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Article: Performance predictions for a new zeolite 13X/CaCl2composite adsorbent for adsorption cooling systems

TitlePerformance predictions for a new zeolite 13X/CaCl<inf>2</inf>composite adsorbent for adsorption cooling systems
Authors
KeywordsComposite adsorbent
Ion-exchange
Zeolite 13X
Adsorption cooling
Adsorption kinetics
Issue Date2012
Citation
International Journal of Heat and Mass Transfer, 2012, v. 55, n. 11-12, p. 3214-3224 How to Cite?
AbstractComposite adsorbents synthesized from zeolite 13X and CaCl2were investigated for applications in solar adsorption cooling systems. The effects of Ca ion exchange on the adsorption properties of zeolite 13X were studied. Ca ion exchange was found to decrease the specific surface area of the zeolite while increasing the total pore volume. Soaking zeolite 13X in 46 wt.% CaCl2solution for 24 h gave the optimum Ca ion exchange. The increase in the total pore volume facilitated further impregnating the zeolite with CaCl2. In all, 41.5 mol% of CaCl2was impregnated in the Ca-ion-exchanged zeolite from a 40 wt.% CaCl2solution to form the zeolite 13X/CaCl2composite adsorbent. A 0.4 g/g difference in equilibrium water uptake between 25 and 75°C at 870 Pa was recorded for the composite adsorbent. This was 420% of that of zeolite 13X under the same conditions. Numerical simulation predicts that an adsorption cooling system using the composite adsorbent could be powered by a low grade thermal energy source using the temperature range 75-100°C. Greatly improved efficiency is predicted compared to a system using pure zeolite 13X or impregnated silica gel. © 2012 Elsevier Ltd. All rights reserved.
Persistent Identifierhttp://hdl.handle.net/10722/255910
ISSN
2023 Impact Factor: 5.0
2023 SCImago Journal Rankings: 1.224
ISI Accession Number ID

 

DC FieldValueLanguage
dc.contributor.authorChan, K. C.-
dc.contributor.authorChao, Christopher Y.H.-
dc.contributor.authorSze-To, G. N.-
dc.contributor.authorHui, K. S.-
dc.date.accessioned2018-07-16T06:14:02Z-
dc.date.available2018-07-16T06:14:02Z-
dc.date.issued2012-
dc.identifier.citationInternational Journal of Heat and Mass Transfer, 2012, v. 55, n. 11-12, p. 3214-3224-
dc.identifier.issn0017-9310-
dc.identifier.urihttp://hdl.handle.net/10722/255910-
dc.description.abstractComposite adsorbents synthesized from zeolite 13X and CaCl2were investigated for applications in solar adsorption cooling systems. The effects of Ca ion exchange on the adsorption properties of zeolite 13X were studied. Ca ion exchange was found to decrease the specific surface area of the zeolite while increasing the total pore volume. Soaking zeolite 13X in 46 wt.% CaCl2solution for 24 h gave the optimum Ca ion exchange. The increase in the total pore volume facilitated further impregnating the zeolite with CaCl2. In all, 41.5 mol% of CaCl2was impregnated in the Ca-ion-exchanged zeolite from a 40 wt.% CaCl2solution to form the zeolite 13X/CaCl2composite adsorbent. A 0.4 g/g difference in equilibrium water uptake between 25 and 75°C at 870 Pa was recorded for the composite adsorbent. This was 420% of that of zeolite 13X under the same conditions. Numerical simulation predicts that an adsorption cooling system using the composite adsorbent could be powered by a low grade thermal energy source using the temperature range 75-100°C. Greatly improved efficiency is predicted compared to a system using pure zeolite 13X or impregnated silica gel. © 2012 Elsevier Ltd. All rights reserved.-
dc.languageeng-
dc.relation.ispartofInternational Journal of Heat and Mass Transfer-
dc.subjectComposite adsorbent-
dc.subjectIon-exchange-
dc.subjectZeolite 13X-
dc.subjectAdsorption cooling-
dc.subjectAdsorption kinetics-
dc.titlePerformance predictions for a new zeolite 13X/CaCl<inf>2</inf>composite adsorbent for adsorption cooling systems-
dc.typeArticle-
dc.description.naturelink_to_subscribed_fulltext-
dc.identifier.doi10.1016/j.ijheatmasstransfer.2012.02.054-
dc.identifier.scopuseid_2-s2.0-84859578085-
dc.identifier.volume55-
dc.identifier.issue11-12-
dc.identifier.spage3214-
dc.identifier.epage3224-
dc.identifier.isiWOS:000303550800047-
dc.identifier.issnl0017-9310-

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