Suspension,Dispersion ,Blending

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    1)Suspension:

    Heterogeneous Miture containing

    solid particles that are su!!icientl"

    large !or sedi#entation$%

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    &articles:

    Larger then 1 but less then 10 micron.Particles are visible under a microscope.Settle over time if left undisturbed.

    Can be separated through a filter.Surface area exposed to fluid is constant.

    &urpose:

    Increase surface area, ate of dissolution.

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    '#peller:

    !xial"flo# impellers are used forsuspension.

    $hree blade #ith s%uare pitch and four

    blade #ith &'degree are common.

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    '#peller Speed:

    Sli# is carrie# up$ar# b% mil# stirring& ntt 'rm pile at bttm

    (cal up$ar# )elcit% is greater thenterminal settling )elcit% ' particals*

    ritical '#peller Speed:Critical +,ust-suspen#e# impeller spee# nc*

    n particle remains lnger than 1 sec n the

    )essel bttm*

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    States o! Suspension:

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    $o dissolve the solids

    $o catal()e a chemical reaction

    $o promote the gro#th of cr(stal from

    a super saturated solution

    'n he#ical &rocessing%%

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    2)Dispersion:

    Heterogeneous Miture in *hich

    dispersed phase is uni!or#l" distri+utedin continuu# phase%$

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    &articles:

    Si)e of particle 0.01*' micron. Settle do#n if not disturbed but ver( little. !t high shear rate particles are bro+en,

    diameter reduces and ne# surface are is

    created. -ermentation Li%uid"li%uid/rops and gas"li%uidubbles

    total interfacial area b# dispersed and

    continuous material ma( var( according to

    conditionand degree of Mixing.(Mean

    diameter).

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    '#peller:adial and axial flo# t(pe impellers.

    $hat provide some of both shearturbulence and movement.

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    )Blending:

    Ho#ogeneous Miture o! t*o Misci+le

    i.uids to !or# a single li.uid *ith no

    /ariation in concentration !ro# point to

    point$%

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    i.uids:7niformit( at drop scale is re%uired.

    $he li%uid is #ell mixed close to the impeller

    /ue to the intense turbulence.

    Large radial mixing but small mixing along the

    flo#.

    !t last li%uid returns to e(e of impeller foragain vigorous mixing.

    889 mixing complete in ' circulations.

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    '#peller:Small tan+"""Propeller,

    :igh ;fficienc( Impeller

    center mounted

    Large tan+""""Side

    ;ntering Propeller or

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    Static Mier:

    :elical"element mixer

    >ortex =ixer

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    For lo* /iscosit":lending is done b( turbulence in #hich eddies

    are formed #hich helps mixing

    For high /iscosit":$he flo# is mostl( laminar

    lending is done b( repeatedl( dragging a la(er

    of one fluid through another.e.g.:and mixing of paint.

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    'n he#ical &rocessing%%

    In the manufacturing of perfume, blending is

    re%uired to dilute the concentrated perfume oils

    b( dissolving them in ethanol.Pharmaceutical, in?ection, s(ringeabilit(, pourse

    level mixing.

    2asoline re%uires uniformit( up to 1mm si)edrop variation in this causes @noc+ing.

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    Char\product

    Suspension Dispersion Blending

    Purpose $urbidit( 7niformit( :omogeneit(

    Si)e ofparticles

    1 to 10 um 0.01*' um Less then0.01 um

    Impellerused

    !xial -lo# adial as #ellas !xial -lo#

    -lat blade adial-lo#

    /egree ofmixing

    >er( small Small Large

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