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    utoclaveValidation

    PHARMACEUTICAL ENGINEERING JULY/AUGUST2002Copyright ISPE 2002

    Practical Guide to AutoclaveValidation

    by Raymond G. Lewis, PE

    In addition topotentialbusinessliabilities, therecan be significantcosts associatedwith an autoclave

    validationprocess. Thepracticalexperience thatthis article isbased on mayprovideassistance inensuring aneffective, efficientvalidation

    process forsteamsterilization.

    Introduction

    This a rticle is based on pra ctical experi-

    ences gained by the author while con-

    ducting hun dreds of val idat ion test r uns

    on dozens of a utoclaves of varied ma nufa cture.

    I t is primari ly intended that personnel who

    perform validation testing on autoclaves may

    benefit from th ese experiences, an d th at it will

    a ssist in ensu ring a high level of compliance inthe va lidat ion process. The a rticle also may be of

    benefit in selecting an appropriate validation

    stra tegy a nd/or cycle. Personnel unfam iliar with

    stea m sterilizat ion principles or a utoclave vali-

    dat ion could use the material as a basic training

    tool and it may be a good refresher for more

    experienced personnel. A list of definitions a nd

    references ar e provided at the end of the a rticle.

    Sterility Assurance LevelThe level of microbial inactivation can be de-

    scribed by an exponential function, Sterility

    Assuran ce Level or SAL. For exam ple, a S AL of

    10-6 means t ha t t he probabi l ity of a single viable

    microorganism being present on a sterilized

    item/product is one in one million a fter th e item

    ha s undergone a sterilizat ion process. A SAL of

    10-3 means t ha t t he probabi l ity of a single viable

    microorganism being present a fter sterilizat ion

    is one in one thousa nd.

    The SAL required is determined by the in-

    ten ded use of th e item/product. S ter ilizat ion

    processes associat ed with pa rentera ls and medi-

    cal devices tha t pose a significant risk in terms

    of the probability and severity of an infection

    (e.g., implant s, sterile fluid pat hw ay s, products

    intended t o come into conta ct wit h compromised

    tissue) generally ha ve been st erilized to an SAL

    of 10-6. Medica l device products n ot intend ed to

    come int o conta ct wit h brea ched skin or compro-

    mised tissue ar e generally sterilized to a SAL of10-3.

    The remainder of this article is written as-

    suming tha t a SAL of 10-6 is required.

    Log ReductionAchieving a 1-log reduction means to decrease

    the microbial population by a factor of 10. The

    bioburden is the number and type of viable

    microorgan isms conta mina ting an it em. A ster-

    ilization cycle tha t provides a S AL of 10-6 effec-

    t ively means that the microorganisms that

    could be present (i.e., bioburden) are killed,

    an d a n a dditional 6-log reduction sa fety fa ctor

    has been provided. The following provides an

    example of a cycle achieving a SAL of 10-6.

    B ioburden (worst case) = 134 CFU (colony

    forming unit ).

    To reduce the microbial populat ion from 134

    to 1 = log (134) = 2.13 (i.e., a 2.13-log red uc-

    tion is required to reduce the

    populat ion from 134 to 1).

    Apply ing an addit iona l 6-log

    reduction will theoretically

    reduce the microbial popu-lation from 1 to 0.000001.

    This pr ovides a S AL of 10-6 or

    a one in one million prob-

    ability of a single surviving

    microorganism.

    Tot a l l og red uct i on = 2. 13 + 6

    = 8.13. Therefore t o provide

    a S A L o f 1 0 -6 w i t h a

    bioburden of 134 CFU re-

    quires a sterilization cycle

    th at provides an 8.13 log re-

    duction.

    Figure 1. Empty chamber

    temperature mapping

    (Photograph provided courtesy

    of Kuhlman Technologies Inc.)

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    Thermal Resistance CharacteristicsThe th erma l resista nce of specific microorga nisms is chara c-

    terized by D -va lues an d Z-va lues. A D-value is the t ime in

    minutes, at a specific temperature, to reduce the surviving

    microbial population by 1-log. A Z-value is the temperature

    chang e required to result in a 1-log reduction in D-value.

    Other t ime measurement variables perta ining to thermal

    resistance are F-values and F o-va lues. An F -value is the

    number of minutes t o kill a specified number of microorga n-

    isms w ith a specified Z-va lue at a specific tempera tur e. An F o-value is t he num ber of minutes t o kill a specified num ber of

    microorganism s with a Z-va lue of 10C (50F ) at a t emperat ure

    of 121.1 C (250 F).

    Common Misconception and EquivalentSterilization Time

    It is not uncommon to encounter the concept that 121.1C

    (250F) is the temperature required for steam sterilization.

