update on esp operation at bp wytch farm
TRANSCRIPT
Update on ESP Operation at BP Wytch Farm OilfieldBy Erwin WahidiyatPresented at the European Artificial Lift Forum 17-18 February 2010
2
Presentation Agenda
Introduction to Wytch Farm Oilfield:
Location
Sherwood Reservoir Summary
Role of ESP in Sherwood Reservoir Development
ESP Run-Life Progression: 1985 �– 2009
Summary of Run-Life Measurements
Failures by Components
High HP ESP System MTTF
Shift in Depletion Plan & Impact on ESP Strategy
Summary of Current ESP Systems
Past-Present Comparisons �– M11 & M15 Examples
Application of Dual ESP to Extend Life Cycle
Application of Dual ESP to Manage Productivity Uncertainties
Closing Remarks
3
Wytch Farm Oilfield - Location
miles
Well sitesBottom hole locations
Sherwood reservoir
BournemouthPoole
Poole Harbour
Purbeck
milesmiles
Well sitesBottom hole locations
Sherwood reservoirWell sitesBottom hole locations
Sherwood reservoir
BournemouthPoole
Poole Harbour
Purbeck
�• Located in a sensitive environmental area on the southern coast of England, about 120 miles from London
�• Oil export via 90km 16�”Purbeck-Southampton pipeline, LPG via road tanker, gas by Purbeck-Sopley pipeline
�• 11 wellsites, total active wells (producers & injectors): 65. Active ESP wells: 31
�• Reservoirs: Sherwood, Bridport, Frome, Kimmeridge, Wareham, Arne, & Stoborough.
�• Current field production: 20+ MBDO at 93% water cut.
4
Sherwood Reservoir: Summary & PVT Properties
Sherwood Reservoir Summary:
�•Triassic sandstone reservoir, with top reservoir at ca. 1585 m-TVDSS with a maximum 110-m column of oil bearing sand above the oil/water contact
�•Upper reservoir: Zones 10-40, Lower reservoir: Zones 50-100. Zones 20, 40, & 60 (muddier intervals) act as barriers
�•Three main oil bearing zones: Zones 30, 50, & 70 (decreasing permeability and net-to-gross in the upper zones). PI ranges from 1 to 100+ BPD/psi
�•The western part of the field lies onshore (below Poole harbour & surrounding area) & the eastern part of the reservoir lies offshore
�•Over half of the Sherwood reserves lies in the offshore area, which necessitated the drilling of ERD wells beginning 1993
�•Production from Sherwood reservoir accounts for 85% of total WYF production
�•Reservoir conditions relatively benign for operating ESPs (See tabulated PVT properties)
�•Normally Occurring Radioactive Material (NORM) is present with the produced fluids and causes complications when retrieving downhole completion and the handling of retrieved ESPs during teardown.
A l l z o n e s in w e s t e r n a r e a s h a v eL o w e r N e t t o G r o s s – t h is l im i t s
V e r t ic a l c o n n e c t iv i t y t o u p p e r r e s e r v o i r
X 0 2 A r e a – Z 7 0 i s v . p o o r q u a l i t y – l im i t s
V e r t i c a l c o n n e c t i v i t y
F a u l t s / f r a c t u r e s c a n b e C o n d u c t i v e a n d n o n - c o n d u c t i v e :* F a u l t o r ie n t a t i o n* N e t : G r o s s* P r o x im it y t o f lo o d f r o n t
I n je c t i v i t y o f u p p e r r e s e r v o irI n o n s h o r e a r e a h a s n o t y e t b e e n t e s t e d
B a s e o f Z 1 0 i n b o t h w e s tA n d e a s t a p p e a r s s a n d ie r
F r o m c o r e o b s e r v a t i o n s
B a s e o f Z 1 0 : is o la t e d f lu v ia l c h a n n e ls o b s e r v e d in c o r e
D is t a l ( f u r t h e r a w a y )f r o m s e d im e n t s o u r c e
D e n s e f a u l t s a n d f r a c t u r e s
D e n s e f a u l t s a n d f r a c t u r e s
R h iz o c r e t io n s a n d s p r e s e n t m o s t l yI n Z 5 0 ( l o c a l l y in Z 3 0 i n o f f s h o r e a r e a )- C o u ld b e m o r e p o o r l y c o n n e c t e d t h a n
- F lu v ia l s a n d s d u e t o m u d d ie r o v e r b a n k- d e p o s i t s
Z 5 0 / Z 7 0 s t r a n d e d A t t i cT a r g e t s p o s s ib le
B a s e Z 1 0 a p p e a r s s a n d ie r f ie ld w id e
M id Z o n e 3 0 s i l t s t o n e / s a b k h aA p p e a r s f ie l d w id e in c o r e
Z 4 0 / Z 6 0 ( a n d lo c a l l y Z 2 0 ) a r e d is c o n t i n u o u s in t h e
o f f s h o r e a r e a s o a r e b a f f le s r a t h e rt h a n b a r r i e r s t o f lu id f lo w
Z 7 0 : p e r m e a b i l i t y c a n b e U p t o 4 D a r c ie s
P r o x im a l ( c l o s e r t o )s e d im e n t s o u r c e
B a s e Z 1 0 : l o c a l i s e d i s o la t e d F lu v ia l c h a n n e ls i n e a s t e r n a r e a s
( a n d o c c a s io n a l l y in w e s t ) .
