SPE Distinguished Lecturer Program

11/18/2008 SPE Distinguished Lecturer Program The SPE Distinguished Lecturer Program is funded principally through a grant from the SPE Foundation. T...
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11/18/2008

SPE Distinguished Lecturer Program The SPE Distinguished Lecturer Program is funded principally through a grant from the SPE Foundation. The society gratefully acknowledges the companies that support this program by allowing their professionals to participate as lecturers. Special thanks to the American Institute of g Metallurgical, g and Petroleum Mining, Engineers (AIME) for its contribution to the program. Society of Petroleum Engineers Distinguished Lecturer Program www.spe.org/dl

Pitfalls to Avoid in Assessing A ifi i l Lift Artificial Lif Run-Life R Lif Performance P f Francisco Alhanati C-FER Technologies

Society of Petroleum Engineers Distinguished Lecturer Program www.spe.org/dl

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Impact on Economics • Artificial Lift Run Run-Life Life Performance directly affects: – Work over frequency – Work over costs – Production losses

Impact of ESP Run-Life

20 Wells average oil production per well: 1,000 bpd average intervention cost: 150 k US$ average workover & waiting time: 60 days oil price: US$60/bbl

Overall Workover Costs $250

30% 25% 20%

$150

15% $100

% revenue

milllions / year

$200

10% $50

5% 0%

$0 0

120

240

360

480

600

720

840

960

Average Runtime (days)

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AL Run-Life Performance is important • Key Performance Indicator (KPI) – effects of changes in operational conditions, equipment selection and operational practices – used in many alliance contracts between operators and vendors

Assessing AL RL Performance • Not as simple as it may sound – Several measures used throughout the industry – Trends are often misleading

• Issues must be understood, so that – Pitfalls can be avoided – Proper RL measures can be selected

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Run-Life and Runtime • For many installations, installations Run-Life Run Life is not known, only Runtime – Systems that are still running – Systems that were pulled for other reasons than system failure

Censoring • The data is said to be “censored” censored • One can only hope to obtain estimates of average Run-Life • Based on all the systems Runtime

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Run-Life Estimates • Average Runtime can be calculated for: – – – –

All systems y (pulled or still running) (p g) Running systems only Pulled systems only Pulled and Failed systems only

• All these averages can be calculated based on p times different exposure – Time-in-Hole, Total Runtime, Actual Runtime

• Over different (calendar) periods of time – Last two years, last five years, etc.

Run-Life Estimates • Average Runtime of pulled systems: • Includes failure of other “systems”: tubing, sand control control, etc etc. • It is a reasonable indicator of the overall production system reliability • But not of the AL system reliability

• Average g Runtime of failed systems: y • Also affected by failures of other “systems” • Not a good indicator of the AL system reliability either

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Run-Life Estimates • At a certain point of time, all you can have is a statistical “best best estimate” estimate , or “expected value” of average Run-Life or Mean Time to Failure (MTTF)

Run-Life Estimates • Average Failure Rate: – Number of failures per well over a period of time

• MTTF estimate: – the inverse of the average failure rate – ratio of the total time in operation (for all systems pulled or still running) to the systems, number of failures: MTTF =

∑T

pulled

+ ∑ T running

# failed

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What is a Failure? • Failure: – The termination of the ability of an item to perform its required functions

ISO 14224: Petroleum and Natural Gas Industries: Collection and Exchange of Reliability and Maintenance Data for Equipment

Common Pitfalls • • • •

Early Failures versus Frequent Failures Improvement versus Aging Component Reliability and System RL Failure Mechanism versus Failure Cause

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ESP-RIFTS Data Locations of Fields

BP

Nexen

Shell

Chevron

PDVSA

Shell PDO

ConocoPhillips

Petrobras

TNK-BP

EnCana

Repsol YPF

TOTAL

ExxonMobil

Rosneft

Kuwait Oil Company

Saudi Aramco

ESP-RIFTS: ESP Reliability and Failure Tracking System

Common Pitfalls • • • •

Early Failures versus Frequent Failures Improvement versus Aging Component Reliability and System RL Failure Mechanism versus Failure Cause

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Average Runtime of Failed Ave erage Run Time (days)

What is the least reliable component? Is it the gas separator?

900 800 700 600 500 400 300 200 100 0 Cable

Downhole Sensors

Gas Separator

Motor

Pump

Pump Intake

Seal

Pump Intake

Seal

ESP Component

Which is more reliable? li bl ? The motor or the cable?

Failure Rate (x10-6 6 / day)

Failure Rate 400 350 300 250 200 150 100 50 0 ESP Cable

Downhole Sensors

Gas Separator

Motor

Pump

ESP Component

Common Pitfalls • • • •

Early Failures versus Frequent Failures Improvement versus Aging Component Reliability and System RL Failure Mechanism versus Failure Cause

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Is the system reliability improving? Or are the systems just aging? 40 4.0

MTTF (3 yr Window) Wi d )

3.5

Average Runtime of Running

Run-Life Estimate R

3.0

2.5

2.0

15 1.5

1.0

0.5

0.0 1997

1998

1999

2000

2001

2002

2003

Calendar Year

Common Pitfalls • • • •

Early Failures versus Frequent Failures Improvement versus Aging Component Reliability and System RL Failure Mechanism versus Failure Cause

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Survival Curve

Is the equipment from both manufacturers equally reliable?

100 90 80

Manufacturer A Manufacturer B

70

50 40 30 20 10 0 0

12

24

36

48

60

72

84

96

time in operation (months)

Failure Rate 400

Failure Rate (x10-66 / day)

S (t)

60

350

Manufacturer A

300

Manufacturer B

250 200 150 100 50 0 Cable

Gas Separator

Motor

Pump

Pump Intake

Seal

ESP Component

Common Pitfalls • • • •

Early Failures versus Frequent Failures Improvement versus Aging Component Reliability and System RL Failure Mechanism versus Failure Cause

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Failure Classifications • Reason for Pull – Suspected system failure or any other reason – e.g.: stimulation, re-completion

• Primary Failed Item and Descriptor – Component (or part) in which the failure likely initiated, and likely mechanism – Based on observations during pull or teardown – e.g. g motor burn

• Failure Cause: – The circumstances during design, manufacture or use which have led to a failure – e.g. improper assembly during installation

Failure Analysis Process System Failure - Reason for Pull defined: e.g., No flow to surface

System Pull and Teardown - Items and Descriptors defined: e.g., Shorted MLE

’Failure Investigation - Cause defined: e.g., Installation; Improper Assembly

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Do I have a manufacturing (QC) problem? Or do I have an operational problem?

Num mber of Failures

Number of Failures by Failure Cause 120

Completion

100

Installation Manufacturing

80

Normal or Expected Wear-and-Tear

60

Operation

40

Other

20

Storage and Transportation System Design / Selection

0 Cable

Gas Separator

Motor

Pump

Pump Intake

Seal

ESP Component

Conclusions • There are several measures used throughout the industry • One needs to understand their meaning to properly interpret the trends • Best picture of the situation likely requires looking at several measures • Improvement I t requires i thorough th h investigation of the failure causes • Be aware of the pitfalls !

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Acknowledgement • ESP ESP-RIFTS RIFTS JIP Participants: – BP – Chevron – ConocoPhillips – EnCana – ExxonMobil – KOC – Nexen

- Petrobras - Repsol-YPF - Rosneft - Shell - StatoilHydro - TNK-BP - Total

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