life cycle asset management system

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Page 1 1 Page 1 Aberdeen May 30 th , 2013 Using design data to reduce risks during operations By Dr. Bruno GERARD, Founder and President OXAND group Life Cycle Asset Management System

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Page 1: Life Cycle Asset Management System

Page 1 1 Page 1

Aberdeen – May 30th, 2013

Using design data to reduce risks during

operations

By Dr. Bruno GERARD,

Founder and President OXAND group

Life Cycle Asset Management System

Page 2: Life Cycle Asset Management System

Page 2

Outline

1. Context and objectives

2. Methodology outline

3. Case study

4. Conclusions

Page 3: Life Cycle Asset Management System

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WHO IS OXAND ?

• INDEPENDENT INTERNATIONAL CONSULTANCY FIRM

SPECIALIZED IN ASSET, AGEING & RISK MANAGEMENT

• FOCUS ON LIFE CYCLE OPTIMISATION OF HIGH RISK CAPITAL

INTENSIVE ASSETS

Spin-off EDF in 2002

TRANSPORT (Railways, Ports…) ENERGY (Oil & Gas, Nuclear…)

•> £ 1000bn OF CAPEX CAPITALIZED IN SIMEOTM

• > 130 PERMANENT CONSULTANTS, > £ 15m

Page 4: Life Cycle Asset Management System

Page 4

OXAND Oil & Gas Business Line

Page 5: Life Cycle Asset Management System

Page 5

OXAND

Renewables

Managing Risks How high is the residual risk ?

Controlling Costs Capital (CAPEX)

Maintenance(OPEX)

Cost of risks

Optimising Asset Performance Availability (Kd), Safety

From design to

deconstruction

PASS 55 (ISO 55000), ISO 31000, ISO 15288

Proprietary Database

and Software SIMEO

Page 6: Life Cycle Asset Management System

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Asset Inventory

Maintenance policy

Historical data

strategy

Client’s data Deliverables

LIBRAIRIES

SIMEOTM SIMULATOR

ALGORITHMS

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Projects are getting more and more complex:

deeper wells, greater water depth, “extreme” operating

conditions

Requirements for greater analysis and

control of RISKS, intensive and better use of

Data

During the design phase, new projects must

integrate new solutions for life extension and

deconstruction

1. Context : a quick change in the approach of developing new assets

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1. Context : Minimize Technological Risks

Prospection /

construction

operations

RISKS

TIME

Gas leakage

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1. Context : Minimize Technological Risks during design

Prospection /

construction

operations

RISKS

TIME

Offer a long term vision for earlier decisions minimizing

life cycle risks

?

Main factor: initial

conditions at the start-

up of operations (as

built)

Balance between CAPEX / OPEX

Page 10: Life Cycle Asset Management System

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WHERE ARE THE MAIN TECHNOLOGICAL RISKS

Sub surface

Sub sea

Surface

facilities

•High number of

systems and

components

•Low uncertainties

•Easy access

•Low number of

systems and

components

•Medium level

uncertainties

•Costly access

•Low number of

systems and

components

•High uncertainties

•Very Costly access

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A full framework for optimising design of assets and

operations processes to maintain a high level of

performance :

Maximize availibility, safety

Minimize costs linked to unexpected events

A full framework for maintaining level of risks

acceptable during life cycle

Tools to support the framework and processes

OBJECTIVES

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Life time

extension

Risk-based integrity

review

Design Construction Operation P&A

Initial condition

evaluation « point

zero »

Periodic Risk-based

integrity review

Intervention

Optimisation Studies

Some Key studies to optimize long

term asset performance

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Global risk management process

QRA due date

or early update

required?

WI Quantitative

Risk Assessment

Scheduled review of

QRA & Well screening

Well classification by

severity potential

no

yes

Well classification

enabling graded approach and prioritization

Quantitative &

predictive decision support for Asset & Safety Management

Control of mitigation

plans & risk monitoring of the well

portfolio

BenefitsProcess

1. C

lassif

y A

ssets

2. A

ssess ris

ks

3. C

on

trol &

up

date

Minor Intermediate Major

Nu

mb

er

of

we

lls

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Overview of the Well Integrity QRA Methodology

Leak rate modelling

WI QRA

WI Management

System Risk identification

Risk identification

Risk estimation

Risk estimation and assessment

Risk evaluation and management

Qualitative assessment Support studies Quantitative assessment WI Management

System characterisation Identification of failure modes and causes Assessment of prevention/mitigation controls

Estimation of potential leakage rates Understanding of well behaviour Indication of potential threats to WI (corrosion...)

