CFD Studies on Efficacy of Flow Modulation in a Hydrotreating Trickle-Bed Reactor

被引:2
|
作者
Dasgupta, Soumendu [1 ]
Atta, Arnab [1 ]
机构
[1] Indian Inst Technol Kharagpur, Multiscale Computat Fluid Dynam mCFD Lab, Dept Chem Engn, Kharagpur 721302, W Bengal, India
关键词
PROCESS INTENSIFICATION; LIQUID DISTRIBUTION; CYCLIC OPERATION; MULTIPHASE FLOW; FLUID-DYNAMICS; PRESSURE-DROP; SIMULATION; GAS; HOLDUP; ENHANCEMENT;
D O I
10.1021/acs.iecr.9b02632
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Hydrodesulfurization (HDS), a pivotal process for sulfur removal that is essential in deep processing of crude oil, is typically carried out in steady-state trickle-bed reactors (TBRs). Being familiar with such an operation, researchers are now investigating the benefits of flow modulation strategies in TBRs for improved conversion efficiency. In this work, a computational fluid dynamics model of a hydrotreating TBR is developed to delineate the efficacy of flow modulation in a HDS reaction system. Fast and slow modes of on-off and min- max flow modulations with different split ratios are compared with time-averaged continuous operation for reaction conversion. On-off and min-max flows resulted in relative improvement in conversion by 36 and 19%, respectively. Combined analysis of reaction conversion improvement along with an oscillating pressure drop revealed the efficacy of fast mode on-off strategy in maximum conversion of the considered system at the expense of lower pressure drop undulations.
引用
收藏
页码:18073 / 18083
页数:11
相关论文
共 50 条
  • [41] Selecting carrier material for efficient biomethanation of industrial biogas-CO2 in a trickle-bed reactor
    Jensen, Mads Borgbjerg
    Poulsen, Susanna
    Jensen, Bjarke
    Feilberg, Anders
    Kofoed, Michael Vedel Wegener
    JOURNAL OF CO2 UTILIZATION, 2021, 51
  • [42] A two-dimensional discrete lumped model for a trickle-bed vacuum gas oil hydrocracking reactor
    Sadighi, Sepehr
    KOREAN JOURNAL OF CHEMICAL ENGINEERING, 2016, 33 (09) : 2538 - 2546
  • [43] Performance analysis of crude terephthalic acid hydropurification in an industrial trickle-bed reactor experiencing catalyst deactivation
    Azarpour, Abbas
    Zahedi, Gholamreza
    CHEMICAL ENGINEERING JOURNAL, 2012, 209 : 180 - 193
  • [44] Parallel Hydrogenation for the Quantification of Wetting Efficiency and Liquid-Solid Mass Transfer in a Trickle-Bed Reactor
    van Houwelingen, Arie Jan
    Nicol, Willie
    AICHE JOURNAL, 2011, 57 (05) : 1310 - 1319
  • [45] Whole Crude Oil Hydrotreating from Small-Scale Laboratory Pilot Plant to Large-Scale trickle-Bed Reactor: Analysis of Operational Issues through Modeling
    Jarullah, Aysar T.
    Mujtaba, Iqbal M.
    Wood, Alastair S.
    ENERGY & FUELS, 2012, 26 (01) : 629 - 641
  • [46] CFD analysis of liquid phase flow in a rotating packed bed reactor
    Shi, Xin
    Xiang, Yang
    Wen, Li-Xiong
    Chen, Jian-Feng
    CHEMICAL ENGINEERING JOURNAL, 2013, 228 : 1040 - 1049
  • [47] Hydrodynamic Simulation of Pulsing-Flow Regime in High-Pressure Trickle-Bed Reactors
    Lopes, Rodrigo J. G.
    Quinta-Ferreira, Rosa M.
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2010, 49 (03) : 1105 - 1112
  • [48] Effects of Prewetting on Bubbly- and Pulsing-Flow Regime Transitions in Trickle-Bed Reactors
    Honda, Gregory S.
    Lehmann, Eric
    Hickman, Daniel A.
    Varma, Arvind
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2015, 54 (42) : 10253 - 10259
  • [49] Flow characteristics and thickness distribution of liquid film in trickle bed reactor
    Guo, Run
    Wei, Bin
    Lan, Xingying
    Gao, Jinsen
    Shi, Xiaogang
    POWDER TECHNOLOGY, 2022, 408
  • [50] Prediction of pulsation frequency of pulsing flow in trickle-bed reactors using artificial neural network
    Liu, GZ
    Mi, ZT
    CHEMICAL ENGINEERING SCIENCE, 2004, 59 (24) : 5787 - 5794