Lect 3 - Fmea & rev

Embed Size (px)

Citation preview

  • 8/8/2019 Lect 3 - Fmea & rev

    1/27

    1

    Hazard IdentificationFMEA HAZ P

    Prof. Ir. Dr. Mohd Sobri Takriff

    Dept. of Chemical & Process Engineering,

    FMEA

  • 8/8/2019 Lect 3 - Fmea & rev

    2/27

    2

    What is FMEA?

    FMEA is an acron m that stands forFailure Modes and Effects Analysis

    Identifies the potential failure of a systemand its effects

    that would eliminate the chance ofoccurrence

    Documents the potential failures

    1963 1965 1975 1977 1980 1986 1990 1996 1998

    NASA Aeronautics Nuclear Presentation Standard- Use in Use in Further Increasedand space Engi- of the FMEA ization in the auto- the different development use in the

    travel neering to the auto- Germany motive branches of to the system automotive

    The History of the FMEA

    motive industry industry FMEA industryindustry (first of all, (since 94(Ford) suppliers) at AOAG)

    QS 9000

  • 8/8/2019 Lect 3 - Fmea & rev

    3/27

    3

    FMEA

    Oriented towards e ui ment rather thanprocess

    Paticularly suited for mechanical and electricalsystems

    FMEA systematically

    on that system

    determines the significance of each failure modewith regard to the system's performance

    Applications & Benefits?

    May be applied at various stages

    Design

    Process (operation)

    Service and Maintenance

    Improvements in: a e y

    Quality

    Reliability

  • 8/8/2019 Lect 3 - Fmea & rev

    4/27

    4

    FMEA - Methodology

    define the s stem to be evaluated

    establish the level of analysis

    Failure Analysis identify failure modes, causes and consequences

    as well as design and operating provisions againstsuch failures

    Reporting

    FMEA System Definition

    define the extent of the s stem to beanalyzed

    usually performed in relatively small steps

    Requires analysts / personnels with aknowledge of the system

    system and their performance requirements

  • 8/8/2019 Lect 3 - Fmea & rev

    5/27

    5

    FMEA Level of Analysis

    based on the functional structure of a s stem

    the failure modes are expressed as failure toperform a particular subsystem function

    primary function is that for which the subsystemwas rovided

    secondary function is one which is merely aconsequence of the subsystem's presence

    FMEA Analysis of Failures

    remature o eration

    failure to operate when required

    intermittent operationfailure to cease operation when required

    loss of output or failure during operation

    degraded output

    etc

  • 8/8/2019 Lect 3 - Fmea & rev

    6/27

    6

    FMEA Analysis of Failures

    Based on Failure modes

    looks at the likely causes and the effects on boththe components and the system

    consideration is given to the relative importance ofthe effects and the sequence

    safeguards against such failures and methods ofdetecting them are then examined

    FMEA - Reporting

    identif the most si nificant failures in termsof their effects on the overall system

    decide whether or not the existing safeguardsand detection devices are adequate

    more detailed analysis on the weak link

  • 8/8/2019 Lect 3 - Fmea & rev

    7/27

    7

    FMEA - Reporting

    No standard re ortin format t icall covers The unit/system

    Failure mode

    Consequence of failure

    Symptoms

    safeguards

    Example 1Household Water Supply system

  • 8/8/2019 Lect 3 - Fmea & rev

    8/27

    8

    FMEA Household water supply system

    Water Supp y System FMEA

    No Component

    DescriptionFailure mode Failure effect(s) Symtoms

    Safe

    GuardsActions

    1 Kitchen Tap Fails open Kitchen Flooded

    Water

    continuously

    flowing out-

    Install flow

    control valve

    2Inlet pipe

    (2 in PVC)Blocked Water Tank Dry

    No water at

    kitchen tap -

    Install waterfilter

    Clean filter

    periodically

    Example 1Household Water Supply system

  • 8/8/2019 Lect 3 - Fmea & rev

    9/27

    9

    Failure Mode Effect Analysis(FMEA)

    CRITICALITY ANALYSIS

    Criticality is defined in the same way as risk - thatis, a combination of the severity of an effect andthe probability or expected frequency

    simplest approach requires a form of ranking or

    effect / consequence

    frequency

    Failure Mode Effect Analysis(FMEA)

    of the following categories loss of mission due to inability of equipment to

    perform

    economic loss due to lack of output orfunction

    damage to plant or third party property

    injury to operating personnel or the public

    death to operating personnel or the publicand/or significant damage to the environment

  • 8/8/2019 Lect 3 - Fmea & rev

    10/27

    10

    Failure Mode Effect Analysis(FMEA)

    order or severity)

    catastrophic - may cause death or totalsystem loss

    critical- may cause severe injury or

    major - may cause some injury or damage

    minor - requires unscheduled maintenance.

