Oil hydrogenation in a HiGee-aided fixed bed reactor: Process intensification and macro-kinetic model

Fan Si-Qiang; Xu Yong-Rui; Zhang Jun-Kai; Li Hua; Xi Yuan-Bing; Zhang Chen; Jiang Lan; Luo Yong; Chen Jian-Feng

doi:null

Your Location：

Home >

Browse articles >

Oil hydrogenation in a HiGee-aided fixed bed reactor: Process intensification and macro-kinetic model

Updated：2026-09-17

- Oil hydrogenation in a HiGee-aided fixed bed reactor: Process intensification and macro-kinetic model
- Oil hydrogenation in a HiGee-aided fixed bed reactor: Process intensification and macro-kinetic model
- 中国化学工程学报（英文） 2026年95卷第7期页码：240-251
- Affiliations：
  
  SINOPEC Dalian Research Institute of Petroleum and Petrochemicals Co., LTD, Dalian 116401, China
  Research Center of the Ministry of Education for High Gravity Engineering and Technology, Beijing University of Chemical Technology, Beijing 100029, China
  SINOPEC Research Institute of Petroleum Processing Co., LTD, Beijing 100083, China
  Beijing Key Laboratory of Enze Biomass Fine Chemicals, School of New Materials and Chemical Engineering, Beijing Institute of Petrochemical Technology, Beijing 102617, China
  Quzhou Innovation Institution for Chemical Engineering and Materials, Quzhou 324000, China
- Author bio：
  
  *Corresponding authors. E-mail addresses:a767997651@163.com(L. Jiang)
  *Corresponding authors. E-mail addresses:luoyong@mail.buct.edu.cn(Y. Luo).
- Funds：
  
  the National Key Research and Development Program of China(2022YFA1504401);the National Natural Science Foundation of China(22525801;22288102)
- DOI：
  中图分类号：
- 收稿：2025-11-13，
  
  修回：2026-02-04，
  
  录用：2026-02-25，
  
  网络首发：2026-04-11，
  
  纸质出版：2026-07
- Accepted：
Scan QR Code
Fan Si-Qiang, Xu Yong-Rui, Zhang Jun-Kai, 等. Oil hydrogenation in a HiGee-aided fixed bed reactor: Process intensification and macro-kinetic model[J]. 中国化学工程学报（英文）, 2026,95(7):240-251.

Fan Si-Qiang, Xu Yong-Rui, Zhang Jun-Kai, et al. Oil hydrogenation in a HiGee-aided fixed bed reactor: Process intensification and macro-kinetic model[J]. Chinese Journal of Chemical Engineering, 2026, 95(7): 240-251.
Fan Si-Qiang, Xu Yong-Rui, Zhang Jun-Kai, 等. Oil hydrogenation in a HiGee-aided fixed bed reactor: Process intensification and macro-kinetic model[J]. 中国化学工程学报（英文）, 2026,95(7):240-251. DOI：

Fan Si-Qiang, Xu Yong-Rui, Zhang Jun-Kai, et al. Oil hydrogenation in a HiGee-aided fixed bed reactor: Process intensification and macro-kinetic model[J]. Chinese Journal of Chemical Engineering, 2026, 95(7): 240-251. DOI：

摘要

Abstract

Vacuum gas oil (VGO)

an important raw material for catalytic cracking and hydrocracking units

undergoes hydrogenation process to remove sulfur and nitrogen compounds. However

the VGO hydrogenation process is limited by the gas-liquid mass transfer

resulting in a low reaction rate and high energy consumption. In this work

a HiGee-aided fixed bed reactor (HFBR) with excellent mass transfer performance has been developed and applied for VGO hydrogenation. The bed structure of HFBR was optimized and the effects of operating conditions on VGO hydrodesulfurization (HDS) and hydrodenitrogenation (HDN) efficiency were investigated. Compared with fixed bed reactor at equivalent removal efficiency

pressure in HFBR was reduced by 5% to 15% and H/O ratio was lowered by 35% to 60%. The macro-kinetic models for HDS and HDN of VGO were established and the deviations between the calculated and experimental values were within ±20%. This study provides guidance for the reactor design and process optimization of VGO hydrogenation.

