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Air Sep Era Tors

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    Air Separators

    All practical dry powder separators use AIR to

    accomplish the separation of coarse and fines.

    All designs have some degree of inherent

    inefficiencies.

    Qf/Qa principle is important for all air

    classifiers.

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    O-S e

    pa

    Arrang

    em

    ent

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    Principle of the

    High-Efficiency Separator

    Cage Rotat ion

    Guide Vane Dir ect ion

    Unif or m

    Flow distribution

    Inlet

    Plenum

    Feed

    Feed Classi f icat ion ZoneOSEPA Details

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    O-Sepa Separator

    Wear plates and air

    seal should be

    inspected regularly

    Guide vanes and rotor

    cage may require

    annual hard facing

    Check ceramic tiling Remove build-up

    inside intakes

    A i r S e a l

    B u f fe r P la te

    D i s p e r s i o n P l a t e

    G u i d e V a n e s

    S w i r l B l a d e

    P a r t i ti o n P l a t e

    F e e d

    S e c o n d a r y

    A i r In takeP r im a r y

    A i r In takeTer tia r y A i r

    I n t a k e &

    D a m p e r

    H o p p e r

    F l a p G a t e

    S h a f t A s s e m b l y

    D r i v e S u p p o r t

    C o u p l i n g

    R e d u c e r

    M o t o r

    R e d u c e r S u p p o r t

    E x i t D u c t ( To D u s t

    C o l le c t o r & F a n )

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    Key Separator Relations

    Circulating Load

    % Recovery

    Tromp Curve Qf/Qa

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    Circulating Load C.L. = R/F (used by Lafarge)

    Others define it as C.L. = A/F

    No right way, but be sure to ask! Governs efficiency

    A: Separator Feed

    F: Fines

    R: Rejects

    (or Tails)

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    % Recovery Standard definition for efficiency

    Quantity of Fines recovered from

    quantity available in the feed

    Quick way to determine

    performance%Recovery =

    f(x)F

    a(x)A

    =fines X (feed - rejects)

    feed X (fines - rejects)

    X 100

    X 100

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    Tromp Curves

    Graph tells a great deal about theperformance of the separator

    efficiency

    sharpness of cut

    agglomeration (grinding aid)

    mechanical state

    Probability vs. log plot

    Plots probability of rejects vs. size

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    How to read- perfect screen A perfect screen will give

    a graph with a vertical

    line

    The line occurs at the

    sieve size

    The area below the line

    is reject1 1 0 4 5 1 0 0

    0

    5 0

    1 0 0

    P a r t i c l e S i z e , m ( lo g s c a l e )

    A r e a a b o v e

    c u r v e

    i s f in i s h

    p r o d u c t

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    How to read - overloaded (Bypass)

    The more you load the

    separator, the greater

    the chance some fineswill be rejected

    This is called (Tromp)

    Bypass Also applies if you

    reduce internal air flow

    1 1 0 4 5 1 0 0

    0

    5 0

    1 0 0

    P a r tic l e S iz e , m ( lo g s c a le )

    Coarse Rejects

    Rejected Fines

    (Bypass)

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    How to read - imperfection

    Akin to a hole in your screen

    Imperfection describes the

    slope of the cut line

    Related to a mechanical design

    problem (or improper

    maintenance)

    1 1 0 4 5 1 0 0

    0

    5 0

    1 0 0

    P a r t ic l e S i z e , m ( lo g s c a le )

    C o a r s e R e j e c ts

    R e j e c t e d F i n e s

    ( B y p a s s )

    C o a r s e P a r t ic l e s i n F i n e s

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    What we dont want

    Splitter gate

    A flat tromp curve means

    that the separators

    beginning to look like asplitter gate

    Opposite to a perfect

    screen

    1 1 0 4 5 1 0 0

    0

    5 0

    1 0 0

    P a r t i c l e S iz e , m ( lo g s c a l e )

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    Example 1

    1000100101

    1

    2

    3

    4

    5

    6

    7

    Example Tromp Curve (Sturtevant)

    Particle Size, m, (x)

    100

    99.38

    93.32

    69.15

    50.00

    30.85

    6.68

    0.62

    Bypass = 56%

    Acuity Limit = 25 m

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    Example 2

    1000100101

    1

    2

    3

    4

    5

    6

    7

    Example Tromp Curve (OSEPA)

    Particle Size, m, (x)

    100

    99.38

    93.32

    69.15

    30.85

    6.68

    0.62

    50.00

    Bypass = 8%Acuity Limit = 11 m

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    Interpretations

    1 10 45 100

    0

    50

    100

    Particle Size, m (log scale)

    Indicatesagglomeration(grinding aidproblem)

    1 10 45 100

    0

    50

    100

    Particle Size, m (log scale)

    Over fed

    Under fed

    1 10 45 100

    0

    50

    100

    Particle Size, m (log scale)

    Good

    Mechanical

    Shape

    Poor

    Mechanical

    Shape

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    Qf/Qa Related to circulating load Qf is the separator feed rate (kg/hour)

    Qa is the air flow (m3/hour)

    So Qf/Qa is in units of kg/m3

    the lower the Qf/Qa, the more efficient the separator

    Qf/Qa should be less than 2 kg/m3 for good operation

    1.0 1.5 2.0 2.5 3.0 3.5

    0

    10

    20

    30

    40

    50

    60

    70

    80

    Bath

    Sturtevant

    Qf/Qa vs Bypass - O-Sepa & Sturtevant

    Qf/Qa (kg feed/m3 separator sweep)

    O-Sepa

    Sturtevant

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    Typical

    Mill Circuit

    1 m / s

    2 5 m / s

    5 m / s

    1 0 m / s

    Dust Collector

    Clean Airto Vent orRecirc toSeparator

    Fresh Feed

    Separator Reject

    Mill Discharge

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    Questions

    What is the basic purpose or function of an air separator? The more heavily loaded the separator, the more efficient the

    separation. True or False?

    If the separator feed is 150 t/hr, and the reject rate is 100 t/hr,

    what is the circulating load?

    If the separator feed is 150 t/hr and the airflow is 50,000 m3/hr,what is the Qf/Qa? Would this be considered good operation?

    The %recovery calculation is based on samples of the

    separator feed, fines, and rejects, and is a quick way to

    determine separator performance. True or False?


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