Chapter 11 Risk Assessment

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    Cha ter 11. RISK ASSESSMENT

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    IntroductionRisk Assessment

    Incident Identification Consequence analysis

    How accident occurs Expected damage

    (Analysis of probability) (loss of life, damage, days outage)

    This chapter discusses

    1. Review probability mathematics

    2. How failure probability of individual components

    contribute to the failure of the entire process.3. Describe two probabilistic methods

    Event tree

    Fault tree

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    Probability Theory

    Failure in a process occurs as a result of interaction ofthe individual components

    The overall probability depends on nature of this

    interaction. Average failure rate as faults/time, On average the

    component fails after certain period of time .

    The robabilit that the com onent will NOT fail durin

    the time interval (0,t) is given by poisson distribution

    As t

    then R(t) goes to 0 and high means less R(t). The complement of the reliability is called probability

    and is given by

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    Probability Theory

    Failure density function : derivative of failure probability

    The failure density function is used to determine the

    probability P at least one failure in the time period t0 to t1

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    Probability Theory

    MTBF : The time interval between two failures of thecomponent is called the mean time between failures (MTBF)

    and is given by

    Many component exhibit bathtub failure rate

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    Probability Theory

    Interaction between Process units

    Parallel: Process failure requires simultaneous failure of a

    number of components in parallel. Failure probabilities

    for the individual components must be multiplied(Parallel Probability)

    n is the total number of components and

    Piis the failure probability of eachcomponent.

    Total reliability for parallel units

    Riis the reliability of an individual process

    component

    Parallel represented by logical AND gate function.

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    Probability Theory

    Interaction between Process unitsSeries:

    Failure of any single component in the series of

    components will result in failure of the process. Represented by logical OR function.

    Overall process reliability is found by multiplying the

    .

    The overall failure probability

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    Probability Theory

    Interaction between Process unitsSeries:

    For system composed of 2 components A and B

    If the failure probabilities are small , then the product term

    can be neglected. For this special case

    ompensa es or coun ng

    the overlapping cases twice

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    Revealed and Unrevealed Failure

    Revealed Failure:Failures that are immediately obvious. e.g Flat tire on a car

    0+ r =MTBF

    The time that the component is operational is called theperiod of operation and is denoted by 0. After a failure

    occurs, a period of time, called the period of inactivity or

    downtime (r), is required to repair the component.

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    Revealed Failure

    Revealed Failure:For revealed failures the period of inactivity or downtime

    for a particular component is computed by averaging the

    inactive period for a number of failures

    Where, n is the number of times the failure or inactivityoccurred and r is the period for repair for a particular

    failure.

    Similarly, the time before failure or period of operation isgiven by

    So,

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    Revealed Failure

    AvailabilityProbability that component found functioning

    Unavailability

    probability that the component or process is found

    not functioning.

    For revealed failures,

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    Unrevealed Failure

    For unrevealed failures if, u is the average period of unavailabilityduring the inspection interval and if i is the inspection interval,

    then

    The average period of unavailability is computed from the failure

    probability

    For unrevealed failures

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    Probability of coincidence

    The dangerous process episode occurs when a process

    upset occurs and the emergency system is unavailable.

    This requires coincidence of events.

    Assume that a dangerous process episode occurs Pd timesinterval Ti. The frequency of this episode is given by

    For an emergency system with unavailability U, a

    dangerous situation will occur when the process episode

    occurs and the emergency system is unavailable. This isevery pdU episodes.

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    Probability of coincidence

    The mean time between coincidences (MTBC) is the reciprocal of

    the average frequency of dangerous coincidences:

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    EVENT TREE ANALYSIS

    Event tree analysis evaluates potential accident

    outcomes that might result following an equipmentfailure or process upset known as an initiating event. It

    is a forward-thinking process, i.e. the analyst begins

    with an initiating event and develops the followingsequences of events that describes potential accidents,

    accounting for both the successes and failures of the

    safety functions as the accident progresses.

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    Guidelines

    1. Identify an initiating event of interest.

    2. Identify the safety functions designed to

    deal with the initiating event.

    3. Construct the event tree.

    4. Describe the resulting accident event

    sequences.

