Paper Title:
Catalytic Hydrogenation and Hydrocracking of PRO Residual Oil over USY-Zeolite Catalyst
  Abstract

The effect of different contents of Ni loaded on USY-zeolite catalyst and the effect of temperature and hydrogen partial pressure on hydrocracking behavior of PRO residual oil were studied. It was observed that the content of Ni showed a great effect on monocyclic selectivity. The overall conversion decreased at first and then increased with reaction temperature, while the impacts of temperature on monocyclic selectivity varied with hydrogen partial pressure. In addition, the overall conversion increased with the increase of hydrogen partial pressure and the maximum overall conversion was 45.4% at 440°C. The increasing of hydrogen partial pressure is slightly helpful to monocyclic selectivity.

  Info
Periodical
Advanced Materials Research (Volumes 347-353)
Chapter
Chapter 9: Energy Chemical Engineering
Edited by
Weiguo Pan, Jianxing Ren and Yongguang Li
Pages
3710-3715
DOI
10.4028/www.scientific.net/AMR.347-353.3710
Citation
Z. X. Yu, B. Wu, Q. Wu, L. Chen, Z. R. Zhu, "Catalytic Hydrogenation and Hydrocracking of PRO Residual Oil over USY-Zeolite Catalyst", Advanced Materials Research, Vols. 347-353, pp. 3710-3715, 2012
Online since
October 2011
Export
Price
$32.00
Share

In order to see related information, you need to Login.

In order to see related information, you need to Login.

Authors: Gang Li Zhu, Tao Chen, Xue Dong Jiang, Hai Liang Zhang, Bo Lun Yang
Chemical Materials
Abstract:Dehydrogenation process of organic chemical hydrides was improved by modifying the catalyst of nickel-activated carbon (Ni/AC) with lanthanum...
2110