logo composite agency
 
contact us
simulation analysis [IDC-SAC]
laboratory analysis
discussion forum
 
page 2 [Feb 2008 - May 2007]
page 3 [May 2007 - Jun 2005]
page 4 [Jun 2005 - Aug 2004]
page 5 [Jun 2005 - March 2003]
lifetime prediction pmc ageing
blister pp al pp pipeline
vapour diffusion multilayer laminate
supercritical saturated carbon dioxide storage grp pipeline
chemical resistance polyurethane joint coating
CO2 membranes and storage
on diffusion coefficient
glossary of phsysical - chemical material properties
case stories grp grfp frp
tables on diffusion, chemical resistance and mechanical retention properties
 
compose a reply | list follow ups | subscribe to newsletter | return to overview

definition of the diffusion coefficient


Posting by composite agency on June 01, 2008 at 16:12:45.

The diffusion coefficient or so called diffusivity has the dimensions of [length2 time-1], [m2 s-1]. These dimensions result from the underlying kinetic theory. The diffusion theory states that chemicals move with a certain molecular velocity, [m/s], depending on particle size and temperature, along a free path, [m]. The free path length is determined by the amount of matter per cubic meter. The less matter is available, the longer the available path length. Hence, self diffusion rates of gases are much higher than liquids.

Then, it is hypothesized that the chance of travelling one times the free path distance in the positive x-direction is equal to 1; the chance of travelling two times the free path in the positive x-direction is 1/2; the chance of travelling four times the free path in the positive x-direction is 1/4, and so on. One can imagine that this yields the following expression for the diffusivity:

Since we live in a three dimensional world, we have to add the chance of going into the positive x-direction (we could also have gone into the - x, +y, -y, +z, -z direction):

Watch species diffusie in real life (including a calculation of the diffusion coefficient): the video on Brownian movement.

Diffusion Distance in Fick's Laws

Fick's First Law adds a driving force - the concentration gradient - to the diffusion coefficient. This enables one to calculate the diffusion flux or mass transport in a preferential direction of for example water, a solvent or natural gas into a coating, packaging polymer, multilayer plastic , fibre metal laminate or glass fibre composite. Moreover, by solving the partial differential equation of Fick's Second Law we can define a function c(x,t) that gives the concentration of the diffusing species as a function of time and place in unsteady conditions. As long as the medium is semi-infinite (penetration from one side), the diffusion coefficient of species in polymer, multilayer and composite materials can be calculated from the weighted average distance travelled. This distance is calculated from the concentration function as follows:

With delta c the concentration gradient. The diffusion coefficient now follows from:

If Fick's First Law applies, the penetration depth for small times (Fourier Mass number << 0.1) follows from:

Determination of Diffusion Coefficients

Often the so called time lag method is used to determine the diffusion coefficient of molecules through plastic materials. In this method the polymer or composite sample is exposed on one side to the gas, liquid, solvent or vapour of interest. On the opposite side, the concentration of molecules is continuously measured by use of analytical equipment. At the same time, species are removed on this side to prevent concentration build-up. Then, after a certain time a steady state diffusion flux is obtained. This time relates to a weighted average diffusion distance. If the diffusion coefficient is constant, this steady state distance is calculated as follows:

With delta x is the thickness of the polymer based material. The related time lag formula is then:

From the experiment, the time and distance is known. Hence, the diffusion coefficient can be calculated. The reader is warned that this formula for time lag can applies when (i) diffusion is governed by Fick's First and Second Law (no pressure gradients or other driving forces than concentration gradients involved), (ii) when the diffusion coefficient is constant and not a function of concentration (when the polymer or composite material swells) or distance (such as the case in multilayer and fibre reinforced composite materials)!

