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ACS <strong>Combinatorial</strong> Science<br />

Figure 15. Advanced QSAR approach in heterogeneous catalysis.<br />

Composition space (left), physicochemical descriptor space (middle)<br />

<strong>and</strong> performance space (right). 140<br />

performance categories. By a preprocessing procedure variables<br />

with a significant projection onto the response space can be<br />

identified, irrelevance eliminated, as well as redundancy <strong>and</strong><br />

multicollinearity addressed. Afterward the data-driven selection<br />

strategies have been applied to obtain an estimate <strong>of</strong> the<br />

differences in variance <strong>and</strong> information content <strong>of</strong> various attributes<br />

including a comparison <strong>of</strong> relative importance. Using probabilistic<br />

neural networks various semiempirical QSAR models have been<br />

created. Machine learning models as neural networks <strong>and</strong> classification<br />

trees have been used by Corma et al. for comparison <strong>of</strong> the<br />

fitting performance to that <strong>of</strong> support vector machines for the<br />

modeling <strong>and</strong> prediction <strong>of</strong> zeolite synthesis, when the gel molar<br />

ratios are used as synthesis descriptors. 141 It was found that support<br />

vector machines models show very good prediction performances<br />

<strong>and</strong> generalization capacity in zeolite synthesis prediction. Overfitting<br />

problems sometimes observed for neural networks may be<br />

overcome by this method. The efficiencies <strong>of</strong> several global<br />

optimization algorithms comparing methods such as GA, evolutionary<br />

strategies, simulated annealing, taboo search <strong>and</strong> GA<br />

hybridized with knowledge discovery procedures have been compared<br />

using the Selox benchmark by Farrusseng, Maschmeyer,<br />

<strong>and</strong> co-workers. 142 Selox st<strong>and</strong>s for the selective catalytic oxidation<br />

reaction <strong>of</strong> carbon monoxide in the presence <strong>of</strong> hydrogen<br />

<strong>and</strong> is investigated for fuel cell applications to relate catalyst<br />

composition <strong>and</strong> reaction temperature effects on the conversion<br />

<strong>and</strong> selectivity <strong>of</strong> CO oxidation. In taboo search, the word taboo<br />

originally coming from the Polynesian language Tongan <strong>and</strong><br />

indicating things, which cannot be touched, because they are<br />

sacred, a list <strong>of</strong> taboo c<strong>and</strong>idate solutions are not repeated in the<br />

subsequent iteration <strong>of</strong> a global optimization algorithm <strong>and</strong> are<br />

updated in each iterative step. The authors find that an adjustment<br />

<strong>of</strong> the size <strong>of</strong> parameter space during different Design <strong>of</strong><br />

Experiment (DoE) stages on the iterations through the highthroughput<br />

optimization cycle bear the risk that synergistic<br />

variables are discarded at an early stage, because their interactions<br />

were not detected. Thus becoming rapidly trapped on a local<br />

optimum or performing too lengthy an optimization may occur.<br />

If a certain number <strong>of</strong> necessary experiments are performed, with<br />

the global optimization algorithms mentioned above the final<br />

(global) optimum is more efficiently achieved <strong>and</strong> guaranteed,<br />

but only a poor underst<strong>and</strong>ing <strong>of</strong> the chemical system in the form<br />

<strong>of</strong> knowledge is obtained. On the other h<strong>and</strong>, the search space<br />

has to have a certain minimum size to apply global optimization<br />

algorithms, so that they are not appropriate for every problem.<br />

A completely different approach for DoE has been suggested<br />

by Schunk, Sundermann, <strong>and</strong> Hibst. 143,144 This is the structure<br />

oriented library design, which was tested with regard to their<br />

usefulness <strong>and</strong> applicability in catalyst screening in two different<br />

research projects with different degree <strong>of</strong> exploratory character,<br />

namely the ammonoxidation reaction for the conversion <strong>of</strong> C 6<br />

feedstocks to adiponitrile intermediates <strong>and</strong> the oxidation <strong>of</strong><br />

acrolein <strong>and</strong> methacrolein to the corresponding acids. Compared<br />