关键词

Keywords

references

I. Elizalde, F.S. Mederos, V.Y. Mena-Cervantes, R. Hernández-Altamirano, J.A. D. Munõz, Dynamic modeling of adiabatic reactor for hydrocracking of VGO by using of the continuous lumping approach, Fuel Process. Technol. 152 (2016) 200—206.

H. Wang, W. Mao, K. Wang, Y.C. Qin, Q. Li, C. Peng, J.F. Wang, Z.L. Sun, L.J. Song, Insight into the effects of mass transfer performance of Y zeolite on the product selectivity of VGO hydrocracking, Ind. Eng. Chem. Res. 61 (50) (2022) 18270—18281.

I.M. Dahl, E. Tangstad, H.B. Mostad, K. Andersen, Effect of hydrotreating on catalytic cracking of a VGO, Energy Fuels 10 (1) (1996) 85—90.

Y. Zhang, E.H. Xing, W. Han, P.F. Yang, S. Zhang, S. Liu, D.X. Cao, M.F. Li, Petrochemical industry for the future, Engineering 43 (2024) 99—114.

A. Tanimu, K. Alhooshani, Advanced hydrodesulfurization catalysts: a review of design and synthesis, Energy Fuels 33 (4) (2019) 2810—2838.

Z.L. Wang, S.Q. Wang, L.X. Ling, C.P. Ma, R.G. Zhang, B.J. Wang, Revealing the regularity of hydrogenation and ring-opening via hydrodenitrogenation on the CaO surface of pyrolysis conditions—taking pyrrole and pyridine as examples, J. Anal. Appl. Pyrolysis 187 (2025) 107000.

H.F. Lu, Y. Frank Cheng, Artificial intelligence in energy pipelines: opportunities and risks, Engineering (2025) https://doi.org/10.1016/j.eng.2025.08. 032.

A.M.A. Karim, Effect of operating conditions on hydrodesulfurization of vacuum gas oil, Diyala J. Eng. Sci. 1 (1) (2008) 19—31.

N.M. Maximov, A.V. Moiseev, P.S. Solmanov, N.N. Tomina, I.I. Zanozina, A.A. Pimerzin, Hydrodesulfurization reactions group kinetics of “vacuum gas oil—deasphalted vacuum residues—heavy coker gasoil” feedstock in the presence of a Ni6—PMonW12-n/γ-Al2O3 catalysts, React. Kinet. Mech. Catal. 132 (2) (2021) 877—892.

M.A. Rodríguez, I. Elizalde, J. Ancheyta, Comparison of kinetic and reactor models to simulate a trickle-bed bench-scale reactor for hydrodesulfurization of VGO, Fuel 100 (2012) 91—99.

P.J. Becker, B. Celse, D. Guillaume, H. Dulot, V. Costa, Hydrotreatment modeling for a variety of VGO feedstocks: a continuous lumping approach, Fuel 139 (2015) 133—143.

A.K. Sinha, M.G. Sibi, N. Naidu, S.A. Farooqui, M. Anand, R. Kumar, Process intensification for hydroprocessing of vegetable oils: experimental study, Ind. Eng. Chem. Res. 53 (49) (2014) 19062—19070.

R. Parmar, S.K. Majumder, Terminal rise velocity, size distribution and stability of microbubble suspension, Asia Pac. J. Chem. Eng. 10 (3) (2015) 450—465.

L.S. Metcalfe, Chemical Reaction Engineering, Oxford University Press, Oxford, 2022.

R. Parmar, S.K. Majumder, Microbubble generation and microbubble-aided transport process intensification: a state-of-the-art report, Chem. Eng. Process. Process Intensif. 64 (2013) 79—97.

L. Zhao, Q. Sun, Z.Y. Tang, Multi-phase CFD modelling for hydroformylation of 1-hexene with microbubbles, Chem. Eng. Process. Process Intensif. 181 (2022) 109163.

W.L. Wang, X.T. Guo, Z.K. Liu, S. Dong, H.J. Liu, Y.D. Wu, Z.G. Cao, Micro-nano H2 bubbles enhanced hydrodehalogenation of 3-chloro-4-fluoroaniline: mass transfer and action mechanism, Chemosphere 363 (2024) 142816.

J. Tan, Y. Zhou, Z.K. Li, Y.N. Ji, Catalytic hydrogenation of acetophenone via an intensified trickle bed reactor for efficient hydrogen storage, Int. J. Hydrog. Energy 86 (2024) 800—807.

