The models used in the prediction of activity coefficients are important tools for designing
major unit operations (distillation columns, liquid-liquid extractors etc). In the petrochemical
and chemical industry, well established methods such as UNIFAC and ASOG are routinely
employed for the prediction of the activity coefficient. These methods are, however, reliant on
binary group interaction parameters which need to be fitted to reliable experimental data. It is
for this reason that these methods are often not applicable to systems which involve complex
molecules. In these systems, typically solid-liquid equilibria are of interest where the solid is
some pharmaceutical product or intermediate or a molecule of similar complexity (the term
complex here refers to situations where molecules contain several functional groups which
are either polar, hydrogen bonding, or lead to mesomeric structures in equilibrium). In many
applications, due to economic and environmental considerations, a list of no more than 20
solvents is usually considered.
It is for this reason that the objective of this work is to develop a method for predicting the
activity coefficient of complex multifunctional compounds in some common solvents. The
segment activity coefficient approaches proposed by Hansen, MOSCED and the NRTL-SAC
models show that it should be possible to “interpolate” between solvents if suitable reference
solvents are available (e.g. non-polar, polar and hydrogen bonding). Therefore it is useful to
classify the different solvents into suitable categories inside which analogous behaviour
should be observed. To accomplish this, a significant amount of data needs to be collected for the common solvents.
Data with water as a solvent was freely available and multiple sources were found with
suitable data. Both infinite dilution activity coefficient (y∞) and SLE (Solid-Liquid Equilibrium) data were used for model development. The y∞ data were taken from the DDB (Dortmund
Data Bank) and SLE data were taken from Beilstein, Chemspider and DDB. The limiting
factor for the usage of SLE data was the availability of fusion data (heat of fusion and melting
temperature) for the solute. Since y∞ in water is essentially a pure component property it was modelled as such, using the experience gained previously by this group. The overall RMD
percentage (in ln y∞) for the training set was 7.3 % for 630 compounds. For the test set the RMD (in ln y∞) was 9.1 % for 25 fairly complex compounds.
Typically the temperature dependence of y∞ data is ignored when considering model development such as this. Nevertheless, the temperature dependence was investigated and it was found that a very simple general correlation showed moderate accuracy when predicting the temperature dependence of compounds with low solubility. Data for solvents other than water were very scarce, with insufficient data to develop a model with reasonable accuracy. A novel method is proposed for the alkane solvents, which allows
the values in any alkane solvent to be converted to a value in the solvent hexane. The method relies on a first principles application of the solution of groups concept. Quite unexpectedly throughout the course of developing the method, several shortfalls were
uncovered in the combinatorial expressions used by UNIFAC and mod. UNIFAC. These
shortfalls were empirically accounted for and a new expression for infinite dilution activity
coefficient is proposed. This expression is however not readily applicable to mixtures and therefore requires some further attention.
The method allows for the extension of the data available in hexane (chosen since it is a common solvent for complex compounds). In the same way as the y∞ data in water, the y∞ data in hexane were modelled as a pure component property. The overall RMD percentage
(in ln y∞) for the training set was 21.4 % for 181 compounds. For the test set the RMD (in ln y∞)
was 11.7 % for 14 fairly complex compounds. The great advantage of both these methods is
that, since they are treated as pure component properties, the number of model parameters
grows linearly with the number of groups, unlike with mixture models (UNIFAC, ASOG, etc.)
where it grows quadratically. For both the water and the hexane method the predictions of the
method developed in this work were compared to the predictions of UNIFAC, mod. UNIFAC,
COSMO-RS(OL) and COSMO-SAC.
Since water and hexane are not the only solvents of practical interest, a method was
developed to interpolate the alcohol behaviour based on the water and hexane behaviour.
The ability to predict the infinite dilution activity coefficient in various solvents allowed for the
prediction of various other properties, viz. air-water partition coefficient, octanol-water partition
coefficient, and water-alcohol cosolvent mixtures. In most cases the predictions of these
properties were good, even for the fairly complex compounds tested. / Thesis (Ph.D.)-University of KwaZulu-Natal, Durban, 2009.
| Identifer | oai:union.ndltd.org:netd.ac.za/oai:union.ndltd.org:ukzn/oai:http://researchspace.ukzn.ac.za:10413/749 |
| Date | January 2009 |
| Creators | Moller, Bruce. |
| Contributors | Ramjugernath, Deresh D., Rarey, Jurgen. |
| Source Sets | South African National ETD Portal |
| Language | English |
| Detected Language | English |
| Type | Thesis |
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