Molecular-size selective hydroconversion of FCC light cycle oil into petrochemical light aromatic hydrocarbons
•Hydrocracking (HDC) of a hydrotreated light cycle oil was studied to produce light aromatics.•Combinative zeolite supports of BYZ (mixture of H-Beta, mesoporous H-Y and H-ZSM-5) were employed for HDC catalyst.•Mesoporous H-Y promoted large molecules conversion into light aromatics.•Mo-S/BYZ catalys...
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Published in | Catalysis today Vol. 352; pp. 329 - 336 |
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Main Authors | , , , , , |
Format | Journal Article |
Language | English |
Published |
Elsevier B.V
01.08.2020
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Subjects | |
Online Access | Get full text |
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Summary: | •Hydrocracking (HDC) of a hydrotreated light cycle oil was studied to produce light aromatics.•Combinative zeolite supports of BYZ (mixture of H-Beta, mesoporous H-Y and H-ZSM-5) were employed for HDC catalyst.•Mesoporous H-Y promoted large molecules conversion into light aromatics.•Mo-S/BYZ catalyst exhibited molecular-size selective HDC behavior with excellent stability.
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The catalytic hydroconversion of light cycle oil (LCO) from a fluid catalytic cracking (FCC) unit into petrochemical light aromatics was conducted in a fixed-bed down-flow reactor under 6 MPa. A hydrocracking (HDC) study was conducted using pre-hydrotreated LCO (HDT-LCO). Due to the wide molecular size distribution of the aromatic compounds in LCO, which range from mono- to tri+-ring aromatics, a combination of H-ZSM-5 (Z), H-Beta (B) and mesoporous H-Y(Y) zeolite was employed as zeolite supports for the HDC catalysts. The Mo-S/BYZ catalyst was found to achieve higher yield of light aromatics and higher conversion of large molecular-size C11+ heavy aromatics than those for Mo-S/BZ without mesoporous H-Y in the HDC of HDT-LCO. Although the Mo-S/ H-Y catalyst itself did not show selectivity toward light aromatics in the HDC of tetralin, the incorporation of a small fraction of mesoporous H-Y in the HDC catalyst promoted the cracking of large molecular-size C11+ heavy aromatics into light aromatics including benzene, toluene and xylene (BTX). The Mo-S/BYZ catalyst also exhibited an excellent stability over more than 100 h. Hence, the Mo-S/BYZ catalyst, which produced a high yield of BTX-rich light aromatics and demonstrated excellent catalyst stability, represents a promising HDC catalyst for LCO upgrading. |
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ISSN: | 0920-5861 1873-4308 |
DOI: | 10.1016/j.cattod.2019.08.037 |