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    VIBRATION 1. Incorrectinstallationoffoundation

    2. Poorcoupling orV-belt drivealignment

    3. Slugs ofwatercarry-overto thepump inlet.

    4. Pipingstress atthe inletdischargeor serviceliquidconnections.

    5. Pumpingestedforeignmaterial i.e.bolts, nuts,weld slag.

    6. Internaldamagedue tocavitation,corrosion,etc.

    Broken couplings,worn V-belt drives orbroken foundationbolts.

    Pump bearings may

    fail prematurely.

    1. Check with SterlingSIHI on properfoundation andgrouting procedures.

    2. Check alignment or

    call Sterling SIHI forassistance.

    3. Check for proper pre-separation

    4. Add flexibleconnections ifnecessary.

    5. Pump should be sentto Sterling SIHI forrepair. Inlet screensshould be installedbefore pump is startedto insure material doesnot enter pump.

    6. Repair or replace worn& damaged parts.

    INGESTION

    DAMAGE

    No inlet screens onthe pump or

    compressor

    Broken impellerblades or seized

    pump.

    Return pump to Sterling SIHIfor repair evaluation.

    SCALE Hard service liquidsi.e. lime or mud.Pumps runninghotter willaccelerate thisproblem.

    a. Scaling willclose theinternalpumpclearances &causebinding.

    b. Scaling willcause adecrease in

    pump

    Use suitable descaler, butflush after use. Consult withSterling SIHI for recommend-ations on the type andquantities.

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    performance.

    c. Scaling willslowly closethe serviceliquid lines

    and causethe pump torun warmer.

    BEARING

    FAILURE

    1. Not usingtherecommendedlubricant.

    2. Over orundergreased.

    3. Couplingsor V-beltdrives notproperlymounted oraligned.

    4. Piping not

    properlysupportedand/oraligned.

    5. Water inthebearings.

    6. Internalpumpclearancessetimproperly.

    Seized pump andbroken or damagedbearing housing.

    1. Check the SterlingSIHI manuals forrecommendedlubricant.

    2. Check & cleanbearings. (replace ifworn)

    3. Check alignment &foundations for propersupport.

    4. Use flexibleconnections for pumpinlet, discharge andservice liquid lines.

    5. Check mechanicalseals or packing.Shield bearings ifenvironment is wet.

    6. Consult Sterling SIHIfor assemblydimension or return forrepair evaluation.

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    PUMP RUNS

    WARMER

    THAN

    NORMAL

    1. Insufficientserviceliquid flow.

    2. Carryover

    of hightemperature liquids.

    3. Carryoverof hightemperature gases.

    4. Pump RPMmay behigher thanrecommended.

    Capacity levels forthe vacuum pump orcompressor maydecline. Also thevacuum level mayfall.

    1. Check the manuals orcall Sterling SIHI forthe proper serviceliquid flow.

    2. Check for proper pre-

    separation or call aSterling SIHItechnician.

    3. High gas temperaturesmay be a processcondition that may beunavoidable. Adjustservice liquid flow asrequired. Call SterlingSIHI if problempersists.

    4. Check pump RPM forthe service. Call ifnecessary.

    PUMP LEAKS 1. Leakingpacking ormechanicalseal. Notesome

    leakage isnecessaryto keep thepackingcool. (Overtighteningwill harden,becomehot & scorethe pumpshaft.)

    2. Leakage

    could befrom thebody, bodygaskets ordrain plugs.(Sometimes a result oferosion orcorrosiondamage.)

    Loss of service liquid.Potential gas leakagewhen shut down. Inminor cases this maybe a house keeping

    problem. In majorcases this may leadto poor pumpperformance ordamage to the pump.

    1. Check packing andtighten or check &replace mechanicalseal. Service liquid orcontaminates from the

    process can coat orabrade mechanicalseal faces.

    2. Check the source ofthe leak. Repair may

    be necessary.

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    HIGHER

    THAN

    NORMAL

    PUMP NOISE

    1. Pump iscavitating.

    2. Pump isoverloadedwith liquid.

    3. Pump hasingestedforeignmaterial.

    4. Bearingsare in poorcondition.

    5. Pumpcoupling orV-belt drivemisalignment.

    An unusual or highnoise level is an earlyindication of aproblem. Thisproblem may lead topump damage or

    failure. Potentialvibration concerns.

    1. Cavitation can be acomplex problem.Consult with SterlingSIHI for solutions.

    2. Check for properservice liquid flow.Also check for goodinlet pre-separation.

    3. Stop the pumpimmediately. Dis-assemble and inspector send the pump toSterling SIHI for repairevaluation.

    4. Inspect bearings. Seethe subject of bearingfailures.

    5. Coupling and V-beltdrive alignment mustbe checked.

    VACUUM

    LEVEL

    PROBLEMS

    1. Poor pipingdesign.

    Vacuum orcompressed airrequirements andpumps mayhave beenaddedwithout therequiredpipingupgrades.

    2. Warmerthanrecommended serviceliquidtemperatures.

    3. Incorrectserviceliquid flow.

    4. Liquid

    Vacuum levels thatare usually lower

    than required.

    1. See the sectiondedicated to piping

    design.

    2. The addition of heatexchangers, coolingtowers or chillers maybe required. Consultwith Sterling SIHI.

    3. Check the manuals orcall Sterling SIHI forproper service liquidflow.

    4. Check for proper pre-separation.

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    carryoverto thepump inlet.

    5. Improperpump

    application.

    6. Poor orinsufficientvacuumcontrol.

    5. Check applicationneeds and call SterlingSIHI for assistance.

    6. Consult with SterlingSIHI for sizing and

    selection of reliefvalves or revisedvacuum control needs.