Numerical study on the mixing effect and parameter optimization of double tank agitator

被引:2
作者
Chen, Chunxia [1 ]
Sun, Xiange [1 ,2 ]
机构
[1] Yangtze Univ, Sch Elect & Informat, Jingzhou, Peoples R China
[2] Yangtze Univ, Sch Elect & Informat, Jingzhou 434024, Peoples R China
关键词
agitated slurry tank; cement slurry; CFD simulation; revolution speed; structural parameters; SOLID-LIQUID SUSPENSIONS; COMPUTATIONAL FLUID-DYNAMICS; CFD SIMULATION; STIRRED TANKS; IMPELLER SPEED; PREDICTION; DRAG; REACTOR; MODEL; FLOW;
D O I
10.1080/10916466.2022.2147543
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
Cementing technology is crucial to the development of oil and gas resources, and the quality of cement slurry required is an important factor affecting the cementing effect. Previous studies ignored mixing speed effect on cement slurry quality. CFD numerical model is established to simulate the flow filed of the agitated slurry tank under various operation and structural parameters. The multiphase flow model and the k-epsilon turbulence model are used to describe the turbulence characteristics in the agitated slurry tank. The multiple reference frame (MRF) model is used to realize the rotation of the area near the stirring blade. The results indicate that the density of the cement slurry in the agitated slurry tank can finally reach a stable state, and the concentration distribution is uniform. Increasing the rotational speed, the stirring time needed to achieve stability becomes shorter, and the uniformity of the cement slurry will also be improved. Reducing the distance between the impeller and the bottom of the agitated slurry tank, the mixing effect can be improved. It provides certain theoretical guidance for the practical application of this agitated slurry tank and has certain reference significance for research on improving the quality of cement slurry required for cementing.
引用
收藏
页码:1481 / 1504
页数:24
相关论文
共 36 条
  • [1] [Anonymous], 2000, 6466 3SYT, DOI [10.1016/j.jmatprotec.2018.06.012, DOI 10.1016/J.JMATPROTEC.2018.06.012]
  • [2] Cheng Y, 2005, CAN J CHEM ENG, V83, P177
  • [3] CFD phenomenological model of solid-liquid mixing in stirred vessels
    Fradette, Louis
    Tanguy, Philippe A.
    Bertrand, Francois
    Thibault, Francis
    Ritz, Jean-Benoit
    Giraud, Eric
    [J]. COMPUTERS & CHEMICAL ENGINEERING, 2007, 31 (04) : 334 - 345
  • [4] Gibbardo B., 2006, 12 EUROPEAN C MIXING, P27
  • [5] Study of Solid-Liquid Mixing in Agitated Tanks through Computational Fluid Dynamics Modeling
    Hosseini, Seyed
    Patel, Dineshkumar
    Ein-Mozaffari, Farhad
    Mehrvar, Mehrab
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2010, 49 (09) : 4426 - 4435
  • [6] Hu Z., 2007, RES DEV MACHINE DESI, V33, P174
  • [7] CFD simulation of liquid-phase mixing in solid-liquid stirred reactor
    Kasat, G. R.
    Khopkar, A. R.
    Ranade, V. V.
    Pandita, A. B.
    [J]. CHEMICAL ENGINEERING SCIENCE, 2008, 63 (15) : 3877 - 3885
  • [8] Computational fluid dynamics simulation of the solid suspension in a stirred slurry reactor
    Khopkar, A. R.
    Kasat, G. R.
    Pandit, A. B.
    Ranade, V. V.
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2006, 45 (12) : 4416 - 4428
  • [9] LIU, 2004, WELL LOGGING TECHNOL, V28, P23
  • [10] CFD simulation of particle suspension height in stirred vessels
    Micale, G
    Grisafi, F
    Rizzuti, L
    Brucato, A
    [J]. CHEMICAL ENGINEERING RESEARCH & DESIGN, 2004, 82 (A9) : 1204 - 1213