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This methodology is illustrated through our numerical results.
This methodology is illustrated through application to a solvolysis reaction.
This methodology is illustrated via simulation of a regulation problem in a continuous stirred tank reactor.
This methodology is illustrated using ethylene oxide production as a case study.
This methodology is illustrated through application to a solvolysis reaction and to a Menschutkin reaction.
The efficiency of this methodology is illustrated through an heating system benchmark.
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The features of this methodology are illustrated using some simple design examples.
The potential of this methodology was illustrated by oxidation of 100% quinoline and 80% of total sulfur in model oil containing 500 ppmw sulfur and 70% of total sulfur in model oil 1500 ppmw in less than 30 min of reaction, in the absence of solvent.
In this work the methodology is illustrated by means of the case study of ethyl tert-butyl ether production.
In this paper, the methodology is illustrated by a sample simulation of high molecular mass compound growth in an environment (T, H, H2, naphthalene, and acenaphthylene concentrations) of a low-pressure laminar premixed benzene/oxygen/argon flame with an equivalence ratio of 1.8.
Based on the deficiency of the NLP method in obtaining an optimal operating path, this paper presents the knowledge-model (K-M) method in which expert knowledge base is combined with process dynamic model to solve this problem Finally, the methodology is illustrated by an example of raising temperature procedures for a subsystem of charge gas dehydrator regeneration in an ethylene plant.
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