5 km2 3D survey
• Second repeat survey (4.9 km2 of active SAGD Pads 1– 4)
o Q1 2012: 8.6 km2 3D survey
• First 4D survey (4.9 km2 of active SAGD Pads 1–4)
• New baseline survey for Pads 5 and 6 (3.7 km2)
o Q1 2009: 4.9 km2 baseline survey (pre-steam) Pads 1–4
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ATHABASCA 2015
RESERVOIR SATURATION LOGGING 18
2018
o RSTs acquired from 13 wells during the reporting period
HISTORICAL
o Baseline acquired in 2010 - 23 wells
o 2011 - 18 wells
o 2012 - 7 wells
o 2013 - 12 wells
o 2014 - 11 wells
o 2015 - 6 wells
o 2018 - 13 wells
o Saturation log results show steam chamber thickness
correlates with observation well temperature profiles
Development AreaPad Drainage AreaPad Drainage Area (Not on Production)
SAGD WellInfill Well2010 RST2011 RST2012 RST2013 RST2014 RST2015 RST2018 RST
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SUBSURFACEWELL DESIGN, INSTRUMENTATION & ARTIFICIAL LIFT
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SAGD DRILLING SUMMARY
2018
o 5 well pairs were drilled on Pad 7 during Q4 2018- Q1 2019
HISTORICAL
o The Leismer project includes a Central Processing Facility
(CPF) and six well pads, with 35 well pairs and 13 infill wells
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Development AreaPad Drainage AreaPad Drainage Area (Not on Production)
SAGD WellInfill Well
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ARTIFICIAL LIFT 21
ARTIFICIAL LIFT
o All wells completed with ESP’s with the exception of two infill wells
• Rod pumps installed on infills L5N3 and L5N4
o Typical artificial lift operating conditions:
• Bottomhole pressure (BHP) range: 2,500-3,300 kPag
• BHP temperature range: 180-235 °C
Artificial Lift Performance ESP Rod
Typical Minimum Rate (m³/d) 120 100
Typical Maximum Rate (m³/d) 1,200 300
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TYPICAL COMPLETION: PADS 1–4 22
3-½” production tubing1.75" Instrumentation coil
11-¾” x 9-5/8" intermediate casing; or 11-¾” casing full length
3-½ x 2-7/8" x 3-½” long tubing
4-½” x 3-½” short tubing
7" wire-wrap screen; or7" slotted liner; or8-5/8" slotted liner
8-5/8" slotted liner
11-3/4" intermediate casing
Pump
PADS 1-4 COMPLETIONS
o Pads 1-4 injection wells completed with parallel tubing strings
o In production wells, instrumentation carried within a 1.75” coiled tubing
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TYPICAL COMPLETION: PADS 5-6 23
PADS 5-6 COMPLETIONS
o Pads 5-6 injection wells completed with concentric tubing strings
o In production wells, instrumentation carried within a 1.5” coiled tubing (coil runs inside a 2-3/8” guide string)
o 5 of 7 injectors on Pad 5 completed with Vacuum Insulated Tubing (VIT) on long tubing string
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ATHABASCA 2015
7" liner (WWS)
2-3/8" x 3-½” guide string
3-½” production tubing
Instrumentation string
16" x 13-3/8" surface casing
11-¾” x 9-5/8" intermediate casing
casing gas
Pump
TYPICAL COMPLETION: INFILL WELL 24
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INSTRUMENTATION 25
TEMPERATURE
o Mixture of thermocouples (TC) and fiber measurements
o Both systems adequate for temperature management along the wellbore
PRESSURE
o Injector BHP is measured with blanket gas
o Producer and infill BHP is measured using optical gauges and/or bubble tubes
