Model and Energy Consumption Characteristics of Liquid Desiccant Regenerator with Ultrasonic Atomization[J]. Journal of refrigeration, 2018, 39(3).
DOI:
Model and Energy Consumption Characteristics of Liquid Desiccant Regenerator with Ultrasonic Atomization[J]. Journal of refrigeration, 2018, 39(3). DOI: 10.3969/j.issn.0253-4339.2018.03.092.
Model and Energy Consumption Characteristics of Liquid Desiccant Regenerator with Ultrasonic Atomization
A regenerator has a significant influence on the energy efficiency of a liquid desiccant system. A conventional packed regenerator has a low specific surface area
which leads to the huge size of the equipment. An ultrasonic atomization method can greatly increase the specific surface area of a regenerator through atomizing the liquid desiccant into micron droplets
which will certainly reduce the equipment size. For the sake of development of ultrasonic atomization regeneration technology
this paper describes a theoretical study conducted on an ultrasound-atomizing regenerator. A model for the ultrasound-atomizing regenerator was established based on some necessary assumptions
and the model was validated experimentally. An index of specific energy consumption (SEC) is also suggested
and the model is used to investigate the energy consumption characteristics of an ultrasound-atomizing regenerator under different regeneration conditions
including the inlet solution temperature and concentration
as well as the inlet regeneration air temperature and humidity. The following conclusions can be drawn from this study: 1) A lower solution temperature is beneficial to improving the efficiency of an ultrasound-atomizing regenerator
but it should satisfy the practical application requirements of liquid desiccant after the regeneration. 2) The SEC of the regeneration of the liquid desiccant shows a clear increase with an increase in the inlet solution concentration. The SEC increases by nearly 40% as the solution concentration increases from 0.28 to 0.33. 3) A higher regeneration air temperature will lead to lower energy efficiency. The SEC of the solution regeneration increases from 3.263 to 4.629 kJ/g as the regeneration air temperature increases from 30 to 41 ℃ under the conditions applied in this study. 4) The higher regeneration air humidity will lead to higher energy consumption. Under the simulation conditions described herein
the SEC of the solution regeneration increases from 3.23 to 10.56 kJ/g as the regeneration air humidity increases from 10 to 28 g/kg (dry air).