A Pipe-Line Temperature Probe for Viscous Liquids and Powders

1984 ◽  
Vol 17 (1) ◽  
pp. 21-23
Author(s):  
B. W. Ramsay ◽  
H. A. Slight
Author(s):  
Hung-Wen Lin ◽  
Goh Seng Yong ◽  
Yu-Kuen Fang ◽  
Wei-Keng Lin

Capillary Pumped Loop (CPL) is a high efficiency two-phase heat transfer device. Since it does not need any other mechanical force such as pump, furthermore, it might be used to do the thermal management of high power electronic component such as spacecraft, notebook and computer servers. It is a cyclic circulation pumped by capillary force, and this force is generated from the fine porous structure in evaporator. This research aims to study the CPL pipe line temperature distributions. A steady state heat transfer method was developed to predict the pipeline temperature from evaporator outlet to evaporator inlet. Condenser inlet temperature; condenser outlet temperature; condenser base temperature; pressure drop along the loop could be calculated from the theoretical model. A good agreement between the theoretical results and experimental values were achieved. This theoretical structure provides designer a new design direction and an axial heat transfer method that allows designer more freedom.


2018 ◽  
pp. 118-129
Author(s):  
Ye.V. Semenenko ◽  
◽  
O.O. Medvedeva ◽  
S.M. Kyrychko ◽  
L.G. Tatarko ◽  
...  
Keyword(s):  

Author(s):  
S. Abanades ◽  
J. M. Badie ◽  
Gilles Flamant ◽  
L. Fulcheri ◽  
J. Gonzales-Aguilar ◽  
...  

1970 ◽  
Vol 68 (3) ◽  
pp. 731-750 ◽  
Author(s):  
J. R. Jones

In (general) elastico-viscous liquids the response to stress at any instant will depend on previous rheological history, the equations of state needed to describe the rheological properties of a typical material element at any instant t being expressible in the form of a (properly invariant†) set of integro-differential equations relating its deformation, stress and temperature histories (as defined by a metric tensor (of a convected frame of reference), a stress tensor and the temperature measured in the element as functions of previous time t'( < t)) together with the time lag (t – t') and physical constant tensors associated with the element (1). Thus in any type of oscillatory motion a rheological history will necessarily be a function of the frequency of the forcing agent, the rheological history of a number of different types of elastico-viscous liquids in some simple shearing oscillatory flows being a rather simple oscillatory history (see, for example, (2–4)). It is, therefore, to be expected that a liquid with elastic properties will behave somewhat differently from any inelastic viscous liquid when subjected to any kind of oscillatory motion, and it is for this reason that oscillatory motions have been used extensively to detect and measure the elastic properties of liquids (see, for example, (2–5)).


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