M. ManimaranS. NagalakshmiV. Chitra
Reactive distillation column is one of the key elements in the process of Petroleum and chemical industries, which is having nonlinear, multivariable and non-stationary characteristics. The conventional controller like PID provides fruitless control action for nonlinear process. This paper deals the design of the various Model predictive controller algorithms to control composition and Temperature of the Reactive distillation column in biodiesel production. Here the Recursive Least square technique is used to estimate the parameters and build the exact model of the Process. The MATLAB policy is used and accomplished of the GPC, SMPC and PID.
Rohit KawathekarJames B. Riggs
Stefan GrünerK. D. MohlAchim KienleE. D. GillesG. FernholzMatthias Friedrich
Stefan GrünerK. D. MohlAchim KienleE. D. GillesG. FernholzFriedrich
Francisco‐Ronay López‐EstradaD. Juárez-RomeroV.M. Alvárado-MartánezC.M. Astorga‐ZaragozaGuillermo Valencia‐PalomoEnrique Quintero-MármolF. Rivas-Cruz