2017
DOI: 10.1007/s11431-017-9176-9
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Numerical investigation on gas flow heat transfer and pressure drop in the shell side of spiral-wound heat exchangers

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Cited by 12 publications
(1 citation statement)
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“…Through experiments, Sharqawy et al 9 studied the influence of the flow structure on the performance of a heat exchanger, and Hu et al 10 established a heat transfer coefficient formula for mixed hydrocarbon refrigerant shellside boiling. Tang et al 11 found that the pressure drop and heat transfer coefficient of a gas-phase fluid on the shell side decreased with an increase in the winding angle. By establishing a three-dimensional numerical model, Zeng et al 12 found that geometric parameters, such as the outer diameter of the heat exchange tube, number of layers of the heat exchange tube, and axial spacing of the first layer of the heat exchange tube, have an important influence on the heat transfer performance and flow performance.…”
Section: Introductionmentioning
confidence: 99%
“…Through experiments, Sharqawy et al 9 studied the influence of the flow structure on the performance of a heat exchanger, and Hu et al 10 established a heat transfer coefficient formula for mixed hydrocarbon refrigerant shellside boiling. Tang et al 11 found that the pressure drop and heat transfer coefficient of a gas-phase fluid on the shell side decreased with an increase in the winding angle. By establishing a three-dimensional numerical model, Zeng et al 12 found that geometric parameters, such as the outer diameter of the heat exchange tube, number of layers of the heat exchange tube, and axial spacing of the first layer of the heat exchange tube, have an important influence on the heat transfer performance and flow performance.…”
Section: Introductionmentioning
confidence: 99%