Pad Drainage AreaDevelopment AreaSAGD Well-PairInfill WellProducer with TCProducer with FiberProducer and Injector with TCProducer with TC and Injector with FiberProducer with Fiber and Injector with TC
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OBSERVATION WELL INSTRUMENTATION
OBSERVATION WELLS
o Instrumentation used to monitor reservoir pressure and temperature
o 30 thermocouples spaced at 1 m above, below, and within SAGD pay
o 10 thermocouple bundles installed in wells previously equipped with fibre optics (DTS), February 2018
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Pad Drainage AreaDevelopment AreaThermocoupleThermocouple RepurposedFiberPiezometer
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ATHABASCA 2015
FLOW CONTROL DEVICES 27
2018
o Installed 1 tubing deployed flow control device (FCD) into L3P3 in 2018
HISTORICAL
o Liner deployed and tubing deployed FCD configurations have been used to optimize asset performance
o Able to operate at lower subcool with positive impact on temperature conformance
Pad Drainage AreaDevelopment AreaSAGD Well-PairInfill WellLiner Deployed Producer FCDLiner Deployed Injector FCDTubing Deployed Injector FCDTubing Deployed Producer FCDLiner Deployed Producer FCD and Injector FCDLinder Deployed Producer FCD and Tubing Deployed Injector FCD
Pre- FCD Install
16 months after FCD Install
Tem
per
atu
re (
⁰C)
180200220240
180200220240
L3P4 TEMPERATURE PROFILES
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SUBSURFACESCHEME PERFORMANCE
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ATHABASCA 2015
FIELD HISTORY 29
LEISMER CONTINUES TO BE A TOP-TIER OIL SANDS ASSET
o 6 producing pads
• 35 SAGD well pairs (34 pairs on production) and 13 infill wells on production
o L3P3 FCD installed in May 2018
o 4 infill wells started on Pad 5 in June 2018
o Once through steam generator (OTSG) commissioned in September 2018 to improve reliability
• Steam capacity increased to ~ 11,600 m3/d (73,000 bbl/d)
o Maximum produced monthly bitumen rate of 3,493m³/d (21,967 bbl/d) with SOR of 3.07 (Mar 2018)
0
1
2
3
4
5
6
SOR
0
20
40
60
80
100
120
140
0
2,000
4,000
6,000
8,000
10,000
12,000
14,000
2010 2011 2012 2013 2014 2015 2016 2017 2018 2019
Wel
l Co
un
t, P
rod
uce
d G
as, 1
03
m3/d
, In
ject
ed G
as, 1
03
m3/d
Flu
id R
ate,
m3/d
Oil Rate (CD) Water Rate (CD) Steam Inj Rate (CD)
Well count Gas Prod Rate (CD) Gas Inj Rate (CD)
CSOR ISOR
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ATHABASCA 2015
PAD RECOVERY FACTOR 30
NOTES:
1 Recovery Factor based on cumulative oil production in Feb 2019
o Volumetrics include 50 m at heel and toe of well pair
Pad
DBIP Above
Producer (103 m3)
DBIP (103 m3)
GBIP(103 m3)
Cumulative Production
(103 m3)
DBIP Above Producer Recovery Factor1
DBIP Recovery Factor1
GBIP Recovery Factor1
Predicted Recovery
Factor
1 2,590 3,467 3,914 2,066 80% 60% 53% 65–75%
2 2,857 2,821 3,344 1,661 58% 59% 50% 65–75%
3 2,650 3,003 3,443 1,658 63% 55% 48% 50–60%
4 1,747 2,236 2,433 1,126 64% 50% 46% 50–60%
5 2,739 3,477 4,479 973 36% 28% 22% 50–60%
6 2,914 3,471 3,836 686 24% 20% 18% 65–75%
Total 15,498 18,475 21,449 8,170 53% 44% 38% ~65%
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ATHABASCA 2015
31PAD PERFORMANCE
HIGH: Pad 6 Medium: Pad 3 LOW: Pad 4
PAD PERFORMANCE DEPENDS ON GEOLOGY AND OPERATING PARAMETERS
o Pads 6, 3 and 4 selected as examples of high, medium and low performing pads, respectively
• Selection based on average monthly oil rate and iSOR
