ISSN: 0256-1115 (print version) ISSN: 1975-7220 (electronic version)
Copyright © 2024 KICHE. All rights reserved

Articles & Issues

Language
English
Conflict of Interest
In relation to this article, we declare that there is no conflict of interest.
Publication history
Received October 16, 2009
Accepted December 18, 2009
articles This is an Open-Access article distributed under the terms of the Creative Commons Attribution Non-Commercial License (http://creativecommons.org/licenses/bync/3.0) which permits unrestricted non-commercial use, distribution, and reproduction in any medium, provided the original work is properly cited.
Copyright © KIChE. All rights reserved.

All issues

Dibenzothiophene hydrodesulfurization over MoP/SiO2 catalyst prepared with sol-gel method

Department of Chemistry, Liaocheng University, Liaocheng, Shandong 252059, P. R. China
gongshw@lcu.edu.cn
Korean Journal of Chemical Engineering, September 2010, 27(5), 1419-1422(4), 10.1007/s11814-010-0234-3
downloadDownload PDF

Abstract

Silica-supported molybdenum phosphide, MoP/SiO2 catalysts with different Mo weight loadings were prepared by temperature programmed reduction of the oxidic catalyst precursors, which were prepared via sol-gel technique using ethyl silicate-40 as silica source. Samples were characterized by X-ray diffraction (XRD), scanning electron microscopy (SEM), BET surface area measurements, and their catalytic activity in hydrodesulfurization (HDS) was tested with dibenzothiophene (DBT) as model compound. XRD analysis revealed the amorphous nature of the catalyst up to 10 wt% Mo loading and the formation of crystalline MoP phase on amorphous silica support with higher Mo loading. BET surface area showed high surface area for catalysts prepared by sol-gel technique with lower Mo content, and the surface area decreased with increasing in Mo loading. The HDS results showed that prepared MoP/SiO2 exhibited high HDS activity and stability toward the catalytic test. Among the series of catalysts prepared, MoP/SiO2 containing 20 wt% Mo was found to be the most active catalyst. And the effects of reaction temperature and hydrogen pressure on conversion and product selectivity were investigated.

References

Oyama ST, J. Catal., 216(1-2), 343 (2003)
Furimsky E, Appl. Catal. A: Gen., 240(1-2), 1 (2003)
Koh JH, Cho A, Lee SI, Moon SH, Korean J. Chem. Eng., 26(4), 999 (2009)
Yamada H, Goto S, Korean J. Chem. Eng., 21(4), 773 (2004)
Liu P, Rodriguez JA, Catal. Lett., 91(3-4), 247 (2003)
Cheng RH, Shu YY, Li L, Zheng MY, Wang XD, Wang AQ, Zhang T, Appl. Catal. A: Gen., 316(2), 160 (2007)
Clark P, Li W, Oyama ST, J. Catal., 200(1), 140 (2001)
Sawhill SJ, Layman KA, Van Wyk DR, Engelhard MH, Wang C, Bussell ME, J. Catal., 231(2), 300 (2005)
Brock SL, Senevirathne K, J. Solid State Chem., 181, 1552 (2008)
Clark P, Wang X, Oyama ST, J. Catal., 207(2), 256 (2002)
Stinner C, Prins R, Weber T, J. Catal., 191(2), 438 (2000)
Phillips DC, Sawhill SJ, Self R, Bussell ME, J. Catal., 207(2), 266 (2002)
Clark PA, Oyama ST, J. Catal., 218(1), 78 (2003)
Oyama ST, Clark P, da Silva VLST, Lede EJ, Requejo FG, J. Phys. Chem. B, 105(21), 4961 (2001)
Shu Y, Oyama ST, Carbon., 43, 1517 (2005)
Wise RS, Markel EJ, J. Catal., 145(2), 344 (1994)
Biradar AV, Umbarkar SB, Dongare MK, Appl. Catal. A: Gen., 285(1-2), 190 (2005)
Shafi R, Hutchings GJ, Catal. Today, 59(3-4), 423 (2000)
Liu YQ, Liu CG, Que GH, Energy Fuels, 16(3), 531 (2002)
Dhandapani B, St Clair T, Oyama ST, Appl. Catal. A: Gen., 168(2), 219 (1998)
Montesmos-Castellanos A, Zepeda TA, Pawelec B, Lima E, Fierro JLG, Olivas A, de los Reyes JA, Appl. Catal. A: Gen., 334(1-2), 330 (2008)

The Korean Institute of Chemical Engineers. F5, 119, Anam-ro, Seongbuk-gu, 233 Spring Street Seoul 02856, South Korea.
TEL. No. +82-2-458-3078FAX No. +82-507-804-0669E-mail : kiche@kiche.or.kr

Copyright (C) KICHE.all rights reserved.

- Korean Journal of Chemical Engineering 상단으로