The invention discloses a design method of dynamic optimization
control layer output constraints of a dilute
acetone rectification industry. The method comprises the following steps: Step one, for a dilute
acetone rectification industrial model predication
control system with a double-layer structure, solving a
gain model of a stable-state optimization layer of a
model prediction controller; step two, finding out uncertain elements in a
process gain matrix in the
gain model; step three, according to the uncertain elements and
system interference variables, solving an upper boundary of an output constraint reachable set and a lower boundary of the output constraint reachable set; and step four, according to the upper boundary of the output constraint reachable set and the lower boundary of the output constraint reachable set, obtaining the dynamic optimization
control layer output constraints. The design method of the dynamic optimization
control layer output constraints of the dilute
acetone rectification industry, provided by the invention, is applied to a non-regular uncertain
system, guarantees the solution feasibility of the dynamic optimization control layer
model prediction controller and enables the benefits of enterprises to be maximized.