• Differences in the productivity of the wells primarily due to geological variability
2010 2011 2012 2013 2014 2015 2016 2017 2018 2019
0
200
400
600
800
1,000
1,200
1,400
Flu
id R
ate,
m3
/d
HIGH
MEDIUM
LOW
0
2
4
6
2010 2011 2012 2013 2014 2015 2016 2017 2018 2019
iSO
R
Pad 1 Pad 2 Pad 3 Pad 4 Pad 5 Pad 6
HIGH
MEDIUM
LOW
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ATHABASCA 2015
PAD 6 SUMMARY
o First steam 2016
o Peak oil rate: ~790 m3/d (600-1300 bbl/d/wellpair)
o cSOR ~ 2.8
o High reservoir quality with thick pay
• Mostly sandy reservoir
• High oil saturation
o Significant steam chamber development since last reporting period
• OBS well 100/09-33 shows 7 m steam chamber rise near heel of L6P5
PAD PERFORMANCE: HIGH PAD 6 32
0
2
4
6
8
10
0
500
1,000
1,500
2,000
2,500
3,000
3,500
Jan 16 Jul 16 Jan 17 Jul 17 Jan 18 Jul 18 Jan 19
SOR
Flu
id R
ate,
m³/
d
Oil Rate Water Rate Steam Rate iSOR cSOR
Temperature PlotsMar 1, 2018Mar 1, 2019
L6P5H-100/09-33-078-10W400 (15m from L6P5)
Thermocouple
Injector
Producer
Res Top
Res Base
OWC
Dev
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PAD 3 SUMMARY
o First steam 2010
o Peak oil rate: ~480 m3/d (150-800 bbl/d/wellpair)
o cSOR ~ 3.0
o Good reservoir quality
o Significant steam chamber development since last reporting period
• OBS well 103/13-27 shows 5 m steam chamber development at the base after FCD installation on L3P4 well
PAD PERFORMANCE: MEDIUM PAD 3 33
0
2
4
6
8
10
0
500
1,000
1,500
2,000
2,500
3,000
3,500
2010 2011 2012 2013 2014 2015 2016 2017 2018 2019
SOR
Flu
id R
ate,
m³/
d
Oil Rate Water Rate Steam Rate iSOR cSOR
L3P4M2- 103/13-27-078-10W400 (14m from L3P4)
Temperature PlotsMar 1, 2018Mar 1, 2019
Thermocouple
Injector
Producer
Res Top
Res BaseOWC
Dev
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ATHABASCA 2015
PAD 4 SUMMARY
o First steam 2010
o Peak oil rate: 311 m3/d (150-700 bbl/d/wellpair)
o cSOR ~ 3.25
o Average reservoir quality
o Historical NCG co-injection on this pad
PAD PERFORMANCE: LOW PAD 4 34
0
2
4
6
8
10
0
500
1,000
1,500
2,000
2,500
3,000
3,500
2010 2011 2012 2013 2014 2015 2016 2017 2018 2019
SOR
Flu
id R
ate,
m³/
d
Oil Rate Water Rate Steam Rate iSOR cSOR
L4P3T- 102/16-28-078-10W400 (19m from L4P3)
Dev
OWC
Res Base
Producer
Injector
Res Top
Temperature PlotsMar 1, 2018Mar 1, 2019
Thermocouple
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ATHABASCA 2015
FCD PERFORMANCE 35
4 DEVICES HAVE BEEN INSTALLED AT LEISMER SINCE 2017
o After installation, oil production increased 125-150% per well
0
1
2
3
4
5
6
7
8
9
10
0
200
400
600
800
1,000
1,200
1,400
Jan 2017 Apr 2017 Jul 2017 Oct 2017 Jan 2018 Apr 2018 Jul 2018 Oct 2018 Jan 2019 Apr 2019
Oil Incremental Oil SORL3P3 Install June 2018
Oil
Rat
e, b
bl/
d
iSOR
0
1
2
3
4
5
6
7
8
9
10
0
200
400
600
800
1,000
1,200
1,400
Jan 2017 Apr 2017 Jul 2017 Oct 2017 Jan 2018 Apr 2018 Jul 2018 Oct 2018 Jan 2019 Apr 2019
L3P4 Install November 2017
Oil
Rat
e, b
bl/
d
iSOR
0
1
2
3
4
5
6
7
8
9
10
0
200
400
600
800
1,000
Jan 2017 Apr 2017 Jul 2017 Oct 2017 Jan 2018 Apr 2018 Jul 2018 Oct 2018 Jan 2019 Apr 2019
L3P6 Install November 2017
iSOR
Oil
Rat
e, b
bl/
d
0
1
2
3
4
5
6
7
8
9
10
0
200
400
600
800
1,000
Jan 2017 Apr 2017 Jul 2017 Oct 2017 Jan 2018 Apr 2018 Jul 2018 Oct 2018 Jan 2019 Apr 2019
L5P5 Install September 2017
Oil
Rat
e, b
bl/
d
iSOR
FCD
Inst
all
FCD
Inst
all
FCD
Inst
all
FCD
Inst
all
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ATHABASCA 2015
