2013
DOI: 10.1016/j.enconman.2012.07.025
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Theoretical and experimental investigation on the transient coupled heat and mass transfer in a radial flow desiccant packed bed

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Cited by 27 publications
(11 citation statements)
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“…The rapid absorption of desiccant at an initial period was because vapor pressure on the desiccant surface is less than the vapor pressure of experimental air. [13] The vapor pressure difference between desiccant surface and air steadily reduced with time. The maximum dehumidification rate was found to be 21.06 g water/min during the first period and decreased continually with time as shown in Figure 3.…”
Section: Dehumidification Processmentioning
confidence: 98%
“…The rapid absorption of desiccant at an initial period was because vapor pressure on the desiccant surface is less than the vapor pressure of experimental air. [13] The vapor pressure difference between desiccant surface and air steadily reduced with time. The maximum dehumidification rate was found to be 21.06 g water/min during the first period and decreased continually with time as shown in Figure 3.…”
Section: Dehumidification Processmentioning
confidence: 98%
“…It has a surface area of 150-500 m 2 /g with pore sizes ranging between 1.5 and 6 nm and heat of adsorption nearly equals 3000 kJ/kg [23]. Many times it has been used for desiccant dehumidification and gives interesting results [32][33][34].…”
Section: Activated Aluminamentioning
confidence: 99%
“…Water sorption analysis of clinoptilolite shows that less dehumidification capability is compared to silica gel and alumina [49]. Activated alumina has shown satisfactory results when used for desiccant dehumidification [50]. Furthermore, use of liquid desiccants, for example, lithium chloride, lithium bromide, and calcium chloride results in good COP of desiccant air conditioning because it regenerates at lower temperature [51].…”
Section: Desiccant Materialsmentioning
confidence: 99%