Numerical analysis of asphaltene particles evolution and flocs morphology using DEM-CFD approach

被引:8
作者
Bagherzadeh, Hadi [1 ]
Mansourpour, Zahra [2 ]
Dabir, Bahram [3 ]
机构
[1] Amirkabir Univ Technol, Petr Engn Dept, Tehran, Iran
[2] Univ Tehran, Coll Engn, Sch Chem Engn, Tehran, Iran
[3] Amirkabir Univ Technol, Chem Engn Dept, Tehran, Iran
关键词
Asphaltene; Particle size distribution; Morphology; Discrete element method; Computational fluid dynamic;
D O I
10.1016/j.petrol.2020.108309
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
The agglomeration and fragmentation of asphaltenes which dictate particle size distribution (PSD) play an important role in deposition behavior of asphaltene. However, the physics underlying the agglomeration/fragmentation processes is grossly missing in the available literature. In this paper, Discrete Element Method (DEM) in combination with a coalescence model is coupled with Computational Fluid Dynamics (CFD) to simulate agglomeration/fragmentation considering asphaltene particles as real/irregular objects in the absence of deposition process. The evolution of asphaltene particles, asphaltene particle size distribution (PSD), and morphology of asphaltene flocs have been examined during the simulation. Also, the effect of fluid velocity (V-f), primary particle concentration (N-0), inter-particle bond strength (F-b), and energy barrier (U-b) have been investigated. During asphaltene flocculation, mean floc size increases until a steady-state condition is attained where floc size and mass fractal dimension approximately remains unchanged. The size of asphaltene flocs increases up to 40 mu m and fractal dimension values change in the range of 1.45-1.75. Higher V-f leads to the steady-state condition is attained more rapidly along with smaller floc sizes and higher fractal dimensions. Increasing N-0 results in faster growth of asphaltene flocs, however, the stable mean asphaltene floc size is approximately insensitive to N-0. The presence of larger flocs at higher N-0 eventuates the smaller fractal dimensions. As F-b increases, the frequency of small particles decreases, and PSD shifts to larger sizes. Consequently, smaller fractal dimensions are obtained. The floc growth is insensitive to U-b at initial times, whereas the steady-state condition is reached more quickly with a smaller stable floc size for higher values of U-b. The fractal dimension shows a weak dependency on the energy barrier.
引用
收藏
页数:13
相关论文
共 53 条
  • [31] 2-S
  • [32] A new multiphase and dynamic asphaltene deposition tool (MAD-ADEPT) to predict the deposition of asphaltene particles on tubing wall
    Naseri, Saman
    Jamshidi, Saeid
    Taghikhani, Vahid
    [J]. JOURNAL OF PETROLEUM SCIENCE AND ENGINEERING, 2020, 195
  • [33] Study of asphaltene deposition in wellbores during turbulent flow
    Paes, D. M.
    Ribeiro, P. R.
    Shirdel, M.
    Sepehrnoori, K.
    [J]. JOURNAL OF PETROLEUM SCIENCE AND ENGINEERING, 2015, 129 : 77 - 87
  • [34] PATANKAR SV, 1977, J HEAT TRANS-T ASME, V99, P180, DOI 10.1115/1.3450666
  • [35] Asphaltene Aggregates Fractal Restructuring Model, A Population Balance Approach
    Rahimi, Hassan
    Nazar, Ali R. Solaimany
    [J]. ENERGY & FUELS, 2010, 24 (02) : 1088 - 1093
  • [36] Fractal structure of asphaltene aggregates
    Rahmani, NHG
    Dabros, T
    Masliyah, JH
    [J]. JOURNAL OF COLLOID AND INTERFACE SCIENCE, 2005, 285 (02) : 599 - 608
  • [37] Characterization of asphaltenes aggregation and fragmentation in a shear field
    Rahmani, NHG
    Masliyah, JH
    Dabros, T
    [J]. AICHE JOURNAL, 2003, 49 (07) : 1645 - 1655
  • [38] Modeling asphaltene deposition in production pipelines
    Ramirez-Jaramillo, E.
    Lira-Galeana, C.
    Manero, O.
    [J]. ENERGY & FUELS, 2006, 20 (03) : 1184 - 1196
  • [39] Kinetics of asphaltene flocculation
    Rastegari, K
    Svrcek, WY
    Yarranton, HW
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2004, 43 (21) : 6861 - 6870
  • [40] Hydrodynamic Perspective on Asphaltene Agglomeration and Deposition
    Schutte, Koen C. J.
    Portela, Luis M.
    Twerda, Aris
    Henkes, Ruud A. W. M.
    [J]. ENERGY & FUELS, 2015, 29 (05) : 2754 - 2767