A l l z o n e s s h o w in c r e a s e in N e t t oG r o s s in o f f s h o r e a r e a , w h e r e
c h a n n e l s a n d s b e c o m e m o r e p r e v a le n t
> P e r m e a b i l i t y d i s t r ib u t io n d r iv e nb y f a c ie s t y p e
> B e s t q u a l i t y s a n d s a n d a v e r a g e s a n d sa r e in d is t in g u is h a b le o n p o r o s i t y lo g s
> 6 - 8 % p o r o s i t y s a n d c a n h a v e g o o dp e r m e a b i l i t y ( c u r r e n t p o r o s i t y c u t - o f ff o r n e t s a n d i s 1 2 % )
A l l z o n e s in w e s t e r n a r e a s h a v eL o w e r N e t t o G r o s s – t h is l im i t s
V e r t ic a l c o n n e c t iv i t y t o u p p e r r e s e r v o i r
X 0 2 A r e a – Z 7 0 i s v . p o o r q u a l i t y – l im i t s
V e r t i c a l c o n n e c t i v i t y
F a u l t s / f r a c t u r e s c a n b e C o n d u c t i v e a n d n o n - c o n d u c t i v e :* F a u l t o r ie n t a t i o n* N e t : G r o s s* P r o x im it y t o f lo o d f r o n t
I n je c t i v i t y o f u p p e r r e s e r v o irI n o n s h o r e a r e a h a s n o t y e t b e e n t e s t e d
B a s e o f Z 1 0 i n b o t h w e s tA n d e a s t a p p e a r s s a n d ie r
F r o m c o r e o b s e r v a t i o n s
B a s e o f Z 1 0 : is o la t e d f lu v ia l c h a n n e ls o b s e r v e d in c o r e
D is t a l ( f u r t h e r a w a y )f r o m s e d im e n t s o u r c e
D e n s e f a u l t s a n d f r a c t u r e sD e n s e f a u l t s a n d f r a c t u r e s
D e n s e f a u l t s a n d f r a c t u r e sD e n s e f a u l t s a n d f r a c t u r e s
R h iz o c r e t io n s a n d s p r e s e n t m o s t l yI n Z 5 0 ( l o c a l l y in Z 3 0 i n o f f s h o r e a r e a )- C o u ld b e m o r e p o o r l y c o n n e c t e d t h a n
- F lu v ia l s a n d s d u e t o m u d d ie r o v e r b a n k- d e p o s i t s
Z 5 0 / Z 7 0 s t r a n d e d A t t i cT a r g e t s p o s s ib le
B a s e Z 1 0 a p p e a r s s a n d ie r f ie ld w id e
M id Z o n e 3 0 s i l t s t o n e / s a b k h aA p p e a r s f ie l d w id e in c o r e
Z 4 0 / Z 6 0 ( a n d lo c a l l y Z 2 0 ) a r e d is c o n t i n u o u s in t h e
o f f s h o r e a r e a s o a r e b a f f le s r a t h e rt h a n b a r r i e r s t o f lu id f lo w
Z 7 0 : p e r m e a b i l i t y c a n b e U p t o 4 D a r c ie s
P r o x im a l ( c l o s e r t o )s e d im e n t s o u r c e
B a s e Z 1 0 : l o c a l i s e d i s o la t e d F lu v ia l c h a n n e ls i n e a s t e r n a r e a s
( a n d o c c a s io n a l l y in w e s t ) .
