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Loop Heat Pipe Operation Using Heat Source Temperature for Set Point Control
Author(s) -
Jentung Ku,
Kleber Vieira de Paiva,
Marcia Mantelli
Publication year - 2011
Publication title -
41st international conference on environmental systems
Language(s) - English
Resource type - Conference proceedings
DOI - 10.2514/6.2011-5122
Subject(s) - temperature control , set point , loop (graph theory) , loop heat pipe , heat pipe , set (abstract data type) , computer science , point (geometry) , control theory (sociology) , control (management) , heat transfer , mechanics , mechanical engineering , engineering , control engineering , physics , mathematics , artificial intelligence , geometry , combinatorics , programming language
The LHP operating temperature is governed by the saturation temperature of its reservoir. Controlling the reservoir saturation temperature is commonly accomplished by cold biasing the reservoir and using electrical heaters to provide the required control power. Using this method, the loop operating temperature can be controlled within +/- 0.5K. However, because of the thermal resistance that exists between the heat source and the LHP evaporator, the heat source temperature will vary with its heat output even if LHP operating temperature is kept constant. Since maintaining a constant heat source temperature is of most interest, a question often raised is whether the heat source temperature can be used for LHP set point temperature control. A test program with a miniature LHP has been carried out to investigate the effects on the LHP operation when the control temperature sensor is placed on the heat source instead of the reservoir. In these tests, the LHP reservoir is cold-biased and is heated by a control heater. Tests results show that it is feasible to use the heat source temperature for feedback control of the LHP operation. Using this method, the heat source temperature can be maintained within a tight range for moderate and high powers. At low powers, however, temperature oscillations may occur due to interactions among the reservoir control heater power, the heat source mass, and the heat output from the heat source. In addition, the heat source temperature could temporarily deviate from its set point during fast thermal transients. The implication is that more sophisticated feedback control algorithms need to be implemented for LHP transient operation when the heat source temperature is used for feedback control.

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