Turbulent three-dimensional air flow and trace gas distribution in an inhalation test chamber

被引:4
作者
Longest, PW [1 ]
Kleinstreuer, C
Kinsey, JS
机构
[1] N Carolina State Univ, Dept Mech & Aerosp Engn, Raleigh, NC 27695 USA
[2] US EPA, Natl Hlth & Environm Effects Res Lab, Res Triangle Pk, NC 27711 USA
来源
JOURNAL OF FLUIDS ENGINEERING-TRANSACTIONS OF THE ASME | 2000年 / 122卷 / 02期
关键词
D O I
10.1115/1.483270
中图分类号
TH [机械、仪表工业];
学科分类号
0802 ;
摘要
Steady incompressible turbulent air flow and transient carbon monoxide transport in an empty Rochester-style human exposure chamber have been numerically simulated and compared with experimental data sets. The system consisted of an inlet duct with a continuous carbon monoxide point source, 45- and 90-degree bends, a round diffuser, a round-to-square transition, a rectangular diffuser, the test chamber, a perforated floor, and again transition pieces from the chamber to an outlet duct. Such a configuration induced highly nonuniform vortical flow patterns in the chamber test area where a pollutant concentration is required to be constant at breathing level for safe and accurate inhalation studies. Presented are validated momentum and mass transfer results for this large-scale system with the main goals of determining the development of tracer gas (CO) distributions in the chamber and analyzing the contributions to CO-mixing. Numerical simulations were conducted employing a k-epsilon model and the latest available RNG k-epsilon model for air and CO-mixing. Both models predict similar velocity fields and are in good agreement with measured steady and transient CO-concentrations. It was found that secondary flows in the inlet section and strong vortical flow in the chamber with perforated flooring contributed to effective mixing of the trace gas at breathing levels. Specifically, in the height range of 1.4 m<h<2.0 m above the chamber floor predicted CO-concentrations rapidly reached a near constant value which agrees well with experimental results. This work can be extended to analyze trace gas mixing as well as aerosol dispersion in occupied test chambers with or without flow redirection devices installed in the upstream section. A complementary application is particle transport and deposition in clean rooms of the electronic, pharmaceutical, and health care industries. [S0098-2202(00)01702-8].
引用
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页码:403 / 411
页数:9
相关论文
共 20 条
[1]  
[Anonymous], 1980, MD39 STANF U
[2]  
BURGESS WA, 1989, VENTILATION CONTROL
[3]  
COMER JK, 1998, P FEDSM 98 WASH
[4]  
*COMM IND VENT, 1992, AM C GOV IND HYG CIN
[5]   SEPARATED FLOW COMPUTATIONS WITH THE K-EPSILON-UPSILON(2) MODEL [J].
DURBIN, PA .
AIAA JOURNAL, 1995, 33 (04) :659-664
[6]  
Enayet M. M., 1982, Int J. Heat and Fluid Flow, V3, P213
[7]  
FRASER H, 1958, J HYDRAULICS DIVISIO, V1684, P1
[8]  
Idelchik I., 1994, Handbook of Hydraulic Resistance, V3rd
[9]   PREDICTION OF LAMINARIZATION WITH A 2-EQUATION MODEL OF TURBULENCE [J].
JONES, WP ;
LAUNDER, BE .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 1972, 15 (02) :301-+
[10]  
KLEINSTREUER C, 1999, TASK 3 REPORT COMPAR