Determination of Suitable Operating Conditions of Fluid Catalytic Cracking Process by Application of Artificial Neural Network and Firefly Algorithm

Document Type : Research Article

Authors

1 Department of Upgrading Process, Division of Refinery Process Technology Development, Research Institute of Petroleum Industry (RIPI), Tehran, I.R. IRAN

2 Department of Chemical Engineering, MahshahrBranch, Islamic Azad University. Mahshahr, I.R. IRAN

Abstract

Fluid Catalytic Cracking (FCC) process is a vital unit to produce gasoline. In this research, a feed forward ANN model was developed and trained with industrial data to investigate the effect of operating variables containing reactor temperature feed flow rate, the temperature of the top of the main column and the temperature of the bottom of the debutanizer tower on quality and quantity of gasoline, LPG flow rate and process conversion. Eventually, validated ANN model and firefly algorithm which is an evolutionary optimization algorithm were applied to optimize the operating conditions. Three different optimization cases including maximization of RON (as the parameter which demonstrates the quality of the gasoline), gasoline flow rate and conversion were investigated. In order to obtain the maximum level of targeted output variables, inlet reactor temperature, temperature of the top of the main column, temperature of the bottom of debutanizer column and feed flow rate should respectively set at 525,138, 169ºC and 43000 bbl/day. Also, sensitivity analysis between the input and output variables were carried out to derive some effective rule-of- thumb to facilitate the operation of the process under unsteady state conditions. The result introduces a methodology to compensate for the negative effect of undesirable variation in some operating variables by manipulating the others.

Keywords

Main Subjects


[1] Zahedi Abghari S., Alizadehdakhel A., Mohaddecy R.S., Alsairafi A.A., Experimental and Modeling Study
of a Catalytic Reforming Unit
, J. Taiwan. Inst. Chem. Eng. (JTICE), 45: 1411-1420 (2014).
[2] Hayati R., Zahedi Abghari S., Sadighi S., Bayat M., Development of a Rule to Maximize the Research Octane Number (RON) of the Isomerization Production From Light Naphtha, Korean J. Chem. Eng. (KJChE), 32(4): 629-63 5(2015).
[3] Zahedi Abghari S., Shokri S., Baloochi B., Marvast M.A., Ghanizadeh S., Behroozi A., Analysis of Sulfur Removal in Gasoil Hydrodesulfurization Process by Application of Response Surface Methodology, Korean J. Chem. Eng. (KJChE), 28(1): 93-98 (2011).
[4] Zahedi Abghari S., Towfighi Darian J., Karimzadeh R., Omidkhah M.R.,Determination of Yield Distribution in Olefin Production by Thermal Cracking of Atmospheric Gasoil, Korean J. Chem. Eng. (KJChE), 25(4): 681-692(2008).
[5] Heydari M., Ebrahim H.A., Dabir B., Modeling of an Industrial Riser in the Fluid Catalytic Cracking. Am. J. Appl.Sci., 7(2): 221-226 (2010).
[6] Elamurugan P., Dinesh Kumar D., Modeling and Control of Fluid Catalytic Cracking Unit in Petroleum Refinery, IJCCIS, 2(1): 56-59 (2010).
[8] Affum H.A., Adu P.S., Dagadu C.P.K., Addo M.A., Mumuni I.I., Appiah G.K., Coleman A., Adzaklo S.Y., Modeling Conversion in a Fluid Catalytic Cracking Regenerator in Petroleum Refining, Res. J. Appl. Sci. Eng. Technol., 3(6): 533-539(2011).
[10] Dagde K.K., Puyate Y.T., Modeling Catalyst Regeneration in an Industrial FCC Unit, Am. J. Sci. Ind. Res., 4(3): 294-305 (2013).
[11] Baldessae F., Negrao C.O.R., Simulation of Fluid Catalytic Cracking Risers- A Six lump Model, Proceeding of COBM 2005(18th International Congress of Mechanical Engineering), Ouro Preto, MG
[12] Ansari S.H., Bin Rasheed T.A., Mustafa I., Naveed S., Optimization of Fluid Catalytic Cracker for Refining of Sybcrude oil for Production of High Quality Gasoline. IJISET, 1(4): 506-511(2014).
[14] Tarjomannejad A., Prediction of the Liquid Vapour Pressure using the Artificial Neural Network-Group Contribution Method, Iran. J. Chem. Chem. Eng. (IJCCE), 34(4): 97-111 (2015)
[15] Ehsani M.R., Bateni H., Modeling of Oxidative Coupling of Methane over Mn/Na2WO4/SiO2 Catalyst using Artificial Neural Network, Iran. J. Chem. Chem. Eng. (IJCCE), 32(3): 1047-114 (2013)
[17] Esfandyari M., Fanaei M.A., Gheshlaghi R., A.Mahdavi M., Neural Network and Neuro-Fuzzy  Modeling to Investigate the Power Density and Clumbic Efficiency of Microbial Fuel Cell, J. Taiwan Inst. Chem. Eng. (JTICE), 58: 84-91 (2016).
[18] Hadi N., Niaei A., Nabavi S.R., Alizadeh R., Navaei Shirazi M., Izadkhah B., An intelligent Approach to Design and Optimization of M-Mn/H-ZSM-5(M:Ce,Cr,Fe,Ni) Catalyst in Conversion of Methanol to Propylene, J. Taiwan Inst. Chem. Eng. (JTICE), 59: 173-185(2016).
[19] Jiang B., Zhang F., Sun Y., Zhou X., Dong J., Zhang L., Modeling and Optimization for Curing of Polymer Flooding Using an Artificial Neural Network and a Genetic Algorithm, J. Taiwan Inst. Chem. Eng. (JTICE),  45(5): 2217-2224 (2014).
[22] Ronda A., Martin Lara M.A., Almendros A.L., Perez A., Blazquez G., Comparison of Two Models for the Biosorption of Pb(II) Using Untreated and Chemically Treated Olive Stone; Experimental Design Methodologies and Adaptive Neural Fuzzy Inference System (ANFIS), J. Taiwan Inst. Chem. Eng. (JTICE), 54: 45-56 (2015).
[23] Mousavi M., Avami A., Modeling and Simulation of Water Softening by Nanofiltration Using Artificial Neural Network, Iran. J. Chem. Chem. Eng. (IJCCE), 25(4): 37-45 (2006).
[24] Saghatoleslami N., Mousavi M., Sargolzaei J., A Neuro-Fuzzy Model for a Dynamic prediction of Milk ultrafiltration Flux and Resistance, Iran. J. Chem. Chem. Eng. (IJCCE), 26(2): 53-61 (2007).
[26] Bispo V.D.S., Sandra E., Silva R.L., Meleiro L.A.C., Modeling, Optimization and Control of A FCC Unit Using Neural Networks and Evolutionary Method, Engevista, 16(1): 70-      (2014).
[28] Chen C., Yang B., Yuan J., Wang Z., Wang L., Establishment and Solution of Eight-Lump Kinetic Model for FCC Gasoline Secondary Reaction Using Particle Swarm Optimization, Fuel, 86(15): 2325-2332 (2007).
[29] Xin-She Yang, “Nature- Inspired Methaheuristic Algorithm”, 2nd ed., Luniver Press (2010).
[30] Froment Gilbert F., Bischoff Kenneth B., “Chemical Reactor Analysis and Design”, John Wiley & Sons, NewYork (1979).