References

[1] Einstein, A., Investigations on the theory of the Brownian movement, Dover Publ. (1956)
[2] Frisch, H.L., Time lag in transport theory, Journal of Chemical Physics, 36, 2(1962)
[3] Cranck. J, The Mathematics of Diffusion, Oxford Clarendon Press (1956)
[4] Cranck, J.; Park G.S., Diffusion in Polymers, Academic Press London
[5] Dlubek, G.; et al., Free Volume Variation in Polyethylenes of Different Crystallinities: Positron Lifetime, Density and X-Ray Studies, J. of Pol. Sci., Part B, 40, 65-81 (2001)
[6] Wesselingh J.A.; Krishna R., Mass Transfer in Multicomponent Mixtures, Delft University Press (2000)

Internal Links

-CASE STUDY 1 In this case study we present a novel solution for the prediction of water resistance of reinforced and unreinforced resins, like epoxy, phenolic, polyurethane, vinyl ester and unsaturated polyester resins reinforced with glass or carbon fibres.
-CASE STUDY 2 on hydrogen permeability, diffusivity, solubility in - and corrosion of - multilayer glass reinforced polyamide polymer - high strength steel laminate. The demonsrated methodoloy also applies to adsorption, diffusion and desorption of natural gas (mainly methane), liquefied natural gas (LNG), liquefied petroleum gas (LPG), Carbon Dioxide (CO2) in Epoxy, Polyurethane (PU), Polyphenylene Sulfide (PPS), Polyether etherketone (PEEK), Liquid Crystal Polymers (LQP) and Polyoxymethylene Resin (POM, Acetal Resin)
-WATCH the video on Brownian movement.
-MORE ON TEMPERATURE dependence of diffusion, solubility & permeability.



          follow up posts
    On June 23, 2008 at 17:27:57 ritesh dewan posts:
    Hello, I want to add some analytical information concerning the diffusion coefficient on for example Carbon Dioxide (CO2), Carbonic Acid or Water Vapour in membrane (i.e. Polyimide, PDMS or Sulfonated PEEK), coating or fibre composite applications. There are number of analytical- experimental techniques which can be used to determine the diffusion coefficient through polymer interfaces. They are summarized as follows:

    1. Scanning infrared microscopy
    -infrared microdensitometry
    -scanning infrared microscopy

    2. light scattering
    -optical Schlieren technique
    -spectroscopic ellipsometry
    -dynamic light scattering

    3. Neutron scattering
    -small-angle neutron scattering (SANS)
    -neutron reflection spectroscopy (NRS)

    4.Raman scattering
    -surface-enhanced Raman scattering (SERS)

    5. Infrared spectroscopy
    -external reflection infrared spectroscopy
    -attenuated total reflectance spectroscopy
    -transmission FTIR
    -reflection absorption spectroscopy
    - attenuated total reflection
    microspectrometry.

    6 Other methods
    -Photon correlation spectroscopy
    -Donor-acceptor fuorescence method
    -Small-angle x-ray scattering (SAXS)
    -Electron microprobe analysis
    -Nuclear reaction analysis (NRA)
    -Ellipsometry
    -Electrical Impedance Spectroscopy

    [responses: 5]

      On 18 Aug 2008 at 14:36:09 Akshay Chibber posts:
      Dear Ritesh:

      I have an interest in getting diffusion rates for metal ions through cation exchange membranes or other cationic media (such as ion exchange resins) in an aquous environment. Example: diffusion rate for K+ ions across a 1 cm barrier of sulfonated poly styrene particles, where [K+] High=1M, and [K+] Lo is 0.0.01M (all components are in water, and the resin is in the K+ form). What is the preferred experimental technique to determine the diffuson coefficient of ion in these organic (polymer) membrane materials?

      Regards,
      Akshay Chibber
      [responses: 0]


      On June 24, 2008 at 21:10:17 composite agency posts:
      Many thanks Ritesh for this valuable comment!
      [responses: 3]
        On June 28, 2008 at 00:10:06 ritesh dewan posts:
        You're more than welcome!
        Ritesh
        [responses: 2]
          On 07 Jul 2008 at 11:34:23 Ralph posts:
          I read that Electrical Impedance Spectroscopy (EIS) or Dielectric Sorption Analysis (DSA) is particularly useful for service life prediction of coatings. Diffusion coefficients, but also chemical degradation, corrosion and UV light initiated degradation, can seemingly be evaluated. Does anyone have experience with a continuous Electrical Impedance Spectroscopy (EIS) coating measurement in the field (oil platforms, vessels, bridge, etc.) and the forthcoming results regarding the diffusion coefficient?

