Effective Coefficients in Fluid Mechanics

One thing is obvious when effective coefficients problem arising for heterogeneous medium. Because the effective coefficients search is the problem of the Upper scale medium consideration, there is no other way to go around the VAT governing equations for formulation of the effective coefficient models.

May be the oldest problem in Fluid Mechanics is the problem of determination of the flow resistance in porous media. This is as that old task as the construction as the craft and industry exists. At the same time, the "state of the art" in here is like defending some experimental data obtained while data reduction was made with the Gauss-Ostrogradsky Theorem (GOT) used as the background tool !

Meanwhile, porous media are Heterogeneous media and by using the HSH-VAT the Momentum 1D equation in the midst of the porous medium filled channel for turbulent (as well as with nonlinear viscosity) flow of incompressible fluid based on the K-theory can be depicted in the form (Shcherban et al., 1986; Travkin and Catton, 1992, 1995a,b)

(1) (1)

A. Closure Modeling for the Integral Resistance Terms with the Simplified VAT and when the Boundary Effects are Taken as in Bulk or Neglected

The nonlocal Upper scale momentum transport equation in porous medium above has been solved so far for quite limited number of morphologies and is the subject of various simulation exercises. That is why the much simpler equations take the role.

So, believe or not, but these Arithmetical models below is the "State of the Art" in Fluid Mechanics up to now, when concerned about the practical application of flow in porous media knowledge. For near 150 years since Darcy publication of the linear dependency for pressure drop and velocity in a porous medium. There are number of models apart of HSP-VAT with differential equations for flow in porous media developed since then. Still, in practice the two or one-term r.h.s. dependency is used everywhere.

There are coefficients in the r.h.s. of these dependencies.

The matter is as usual with the proper coefficients - the flow resistance coefficients.

We did bring as like for already many years the integro-differential VAT governing equations for velocity in porous media to these simplified forms of flow resistance to connect, communicate the homogeneous Darcy and Darcy - Forchheimer dependencies to the simplified VAT equations. That was and is like making a compromise for better understanding and more introduction for usage of simplified, but still more accurate than conventional dependencies the VAT based Flow Resistance in Porous Media formulae.

Few models for momentum transport in porous media were analyzed by Travkin and Catton (1992, 1995a,b, etc.). Momentum equation for laminar regime given by Vafai and Kim (1989) for the middle part of the regenerator's layer can be written as

(2) (2)

while Poulikakos and Renken (1987) equation for turbulent regime looks like

(3) (3)

as well as by Ergun (1952)

(4) (4)

and that simplified obtained using the VAT momentum equation (SVAT)

(5) (5)

where is the friction factor and the form drag, is actually the cross flow form specific surface. The drag terms can be combined for simplicity into a single total drag coefficient to model the flow resistance terms in the general simplified momentum VAT equation

(6) (6)

where is the set of porous medium morphological parameters or descriptive functions (see Shcherban et al., 1986; Travkin and Catton, 1992, 1995a). These correlations of drag resistance can be evaluated for homogeneous properties porous media by experimental relationships for pressure drop, for example, used for packed beds resistance correlations

(7) (7)

The ideal one diameter parallel tubes morphology model yields the following Darcy friction coefficient models (see, for example, Schlichting, 1979)

(8) (8)

(9) (9)

In the above formulae taken that the mean velocity in a vessel (tube) where is equal to the intrinsic value averaged over the REV. A straight equal diameter tube morphology model yields the morphology function ,

(10) (10)

or

(11) (11)

and there results in the Darcy friction factor exact expression

(12) (12)

from this one can easily get the Fanning friction factor for this specific morphology (using 10)

(13) (13)

(14) (14)

from which one obtains for capillary morphology with prevailing skin friction coefficient (Travkin and Catton, 1995a)

(15) (15)

This relation obviously means that the strict consecutive upscale development of porous medium capillary morphology momentum equation brings to the exact same equation (5) which was derived making "downscale" VAT analysis. The well-known friction factor for laminar flow regime in a pipe is

(16) (16)

while the Darcy coefficient is

(17) (17)

It is quite relevant to compare the results of the SVAT 1D momentum equation derived directly from the general form VAT momentum equation with accounting of few simplifications to the equation derived by Blick (1966) for the straight pore with orifice medium morphology by using the conventional fluid mechanics bulk integration over the volume of interest. As one can write down the Blick's equation (5) without the two last terms which reflect the compressibility and mass force influence in the form