A l l z o n e s s h o w in c r e a s e in N e t t oG r o s s in o f f s h o r e a r e a , w h e r e
c h a n n e l s a n d s b e c o m e m o r e p r e v a le n t
> P e r m e a b i l i t y d i s t r ib u t io n d r iv e nb y f a c ie s t y p e
> B e s t q u a l i t y s a n d s a n d a v e r a g e s a n d sa r e in d is t in g u is h a b le o n p o r o s i t y lo g s
> 6 - 8 % p o r o s i t y s a n d c a n h a v e g o o dp e r m e a b i l i t y ( c u r r e n t p o r o s i t y c u t - o f ff o r n e t s a n d i s 1 2 % )
0H2S, % mol
0.09CO2 % mol
1600-2200Current pressure, at datum, psig
150Reservoir Temperature at datum, deg. F
2420Initial Reservoir Pressure at datum,
psig
1070Bubble Point Pressure, psig
357Solution GOR, SCF/STB
38.3Oil Gravity (API) at 60 deg. F
ValuePVT Properties
5
Role of ESP in The Development of Sherwood Reservoir
Sherwood Development History & its relation to number of ESP installations:
1978 - Discovery of Sherwood Reservoir
1985 �– 1st ESP installation (3 installations in 1985)
1990 - Start of multi-zone, vertical onshore development wells �– 16 ESP installations
1993 - Start of ERD wells (offshore Sherwood development) �– 9 ESP installations
1996 �– Field production peaked at 101+ MBOPD (average ESP installations during the field production peak, from 1995-1998: 13)
1997 - Start of infill drilling program �– 14 ESP installations
1998 �– Over 100 ESP installations to date.
1999 - Production came off plateau
2009 - Average Sherwood Oil Rate: 17.2 MBOPD, water cut: 93%. Average ESP Installations 1999 �– 2009: 8. Cumulative ESP installation count to date: 193.
S h e rw o o d Re s e r v o ir O il P ro d u c tio n : 1 9 7 8 - 2 0 0 9
0
5 0
1 0 0
1 5 0
2 0 0
2 5 0
1 9 7 5 1 9 8 0 1 9 8 5 1 9 9 0 1 9 9 5 2 0 0 0 2 0 0 5 2 0 1 0 2 0 1 5
MB
PD
0 %
1 0 %
2 0 %
3 0 %
4 0 %
5 0 %
6 0 %
7 0 %
8 0 %
9 0 %
1 0 0 %
Wat
er C
ut
F ie ld O il P ro d uc tio n -S he rwo o d F ie ld W a te r P ro d uctio n - S he rwo o dF ie ld W a te r C ut - S he rw o o d
Sherwood Reservoir Development & ESP Installations 1978-2009
0
2
4
6
8
10
12
14
16
18
1975 1978 1981 1984 1987 1990 1993 1996 1999 2002 2005 2008
ESP
Inst
alla
tion
Cou
nt
0
10
20
30
40
50
60
70
80
90
1001974.5 1979.5 1984.5 1989.5 1994.5 1999.5 2004.5
Sher
woo
d O
il Pr
oduc
tion,
MB
OPD
ESP Installation Count Sherwood Field Oil Production
6
Wytch Farm ESP Run-life Progression
Failure ESPRuntime ESP
MTTF
Wytch Farm ESP Installation, Failure Counts & MTTF: 1985-2009
02468
1012141618
1985
1987
1989
1991
1993
1995
1997
1999
2001
2003
2005
2007
2009
0
250
500
750
1000
1250
1500
ESP
MTT
F, d
ays
Failure Count Premature Failure Installation Count ESP MTTF
1985 �– 1st ESP installation:
�•Three installations, with two premature failures**
�•1st ESP installed had a zero run life.
�•MTTF*: 68 days, Runtime to Failure*: 1 day
2009 �– As of 25th of November:
�•Total ESPs installed to date: 193
�•Total premature failures** to date: 23
�•Total failed ESPs to date: 113
�•MTTF*: 1,415 days, Runtime to Failure*: 805 days
Notes:
*Per day, runtime is calculated as follows: If runtime <12 hours = 0, If runtime>, or equal to 12 hours = 1
** Premature failure: <, or equal to 3-month runtime
Failure ESPRuntime ESP Failed
Failure To Runtime
Wytch Farm ESP Run-Life Measurements: 1985-2009
0
200
400
600
800
1000
1200
1400
1600
1985 1990 1995 2000 2005 2010
Installation Period
Day
s
020406080100120140160180200
Cum
ulat
ive
ES
P In
stal
latio
n C
ount
Mean Time To Failure, Days Runtime to Failure, Days ESP Installation Count
7
Wytch Farm ESP Failures By Components*
* Estimated, component failure does not translate to it being the root cause of failure
Wytch Farm ESP Failure Modes
Penetrators (Wellhead & Packer):
6%"Cable" including main cable, MLE, pigtail, splice, surface
cable, etc.22%
Pump14%
Motor44%
Seal2%
External - ESP Not at fault4% Unknown
8%
Penetrators (Wellhead & Packer): "Cable" including main cable, MLE, pigtail, splice, surface cable, etc.Pump Motor
Seal External - ESP Not at faultUnknown
8
Experiences with High HP Motor ESP Systems
The drilling of prolific Sherwood wells, particularly in the offshore area, necessitated the use of high flow rate ESP with high HP motor system (defined arbitrarily as greater than, or equal to 800 HP).
