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TOPIC : SAFETY ANALYSIS & PREVENTION DATE : June 20 14 LECTURE : DE TAILED HAZARD ANALYSIS, RISK ANA LYSIS an d Man age men t Lecturer : Dr Ghulam Murshid (GM) Health, Safety & Environment (CCB 2012)

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  • TOPIC : SAFETY ANALYSIS & PREVENTIONDATE : June 2014LECTURE : DETAILED HAZARD ANALYSIS,

    RISK ANALYSIS and ManagementLecturer : Dr Ghulam Murshid (GM)

    Health, Safety &Environment (CCB 2012)

  • Lecture Content Part 2 Detailed Hazard Analysis

    Failure mode and effect analysis (FMEA) Hazard and operability (HAZOP) Fault tree analysis (FTA) Risk analysis (RA)

  • You should be able to identify, defineand differentiate Detailed Hazard Analysis (for complex system)

    Failure mode and effect analysis (FMEA) Hazard and operability review (HAZOP) Human error analysis (HEA) Fault tree analysis (FTA) Risk analysis and Management

    Lecture Outcome

  • Proceeds as follows: Critically examine the system in question. Divide the system into its various components. Each component is studied to determine how itcould fail.

    Rate each potential failure according to itsconsequences (0 to 10).

    Failure mode and effect analysis (FMEA)

    Weaknesses: no human error factor. does not account for component interfaces.

  • FMEA Example

  • HAZOP HAZOP highlights include: Systematic examination Multidisciplinary study Utilization of operational experience Safety as well as operational evaluations May indicate solutions to the identified

    problems Considers operational procedures Led by an independent person Results are recorded.

  • Preparation for HAZOP Detailed information on the processmust be available

    Process flow diagrams (PFD), processand instrumentation diagrams(P&Ids), detailed equipmentspecifications, materials ofconstruction and mass & energybalances are very essential for thestudy.

  • Process Flow Diagram (PFD)

  • HAZOP Guide WordGuide words describe ways in which the component maydeviate from its design.

    No Less More Part of As well as Reverse Other than

    Never none Quantitative decrease Quantitative increase Qualitative decrease Qualitative increase Opposite of forward Complete substitution

    Guide words Meaning

  • Stages of HAZOP as applied to eachcomponent of a chemical processing systemare described below:1. Identify the design intent of the selected partof process.2. Consider each condition or action using theHAZOP guide word to suggest possibledeviations3. Consider causes and consequences of thedeviation4. Define and note the action required to addressthe problems.

    Procedure

  • EXAMPLEThe phosphoric acid and ammonia are mixed,and a non-hazardous product, diammoniumphosphate (DAP), results if the reaction ofammonia is complete. If too little phosphoricacid is added, the reaction is incomplete, andammonia is produced. Too little ammoniaavailable to the reactor results in a safe butundesirable product. The HAZOP team isassigned to investigate "Personnel Hazardsfrom the Reaction".

  • SOLUTIONStorage A

    Storage B

    Reactor C Storage C

    Valve A

    Valve B

  • Parameter Deviation Possible Causes Consequences Action

    Flow NO flow into reactor Blockage or leaking pipe into R Rate of reaction decreases

    No reaction occurring

    Install flow indicator and flow

    control valve

    NO flow out of reactor Reactor outlet clogged or

    blocked

    No flow to subsequent

    separation units

    Stop operation

    Perform reactor maintenance

    MORE Control valve failure trim

    changed

    Exchanger tube leaks

    Incorrect instrument readings

    Reactants build-up

    Increase in reaction rate

    Check flow indicators and

    controllers

    By-pass flow

    LESS Blockage or leaking in piping

    system into R-100

    (line restriction)

    Reduced rate of reaction

    Less production

    Install flow indicator and

    controllers

    HAZOP

  • Parameter Deviation Possible Causes Consequences Action

    Pressure MORE Reactants build-up

    Blocked pipeline

    Pressure indicator failure

    Pressure build-up inside

    reactor

    Runaway reaction

    Install high pressure alarm

    Pressure relief system (PRV)

    LESS Leakage in piping of reactor Reduced reaction rate

    Reverse flow

    Check feed pressure

    Install Pressure indicator at

    feed to reactor

    Temperature MORE Higher reaction rate

    Excess feed into reactor

    Cooling system failure

    Feed heater failure

    R-100 out of control

    Runaway reaction

    Catalyst deactivation

    Install high temperature alarm

    Install coolant flow meter and

    low flow alarm

    Perform maintenance on feed

    heater

    LESS Low feed temperature

    Feed heater failure

    Low reaction rate

    Low product purity

    Increase feed temperature

    Install temperature indicator

  • Human Error Analysis (HEA)

    It is best to perform HEA together witheither FMEA or HAZOP. This will enhancethe effectiveness of all three processes.