R. Zhang, H.Q. Wang, E.M. Hu, Z.W. Lei, F. Hu, W. Hou, Q.L. Wang, Oxidation of pyrite using ozone micro-nano bubbles, Min. Metall. Explor. 39 (2) (2022) 709—719.

X.L. Yang, L. Chen, S. Oshita, W.H. Fan, S. Liu, Mechanism for enhancing the ozonation process of micro- and nanobubbles: bubble behavior and interface reaction, ACS ES&T Water 3 (12) (2023) 3835—3847.

L.H. Wang, L. Jiang, H.L. Liao, S.H. Cai, Y. Luo, J.F. Chen, A pilot-scale HiGee-aided fixed bed reactor: size characteristics of microbubbles in diesel, Ind. Eng. Chem. Res. 62 (45) (2023) 18867—18878.

C. Yang, G.W. Chu, X. Feng, Y.B. Li, J. Chen, D. Wang, X.X. Duan, J.F. Chen, Mixing intensification for advanced materials manufacturing, Engineering 44 (2025) 135—144.

Z.L. Yang, S.J. Ding, Y. Liu, S.Z. Peng, H.G. Wang, H. Jiang, J.F. Wang, F.Z. Wang, P. Wang, Grading system of hydrogenation catalyst and application thereof and grading method of hydrogenation catalyst, US Pat., 18704623 (2024).

H. Zhang, B.S. Nie, X.F. Liu, F.F. Hu, H.Y. He, P.J. Liu, L.T. Zhang, The availability of industrial purge gas: experimental and kinetic study of explosion characteristics of low-concentration H2/CH4 mixtures, Energy 313 (2024) 133910.

S. Ramírez, M.C. Cabrera, P. Vega, H. Vaca, O. Bermúdez, C. Aguilar, A. García, R. Agueda, R. Santiago, P. Schacht, Integral evaluation for hydrotreating catalyst activity, Petrol. Sci. Technol. 22 (1—2) (2004) 189—199.

S.K. Bej, Performance evaluation of hydrop rocessing CatalystsA review of experimental techniques, Energy Fuels 16 (3) (2002) 774—784.

Q. Luo, L.H. Wang, W.T. Jiang, C.H. Li, Y. Luo, H.K. Zou, J.F. Chen, Flow behavior and size characteristics of microbubble swarm in a HiGee-aided fixed bed reactor with different packed structures, Chem. Eng. Sci. 291 (2024) 119960.

A. Srivastava, K.D.P. Nigam, S. Roy, Bed structure and its impact on liquid distribution in a trickle bed reactor, AIChE J. 69 (1) (2023) e17649.

Z.L. Gao, J. Wei, H.Y. Wang, C.Y. Zhou, Research on the influence of the scaling-up process on the flow structure and two-phase distribution of gas—solid fluidized beds, Separations 11 (7) (2024) 202.

G.C. Gardner, The effect of fine material on the structure and resultant pressure drop of a bed charged against an uprising gas stream, Chem. Eng. Sci. 7 (1—2) (1957) 73—82.

N.H. Fu, X. Liang, Z. Li, Y.D. Li, Single-atom site catalysts based on high specific surface area supports, Phys. Chem. Chem. Phys. 24 (29) (2022) 17417—17438.

H.L. Liao, L. Jiang, L.H. Wang, Y. Luo, Q.F. Tan, S.T. Ma, J.F. Chen, Hydrodynamics, mass transfer, and hydrogenation performance of a HiGee-aided fixed bed reactor, AIChE J. 70 (5) (2024) e18384.

浏览量

Downloads

CSCD

文章被引用时，请邮件提醒。

Submit

工具集

关联资源

Analysis of the competitive reaction rates of dibenzothiophene and naphthalene in the hydrodenitrogenation of 1,2,3,4-tetrahydroquinoline over Pt-based catalysts

Semi-hydrogenation of acetylene on Ni/H-zeolite catalysts with different zeolite topologies

High-resolution mass spectrometry-informed molecular reconstruction of vacuum gas oil

Catalytic depolymerization of organic extraction pine lignin over Ni/MLG coupled with NaOH for aromatic monomer production

Hydrophobic Pd/Al2O3 catalyst intensified nitrobenzene hydrogenation in flow