The effect of droplets thermophysical properties on turbulent heat transfer in a swirling separated mist flow

被引:3
作者
Pakhomov, Maksim [1 ]
Terekhov, Viktor [1 ]
机构
[1] Kutateladze Inst Thermophys SB RAS, Lab Thermal & Gas Dynam, Ac Lavrentev Ave 1, Novosibirsk 630090, Russia
基金
俄罗斯科学基金会;
关键词
Droplet-laden swirling flow; Evaporation; Turbulence; Sudden pipe expansion; Eulerian two-fluid model; LARGE-EDDY SIMULATION; PARTICLE RESPONSE; SPRAY; MODEL; EVAPORATION; MODULATION; TRANSPORT; ETHANOL; PIPE; MASS;
D O I
10.1016/j.ijthermalsci.2019.106180
中图分类号
O414.1 [热力学];
学科分类号
摘要
The numerical investigation of the effect of the swirl number and the thermophysical properties of water, ethanol, and acetone droplets on the particle scattering, turbulence modification and heat transfer in a droplet-laden flow is carried out. The set of 3D steady-state Reynolds-averaged Navier-Stokes (RANS) equations for the two-phase flow is utilized. The dispersed phase is modeled by the Eulerian approach. The flow swirling significantly shortens the length of the recirculation zone (up to two times in comparison with non-swirling flow at swirl number S = 0.5) for all types of the studied liquids. The highest value of heat transfer rate is obtained for the ethanol droplets (up to 10%), and the lowest one is obtained for the acetone droplets (up to 50%), both in comparison with water droplets. The swirling of the turbulent mist flow causes heat transfer enhancement (more than 1.5 times in comparison with the non-swirling droplet-laden flow). In the swirling flow, the value of the volume fraction of the dispersed phase has a maximum in the axial region of the pipe, and further in the direction of the wall its value is very small. The effect of heat transfer enhancement weakens with increasing Reynolds number of the flow. A region without droplets appears in the wall zone of the swirling two-phase flow, and the region is largest for acetone droplets.
引用
收藏
页数:15
相关论文
共 48 条
[1]   Large-eddy simulation of evaporating spray in a coaxial combustor [J].
Apte, Sourabh V. ;
Mahesh, Krishnan ;
Moin, Parviz .
PROCEEDINGS OF THE COMBUSTION INSTITUTE, 2009, 32 :2247-2256
[2]   Large-eddy simulation of swirling particle-laden flows in a coaxial-jet combustor [J].
Apte, SV ;
Mahesh, K ;
Moin, P ;
Oefelein, JC .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 2003, 29 (08) :1311-1331
[3]   Current status of droplet evaporation in turbulent flows [J].
Birouk, Madjid ;
Goekalp, Iskender .
PROGRESS IN ENERGY AND COMBUSTION SCIENCE, 2006, 32 (04) :408-423
[4]   Direct numerical simulation of turbulence modulation by particles in isotropic turbulence [J].
Boivin, M ;
Simonin, O ;
Squires, KD .
JOURNAL OF FLUID MECHANICS, 1998, 375 :235-263
[5]   PARTICLE-SOURCE IN CELL (PSI-CELL) MODEL FOR GAS-DROPLET FLOWS [J].
CROWE, CT ;
SHARMA, MP ;
STOCK, DE .
JOURNAL OF FLUIDS ENGINEERING-TRANSACTIONS OF THE ASME, 1977, 99 (02) :325-332
[6]   On models for turbulence modulation in fluid-particle flows [J].
Crowe, CT .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 2000, 26 (05) :719-727
[7]   MEASUREMENTS IN TURBULENT SWIRLING FLOW THROUGH AN ABRUPT AXISYMMETRIC EXPANSION [J].
DELLENBACK, PA ;
METZGER, DE ;
NEITZEL, GP .
AIAA JOURNAL, 1988, 26 (06) :669-681
[8]  
Derevich I. V., 1988, Fluid Dynamics, V23, P722, DOI 10.1007/BF02614149
[9]   Statistical modelling of mass transfer in turbulent two-phase dispersed flows - 1. Model development [J].
Derevich, IV .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2000, 43 (19) :3709-3723
[10]   MATHEMATICAL-MODELING OF 2-PHASE FLOW [J].
DREW, DA .
ANNUAL REVIEW OF FLUID MECHANICS, 1983, 15 :261-291