          Thanks
          Ralph

          p.s I am mainly interested in polyurethane / epoxy based coatings and exposure to weathering conditions
          [responses: 1]

            On 08 Jul 2008 at 10:46:22 Ritesh Dewan posts:
            Dear Ralph,

            Thank you for your valuable remark on Electrical Impedance Spectroscopy for coating maintenance management, etc. Especially the non destructive character of EIS makes it attractive. Question is whether current simulation capability, such as IDC-SAC, in combination with current library knowledge on materials, still requires a continuous measurement device. Although I like experiment, my personal opinion is that assessment on chemical corrosion rates of coatings and or steel, can readily be solved from behind the desk. In fact, it would be a shame if this would not be so.

            Regards,

            [responses: 0]


    On June 01, 2008 at 16:38:39 rodney posts:
    Diffusion coefficient according free volume theory

    Probably still the best theory for calculation of an unknown diffusion coefficient of a liquid or gas in a polymer, is the free volume theory for diffusion. The theory is developed by Cohen and Turnbull (1959) who considered transport in a liquid of hard spheres. Molecules reside, most of the time, in cages bound by their neighbours. Occasionaly a fluctuation in density opens up a hole within a cage large enough to permit considerable displacement of the molecule contained by it. Succesful diffusive transport occurs if another molecule jumps into the hole before the first can return to its original position. In the model of Cohen and Turnbull, diffusion is treated as translation of a molecule across the void within its cage.

    Diffusion occurs not only as a result of an activation in the ordinary sense, but rather as a result of redistribution of the free volume within the liquid or frozen liquid: a polymer.

    Now, the diffusion activation related theories aren't very useful: some models are too simple (Arrhenius / Van't Hoff) and others are too complex, in the sense that they require too much parameters to fit the eventually experimentally obtained diffusivity figures.

    On the contrary, the free volume approach requires a limited amount of parameters, which can be calculated rather well by using the work from Guggenheim (for the free volume of the liquid) and Positron Lifetime Spectroscopic information (for the free volume in the polymer and resins).

    [responses: 0]


    On June 01, 2008 at 16:53:55 diffusio posts:
    Mass balance for (multicomponent) diffusion

    For studying permeation of one or more gas or liquid components diffusing alone (binary diffuson) or simultaneously (multicomponent) in a polymer or composite material, a mass balance is essential.

    The mass balance is used for interpretation of the diffusion experiment, according to gravimetric methods and gas chromatography measurements and subsequently for application of the diffusive mass transfer in the real life application, such as mass transport through a membrane, containment, pipeline or package.

    Usually Fick's first and second laws are used to balance the driving force (the concentration gradient) with the friction force (the diffusivity).

    This goes well as long as we have [1] binary diffusion + [2] the concentration gradients acting as the only driving force + [3] the solubility obeys Henry Law. If we have to consider i.e. multicomponent diffusion, Fick's laws hardly make any sense.

    The Maxwell-Stefan equation uses the chemical potential gradient as the driving force for diffusing chemicals. The motion with respect to other chemicals (especially the polymer matrix) causes friction. The driving force is equal to the sum of these friction forces, because acceleration effects are negligible in diffusion. [responses: 2]

      On 09 Jul 2008 at 19:57:56 Sandra posts:
      Can you give an example of the application of Maxwell-Stefan diffusion for a hydrogen fuel cell, in which there is - besides a concentration gradient - also an electrical gradient due to proton exchange cathode. Is the Maxwell Stefan diffusion equation particularly useful for hydrogen fuel cell and related equipment?

      Can you give me another example of cathode - anode membrane applications and the use of Maxwell Stefan formulae?

      Sandra
      [responses: 0]


      On June 12, 2008 at 00:20:29 francis posts:
      Can we determine the Maxwell-Stefan diffusion coefficient mathematically from Fick's first and/or second law?

      Thanks,
      Francis
      [responses: 0]




Compose your reply to composite agency below. To respond to other authors, please click their respective posting at "follow up posts".

name:   
subject: 

comments: