Condensation of high-concentration NH3/H2O in plate heat exchangers

A combined model

Journal Article (2025)
Author(s)

Xuan Tao (Hangzhou City University)

Yunwei Shen (Hangzhou City University)

Haoren Wang (Hangzhou City University, Zhejiang University)

Bo Wang (Hangzhou City University)

Carlos Infante Ferreira (TU Delft - Engineering Thermodynamics)

Research Group
Engineering Thermodynamics
DOI related publication
https://doi.org/10.1016/j.applthermaleng.2025.128315
More Info
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Publication Year
2025
Language
English
Research Group
Engineering Thermodynamics
Bibliographical Note
Green Open Access added to TU Delft Institutional Repository 'You share, we take care!' - Taverne project https://www.openaccess.nl/en/publishing/publisher-deals Otherwise as indicated in the copyright section: the publisher is the copyright holder of this work and the author uses the Dutch legislation to make this work public.@en
Issue number
3
Volume number
280
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Abstract

NH3/H2O based systems are promising for thermal energy storage and thermal energy conversion. These systems are used for absorption energy storage and Kalina cycles. This paper investigates the condensation of high-concentration NH3/H2O in vertically downward plate heat exchangers. A combined method is proposed by discussing the applicability of equilibrium and non-equilibrium models. Both models are necessary for zeotropic mixtures with large temperature glide. The non-equilibrium model applies where the temperature glide is non-linear or the vapor is in non-equilibrium with the liquid. The equilibrium model becomes applicable with decreasing vapor qualities. Heat transfer correlations are proposed according to the equilibrium model, which interpret convective condensation and gravity-controlled condensation. The additional heat transfer resistance is calculated considering mass transfer. The non-equilibrium model is further developed quantifying the heat and mass transfer of vapor and neglecting the mass transfer resistance of the liquid. The non-equilibrium model transforms into the equilibrium model as the concentration gradient of vapor approaches zero. Additionally, a frictional pressure drop model for separated flow conditions is proposed and quantifies the two-phase shear force.

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