    This underst a nding is not ent irely correct. E xtensive empirica l

    studies w ere conducted an d one of th e critical va ria bles (tem-

    perature) was pre-selected. It is not surprising that the tem-

    perature selected was an obvious round number in the tem-

    perat ure ra nge of interest (250F). The F o-value equa tion can

    be used to determine the relative sterilization time at other

    tempera tur es as per th e following (with Z-va lue = 10 C):

    F o = 10(T 121. 1) /10

    where T = tempera ture ( C) and F o = equivalent steri l iza-

    tion time (min.)1

    Table A provides some exam ples a nd the relat ionship follows

    in gra phical form in F igure 2.

    As is demonstrated by the data above, sterilization can be

    achieved using any of these temperatures. The lower the

    tempera tur e the longer th e sterilizat ion cycle required. This is

    an importa nt concept t o consider because th ere are occas ions

    where the temperature needs to be carefully selected. Anexample is a l iquid that cannot withsta nd high temperatures.

    Ideal ly , the highest temperature tha t the load can w ithsta nd

    is selected, since this will provide the shortest possible cycle.

    Variables Required to Determine anIdeal Sterilization Cycle

    An ideal sterilization cycle presumes an ideal sterilizing

    environment (i.e. , satur a ted stea m w ith n o air). The ideal cycle

    can be determined with t he followin g thr ee va ria bles: bioburden,

    D-value, and required SAL. The following provides some ex-

    amples:

    a) G iven: B ioburden = 75 CFU , D-value = 0.5 min./log at

    121.1 C, Required S AL = 10-6Then: Log (75) = 1.88

    Log Reduction r equired = 1.88 log + 6 log = 7.88 log

    Idea l Cy cle at 121.1C (250 F) = (7.88 log)(0.5 min./

    log) = 3.94 min ut es

    b) G iven: B ioburden = 1,215 CFU, D-value = 1.6 min./log a t

    121.1 C, Required S AL = 10-6

    Then: Log (1215) = 3.08

    Log Reduction r equired = 3.08 log + 6 log = 9.08 log

    Idea l Cy cle at 121.1C (250 F) = (9.08 log)(1.6 min./

    log) = 14.53 minut es

    Overkill ApproachDetermining the bioburden and D-value for all i tems to be

    sterilized in a load ca n be quit e time consuming an d costly. As

    a result , for i tems tha t a re not heat sensit ive, an overki ll

    a pproach is generally employed.

    An overkill approach avoids collecting bioburden and D-

    va lue dat a by a ssuming w orst-case conditions. A bioburden of

    106 of a h ighly heat resista nt spore forming bacteria (Ba cillus

    stearothermophilus) is utilized. The D-value at 121.1C for

    these bacteria is generally slightly above 2 minutes, andth erefore using 2.5 minutes is a good w orst-case va lue.

    With a bioburden of 106, to a chieve a SAL of 10-6 requires a

    12 (6 + 6) log reduction. Un der ideal conditions, t he length of an

    overkill ster ilizat ion cycle a t 121.1C is th erefore (12 log)(2.5

    min ./log) = 30 minut es.

    Bioburden and D-Value ApproachFor i tems that are heat sensi t ive and cannot withstand an

    overkill approach, it is necessary to collect bioburden and

    possibly D-value data. This will dramatically shorten the

    sterilizat ion cycle required. For example, if th e bioburden is

    low (e.g., 10 CFU ) and even m odera tely resista nt (e.g., D-value

    = 0.5), an id eal 30-minu te overkill cycle at 121.1 C can be

    repla ced by a n id ea l cycle of 3.5 minu tes (7 log x 0.5 min ./log).

    Alterna tively, the sterilizat ion t emperat ure could be reduced

    Figure 2. Equivalent sterilization time.

    Figure 3. Ideal cycle time.

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    to 112C and yet only require slightly less than a 30 minute

    ideal cycle. I t may be a signi ficant a dvant age to reduce the

    sterilizat ion t emperat ure a nd/or time.

    A compromise approach m a y sometimes be utilized wh ere

    bioburden da ta is collected, but D -value st udies ar e not per-

    formed. A worst case D-value of 2.5 could then be employed.

    This approach will provide a somewhat shortened cycle and

    avoids the time and cost of D-value studies. Following our

    example with a bioburden of 10 CFU , the ideal cycle a t 121.1C

    can be shortened from a 30-minute overkill cycle to a 17.5-

    min ut e cycle (7 log x 2.5 m in./log).

    Figure 3 shows the st eriliza tion time required a t 121.1C for

    an ideal cycle to achieve a SAL of 10-6 at varying levels ofbioburden (D-va lue = 2.5 min.).

    Vacuum and Non-Vacuum CyclesPreviously, this article has addressed ideal cycles that pre-

    sume an idea l sterilizing environment. In term s of the length

    of cycle required, one can only a pproach idea l cycles for item s

    tha t a re easily st erilized. Most often, items/loa ds w ith less

    tha n ideal conditions ar e encount ered.

