2003
DOI: 10.1016/s0950-4230(03)00003-2
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A general criterion to define runaway limits in chemical reactors

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Cited by 100 publications
(81 citation statements)
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“…To analyze the variation of the temperature and its sensitivity, the model equations (4) and (5) and the sensitivity equations (18) and (19) along with the ICs (6) and (20) are solved together numerically using ODE15s (Gear method) of Matlab 7.1. Both the dependent variable h and the corresponding local sensitivity S(h,h 0 ) can be given as a function of time.…”
Section: Computation Of Local Sensitivity Coefficientmentioning
confidence: 99%
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“…To analyze the variation of the temperature and its sensitivity, the model equations (4) and (5) and the sensitivity equations (18) and (19) along with the ICs (6) and (20) are solved together numerically using ODE15s (Gear method) of Matlab 7.1. Both the dependent variable h and the corresponding local sensitivity S(h,h 0 ) can be given as a function of time.…”
Section: Computation Of Local Sensitivity Coefficientmentioning
confidence: 99%
“…Then, considering the correlation between the state space volume and the divergence of the vector field, the divergence criterion was defined as the sum of the partial derivatives of the mass and energy balance equations with relation to the corresponding state variables [19]. The divergence criterion was then validated for single as well as for multiple reaction types (single, consecutive, parallel, equilibrium), for several types of reactors (batch reactor, semibatch reactor, continuous stirred tank reactor), and for different types of operating conditions (isoperibolic and isothermal) [20]. In subsequent articles [21,22], the most advanced technique has been concentrated on the early detection of runaway conditions based on a reconstruction of the phase space using only one state variable (temperature or pressure).…”
Section: Introductionmentioning
confidence: 99%
“…The mass and energy dimensionless balances (z, , w ) that describe the dynamic behaviour of a well-stirred controlled batch reactor (BR) in which the reaction: A B occurs can be written as [7]: …”
Section: Batch Reactorsmentioning
confidence: 99%
“…This configuration is typical of reaction calorimeters [16] and it has been used in pilot plant reactors [17]. In this case, it is possible to write [7]:…”
Section: Batch Reactorsmentioning
confidence: 99%
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