The feasibility of model predictive control (MPC) applied to a laboratory g
as turbine installation is investigated. MPC explicitly incorporates (input
and output) constraints in its optimizations, which explains the choice fo
r this computationally demanding control strategy. Strong nonlinearities, d
isplayed by the gas turbine installation cannot always be handled adequatel
y by standard linear MPC. Therefore, we resort to nonlinear methods, based
on successive linearization and nonlinear prediction as well as the combina
tion of these. We implement these methods, using a nonlinear model of the i
nstallation and compare them to linear MPC. It is shown that controller per
formance can be improved, without increasing controller execution-time exce
ssively.