VUT 6.4.2006-2

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    Funkn bezpenost

    elektrickch pstrojsouvisejcch s bezpenost

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    Funkn bezpenost

    st celkov bezpenosti tkajc seEUC a systmu zen EUC zvisl nasprvnm fungovn E/E/EP systmsouvisejcch s bezpenost,systmech souvisejcch s bezpenostzaloench na jinch technickch

    principech a vnjch prostedcch prosnen rizika

    SN EN 61508-4

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    Mechanical Safety Action (if available)

    Plant Shut-down

    Wild Processparameter

    High Control level

    High Alarm level

    Time

    If Operator takes action

    Certain Process

    parameter value Low Control level

    Normal behavior

    DCS

    Functionality

    Process.

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    Mechanical Safety Action (if available)

    Plant Shut-down

    Wild Processparameter

    High Control level

    High Alarm level

    ESD controlled

    Trip level

    Time

    If Operator takes action

    Certain Process

    parameter value

    Safety Instrumented

    System Functionality

    Low Control level

    Normal behavior

    DCS

    Functionality

    Safety System.

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    Safety Issues for End User / Operators

    How do you demonstrate that your operations are safe?

    How do you demonstrate that your equipment is safe?

    How do you demonstrate that your safety and protectivesystems protect against your hazards?

    You can answer these questions by demonstrating compliancewith Industry Safety Standards

    IEC61508 - Functional safety ofelectrical/electronic/programmable electronic

    safety-related systems

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    What is IEC61508?

    An international standard relating to the Functional Safetyof electrical / electronic / programmable electronic safety

    related systems

    Mainly concerned with E/E/PE safety-related systemswhose failure could have an impact on the safety of

    persons and/or the environment

    Could also be used to specify any E/E/PE system usedfor the protection of equipment or product

    It is an industry best practice standard to enable you to

    reduce the risk of a hazardous event to a tolerable level

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    Technologies Concerned

    E Electrical electro-mechanical / relays / interlocks

    E Electronic

    solid state electronics

    PES Programmable Electronic Systems

    Programmable Logic Controllers(PLCs);

    Microprocessor based systems

    Distributed Control Systems Other computer based devices

    (smart sensors / transmitters /actuators)

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    Features

    Generic Standard

    Guidance on the use of E/E/PES

    Comprehensive approach involving concepts of Safety Lifecycle andincludes all elements of the protective system

    Risk-based approach leading to determination of Safety IntegrityLevels (S.I.Ls)

    Considers the entire Safety Critical Loop

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    Generic and Application Sector Standards

    IEC61511 :

    Process Sector

    Medical Sector

    IEC61513 :

    Nuclear Sector

    IEC62061 :

    Machinery Sector

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    Functional Safety

    Safety instrumented systemsfor the

    Process industry sector

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    IEC 61511

    FUNCTIONAL SAFETY: SAFETY

    INSTRUMENTED SYSTEMS FOR

    THE PROCESS INDUSTRYSECTOR

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    Industries

    Applies to a wide variety ofindustries across the processsector

    Including:

    Chemicals

    Oil refining

    Oil and gas production

    Pulp and paper

    Non-nuclear power

    generation

    Pharmaceuticals / Fine

    Chemicals

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    Scope

    Process (chemicals, oil & gas, paper, non-nuclear power generation)

    End-to-end safety instrumented system (SIS) -

    h/w, s/w, mgt. and human factors

    Full safety lifecycle - specification, design,integration, operation, maintenance

    Intended for integrators / users not for equipment designers / vendors

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    Structure

    IEC 61511 Structure

    Part 1Framework, definitions, system,hardware and software requirements.

    Part 2Guidelines for the application ofIEC 61511-1.

    Part 3Guidance for the determination ofsafety integrity levels.

    Normative

    Informative

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    IEC 61511

    TITLE - Functional Safety Safety Instrumented

    Systems for the Process Industry sector

    This international Standard gives requirements for

    the specification, design, installation, operation and

    maintenance of a safety instrumented system, so

    that it can be confidently entrusted to place and/or

    maintain the process in a safe state.

    This standard has been developed as a processsector implementation of IEC 61508.

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    Relationship IEC 61511 & IEC 61508

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    Relationship IEC 61511 & IEC 61508

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    Similarities (IEC 61508 - IEC 61511)

    Whole safety lifecycle Concept, Hazard & Risk Analysis and Design

    through operation & maintenance to eventualdecommissioning

    Safety requirements specification Safety integrity levels (SIL 1 to 4)

    End-to-end system

    (Sensor via Logic to Actuator)

    Hardware reliability analysis (PFD)

    Management of functional safety

    Architectural constraints (fault tolerance)

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    Key Differences IEC 61511 (IEC 61508)

    Terminology Process (EUC)

    Basic Process Control System (EUC Controlsystem)

    Safety Instrumented System (E/E/PE S-R-S) Safety Instrumented Function (Safety function)

