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Table of Contents
Sorption and Diffusion Effect on Sample Size and Test Duration
One of the critical variables in the Sequential Immersion Test is the duration of each
portion of the test. Though the final equilibrium state or possible steady state movement
of components between the environment and the interior of the material is not necessary,
the mass change at the end of the soak portion and mass change at the end of the drying
portion should be close enough to the "final" mass change that the values extracted from
the curves provide enough of a reasonable estimate of the final state that a prediction
can be made. The question is how close is close. The following discussion provides a
framework for making a gross estimate of the test time. Note that by including additional
information on the final curvature, SEQEXPERT allows some leeway in the choice possibly
decreasing test time.
The process of migration can be divided into two main steps, adsorption onto or desorption
from the surface and diffusion between the surface and the interior. The assumption is
that diffusion of species between the bulk environment and the surface of the nonmetallic
material is rapid so that the amount of material adsorbed on the surface is in equilibrium
with the bulk environment. This assumption is reasonable because the diffusion coefficient
within the material should be several orders of magnitude lower than diffusion in the bulk
fluid. Under these circumstances the concentration difference between the surface and
the interior creates the concentration driving force for migration into and out of the
nonmetallic material. The surface concentration becomes a boundary condition. The
migration, then, is governed by Fick’s laws of diffusion.
Though diffusion is three dimensional, by appropriate choice of geometry one can force one
dimensional diffusion in Cartesian (rectangular x,y,z) coordinates. To do so, the dimension
in the direction of diffusion must be much less than the other dimensions. This choice is
shown in this figure.
The thickness l is much less than the other dimensions. Using
dimensions of 1" to 2" for the width and height and 0.0625" to 0.125" for the thickness
should force diffusion in one dimension, l. Under these circumstances, the equation
in the figure would predict the concentration profile in terms of the mass uptake at time
t and distance l in terms of the mass uptake at infinite time.
This figure .
shows how the concentration profile changes with time and position.
Some important assumptions are that only one component is diffusing, the concentration
difference of this one component is the only force driving diffusion, the structure of
the non-metallic material is uniform, and diffusion is in one direction. One of the
important parameters in the analysis is the dimensionless quantity
where D is the
diffusion coefficient, t is the time, and l is the dimension in the direction of
diffusion (in this case one-half of the total thickness). This quantity is a
dimensionless time. It is the ratio of the actual time to the time that a diffusing
species would travel a distance of radius l or carve out an area of radius l.
This non-dimensional time is the important variable for estimating the needed exposure
time.
One possible method of making this estimate is built on information found in
E. M. Rosen and D. C. Silverman, "Sorption/Diffusion Prediction in Non-metallics
Using Fick’s Law", Corrosion, Volume 46, p. 945, 19901 (450k).
The procedure is as follows. The equation shown in the previous figure above provides
the outline. The assumption is made that the test duration of the soak cycle and the drying
cycle have to be long enough so that if the test time is inserted into
the above equation that equation when solved by regression provide predictions of
the diffusion coefficient and the final mass change at infinite time that are within
a certain defined error of the actual values. This figure .
shows the boundary created by imposing a 10% error between calculated and
actual diffusion coefficient,
a total mass change of 10%, and either a 10% or 0.1% error between the calculated and
actual mass change at infinite time. The region labeled as "Solution obtainable"
is the region in which the test time is long enough that the estimate can be made.
The region labeled as "Solution not obtainable" is the region in which the test time
is not long enough to allow for an estimate to be made. The lines denote the boundary between
the two regions as a function of Diffusion coefficient divided by the square of the
half thickness and the allowable error in mass uptake.
The required thickness as function of soak time and diffusion coefficient or required soak
time as a function of thickness and diffusion coefficient might be estimated from a
plot such as that above. The assumption is that appropriate soaking times are those
that would enable the diffusion coefficient and mass gain at infinite time to be
estimated reasonably well by regression of the analytical solution to the experimental
mass gain data versus time. In other words, the diagonal line in the above figure
would form a minimum for each tolerance. Appropriate test times would lie above and
to the right of the diagonal line.
An example is as follows. Suppose the desire is to design a test so that if a regression
were performed against the measured data using the analytical solution, the error in the
diffusion coefficient and in the mass gain at infinite time would be 10%. In addition,
the estimated total mass gain is 10%. The lower diagonal line would become the
minimum boundary. That line could be used to solve for the thickness as a function
of test time and diffusion coefficient. The results are shown in this figure.
.
The legend in the figure is the test time for soaking in days.
This analysis is limited to
- only one component diffusing into or out of the material
- the concentration difference of this one component being the only force driving
diffusion
- the structure of the non-metallic material being uniform
- diffusion being in one direction
This discussion provides a good framework within which to view
the test and the relationship among the variables thickness, test time, and
diffusion coefficient. The results indicate that the smaller the diffusion coefficient,
the thinner the required sample in order to have interpretable results (mass changes
that reflect long term exposure) in a reasonable length of time. Since diffusion
coefficients in good candidate non-metallic materials are often in the range of less
than 10-11 up to about 10-9 cm2/s, reasonable immersion
test times of the order of
30 to 60 days requires samples to have a thickness of several millimeters.
A quantitative analysis such as that above is far more complicated for a real system.
Very often, more than one species is diffusing into and out of the sample simultaneously.
The result can be an acceleration or deceleration of diffusion depending on the
interaction and motion of the species relative to each other.
Nonmetallic materials may not be uniform meaning that diffusion coefficients may vary
across the specimen. And since the mass loss in a real system is usually caused by
migration of more than one species, the diffusion coefficient estimated from the
total mass loss is probably a composite diffusion coefficient at best which may
have only a limited relationship to the diffusion coefficients of the individual
components. These impediments to designing a quantitative framework within which
to interpret individual tests led to the development of SEQEXPERT as a way to make
predictions from this type of data without needing mathematical analysis or a full
understanding of what components are migrating into or out of the specimen.
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1 © NACE International publication and year shown in citation above. All rights reserved. Displayed with permission from NACE International, Houston, TX (http://www.nace.org). Published in Corrosion, in the month and year shown in the citation above.
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