Synthesis of 4-Chloro-3-nitrobenzotrifluoride: Industrial thermal runaway simulation due to cooling system failure

Abstract In pharmaceutical and fine chemical industries, fast and strongly exothermic reactions are often carried out in semibatch reactors (SBRs) to better control the heat evolution by the feeding rate. In fact, for such processes, a thermal runaway event may be triggered whenever the rate of heat removal becomes lower than the rate of heat production. Such a dangerous phenomenon consists in an uncontrolled reactor temperature increase that, occurring in practically adiabatic conditions, can trigger secondary undesired exothermic reactions or, worse, decompositions of the whole reacting mixture with consequent reactor pressurization due to uncontrollable gases formation. In this work, dedicated software has been developed and used to simulate a cooling system breakdown in an industrial SBR where the nitration of 4-Chlorobenzotrifluoride is carried out. The mathematical model is able to simulate both reactor temperature and pressure vs. time profiles thanks to a complete description of both the desired reaction and the unwanted reacting mixture decomposition kinetics. Different accidental scenarios have been simulated, showing both the wide different consequences that can arise from the same initiating event and, therefore, the usefulness of a complete simulation of the hypothesized accidental scenario in the frame of a Quantitative Risk Analysis.

[1]  Kamarizan Kidam,et al.  Analysis of equipment failures as contributors to chemical process accidents , 2013 .

[2]  William L. Luyben,et al.  Use of dynamic simulation for reactor safety analysis , 2012, Comput. Chem. Eng..

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

[4]  Hua Wu,et al.  Parametric sensitivity in chemical systems , 1999 .

[5]  Carlo Sala Cattaneo,et al.  Thermochemical stability: A comparison between experimental and predicted data , 2014 .

[6]  Francis Stoessel,et al.  Planning protection measures against runaway reactions using criticality classes , 2009 .

[7]  B. Roduit,et al.  Advanced kinetics-based simulation of time to maximum rate under adiabatic conditions , 2008 .

[8]  John Farquharson,et al.  QRA of chemical reaction systems: The state of the practice , 1997 .

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

[10]  C. Shu,et al.  Using VSP2 to separate catalytic and self-decomposition reactions for hydrogen peroxide in the presence of hydrochloric acid , 2002 .

[11]  F. Stoessel,et al.  What is your thermal risk , 1993 .

[12]  Enrique Velo,et al.  Safe operation of stirred-tank semibatch reactors subject to risk of thermal hazard , 2006 .

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

[14]  J. Markoš,et al.  Steady States Analysis and Dynamic Simulation as a Complement in the Hazop Study of Chemical Reactors , 2005 .

[15]  V. Balakotaiah,et al.  Runaway limits for homogeneous and catalytic reactors , 1995 .

[16]  Fernanda Strozzi,et al.  Generalized Criteria for Boundary Safe Conditions in Semi-Batch Processes: Simulated Analysis and Experimental Results. , 1998 .

[17]  Yong Pan,et al.  Investigation on Thermal Runaway in Batch Reactors by Parametric Sensitivity Analysis , 2011 .

[18]  Klaas R. Westerterp,et al.  The nitric acid oxidation of 2-octanol. A model reaction for multiple heterogeneous liquid-liquid reactions , 2000 .

[19]  R Rota,et al.  Emulsion polymerization of vinyl acetate: safe optimization of a hazardous complex process. , 2011, Journal of hazardous materials.

[20]  Gheorghe Maria,et al.  Evaluation of Critical Operating Conditions for a Semi-batch Reactor by Complementary Use of Sensitivity and Divergence Criteria , 2011 .

[21]  Maria Francesca Milazzo,et al.  Comparison of criteria for prediction of runaway reactions in the sulphuric acid catalyzed esterification of acetic anhydride and methanol , 2012 .

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

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

[24]  Аrcady A. Kossoy,et al.  Simulation-based approach to design of inherently safer processes , 2012 .

[25]  R. Gygax Chemical reaction engineering for safety , 1988 .

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