Computational-fluid-dynamics study of a Kenics static mixer as a heat exchanger for supercritical carbon dioxide

被引:59
|
作者
Lisboa, Pedro F. [1 ]
Fernandes, Joao [1 ]
Simoes, Pedro C. [1 ]
Mota, Jose P. B. [1 ]
Saatdjian, Esteban [2 ]
机构
[1] Univ Nova Lisboa, Fac Ciencias & Tecnol, Dept Quim, REQUIMTE, P-2829516 Caparica, Portugal
[2] CNRS, LEMTA, F-54500 Vandoeuvre Les Nancy, France
来源
JOURNAL OF SUPERCRITICAL FLUIDS | 2010年 / 55卷 / 01期
关键词
Supercritical extraction; Heat transfer; Kenics static mixer; Computational fluid dynamics; GAS-LIQUID FLOW; MASS-TRANSFER; PRESSURE-DROP; PERFORMANCE; HYDRODYNAMICS; EXTRACTION;
D O I
10.1016/j.supflu.2010.08.005
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
The thermal efficiency of a Kenics (R) KM static mixer used to pre-heat supercritical carbon dioxide, under high pressure conditions, is studied using computational fluid dynamics (CFD). A mesh sensitivity analysis is performed and the CFD model is validated against experimental results on heat transfer with conventional and supercritical fluids. Three turbulent models - standard k-epsilon, RNG k-epsilon, and k-omega - are employed to model the flow and heat transfer under high pressure conditions: the effects of large variations of the physical properties in the pseudo-critical region of the fluid are also studied. The RNG k-e model gives results that are closer to the experimental data than the other two turbulence models. The numerical results show that the static mixer has a thermal efficiency more than three times higher than that of a conventional empty pipe heat exchanger with similar heat transfer area. (C) 2010 Elsevier B.V. All rights reserved.
引用
收藏
页码:107 / 115
页数:9
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