    Presentation

    less rigorous than IEC 61508

    more guidance (especially in Parts 2 & 3)

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    Overall Installation

    & Commissioning

    11

    2

    External Risk

    ReductionFacilities

    Overall Scope Definition

    Realisation

    1 Concept

    3 Hazard Risk Analysis

    4 Overall Safety Requirements

    Safety Related

    Systems:E / E / PES

    12

    Realisation

    Overall Planning

    Safety Related

    Systems:

    Other

    Technology

    Realisation

    10

    Overall

    Installation &

    CommissioningPlanning

    Overall

    Validation

    Planning

    Overall

    Operation &

    MaintenancePlanning

    8

    9

    76

    Safety Requirements Allocation5

    Back to appropriate

    Overall Safety Lifecycle

    Phase

    15

    16 Decommissioning

    13 Overall Safety Validation

    Overall Operation & Maintenance14 Overall Modification & Retrofit

    Overall Safety Lifecycle in IEC 61508

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    IEC 61508 - ownership of phases

    PRE-DESIGN

    (Phases 1 to 5)

    OPERATION

    (Phases 14 to 16)

    DESIGN AND

    INSTALLATION

    (Phases 6 to 13)

    End user / operator

    End user / operator

    Engineering Contractors/ Equipment

    Supplier

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    Pre-Design : Phases 1 - 5

    1 : Concept

    2 : Overall Scope

    Definition

    3 : Hazard Risk

    Analysis

    4 : Overall Safety

    Requirements

    5 : Safety

    Requirements

    Allocation

    Can you demonstrate that

    you have identified all

    your hazards?

    Can you demonstrate that

    you are using adequateand correct methods of

    hazard protection?

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    Design & Implementation : Phases 6 - 13

    Overall Planning

    6 : Overall Operations and

    Maintenance Planning

    7: Overall Validation

    Planning

    8: Overall Installation &

    Commissioning Planning

    9 : Safety

    Related

    Systems :E/E/PES

    12 : Overall Installation &

    Commissioning

    13 : Overall

    Safety Validation

    10 : Safety

    Related

    Systems :

    OtherTechnology

    11 : External

    Risk

    ReductionFacilities

    How do you ensure

    competencies for all these

    activities?

    Can you demonstrate that you

    pass the necessary information

    into these activities?

    Can you demonstrate that all

    necessary information has been

    passed to you from these activities?

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    Operation : Phases 14 - 16

    14 : Overall

    Operations and

    Maintenance

    15 : OverallModification and

    Retrofit

    16 : Decommissioning

    Can you demonstrate thatyou maintain / test /

    analyse your protective

    systems correctly?

    Can you demonstratethat you are in control

    of your modification

    process?

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    Supply Chain

    IEC6

    1511

    IEC6

    150

    8

    Requirement

    SpecificationCommissioning

    and Use

    End User

    System DesignerIntegrator

    Sub-system

    Designer

    Component

    Manufacturer

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    Risk

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    What is Risk?

    The probable rate of occurrence of a hazardcausing harm

    AND

    the degree of severity of the harm

    Qualitatively - Words

    Quantitatively - Figures

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    Risk cannot be justified

    except in extraordinary

    circumstances

    Tolerable only if risk reduction

    is impracticable or if its cost is

    grossly disproportionate to the

    improvement gained

    Necessary to maintain

    assurance that risk

    remains at this level

    Unacceptable

    region

    Broadly acceptable

    region

    Negligible risk

    (No need for detailed working

    to demonstrate ALARP)

    The ALARP or

    Tolerability region

    As the risk is reduced the less,

    proportionately, it is necessary to

    spend to reduce it further. The

    concept of diminishing proportion

    is shown by the triangle.

    (Risk is undertaken only

    if a benefit is desired)

    Levels of Risk and ALARP(As Low As Reasonably Practicable)

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    Risk reduction: General concepts

    Increasingrisk

    Risk to meet

    Level of SafetyPlant Under

    Control risk

    Necessary minimum risk reduction

    Actual risk reduction

    Risk reduction achieved by all protective systems &

    External Risk Reduction Facilities

    Actual risk

    remaining

    Partial risk covered

    by E/E/PESprotective systems

    Partial risk covered

    by Other Technologysafety-related systems

    Partial risk covered

    by External Risk

    Reduction Facilities

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    SENSOR ACTUATORPROGRAMMABLEELECTRONICS

    Equipment(plant)

    UnderControl (EUC)

    PE

    SRS

    Extent of Safety Related System

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    What is a Safety Related System (SRS) ?

    Any system thatimplements safety

    functions necessary to

    achieve a safe state for

    the Equipment UnderControl, or to maintain itin a safe state.

