TY - GEN
T1 - Computational Fluid Dynamics (CFD) Modeling of Falling Film Heat Transfer Over Horizontal Tube for Multi-effect Desalination (MED) Evaporator
AU - Tahir, Furqan
AU - Mabrouk, Abdelnasser
AU - Koç, Muammer
N1 - Publisher Copyright:
© 2022, The Author(s), under exclusive license to Springer Nature Switzerland AG.
PY - 2022
Y1 - 2022
N2 - Horizontal-type falling film evaporators are commonly used in multi-effect desalination (MED) plants, refrigeration, air conditioning and waste heat recovery application. In falling film evaporators, a thin liquid film covers the tube, and heat is transferred from the heating medium inside the tube to the thin film. The heat transfer in falling films is governed by the film hydrodynamics, temperature gradient and tube material. In order to analyze film heat transfer at microscopic level, computational fluid dynamics (CFD) tool is implemented in this work. A 25.4 mm horizontal tube with an impingement height of 5 mm is selected as the computational domain. Water enters at 65 °C that is the top brine temperature of MED plant. The liquid load and temperature difference varied from 0.01 kg/(m s) to 0.09 kg/(m s) and from 2 °C to 10 °C, respectively. It is found that the heat transfer coefficient is very high at the stagnation point and then decreases, as the flow moves along the tube surface. The recirculation in the film enhances the heat transfer. Furthermore, increasing liquid load from 0.01 to 0.09 kg/(m s) with ΔT = 5 °C, increase the heat transfer coefficient by 231%.
AB - Horizontal-type falling film evaporators are commonly used in multi-effect desalination (MED) plants, refrigeration, air conditioning and waste heat recovery application. In falling film evaporators, a thin liquid film covers the tube, and heat is transferred from the heating medium inside the tube to the thin film. The heat transfer in falling films is governed by the film hydrodynamics, temperature gradient and tube material. In order to analyze film heat transfer at microscopic level, computational fluid dynamics (CFD) tool is implemented in this work. A 25.4 mm horizontal tube with an impingement height of 5 mm is selected as the computational domain. Water enters at 65 °C that is the top brine temperature of MED plant. The liquid load and temperature difference varied from 0.01 kg/(m s) to 0.09 kg/(m s) and from 2 °C to 10 °C, respectively. It is found that the heat transfer coefficient is very high at the stagnation point and then decreases, as the flow moves along the tube surface. The recirculation in the film enhances the heat transfer. Furthermore, increasing liquid load from 0.01 to 0.09 kg/(m s) with ΔT = 5 °C, increase the heat transfer coefficient by 231%.
KW - CFD
KW - Falling film
KW - Heat transfer coefficient
KW - Horizontal tube
KW - Numerical model
UR - https://www.scopus.com/pages/publications/85129880198
U2 - 10.1007/978-3-030-76081-6_28
DO - 10.1007/978-3-030-76081-6_28
M3 - Conference contribution
AN - SCOPUS:85129880198
SN - 9783030760809
T3 - Advances in Science, Technology and Innovation
SP - 233
EP - 240
BT - Sustainable Energy-Water-Environment Nexus in Deserts - Proceeding of the 1st International Conference on Sustainable Energy-Water-Environment Nexus in Desert Climates
A2 - Heggy, Essam
A2 - Bermudez, Veronica
A2 - Vermeersch, Marc
PB - Springer Nature
T2 - 1st International Conference on Sustainable Energy-Water-Environment Nexus in Desert Climates, ICSEWEN 2019
Y2 - 2 December 2019 through 5 December 2019
ER -