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    Construction of the Event Tree Enter the initiating event on the left hand side

    List the functional responses chronologically

    Decide whether or not the success-failure ofthe function can or does effect the course of

    17

    If the answer is yes, the event tree is branchedto distinguish between success and failure ofthe function; success always branches

    upword, failure downward. If the systemfunction has no effect, the tree does notbranch, but proceeds to the next systemfunction (to the right)

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    Step 1 Identify the initiating event

    system or equipment failure

    human error

    process upset

    [Example]

    Loss of Cooling Water

    to an Oxidation Reactor

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    Step 2 Identify the Safety Functions

    Designed to Deal with the Initiating

    Event

    Safety system that automatically respond tothe initiating event.

    initiating event occurs and operator actionsdesigned to be performed in response toalarms or required by procedures.

    Barriers or Containment methods that areintended to limit the effects of the initiatingevent.

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    Example

    Oxidation reactor high temp. Alarm alerts

    operator at temp T1. Operator reestablish cooling water flow to the

    oxidation reactor.

    Automatic shutdown system stops reaction attemp. T2. T2 > T1

    These safety functions are listed in the order inwhich they are intended to occur.

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    Step 3: Construct the Event Tree

    a. Enter the initiating event and safety functions.

    SAFETY

    FUNCTION

    Oxidation reactor

    high temperature

    alarm alertsoperator

    at temperature T1

    Operator

    reestablishes

    cooling water flow

    to oxidation reactor

    Automatic

    shutdown system

    stops reaction at

    temperature T2

    INITIATING EVENT:

    Loss of cooling waterto oxidation reactor

    FIRST STEP IN CONSTRUCTING EVENT TREE

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    Step 3: Construct the Event Tree

    b. Evaluate the safety functions.

    SAFETY

    FUNCTION

    Oxidation reactorhigh temperature

    alarm alertsoperator

    at temperature T1

    Operatorreestablishes

    cooling water flow

    to oxidation reactor

    Automaticshutdown system

    stops reaction at

    temperature T2

    INITIATING EVENT:

    Loss of cooling waterto oxidation reactor

    REPRESENTATION OF THE FIRST SAFETY FUNCTION

    Success

    Failure

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    Step 3: Construct the Event Tree

    b) Evaluate the safety functions.

    SAFETY

    FUNCTION

    Oxidation reactorhigh temperature

    alarm alertsoperator

    at temperature T1

    Operatorreestablishes

    cooling water flow

    to oxidation reactor

    Automaticshutdown system

    stops reaction at

    temperature T2

    INITIATING EVENT:

    Loss of cooling waterto oxidation reactor

    REPRESENTATION OF THE SECOND SAFETY FUNCTION

    Success

    Failure

    If the safety function does not affect the course of the

    accident, the accident path proceeds with no branch pt to

    the next safety function.

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    Step 3: b. Evaluate safety functions.

    SAFETY

    FUNCTION

    Oxidation reactor

    high temperature

    alarm alertsoperator

    at temperature T1

    Operator

    reestablishes

    cooling water flowto oxidation reactor

    Automatic

    shutdown system

    stops reaction attemperature T2

    INITIATING EVENT:

    Loss of cooling waterto oxidation reactor

    COMPLETED EVENT TREE

    Success

    Failure

    Completed !

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    Step 4: Describe the Accident Sequence

    SAFETY

    FUNCTION

    Oxidation reactor

    high temperature

    alarm alertsoperator

    at temperature T1

    Operator

    reestablishes

    cooling water flowto oxidation reactor

    Automatic

    shutdown system

    stops reaction attemperature T2

    INITIATING EVENT:

    Safe condition,return to normaloperation

    Safe condition,process shutdown

    B C D

    A

    AC

    Loss of cooling water

    to oxidation reactor

    ACCIDENT SEQUENCES

    Success

    Failure

    nsa e con on,

    runaway reaction,operator aware ofproblem

    Unstable condition,process shutdown

    Unsafe condition,runaway reaction,

    operator unawareof problem

    A

    ACD

    AB

    ABD

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    Example Event Tree

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    Cooling CoilsReactor Feed

    Cooling Water Out

    Cooling

    Figure 11-8 Reactor with high temperature alarm

    and temperature controller.