The 1st high HP ESP motor system installed in October 1997
To date, a total of 47 high HP ESP systems have been installed (27 failures, of which 3 were premature failures).
Nominal pump flow rates: 8,500 �– 28,000 BFPD
The largest HP ESP motor system: 1,400 HP (2 x 700 HP motors, installed in 2006), with 28 MBD nominal pump flow rate
Large HP Motor ESP System MTTF Comparison:
Installation Period: 1997 - 2009 MTTF, days
All ESPs 1919Large HP Motor ESP Systems 1634
9
Factors Contributing to Improvement in ESP Run-Life
Continuous learning from previous installations & operations (in total 25 years of ESP operation at WYF)
Abundance of local knowledge & experience: Some field operators have been around since day 1.
Onsite presence of ESP vendor support
Continuous training of field operators on the day-to-day ESP operations.
Relatively benign downhole (reservoir) conditions in the Sherwood reservoir (i.e., relatively low P, T, consolidated sandstone).
High water cut means less tweaking of ESP frequency to optimise production.
Upgrade of ESP equipment to suit operating conditions:
Change in ESP housing metallurgy along with upgrade of tubing metallurgy.
Upgrade & standardisation of ESP ancillary equipment (penetrator systems, cable, etc.)
Upgrade of shaft material (higher shaft HP rating) for high HP motor ESP system
Availability of downhole data for monitoring and troubleshooting purposes.
Very stable power supply (very few unplanned shutdowns due power supply interruptions)
Layers of automated protection system put in place:
Drive underload and overload protection
Surface (wellhead) pressure (high/low) protection system. This would, for example, protect ESP from deadheading situation which could arise as a result of blocked/closed surface valve.
Automated trip on (high) motor temperature signal. This system protects ESP motors from being burnt (e.g., in no-flow conditions). It also provides additional protection for those lightly loaded motors that may not necessarily trip on current underload alone.
10
Maturing Wytch Farm Oilfield & Its Impact on ESP Completion Strategy
The drilling of barefoot multilateral wells as a way to maximise well production in WytchFarm started at around 1998.
As the field is maturing, the depletion strategy focus shifted to being able to achieve maximum drawdown (from all laterals) for maximum liquid (both oil & water) rate at surface.
The increase in water cut over time, along with the desire to keep development cost down, also led to the phasing out of smart completions (use of down hole flow control, flow meter, etc.) The relatively short run-life of the downhole instrumentations coupled with increasing ESP run-life also contributed to the phasing out of these downholeinstrumentations.
Effect of corrosion seen as a result of increase in water cut led to the introduction of Chrome tubing and the use of corrosion resistant alloys for ESP housing (ca. 2000).
The continued increase in water cut made it possible to move ESP setting depth up, particularly on the high PI wells without sacrificing production or without introducing excessive amount of free gas at pump intake, and generally reduce the power requirement (per bbl lifted)
Larger capacity and more efficient medium voltage drives (MVD) up to 2050 KVA (200A) were introduced in 2001 to enable high rate production from the prolific Sherwood wells
The installations of Dual-ESP completions, beginning in 2004, address two needs at Wytch Farm:
Extending well life-cycle (i.e., minimising the number of ESP replacement workovers)
Managing uncertainty in productivity in new wells
11
Summary of Current Wytch Farm ESPs
Number of active (ESP) wells: 31
Number of Dual-ESP installations: 11
ESP Nominal Flow Rate Range: 1,000 �– 28,000 BPD �– 4.00�” to 6.75�” nominal OD
Average liquid production from ESP wells: 8,700 BLPD
Oil production from ESPs represents over 85% of total field oil production at Wytch Farm
Motor HP Range: 84 to 1,400 HP (average: 550 HP) �– 4.56�” to 7.38�” nominal OD
Most ESPs set in 9-5/8�” casing, though some in 7�” liner, and some ESPs are shrouded.