(18) (18)

where

The first right hand term in this equation is exactly the Fanning friction factor for the smooth tube with diameter written as

That means that the friction resistance term in the equation by Blick (1966) is exactly the term which reflects friction resistance for the like kind of morphology using the VAT equation closure procedure (Travkin and Catton 1992, 1995a,b) as given above. The friction resistance term in the SVAT equation is

(19) (19)

so

In the second form resistance term in the equation by Blick (18) the drag resistance coeffcient is given by expression

(20) (20)

which does not have any parameters describing the obstacle making that form resistance. Contrary, the VAT conventional closure suggests that this drag resistance coefficient be defined as that commonly used in fluid mechanics

(21) (21)

with form resistance term written in the form

(22a) (22a)

where

(23) (23)

The difference between both form resistance terms is merely due to interpretation of the drag resistance coefficient definition. It is easily can be shown that the morphological characteristics in the drag resistance VAT term (22a) written in the exact form for (as assigned in the Blick's work)

(24) (24)

where is the orifice internal diameter. The last expression when the orifice internal diameter is limiting to , so roughness on the wall becomes vanishing when , and the whole VAT form resistance term is going to zero. Meanwhile, the form resistance term derived by Blick (1966)

(25) (25)

should be assigned equals or close to zero, because it doesn't content any morphological parameters of obstacles, which could bring it to a zero value when physical situation is obviously trends to that value of form resistance. In another characteristic situation when then

which means that the VAT drag resistance coefficient and form resistance term are approaching the definition and value given in work by Blick (1966)

(26) (26)

The later means that an interpretation of flow resistance coefficient and term given by Blick (1966) is just the simplification that accommodate the form resistance of orifice without including of morphological characteristics of orifice itself.

A model representing the slit morphology of a porous medium with the width equal H (and h = H/2) has defined the local friction factor on the slit wall

(27) (27)

(28) (28)

where also for a regular one size slit the bulk velocity value is The morphology ratio for a porous medium morphology model of straight equal slits is

(29) (29)

(30) (30)

where pz is the pitch between slits in z direction.

One needs to remember that at the same time the hydraulic diameter for a slit equal

(31) (31)

but not the dh =2h as adopted in many textbooks (Bird et al., 1960). The Fanning friction factor for this morphology yields factor as

(32)

(32) (32)

identifying that for the smooth slit porous medium morphology

(33) (33)

Here in this subsection we should comment on the key trends and studies related to issues of effective momentum equation and effective coefficients in porous media.

As we have mentioned in our (Travkin and Catton, 1999) study the same character of our final dependencies for averaged effective momentum transport in the porous medium of Straight Parallel Pore Morphology (SPPM)

has with some of the results by Whitaker (1986). In our work the exact solution for different diameter pores medium allowed to exist the very nonlinear along with the linear and creeping flow regimes.

That does not mean that the exact effective resistance dependencies MATH ($17)$

MATH

for the exact averaged (of Upper scale) momentum equation (2), (6)

MATH

MATH

in Travkin and Catton, (1999) and the final equation for averaged pressure and velocity (C.12) (in Whitaker, 1986)

MATH

are obtained for describing the same kind of phenomena in the same kind of SPPM. The only situation with a single pore diameter in porous medium is allowed while the dependency (C.12) was derived based on linear dependencies for fluctuations of averaged variables. This condition fortunately happens in creeping flow regime.

Obviously, in the SPPM with the variety of diameters, the flow regimes and nonlinearities the linear closure methodology ascribed in work (Whitaker, 1986) is not able to solve either the Upper Scale momentum problem or to find out the effective resistance coefficients.

In the SPPM medium that had been shown in Travkin and Catton (1999)

MATH

where $\overline{p}$ and $\overline{U}$ - might be either of usual laminar (creeping) regime flow pattern or of turbulent regime functions. We note, that when the SPPM medium is taken as having only a single diameter pores (tubes) and only with the laminar flow then the second equation (T.SPPM) can be brought to the simplest case presented by equation $(C.12^{\prime }).$

Citing here these two figures from the publication (Travkin and Catton, 1999)

we would like to remind that no other theory or method were able to obtain this kind of effective coefficients. Coefficients that are actually exact in their Upper scale class definitions - because we have here the Upper scale exact solutions for flow in this kind of porous medium - the SPPM medium.

The second after Darcy equation in use and referring is the Forchheimer effective momentum equation for flow in porous media. In the very elaborative study by Whitaker (1996) we had got to notice the main outcome first -

is that for the exact solution of the closure problem one needs actually to solve the full scale Lower (initial homogeneous) scale mathematical statement (for laminar flow regime).

