Mathematical Modelling and Control of a Fluid Catalytic Cracking Unit

Autores/as

  • Ademola S. O. Autor/a
  • Paul E. O. Autor/a

Resumen

Using MATLAB software, the Matrixes Laboratory developed a model to simulate the performance of an industrial Fluidized Catalytic Cracking (FCC) unit in both steady and dynamic states. This model is intended for future applications in control studies and real-time optimization. The study presents a dynamic model for an R2R-type FCC unit, incorporating the riser, stripper/disengager, regeneration system, and catalyst transport lines. Material, energy, and pressure balances were performed for each of these sections. Simulation results for both steady and dynamic states are presented and qualitatively compared with those from previous FCC models.

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Referencias

Ahmed, A. O. M., Maulud, A. S., Ramasamy, M., & Mahadzir, S. (2010). Steady state modeling and simulation of the riser in an industrial RFCC Unit. Journal of Applied Sciences, 10(24), 3207–3214.

Arbel, A., Rinard, I. H., Shinnar, R., & Sapre, A. V. (1995). Dynamic and control of fluidized catalytic crackers. 2. Multiple steady states and instabilities. Industrial & Engineering Chemistry Research, 34, 3014–3026.

Elamurugan, P., & Dinesh, K. D. (2010). Modeling and control of fluid catalytic cracking unit in petroleum refinery. International Journal of Computer Communication and Information System, 2(1), 55–59.

Gauthier, T., Bayle, J., & Leroy, P. (2000). FCC: Fluidization phenomena and technologies, oil & gas science and technology – A review. IFP, 55(2), 187–207.

Han, I. S., & Chung, C. B. (2001). Dynamic modeling and simulation of a fluidized catalytic cracking process. Part II: Property estimation and simulation. Chemical Engineering Science, 56, 1973–1990.

Jafar, S., Ahari, A. F., & Khaled, F. (2008). A mathematical modeling of the riser reactor in industrial FCC unit. Petroleum and Coal, 50(2), 15–24.

Malay, P., Milne, B. J., & Rohani, S. (1999). The modified dynamic model of a riser type fluid catalytic cracking unit. The Canadian Journal of Chemical Engineering, 77, 169–179.

NNPC. (1987). Port Harcourt Refinery Company (PHRC) Project, Area 3 FCCU, Project No. 9465A. Nigerian National Petroleum Corporation Process, 16, 1–205.

Rajkumar, G., Vineet, K., & Srivastava, V. K. (2005). Modeling and simulation of fluid catalytic cracking unit. Reviews in Chemical Engineering, 21(2), 95–131.

Souzaa, J. A., Vargasa, J. V. C., Von Meiena, O. F., & Martignonib, W. (2003). Numerical simulation of FCC risers. Engenharia Termica, 4, 17–21.

Vale, H. (2002). Development of a simulator for a complete R2R catalytic cracking unit: IFP Report.

Wei, J., & Kuo, J. C. W. (1969). A lump analysis in monomolecular reaction systems: Analysis of the exactly lumpable system. Industrial & Engineering Chemistry Fundamentals, 8, 114–123.

Xu, O., Su, H., Mu, S., & Chu, J. (2006). 7-lump kinetic model for residual oil catalytic cracking. Journal of Zhejiang University Science A, 7, 1932–1941.

Yousuo, D. (2015). A study of the ten-lump kinetic model in the fluid catalytic cracking unit using COMSOL Multiphysics. International Journal of Applied Science and Technology, 5(5), 81–91.

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Publicado

2015-09-25

Cómo citar

Mathematical Modelling and Control of a Fluid Catalytic Cracking Unit. (2015). Nigerian Journal of Oil and Gas Technology, 1(2), 95-103. https://rsustnjogat.org/ojs/index.php/home/article/view/30