Heat Transfer Coefficients for Particulate Airflow in Shell and Coiled Tube Heat Exchangers
In this work, we experimentally study heat transfer
from exhaust particulate air of detergent spray drying tower to water
by using coiled tube heat exchanger. Water flows in the coiled
tubes, where air loaded with detergent particles of 43 micrometers
in diameter flows within the shell. Four coiled tubes with different
coil pitches are used in a counter-current flow configuration. We
investigate heat transfer coefficients of inside and outside the heat
transfer surfaces through 400 experiments. The correlations between
Nusselt number and Reynolds number, Prandtl number, mass flow
rate of particulates to mass flow rate of air ratio and coiled tube
pitch parameter are proposed. The correlations procured can be used
to predicted heat transfer between tube and shell of the heat
exchanger.
[1] Su Thet Mon Than, Khin Aung Lin, Mi Sandar Mon, 2008, Heat
exchanger design, Proceedings of world academy of science, Engineering
and technology, 36: 619-626.
[2] P.Naphon, 2006, A review of flow and heat transfer characteristics in
curved tubes, Renewable and sustainable energy reviews, 10: 463-490.
[3] A.nuntaphan, T.Kiatsiriroat, 2007, Thermal behavior of spiral fin and
tube heat exchanger having fly ash deposit, Experimental thermal and
fluid science, 31: 1103-1109.
[4] D.G. Prabhanjan, G.S.V. Raghavan, T.J. Rennie, 2002, Comparison of
heat transfer rates between a straight tube heat exchanger and a helically
coiled heat exchanger, International communications of heat and mass
transfer, 29: 185-191.
[5] M.R. Salimpour, 2008, Heat transfer coefficient of shell and coiled tube
heat exchangers, Experimental thermal and fluid science.
[1] Su Thet Mon Than, Khin Aung Lin, Mi Sandar Mon, 2008, Heat
exchanger design, Proceedings of world academy of science, Engineering
and technology, 36: 619-626.
[2] P.Naphon, 2006, A review of flow and heat transfer characteristics in
curved tubes, Renewable and sustainable energy reviews, 10: 463-490.
[3] A.nuntaphan, T.Kiatsiriroat, 2007, Thermal behavior of spiral fin and
tube heat exchanger having fly ash deposit, Experimental thermal and
fluid science, 31: 1103-1109.
[4] D.G. Prabhanjan, G.S.V. Raghavan, T.J. Rennie, 2002, Comparison of
heat transfer rates between a straight tube heat exchanger and a helically
coiled heat exchanger, International communications of heat and mass
transfer, 29: 185-191.
[5] M.R. Salimpour, 2008, Heat transfer coefficient of shell and coiled tube
heat exchangers, Experimental thermal and fluid science.
@article{"International Journal of Chemical, Materials and Biomolecular Sciences:52043", author = "W. Witchayanuwat and S. Kheawhom", title = "Heat Transfer Coefficients for Particulate Airflow in Shell and Coiled Tube Heat Exchangers", abstract = "In this work, we experimentally study heat transfer
from exhaust particulate air of detergent spray drying tower to water
by using coiled tube heat exchanger. Water flows in the coiled
tubes, where air loaded with detergent particles of 43 micrometers
in diameter flows within the shell. Four coiled tubes with different
coil pitches are used in a counter-current flow configuration. We
investigate heat transfer coefficients of inside and outside the heat
transfer surfaces through 400 experiments. The correlations between
Nusselt number and Reynolds number, Prandtl number, mass flow
rate of particulates to mass flow rate of air ratio and coiled tube
pitch parameter are proposed. The correlations procured can be used
to predicted heat transfer between tube and shell of the heat
exchanger.", keywords = "Shell and coiled tube heat exchanger, Spray drying
tower, Heat transfer coefficients.", volume = "3", number = "5", pages = "240-5", }