    There are three basic types of cycles as follows:

    a) Ha rd Goods (Vacuum):

    Suitable for items easy to sterilize since air removal and

    steam penetra t ion a re highly effect ive. Examples are ma ny

    types of glasswa re a nd lar ge diameter piping. A typical har d

    goods cycle may draw one vacuum prior to introducing

    steam, r eaching t he desired st eril izat ion tempera ture, a nd

    beginning th e sterilizat ion dw ell period. A typical pressure

    vs. time gra ph for a h ar d goods cycle is shown in Figure 4.

    b) Wra pped G oods (Vacuum):

    Ut ilized for items difficult t o sterilize since air removal a nd

    steam penetrat ion are harder to achieve. Examples are

    gowns, long lengths of tubing, a nd ta nks/vessels/appa ra tus

    wit h sm a ll inlet/outlet port s a nd/or vent filt ers. A ty pical

    wr apped goods cycle may d ra w t hree or more vacuums prior

    to reaching the desired sterilization temperat ure an d begin-ning the sterilization dwell period. A post sterilization

    vacuum also is usual ly draw n to evacuate the steam from

    the load items. Often t he length of time to pull an d release

    the va cuums exceeds the length of the sterilizat ion dw ell. A

    typical pressure vs. time gr a ph for a wr apped goods cycle is

    shown in Figur e 5.

    c) Liquids/G ra vity Displacement (Non-Vacuum):

    Items that contain l iquids general ly cannot have a deep

    vacuum pulled or th e liquid w ill be draw n out of the item.

    Liquid cycles generally just heat up an d cool down a nd do

    not utilize vacuums. These items may require a lengthy

    cycle time especially where the liquid volume is large

    becau se the length of time required to heat up an d cool down

    the liquid may be considerable. Another term for a liquid

    cycle is gravity displacement as the air is displaced by

    gra vity (i.e. , removing air by int roducing st eam int o the top

    of a chamber an d displacing the air , w hich is heavier tha n

    stea m, by removing the a ir from the bottom of the cha mber).

    A typical pressur e vs. time gra ph for a liquids cycle is shown

    in Figure 6.

    Basic Validation ApproachInstallation Qualif ication (IQ )

    The IQ process is int ended to demonstra te th a t th e aut oclave

    a s insta lled meets a ll specifica tions, is inst alled properly, andthat the supporting programs needed for ongoing operation

    (e.g., standard operating procedures, maintenance program,

    etc.) are in place.

    An IQ ma y include the following checks:

    Mecha nical Equipment Speci ficat ions (chamber, valves,

    traps, s trainers, f i l ters , regulators, vacuum pump, heat

    excha nger, condenser, etc.)

    Control and Ins t rumenta t ion S peci fi ca t ions (programmable

    logic cont roller, opera tor in terf a ce, printer /recorder, cont rol

    valves, transducers, pressure and temperature transmit-

    ters, resistance temperature devices, switches, level sen-

    sors, int erlocks, ph otocells, etc.)

    Si te Specificat ions/Ut i li t ies (power, grounding, surge pro-

    tector, unint erruptible power supply, breakers, wa ter, air,

    clean steam, plant steam, drain, shutoff /isolation valves,

    electrical disconnect switches, etc.)

    Dra wings Veri ficat ion (P &ID, mechan ical , electrical)

    Const ruct ion Mat er ia l s/Mater ia l s in P roduct C ontac t

    Approval D ocumentat ion (e.g. , pressure vessel, electrical ,

    etc.)

    C h a ng e/S pa r e P a r t s

    B i ll of Ma t er ia ls

    Vendor Speci fi ca t ion Sheets

    P u rch a se Or der s

    F a ct ory Per forma nce Te st s

    C ommis s ion i ng Repor t P r ev en t iv e Ma i nt en a n ce P r og ra m

    Sta ndard Opera t ing Procedures (opera t ing , maintenance ,

    calibration)*

    O per a t in g a n d M a in t en a n ce Ma n u a ls

    P iping Insta l lat ion Verificat ion (slope, dead legs)

    Weld Inspection/Sur face Roughness Documenta tion/Met-

    allurgical Documentation

    Control System Documentat ion (system configurat ion/block

    diagr a m, flow sheets, display/report layouts, r equired inter-

    lock considerations, general process limits, conditions for

    operat ing over ran ge, har d copy a nd electronic applicat ion

    code listing, t iming dia gra m, syst em security, input /output

    point l is t ing, dat a monitoring, alarms, softwa re inventory

    Table A. Equivalent sterilization time.

    Temperature Fo Equivalency to 121.1C (250F)

    115C (239F) 0.25 min. 1 minute at 115C provides the same lethality as 0.25 minutes at 121.1C

    120C (248F) 0.78 min. 1 minute at 120C provides the same lethality as 0.78 minutes at 121.1C

    121.1C (250F) 1 min. 1 minute at 121.1C provides the same lethality as 1 minute at 121.1C

    122C (251.6F) 1.23 min. 1 minute at 122C provides the same lethality as 1.23 minutes at 121.1C

    125C (257F) 2.45 min. 1 minute at 125C provides the same lethality as 2.45 minutes at 121.1C

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    and version, software configurations, parameter listings,

    softwa re development a nd t esting records, chan ge control,

    vendor qua lification, modular softw ar e development docu-

    ments, deta iled m odule functiona l specificat ions, et c.)

