2023
DOI: 10.1016/j.cej.2022.140374
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Liquid-liquid dispersion and flow characteristics in a miniaturized annular rotating device

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Cited by 17 publications
(5 citation statements)
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“…To quantify the effect of fluid flow and reaction on degradation efficiency in the microdevices, the dimensionless numbers (Reynolds number, Re; and Damkohler number, Da) are chosen. Re is the ratio of inertial and viscous forces . Da represents the relative time scale of chemical reactions compared to other phenomena in the same system.…”
Section: Methodsmentioning
confidence: 99%
See 1 more Smart Citation
“…To quantify the effect of fluid flow and reaction on degradation efficiency in the microdevices, the dimensionless numbers (Reynolds number, Re; and Damkohler number, Da) are chosen. Re is the ratio of inertial and viscous forces . Da represents the relative time scale of chemical reactions compared to other phenomena in the same system.…”
Section: Methodsmentioning
confidence: 99%
“…Re is the ratio of inertial and viscous forces. 26 Da represents the relative time scale of chemical reactions compared to other phenomena in the same system. Re and Da are defined as follows:…”
Section: Photocatalytic Degradation Experimentsmentioning
confidence: 99%
“…According to Equation (1), the crystal's terminal velocity [15] when suspended is approximately 1.61 m/s. According to Equation (3), the flow [16] rate required to suspend the crystal is approximately 1.64 L/s.…”
Section: Design Solutionsmentioning
confidence: 99%
“…In the past few decades, microfluidic technology has been rapidly developed into a prevailing method for generating droplets with controllable size and excellent monodispersity, which are widely used in numerous fields such as microreactions, , material synthesis, drug delivery, and so on. Compared to common microfluidic devices with T-junction, coflow, and flow-focusing configurations in which the regulation of the droplets’ generation mainly depends on the shearing force induced by another immiscible continuous phase, droplet formation in step emulsification is instead caused by the Rayleigh–Plateau instability of the liquid thread triggered by an abrupt change in flow confinement . Owing to the special breakup mechanisms, the size of droplets formed in step emulsification is therefore dominated by the geometric features of the device and the fluid wettability but is insensitive to the flow rates of both phases, which obviously contributes to the construction of parallelized microfluidic networks for the mass production of monodisperse droplets. , To rationally design the parallelized microfluidic networks, it is essential to reveal the droplet formation mechanisms in step emulsification and further establish the relevant regulation models of flow pattern and droplet size.…”
Section: Introductionmentioning
confidence: 99%
“…In the past few decades, microfluidic technology has been rapidly developed into a prevailing method for generating droplets with controllable size and excellent monodispersity, 1−3 which are widely used in numerous fields such as microreactions, 4,5 material synthesis, 6 drug delivery, and so on. 7−9 Compared to common microfluidic devices with Tjunction, 10−12 coflow, 13−15 and flow-focusing configurations in which the regulation of the droplets' generation mainly depends on the shearing force induced by another immiscible continuous phase, 16−19 droplet formation in step emulsification is instead caused by the Rayleigh−Plateau instability of the liquid thread triggered by an abrupt change in flow confinement.…”
Section: Introductionmentioning
confidence: 99%