2019
DOI: 10.1016/j.ijrefrig.2018.12.012
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Modelling and experimental validation of an in-tube vertical falling film absorber with counter flow arrangement of solution and gas

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Cited by 12 publications
(3 citation statements)
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“…The atomization absorption and falling film absorption are coupled by the heat and mass transfer at the phase interface in the model. The model is validated by the reported data in the reference [8,27,28]. The improvement of two installation strategies on absorption effect is calculated by the verified model.…”
Section: Introductionmentioning
confidence: 84%
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“…The atomization absorption and falling film absorption are coupled by the heat and mass transfer at the phase interface in the model. The model is validated by the reported data in the reference [8,27,28]. The improvement of two installation strategies on absorption effect is calculated by the verified model.…”
Section: Introductionmentioning
confidence: 84%
“…Absorber is the fundamental equipment of the ARS, and its mass transfer area occupies more than 50% of the total system [8,9]. Meanwhile, the mass fraction difference of the inlet and outlet determines the mass flow rate of absorbent in the system, which influences the heat load of the generator and absorber.…”
Section: Introductionmentioning
confidence: 99%
“…Aminyavari et al validated a counter-current in-tube falling-film absorber model by experimental data, and the difference ranges between the calculated results and experimental data are 5.9%. Through the profile study among the length and solution mass fraction, temperature, and heat/mass transfer coefficient, the author mainly proposed that the control process was heat and mass transfer between the falling film and the interface.…”
Section: Introductionmentioning
confidence: 99%