STEAM
STEAM PRESSURE
o Steam upstream of pads 7,000–9,000 kPa
o Steam pressure let-down to 5,000–6,000 kPa at pads
STEAM QUALITY
o Steam quality decreases during transportation to well pads due to heat losses
• Estimated at 95% for Pads 1–4, 6
• Estimated at 90% at Pad 5 due to longer, larger diameter pipe line
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ATHABASCA 2015
WELL INTEGRITY & ABANDONMENTS
WELL INTEGRITY
o No wellbore integrity failures during the reporting period (liner or casing)
ABANDONMENTS
o No producer/injector well pairs have been abandoned or suspended to date
o Well network in place to monitor conditions at 102/05-08-079-10W4
• 107/05-08-079-10W4 observation well
• 100/02-08-079-10W4 observation well
• Pressure differentials across the LGR and CLW-B have remained stable year over year
o No near term plans for well pad abandonments
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SUBSURFACEPILOTS
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ATHABASCA 2015
Development AreaPad Drainage AreaPad Drainage Area (Not on Production)
SAGD WellInfill Well
NON-CONDENSABLE GAS CO-INJECTION 39
PAD 4 NCG PERFORMANCE
o Pad 4 NCG co-injection stopped Nov 2018 after installation of once
through steam generator 5 (OTSG 5)
LEISMER FUTURE NCG PLANS
o Field-wide NCG co-injection approval received in Nov 2018
• Implementation as required in the medium term to optimize steam allocation
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ATHABASCA 2015
LEISMER FUTURE DEVELOPMENT PLANS
2019 SUBSURFACE DEVELOPMENT PLANS
o Finish Pad 7 well completions on 5 wellpairs
• Anticipated first steam in summer 2019
• Producer wells completed with ESPs and FCDs
o Evaluating opportunities for tubing deployed FCDs into producer wells on Pads 1-5
o Regulatory approval received for 10 well pairs and 9 infills on Pad 8, August 2018
o Regulatory approval received for 4 infills on Pad 6, September 2018
PAD ABANDONMENTS
o No pad abandonments anticipated at Leismer within next five years
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Development AreaPad Drainage AreaPad Drainage Area (Not on Production)
SAGD WellInfill Well
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SURFACE OPERATIONSFACILITIES
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ATHABASCA 2015
CENTRAL PROCESSING FACILITY 42
OTSG 5
Degasser
Diluent Optimization
INLET DEGASSER, OTSG 5 AND DILUENT OPTIMIZATION COMPLETED DURING REPORTING PERIOD
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FACILITY SCHEMATIC 43
UPDATED FACILITY SCHEMATIC
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SURFACEMEASUREMENT, ACCOUNTING AND REPORTING PLAN (MARP)
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ATHABASCA 2015
MEASUREMENT AND REPORTING 45
WELL TESTING
o Well tests used to calculate daily bitumen and water production
o Six hour test with 1 hr. purge to improve oil calculation accuracy
o Pads 1, 3, 5 and equipped with full test headers and test separators
o Pad 4 equipped with full test header and Multi-Phase Flow Meters (MPFM)
o Pad 2 and 4 equipped with MFPM
FQI – flow quantity indicator
AE – analyzer element
OR - orifice plate
CPF
o MARP updated to reflect additional metering associated with OTSG 5, diluent optimization and degasser projects
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ATHABASCA 2015
PRORATION FACTORS 46
0.9
2
0.8
9
0.7
7
0.9
2
0.9
