The use of the CFD for the hydrodynamic flow diagnostic and study in a Phosphoric Acid Reactor

被引:2
作者
Khamar, L. [1 ]
Samrane, K. [1 ]
机构
[1] R&D OCP SA Grp, Rabat, Morocco
来源
SYMPHOS 2015 - 3RD INTERNATIONAL SYMPOSIUM ON INNOVATION AND TECHNOLOGY IN THE PHOSPHATE INDUSTRY | 2016年 / 138卷
关键词
Phosphate; CFD; agitation; desupersaturation; phosphorique acid;
D O I
10.1016/j.proeng.2016.02.096
中图分类号
T [工业技术];
学科分类号
08 ;
摘要
The multiphase flows and the solid particles suspension are among the key elements and aspects to study during the desupersaturation of the crude phosphoric acid. When the multiphase is characterized by a separated liquid and solid phases within a particle volume fraction lower than 10%, the single-phase model can be used to represent this type mixture [1]. For the desupersaturation case of the weak phosphoric acid referring to the OCP facilities, the quality of the solid particles suspension can be approached through the study of the agitation and the evaluation of hydrodynamic flow parameters within stirred tanks. This study has in fact a dual vocation. Firstly, it permits to diagnose and evaluate through the CFD approach (Computational Fluid Dynamics) the hydrodynamic flow quality, and defines the performance of the agitation system installed in the desupersaturation reactor for the weak phosphoric acid. Secondly, based on the diagnosis results, the study will determine also if there will be a potential capacity to feed the existing desupersaturation reactor by the concentrated phosphoric acid sludge, which could be transferred from of the clarification units of the concentrated phosphoric acid, and if there will be any problems that may accompany it. (C) 2016 The Authors. Published by Elsevier Ltd.
引用
收藏
页码:369 / 377
页数:9
相关论文
共 9 条
  • [1] Fransolet E., 2006, 10 C FRANC TECHN LAS
  • [2] Evolution of soluble impurities concentrations in industrial phosphoric acid during the operations of desupersaturation
    Khamar, L.
    Guendouzi, M. El
    Amalhay, M.
    El Alaouia, M. Aboufaris
    Rifai, A.
    Faridi, J.
    Azaroual, M.
    [J]. SYMPHOS 2013 - 2ND INTERNATIONAL SYMPOSIUM ON INNOVATION AND TECHNOLOGY IN THE PHOSPHATE INDUSTRY, 2014, 83 : 243 - 249
  • [3] Lakhdari H., 2009, ECOLE MINE NANTE
  • [4] NEW PROCESS FOR TECHNICAL-GRADE PHOSPHORIC-ACID
    LEDER, F
    PARK, WC
    CHANG, PW
    ELLIS, JD
    MEGY, JA
    HARD, RA
    KYLE, HE
    MU, J
    SHAW, BW
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1985, 24 (03): : 688 - 697
  • [5] Numerical simulation of the two-phase flow in an axially stirred vessel
    Ljungqvist, M
    Rasmuson, A
    [J]. CHEMICAL ENGINEERING RESEARCH & DESIGN, 2001, 79 (A5) : 533 - 546
  • [6] A comparison of some recent eddy-viscosity turbulence models
    Menter, FR
    [J]. JOURNAL OF FLUIDS ENGINEERING-TRANSACTIONS OF THE ASME, 1996, 118 (03): : 514 - 519
  • [7] Effect of the shaft eccentricity on the hydrodynamics of unbaffled stirred tanks
    Montante, G
    Bakker, A
    Paglianti, A
    Magelli, F
    [J]. CHEMICAL ENGINEERING SCIENCE, 2006, 61 (09) : 2807 - 2814
  • [8] Roustan M., 2009, CARACTERISTIQUES MOB
  • [9] SAMRANE K., 2012, OCP INTERNAL REPORTS