Simple Monitoring of Semibatch Polymerization Processes: An Integrated Criterion

A number of potential runaway reaction systems of the fine chemical industry (e.g., polymerization processes) undergo significant changes of their physical properties with the reaction extent, resulting in thickening phenomena of the reaction mass and in a consequent decay of the reactor heat-transfer efficiency. In this work, a set of key process indicators have been developed, allowing for monitoring of safe operating conditions of industrial semibatch polymerization reactors without requiring any kinetic characterization of the reaction system. The only required information are the heat of reaction and some fully available process variables that are normally recorded for any industrial reactor. The proposed criterion has been successfully validated using some experimental data measured on an industrial polymerization reactor for the production of polyacrylic rheology modifiers.

[1]  Giuseppe Maschio,et al.  A general criterion to define runaway limits in chemical reactors , 2003 .

[2]  Renato Rota,et al.  Temperature diagrams for preventing decomposition or side reactions in liquid–liquid semibatch reactors , 2006 .

[3]  Klaas R. Westerterp,et al.  Thermally safe operation of a semibatch reactor for liquid-liquid reactions. Slow reactions , 1990 .

[4]  Renato Rota,et al.  Kinetic-Free Safe Optimization of a Semibatch Runaway Reaction: Nitration of 4-Chloro Benzotrifluoride , 2016 .

[5]  K. R. Westerterp,et al.  Thermally safe operation of a cooled semi-batch reactor: slow liquid-liquid reactions , 1988 .

[6]  Marco Derudi,et al.  Topological Criterion To Safely Optimize Hazardous Chemical Processes Involving Arbitrary Kinetic Schemes , 2011 .

[7]  K. Reichert,et al.  Precipitation polymerization of acrylic acid: Kinetics, viscosity and heat transfer , 1993 .

[8]  Marco Derudi,et al.  On the divergence criterion for runaway detection: Application to complex controlled systems , 2014 .

[9]  Rui Wang,et al.  A new criterion to identify safe operating conditions for isoperibolic homogeneous semi-batch reactions , 2017 .

[10]  L. Gigante,et al.  Simple Procedure for Optimal Scale-up of Fine Chemical Processes. II. Nitration of 4-Chlorobenzotrifluoride , 2009 .

[11]  Eugeniusz Molga,et al.  No more runaways in fine chemical reactors , 2004 .

[12]  L. Gigante,et al.  Simple Procedure for Optimally Scaling-up Fine Chemical Processes. I. Practical Tools , 2009 .

[13]  Giuseppe Maschio,et al.  Sensitivity Analysis in Polymerization Reactions Using the Divergence Criterion , 2004 .

[14]  Renato Rota,et al.  Kinetic-Free Safe Operation of Fine Chemical Runaway Reactions: A General Criterion , 2016 .

[15]  Klaas R. Westerterp,et al.  Runaway behavior and thermally safe operation of multiple liquid–liquid reactions in the semi-batch reactor: The nitric acid oxidation of 2-octanol , 2002 .

[16]  Eugeniusz Molga,et al.  Runaway prevention in liquid-phase homogeneous semibatch reactors , 2007 .

[17]  Eugeniusz Molga,et al.  Boundary Diagrams Safety Criterion for Liquid Phase Homogeneous Semibatch Reactors , 2014 .

[18]  Renato Rota,et al.  Safe and Productive Operation of Homogeneous Semibatch Reactors Involving Autocatalytic Reactions with Arbitrary Reaction Order , 2007 .