ESP Setting depths: 600 m-MD to 4,600 m-MD (average 2,300 m-MD)
VSDs: 400 KVA to 2,050 KVA
12
Sustaining Production in High PI, High Water Cut Wells by Moving ESP Up �– M11 Example
1998:SPE 50586 discussed ESP installation in M11, set at a depth of ca. 8420 m-MD.
Well trajectory: 10,114 m-MD �–Longest well trajectory at the time
Pump size: 20,000 BPD with 900HP tandem motor
Production rate: 18,000 BPD at 30% water cut
VSD: 1,050 KVA
2009: M11 ESP setting depth at 3400 m-MD
Pump size: 28,000 BPD with 1400 HP tandem motor
Production rate: 26,500 BPD at 95% water cut.
VSD: 2,050 KVA
13
Sustaining Production in High PI, High Water Cut Wells by Simplifying Downhole Completion �– M15 Example
1999:
SPE 62951 discussed the use of Down Hole Flow Meter to measure production rate & DHFC to facilitate selective production from the two well laterals.
ESP setting depth: 5,150 m-MD (1452 m-TVD)
Pump size: 21,500 BPD with 1170HP (3x390HP) triple tandem motor
Initial production rate: 15,000 BPD at 50% water cut
VSD: 1,050 KVA
E S P
F S V
D i s c o n n e c tD i s c o n n e c tS h r o u dB l i n d
B a r e f o o t f o r t h e 8 1 / 2 ” h o l e
7 ” l i n e rC a s e d & p e r f e d
F l o w c o n t r o l v a l v e s
C o n t r o l l i n ef l a t p a c k
F l o w m e t e r
A t W o r k o v e r : a d d 4 t h P r e s s u r e g a u g e ? ( M u l t i p l e x e d )
4 t h c o n t r o l l i n e - p r e s s u r e m o n i t o r n o d i s c h a r g e
S u m p p a c k e rP h o e n i x m u l t i - s e n s o r F S V p a c k e r
2009:
Production opened to both laterals (simple packered ESP completion, with 5-1/2�” tubing)
M15 ESP setting depth: 3,800 m-MD (1323 m-TVD)
Pump size: 21,500 BPD with 1170 HP (3x390HP) triple tandem motor
Production rate: 18,000 BPD at 95% water cut.
VSD: 2,050 KVA
14
Application of Dual-ESP Completion �– Extending Well Life Cycle
Retrievable Packer
Primary system: 15000-BPD (89-stg) Nominal ESP with 900-HP motor
Secondary System: 15000-BPD (92-stg) Nominal ESP with 900-HP motor
2-7/8" bypass tubing
9-5/8" casing
In this example, remaining oil reserves is sufficient to sustain economic production rate for at least 15 years.
Liquid rate decline rate is very small (i.e., liquid rate expected to be more or less constant over time)
Present Liquid rate: 17,600 BLPD at 95% water cut
Pump setting depth: 1,900 m-MD (1295 m-TVD)
Pump Intake Pressure: 460 psia (4.2% estimated free gas volume at intake conditions)
Workover frequency to replace ESP is expected to reduce over the 15-year period
15
Application of Dual-ESP Completion �– Managing Productivity Uncertainty in New Wells
Gross Liquids Over Time
2007 2008 200905001000150020002500300035004000
Gro
ss L
iqui
d [b
pd]
Primary system: 6000-BPD Nominal ESP with 270-HP motor
Secondary System: 2600-BPD Nominal ESP with 150-HP motor
9-5/8" casing
Retrievable Packer
2-7/8" bypass tubing
7" liner hanger
When drilled, there was a lot of subsurface uncertainties (PI, SBHP, etc).
Initial rate estimates: 1,000-6,000 BPD Need 2 ESPs to cover the range.
Primary ESP (3,500-7,800) ran for almost one year before switching to smaller ESP.
Currently still running on the secondary ESP (1,600-3,200 BPD)
16
Closing Remarks
As Wytch Farm oilfield continues to mature (i.e., declining oil rate & increasing water cut) the need to operate ESP more efficiently becomes more important.
This involves the use of efficient ESP system, coupled with extended well life cycle (i.e., extending the ESP run-life & the application of dual-ESP, where applicable).
It is expected that the conventional, tubing-deployed ESP systems to continue to dominate the ESP population at Wytch Farm, especially for those wells producing from the prolific offshore Sherwood reservoir.
17
Acknowledgments
The presenter would like to thank the following companies for making this presentation possible:
BP Exploration & Operating Co Limited
Premier Oil Exploration Limited
Summit Petroleum Dorset
Maersk Oil North Sea UK Limited
Talisman North Sea Limited
18
Questions?