7. Cavitation

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    SS 2012 Fachgebiet Strmungsmaschinen

    Prof. Dr.-Ing. Martin Gabi

    Machines und Prozesses Hydraulic FluidMachinery

    7.

    Cav

    itation

    1

    Cavitation

    What is cavitation?

    Formation of local vapor areas and vapor bubbles in the inside

    of flowing fluids.

    When does cavitation occur?

    When the static pressure drops below the vaporpressure of the liquid

    What are determining factorscavitation in centrifugal pumps?

    Operating state, rotor/blade geometry, fluid properties.

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    SS 2012 Fachgebiet Strmungsmaschinen

    Prof. Dr.-Ing. Martin Gabi

    Machines und Prozesses Hydraulic FluidMachinery

    7.

    Cav

    itation

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    SS 2012 Fachgebiet Strmungsmaschinen

    Prof. Dr.-Ing. Martin Gabi

    Machines und Prozesses Hydraulic FluidMachinery

    7.

    Cav

    itation

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    Cavitation (2)

    Why is cavitation potentially dangerous?

    If the steam bubbles are carried by the flow into areasin which the static pressure rises again above the

    vapor pressure, then the vapor bubbles implode. At the sametime extremely high flow velocities are locally present around thevapor bubbles.If this takes place in the vicinity of a wall, then the impulse

    forces of the high flow velocities can cause material damages.

    Is it sensible to avoid cavitation?

    No. Cavitation is only dangerous if an intensive interactionwith the walls occurs. Modern centrifugal pumps operate with a partial andcontrolled amount of cavitation.

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    SS 2012 Fachgebiet Strmungsmaschinen

    Prof. Dr.-Ing. Martin Gabi

    Machines und Prozesses Hydraulic FluidMachinery

    7.

    Cav

    itation

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    Cavitation damages (examples)

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    SS 2012 Fachgebiet Strmungsmaschinen

    Prof. Dr.-Ing. Martin Gabi

    Machines und Prozesses Hydraulic FluidMachinery

    7.

    Cav

    itation

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    Cavitation (examples)

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    Prof. Dr.-Ing. Martin Gabi

    Machines und Prozesses Hydraulic FluidMachinery

    7.

    Cav

    itation

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    Harmful effects of cavitation inhydraulic FM

    Two-phase flowThe vapor bubbles cause two-phase flow. Sincethe specific volume of the vapor phase is much more larger, theeffective cross-section of the flow is narrowed. This leads to

    blockage and reduction of performance and efficiency.

    Noise and vibrations

    The implosions of the vapor bubbles cause high-frequencynoises. Through blockage effects, unstationary flowphenomenon can occur.

    Material removal, destructionThrough the intensive and frequent pressure peaks, due to theimplosions near the wall, local material strains can appear, whichcan lead to erosion and corrosion.

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    SS 2012 Fachgebiet Strmungsmaschinen

    Prof. Dr.-Ing. Martin Gabi

    Machines und Prozesses Hydraulic FluidMachinery

    7.

    Cav

    itation

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    Evap

    oration

    curve

    K

    avitation

    p T diagram

    Evaporation

    Temperature T

    Absolu

    te

    pressur

    e

    p

    fluid

    solid

    gasTP

    CP

    CP critical point

    TP Triple pointMelting

    curve

    p > pD

    p < pDS

    ublim

    atio

    n

    c

    urve

    Solid

    ifica

    tioncurve

    M

    elting

    curve

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    Prof. Dr.-Ing. Martin Gabi

    Machines und Prozesses Hydraulic FluidMachinery

    7.

    Cav

    itation

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    avoiding cavitation?

    Nowhere in the fluid machine the pressure shall be lower than the vaporpressure of the fluid.

    Criteria:

    Problem: Where is pmin?Only the manufacturer has this information.

    Solution: Manufacturer must give the permissible minimal pressure ata reference point (usually at the inlet flange)

    min Dp p>

    , , mintot E D tot E

    p p p p >

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    Prof. Dr.-Ing. Martin Gabi

    Machines und Prozesses Hydraulic FluidMachinery

    7.

    Cav

    itation

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    Cavitation index

    Definition:

    (Net positive suction head)

    Difference of the total pressure to the vapor pressure at theinlet (E)

    Given by manufacturer: NPSHerf , NPSHreq

    ( ) ( ),1

    tot E DNPSH p pg=

    2

    , ,2

    tot E I I Verl S I p p gz p c

    = + +

    To be figured out by operator: NPSHvorh , NPSHav

    Energy balance at inlet part of facility (I E):

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    Prof. Dr.-Ing. Martin Gabi

    Machines und Prozesses Hydraulic FluidMachinery

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    Prof. Dr.-Ing. Martin Gabi

    Machines und Prozesses Hydraulic FluidMachinery

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    Cav

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    2

    ,1 ( )

    2= + +vorh DI I Verl S INPSH p gz p p c

    g

    2

    , , 2tot E I I Verl S I p p gz p c

    = + +

    ( )( ),

    1tot E DNPSH p p

    g=

    vorh erf NPSH NPSH

    Criteria for free of cavitation

    Inlet facility Machine

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    Prof. Dr.-Ing. Martin Gabi

    Machines und Prozesses Hydraulic FluidMachinery

    7.

    Cav

    itation

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