    For predicting human error before accidents occurby:

    observing employees at work and notinghazards.

    actually performing job tasks to get a first handfeel for hazards.

  • FTA The analysis process is displayed visually. Between Basic event and Top Event. Uses symbols derived from Booleanalgebra.

    The resultant model looks like a logicdiagram or a flow chart.

    Fault Tree Analysis (FTA)

  • OR gate

    AND gate

    Top eventIntermediateevent

    Basic event

    Undevelopedevent

    External orhouse event

    TransferIN-OUT

    Logic and Event Symbols

  • Top Event ContributingEvents

    Undeveloped Event Basic Event

    The FaultTree

    Concept

  • FaultTree Fault tree: top-down approach startingwith the unwanted consequences as thetop event & identifying all factors thatcould contribute to the top event.

    Used to think through possible causesof a loss, to find most probablesequence of events leading to the loss& to quantify the probability of loss.

  • Steps: FTATo draw a fault tree take the followingsteps.1. Determine undesirable event, which is to be the Top

    Event.2. Determine the Basic Events, which could immediately

    cause the Top Event.3. Determine the relationship between the Basic

    Events and the Top Event in terms of AND and ORgates.

    4. Determine whether any of the Basic Events needfurther analysis, if so repeat steps 2 & 3.

  • Example: Fault TreeConsider a case of a motor overheated. TheBasic Events could be the primary motor failsor excessive current load to the motor.The current load might be excessive due toexcess current flow in the circuit and failure ofthe fuse.It could be either short circuiting or a powersurge that contributed to the excess currentflow.

  • Example: Fault TreeMotor OverheatedPrimaryMotorFailure

    A

    FuseFails

    B

    ExcessiveCurrent to

    Motor

    ExcessCurrent In

    Circuit

    Shortcircuit

    C

    PowerSurge

    D

    AND

    OR

    OR

    The probability of the Top Event (themotor overheated) is obtained bycombining the base events accordingto the logic rules:

    For this case, probability= [(C+D) x B] + A

    For an OR gate (ADD theprobabilities)

    For an AND gate(MULTIPLY the value)

  • Example: Fault TreeMotor OverheatedPrimaryMotorFailure

    0.05

    FuseFails

    0.1

    ExcessiveCurrent to

    Motor

    ExcessCurrent In

    Circuit

    Shortcircuit

    0.007

    PowerSurge

    0.003

    AND

    OR

    OR

    The probability of the Top Event(the motor overheated) isobtained by combining the baseevents according to the logicrules:

    For this case, probability

    = [(0.007+0.003) x 0.1] + 0.05

    = 0.051

  • Risk Analysis (RA) Decision-making tool normally associatedwith insurance and investments. It can also be used to analyse theworkplace, identify hazards and developstrategies for overcoming hazards. Focuses on TWO questions:

    How frequently does a given eventoccur? How severe are the consequences of agiven event?

  • What is a risk?Risk may be considered as the potential foradverse effects resulting from an activity orevent

    Acceptable level of riskThis is generally determined by what isprepared to be lost balanced against possiblegains

  • The Risk Management ProcessThe total procedure associated with

    identifying a hazard,

    assessing the risk,

    putting in place control measures,

    and reviewing the outcomes.

  • Hazard IdentificationRemember Hazard:

  • Risk Assessment

  • Risk Control

  • Risk AssessmentRisk:The possibility of an unwanted eventoccurring

    Likelihood:The chance of an event actually occurring.

  • Likelihood Very Likely -- Could happen frequently

    Likely -- Could happen occasionally

    Unlikely -- Could happen, but only rarely

    Highly Unlikely -- Could happen butprobably never will

  • When evaluating the likelihood of an accident,a factor that will modify the likelihood category, is

    exposure.

    Very Rare -- Once per year or less Rare -- A few times per year Unusual -- Once per month Occasional -- Once per week Frequent -- Daily Continuous -- Constant

    Likelihood

  • ConsequencesFATAL Death

    MAJOR INJURIES Normally irreversible injury ordamage to health requiring extended time off work to effectbest recovery.

    MINOR INJURIES Typically a reversible injury ordamage to health needing several days away from work torecover. Recovery would be full and permanent.

    NEGLIGIBLE INJURIES Would require first aid and mayneed the remainder of the work period or shift off beforebeing able to return to work.