4
0.9
5
0.9
5
0.9
7
0.9
6
1.0
5
1.0
5
1.0
8
1.0
8
1.0
7
0.9
9
1.0
4
1.0
3
1.0
3
1.0
4
1.0
4
1.0
0
1.0
0
1.0
2
1.0
3
0.70
0.75
0.80
0.85
0.90
0.95
1.00
1.05
1.10
1.15
1.20
Pro
rati
on
Fact
or
(-)
Net Oil Proration Net Water Proration Proration Limits
Out of range due to facility turnaround
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ATHABASCA 2015
SURFACEFACILITY PERFORMANCE
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FACILITY PERFORMANCE
SITE RELIABILITY HAS REMAINED HIGH
o CPF availability was 93% for 2018 including shutdown for planned turnaround
o Plant availability > 97% excluding turnaround
o Availability calculated based on steam capacity
MAJOR ACTIVITIES
o Completed planned turnaround at CPF - May
o Completed Norlite pipeline tie-in (reduces diluent costs) - June
o Installed and start-up of de-gasser (reduces diluent use) - May
o Commissioned OTSG 5 (improves steam reliability) - September
o Completed diluent optimization at CPF (reduces diluent costs) - November
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PRODUCTION & ELECTRICITY CONSUMPTION 49
0
20,000
40,000
60,000
80,000
100,000
120,000
Pro
du
ced
Bit
um
en
(m
3)
Bitumen Production
voluntary curtailment
0
1,000
2,000
3,000
4,000
5,000
6,000
7,000
8,000
9,000
Ele
ctri
cty
Co
nsu
mp
tio
n (
MW
h)
Electricity Consumption
turnaround
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ATHABASCA 2015
PURCHASED & PRODUCED GAS VOLUMES 50
8,000
10,000
12,000
14,000
16,000
18,000
20,000
22,000
24,000
Pu
rch
ase
d G
as
(Se
3m
3)
Purchased Gas
0
200
400
600
800
1,000
1,200
1,400
1,600
1,800
Pro
du
ced
Gas
(Se
3m
3)
Produced Gas
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ATHABASCA 2015
FLARING AND VENTING 51
0.0
10.0
20.0
30.0
40.0
50.0
60.0
70.0
Flare
d G
as
(Se
3m
3)
Flaring
LP Flare HP Flare
0.0
0.5
1.0
1.5
2.0
Raw
Wate
r V
en
ted
Gas
(Se
3m
3)
Venting
CPF Plant Trip
Lightning Strike –Partial CPF Trip
Turnaround –Shutdown/ Startup
OTSG 5 Commissioning
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ATHABASCA 2015
CO2 EMISSIONS 52
0
10,000
20,000
30,000
40,000
50,000
60,000
CO
2Eq
uiv
ale
nt
(to
nn
e)
CO2e Emissions
0.30
0.35
0.40
0.45
0.50
0.55
0.60
Em
issi
on
s In
ten
sity
(to
nn
es
CO
2e/m
3b
itu
men
)
CO2e Emissions Intensity
-
SURFACEWATER PRODUCTION, INJECTION & USES
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ATHABASCA 2015
WATER USE
SOURCE WATER USE o Water Act license allocation 317,915 m3/year (871 m3/day)
o Total non-saline water use from source wells during reporting period 199,000 m³ (545 m³/d)
• 62% of license allocation
• ~ 98.5% for process use at CPF
• ~ 1.5% for domestic use at CPF
o No saline water use
SOURCE WATER MINIMIZATION o Source water use reduced by approximately 20% from previous reporting period
o Source water intensity of 0.18 bbl water/bbl bitumen over the reporting period
o Balanced reservoir conditions minimize make-up water volume requirements
o High blowdown recycle rates minimize source water demand
TYPICAL WATER QUALITY
54
Parameter Non-saline Water Produced Water Disposal Water
TDS [mg/L]
1,475 2,450 28,400
pH [-]
8.1 7.4 12.0
Hardness [mg/L as CaCO3]
4.7 22 1.1
Total Alkalinity[mg/L as CaCO3]
850 230 6,300
SiO2[mg/L]
0 255 200
Cl[mg/L]
230 1200 11,000
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ATHABASCA 2015
SOURCE AND DISPOSAL WELLS
SOURCE WATER NETWORK
o 5 Lower Grand Rapids non-saline wells