    Ins t rumenta t ion and Input/Output Dry Loop and Wet Loop

    Checks**

    P I D Tun in g**

    I n st r um en t C a lib ra t i on s**

    * Operat ing Procedures can only be final ized after Perfor-

    mance Qualifications tests are completed when vali-da ted load configurat ions a nd cycles are known.

    ** Note: in some approaches, these checks a re capt ured as

    initial Operational Qualification activities.

    Operat ional Q ualif icat ion (OQ)

    The OQ process is intended to demonstrate that the compo-

    nents of the a utoclave operate properly and tha t t he aut oclave

    is deemed rea dy for performa nce or load test ing.

    An OQ may include the following checks:

    Opera t iona l Tests (opera t or/supervisory/ma intena nce

    modes, doors, abort a nd emergency stop, a larm s, progra m-

    mable parameters, menu navigation, security, power-up

    an d shut down, opera tor interfa ce display checks, interlock

    override cont rol, procedure select/sta rt cont rol, step a d-

    van ce control, switch a nd int erlock tests, etc.)

    Po w er Los s Recovery Tes t

    S ou r ce C od e R ev iew

    F ilt er S t er ili za t i on

    Leak/Air Removal/St eam P enetra tion/Vacuum Hold Test*

    J a cket Ma ppin g

    S a t ur a t ed S t ea m C heck

    E m pt y Ch a m ber Tes ts

    * The Bowie Dick test is designed to test a ir removal , the

    a bsence of air leaks a nd stea m penetra tion into a porous

    load . It u ses a t est pa ck of fabr ic wit h specific dimensions

    or there ar e commercial, use once packs a va ilable. It ha sbeen widely employed in Europe. In North America, a

    Vacuum H old Test ha s often been employed. Eur opea n

    St an da rd E N 554 specifies tha t if a sterilizat ion process

    includes air removal from the product, a st eam penetra -

    tion test shall be carried out at the commencement of

    each da y the a utoclave is used. Although a va cuum hold

    test ma y be less sensit ive than a Bowie Dick test , the

    aut hor assumes tha t a vacuum hold test can be consid-

    ered as a sat isfactory al ternative i f s tric t acceptance

    criteria a re applied. This assu mption is based on steam

    penetra tion/letha lity in t he worst case load items being

    demonstra ted and t hat the vacuum hold test therefore

    demonstrates absence of leaks and that the val idated

    condit ions t hat resul ted in letha l i ty ar e being met on anongoing ba sis.

    Empty Chamber Distribut ion Tests (Figure 1)

    The ba sic objective is to show the chamber provides a uniform

    sterilizing environment. In the opinion of the author, cold

    spots in au tocla ves ar e ra rely encount ered. Sometimes cold

    therm ocouples a re misint erpreted a s cold spots (refer to fol-

    lowing section Tips).

    Three consecutive successful runs are performed for each

    cycle type with typical a cceptan ce criteria as per the following:

    Throughout the dwel l t ime, a l l tempera tures measured in

    Figure 4. Hard goods cycle.

    Figure 5. Wrapped goods cycle.

    the chamber are within a 3C ba nd (steri lizat ion temperature

    + 3C ).2 Note: th e dwell set-point -1C /+ 2 C is often used.

    Throughout the dwell t ime a l l tempera tures measured in

    the chamber do not f luctua te by more than 1C. 2

    Throughout the dwel l t ime, a l l tempera tures measured in

    the cham ber do not differ from each other by more than 2C .2

    The s team i s a t a t empera ture corresponding to i t s vapor

    pressure.2

    The interva l of t ime between the a t t a inment of the s ter i li za-

    t ion temperature in the hottest and coldest parts of the

    chamber does not exceed 15 seconds for chambers of not

    more than 800L and not to exceed 30 seconds for larger

    chambers.2

    Timed measurements shal l be control led to an a ccuracy of

    1%.2

    Required pre-cert i f icat ion and post-cert i f icat ion of the dat a

    logger ensures th at the temperature m easurement system

    is accura te to within 0.5C.

    The vacuum hold test should achieve a vacuum level of 2.5

    psia (with va cuum pump) an d ma intain t he vacuum (with-

    out further vacuum being initiated) within 0.4 psi over a

    period of five minutes.

    Performance Qualificat ion (PQ)

    Loaded Chamber Steam Penetration Tests

    Loaded chamber steam penetrat ion r uns a re then conducted

    on every load. Note: this is a very time consuming process,

    especially if you have a significant number of items to be

    sterilized. It is necessa ry to determine which load it ems are th e

    most difficult to sterilize and which location(s) within the

    items presents the w orst-case conditions.