    Examples

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    Hazard Identification and Risk Analysis

    A typical Methodology for Hazard Identification and Risk

    Analysis

    (by the end user)

    Hazard studies and HAZOPs Evaluate possible consequences Establish tolerable frequencies vs ALARP Build event chain Estimate demand rates Define protection required

    Specify required SIL

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    Failure categories in IEC 61508

    A = Random HardwareFailuresOR

    B = Systematic Failures

    specification;

    systematic hardware;

    software;

    maintenance;

    all failures that are not random

    AB

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    Safety Integrity Level SIL

    SAFETY

    INTEGRITY

    LEVEL

    (SIL)

    LOW DEMAND MODEOF OPERATION

    (Probability of failure

    to perform its

    designed function on

    demand)

    CONTINUOUS/HIGHDEMAND MODE OF

    OPERATION

    (Probability of one

    dangerous failure per

    hour)

    4 >= 10-5

    up to < 10-4

    >= 10-9

    up to < 10-8

    h-1

    3 >= 10-4

    up to < 10-3

    >= 10-8

    up to < 10-7

    h-1

    2 >= 10-3

    up to < 10-2

    >= 10-7

    up to < 10-6

    h-1

    1 >= 10-2

    up to < 10-1

    >= 10-6

    up to < 10-5

    h-1

    PFD PFH

    Probability ofFailure on

    Demand

    Probability ofFailure per

    Hour

    Ri k d D t i ti f S f t I t it

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    Risk and Determination of Safety Integrity

    Levels

    Basic

    Design

    Unacceptable

    No

    ProtectionIncrea

    sing

    Severity

    Increasing Likelihood

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    Risk Reduction Requirements

    Safety IntegrityLevel

    Risk Reduction

    1 10-100

    2 100 1,000

    3 1,000 10,000

    4 10,000 100,000

    Reliability Failure Rate and Availability at each level

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    Reliability, Failure Rate and Availability at each level

    SIL 1

    SIL 2

    SIL 3

    SIL 4

    Reliability Probability of

    failure on

    demand

    Trip Unavailable

    (per year)

    90% - 99% 0.1 to 0.01 876 to 87.6hrs

    99% - 99.9% 0.01 to 0.001 87.6 to 8.76hrs

    99.9% -

    99.99%

    0.001 to 0.0001 8.76hrs to 52.6

    mins

    99.99% -

    99.999

    %

    0.0001 to 0.00001 52.6 mins to 5.3

    mins

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    Protective System Technology

    Standard components, single channel or twinnon-diverse channelsSIL 1

    Standard components, 1 out of 2 or 2 out of 3,

    possible need for some diversity. Allowance forcommon-cause failures needed

    SIL 2

    Multiple channel with diversity on sensing and

    actuation. Common-cause failures a major

    consideration. Should rarely be required in

    Process Industry

    SIL 3

    Specialist design. Should never be required in

    the Process IndustrySIL 4

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    Determined to achieve the correct SIL level...

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    Various methods available:

    Qualitative risk graph Calibrated risk graph (methodology only

    not definitive)

    Layer Of Protection Analysis (LOPA)

    Hazardous event severity Matrix Quantified Risk Analysis (QRA)

    Which one to use? Develop your own?

    SIL assessment

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    Calculation of PFDAVG

    35% of PFDAvg SE 15% of PFDAvg LS50% of PFDAvg FE

    Distribution of the Failure Measures

    35 % Sensors + 15 % Logic solver + 50 % Final elements

    PFD fi f HIMA t l

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    35 % 15% 50%

    PFD-figures for a HIMA system, example

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    RC/AK according DIN V VDE 19250

    SIL according IEC 61508

    consequence

    risk

    parameter

    minorinjury

    no influence

    to the environment

    possibility

    of avoiding

    hazardousevents

    frequency

    & exposure

    time

    probability of the

    unwanted occurrence

    very slightrelativelyhigh slight

    dead of 1 personrare

    frequent

    periodic influence

    to the environment

    dead to

    several people

    permanent influence

    to the environment

    disaster

    rare

    frequent

    possible

    not

    possible

    possible

    not

    possible

    requirement

    classes

    RC or AK

    Safety Integrity

    Levels (SIL)

    IEC 61508

    Risk Graph acc. DIN V VDE 19250

    C f l f i IEC 61511

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    Concept of layers of protection acc. IEC 61511

    PROCESS

    CONTROL and MONITORING

    Basic process control systems

    Monitoring systems (process alarms)

    Operator supervision

    PREVENTION

    Mechanical protection systemProcess alarms with operator corrective action

    Safety instrumented control systems

    Safety instrumented prevention systems

    MITIGATION

    Mechanical mitigation systems

    Safety instrumented control systems

    Operator supervision

    PLANT EMERGENCY RESPONSE

    Evacuation procedures

    COMMUNITY EMERGENCY RESPONSE

    Emergency broadcastingLOPA

    Hazardous event severity Matrix

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    Hazardous event severity Matrix

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    Funkn bezpenost

    st celkov bezpenosti tkajc seEUC a systmu zen EUC zvisl nasprvnm fungovn E/E/EP systm

    souvisejcch s bezpenost,systmech souvisejcch s bezpenostzaloench na jinch technickch

    principech a vnjch prostedcch prosnen rizika