• 1F1/16-09-079-10W4/00, 1F1/07-10-079-10W4/00
• F1/04-09-079-10W4/00, 1F1/16-04-079-10W4/00
• 1F1/03-04-079-10W4/00
o 2 Clearwater B saline wells
• 1F2/04-28-078-10W4/00
• 1F2/01-10-078-10W4/00
o 3 well source water monitoring network
• 100/03-05-079-10 W4/00 (local)
• 100/11-02-078-10 W4/00 (regional)
• 100/03-22-081-08 W4/00 (regional)
DISPOSAL NETWORK
o Class 1b Disposal, Approval No. 11479B
o 2 Basal McMurray disposal wells
• 100/12-33-078-10W4/00
• 100/13-33-078-10W4/00
o 2 well disposal monitoring network
55
Development AreaPad Drainage Area
Pad Drainage Area (Not on Production)
Disposal WellNon-saline WellSaline WellDisposal Monitoring WellSource Monitoring Well
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ATHABASCA 2015
DISPOSAL WELL MONITORING 56
5
8
11
14
17
20
Feb 18 Apr 18 Jun 18 Aug 18 Oct 18 Dec 18 Feb 19
Tem
per
atu
re (
C)
Bottom Water Temperature
15-28 L6 10-33
DISPOSAL WELL MONITORING
o 2 monitoring wells measuring pressure and temperature
• 100/10-33-078-10W4/2
• 102/15-28-078-10W4/00
o Bottom water temperature and pressure measurements consistent year-over-year
2,500
2,700
2,900
3,100
3,300
3,500
Feb 18 Apr 18 Jun 18 Aug 18 Oct 18 Dec 18 Feb 19
Pre
ssu
re (
kPa)
Bottom Water Pressure
15-28 L6 10-33
Data transmission offline
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ATHABASCA 2015
SOURCE WATER USAGE 57
0
5,000
10,000
15,000
20,000
25,000
30,000
35,000
40,000
Vo
lum
e (
m3)
03-04-079-10W4 04-09-079-10W4 07-10-079-10W4 16-04-079-10W4 16-09-079-10W4
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ATHABASCA 2015
STEAM INJECTION 58
0
50,000
100,000
150,000
200,000
250,000
300,000
350,000
400,000
Mo
nth
ly V
olu
me (
m³)
Monthly Volume Monthly Capacity
Turnaround
Voluntary Curtailment
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ATHABASCA 2015
PRODUCED WATER 59
0
50,000
100,000
150,000
200,000
250,000
300,000
350,000
400,000
Mo
nth
ly V
olu
me (
m³)
Monthly Volume
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ATHABASCA 2015
DISPOSAL WATER 60
o Disposal limit calculated as per Directive 081
0
5,000
10,000
15,000
20,000
25,000
30,000
35,000
40,000
Mo
nth
ly V
olu
me (
m³)
Monthly Volume Monthly D81 Limit
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ATHABASCA 2015
DISPOSAL WATER PRESSURE & TEMPERATURE 61
0
10
20
30
40
50
60
70
80
90
-1,000
0
1,000
2,000
3,000
4,000
5,000
6,000
Dis
po
sal Te
mp
era
ture
(°C
)
Dis
po
sal W
ellh
ead
Pre
ssu
re (
kPag
)
13-33-078-10W4 WHP (kPag) 12-33-078-10W4 WHP (kPag)
WHP Limit (kPag) Disposal Water Temp. (C)
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ATHABASCA 2015
BLOWDOWN RECYCLE & SLOP OIL 62
0%
10%
20%
30%
40%
50%
60%
70%
80%
90%
Blo
wd
ow
n R
ecy
cle R
ate
(%
)
Axis Title
Blowdown Recycle
0
200
400
600
800
1,000
1,200
1,400
1,600
1,800
2,000
Slo
p V
olu
me (
m3)
Slop Volume
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ATHABASCA 2015
OTHER WASTE STREAMS
SOLIDS DISPOSAL:
o Water treatment solids (lime softening) are pumped to settling pond
o The pond is dredged and solids removed for offsite disposal as required
o No disposal required during this reporting period
63
-
SURFACESULPHUR PRODUCTION
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ATHABASCA 2015
SULPHUR & SULPHUR DIOXIDE
SULPHUR & SULPHUR DIOXIDE REPORTING
o EPEA Approval No. 241311 limit is 2.0 t/d of SO2 emissions
o Average daily SO2 emissions over period was 0.99 t/d (50% of approval limit)
