TY - JOUR
T1 - Dual role of ferric chloride in modification of USY catalyst for enhanced olefin production from refinery fuel oil
AU - Shirvani, Samira
AU - Ghashghaee, Mohammad
AU - Kegnæs, Søren
PY - 2019
Y1 - 2019
N2 - Herein, ultra-stable Y zeolite (USY) catalysts modified with iron doping (1, 3, and 5 wt%) using FeCl3•6H2O as a precursor have been investigated. Detailed characterization of the synthesized catalysts was implemented through different analytical techniques including XRD, FTIR, UV–vis DRS, NH3-TPD, H2-TPR, N2 physisorption, EDX, FESEM, ICP-EOS, and XRF. The strong Lewis acidity of the precursor bestowed improved acidic properties to the parent USY besides a satisfactory partial dealumination of the zeolite structure. The optimal dispersion and structural properties were obtained in the case of 1 wt% doping of iron, which eventually led to superb olefin productivity (more than 56 wt%) in the upgrading of refinery fuel oil at mild operating conditions (atmospheric pressure and 550 °C). The optimum catalyst (1Fe/USY) has undergone further experiments with varying temperatures and space velocities to assess the apparent kinetics based on the Arrhenius model. A threefold increase in the space velocity (from 18.3 to 54.9 h–1) only slightly reduced the olefin productivity of the catalyst (to 47.1 wt%), which was still notable from a heavy feedstock. Reduction of the reaction temperature to 450 °C led to a decrease in the olefins yield to less than a half (23.3 wt%). Overall, the modified catalysts were capable of producing a high amount of light olefins from heavy fuel oil, with an orientation toward propylene as the most favored building block in the petrochemical industries.
AB - Herein, ultra-stable Y zeolite (USY) catalysts modified with iron doping (1, 3, and 5 wt%) using FeCl3•6H2O as a precursor have been investigated. Detailed characterization of the synthesized catalysts was implemented through different analytical techniques including XRD, FTIR, UV–vis DRS, NH3-TPD, H2-TPR, N2 physisorption, EDX, FESEM, ICP-EOS, and XRF. The strong Lewis acidity of the precursor bestowed improved acidic properties to the parent USY besides a satisfactory partial dealumination of the zeolite structure. The optimal dispersion and structural properties were obtained in the case of 1 wt% doping of iron, which eventually led to superb olefin productivity (more than 56 wt%) in the upgrading of refinery fuel oil at mild operating conditions (atmospheric pressure and 550 °C). The optimum catalyst (1Fe/USY) has undergone further experiments with varying temperatures and space velocities to assess the apparent kinetics based on the Arrhenius model. A threefold increase in the space velocity (from 18.3 to 54.9 h–1) only slightly reduced the olefin productivity of the catalyst (to 47.1 wt%), which was still notable from a heavy feedstock. Reduction of the reaction temperature to 450 °C led to a decrease in the olefins yield to less than a half (23.3 wt%). Overall, the modified catalysts were capable of producing a high amount of light olefins from heavy fuel oil, with an orientation toward propylene as the most favored building block in the petrochemical industries.
KW - Catalytic cracking
KW - Fuel oil
KW - Iron
KW - Light olefins
KW - USY
KW - Zeolite
U2 - 10.1016/j.apcata.2019.05.010
DO - 10.1016/j.apcata.2019.05.010
M3 - Journal article
AN - SCOPUS:85066128194
SN - 0926-860X
VL - 580
SP - 131
EP - 139
JO - Applied Catalysis A: General
JF - Applied Catalysis A: General
ER -