While modern feedback controllers are based on linear models, many processe
s of concern to chemical engineers are non-linear. The models for these pro
cesses are often too complex for non-linear controller design, and their li
nearized counterparts may not adequately represent the process dynamics. Ad
aptive radial basis function neural networks have been implemented in proce
ss estimators and controllers to approximate non-linear functions that desc
ribe the process. Existing algorithms have been proposed which require spec
ification of network properties such as dilation of the basis functions. Th
is work demonstrates that the function representation may be improved by se
lection of an optimal dilation, and presents an algorithm that allows simul
taneous adaptation of dilation and node weights. In order to deal with func
tions that may have more than one dominant dilation, a multiresolution netw
ork adaptation algorithm is proposed. Lyapunov stability is proven for both
strategies, and performance is evaluated for the control of an exothermic
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