    There a re tw o commonly used methods for determining t he

    worst-case items/locations, t hermocouples, an d stea m integra -

    tors. Steam integrators a re commercial ly ava i lable strips tha t

    provide a q ua nt ita tive indica tion of the exposure to stea m. The

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    am ount of stea m exposure can be determined by measuring

    the movement of a chemical indicator on the integrator

    strip. The author recommends utilizing steam integrators

    since they are designed to measure steam exposure and

    therm ocouples can result in misleading da ta (i .e. , measur -

    ing temperat ure without ta king into account whether t here

    is any air present).

    Determining which load items are the most difficult to

    sterilize and which location(s) within the items presents the

    worst-ca se conditions can be a da unt ing ta sk. With a lar ge loadcontaining a wide variety of different types of items, the

    number of possible test locat ions seems t o approach infinity. I t

    also can be difficult t o get t he th ermocouple a nd/or stea m

    integra tor into the item wit hout ad versely affecting the item's

    ability t o be sterilized a nd/or ruining t he item (a concern w ith

    expensive items).

    One must evaluate an item on a case-by-case basis and

    determine how best to challenge the item. Often th e item must

    be sealed somehow to return th e i tem to a sta te tha t represents

    equivalency with respect to stea m penetra tion. No a tt empt will

    be made t o provide an exha ustive commenta ry h ere, but rat her

    provide a few basic techniques for answering questions that

    inevitably arise:

    What is the most di ff icult point to steril ize in a h ose of

    uniform diameter? Common sense can somtimes assist,

    dicta ting in this insta nce tha t th e most difficult to sterilize

    point is in th e center of the hose.

    How do you get a 10-foot length of thermocouple and/or

    stea m int egrat or into th e middle of a 50-foot hose? You can

    put a slice/cut into t he middle of the hose an d insert the

    th ermocouple/int egra tor th rough t he slice. Note: the cut

    must be sealed or you will not be challenging the hose

    properly. You can use silicon to seal t he cut. Alterna tively,

    if tw o 25-foot lengt hs of th e hose are a va ilable you ca n join

    the two lengths with a connector and insert the thermo-

    couple into the connector. The connector then must besealed. The a dva nta ge here is tha t you dont ruin t he 50-foot

    hose. The connector technique ca n be used for sma ll diam-

    eter tubing w here the hose is too sma ll to insert a therm o-

    couple an d/or stea m integra tor.

    What i s the wors t-case loca t ion w i thin a bot t le, f lask , or

    cylinder? This ha s been shown to be in the cent er, near, but

    not at the bottom.

    How can you minimize the number of runs requi red to

    cha l lenge a load? Using st eam int egrators can h elp mini-

    mize the nu mber of runs r equired to challenge a load. There

    are a limited number of thermocouples available, but as

    many integrators as desired can be placed in the load.

    Load Configurat ionsAnother va riable of concern is w hether fixed load configura-

    tions or flexible load configurations are desired. A fixed load

    configuration means that the load to be sterilized will be

    identical for all future processing runs and that the load is

    placed in the chamber in exactly the sa me wa y for al l future

    processing ru ns.

    In t he opinion of the aut hor, the location of a n item in th e

    chamber d oes not influence its ability t o be sterilized (ass um-

    ing tha t t he location chan ge does not involve a chan ge in load

    density). This observation is based on the experiences of the

    author in conducting hundreds of validation test runs on

    dozens of aut oclaves of varied ma nufa cture. However, one

    should proceed as if the location within the autoclave is a

    va riable of concern. One can eliminat e this var iable by rota ting

    the i tems within a load from run to run and t hereby at tempt to

    demonstrate positional equivalency.

    For most load s, aga in in the opinion of the au thor ba sed on

    experience, the number of items in the chamber does not

    influence an items ability to be sterilized (unless the load

    becomes so dense th a t st eam penet ra tion/circulat ion becomes

    a n issue). One should proceed as if t his is a var iable of concern.You can su ccessfully validat e a load w hile encompas sing th is

    si tuat ion by performing minimum a nd ma ximum load studies.

    The followin g provides a n exa mple of fixed vs. flexible loa d

    configurations:

    E xa m ple loa d:

    - t hree (3) f la s k s

    - four (4) graduated cy l inders

    - 24 plas t i c bot t les w i th vent f i lters

    F ixed Load/Fixed Pos it ion:

    In this situation, all of the load items are placed in the

    au tocla ve, each t ime in the sam e position for each item, a nd

    a diagram of the load configurat ion is avai lable in theprocedures so tha t t he opera tors can reproduce the load for

    every processing run. This situat ion w ill require the least

    va lidation run s, but offers no flexibility in load configura-

    tion.

