2012
DOI: 10.1016/j.ijrefrig.2010.07.019
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Reallocation of adsorption and desorption times for optimisation of cooling cycles

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Cited by 132 publications
(23 citation statements)
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“…Zeolite coated concept (5 plates) Finned flat tube þ loose grains [10] Finned tube þ consolidated [11] Exchanger Obtained results, in terms of temperature distribution are showed in Fig. 10.…”
Section: Exchanger Typementioning
confidence: 97%
“…Zeolite coated concept (5 plates) Finned flat tube þ loose grains [10] Finned tube þ consolidated [11] Exchanger Obtained results, in terms of temperature distribution are showed in Fig. 10.…”
Section: Exchanger Typementioning
confidence: 97%
“…Not only that in proposed case, it was observed that adsorption time is more than twice longer than the desorption time as well as the sum of desorption time, pre-cooling and pre-heating time. Aristov et al [31] also gave similar practical recommendations to manage cooling cycles with non-equal durations of adsorption and desorption time. Due to the longer adsorption time the total adsorption of the proposed cycle is higher than that of the the former cycle.…”
Section: Proposed Formermentioning
confidence: 99%
“…For instance, lithium nitrate was introduced into silica gel [76] and vermiculite [75] matrices and tested in typical AHS cycle (Fig. 5).…”
Section: Adsorptive Inter-seasonal Heat Storagementioning
confidence: 99%
“…This can be obtained by using new advanced heat exchangers [78,81,90], heat pipes [91], coating a heat exchanger fins with an adsorbent [60,61], etc. ; -optimization of AHS cycles due to a proper choice of durations of isobaric stages [76], heat and mass recovery [92], cascade cycles [93], etc. ; -improvement of AHS hardwire [94], first of all, an evaporator that operates at low temperature and pressure [88].…”
Section: Future Randd For Ahs Optimizationmentioning
confidence: 99%