3
high-temperature. Under certain operating conditions, a local oxidizing environment can form within the reactor,
leading to the deactivation of Ni due to NiO being present. Thermodynamics can predict the conditions at which this
can occur [68]. However, in general, it is still a challenge to obtain reliable or accurate thermodynamic parameters
for strongly correlated oxide materials, especially when they deviate form the bulk limit such as in nanoparticles.
Methane has an estimated greenhouse warming potential (GWP 100) of 27.9 [69], meaning its emissions contribute
significantly to global warming and climate change; it is therefore necessary to reduce them wherever possible. Among
the many different technologies for methane abatement, methane combustion catalysts based on palladium can be
found. Such technologies include after-treatment for combustion of natural gas engines (CNG) and diesel oxidation
catalysts (DOC) as well as in mine ventilation systems.
In the above applications, methane is efficiently combusted over palladium (or alloyed) oxide catalyst to produce
H2O and CO2, with activity in this process influenced by a number of factors. A technical target in practical catalysis
is to reduce the temperature at which this occurs, allowing for a lower operating temperature and more efficient
handling of emissions. Partial oxidation can sometimes occur, and may indeed be desirable in the development of
processes to produce precursors for more complex chemicals. The ability to simulate accurately not only the activity
but also the selectivity, which is a measure of a catalyst’s ability to promote the formation of the desired product(s)
over other possibilities, is crucial to the prediction of new catalysts.
Figure 1(a) shows a schematic of a typical catalyzed reaction. The presence of a catalyst provides additional
reaction coordinates, or reaction intermediates, with their own activation energies (ET S1,ET S2). For an effective
catalyst, these energies are necessarily lower than the uncatalyzed activation energy Ea. In the case of heterogeneous
catalysts, reaction intermediates are typically adsorption steps, where one or more of the reactants binds to a surface
site of the catalyst. Depending on the complexity of the reaction mechanisms, there may be a large number of these
intermediates as well as branches and side reactions that must be considered when studying a reaction in order to
determine the key step(s). It is often necessary to find these steps, which govern the activity and/or selectivity of
a catalyst, as in doing so, the problem is reduced to fewer dimensions and descriptors that facilitate a more rapid
study. For example, in a kinetic analysis the largest activation energy is usually of most interest, as this will be the
rate determining step. Whilst this knowledge may be well established in well known reactions, it can be necessary
to perform many calculations in more novel applications. Furthermore, whilst the accuracy of current computational
approaches may be good enough to predict trends in similar systems, obtaining chemical accuracy and absolute values
for detailed kinetic studies remains a challenge. Figure 1(b) shows a typical set of model systems that would be used
to estimate the energetics of a heterogeneous catalytic process.
When running simulations of a catalyst, consideration needs to be made of the question at hand and the level of
accuracy that is needed. Broadly speaking, we are interested in activity, selectivity and stability. When simulating
activity, we often need a kinetic model which can provide rates or turn-over frequencies. If we are interested in
screening for materials, it is often sufficient to correlate these rates with descriptors [71].
For example, following the Sabatier principle [72], which is employed primarily for materials screening, calculating
the (heterogeneous) catalytic activity of a material is performed by determining the binding strengths of the reactants,
products and any important intermediates of a given reaction with the surface of that material. These binding
strengths can be determined from energy calculations using a wide variety of models, each with their own trade-offs
between accuracy, transferability and computational cost.
However, if we are interested in predicting reactor performance or process conditions then we need significantly
greater precision in the simulated parameters. Likewise, simulating the often subtle differences in competing reactions
(which result in different products) typically requires greater accuracy in calculations to predict selectivity.
Whilst the questions of activity and selectivity are crucial for a material’s function as a catalyst, when looking
for a technical solution, the question of stability becomes critical. Catalysts often need to operate over many years
under harsh conditions (high temperature, pressure, contaminated conditions and, in the case of electrocatalysis,
high potentials and corrosive environments). The simulation of stability introduces a whole range of other problems;
for instance, predicting morphological changes and thermal degradation of a catalyst requires a large number of
calculations, often of large model systems, to allow sintering of nanoparticles or ceramic supports to be conducted.
Material complexity (e.g. simulation of realistic metal/ceramic interfaces), bridging time and length scales where
accurate atomic-scale materials properties can be fed into multi-scale models, are all open challenges in this area.
DFT is one of the most successful and widely used models for calculating the energies of molecular and solid state
systems relevant to industrial processes. It is an ab initio method that uses functionals of the electronic density to
calculate energy rather than attempt to deal directly with the many-body wavefunction. In KS-DFT, the electronic
density is constructed using a fictitious set of non-interacting single electron wavefunctions and approximating an
unknown correction term. This term, known as the exchange-correlation (XC) functional, includes exchange and
correlation effects as well as discrepancy between the real and non-interacting kinetic energy. There are many choices,
though all of them approximated, for its form.
Ultimately, it is the use of single-particle wavefunctions in DFT that leads to some of its most prominent short-