    F ixed Load/Variable Pos it ion:

    In this situation, all of the load items are placed in the

    au toclave, but t he location of the item in the a utoclave can

    vary an d only a l is t of the load i tems is required for the

    procedures. The validation runs must demonstrate posi-

    tional equivalency by rotating the items from location to

    location during t he test r uns. It ma y be possible to accom-

    plish th is with t he same number of val idat ion runs a s a bove

    and offers the operators some flexibility in loading theautoclave. This can be an advantage especially for large

    loads containing numerous items.

    Var iable Load/Variable Pos it ion:

    In this situation, any or all of the load items (i.e. , any

    combin a tion of from 0 to 3 fla sks, from 0 to 4 cylinder s, from

    0 to 24 bottles) can be pla ced in t he a utoclave in an y position

    in the a utoclave and only a maximum load l ist is required

    for the procedures. The valida tion runs mu st demonstr at e

    positional equiva lency by rota ting t he items from location to

    location during t he test run s. The valida tion runs a lso must

    demonstra te tha t t he cycle is adequate for both a maximum

    Figure 6. Liquids cycle.

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    loa d an d minimum load configurat ion. The minimum load

    tests a re done with only one item in the aut oclave, tha t item

    being the load item demonstra ted a s being the most difficult

    to sterilize. This meth od will require the grea test n umber of

    validation runs, but offers the operators a great deal of

    flexibility in loadin g th e au toclav e. This can be a s ignifican t

    advantage in many si tuat ions.

    Loaded Chamber Biological Challenge Tests

    After determining the worst-case items and worst-case loca-tions within items, these items are then challenged with

    biological indica tors (spore strips a nd/or vials for pla cement

    wit hin liquids). A thermocouple should be placed along w ith

    each indicator, as the temperature data wi l l be required to

    extra polat e the cycle to achieve the SAL of 10-6.

    Tests are conducted until a cycle time results in three

    consecutive runs w here th e biological indica tors show n o growt h.

    If it is important to achieve the shortest possible cycle, this

    process can consume a great deal of time as t o determine t he

    success/failure point likely r equires obta ining fa iled t est re-

    sults along with successful test results. In addition, it takes

    time to determine wh ether th e indicators exhibit growt h (a fter

    tw o days of incuba tion you can be reasonably confident w hether

    there is growth or not in most cases). If a few minutes of

    possibly unnecessa ry t ime added t o the cycle is not a significa nt

    issue, it can be a dva nta geous to at tempt t o predict a cycle time

    that you feel will pass. This can save considerable time and

    validation costs.

    Once one ha s a chieved thr ee consecutive run s resulting in

    no growth and therefore demonstrating a 6log reduction

    (a ssuming y ou were using indicat ors of 106 spores /st rip), th e

    following equa tions/example show h ow to extra polat e the full

    cycle requ ired t o achieve th e SAL of 10-6:

    La = [12 x (Fo/R)] - Fo

    w he re La = t he a d di t iona l l et ha l it y (F o) required

    12 = used to extra polat e a 12-log reductionFo = the minimum accumula ted F o va lue from the bio-

    logica l cha llenge run s a t t he end of the cycle

    R = the log reduction demonstra ted (i .e. log [spore

    population])

    Fi = 10(T-121.1)/10

    w h er e F i = t h e in st a n t a n eou s F o value

    T = the minimum temperature expected during the

    additional lethality period (Note: this tempera-

    ture should be taken a s the t emperat ure achieved

    at the end of the dwell period at the challenge

    location where the minimum a ccumula ted F o value

    resulted)

    Ta = La/Fi

    where Ta = the addit iona l t ime required

    C = Ta + D

    w he re C = t ot a l d w el l per iod t i me req u ired

    D = the dwell period t ime which resul ted in the dem-

    onstrated reduction

    Exa mple Calculat ion:

    The biological cha llenge run s wer e performed using spore

    strips tha t w ere enumerat ed at 1.21 x 106 spores /st rip.

    Ther efore R = log (1,210,000) = 6.08

    The minimum accumulated F o value (at the end of the

    cycle) from th e biological challenge ru ns w as 30.2 minutes.

    Therefore Fo = 30.2 minut es

    La = [12 x (30.2/6.08)] - 30.2 = 29.4 min ut es

    The temperature in the coldest item at the end of the

    dwell period w as 119.4 C

    Therefore T = 119.4C

    Fi = 10(119.4-121.1 )/10 = 0.676

    Ta = La /Fi = 29.4/0.676 = 43.5 minu tes

    The biological challenge runs were conducted with a

    dw ell period of 45 minu tes. Therefore D = 45 minu tes

    C = 43.5 + 45 = 88.5 minutes (note: this num ber should be

    rounded up)

    Therefore t he dw ell period must be 89 minutes t o achieve

    a 12-log reduct ion.

    Three consecutive successful biological challenge runs

    are performed for each load with typical acceptance

    criteria consistent with the empty chamber distribution

    test a cceptan ce criteria a nd a ll biological indicators used

    during the t est cycle must show negat ive growth .

