Production of aromatic compounds in the heavy naphtha and light cycle oil ranges: catalytic cracking of aromatics and <scp>C₁₀</scp> naphthenic‐aromatics

Abstract

Abstract BACKGROUND The conversions of bicyclic compounds, both a naphthenic‐aromatic compound (tetralin) and an aromatic compound (naphthalene), as model reactants representative of the heavy gasoline and light cycle oil ( LCO ) cuts in fluid catalytic cracking ( FCC ), were studied to understand the formation of C 10 –C 20 aromatic compounds in gasoline and middle distillates cuts, in view of their impact on the properties of the cuts. A commercial FCC catalyst was used in its fresh, hydrothermally de‐aluminated and equilibrium forms, at 450 °C in a fluidized bed CREC Riser Simulator reactor in the 2–8 s reaction time range. RESULTS Products were C 1 –C 14 hydrocarbons and coke. Based on the product distributions, reaction networks were proposed for both reactants. The reactions considered in the networks were hydrogen transfer, cracking, ring opening and contraction, alkylation and disproportionation. CONCLUSION The load of zeolite in the catalysts and their acidities have the strongest influences on reaction selectivities. In the case of tetralin, the prevalent reaction is hydrogen transfer, which becomes more important as the catalysts are less active, the hydrocarbons with highest yields being C 10 aromatics. Cracking reactions predominate in naphthalene conversion over all the catalysts, a fact which favors mono‐aromatic C 9 − hydrocarbons. These results can help in the design of new FCC catalysts with better selectivity control. © 2014 Society of Chemical Industry