1. Thermal Runaway Limit of Tubular Reactors, Defined at the Inflection Point of the Temperature Profile;Bashir;Ind. Eng. Chem. Res.,1992
2. Nonlinear and robust control of PDE systems: Methods and applications to transport-reaction processes;Christofides,2001
3. Boundary control for an industrial under-actuated tubular chemical reactor;Del Vecchio;Journal of Process Control,2005
4. Eigenberg, G. (1975), Influence of the Wall on the Dynamic Behavior of Homogeneous Tubular Reactors with a Highly Exothermic Reaction, Chemical Reaction Enginng-II Ch3, Advances in chemistry series, 133, 477488.
5. Estimation structure design for staged systems;Fernandez;Journal of Process Control,2012