2012
DOI: 10.1016/j.enbuild.2012.03.041
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Designing a PCM storage system using the effectiveness-number of transfer units method in low energy cooling of buildings

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Cited by 88 publications
(39 citation statements)
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“…This method was used to define the actual heat transfer that can be derived from a specific design at a specific fraction of phase change [16,17], or the average heat transfer across the phase change process [18,19]. The NTU is a function of the total thermal resistance between the phase change front and the heat transfer fluid, and this resistance can be expressed in terms of the phase change fraction.…”
Section: Introductionmentioning
confidence: 99%
“…This method was used to define the actual heat transfer that can be derived from a specific design at a specific fraction of phase change [16,17], or the average heat transfer across the phase change process [18,19]. The NTU is a function of the total thermal resistance between the phase change front and the heat transfer fluid, and this resistance can be expressed in terms of the phase change fraction.…”
Section: Introductionmentioning
confidence: 99%
“…In addition, if we consider running in cool mode where supply air temperature is limited to dew point, it not only provides us with energy savings compared to other forced air, radiant and convective systems, but allows achieving powers of 75-90 W/m 2 in cooling mode, which other radiant systems cannot reach. Therefore, it has advantages over chilled beams systems [32,33], passive phase change materials systems (PCMs) applied in natural ventilation slabs at night phase [5,34], displacement diffusion or UFAD (underfloor air diffusion) systems or drive of large air flows at low speed systems. The comparison with chilled beam systems is interesting.…”
Section: Water As a Medium For Transporting Energymentioning
confidence: 99%
“…A mesh independence study was performed in order to determine the appropriate size of elements to use, providing an accurate mesh independent solution and limiting the overall calculation time. To this end, two meshes were compared using 16 Figure 3 shows the average PCM temperature and the heat transfer rate as a function of time, for the two selected meshes, in the case of 6 cm channel size, 1 m/s inlet velocity, and 70 °C inlet temperature. It can be observed that the average PCM temperature profiles are almost overlapping for the two meshes, whereas the heat transfer rate obtained with the largest element number (Mesh 2) is slightly lower compared to the one resulting from Mesh 1.…”
Section: Mesh Sensitivity Studymentioning
confidence: 99%
“…These studies cover different heat exchanger configurations: parallel PCMs slabs with rectangular air flow channels in-between [1][2][3][4][5][6][7][8][9][10][11]; cross-flow heat exchangers where one [12] or multiple PCMs [13] filled tubes and air is driven across the tubes bank; single [14] or modular [15,16] heat exchangers based on a shell and tubes design where the PCM is on the shell side and air is flowing either across the cylinder containing the PCM or through the tubes; and a cylindrical reactor where air passes through packed layers of spherical PCM capsules [17].…”
Section: Introductionmentioning
confidence: 99%