I am glad to confirm here that this statement exactly what we are saying with regard of the closure problem and not only for laminar, but other flow regimes as well, since 1980-th. Our description and basic arguments are just simpler and more straightforward then of Whitaker (1996) - we have been suggesting solving the various kinds of Lower (first) scale mathematical statement in any case, situation. After all - the both Scale Statements are directly tied, and one can not be solved without the other in the Bottom-Up sequence and in the Top-Down sequence often either.

The second issue in the study by Whitaker (1996) about the Forchheimer form of effective momentum equation is the validity of the "best" value Forchheimer coefficient.

In the page 52 we read: "The closure problem represented by Equations (4.3) has been solved by Snyder and Stewart (1966), Sorenson and Stewart (1974), Eidsath (1981), Sangani and Acrivos (1982), Zick and Homsy (1982), Edwards et al. (1991), Quintard and Whitaker (1995), and others for arrays of spheres and cylinders. For uniform arrays of spheres, the Darcy's law permeability tensor determined by Equation (4-3e) is isotropic, thus is a single distinct component that can be compared with Equation (5.6) arranged in the form

MATH

so, this is the constant permeability coefficient depending only on the morphology properties.

Meanwhile, we have shown in our (Travkin and Catton, 1999) that this coefficient is the function by purely solving the problem with SPPM medium. And even the nonlinear function in the case of three flow regimes or when just laminar and turbulent regimes are present in such a simple medium.

And what is more important that the experiments and modeling in mentioned studies were made with the homogeneous physics analysis and data reduction.

That alone makes the comparison the issue of verification of basic dependencies laying in the ground of corresponding theoretical studies, highly questionable.

The HSP-VAT scaling approach allowed in 90-th for the first time to get the generalized plots of flow resistance curves in which the different scale and method studies had been brought together for combined observation -

MATH

We need to say here that this kind of plots no other theory were able to produce so far for momentum transport in porous media.

Continue this topic on the Upper scale effective momentum transport coefficients we would like to say that the first case-study of initial attempt on providing the combined theoretical and experimental HSP-VAT two scale investigation of flow and heat transfer in the porous medium had been explained and has a certain level of detail in the following sub-section -

  • - "Case-Study - Design of Porous Recuperator's Flow Resistance and Heat Exchange Properties"

    We did only some preliminary work-study based on the SVAT, the learning curve for architects is a great problem usually for application of the HSP-VAT. The amount of knowledge in HSP-VAT studies for any level of participants is outstanding and usually is an obstacle for performance.

    That is why I am not a strong supporter of that study, and consider it as just the first martin that could show the unique usefulness, while for some features that still have been obtained for the first time among the HSP-VAT results.

    The piece of text below might be helpful in studying the various HSP-VAT forms of Upper scale momentum equations along with the some analysis of the problem:

    Effective Pressure Loss Coeffcients for Capillary Morphologies with Regular and Random Morphological Characteristics ( 97K)

    More on VAT methods applicable and used for heterogeneous media effective coefficients determination can be found in Thermal_Physics/Effective_Thermal_Properties

    Through the last more than ten years, mostly because I was affiliated with UCLA, I was careful when emphasized my opinion and mathematics with regard of homogeneous "effective" coefficients for heterogeneous media. The common knowledge and use coefficients. We published few works with the two scale VAT analysis of the problem, as those referred above and below, but no strong message was sent?

    Nowadays, especially when after 2002 the few more common textbooks known problems were solved as they should be - on the two scales, see in -

  • - "When the 2x2 is not going to be 4 - What to do?"

  • - "Globular Morphology Two Scale Electrostatic Exact Solutions"

  • - "Two Scale EM Wave Propagation in Superlattices - 1D Photonic Crystals."

  • - "Classical Problems in Fluid Mechanics"

  • - "Classical Problems in Thermal Physics"

    there is the belief that then we serve to the good purpose when stressing out following the all above information and proofs, as well as to the mathematical analysis in -

  • - "Effective Coefficients in Electrodynamics"

    that

    1) The all effective coefficients obtained for heterogeneous media with mathematics based on the homogeneous GO theorem give incorrect results!

    The actions ought to be corresponding to this message.

