Experimental study and modeling development of pressure drop in concurrent gas-liquid columns with a tridimensional rotational flow sieve tray

被引:24
作者
Tang, Meng [1 ]
Zhang, Shaofeng [1 ]
Wang, Dewu [1 ]
Liu, Yan [1 ]
Wang, Lusha [1 ]
Liu, Chen [1 ]
机构
[1] Hebei Univ Technol, Chem Engn Inst, Tianjin 300401, Peoples R China
关键词
Tray columns; Dry and wet pressure drops; Rotational flow; Flow through perforations; Mathematical models of pressure drop; COMPUTATIONAL FLUID-DYNAMICS; TRICKLE-BED REACTORS; MASS-TRANSFER; PACKED-BEDS; 2-PHASE FLOW; EXPERIMENTAL VALIDATION; COCURRENT DOWNFLOW; CAP TRAY; HYDRODYNAMICS; DISTILLATION;
D O I
10.1016/j.ces.2018.06.080
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A novel column internal is proposed, named the tridimensional rotational flow sieve tray (TRST), which has a three-dimensional hollow structure that can make the gas form two kinds of flow pattern coupled with each other: one is rotational flow and the other is flow through the perforations. Using an air-liquid system, we experimentally measured the pressure drops (dry and wet) when gas-liquid flows concurrently downwards through the TRST. We also examined the effects of gas-liquid flux, various geometric parameters of the TRST (i.e. number of blades, twist angles of the blades, tray heights and sieve hole diameters), tray installation methods (forward and backward) and number of installed trays on the pressure drop. The results indicate that the pressure drop increases with increasing gas-liquid flux, number and twist angles of the blades, but decreases with increasing tray heights and sieve hole diameters. The pressure drop of the tray is largest in backward installation, smaller in first installed location and smallest in forward installation. Compared with other new types of trays, the pressure drop of the TRST is lower and there is a significant resistance performance advantage. In addition, according to the mechanism of gas-liquid flow in the TRST, we established the mathematical model of TRST performance in the range of operating conditions. The fitting values agree well with the experimental values. (C) 2018 Elsevier Ltd. All rights reserved.
引用
收藏
页码:383 / 397
页数:15
相关论文
共 33 条
  • [1] Effects of liquid property on gas holdup and mass transfer in co-current downflow contacting column
    Akosman, C
    Orhan, R
    Dursun, G
    [J]. CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2004, 43 (04) : 503 - 509
  • [2] Modeling of gas absorption accompanied by chemical reaction in downflow co-current packed columns
    Beg, SA
    Hassan, MM
    Naqvi, MSM
    [J]. CHEMICAL ENGINEERING COMMUNICATIONS, 1998, 165 : 41 - 66
  • [3] CFD simulations of a bubble column with and without internals by using OpenFOAM
    Bhusare, V. H.
    Dhiman, M. K.
    Kalaga, D. V.
    Roy, S.
    Joshi, J. B.
    [J]. CHEMICAL ENGINEERING JOURNAL, 2017, 317 : 157 - 174
  • [4] Hydrodynamics of trickle bed reactors at high pressure: Two-phase flow model for pressure drop and liquid holdup, formulation and experimental validation
    Boyer, C.
    Volpi, C.
    Ferschneider, G.
    [J]. CHEMICAL ENGINEERING SCIENCE, 2007, 62 (24) : 7026 - 7032
  • [5] Experimental hydrodynamic study of valve trays
    Brahem, R.
    Royon-Lebeaud, A.
    Legendre, D.
    Moreaud, M.
    Duval, L.
    [J]. CHEMICAL ENGINEERING SCIENCE, 2013, 100 : 23 - 32
  • [6] Prevention of flooding in a countercurrent. trickle-bed reactor using additional void space
    Breijer, Alex A. J.
    Nijenhuis, John
    van Ommen, Ruud
    [J]. CHEMICAL ENGINEERING JOURNAL, 2008, 138 (1-3) : 333 - 340
  • [7] Hydrodynamics of gas-liquid cocurrent downflow in floating packed beds
    Dashliborun, Amir Motamed
    Larachi, Feical
    [J]. CHEMICAL ENGINEERING SCIENCE, 2015, 137 : 665 - 676
  • [8] Prediction of two-phase pressure drop and liquid holdup in co-current gas-liquid downflow of air-Newtonian systems through packed beds
    Ettiyappan, P
    Babu, J
    Arunagiri, A
    Murugesan, T
    [J]. JOURNAL OF CHEMICAL TECHNOLOGY AND BIOTECHNOLOGY, 2006, 81 (01) : 70 - 81
  • [9] [冯殿义 Feng Dianyi], 2010, [核动力工程, Nuclear Power Engineering], V31, P52
  • [10] Application of CFD in the study of supercritical fluid extraction with structured packing: Wet pressure drop calculations
    Fernandes, Joao
    Lisboa, Pedro F.
    Simoes, Pedro C.
    Mota, Jose P. B.
    Saatdjian, Esteban
    [J]. JOURNAL OF SUPERCRITICAL FLUIDS, 2009, 50 (01) : 61 - 68