DSMC Prediction of Particle Behavior in Gas-Particle Two-Phase Impinging Streams

被引:3
作者
Du, Min [1 ,2 ]
Zhao, Changsui [2 ]
Zhou, Bin [3 ]
Hao, Yingli [3 ]
机构
[1] Jiangsu Univ, Sch Energy & Power Engn, Zhenjiang 212013, Peoples R China
[2] Southeast Univ, Sch Energy & Environm, Minist Educ, Key Lab Energy Thermal Convers & Control, Nanjing 210096, Jiangsu, Peoples R China
[3] Southeast Univ, Inst Space Sci & Technol, Nanjing 210096, Jiangsu, Peoples R China
基金
中国国家自然科学基金;
关键词
SIMULATION;
D O I
10.1155/2013/254082
中图分类号
T [工业技术];
学科分类号
08 ;
摘要
Devices with impinging streams have been employed in various fields of chemical engineering, as a means of intensifying heat and mass transfer processes. The particle behavior in gas-particle two-phase impinging streams (GPISs), which is of essential importance for the research of transfer processes, was simulated by an Eulerian-Lagrangian approach in this paper. Collisional interaction of particles was taken into account by means of a modified direct simulation Monte Carlo (DSMC) method based on a Lagrangian approach and the modified Nanbu method. A quantitative agreement was obtained between the predicted results and the experimental data in the literature. The particle motion behavior and the distributions of particle concentration and particle collision positions were presented reasonably. The results indicate that the particle distribution in GPIS can be divided into three zones: particle-collision zone, particle-jetting zone, and particle-scattering zone. Particle collisions occur mainly in the particle-collision zone, which obviously results in a few particles penetrating into the opposite stream. The interparticle collision rate and the particle concentration reach their maximum values in the particle-collision zone, respectively. The maximum value of the particle concentration increases with the increasing inlet particle concentration according to a logarithmic function. The interparticle collision rate is directly proportional to the square of local particle concentration.
引用
收藏
页数:11
相关论文
共 50 条
[21]   Flow regime transition and bubble behavior in gas-liquid two-phase impinging jet reactor [J].
Zhang, Jianwei ;
Zhang, Jin ;
Dong, Xin ;
Feng, Ying .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2024, 201 :275-285
[22]   Filtered models for reacting gas-particle flows [J].
Holloway, William ;
Sundaresan, Sankaran .
CHEMICAL ENGINEERING SCIENCE, 2012, 82 :132-143
[23]   Two-fluid turbulence modeling of swirling gas-particle flows - A review [J].
Zhou, Lixing .
POWDER TECHNOLOGY, 2017, 314 :253-263
[24]   Dilute gas-particle suspension in a diffuser: A two-fluid modelling approach [J].
Senapati, Santosh Kumar ;
Dash, Sukanta Kumar .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 2022, 100 (S1) :S72-S93
[25]   Verification of Filtered Two-Fluid Models for Gas-Particle Flows in Risers [J].
Igci, Yesim ;
Sundaresan, Sankaran .
AICHE JOURNAL, 2011, 57 (10) :2691-2707
[26]   A two-component two-phase dissipative particle dynamics model [J].
Tiwari, Anupam ;
Abraham, John .
INTERNATIONAL JOURNAL FOR NUMERICAL METHODS IN FLUIDS, 2009, 59 (05) :519-533
[27]   MODELLING OF SOOT PARTICLE COLLISION AND GROWTH PATHS IN GAS-SOLID TWO-PHASE FLOW [J].
Ju, Hongling ;
Bian, Fanquan ;
Wei, Mingrui .
THERMAL SCIENCE, 2021, 25 (05) :3741-3752
[28]   Regimes of subsonic compressible flow in gas-particle systems [J].
Macak, Jelena ;
Goniva, Christoph ;
Radl, Stefan .
POWDER TECHNOLOGY, 2021, 394 :44-61
[29]   Periodic flow structures in vertical gas-particle flows [J].
Yan, Xiaokang ;
Holloway, William ;
Sundaresan, Sankaran .
POWDER TECHNOLOGY, 2013, 241 :174-180
[30]   A Numerical Analysis of the Turbophoresis in a Turbulent Gas-Particle Flow [J].
Utzig, Jonathan ;
de Souza, Francisco Jose ;
Meier, Henry Franca .
ASME FLUIDS ENGINEERING DIVISION SUMMER MEETING - 2014, VOL 1C: SYMPOSIA, 2014,