2017
DOI: 10.1016/j.renene.2016.09.047
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Adsorbent working pairs for solar thermal energy storage in buildings

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Cited by 82 publications
(33 citation statements)
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“…Starting from the boundary conditions defined in the previous sections, the potential application of some adsorbent working pairs reported in the literature is analysed. In particular, the analysis is performed following the approach for the STES density calculation applied in [31], while the two most promising working pairs there reported, namely, MWCNT-LiCL and AQSOA Z02, with water as the working fluid are considered. The former one is a composite sorbent, using multi-wall carbon nanotubes (MWCNT) as a support matrix and LiCl as hygroscopic salt [23], while the latter one is a pure adsorbent material, belonging to the zeotype family [28].…”
Section: Potential Assessment Of Different Working Pairs For Stes Appmentioning
confidence: 99%
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“…Starting from the boundary conditions defined in the previous sections, the potential application of some adsorbent working pairs reported in the literature is analysed. In particular, the analysis is performed following the approach for the STES density calculation applied in [31], while the two most promising working pairs there reported, namely, MWCNT-LiCL and AQSOA Z02, with water as the working fluid are considered. The former one is a composite sorbent, using multi-wall carbon nanotubes (MWCNT) as a support matrix and LiCl as hygroscopic salt [23], while the latter one is a pure adsorbent material, belonging to the zeotype family [28].…”
Section: Potential Assessment Of Different Working Pairs For Stes Appmentioning
confidence: 99%
“…For instance, referring to Scenario 1, the energy density when 10% of the space heating needs are covered by the STES is up to 20% higher than the density achievable when 60% of the space heating needs are covered by the STES. The effect of this analysis is even more important when comparing the STES density that can be estimated with this proposed approach against the typical approaches reported in the literature [28,30,31], where, usually, fixed temperature boundary conditions are considered, regardless of the ambient temperature variability typical of each climatic zone. Indeed, considering, for instance, a constant T ads = 35 • C for providing space heating throughout the winter, when the STES coverage fraction is 60%, the evaluated density is underestimated in a range between 10% and 40%, depending on the working pair and scenario analysed.…”
Section: Potential Assessment Of Different Working Pairs For Stes Appmentioning
confidence: 99%
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“…Here, the energy density is an integrated heat from the initial discharging conditions, i.e., the temperature and pressure at the end of the discharging process. In some cases, the heat of adsorption is assumed constant, and thus, the energy density is calculated considering the uptake difference [47]. For low-pressure adsorption, the adsorbed phase density and nonideality are rather insignificant, whereas these factors must be considered in calculating the isosteric heat of adsorption.…”
Section: Selection Of Working Pairmentioning
confidence: 99%
“…Heat is supplied and extracted via heat exchangers. Due to its favorable properties, many potential working pairs using water as the sorbate have been investigated, e.g., silica gel [4], zeolites [5,6], aluminum phosphates (AlPOs) [7], metal organic frameworks (MOFs) [8], activated carbon, and a variety of composites [4,7].…”
Section: Introductionmentioning
confidence: 99%