Pope Pecs 85

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    The princrpal influence of inhom ogeneity is to cau se

    convective transport in physical space. This effect

    appears in closed form in the joint pdf equation

    through the term Vjaf/axj. In contrast, in second-

    order closures, this term gives rise to the correlations

    ( u , u , u ~ ) . ( u , u , ~ ~ )nd (u,4:4;) which are generally

    modelled by gradient diffusion. It is emphasized tha t,

    in the joint pdf equa tion, the conv ective term is in

    closed form and therefore no gradient diffusion

    models are needed.

    The first term on the right-h and side ofEq (5.196)

    represents translport in physical space due to

    molecular diffusion, and (at high Reynolds nu mb er) is

    usually negligible. Nevertheless, the term appears in

    closed form and can be retained without additional

    modelling being required.

    The next three terms represent the effects of

    dissipation and pressure fluctuations that have been

    modelled in Sections 5.3-6. Since dissipation and (to a

    lesser exten t) the slow pressure a re associated with th e

    smaller turbulent scales, it is reasonable to assume

    that these processes are unaffected by inhomo-

    geneities.

    Fo r flows remote from walls, it is assumed that the

    rapid-pressure models still apply. An analysis of the

    rapid pressure ra te of s traing 9 shows tha t, to first

    order, departures from homogeneity have no effect.

    Near walls, however, the velocity gradients and

    Reynolds stresses vary rapidly. Fur the r, the analysis of

    Section 5.4.1. has to be modified to include surface

    rnteprals at the wall. Consequently, the models (Eqs

    5.1 19 an d 5.148) (or a t least the tenso rs C and G ave

    to be mod ified: this is a su bject for future work.

    The final term in Eq. (5.196) represents tra nsp ort

    due to the fluctuating pressure. Pope7' suggested the

    model

    which is consistent with Lumley's mode l for (pluj).

    But this mode l has not been tested.

    5.7.2. Intermittency

    Nea r to the edge of bou nda ry layers and free shear

    layers the flow is intermittent-sometimes turbu lent,

    Fig 5 8 Pdf of indicator

    4

    showing a delta function of

    magnitude 1 - y at

    , =

    0

    sometimes non-turbulent.loO Consider a high

    Reynolds number jet which transports a conserved

    passive scalar (b,(%t), where

    y

    =

    a

    1. At th e jet exit

    4,

    is positive, while in the non-turbulent, irrotational

    fluid remote from the jet

    4,

    is zero. As the Reynolds

    number tends to infinity, the condition ,&, t) >

    0

    can be used a s an indicato r of turbu lent fluid. Th at is,

    if &&t)

    > 0,

    the fluid is in turbulent motion, if

    ,& t)

    =

    0, the fluid is in irrotational, non-turbulent

    motion. The intermittency factor y

    t

    is defined as

    the prob ability of the fluid at ) being turbule nt. In

    terms of the indicato r ,, th e intermittency facto r is

    Th e pdf of 4,,

    f4? ( ,

    ;&

    t),

    is zero for

    II

    0, see Fig. 5 8

    Integration over th e delta function an d over the con-

    tinuous distribution yields

    I $, w ; & t) dl17 = 1 -?(is t). (5.199)

    and

    The joint pdf

    y,

    k;z t) can be decomposed into

    two parts: the first f T ( K & ; g ) is the joint pdf of jJ

    and conditional upo n the fluid being turbulent, the

    second fN(V-&; 5 t s conditional o n th e fluid being

    non-turbulent :

    In terms of fw,(V,&,$,; 5 [)-the joint pdf of U

    and 4,-these two conditional pdf's are

    and

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