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NUI Galway – UL Alliance First Annual ENGINEERING AND - ARAN ...

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Energy Storage using Microencapsulated Phase Change Materials<br />

James Howard and Patrick Walsh<br />

Stokes Research Institute, University of Limerick, Ireland<br />

james.howard@ul.ie<br />

Abstract<br />

This paper investigates laminar heat transfer<br />

characteristic of two-phase microencapsulated phase<br />

change material (MPCM) suspension flows within minichannels<br />

under a constant wall heat flux boundary.<br />

Capsules containing paraffin are examined and found<br />

to be well suited for electronics cooling applications<br />

using liquid cold plate technologies. In particular, it is<br />

shown that the large thermal capacity of MPCM<br />

slurries around the phase change temperature can lead<br />

towards greater isothermality of isoflux systems, a<br />

characteristic of significant interest to<br />

telecommunication, laser and biomedical applications.<br />

Introduction<br />

Phase Change Materials (PCMs) have been widely<br />

used in thermal energy storage applications. They offer<br />

the ability to absorb and store large quantities of<br />

thermal energy through the endothermic melt process.<br />

The high latent heat of fusion and considerable energy<br />

densities associated with such materials have made<br />

them very desirable and these thermal properties have<br />

led to many direct applications in a range of fields.<br />

Investigations have found important uses in solar<br />

energy storage to reduce peak demands on systems, El-<br />

Sebaii et al. [1] and subsequent incorporation in<br />

numerous building materials, such as wallboard and<br />

under floor heating, Farid et al. [2] However,<br />

significant potential lies in the field of MPCM slurry<br />

flows, allowing store energy to be easily transported.<br />

Thermo Physical Properties<br />

The primary aspect of the MPCM slurry is the latent<br />

heat of fusion associated with the phase change process.<br />

This can be quantified using a DSC and for simplified<br />

modeling, the latent heat is absorbed as a specific heat<br />

capacity enhancement. This results in a step change in<br />

the apparent heat capacity over the melt temperature<br />

range as demonstrated in Figure 1.<br />

Figure 1: Modified enthalpy model over phase change<br />

region<br />

Analytical Model<br />

23<br />

Heat transfer for single phase flows in circular<br />

geometries is described using the Graetz solution. This<br />

is characterized by the Nusselt number which in based<br />

on the inverse of the temperature difference between<br />

the wall and bulk mean of the fluid. Theoretical wall<br />

temperatures can be determined based on the modified<br />

bulk temp from the enthalpy model shown in Figure 1.<br />

Results<br />

Experimental wall temperatures determined from the<br />

Infrared Thermography are plotted versus the<br />

predictions using the Graetz solution. An example using<br />

30.2% mass particle concentration is represented in<br />

Figure 2. Further tests were carried out investigating<br />

various scenarios, i.e. constant heat flux or constant<br />

flow rate. Different particle concentrations were also<br />

investigated, from 5.03 <strong>–</strong> 30.2%.<br />

Temperature [°C]<br />

64<br />

59<br />

54<br />

49<br />

44<br />

39<br />

34<br />

29<br />

24<br />

19<br />

Twall (mean) Twall (theory) Tfluid (theory) T1 T2<br />

0 0.02 0.04 0.06 0.08 0.1 0.12 0.14<br />

Distance from Thermal Entrance, x [m]<br />

Figure 2: Experimental and Theoretical Wall<br />

Temperatures plotted against distance downstream (Re<br />

= 3.6 and q″ = 11077.8 W/m 2 )<br />

Discussion<br />

From the experimental conditions examined, there is<br />

very agreement in the temperatures until the wall value<br />

reaches the onset melt temperature. Downstream of this<br />

experimental values deviate from predictions, resulting<br />

in and augmentation followed by a degradation in heat<br />

transfer. This is before the temperatures collapse once<br />

more, when the particles have changed from solid to<br />

liquid phase. Compared with single phase flows,<br />

MPCM slurries can provide temperature reductions up<br />

to 33%.<br />

References<br />

[1] El-Sebaii, AA, Al-Ghamdi, AA, Al-Hazmi, FS, et al.,<br />

2009, “Thermal performance of a single basin solar still with<br />

PCM as a storage medium”, Appl Energy; 86 (7<strong>–</strong>8):1187<strong>–</strong>95<br />

[2] Farid, M.M., Khudhair, A.M., Razack, S.A.K., Hallaj,<br />

A.A., 2004, “A review on phase change energy storage:<br />

materials and applications”, Energy Convers. Manage. 45<br />

1597<strong>–</strong>1615

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