Modeling and analysis of dilute phase pneumatic conveying of fine particles

被引:19
|
作者
Behera, Niranjana [1 ]
Agarwal, Vijay K. [1 ]
Jones, Mark G. [2 ]
Williams, Kenneth C. [2 ]
机构
[1] Indian Inst Technol, New Delhi 110016, India
[2] Univ Newcastle, Sch Engn, Ctr Bulk Solids & Particulate Technol, Callaghan, NSW 2308, Australia
关键词
Dilute; Granular temperature; Pressure drop; Restitution coefficient; FLOW; SIMULATION; TRANSPORT; REGIMES;
D O I
10.1016/j.powtec.2013.08.014
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Mathematical models of pneumatic conveying in dilute mode of flow have been presented by many researchers. Continuum approach is the most commonly used approach of modeling this kind of flow. In the present work a mathematical model has been developed which is in the form of governing equations such as continuity, momentum and energy equation. Energy equation has been written including a parameter called granular temperature. In this model, the dilute mode of conveying has been described as chaotically moving particles as granular gas characterized by granular temperature. Simulations have been performed in order to predict different parameters. The predicted pressure drop values were found to be in good agreement with the experimental data. Variations of important parameters such as absolute pressure, granular temperature along the length of the pipeline have been analyzed for different values of normal and restitution coefficients. (C) 2013 Elsevier B.V. All rights reserved.
引用
收藏
页码:196 / 204
页数:9
相关论文
共 50 条
  • [1] CFD modeling and analysis of dense phase pneumatic conveying of fine particles including particle size distribution
    Behera, Niranjana
    Agarwal, Vijay K.
    Jones, Mark G.
    Williams, Kenneth C.
    POWDER TECHNOLOGY, 2013, 244 : 30 - 37
  • [2] Computational model for prediction of particle degradation during dilute-phase pneumatic conveying: modeling of dilute-phase pneumatic conveying
    Chapelle, P
    Christakis, N
    Abou-Chakra, H
    Bridle, I
    Bradley, MSA
    Patel, M
    Cross, M
    ADVANCED POWDER TECHNOLOGY, 2004, 15 (01) : 31 - 49
  • [3] DILUTE-PHASE PNEUMATIC CONVEYING: Instrumentation and Conveying Velocity
    Agarwal, Amrit
    CHEMICAL ENGINEERING, 2014, 121 (03) : 54 - 58
  • [4] Particle fragmentation in dilute phase pneumatic conveying
    Salman, AD
    Hounslow, MJ
    Verba, A
    POWDER TECHNOLOGY, 2002, 126 (02) : 109 - 115
  • [5] Particle trajectories in dilute phase pneumatic conveying
    Godbole, Ajit
    Kosasih, Buyung
    Fuchs, Anton
    PARTICULATE SCIENCE AND TECHNOLOGY, 2007, 25 (04) : 381 - 385
  • [6] Friction factor for dilute phase pneumatic conveying
    Szikszay, George
    Bulk Solids Handling, 1988, 8 (04): : 395 - 399
  • [7] Analysis of pneumatic conveying of particles
    Pelegrina, AH
    LATIN AMERICAN APPLIED RESEARCH, 2002, 32 (01) : 91 - 96
  • [8] Experimental study on the solid velocity in horizontal dilute phase pneumatic conveying of fine powders
    Wang Wei
    Guan Qingliang
    Wu Yuxin
    Yang Hairui
    Zhang Jiansheng
    Lu Junfu
    POWDER TECHNOLOGY, 2011, 212 (03) : 403 - 409
  • [9] Air movers for dilute-phase pneumatic conveying
    Liu, Gary
    Chemical Engineering (United States), 2019, 126 (10): : 56 - 62
  • [10] Pneumatic conveying: Dilute vs. dense phase
    Mills, D
    CHEMICAL ENGINEERING, 2005, 112 (01) : 51 - 57