Feedback control of polymer quality in semi-batch copolymerization reactors

An on-line, nonlinear inferential feedback control strategy for semi-batch emulsion copolymerization reactors is proposed. The proposed strategy features a nonlinear estimator to infer copolymer properties from indirect noisy measurements taken from the process during operation, an on-line implementation of optimal open-loop operating policies for the control of copolymer properties and reactor conditions, and a feedback controller to correct for errors in the recomputed optimal trajectories. In this paper, simulated control of the properties of styrene/butadiene rubber (SBR) is considered. Using knowledge of the modelled chemical reaction mechanisms, a procedure is proposed for developing optimal operating policies based on establishing conditions for maintaining fixed instantaneous copolymer properties or reactor conditions. Well-known univariate approaches are extended to the multivariate case, and new policies are proposed. It is shown that a wide range of copolymer property specifications can be met through the applications of these operating policies. The open-loop feedforward control trajectories required in these policies are simple to compute and, therefore, can be continually recomputed on-line using the improved state estimates provided by the nonlinear state estimator. When the estimated instantaneous conditions or copolymer properties are not at their desired set points, feedback control corrections to the computed open-loop input trajectories are required to eliminate the error. A simple modification to the computation of any open-loop control policy is proposed to introduce feedback control. The modification leads to decoupled, linear first-order responses to estimated set point errors. In the simulation example, the nonlinear inferential feedback control strategy is shown to provide excellent control over copolymer properties, and is demonstrated to the robust to state initialization errors, disturbances and model mismatch. The simple and effective semi-batch control strategy offers a very useful alternative to computationally intensive on-line optimization procedures.

[1]  John Derrick Kozub Multivariable Control: Design, Robustness, And Nonlinear Inferential Control For Semi-Batch Polymerization Reactors , 1989 .

[2]  G. Stephanopoulos,et al.  Multiobjective dynamic optimization of semibatch copolymerization reactors , 1982 .

[3]  E. Kreund,et al.  The structure of decoupled non-linear systems , 1975 .

[4]  Shi-Shang Jang,et al.  Dynamic optimization of batch emulsion polymerization of vinyl acetate—an orthogonal polynomial initiator policy , 1989 .

[5]  C. Kravaris,et al.  Nonlinear State Feedback Synthesis by Global Input/Output Linearization , 1986, 1986 American Control Conference.

[6]  Sirish L. Shah,et al.  Computer optimal control of batch polymerization reactors , 1987 .

[7]  K. S. Knaebel,et al.  Optimization of semibatch polymerization reactions , 1989 .

[8]  Matthew Tirrell,et al.  Composition control of batch copolymerization reactors , 1981 .

[9]  W. H. Ray,et al.  The Control of Copolymer Composition Distributions in Batch and Tubular Reactors , 1969 .

[10]  R. A. Wright,et al.  Nonlinear controllers for trajectory tracking in batch processes , 1989 .

[11]  G. R. Sullivan,et al.  Generic model control (GMC) , 1988 .

[12]  Coleman B. Brosilow,et al.  Nonlinear inferential control , 1988 .

[13]  S. Chen,et al.  Minimum end-time policies for batchwise radical chain polymerization: the piecewise initiator addition policy , 1988 .

[14]  H. Amrehn Computer control in the polymerization industry , 1977, Autom..

[15]  G. E. Eliçabe,et al.  Estimation and control in polymerization reactors. A review , 1988 .

[16]  D. Butala,et al.  Control of Batch Free Radical Polymerization Reactors , 1987 .

[17]  Carlos E. Garcia,et al.  Internal model control. 2. Design procedure for multivariable systems , 1985 .

[18]  Alexander Penlidis,et al.  Multicomponent free‐radical polymerization in batch, semi‐ batch and continuous reactors , 1987 .

[19]  Sirish L. Shah,et al.  Self-tuning and stable adaptive control of a batch polymerization reactor , 1983, Autom..

[20]  E. Freund Fast Nonlinear Control with Arbitrary Pole-Placement for Industrial Robots and Manipulators , 1982 .

[21]  J. A. Biesenberger,et al.  Effect of Temperature Variations on Molecular Weight Distributions - Batch, Chain Addition Polymerizations , 1973 .

[22]  Archie E. Hamielec,et al.  Dynamic modelling of the batch, semi‐batch and continuous production of styrene/butadiene copolymers by emulsion polymerization , 1985 .

[23]  J. Farber,et al.  THE MINIMUM TIME PROBLEM IN BATCH RADICAL POLYMERIZATION: A COMPARISON OF TWO POLICIES , 1986 .

[24]  E. Freund Decoupling and pole assignment in nonlinear systems , 1973 .