Reactivation of an industrial batch of CoMo/Al2O3 catalyst for the deep hydrotreatment of oil fractions
- Authors: Budukva S.V.1, Klimov O.V.1, Noskov A.S.1, Golovachev V.A.2, Kondrashev D.O.2, Kleimenov A.V.2, Esipenko R.V.3, Kubarev A.P.3, Khrapov D.V.3
-
Affiliations:
- Boreskov Institute of Catalysis, Siberian Branch
- PAO Gazprom Neft
- AO Gazprom Neft-Omsk Refinery
- Issue: Vol 9, No 2 (2017)
- Pages: 136-145
- Section: Catalysis in Petroleum Refining Industry
- URL: https://journal-vniispk.ru/2070-0504/article/view/202514
- DOI: https://doi.org/10.1134/S2070050417020027
- ID: 202514
Cite item
Abstract
The results from industrial tests of technology developed earlier for the reactivation of CoMo/Al2O3 catalyst for the deep hydrotreating of diesel fuel, including the oxidative regeneration of the catalyst with subsequent treatment using organic complexing agents, are presented. Samples of the catalyst, fresh and at different stages of its reactivation, are investigated using a set of analytical and physicochemical methods. The chemical composition, textural characteristics, mechanical strength, structure of the active sulfide component (TEM, XPS) are determined. Catalytic tests are performed that include lifetime tests (360 h) in the hydrotreatment of a straight-run diesel fraction. The restoration of the physicochemical and catalytic properties is observed for a sample subjected to oxidative regeneration with subsequent treatment using organic complexing agents. An industrial batch of deep hydrotreatment catalyst reactivated by this technology is loaded into an L-24-6 industrial plant facility and ensures stable purification of straight-run diesel fuel containing up to 10% of light catalytic cracking gas oil to a residual sulfur content of less than 10 ppm. Comparison of the obtained results and data on the industrial operation of fresh catalysts shows that the technology developed by the Institute of Catalysis and PAO Gazprom Neft ensures almost complete restoration of the properties of the deactivated catalysts.
About the authors
S. V. Budukva
Boreskov Institute of Catalysis, Siberian Branch
Author for correspondence.
Email: zsm@catalysis.ru
Russian Federation, Novosibirsk, 630090
O. V. Klimov
Boreskov Institute of Catalysis, Siberian Branch
Email: zsm@catalysis.ru
Russian Federation, Novosibirsk, 630090
A. S. Noskov
Boreskov Institute of Catalysis, Siberian Branch
Email: zsm@catalysis.ru
Russian Federation, Novosibirsk, 630090
V. A. Golovachev
PAO Gazprom Neft
Email: zsm@catalysis.ru
Russian Federation, St. Petersburg, 190000
D. O. Kondrashev
PAO Gazprom Neft
Email: zsm@catalysis.ru
Russian Federation, St. Petersburg, 190000
A. V. Kleimenov
PAO Gazprom Neft
Email: zsm@catalysis.ru
Russian Federation, St. Petersburg, 190000
R. V. Esipenko
AO Gazprom Neft-Omsk Refinery
Email: zsm@catalysis.ru
Russian Federation, Omsk, 644040
A. P. Kubarev
AO Gazprom Neft-Omsk Refinery
Email: zsm@catalysis.ru
Russian Federation, Omsk, 644040
D. V. Khrapov
AO Gazprom Neft-Omsk Refinery
Email: zsm@catalysis.ru
Russian Federation, Omsk, 644040
Supplementary files
