2003
DOI: 10.1016/s0098-1354(03)00153-4
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Multi-objective optimization of an industrial fluidized-bed catalytic cracking unit (FCCU) using genetic algorithm (GA) with the jumping genes operator

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Cited by 185 publications
(109 citation statements)
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“…Figure 9 and 10 show that increasing of input feed rates and catalyst-to-oil ratio, the gasoline yield decreases, because gas and catalyst velocities increase with increasing of input catalyst temperature, so the catalyst residence time will decrease. The short residence time minimizes gasoline cracking and coke yield (Kasata and Gupta, 2003).…”
Section: Discussionmentioning
confidence: 99%
“…Figure 9 and 10 show that increasing of input feed rates and catalyst-to-oil ratio, the gasoline yield decreases, because gas and catalyst velocities increase with increasing of input catalyst temperature, so the catalyst residence time will decrease. The short residence time minimizes gasoline cracking and coke yield (Kasata and Gupta, 2003).…”
Section: Discussionmentioning
confidence: 99%
“…One of the most popular multiobjective optimization algorithms is the Non-dominated Sorting Genetic Algorithm, NSGA-II 3 , which is a very robust tool and it is easy to implement. However, the principal disadvantage of genetic algorithms, and its variants, is the large amount of computational time that is often required for multiobjective optimization of industrial operations 4 ; this fact without considering if the evaluation of the objective function is computationally expensive. This has led to the development of new strategies or combination of strategies to reduce the required computational time; basically, these strategies are classified as those that modify the parameters of the algorithm, and those using surrogate models.…”
Section: Introductionmentioning
confidence: 99%
“…Amongst various multi-objective adaptations of the genetic algorithm, the nondominated sorting genetic algorithm (NSGA-II) 25 has been widely used in many areas in engineering optimization. A significant contribution in the area of the multi-objective optimization in the field of chemical engineering is due to Gupta and coworkers 26 through various adaptation of NSGA-II to different complex systems such as the polymerization reactor, fluidized bed catalytic cracker, 27 membrane separation, 28 heat integration, 29 etc. As far as multi-objective optimization in crystallization is concerned, the first and the latest effort has been by Sarkar et al 30 for optimization of seeded batch cooling crystallization using NSGA-II for problems involving two and three objectives.…”
Section: Introductionmentioning
confidence: 99%