REVIEW<br />

to descriptor-based approaches here the additional information<br />

taken into account for discrimination <strong>of</strong> the catalyst c<strong>and</strong>idates<br />

is limited to structural parameters estimated by X-ray diffraction<br />

techniques prior to <strong>and</strong> after catalytic testing. In this case<br />

the choice <strong>of</strong> the target structure is regarded as crucial to the<br />

success <strong>of</strong> the program. In the first step an initial library was set up<br />

mainly consisting <strong>of</strong> c<strong>and</strong>idates structurally well characterized<br />

<strong>and</strong> known to be catalytically active <strong>and</strong> selective in the reactions<br />

given above. From this initial phase, a lead c<strong>and</strong>idate <strong>of</strong> highly<br />

complex structure was identified by testing. Despite the identification<br />

<strong>of</strong> a high amorphous oxide content with crystalline<br />

portions in this lead composition, again a structure-based approach<br />

was chosen to develop this c<strong>and</strong>idate further. After deconvolution<br />

<strong>of</strong> the lead compound into binary, ternary <strong>and</strong> quaternary oxides<br />

<strong>and</strong> inclusion <strong>of</strong> other element combinations from structural<br />

databases forming the same structure types these potential<br />

c<strong>and</strong>idates <strong>of</strong> less complex nature were taken as reference points<br />

<strong>of</strong> compositional designs to build a multidimensional grid <strong>of</strong><br />

highly crystalline multinary c<strong>and</strong>idate materials. A variation in<br />

stoichiometry, phase composition <strong>and</strong> crystalline nature increases<br />

the diversity <strong>of</strong> the library constituents further on a<br />

systematic basis. Classical DoE elements such as composite<br />

designs facilitate the evaluation <strong>of</strong> the results <strong>and</strong> the approach<br />

may be combined with even more complex methods as artificial<br />

neural networks (ANN) or GA. Problem in this approach may<br />

arise from differences between bulk <strong>and</strong> surface structure, as the<br />

catalytic activity is exclusively related to the latter, but the crystal<br />

(bulk) structure has been here the decisive design parameter.<br />

Perhaps one can argue that both are related, that a certain bulk<br />

structure enables a specific surface structure, which gives the<br />

catalytic activity.<br />

Another general problem in catalytic studies is that not only a<br />

single objective function has to be optimized, a common scenario<br />

is the evaluation <strong>of</strong> response surfaces for conversion as well as<br />

selectivity to a number <strong>of</strong> alternative products. A GA based<br />

multiobjective DoE aided a high-throughput approach to optimize<br />

the combinations <strong>and</strong> concentrations <strong>of</strong> a noble metal-free<br />

catalyst system active in the selective catalytic reduction <strong>of</strong> NO<br />

by propene. 145 A direct comparison <strong>of</strong> single- <strong>and</strong> multiobjective<br />

design <strong>of</strong> combinatorial experiments was also performed for the<br />

optimization <strong>of</strong> a solid catalyst system active in the selective<br />

oxidative dehydrogenation (ODH) <strong>of</strong> propane. 146 The basis <strong>of</strong><br />

the multiobjective optimization was a strength Pareto evolutionary<br />

algorithm (SPEA-2), that is, a Pareto-based algorithm<br />

operating toward two objectives, minimization <strong>of</strong> the distance<br />

toward the Pareto-optimal set <strong>and</strong> maximization <strong>of</strong> the diversity<br />

within this set. Elitism is implemented in SPEA-2 by an additional<br />

archive population composed <strong>of</strong> the best 24 nondominated<br />

individuals during the search, which is used in combination<br />

with the regular population as mating pool. Due to the SPEA-2<br />

features it is not surprising that in a Pareto plot <strong>of</strong> selectivity<br />

versus conversion (Figure 16) the SPEA-2 solutions are well<br />

distributed over Pareto space. The most important element<br />

combinations found in the high conversion <strong>and</strong> high selectivity<br />

region are highlighted. To have a fair comparison, a new<br />

population has been created, denoted as the archive population<br />

<strong>of</strong> the single objective approach. Similar to the way the multiobjective<br />

archive population was created, the single objective<br />

archive population consisted <strong>of</strong> the 24 best catalysts found so far.<br />

The major difference compared to the SPEA-2 archive is that<br />

no Pareto-selection was performed <strong>and</strong> the catalysts were only<br />

selected with respect to their yield. For the single objective approach<br />

593 dx.doi.org/10.1021/co200007w |ACS Comb. Sci. 2011, 13, 579–633

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