Quantification of risks (likelihood, severity) Ability to predict varying risk levels over time Results to cover various scenarios

Risk-informed decision-making Optimisation of operational procedures/practices Ensure ability to produce while managing risks

FMEA

Thermo-mecha analysis

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Methodology Workflow

Data collection

and analysis

Mesh and

boundaries

definitions

Scenarios:

base case +

sensitivity

Conclusions

and

recommendations

Section across 2 annuli

Overburden 1

Aquifer 1

Overburden 2

Overburden 3

Aquifer 2

Caprock

Reservoir

Cement logs

Drilling reports

Geological profiles

Data collection

Kzone_8

Kdeg

Portlanditedissolution

Kzone_7

Aggressiveagent concentration

Dynamic modeling

Risk mapping

(SSci, PSci)

Static modeling (T0)

Formations

Fluide des formations

CasingsGaines

Cavités_FC

Bouchons(F 1)

(F 3)

(F 4)

(F 2)

Risk =

Probability x SeverityK5*K4*K3

K5*K4

K3*K1

K1

K4*K3

K4

K3*K2

K2

K5*K1*K3*K2

K5*K1*K2

K5*K2

K5*K3*K2

K3

0,E+00 5,E-08 1,E-07 2,E-07 2,E-07 3,E-07

Relative influence

Consequence grid

CO2 leakage mass

(T0 + x years) for Scenario Sci

X

Failure scenarios selection

Recommandations

Probability for

Scenario i(S)Sci

(P)Sci

Concerns

Objectives

Key performance

indicators

Project context

Cement logs

Drilling reports

Geological profiles

Data collection

Kzone_8

Kdeg

Portlanditedissolution

Kzone_7

Aggressiveagent concentration

Kzone_7

Aggressiveagent concentration

Dynamic modeling

Risk mapping

(SSci, PSci)

Static modeling (T0)

Formations

Fluide des formations

CasingsGaines

Cavités_FC

Bouchons(F 1)

(F 3)

(F 4)

(F 2)

Formations

Fluide des formations

CasingsGaines

Cavités_FC

Bouchons(F 1)

(F 3)

(F 4)

(F 2)

Risk =

Probability x SeverityK5*K4*K3

K5*K4

K3*K1

K1

K4*K3

K4

K3*K2

K2

K5*K1*K3*K2

K5*K1*K2

K5*K2

K5*K3*K2

K3

0,E+00 5,E-08 1,E-07 2,E-07 2,E-07 3,E-07

Relative influence

K5*K4*K3

K5*K4

K3*K1

K1

K4*K3

K4

K3*K2

K2

K5*K1*K3*K2

K5*K1*K2

K5*K2

K5*K3*K2

K3

0,E+00 5,E-08 1,E-07 2,E-07 2,E-07 3,E-07

Relative influence

Consequence grid

CO2 leakage mass

(T0 + x years) for Scenario Sci

CO2 leakage mass

(T0 + x years) for Scenario Sci

X

Failure scenarios selection

Recommandations

Probability for

Scenario i(S)Sci

(P)Sci

Concerns

Objectives

Key performance

indicators

Project context

Iterative process

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Context:

• Offshore project

• Pre-FEED phase

Needs:

• Check if proposed cement will contribute to

avoid leakage into the geology or

atmosphere

• Propose recommendations regarding

cement properties

• Reassure project partners

• Demonstrate authorities efficiency of well

design

Business case Context and needs

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Providing a framework for :

• Understanding threats to well integrity

• Identifying component failure modes

• Characterising failure scenarios

• Quantifying likelihood of failure

• Assessing controls in place to prevent failure / mitigate consequences

Library of failure modes and causes:

• Industry & Oxand experience

• Expert opinion

• Industry research projects

Failure Modes and Effects Analysis Overview

Qualitative assessment

Risk identification

Qualitative Approach of QRA

© Oxand UK Ltd 2013

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Leaking Casing

Loss of leak tightness

Mechanical failure

Fatigue

Degradation of Joints

Reduced Mechanical Resistance

Corrosion

Degradation of Casing

Erosion

Degraded cement

Presence of H2S

Bacterial activity

Sulphide stress cracking

Acids and brines

Completion fluids

Geological Fluids

Different Grades of steel used

Velocity of fluids

Production of fine particles

Inappropriate flow coupling (missing)

Aggressive Fluids

Oxygen intrusion

Ineffective protection of casing

by cement

Galvanic corrosion

Presence of H2S

Corrosion

Erosion

Degraded cement

Bacterial activity

Acids and brines

Completion fluids

Geological Fluids

Different Grades of steel used

Velocity of fluids

Production of fine particles

Inappropriate flow coupling (missing)

