TY - JOUR
T1 - Accelerated pre-coking of NiMo/Γ-Al2O3 catalyst
T2 - Effect on the hydroprocessing activity of vacuum residue
AU - Kohli, K.
AU - Prajapati, R.
AU - Maity, Samir K.
AU - Sau, M.
AU - Sharma, Brajendra K.
N1 - Funding Information:
K. Kohli acknowledges Department of Science and Technology (DST) for fellowship and community CSIR-Indian Institute of Petroleum (CSIR-IIP) for the technical and scientific support. K. Kohli also acknowledges the financial support from R&D Indian Oil Corporation (IOC), Faridabad.
Publisher Copyright:
© 2018 Elsevier Ltd
PY - 2019/1/1
Y1 - 2019/1/1
N2 - A pre-coking process for acceleration of hydrotreating catalyst deactivation is proposed in this work. An artificial pre-coked catalyst is synthesized by using methylnaphthalene as a coke precursor. During the pre-coking process, coke precursor got cracked into smaller aromatic hydrocarbons which penetrates into the pore cavity and covers the active sites. The carbon-coated catalyst has been characterized using N2-sorption isotherms, thermogravimetric analyser (TGA), X-ray electron microscopy (XPS), scanning electron microscopy (SEM), and high resolution-transmission electron microscopy (HR-TEM). The activity of the carbon-coated catalyst has been evaluated using vacuum residue as feed and results were compared with fresh catalyst. The findings indicate that proposed methodology is able to deactivate the catalyst effectively. It also indicates that proposed pre-coking process can predict the causes of catalyst deactivation in advance. Kinetic parameters of hydrodesulfurization (HDS) reactions are also estimated. The quality of the hydrotreated products at different reaction temperature is also studied. The amount of aromatic and resin are higher in the products obtained with carbon coated catalyst.
AB - A pre-coking process for acceleration of hydrotreating catalyst deactivation is proposed in this work. An artificial pre-coked catalyst is synthesized by using methylnaphthalene as a coke precursor. During the pre-coking process, coke precursor got cracked into smaller aromatic hydrocarbons which penetrates into the pore cavity and covers the active sites. The carbon-coated catalyst has been characterized using N2-sorption isotherms, thermogravimetric analyser (TGA), X-ray electron microscopy (XPS), scanning electron microscopy (SEM), and high resolution-transmission electron microscopy (HR-TEM). The activity of the carbon-coated catalyst has been evaluated using vacuum residue as feed and results were compared with fresh catalyst. The findings indicate that proposed methodology is able to deactivate the catalyst effectively. It also indicates that proposed pre-coking process can predict the causes of catalyst deactivation in advance. Kinetic parameters of hydrodesulfurization (HDS) reactions are also estimated. The quality of the hydrotreated products at different reaction temperature is also studied. The amount of aromatic and resin are higher in the products obtained with carbon coated catalyst.
KW - Accelerated deactivation
KW - Carbon coated catalyst
KW - Hydrodesulfurization
KW - Pre-coking process
KW - Residue hydrocracking
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U2 - 10.1016/j.fuel.2018.08.026
DO - 10.1016/j.fuel.2018.08.026
M3 - Article
AN - SCOPUS:85051387262
SN - 0016-2361
VL - 235
SP - 437
EP - 447
JO - Fuel
JF - Fuel
ER -