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Figure 1.
(a) Hazard identification and (b) reaction device classification of high-risk processes.
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Figure 2.
Diagrammatic sketch of a batch reactor.
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Figure 3.
Schematic set up of the VSP2 adiabatic calorimeter[31].
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Figure 4.
CFD simulation of shortstopping and jet mixers in preventing runaway reactions, (a) solution domain and grid, (b) predicted evolution of average reactor temperature, and (c) locations of shortstopping and jet mixers.
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Figure 5.
Simulation on runaway inhibition of styrene polymerization, (a) inhibited regions at various times, volume average temperature for (b) different amounts of cold diluents and (d) different cold diluent addition locations, and (c) temperature profile of Y-axis.
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Figure 6.
Runaway inhibition of esterification process using encapsulated phase change materials.
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