o SO2 emissions are calculated based on analytical results of produced gas samples
o There are no sulphur recovery facilities at Leismer
65
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ATHABASCA 2015
DAILY & QUARTERLY SULPHUR EMISSIONS 66
0
10
20
30
40
50
60
70
Su
lph
ur
Dio
xid
e E
mis
sio
ns
(to
nn
es)
Sulphur Dioxide Emissions
Avg Quarterly Emissions Q1-2018: 1.29 t/dQ2-2018 0.77 t/dQ3-2018 0.98 t/dQ4-2018 0.96 t/d
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ATHABASCA 2015
FUTURE PLANS
LEISMER FUTURE PLAN
o CPF debottlenecking to support additional pads/production as required
67
-
COMPLIANCEREGULATORY & ENVIRONMENT
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ATHABASCA 2015
69
69
Date Approval/Amendment Activity
March 2018OSCA Approval No. 10935
EPEA 241311-00-06Replace approved 104.3 MW OTSG with a 124 MW OTSG
July 2018 Disposal Approval No. 11479B Amend monitoring well network (replacement well)
August 2018 OSCA Approval No. 10935V Pad 8 Development - 10 well pairs and 9 infill wells
September 2018 OSCA Approval No. 10935W Pad 6 Infill Development – 4 infill wells
November 2018 OSCA Approval No. 10935X Non-Condensable Gas Co-injection – project pads as required
January 2019 WA License No. 00239880 Amendment to measure water level when a well is producing
69
APPROVALS AND AMENDMENTS
Noteso OSCA – Oil Sands Conservation Act (scheme approval) o EPEA – Environmental Protection and Enhancement Act Approvalo WA - Water Act
COMPLIANCE - REGULATORY
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ATHABASCA 2015
70
70
Inspections
Event Location Inspection ID Result
AER Watercourses, August 3, 2018 LOC 930765LOC 931332
47717 Satisfactory
AEP Borrow Pit, July, 11, 2018 SML 140055 N/A Compliance, August 2018
AER EPEA 241311, October 22, 2018 CPF 08-02-079-10 W4 482196 Satisfactory
AER Pipeline, October 22, 2018 License 58659 482196 Satisfactory
AER EPEA 241311, November 22, 2018 CPF 08-02-079-10 W4 482418 Satisfactory
COMPLIANCE – INSPECTIONS AND AUDITS
70
AUDITS
o AER, July 27, 2018, requested the Site-Specific Liability Assessment (SSLA) for CPF
• SSLA Submitted, August 2018
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ATHABASCA 2015
71
71
Non-Compliance Summary
Event Corrective Action
April 18, 2018 – AER Notice of Non-Compliance (MARP), Directive 017, Section 12.3.2
January 21, 2019 - AER requested Directive 017 Variance for bitumen measurement outside the scheme boundary (MARP)
AOC submitted requested information May 24, 2018
AOC submitted Directive 017 Variance Request February 7, 2019
August 27, 2018 – heavy rain washed out berm resulting in unapproved release of surface water (EPEA Approval No. 241311)
AOC repaired damaged berm and inspected entire berm system to ensure no further potential
January 30, 2019 – transducer failure prevented daily water level measurement in wells (Water Act Approval No. 239880)
AOC completed equipment repair and replacement
COMPLIANCE – NON-COMPLIANCE SUMMARY
71
From March 1, 2018 to February 28, 2019 there were 3 reportable releases
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ATHABASCA 2015
COMPLIANCE - MONITORING PROGRAMS
AIR QUALITY MONITORING
o Passive air monitoring – no exceedances (SO2, NO2, H2S) of Ambient Air Quality Objectives
o Continuous ambient air monitoring
• WBEA air monitoring station used, Q1 2018 – only March 2018 data applicable for this reporting period