    Tips1. If you are going to draw a vacuum(s), ensure that the load

    i tems can withst and the va cuum(s). You dont w ant to be the

    person w ho has to report tha t t he new $10,000 ta nk is now

    as f l a t a s a pancake .

    2. Rota te thermocouples from run to run. This avoids misin-

    terpreting th ermocouples tha t read slightly lower tempera-

    tu res (i.e., cold th ermocouples) as cold spots or cold items.3. Label the thermocouples by number using a sma ll s trip of

    aut oclave ta pe. This wil l great ly assist w i th ensuring tha t

    you ar e properly recording w ha t t hermocouple wa s placed in

    each location and will save validation time.

    4. I f you are performing a large number of test run s (e.g . , over

    the course of severa l w eeks), st rike a compromise between

    post-calibra tion verification of t hermocouples a fter every

    run a nd a t t he end of the entire test ing period. I f you wai t

    unt il the end of th e testing period, you run the risk tha t a ll

    of the runs ar e of no value due t o not meeting th e verification

    acceptance criteria. If you verify after every run, you will

    ad d considera bly to th e lengt h of time required t o complete

    the test ing. The author has found that performing the

    verifica tion every few run s or every few da ys is a rea sonablecompromise.

    5. B e caut ious w ith th e acceptance cri teria you employ for

    post-calibration of thermocouples. If the criterion is too

    tight (e.g., all thermocouples must meet the acceptance

    criteria), you may lose a lot of runs if one or two thermo-

    couples cease functioning or a re outside of the tempera tur e

    tolerance aft er the ru n(s).

    6. Take great care with documenting the val idat ion test runs.

    The documenta tion should include: a dia gra m showing t he

    location of all load items wit hin th e aut oclave cham ber, the

    items conta ining th ermocouples, integra tors a nd biological

    indica tors, t he precise loca tion/num ber of ea ch ther mo

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    couple, int egrat or an d biologica l indicat or with in each item,

    the printout from the da ta recorder, the printout or chartfrom the autoclave, the time that the dwell period begins

    an d ends (a s per the dat a r ecorder time), an d the results for

    each integrator or indicator. Each document should be

    clearly la beled with t he dat e, test ru n number, etc. If you fail

    to generat e good documenta tion wh ile conducting the ru ns,

    you w il l not be able to recover when a nalyzing the da ta /

    putting together the report, and you will end up with

    inadequat e or poor qua l ity da ta to support the va l idat ion

    process.

    7. A therm ocouple should alwa ys be placed beside the dra in

    tempera ture sensor (usual ly a drain temperat ure sensor is

    used to control the temperat ure wit hin th e aut oclave).

    Cautions1. If you are using a non-vacuum cycle to sterilize a n on-liquid

    load, you are taking a significant risk. Some regulatory

    bodies will simply not allow processing of non-liquid loads

    with non-va cuum cycles.

    2. Some regulatory bodies ar e extremely concerned tha t a l l

    points within the load achieve sterilization temperature

    when sta rt ing the dw ell period. This may mean t ha t you are

    not draw ing enough va cuums or t hat modificat ions to th e

    items being st erilized a re necessary to a llow more efficient

    steam penetrat ion.

    3. I f you are not using biological indicat ors to val idat e your

    cycle, you a re ta king a significant risk. Using t emperat ure

    dat a alone means tha t you ar e assuming ideal condit ions

    wh ere it is not justified.4 . I f you are placing a smal l quant i ty o f water w i thin load

    items to assist with sterilization, you must have appropri-

    at e procedura l cont rols in place to ensure ongoing consis-

    tency with the am ount of wa ter present during th e val ida-

    tion runs and all subsequent processing runs.

    SummaryThe requirements to validate steam sterilization processes

    ha ve been document ed for ma ny yea rs. For example, perha ps

    the most historically significant reference guide, the PDA

    Technical Monograph No. 1 Validat ion of St eam St erilization

    Cycles wa s published in 1978. Nonetheless, stea m st erilization

    validation remains a significant issue to regulatory bodies,

    par ticularly for processes associat ed with h igh risk in terms of

    the probability and severity of an infection. Failure to ad-

    equa tely addr ess this requirement can place the public at risk

    an d lead to regulat ory citat ions/a ction.

    In addition to potential business liabilities, there may be

    significan t costs a ssociat ed with th e validat ion process. Large

    numbers of time consuming and costly test runs may be

    required, and if appropriate consideration is not given to

    employing t he correct a pproach, unnecessary ongoing opera -

    tional costs may result.

    It is hoped tha t th e pra ctical experience tha t th is document

    is based on will provide assistance in ensuring an effective,

    efficient va lidat ion process for stea m sterilization an d tha t the

    end result provides th e best possible validat ed cycle to meet th e

    needs of the specific application.

    DefinitionsSAL: sterility assurance level.