    Failure Mode Effect Analysis(FMEA)

    uantification of fre uenc de ends on thedata available and may again be a simpleranking, such as one depending on failure

    probability during the operating time interval extremely unlikely

    remote

    ccas ona

    reasonably frequent

    frequent

  • 8/8/2019 Lect 3 - Fmea & rev

    11/27

    11

    Failure Mode Effect Analysis(FMEA)

    extremely unlikely - 0.001

    remote - between 0.001 and 0.01

    occasional- between 0.01 and 0.1

    - .and 0.2

    frequent - 0.2.

    Failure Mode Effect Analysis(FMEA)

    5 A C C D D

    4 A B C C D3 A B B C C

    2 A A B B C

    1

    1 2 3 4 5

    A B C DACCEPTABLE UNACCEPTABLE

    Threshold value = 10

  • 8/8/2019 Lect 3 - Fmea & rev

    12/27

    12

    FMEA

    -

    reduce probability that the cause offailure will result in the failure mode

    reduce severity of failure by redesignor add rotection redundanc

    increase probability of detection

    HAZOP

  • 8/8/2019 Lect 3 - Fmea & rev

    13/27

    13

    HAZOP

    OPerability studies

    The term 'HAZOP' originated in ICI andfirst appeared in the literature in the

    early 1970s

    HAZOPSkelton, B, 1997

    , , ,the process and engineering intentions of new andexisting facilities to assess the hazard potential of mal-

    operation or mal-function of individual items of equipment and the consequential effects

    e s, ,

    HAZOP is formal, systematic examination of aprocessing plant in order to identify hazards, failuresand operability problems, and assess theconsequences from such mal-operation

  • 8/8/2019 Lect 3 - Fmea & rev

    14/27

    14

    WHY DO HAZOP??

    Generates a list of identified roblemsusually with some suggestions forimprovement of the system

    improves safety, reliability and quality bymaking people more aware of potential

    .

    help to sort out loopholes and inconsistenciesin procedures and force plant personnel toget their instructions up to date

    HAZOP

    Basic hiloso h if a process operates within its intended

    design philosophy then undesired

    hazardous events should not occur

    The ob ective of a HAZOP mainly to identify how process deviations

    can be prevented or mitigated to minimizeprocess hazards

  • 8/8/2019 Lect 3 - Fmea & rev

    15/27

    15

    Basic Ideas of HAZOP

    to stimulate the ima ination of a reviewteam, including designers and operators, in asystematic way so that they can identifypotential hazards in a design

    in order to consider all the possible ways thatprocess and operational failures can occur

    HAZOP

    recommend necessary changes to asystem to meet company risk guidelines

    recommend procedures or changes fore m na ng or re uc ng e pro a y ooperating deviations.

  • 8/8/2019 Lect 3 - Fmea & rev

    16/27

    16

    HAZOP

    a lication at the correct sta e in aproject means that problems areidentified and can be rectified duringdetailed design.

    material for inclusion in the plantoperating instructions

    HAZOP Terminology

    Desi n intent

    the way in which the plant is intended to operate.

    Deviation

    any perceived deviations in operation from thedesign intent. Cause- the causes of the perceiveddeviations.

    Consequence

    the consequences of the perceived deviations

  • 8/8/2019 Lect 3 - Fmea & rev

    17/27

    17

    Hazop TerminologySafeguards

    consequences of the perceived deviations and to informoperators of their occurrence

    Actions the recommendations or requests for information made by

    the study team in order to improve the safety and/or

    operability of the plant.

    u e wor s simple words used to qualify the intent and hence discover

    deviations.

    Parameters basic process requirements such as 'flow', 'temperature',

    'pres-sure' and so on.

    HAZOP COMPONENTS

    Procedure

    Guide words

  • 8/8/2019 Lect 3 - Fmea & rev

    18/27

    18

    Hazop Team

    normall com rises between four and ei htmembers, each of whom can provide knowledge and

    experience appropriate to the project to bestudied

    efficient and allow each member to make acontribution, whilst containing sufficient skillsand experience to cover the area of studycomprehensively

    Hazop Team

    Hazop team:

    those with detailed technical knowledge ofthe process;

    those with knowledge and experience of

    chair and report upon technical meetings

  • 8/8/2019 Lect 3 - Fmea & rev

    19/27

    19

    Hazop Team

    t ical member of a Hazo team

    chairman or team leader

    secretary

    process design engineer

    control engineer

    operations specialist

    project engineer

    Other specialists may be consulted or beavailable for specific points

    Hazop Team

    selected for his or her ability to effectivelylead the study

    should have sufficient seniority to give thestudy recommendations the proper level of

    knowledge and experience of the Hazoptechnique

  • 8/8/2019 Lect 3 - Fmea & rev

    20/27

    20

    Hazop Team

    should have a technical appreciation of theproject and be familiar with the HAZOPtechnique

    technical members usually part of the project design team

    Hazop PROCEDURE1. Begin with a detailed flow sheet. Break the flow

    eg the reactor area might be one unit, and the storagetank another. Select a unit for study.

    2. Choose a study node (vessel, line, operatinginstruction).

    3. Describe the design intent of the study node. eg example, vessel V-I is designed to store the benzene

    feedstock and provide it on demand to the reactor.

