HI Georg,

thank you very much for your explanations. We agree with the second part of your e-mail. What do you, would we like to meeting us to try to clarify the open questions? We are still working on similar problems and we can try to optimize it.

Have a  nice weekend,
best wishes,
Rainer

Am 04.12.2015 um 10:29 schrieb [email protected]:

Here is a Mickey Mouse example that shows the what the Dumux diffusion formulation can produce:

I just plotted an imaginary molfraction gradient and 2 gradient of molar density over some spatial domain. For an ideal gas, the molar density is propotional to the gas pressure (ideal gas law).

So the molar density gradient corresponds to a pressure gradient which is again proportional to 1/K (the permeability).

I also plotted the molar concentration which is rho*x.

If only a gradient of the molfraction drives the diffusion, transport will be from right to left. However, it is obvious that for case 2 (high pressure gradient), the concentration has its maximum not at the right boundary but inside the domain. I think this illustrates that Fickian diffusion breaks down even for a binary system in porous media if the permeability is low.

A better approach would probably be the dusty gas model (Stefan-Maxwell + Knudsen diffusion) but I need to check how it is derived. Maybe the same problem can occur when the dusty gas model is used.

Best regards

Georg

*Von:*Dumux [mailto:[email protected]] *Im Auftrag von *Alexander Kissinger
*Gesendet:* Donnerstag, 3. Dezember 2015 16:06
*An:* DuMuX User Forum
*Betreff:* Re: [DuMuX] A fundamental question concerning diffusion in Dumux

sorry one more clarification to the last post:

I wrote:


Mass or molar gradients are only valid if



I meant:

Mass or molar *concentration* gradients [mol_comp/m3] are only valid if



On 12/03/2015 03:56 PM, Alexander Kissinger wrote:

    Dear Dumux,

    one clarification to the last post:

    The driving force for Fickian diffusion is a gradient in the mole
    fractions x [mol_comp/mol_total] as implemented in the Dumux models:
    Diffusive flux: J_D = -rho_molar [mol_total/m3] * D * grad x

    Mass or molar gradients are only valid if
    - the volume of the solute is much smaller than the total
    concentration or molar density [mol_total/m3] and
    - isothermal conditions prevail, i.e. no volume change due to
    changes in temperature

    A detailed explanation can be found in:
    Taylor, Ross, and Rajamani Krishna. /Multicomponent mass
    transfer/. Vol. 2. John Wiley & Sons, 1993.

    Chapter 3.1 and 3.1.1


    Best regards
    Alex



    On 12/03/2015 01:40 PM, Bernd Flemisch wrote:

        Hi,

        I discussed this a bit here with Alex, Holger and Rainer. The
        main point is that Fickian diffusion is described by _molar_
        concentrations [mol/m3], not _mass_ concentrations [kg/m3],
        https://en.wikipedia.org/wiki/Fick's_laws_of_diffusion
        <https://en.wikipedia.org/wiki/Fick%27s_laws_of_diffusion>

        The multiplication by molar/mass density comes then from the
        fact that we balance moles/mass. But it happens outside of the
        gradient.

        This indeed allows diffusion to occur against the mass
        concentration gradient, if that differs from the molar
        concentration gradient like in the setup that you prescribe.

        Kind regards
        Bernd

        On 12/02/2015 10:45 AM, [email protected]
        <mailto:[email protected]> wrote:

            I forgot the attached file…

            *Von:*Dumux
            [mailto:[email protected]] *Im
            Auftrag von *[email protected] <mailto:[email protected]>
            *Gesendet:* Mittwoch, 2. Dezember 2015 10:44
            *An:* [email protected]
            <mailto:[email protected]>
            *Betreff:* Re: [DuMuX] A fundamental question concerning
            diffusion in Dumux

            Hello Dumux,

            I am back with the same question and some more infos. The
            modeling approach for diffusion in Dumux is (in my
            opinion) wrong and gives unphysical results. This is most
            pronounced for diffusion in a gas phase and when the
            intrinsic permeability is low.

            Consider the model setup depicted in Figure1.jpg. In this
            setup the only transport mechanism for H2O from the right
            boundary is diffusion because the sink of N2 is high and
            the advective flow is from left to right. In this setup,
            the pressure will drop to the right while the gradient of
            x_g^H2O is vice versa. However, the concentration of H2O
            will be lower at the right boundary and *diffusion will
            occur from a lower to a higher concentration!*

            This is completely unphysical. There is no reason why the
            component should flow against its concentration gradient.
            The reason for this lies in the formulation of the
            diffusive fluxes:



            Where



            In the Dumux formulation, the second (pressure dependent)
            term on the very right is neglected resulting in the
            possibility that species diffuse against their
            concentration gradient.

            The density gradient is proportional to the pressure
            gradient from left to right while the molfraction gradient
            is vice versa.

            I hope this made things more clear.

            I would recommend to use grad(rho*x) instead of grad(x)
            for the calculation of the diffusive fluxes.

            I am always open for discussion.

            Kind regards

            Georg

            *Von:*Dumux
            [mailto:[email protected]] *Im
            Auftrag von *[email protected] <mailto:[email protected]>
            *Gesendet:* Mittwoch, 25. November 2015 14:30
            *An:* [email protected]
            <mailto:[email protected]>
            *Betreff:* [DuMuX] A fundamental question concerning
            diffusion in Dumux

            Hello Dumuxers,

            I was wondering why the diffusive fluxes in Dumux are
            defined as D*rho*grad(mol-or-massfraction). Typically one
            would use D*grad(c) (e.g. Ficks law) where
            c=rho*mol-or-massfraction. Using the Dumux equation means
            that local differences in the density are neglected for
            diffusive fluxes. Is there any reason/justification for
            this? Or is my thinking just wrong?

            Best regards

            Georg Futter

            ——————————————————————————

            *German Aerospace Center *(DLR)

            Institute of Engineering Thermodynamics | Computational
            Electrochemistry | Pfaffenwaldring 38-40 | 70569 Stuttgart

            Dipl.-Ing. *Georg Futter* | Ph.D. student

            Telefon 0711/6862-8135 | [email protected]
            <mailto:[email protected]>

            www.DLR.de <http://www.DLR.de>




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        IWS, Universität Stuttgart             fax:   +49 711 685 60430

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<mailto:[email protected]>

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    Telefon: +49 (0) 711 685-64729

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Lehrstuhl für Hydromechanik und Hydrosystemmodellierung
Pfaffenwaldring 61
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Telefon: +49 (0) 711 685-64729
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