    Reactor

    TIA

    TIC

    Alarmat

    T > TA

    Thermocouple

    High Temperature Alarm

    Temperature

    Controller

    Water In

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    Safety Function:

    Identifier: B C D E

    Failures/Demand: 0.01 0.25 0.25 0.1

    High TempAlarm Alerts

    Operator

    OperatorNotices

    High Temp

    OperatorRe-startsCooling

    OperatorShuts Down

    Reactor Result

    A

    A

    0.7425

    AD0.2227

    ADE

    0.02475

    AB

    0.99

    0.2475

    Continue Operation

    Shut Down

    Runaway

    Continue Operation

    Shutdown = 0.2227 + 0.001688 + 0.005625 = 0.2250 occurrences/yr.

    Runaway = 0.02475 + 0.0001875 + 0.0000625 = 0.02500 occurrences/yr.

    Figure 11-9 Event tree for a loss of coolant accident for the reactor of Figure 11-8.

    Initiating Event:

    Loss of Cooling

    1 Occurrence/yr.

    0.005625

    ABD

    0.001688

    ABDE

    0.0001875

    ABC

    0.001875

    ABCD

    0.0005625

    ABCDE

    0.0000625

    0.01

    0.001875

    0.000625

    0.0075

    0.0025

    Shut Down

    Runaway

    Continue Operation

    Shut Down

    Runaway

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    Safety Function0.01 Failures/Demand

    Initiating

    Event0.5 Occurrences/yr.

    Success of Safety Function

    (1-0.01)*0.5 = 0.495 Occurrence/yr.

    Failure of Safet Function

    0.01*0.5 = 0.005 Occurrence/yr.

    Figure 11-10 The computational sequence across a safety function in anevent tree.

    Hi h T O t O t Hi h T O t

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    Safety Function:

    Identifier: B C D E FFailures/Demand: 0.01 0.25 0.25 0.01 0.1

    High TempAlarm Alerts

    Operator

    OperatorNotices

    High Temp

    OperatorRe-startsCooling

    High TempShuts Down

    Result

    A

    1

    A0.7425

    0.99

    0.2475

    Continue Operation

    Shut Down

    Shut Down

    Runaway

    OperatorShuts Down

    Reactor

    AD0.2450

    ADE0.002228

    ADEF0.0002475

    AB0.005625

    0.002475

    Continue Operation

    Shutdown = 0.2450 + 0.001856 + 0.00001688 + 0.0006187 = 0.2475 occurrences/yr.

    Runaway = 0.0002475 + 0.000001875 + 0.000000625 = 0.0002500 occurrences/yr.

    Figure 11-11 Event tree for the reactor of Figure 11-8. This includes a high temperature shutdown system.

    Loss of Cooling1 Occurrence/yr.

    0.01

    0.001875

    0.000625

    0.00750

    0.0025

    0.001856

    ABDE0.00001688

    ABDEF0.000001875ABC0.001875

    ABCD

    0.0006187ABCDE0.00000563

    ABCDEF0.000000625

    0.00001875

    0.00000675

    Shut Down

    Shut Down

    Runaway

    Continue Operation

    Shut Down

    Shut Down

    Runaway

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    What is Fault Tree Analysis? Fault Tree Analysis(FTA) is one of the several deductive logic model techniques,

    and one of the most common hazard identification tool.

    The deduction begins with a stated top level hazardous/undesired event.

    It uses logic diagrams and Boolean Algebra to identify single events and

    combinations of events that could cause the top event.

    Probability of occurrence values are assigned to the lowest events in the tree in

    order to obtain the probability of occurrence of the top event.

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    Fault tree main symbols.Commonly Used Symbols Occasionally Used Symbols

    OR gate Incomplete event

    An Event / Fault Inhibit gate

    Basic Event

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    FTA Symbols Explained

    Basic Event: A lower most event that can not be further developed.

    E.g. Relay failure, Switch failure etc.,

    An Event / Fault: This can be a intermediate event (or) a top event. They are aresult logical combination of lower level events.

