|
Type
|
Journal
Article
|
|
Author
|
D.
Ishutenko
|
|
Author
|
P.
Nikulshin
|
|
URL
|
|
|
Series
|
International
Symposium On Advances In Hydroprocessing Of Oil Fraction (Isahof 2015)
|
|
Volume
|
271
|
|
Pages
|
16-27
|
|
Publication
|
Catalysis
Today
|
|
Date
|
August
1, 2016
|
|
Abstract
|
K-Mo/Al2O3
and K-CoMo/Al2O3 catalysts with various amount of potassium were fabricated
using H3PMo12O40, CoCO3 and KOH. The catalysts were tested in hydrotreating
of model fluid catalytic cracking gasoline containing 1000 ppm of sulphur
from thiophene and 36 wt. % of n-hexene-1. Researchers found that potassium
incorporation led to the strong changes in both physical-chemical
characteristics and catalytic behavior of sulfide catalysts.
The use of potassium favored the growth of average slab length and sulfidation degree of metals with selective formation of CoMoS active phase. Addition of potassium also led to the partial poisoning of the active sites that resulted in decrease of catalyst activities compared with the reference Mo/Al2O3 and CoMo/Al2O3 samples. Olefin hydrogenation was more sensitive to potassium than thiophene hydrodesulphurization what resulted in the growth of the dependence of selectivity factor on potassium content in the catalysts. |
Tuesday, August 9, 2016
Relation between composition and morphology of K(Co)MoS active phase species and their performances in hydrotreating of model FCC gasoline
Subscribe to:
Post Comments (Atom)
No comments:
Post a Comment