Aggressive Fluids

Oxygen intrusion

Ineffective protection of casing

by cement

Galvanic corrosion

Presence of H2S

Thermo-mechanical

stresses

Variation in temperature

Variation in pressure

Geological stresses

Variation of lithostatic pressure

Well Status (In production or

Shut-in)

Variation of Geological fluids

pressure

Well Status (In production or

Shut-in)

Operational Actions

Geological Temperature

Seismic events

Subsidence / dilatation

Faults and fractures

Variation in temperature

Variation in pressure

Variation of lithostatic pressure

Well Status (In production or

Shut-in)

Variation of Geological fluids

pressure

Well Status (In production or

Shut-in)

Operational Actions

Geological Temperature

Sea Water 1, 3

Cathodic Action 1

Cathodic Action 1Electric Current in

seabed 1

Electric Current in seabed 1

Sea water 1, 3

In situ stresses 2

Geological fluids pressure 2

1. Only valid for Surface Casing2. Not valid for Surface Casing 3. Only valid for Mud Line Suspension

A.b

, A.c

, B.b

, C.a

, D

.c, E

.dA

.b, A

.c, B

.b, C

.a,

D.c

, E.d

A.b

, A.c

, B.b

, C.a

, D

.c, E

.d

A.b

, B.b

, C.a

, D.a

A.b

, B.b

, C.a

, D.a

A.b

, A.c

, B.b

, C.a

, D

.c, E

.d

A.b

, A.c

, B.b

, C.a

, D

.a, D

.c, E

.d

Presence of CO2

Presence of CO2

Hydrogen embrittlement

Immediate consequence

Failure causes / factors

Controls for prevention / mitigation

Failure mode

• Design criteria • Manufacturing/procurement specs • Installation practices • Operational procedures • Maintenance doctrines • Data gathering/analysis • Etc...

Qualitative assessment

Risk identification

Failure Modes and Effects Analysis Failure Mode Diagrams

SIMEOTM Well-Base Library

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Wellhead

Packer

Tubing (Inside)

Annulus 2Casing

Cement

Seal Seal Tubing Hanger

ValveValve Valve

X-mas Tree

Annulus Casing

CementAnnulus 3

Casing Cement

An

nu

lus

C

asin

g

Annulus 3

An

nu

lus

3 C

asin

g

Annulus 2

An

nu

lus

2 C

asin

g

Annulus 1 Casing

Cement

An

nu

lus

1 C

asin

g Annulus 1

Liner Cement

Tub

ing

Lin

er

Packer

SCSSV

Formation 1Gas Bearing

Formation 2

Formation 3

Formation 5Gas Bearing

Formation 6

Formation 6

ProductionAtmosphere

Sea Bed

Formation 4Gas Bearing

Perforations

Leakage Path

Source/Sink

Component

Qualitative assessment

Risk identification

Failure Modes and Effects Analysis Leakage Pathway Diagrams

Map of potential leakage pathways from source to sink (including atmosphere)

NOTE: Generic well and geology represented

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Failure Mode

Qualitative assessment

Risk identification

Failure Modes and Effects Analysis Leakage Pathway Diagrams

Combined with FMDs, provides overall picture of threats to well integrity

NOTE: Generic well and geology represented

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Supporting Studies Some examples

Support Studies

Risk identification & estimation

Thermo-mechanical modelling

• Indications of likelihood of failures

Leakage rate estimation

• Quantitative estimation of leakage rates

(indication of severity)

Calculations of annulus pressures and

inventories in reduced integrity

conditions V=cst

Vg(t1)

Vw(t1)

fwVw(t1)

fgVg(t1) Vg(t2)

Vw(t2)

mg(t1)

mg(t2) = mg(t1)+ Δmg

mw(t1)mw(t1)=mw(t2)

pt1 t2

© Oxand UK Ltd 2013

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Potential failure and leakage paths:

• Casing deformation

• Micro-annuli opening at interfaces

potential leakage

• Cement cracking

Parameters

• Properties of geology

• Evolution of cement properties over

time (aging)

• Initial casing thickness

• Orthotropy of geological stresses

• Evolution of P&T over time

Business case

P T

Short

shut-in

Long

shut-in

P&T profiles considered

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Quantification of risk:

• Scenarios are classified in

risk grids

Prediction of risk levels

over time:

• risk levels due to ageing

components/materials

Quantitative Risk Assessment Model Results

Initiating Event: A live

Ann. A valve unrestricted

flow

Production Casing Failure

Production Casing Seal

Failure

Annulus AET 1,1

Ann. B valve unrestricted

flow

Intermediate Casing Failure

Intermediate Casing Seal

Failure

Ann. C valve unrestricted

flow

Surface Casing Failure

Annulus D (Cemented)

