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Modeling of the venting of an untempered system under runaway conditions
Institution:1. Mary Kay O''Connor Process Safety Center – Qatar, Texas A&M University at Qatar, PO Box 23874, Education City, Doha, Qatar;2. Health and Safety Laboratory, Harpur Hill, Buxton, United Kingdom;1. Mary Kay O''Connor Process Safety Center, Artie McFerrin Department of Chemical Engineering Department, Texas A&M University System, College Station, TX 77843-3122, USA;2. Mary Kay O''Connor Process Safety Center – Qatar, Texas A&M University at Qatar, PO Box 23874, Education City, Doha, Qatar;1. Science Systems and Applications Inc., Hampton, VA 23666, USA;2. NASA Langley Research Center, Hampton, VA 23681, USA;1. Mary Kay O’Connor Process Safety Center, Artie McFerrin Department of Chemical Engineering, Texas A&M University System, College Station, TX 77843-3122, USA;2. Mary Kay O’Connor Process Safety Center – Qatar, Texas A&M University at Qatar, PO Box 23874, Doha, Qatar;1. College of Computer Science & IT, University of Dammam, 31441 Dammam, Saudi Arabia;2. Faculty of Computing, Universiti Teknologi Malaysia, 81310 UTM Johor Bahru, Johor, Malaysia;3. Department of Petroleum Engineering, King Fahd University of Petroleum and Minerals, Saudi Arabia
Abstract:The prediction of the consequences of a runaway reaction in terms of temperature and pressure evolution in a reactor requires the knowledge of the reaction kinetics, thermodynamics and fluid dynamics inside the vessel during venting. Such phenomena and their interaction are complex and yet to be fully understood, especially reactions where the pressure generation is totally or partially due to the production of permanent gases (gassy or hybrid systems). Moreover, these phenomena cannot be easily determined by laboratory scale experiments. In this paper, a dynamic model developed to simulate the behavior of an untempered reacting mixture during venting is presented. The model provides the temperature, pressure and mass inventory profiles before and during venting. A sensitivity study of the model was performed. This modeling work provides some insight regarding the interpretation of the data obtained from untempered system venting experiments. The outcome of this work contribute to improving the design of emergency relief systems for hybrid and gassy systems, where significant progress is still to be made in the experimental and modeling areas.
Keywords:Runaway reaction  Organic peroxide decomposition  Untempered system  Vent sizing  Dynamic modeling  Cumene hydroperoxide
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