    SAL of 10-6: th e proba bility of a single viable microorga nismbeing present is one in one million.

    Bioburden: th e number /ty pe of viable microorga nism s con-taminat ing an i tem.

    Overkill Approach: a steri l izat ion approach based on as-suming worst-case conditions (a bioburden of 106 of a highly

    heat r esista nt ba cteria) .

    Log Reduction:reduce the surviving microbial population by

    1 log or decrease th e surviving populat ion by a factor of 10.

    12-Log Reduction:th e log reduction required a chieving over-

    kill and a SAL of 10-6.

    CFU: colony-forming unit.

    D-value:time in minut es, at a specific tempera tur e, to reducethe surviving microbial population by 90%(one logarithmic

    reduction).

    Z-value: temperature change required resulting in a 1-logreduction in D -value.

    F-value: the n umber of minut es to kill a specified number of

    microorganisms wit h a specified Z-value a t a specific tempera -

    ture.

    Fo-value: the n umber of minut es to kill a specified num ber ofmicroorganisms w ith a Z-value of 10 C (50 F) at a t emperat ure

    of 121.1 C (250 F).

    1 Fo:the equ ivalent of 1 minute a t 121.1C (250F).

    Dwell Period:the t ime period th at begins w hen th e aut oclave

    temperature has reached the set-point and ends when thetimer has expired.

    Worst case items: i tems in the load which are the mostdifficult to sterilize (as det ermined by steam penetra tion stud-

    ies).

    Worst case location: the locat ion within a n i tem tha t is the

    most difficult t o sterilize (as determined by stea m penetra tion

    studies).

    Gravity Displacement: a method of removing air by intro-ducing steam into the top of a chamber and displacing th e air ,

    ...steam sterilizat ion validat ion remains a significant issue to regulat ory bodies,

    part icularly f or processes associat ed with high risk in t erms of t he probabil it y

    and severit y of an inf ection.

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    which is heavier than steam, by removing the air from the

    bottom of the cha mber.

    Vacuum Cycle: a sterilization cycle that draws one or morevacuums t o remove air prior to star ting t he dwell period.

    Pre-vacuum: a vacuum drawn prior to start ing the dwellperiod t o remove air.

    Post-vacuum: a vacuum drawn after the dwell period has

    finished to remove stea m.

    Hard Goods Cycle:a sterilizat ion cycle designed for items forwh ich a ir removal is not difficult an d therefore genera lly one

    pre-vacuum is dr aw n.

    Wrapped Goods Cycle: a sterilization cycle designed for

    items for which a ir removal is difficult a nd t herefore generally

    thr ee or more pre-va cuums are dra wn .

    Liquids Cycle:a cycle designed for liquid loads th at generally

    uses gravi ty displacement ra ther tha n draw ing a vacuum.

    Bowie Dick Test:a test designed to verify tha t a n a utoclaves

    vacuum phase is removing a sufficient amount of air prior tothe introduction of steam into the chamber and tests for air

    leaks into the chamber.

    Empty Chamber Tests:tests with an empty cha mber essen-tial ly designed to demonstra te th at an aut oclave provides a

    uniform sterilizing environment .

    Steam Penetration Tests:load ed cha mber tests designed to

    determine the w orst-case items a nd w orst-case locations wit hin

    a load.

    Biological Challenge Tests: load ed cha mber tests designedto challenge the w orst-case locat ions (within worst case items)

    wit h biologica l indicators t o demonst ra te t he effectiveness of asterilizat ion cycle.

    Steam Integrators: commercially available indicators thatprovide an indication of exposure to steam .

    Fixed Load: a load configurat ion where the quanti ty and

    location of items w ithin t he chamber a re fixed.

    SIP: steam-in-place or sterilize-in-place (often used inter-changea bly a lthough t he level of microbial destr uction achieved

    ma y differ).

    References

    1. Validat ion of Steam Steri l izat ion C ycles: PDA TechnicalMonograph No. 1 (1978).

    2. Steri l izat ion of Medical Devices Val idat ion a nd Routine

    Control of Steri lizat ion by Moist Heat : European Sta ndar d

    EN 554 (1994).

    About the AuthorRaymond G. Lewis, PE is a Val idat ion Man-ager for Industria l Design a nd Construction

    Inc. (IDC) in Portland, Oregon. In this posi-

    tion, he is responsible for int erna tional cG MP

    regulat ory issues involved in the d esign, con-

    struction, a nd val idat ion of pharma ceutical ,

    biotech, a nd medica l device fa cilities. He h olds

    a degree in chemical engineering from the

    Universi ty of Saskatchewan and a Cert i f icate in computerscience from th e Un iversity of Regina . Lewis ha s 16 year s of

    experience in the pha rm a ceutical/biotechnology indu str y in

    va lidat ion, engineering, production, fa cility services, and com-

    puter opera tions.

    IDC, 2020 SW 4th Ave., 3rd Floor, Portland, OR, 97201.