Analysis and active control of pressure-drop flow instabilities in boiling microchannel systems

被引:119
|
作者
Zhang, TieJun [1 ]
Peles, Yoav [1 ]
Wen, John T. [1 ]
Tong, Tao [2 ,4 ]
Chang, Je-Young [4 ]
Prasher, Ravi [3 ,4 ]
Jensen, Michael K. [1 ]
机构
[1] Rensselaer Polytech Inst, Dept Mech Aerosp & Nucl Engn, Ctr Automat Technol & Syst, Troy, NY 12180 USA
[2] Univ Calif Berkeley, Dept Mech Engn, Berkeley, CA 94720 USA
[3] Arizona State Univ, Dept Mech & Aerosp Engn, Tempe, AZ 85287 USA
[4] Intel Corp, Chandler, AZ 85226 USA
基金
美国国家科学基金会;
关键词
Boiling; Microchannel; Pressure-drop oscillation; Two-phase flow instability; Active control;
D O I
10.1016/j.ijheatmasstransfer.2010.02.005
中图分类号
O414.1 [热力学];
学科分类号
摘要
Pressure-drop oscillations are one of the most severe dynamic instabilities for boiling flow especially in microchannel systems. This paper presents a systematic framework for the transient analysis and active control of microchannel flow oscillations at a system-level view. To quantify the upstream compressibility and the associated oscillatory transients in an experimental microchannel boiling system, a lumped oscillator model is derived from the momentum balance equation, and both analytical and numerical nonlinear parameter identification methods are proposed. The predictions from the flow oscillation model agree well with the experimental pressure-drop observations across a flow meter and a microchannel heat sink. Based on the identified nonlinear oscillator model, a virtual state observer is designed to estimate the mass flow acceleration from the mass flowrate measurement in the boiling channel. Then a family of state and dynamic output-feedback active flow controllers is developed and evaluated for the dynamic pressure-drop instability suppression. Further analysis and simulations show the flow oscillation amplitude can be regulated to whatever level is desired under certain conditions. (C) 2010 Elsevier Ltd. All rights reserved.
引用
收藏
页码:2347 / 2360
页数:14
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