2015
DOI: 10.1016/j.applthermaleng.2015.02.052
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SAPO-34 coated adsorbent heat exchanger for adsorption chillers

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Cited by 199 publications
(86 citation statements)
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“…The exothermic adsorption process of water and zeolite in combination with the saturation behavior caused by increasing temperature requires a cooling mass flow through the adsorption bed. Therefore valves V6 and V1 have to be open while valves V2 and V5 have to be closed.…”
Section: Adsorption Cooling Systemmentioning
confidence: 99%
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“…The exothermic adsorption process of water and zeolite in combination with the saturation behavior caused by increasing temperature requires a cooling mass flow through the adsorption bed. Therefore valves V6 and V1 have to be open while valves V2 and V5 have to be closed.…”
Section: Adsorption Cooling Systemmentioning
confidence: 99%
“…Freni et al compare the adsorption kinetics of SAPO‐34 granulates and coatings. The effective diffusivities for SAPO‐34 and water were measured in the range of k eff (50 – 80 °C) = 1.7 · 10 −11 – 1.97 · 10 −10 m 2 s −1 .…”
Section: Simulation Reviewmentioning
confidence: 99%
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“…In fact, similar concepts of adsorption heat exchangers have been studied by several researchers1317181920, but most were designed to dehumidify the air or to be used for adsorption refrigeration that focused on the mass-exchange process. To achieve the above-mentioned goals, four problems need to be solved: (1) novel desiccants that have an adequate moisture uptake capacity difference under two-cycle conditions should be invented; (2) sensible heat transfer should not be obviously weakened by the desiccant coated layer; (3) a matched control strategy with a DDX HP to achieve high efficiency at any mix of sensible and latent loads should be developed; and (4) the loss of sensible-load capacity due to operational mode switching should be minimized.…”
mentioning
confidence: 99%