Affiliation:
1. Department of Chemical Engineering , National Institute of Technology Calicut , Kerala , India , PIN-673601
Abstract
Abstract
In oil refineries, fluid catalytic cracking (FCC) is a major unit consisting of several process variables and multiple products. Since FCC units are given prime importance as they are contributing a large share in profits, the optimal operation of FCC is always desirable while considering the changing economic scenarios with respect to the products. However, optimization of FCC is quite challenging due to the complex nature of the process. In this work, using Aspen HYSYS V9® catcracker module, process data of FCC was obtained using central composite design (CCD). Second order regression equations for the selected responses were obtained using Analysis of variance (ANOVA) approach. The interaction effects of feed flow, feed temperature, feed pressure, air blower discharge temperature and catalyst circulation rate on responses (yield of products) were presented. Further, the optimization was performed based on a multi-response optimization technique in the Design expert software and the optimal values of the input variables were obtained for the chosen objectives (representing various operation scenarios). The optimal operation scenarios that were obtained for the objectives were validated successfully. This work highlights the use of statistics based soft computing techniques for the optimization of complex chemical engineering operations such as FCC.
Subject
Modeling and Simulation,General Chemical Engineering
Cited by
1 articles.
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1. Steady State Analysis of a UOP SBS Fluid Catalytic Cracking Unit in Aspen HYSYS;2023 IEEE International Conference on Recent Advances in Systems Science and Engineering (RASSE);2023-11-08