2019
DOI: 10.1016/j.ijheatmasstransfer.2019.04.123
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Computer modeling of the vapour vortex orientation changes in the short low- temperature heat pipes

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Cited by 5 publications
(13 citation statements)
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“…Experimental values in the stationary state of the thermal resistance R HP of a short HP's are defined as the thermophysical characteristic of the heat transfer device as a whole [28], at a constant value of the temperature load (pressure) on the evaporator δt = T ev -T B and calculated using formula (18) and a vacuum adiabatic calorimeter, Figure 2, in which all parameters of the working HP, including temperature and transmitted thermal power, are measured using thermocouples.…”
Section: Thermal Resistance Resultsmentioning
confidence: 99%
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“…Experimental values in the stationary state of the thermal resistance R HP of a short HP's are defined as the thermophysical characteristic of the heat transfer device as a whole [28], at a constant value of the temperature load (pressure) on the evaporator δt = T ev -T B and calculated using formula (18) and a vacuum adiabatic calorimeter, Figure 2, in which all parameters of the working HP, including temperature and transmitted thermal power, are measured using thermocouples.…”
Section: Thermal Resistance Resultsmentioning
confidence: 99%
“…Earlier calculations of the flow velocity and vapour density of diethyl ether using the Navier Stokes equation system in a short HP's vapour channel similar to the Laval nozzle [16] [18], allow us to calculate the temperature distribution in this channel. The ratio between the pressure, density and temperature of the condensing vapor in the first approximation can be given by the equation of state of an ideal gas in the following form [19] [20] [21]:…”
Section: Temperature Distribution Inside the Vapour Channelmentioning
confidence: 99%
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“…Среднюю температуру кипящего слоя эфираТ fev на поверхности нижней крышки ТТ оценивают с помощью уравнения (2), и температура Т fev определяет частоту образования пузырьков и интенсивность парообразования в целом [30]. По мере уменьшения толщины кипящего слоя диэтилового эфира δ film коэффициент теплоотдачи α ev испарителя TT возрастает, частота и интен сивность возникновения пузырьков также возрастают до тех пор, пока толщина слоя δ film не достигнет граничной величины δ film ~ 2r min ~ 10 -5 м, равной диаметру пузырька с минимальным критическим размером.…”
Section: вибрационное повышение теплопередачи тт результаты и обсуждениеunclassified