2011
DOI: 10.1007/s00231-011-0875-8
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A comparison of three adsorption equations and sensitivity study of parameter uncertainty effects on adsorption refrigeration thermal performance estimation

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Cited by 10 publications
(6 citation statements)
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“…The similarity of the small value of the exponent, n, on the other hand suggests both carbons are highly activated as they have broad pore size distributions. 25 Comparing the results obtained here with those of Zhao et al 13 reveals significant differences. The maximum adsorbate capacities (x 0 ) obtained for the 207EA and WS-480 activated carbons in their work were a fraction of that obtained here (85 % and 55 %, respectively).…”
Section: Journal Of Chemical and Engineering Datasupporting
confidence: 45%
See 2 more Smart Citations
“…The similarity of the small value of the exponent, n, on the other hand suggests both carbons are highly activated as they have broad pore size distributions. 25 Comparing the results obtained here with those of Zhao et al 13 reveals significant differences. The maximum adsorbate capacities (x 0 ) obtained for the 207EA and WS-480 activated carbons in their work were a fraction of that obtained here (85 % and 55 %, respectively).…”
Section: Journal Of Chemical and Engineering Datasupporting
confidence: 45%
“…5−15 Few have addressed adsorption isotherms of the activated carbon/methanol pair, and the heat of adsorption data are scarce. 8,13,14 In this paper, we report multiple temperature methanol adsorption isotherms and their resulting isosteric heats of adsorption for two different commercial activated carbons: a granular activated carbon, 207EA, and a pelleted activated carbon, WS480. Although these carbons are used primarily for water treatment and volatile organic compound capture, respectively, 16 each is also readily available and relatively inexpensive.…”
Section: Introductionmentioning
confidence: 99%
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“…Summary of solar driven adsorption cycles for cooling application. -0.50612 x 10 -3 K -2 β 3 0.5329 x 10 -6 K -3 ACF-ethanol pair [5] x 0 0.797 kg ethanol/kg ACF D 1.716x10 -6 K -2 AC-methanol pair [28] x 0 0.28 kg/kg D 8.45x10 -7 K -2 n 2.08…”
Section: Discussionmentioning
confidence: 99%
“…The temperature at state 1 (T 1 ) is the ambient temperature at the beginning of a heating process. The concentration at state 1 ( x 1 ) can be calculated from Dubinin-Astakov (D-A) equation, which can be written as [21,22]:…”
Section: Isosteric Heating (Or Re-heating) Processmentioning
confidence: 99%