Application of a New Catalyst Deactivation Model for Residue Hydrotreating

被引:0
作者
Zhang Kui [1 ]
Nie Hong [1 ]
Dai Lishun [1 ]
机构
[1] SINOPEC, Res Inst Petr Proc, Beijing 100083, Peoples R China
关键词
residue; hydrotreating; hydrodesulfurization; kinetic model; deactivation model; HYDROPROCESSING MULTICATALYST DEACTIVATION; HEAVY CRUDE-OIL; KINETIC-MODEL; DEPOSITION; COKE;
D O I
暂无
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
This article reports a new catalyst deactivation model for residue hydrotreating technology (RHT) with three adjustable parameters, named as "active-region-migration model". The active-region-migration model is proposed to describe the catalyst deactivation of RHT where the catalysts are deactivated due to metal loading. Along with the lumped reaction kinetics, the deactivation model can be applied to simulate the hydrogenation reaction performance in RHT. Industrial data from a commercial RHT unit show reasonably good agreements with the model calculations. Essentially, the active-region-migration model can separately simulate the catalytic-activity-change of each hydrogenation reaction during the whole run of RHT, with a single curve.
引用
收藏
页码:11 / 20
页数:10
相关论文
共 50 条
  • [1] Application of a New Catalyst Deactivation Model for Residue Hydrotreating
    Zhang Kui
    Nie Hong
    Dai Lishun
    ChinaPetroleumProcessing&PetrochemicalTechnology, 2021, 23 (02) : 11 - 20
  • [2] Catalyst deactivation pattern along a residue hydrotreating bench-scale reactor
    Torres-Mancera, Pablo
    Rayo, Patricia
    Ancheyta, Jorge
    Marroquin, Gustavo
    Centeno, Guillermo
    Alonso, Fernando
    CATALYSIS TODAY, 2014, 220 : 153 - 158
  • [3] Kinetics and deactivation model of residue hydrotreating reaction
    Weng Y.
    Jiang L.
    Geng X.
    Shiyou Xuebao, Shiyou Jiagong/Acta Petrolei Sinica (Petroleum Processing Section), 2010, 26 (SUPPL. 1): : 37 - 40
  • [4] Catalyst deactivation in distillate hydrotreating (Part 1) Catalyst deactivation in the commercial vacuum gas oil hydrotreating unit
    Amemiya, M
    Suzuka, T
    Korai, Y
    Mochida, I
    SEKIYU GAKKAISHI-JOURNAL OF THE JAPAN PETROLEUM INSTITUTE, 2000, 43 (01): : 52 - 58
  • [5] Application of a three-stage approach for modeling the complete period of catalyst deactivation during hydrotreating of heavy oil
    Elizalde, Ignacio
    Ancheyta, Jorge
    FUEL, 2014, 138 : 45 - 51
  • [6] Effect of different heavy feedstocks on the deactivation of a commercial hydrotreating catalyst
    Centeno, Guillermo
    Ancheyta, Jorge
    Alvarez, Anton
    Marroquin, Gustavo
    Alonso, Fernando
    Castillo, Alfredo
    FUEL, 2012, 100 : 73 - 79
  • [7] Promotion of catalytic activity and suppression of deactivation by solvent addition in the hydrotreating of atmospheric residue
    Mizutani, H
    Kiriyama, K
    Idei, K
    Mochida, I
    JOURNAL OF THE JAPAN PETROLEUM INSTITUTE, 2004, 47 (05) : 303 - 310
  • [8] Effect of protective bed composition on deactivation of a hydrotreating catalyst
    Yunusov, Mirakhmad P.
    Teshabaev, Zafar A.
    Mirzaeva, Elena, I
    Nasullaev, Khikmatullo A.
    Ergashev, Makhmudjon M.
    Ruzimuradov, Olim N.
    Murzin, Dmitry Yu
    JOURNAL OF CHEMICAL TECHNOLOGY AND BIOTECHNOLOGY, 2022, 97 (03) : 771 - 778
  • [9] Reactor Model for Heavy Oil Hydrotreating with Catalyst Deactivation Based on Vanadium and Coke Deposition
    Jurado, Javier
    Ancheyta, Jorge
    ENERGY & FUELS, 2022, : 11132 - 11141
  • [10] Deactivation of a hydrotreating catalyst in a bench-scale continuous stirred tank reactor at different operating conditions
    Torres-Mancera, Pablo
    Ancheyta, Jorge
    Martinez, Jeremias
    FUEL, 2018, 234 : 326 - 334