Issue
Korean Journal of Chemical Engineering,
Vol.31, No.3, 419-426, 2014
Kinetic modeling of hydrocracking reaction in a trickle-bed reactor with Pt/Y-zeolite catalysts
A kinetic model is developed to predict the entire distribution of hydrocarbon products for the hydrocracking reaction with Pt/Y-zeolite catalysts in a trickle-bed reactor. Operating conditions, such as temperature, pressure, and wax and H2 flow rates were varied to evaluate their effects on conversion and distribution, and kinetic parameters were estimated using the experimental data that covers the window of operating conditions. The comparison between experimental data and simulated results corroborated the validity of the developed model, and the quantitative prediction of the reactor performance was clearly demonstrated. To make evident the usefulness of the model, an optimization method, genetic algorithm (GA), was applied, and the optimal condition for the maximum production of C10-C17 was successfully calculated.
[References]
  1. Fernandes FAN, Teles UM, Fuel Process. Technol., 88(2), 207, 2007
  2. Khodakov AY, Chu W, Fongarland P, Chem. Rev., 107(5), 1692, 2007
  3. Collins JP, Font Freide JJHM, Nay B, J. Nat. Gas Chem., 15, 1, 2006
  4. Elizalde I, Rodriguez MA, Ancheyta J, Appl. Catal. A: Gen., 382(2), 205, 2010
  5. Bouchy C, Hastoy G, Guillon E, Martens JA, Oil Gas Sci. Technol., 64, 91, 2009
  6. Callejas MA, Martinez MT, Ind. Eng. Chem. Res., 38(9), 3285, 1999
  7. Klein MT, Hou G, In practical advances in petroleum processing, Ed. by C. S. Hsu, P.R. Robinson, Springer, New York, 187, 2006
  8. Martinez J, Ancheyta J, Fuel, 100, 193, 2012
  9. Moghadassi AR, Amini N, Fadavi O, Bahmani M, Pet. Sci. Technol., 29, 2416, 2011
  10. Pellegrini L, Bonomi S, Gamba S, Calemma V, Molinari D, Chem. Eng. Sci., 62(18-20), 5013, 2007
  11. Qader SA, Hill GR, Ind. Eng. Chem. Proc. Des. Dev., 8, 98, 1969
  12. Baltanas MA, Vansina H, Froment GF, Ind. Eng. Chem. Prod. Res. Dev., 22, 531, 1983
  13. Pellegrini L, Locatelli S, Rasella S, Bonomi S, Calemma V, Chem. Eng. Sci., 59(22-23), 4781, 2004
  14. Gamba S, Pellegrini LA, Calemma V, Gambaro C, Ind. Eng. Chem. Res., 48(12), 5656, 2009
  15. Kim YH, Hwang DY, Song SH, Lee SB, Park ED, Park MJ, Korean J. Chem. Eng., 26(6), 1591, 2009
  16. Gambaro C, Calemma V, Molinari D, Denayer J, AIChE J., 57(3), 711, 2011
  17. Leckel D, Energy Fuels, 19(5), 1795, 2005
  18. Thybaut JW, Narasimhan CSL, Denayer JF, Baron GV, Jacobs PA, Martens JA, Marin GB, Ind. Eng. Chem. Res., 44(14), 5159, 2005
  19. Nasri Z, Binous H, J. Chem. Eng. Jpn., 40(6), 534, 2007
  20. Naji HS, Emirates J. Eng. Res., 13, 81, 2008
  21. Savitzky A, Golay MJE, Anal. Chem., 36, 1627, 1964
  22. Lee MR, Park MJ, Jeon W, Choi JW, Suh YW, Suh DJ, Korean J. Chem. Eng., 28(11), 2142, 2011