• No exceedances (SO2, NO2, H2S) of Ambient Air Quality Objectives
o All monitoring stations registered as required by new Air Monitoring Directive - Jan. 2019
o Leismer has 2 CEMS units reporting data
• New CEMS units on OTSG 4 & OTSG 5 installed and certified during reporting period
• CEMS unit on OTSG 1 decommissioned December 2018
72
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ATHABASCA 2015
COMPLIANCE - MONITORING PROGRAMS 73
0
2
4
6
8
10
12
14
Mar-18 Apr-18 May-18 Jun-18 Jul-18 Aug-18 Sep-18 Oct-18 Nov-18 Dec-18 Jan-19 Feb-19
kg/h
r
OTSG 1 &4 - Monthly Average NOx
OTSG 1 OTSG 4 Limit
0
2
4
6
8
10
12
14
16
18
20
Oct-18 Nov-18 Dec-18 Jan-19 Feb-19
kg/h
r
OTSG 5 - Monthly Average NOx
OTSG 5 Limit
NOX MONTHLY AVERAGE
o New CEMS installed on OTSG 4 & 5, operational October 2018
o CEMS on OTSG 1 no longer reporting as of January 2019
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ATHABASCA 2015
COMPLIANCE – MONITORING PROGRAMS
ENVIRONMENTAL PROTECTION & ENHANCEMENT ACT (EPEA) APPROVAL
o EPEA monitoring programs and/or reports completed during the reporting period:
• Monthly and annual air emissions
• Industrial wastewater and runoff
• Groundwater water - including thermal screening assessment for well pads, new requirement June 2018
• Soil Monitoring Program report and Soil Management Program Proposal
• Conservation and Reclamation
• Wildlife – wildlife monitoring report is submitted every 3 years (May 15, 2018)
o The AER authorized the following program/plans during the reporting period:
• Reclamation Monitoring Program - October 2018
• Project-Level Conservation, Reclamation and Closure Plan - January 2019
WATER ACT
o All diversions were below license limits and monthly and annual reporting completed
• Groundwater licenses (0239880, 0029742, 00368609)
• Surface water licenses (00273542,00364442, 00364731)
74
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ATHABASCA 2015
COMPLIANCE – RECLAMATION PROGRAMS
RECLAMATION PROGRAMS
o MSL 121772 - completed soil placement, contouring, woody debris placement in preparation for tree planting in spring 2019
o Outstanding OSE sites (251) received reclamation certificates in January 2019
o AOC has received reclamation certificates for all OSE programs at Leismer
75
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ATHABASCA 2015
COMPLIANCE – REGIONAL INITIATIVES
AOC IS A FUNDING MEMBER OF:
o Oil Sands Environmental Monitoring
o Wood Buffalo Environmental Association (WBEA) – air shed monitoring
o Regional Industry Caribou Collaboration (RICC)
o Oil Sands Black Bear Partnership
o Faster Forests – reclamation research industry collaboration
o Industrial Footprint Reduction Options Group (iFROG) – wetland reclamation industry collaboration
AOC PARTICIPATES IN:
o Various CAPP Committees
• Oil Sands Environmental Policy and Regulatory Committee
• NE Alberta Caribou Working Group
• Indigenous Affairs Committee
• Air Issues Committee
76
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ATHABASCA 2015
COMPLIANCE – STATEMENT OF COMPLIANCE
ATHABASCA OIL CORPORATION LEISMER PROJECT IS IN COMPLIANCE WITH AER APPROVALS AND REGULATORY REQUIREMENTS
o For the period of March 1, 2018 to February 28, 2019 AOC has no unaddressed non-compliant events
77
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ATHABASCA 2015
78
78
ATHABASCA OIL CORPORATIONSUITE 1200, 215 - 9TH AVENUE SW
CALGARY, AB T2P 1K3P:403-237-8227F:403-264-4640