    E.g. Both transmitters fail, Run away reaction

    OR Gate:Either one of the bottom event results in occurrence of

    the top event.

    E.g. Either one of the root valve is closed, process signal to transmitter fails.

    AND Gate: For the top event to occur all the bottom events should

    occur.

    E.g. Fuel, Oxygen and Ignition source has to be present for fire.

    S b l l i d

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    FTA Symbols Explained

    Incomplete Event: An event which has scopefor further development but not done usuallybecause of insufficient data.

    E.g. Software malfunction, Human Error etc.,

    External Event: An event external to the system.

    E.g. Fire.

    Inhibit Gate: The top event occurs only if the

    bottom event occurs and the inhibit condition istrue.E.g. False trip of unit on maintenance overridenot ON.

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    Procedure

    Procedure for Fault Tree AnalysisDefine TOP

    event

    Define overall

    structure.

    Explore each

    branch in

    successive level

    .

    Solve the fault

    tree

    Perform

    corrections if

    required and

    make decisions

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    ProcedureDefine Top Event: Use PHA, P&ID, Process description etc., to define the top event.

    If its too broad, overly large FTA will result. E.g. Fire in process.

    If its too narrow, the exercise will be costly. E.g. Leak in the valve.

    The boundaries for top event definition can be a System, Sub-system,

    Unit, Equipment (or) a Function.

    Some good examples are: Overpressure in vessel V1, Motor fails to start,

    Reactor high temperature safety function fails etc.,

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    ProcedureProcedure for Fault Tree Analysis

    Define TOP

    event

    Define overall

    structure.

    Explore each

    branch in successive

    .

    Solve the faulttree

    Perform corrections

    if required andmake decisions

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    Procedure

    Procedure for Fault Tree Analysis:Define TOP

    event

    Define overall

    structure.

    Explore each

    branch in

    successive level

    .

    Solve the fault

    tree

    Perform

    corrections if

    required and

    make decisions

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    ProcedureExplore each branch in successive level of detail:

    Continue the top down process until the root cause for each

    branch is identified and/or until further decomposition isconsidered unnecessary.

    So each branch will end with a basic event or an undeveloped

    event.

    Consider Common cause failure & Systematic failures in the

    process of decomposition.

    A good guide to stop decomposing is to go no further than

    physical (or) functional bounds set by the top event.

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    Procedure

    Procedure for Fault Tree Analysis:

    Define TOP

    event

    Define overall

    structure.

    Explore each

    branch in

    successive level

    .

    Solve the fault

    tree

    Perform

    corrections if

    required andmake decisions

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    ProcedureSolve the Fault Tree:

    Assign probabilities of failure to the lowest level event in each

    branch of the tree.

    From this data the intermediate event frequency and the top

    level event frequency can be determined using Boolean

    Algebra and Minimal Cut Set methods.

    P d

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    Procedure

    Minimal Cut Set theory:

    The fault tree consists of many levels of basic andintermediate events linked together by AND and OR gates.

    Some basic events may appear in different places of the fault

    .

    The minimal cut set analysis provides a new fault tree,

    logically equivalent to the original, with an OR gate beneath

    the top event, whose inputs (bottom)are minimal cut sets.

    Each minimal cut set is an AND gate with a set of basic event

    inputs necessary and sufficient to cause the top event.

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    Procedure

    Procedure for fault tree analysis:

    Define TOP

    event

    Define overall

    structure.

    Explore each

    branch in

    successive level

    .

    Solve the fault

    tree

    Perform

    corrections if

    required andmake decisions

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    Advantages of FTA

    Plus points of FTA:

    Deals well with parallel, redundant or alternative fault paths.

    Searches for possible causes of an end effect which may not

    ave een oreseen.

    The cut sets derived in FTA can give enormous insight into

    various ways top event occurs.

    Very useful tool for focused analysis where analysis is

    required for one or two major outcomes.

    d f

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    Disadvantages of FTA

    Minus points of FTA:

    Requires a separate fault tree for each top event and makes itdifficult to analyze complex systems.

    Fault trees developed by different individuals are usuallydifferent in structure, producing different cut set elements

    and results.

    The same event may appear in different parts of the tree,

    leading to some initial confusion.

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