Failure

Leak into A, Bleed off

Consequence

Leak from A to CC to atmosphere

Annulus B Annulus CAnn. B valve blocked, no

AMS

Ann. C valve blocked, no

AMS

Leak from A to C

Conductor Casing Failure

Annulus D

Leak from A to DD to atmosphere

Ann. A valve blocked, no

AMS

1,1,1

1,1,3

1,1,4

1,1,5

1,1,7

1,1,2

1,1,8

1,1,9

1,1,10

1,1,12

1,1,17

1,1,18

1,1,19

1,1,20

1,1,22

1,1,23

1,1,25

1,1,26

1,1,28

1,1,24

1,1,35

1,1,36

1,1,38

1,1,34

1,1,43

1,1,6

1,1,11

1,1,21

1,1,27

1,1,37

1,1,44

1,1,29

1,1,30

1,1,31

1,1,33

1,1,32

1,1,39

1,1,40

1,1,41

1,1,42

1,1,45

1,1,46

1,1,47

1,1,49

1,1,50

1,1,51

1,1,52

1,1,54

1,1,56

1,1,57

1,1,59

1,1,60

1,1,61

1,1,62

1,1,64

1,1,55

1,1,65

1,1,67

1,1,68

1,1,69

1,1,71

1,1,66

1,1,78

1,1,79

1,1,77

1,1,48

1,1,53

1,1,58

1,1,63

1,1,70

1,1,80

1,1,72

1,1,73

1,1,74

1,1,76

1,1,75

1,1,14

1,1,15

1,1,13

1,1,16

Leak from A to D

Leak from A to D

Leak from A to DD to atmosphere

Leak from A to C

Leak from A to D

Leak from A to D

Leak from A to CC to atmosphere

Leak from A to C

Leak from A to DD to atmosphere

Leak from A to D

Leak from A to D

Leak from A to DD to atmosphereLeak from A to BB to atmosphere

Leak from A to C

Leak from A to D

Leak from A to D

Leak from A to CC to atmosphere

Leak from A to B

Leak from A to C

Leak from A to DD to atmosphere

Leak from A to D

Leak from A to D

Leak from A to DD to atmosphere

Leak from A to C

Leak from A to D

Leak from A to D

Leak from A to CC to atmosphere

Leak from A to C

Leak from A to DD to atmosphere

Leak from A to D

Leak from A to D

Leak from A to DD to atmosphere

Leak from A to C

Leak from A to D

Leak from A to D

Leak from A to CC to atmosphere

Leak from A to B

Leak from A to C

Leak from A to DD to atmosphere

Leak from A to D

Leak from A to D

Leak from A to DD to atmosphere

Leak from A to C

Leak from A to D

Leak from A to D

Leak from A to CC to atmosphere

Leak from A to C

Leak from A to DD to atmosphere

Leak from A to D

Leak from A to D

Leak from A to DD to atmosphereLeak from A to BB to atmosphere

Leak from A to C

Leak from A to D

Leak from A to D

Leak from A to CC to atmosphere

Leak from A to B

Leak from A to C

Leak from A to DD to atmosphere

Leak from A to D

Leak from A to D

Leak from A to DD to atmosphere

Leak from A to C

Leak from A to D

Leak from A to D

Leak from A to CC to atmosphere

Leak from A to C

Leak from A to DD to atmosphere

Leak from A to D

Leak from A to D

Leak from A to DD to atmosphere

Leak from A to Atmosphere

Leak RateKg/s

Probability/year

Leak from A to C

Leak from A to D

Leak from A to D

Leak from A to B

Annulus A Live, A-Bleed off functioning

Result of Middle ingress leak rate at year 1

Quantitative Assessment

Risk estimation & assessment

© Oxand UK Ltd 2013

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A FULL RISK MANAGEMENT SYSTEM FROM DESIGN TO END OF LIFE

SIMEOTM

3- Integrate Risk mitigation

actions in project planning

1 – Predictive Life Cycle Risk assessment

2 - Corrective actions

4 – Risk Informed Decision System

5- Control and quantifiy

Costs/Benefits

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A risk-informed decision approach provides benefits

for decision making at all stages of the lifecycle

Design

Determining optimum well design, component specs...

Operations

Developing operational risk management plans, maintenance strategies...

Abandonment

Planning abandonment to ensure safety, minimise disruption to production...

... when deployed as part of a successful overall risk management

process

Conclusions

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