  • 8/8/2019 Lect 3 - Fmea & rev

    21/27

    21

    Hazop PROCEDURE4. Pick a process parameter:

    ,

    level,

    temperature,

    pressure,

    concentration,

    pH,

    viscosit

    power,

    Inert

    etc

    Hazop PROCEDURE

    5. Apply a guide word to the process parameter to.

    NO

    MORE

    LESS REVERSE

    etc

    6. If the deviation is applicable, determine possiblecauses and note any protective systems.

  • 8/8/2019 Lect 3 - Fmea & rev

    22/27

    22

    Hazop PROCEDURE7. Evaluate the consequences of the

    .

    8. Recommend action what?

    by whom?

    b when?

    Hazop PROCEDURE

    9. Record all information.

    10.Repeat steps 5 through 9 until allapplicable guide words have beenapplied to the chosen process

    .

  • 8/8/2019 Lect 3 - Fmea & rev

    23/27

    23

    Hazop PROCEDURE

    11. Re eat ste s 4 throu h 10 until all a licableprocess parameters have been considered forthe given study node.

    12. Repeat steps 2 through 11 until all studynodes have been considered for the givensection and roceed to the next section on the

    flow sheet.

    Hazop PROCEDURE

  • 8/8/2019 Lect 3 - Fmea & rev

    24/27

    24

    Hazop GUIDE WORDSGuide words Meaning Comments

    NO, NOT,

    NONE

    The complete negation of the

    intention Quantitative decrease

    No part of the design intention is achieved, but

    nothing else happens.

    MORE, HIGHER,GREATER

    LESS, LOWERQuantitative increase

    Applies to quantities such as flow rate and

    temperature and toiattivities such as heating and

    reaction.

    AS WELL AS Quali ta tive increase

    All the design and operating intentions e achieved

    along with some additional activity, such as

    contamination of process streams.

    PART OF Qualitative decreaseOnly some of the design intentions are achieved,

    some are not.

    REVERSE The logical opposite of

    Most applicable to activities such as flow or chemical

    reaction. Also applicable to substances, for example,

    po son nstea o ant ote.

    OTHER THAN Complete substi tut ionNo part of the original intention is achieved - the

    original intention is replaced by something else

    SOONER THAN Too early or in the wrong order Applies to process steps or actions.

    LATER THAN Too late or in the wrong order Applies to process steps or actions.

    WHERE ELSE In additional locationsApplies to process locations, or locations in operating

    procedures.

    Hazop Worksheet

    HAZARDANDOPERABILITY STUDYREPORTProject Title:

    Project Number; Date:

    P&ID Number: Chairman:

    Line Number: Study Team:

    Guideword

    Deviation Cause Consequences Safeguards

    Action

    Number By DetailsReply

    Accepted

  • 8/8/2019 Lect 3 - Fmea & rev

    25/27

    25

    Hazop WorksheetHAZOP ACTION SHEET

    Project: Project no: Action no:

    Action on: Date for reply:

    Description:

    Reply:

    Review comments:

    Accepted/rejected (Leader) Date:

    Issued Returned Complete

    Return completed form to:

    Example 3Household Water Supply system

  • 8/8/2019 Lect 3 - Fmea & rev

    26/27

    26

    Example 3Household Water Supply system

    HAZARD AND OPERABILITYSTUDY REPORT

    Project Title: household water supply system

    Project Number; 2008-101 Date: 25 Oct 2008

    Drawing Number: Myhome-101 Chairman: Mywife

    Line Number: Line No 1 ( pipe from water tank

    and kitchen tap)

    Study Team: MyHusband, Maid, eldest son

    Item:KitchenTap Paramter:FlowGUIDE

    WORDSDEVIATIONS CAUSES CONSEQUENCES SAFEGUARDS ACTION REQUIRED

    REVERSEWater flow

    continuously

    Valve (kitchen tap)

    fails openKitchen flooded none

    Install flow control

    valve

    NO No Flow Pipe BlockedNo water supply

    to kitchennone

    Install tank cleaning

    system

    LESS Low flowPipe partially

    Blocked

    Reduced ater

    flow to kitchennone

    Install tank cleaning

    system

    MORE

    Example 3Household Water Supply system

    HAZARD AND OPERABILITYSTUDY REPORT

    Project Title: household water supply system

    ro ect um er: - ate: ct

    Drawing Number: Myhome-101 Chairman: Myhusband

    Line Number: Line No 2 (main valve, pipe &

    tank)

    Study Team: Mywife, Maid, eldest son

    Item:WaterTank Paramter:WaterSupplyGUIDE

    WORDSDEVIATIONS CAUSES CONSEQUENCES SAFEGUARDS ACTION REQUIRED

    MOREMore water than

    tanks capacity

    House owner forgot

    to close water

    supply valve

    Water tank

    overflow, house

    flooded

    none Install level control ler

    NO No water Pipe blocked Tank dry none Install water filter

    LessLow water level

    in tank

    Pipe partially

    blocked

    Low water

    pressure to

    bathroom and

    kitchen

    none Install water filter

  • 8/8/2019 Lect 3 - Fmea & rev

    27/27

    Example 3

    Household Water Supply system