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Table of Contents
Isothermal and Thermal Liquid
Junction Potentials - Theory
Isothermal Liquid Junction Potential Theory
A very common method for checking a
Class 2 reference
electrode is to compare its half cell voltage to that of another reference
electrode known to be behaving properly. The two electrodes are immersed in the
same environment. That environment usually has a different ionic strength from
that in the compartments surrounding the reference electrodes being used. The
electrodes are then connected through a high impedance voltmeter which measures
the voltage difference. That voltage difference is compared to the "expected"
difference. One artifact that can affect the voltage is the isothermal liquid
junction potential. This potential is caused by the differences in cation and
anion mobilities through the porous frits. The diffusion process is caused by
the difference in concentration between the fluid directly surrounding the
electrode and the environment on the other side of the frit. The result is
a potential difference across the frit. The magnitude is a function of the
relative mobilities of the salt constituents through the frit. An example
of estimating this potential is in the section entitled
Isothermal
and Thermal Liquid Junction Potentials - Calculation.
This figure
is an illustration of the geometry creating the isothermal liquid junction potential.
In this case, two identical salts of differing concentration at the same
temperature are separated by a membrane (frit) that allows very restricted
diffusion between the compartments. In this case the ions are singly charged
but any charge is possible as long as electrical neutrality exists in the
compartments. The theory behind the junction potential for this case is as follows.
The concentration gradient between the two compartments creates diffusion
through the frit. The diffusion process itself is irreversible. But, if
the interface movement is slow relative to the experimental time as, for
example, when a frit is present, then the system can be assumed to be at
"equilibrium". The boundary motion can be ignored. A potential is
developed across this boundary because M+ and A-
ions travel at different speeds (have different ionic mobilities). This
potential is the isothermal liquid junction potential. The potential is
actually an irreversible contribution to the overall cell potential.
Values can be very high depending on the differences in mobility of the ions
through the boundary.
The equation for the isothermal liquid junction potential can be written as
(12)
where VLJ is the potential, a is the activity of each ion, t is the
transference number of each cation or anion, z is the charge, and the summation
is over all charged species passing through the frit. The transference number
is the fraction of the charge carried by the ion. It depends on the ion activity
and its diffusion coefficient. The value cannot be easily calculated.
Several models exist for estimating the liquid junction potential. The simplest
is as follows. The integration of equation (12) is carried out across the
junction with the activities being a function of position. The junction
normally encountered in corrosion studies involves an actual separation of
the two fluids
.
The assumption made in this simple development is the transference number
is independent of activity (concentration). If the diffusion is rapid enough,
the boundary may be considered to be a series of mixtures of the two solutions.
The assumption results in two equations depending on whether the two sides of the
frit have the same or different ionic constituents. Note that these equations should
be used with caution. Their applicablility decreases as systems become more
complex.
If the two solutions have the same univalent electrolyte, the equation for
the liquid junction potential becomes
(13)
where t+ is the transference number of the cation. Since the two transference
numbers are a fraction, if they are about equal their value is close to 0.5 and
the liquid junction potential approaches zero.
If two univalent electrolytes are present and they have a common ion, for
example NaCl and KCl, then the liquid junction potential becomes
(14)
where Λ is the equivalent conductance for each salt. The conductance
is a function of concentration. Conductance values along with a review of
the theory of conductance can be found in, for example R. Fernandez-Prini,
"Conductance and Transference Numbers", ch. 5, in "Physical Chemistry of
Organic Solvent Systems", (Covington and Dickinson, ed.), Plenum, 1973.
The liquid junction potential can be expressed in terms of the transference
numbers for the special case that the sum of species remains constant through
the regions of restricted transport.
(15a)
where
(15b)
In equations (15), A and B denote the two solutions, tj is the
transference number in solution A or B depending on superscript, and
aj is the activity coefficient of constituent j. Many of
these values are difficult to estimate. Other theories exist but they
often result in equations far too difficult to evaluate on a routine basis.
Some conclusions about junction potentials are as follows:
- Isothermal liquid junction potentials cannot be easily calculated for systems normally
encountered in corrosion.
- Equations (12) - (15) may provide a gross estimate of the junction potential.
- Temperature will affect the magnitude of the junction potential.
- Junction potentials can be of the order of 0.1V for some systems.
- Establishing a steady state junction potential across a frit can take
hours from time of initial set up. The time depends on how restricted the
diffusion process is through the junction. This time can affect the judgment
of when steady state is reached prior to making a corrosion measurement.
Table of Contents
Thermal Liquid Junction Potential Theory
The corrosion practitioner is often faced with evaluating corrosion at elevated
temperatures. Sometimes these temperatures are higher than the laboratory
reference electrode can withstand. A common approach is to keep the reference
electrode outside of the electrochemical cell with communication being through
a filled capillary between the reference electrode and the cell. A
temperature gradient exists along this capillary because the reference
electrode and cell are at different temperatures. So-called pressure balanced
external reference electrodes as used in autoclave studies
tend to have these characteristics. An example of estimating
this potential is in the section entitled
Isothermal and Thermal Liquid Junction Potentials - Calculation.
This temperature gradient causes material to migrate between the two temperatures.
This migration creates a diffusion gradient. This process has a name, the Soret
effect and falls under the general category of irreversible thermodynamics. For
the case of a single salt which dissolves into two types of ions, the Soret
coefficient σ is given by
(16)
where m is the molality of the salt, T is the absolute temperature, and the
derivative is taken at steady state (signified by the subscript "st"). Since
the ionic mobilities of the salt constituents differ, the diffusion gradient
establishes a potential difference between the hot and cold ends of the capillary.
This potential difference is the thermal liquid junction potential. Values
can be of the order of 0.05V depending on electrolyte, concentration, and temperature
difference.
The case of the single electrolyte in a solvent has been presented in the
literature (A. A. Seys, et al., "The Value of the Thermal Diffusion
Potential in Corrosion Experiments at High Temperature Introduction
of a Thermal Diffusion Coefficient", in "High Temperature High Pressure
Electrochemistry in Aqueous Systems", NACE-4, 1976). For that
case, the potential gradient along the capillary can be expressed in
terms of the mole fraction gradients or temperature gradients as
(17a)
and
(17b)
where n is the mole fraction of constituents 1 and 2 in the salt, h is the
heat of transport, t is the transference number, z is the valence, and x is
the distance. The third term in equation (17a) is the Soret effect.
Calculation of the thermal liquid junction potential in the absence of
any measurements is often not possible. But certain properties of this
potential can have a large effect on the corrosion measurement.
- The larger the temperature difference is between cell and external
reference electrode, the larger is the potential difference.
- The closer the values of the transference numbers between constituents
in the electrolyte, the smaller is the potential.
- The time to establish this potential at steady state can be long,
24 hours being a very reasonable estimate. This time to reach steady state
should be incorporated into the judgment of when steady state has been
reached so the corrosion measurement can proceed.
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