    References and Bibliography (some):

    Bird, R. B., Stewart, W. E. and Lightfoot, E. N., Transport Phenomena, Wiley, (1960)

    Blick, E. F., "Capillary-orifice model for high speed flow through porous media," I & EC Process Design And Development, Vol.5, No.1, pp. 90-94, (1966)

    Ergun, S., "Fluid flow through packed columns," Chemical Engineering Progress, Vol. 48, pp. 89-94, (1952)

    Shcherban, A.N., Primak, A.V., Travkin, V.S., "Simulation of Mass- and Heat Transfer Under Atmospheric Air Pollution in Towns and Industrial Centers", Prom. Teplotekhnika, Vol.5, No.4, pp.96-104, (1983), (in Russian)

    Primak, A.V., Shcherban, A.N. and Travkin, V.S., "Turbulent Transfer in Urban Agglomerations on the Basis of Experimental Statistical Models of Roughness Layer Morphological Properties," in Trans. World Meteorological Organization Conference on Air Pollution Modelling and its Application, Geneva, Vol. 2, pp.259-266, (1986)

    Scherban, A.N., Primak, A.V., and Travkin, V.S., "Mathematical Models of Flow and Mass Transfer in Urban Roughness Layer," Problemy Kontrolya i Zaschita Atmosfery ot Zagryazneniya, No. 12, pp. 3-10, (1986), (in Russian)

    Travkin, V.S. and Catton, I., "Models of turbulent thermal diffusivity and transfer coefficients for a regular packed bed of spheres," Procs., 28th National Heat Transfer Conference, San Diego, CA, ASME, HTD-Vol. 193, pp. 15-23, (1992)

    Travkin, V. S., Catton, I., and Gratton, L., "Single phase turbulent transport in prescribed non- isotropic and stochastic porous media," HTD Vol. 240, Heat Transfer In Porous Media, ASME, pp. 43- 48, (1993)

    Travkin, V.S. and Catton, I., "A two temperature model for turbulent flow and heat transfer in a porous layer," Journal of Fluids Engineering, Vol. 117, pp. 181-188, (1995)

    Travkin, V. S. and Catton, I., "Porous Media Transport Descriptions - Non-Local, Linear and Non-linear Against Effective Thermal/Fluid Properties," Advances in Colloid and Interface Science, Vol. 76-77, pp. 389-443, (1998)

    Travkin, V. S., Catton, I., and Hu, K., "Channel Flow In Porous Media In The Limit As Porosity Approaches Unity" in Proc. ASME HTD-Vol. 361-1, Vol. 1, pp. 277-284, (1998)

    Travkin, V.S. and Catton, I., "Nonlinear Effects in Multiple Regime Transport of Momentum in Longitudinal Capillary Porous Medium Morphology", J. Porous Media, Vol. 2, No.3, pp. 277-294, (1999)

    Travkin, V.S. and Catton, I., Transport phenomena in heterogeneous media based on volume averaging theory, Advances in Heat Transfer, New York, Academic Press, Vol. 34, pp.1-144, (2001)

    Travkin, V.S., Hu, K., and Catton, I., ''Exact Closure of Hierarchical VAT Capillary Thermo-Convective Problem for Turbulent and Laminar Regimes," in Proc. Intern. Mech. Engin. Congress and Exposition (IMECE'2001), IMECE/HTD-24261, pp.1-12, (2001)

    Whitaker, S., "Flow in porous media I: A theoretical derivation of Darcy's Law," Transport in Porous Media, Vol. 1, pp. 3-25, 1986.

    Whitaker, S., "The Forchheimer Equation: A Theoretical Development," Transport in Porous Media, Vol. 25, pp. 27-61, 1996.

  • These publications below also are relevant to the Effective Coefficients topic, in spite of the content which is mostly from another physical field.

    Travkin, V. S. and Ponomarenko, A. T., "The Non-local Formulation of Electrostatic Problems for Sensors Heterogeneous Two- or Three Phase Media, the Two-Scale Solutions and Measurement Applications -1," Journal of Alternative Energy and Ecology, No. 3, pp. 9-19, (2005).

    Travkin, V. S. and Ponomarenko, A. T., "The Non-local Formulation of Electrostatic Problems for Sensors Heterogeneous Two- or Three Phase Media, the Two-Scale Solutions and Measurement Applications - 2," Journal of Alternative Energy and Ecology, No. 4, pp. 9-22, (2005).

    Travkin, V. S. and Ponomarenko, A. T., "The Non-local Formulation of Electrostatic Problems for Sensors Heterogeneous Two- or Three Phase Media, the Two-Scale Solutions and Measurement Applications - 3," Journal of Alternative Energy and Ecology, No. 5, pp. 34-44, (2005).


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