Mild hydrocracking of 1-methyl naphthalene (1-MN) over alumina modified zeolite

[1]  Joo-Il Park,et al.  Characteristics on HDS over amorphous silica–alumina in single and dual catalytic bed system for gas oil , 2011 .

[2]  M. Pospišil,et al.  Storage stability of FCC light cycle oil , 2010 .

[3]  V. Calemma,et al.  Upgrading of LCO by partial hydrogenation of aromatics and ring opening of naphthenes over bi-functional catalysts , 2010 .

[4]  耕二 吉永,et al.  Ni-Mo担持触媒との組合せによるPt-Pd担持触媒でのLight Cycle Oilの水素化精製 , 2009 .

[5]  H. Yang,et al.  LCO hydrotreating with Mo-Ni and W-Ni supported on nano-and micro-sized zeolite beta , 2009 .

[6]  R. G. Tailleur.  Catalyst Deactivation during Upgrade of Light Catalytic Cracking Gas Oil to Ultralow-Sulfur and Low-Aromatic Diesel , 2008 .

[7]  Kevin J. Smith,et al.  Acidity and deactivation of Mo2C/HY catalysts used for the hydrogenation and ring opening of naphthalene , 2008 .

[8]  A. Corma,et al.  New materials as FCC active matrix components for maximizing diesel (light cycle oil, LCO) and minimizing its aromatic content , 2007 .

[9]  Zisheng Zhang,et al.  Hydrotreating of light cycle oil using WNi catalysts containing hydrothermally and chemically treated zeolite Y , 2007 .

[10]  S. Järås,et al.  Catalytic ring opening of naphthenic structures. Part I. From laboratory catalyst screening via pilot unit testing to industrial application for upgrading LCO into a high-quality diesel-blending component , 2006 .

[11]  W. Li,et al.  Novel Ni2Mo3N/zeolite catalysts used for aromatics hydrogenation as well as polycyclic hydrocarbon ring opening , 2005 .

[12]  Ulf Nylén,et al.  Characterization of alkylated aromatic sulphur compounds in light cycle oil from hydrotreated vacuum gas oil using GC-SCD , 2004 .

[13]  Y. Korai,et al.  An approach to the deep hydrodesulfurization of light cycle oil , 2004 .

[14]  Joo-Il Park,et al.  Hydro-conversion of 1-methyl naphthalene into (alkyl)benzenes over alumina-coated USY zeolite-supported NiMoS catalysts , 2011 .