2004
DOI: 10.1016/j.ijheatmasstransfer.2003.12.014
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Heat and mass transfer during absorption of ammonia vapour by LiNO3–NH3 solution droplets

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Cited by 24 publications
(17 citation statements)
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“…At this regard, it is important to note that in non adiabatic absorption large incre ments of absorbate mass fraction and temperature can occur, being in that case recommendable to calculate the local variation of working pair properties with X and T (see for example [28]). This contrasts with adiabatic absorption for which the assumption of unvarying properties in the mixture is particularly suited because potential increments of T and, above all, X are significantly smaller [3,23], as demonstrated in Appendix A.…”
Section: Physical Model and General Assumptionsmentioning
confidence: 99%
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“…At this regard, it is important to note that in non adiabatic absorption large incre ments of absorbate mass fraction and temperature can occur, being in that case recommendable to calculate the local variation of working pair properties with X and T (see for example [28]). This contrasts with adiabatic absorption for which the assumption of unvarying properties in the mixture is particularly suited because potential increments of T and, above all, X are significantly smaller [3,23], as demonstrated in Appendix A.…”
Section: Physical Model and General Assumptionsmentioning
confidence: 99%
“…(iii) The equilibrium mass fraction of absorbent at the free sur face, under small thermal variations, is commonly expressed (see for example, [23,33]) as a linear function of the solution temperature:…”
Section: mentioning
confidence: 99%
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“…The last method is an alternative to conventional designs of absorbers that has received increasing attention in the last years; among others, Ryan [3], Ryan et al [4], Summerer et al [5], Venegas et al [6,7], Arzoz et al [8], Warnakulasuriya and Worek [9,10], Palacios et al [11,12], Acosta-Iborra et al [13], Gutiérrez [14], Zacarías [15] and Ventas [16]. In this configuration, the heat and mass transfer processes are separated into two different devices: the single-phase solution subcooler and the absorption chamber.…”
mentioning
confidence: 99%
“…Venegas et al (2004Venegas et al ( , 2005 and Arzoz et al (2005) The literature review about recent publications in the field of adiabatic absorption using aqueous LiBr or lithium-based liquid absorbents is presented by Gutiérrez-Urueta et al (2011). This includes the works reported by Warnakulasuriya and Worek (2006), Elperin et al (2007) and Wang et al (2007).…”
Section: Introductionmentioning
confidence: 99%