2017
DOI: 10.1115/1.4036879
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Numerical Simulation of Evaporating Two-Phase Flow in a High-Aspect-Ratio Microchannel with Bends

Abstract: Flow boiling was investigated on a hydrophobic surface by coating Teflon® onto a 1×1 cm2 copper surface, resulting in contact angle of 118°. The images depicted were taken using distilled water flowing at 299 kg/m2s with 3°C subcooling. In the first series, the number of active nucleation sites increased as heat flux increased. For lower values of heat flux (< 80 kW/m2), vapor bubbles remained almost stationary on the surface. The hydrophobic contact angle makes the horizontal component of surface tension f… Show more

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Cited by 5 publications
(4 citation statements)
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“…Here: C v is the effective specific heat, is the airflow velocity, and D f is the diffusion coefficient (m 2 s −1 ). In addition, the mass out-flux at the droplet interface is given by 21 , 22 : where: is the interfacial velocity, is the outward unit vector at the interface, the vapor phase is designated by v , and the liquid phase is by f .…”
Section: Numerical Modelingmentioning
confidence: 99%
“…Here: C v is the effective specific heat, is the airflow velocity, and D f is the diffusion coefficient (m 2 s −1 ). In addition, the mass out-flux at the droplet interface is given by 21 , 22 : where: is the interfacial velocity, is the outward unit vector at the interface, the vapor phase is designated by v , and the liquid phase is by f .…”
Section: Numerical Modelingmentioning
confidence: 99%
“…Droplet surface evaporation into the air ambient can be included via utilizing diffusion-convection analogy, which can be written as 22 : Here: C v is the specific heat at constant volume, being airflow velocity, and D v is diffusion coefficient (m 2 s −1 ). The interfacial mass-flux at droplet fluid and air contact surface can be obtained through the adoption of the mass-conservation terms, which are 23 , 24 : Here: represents interfacial velocity, is outward unit vector being normal to droplet fluid-air interface, vapor phase is specified by v and liquid phase is by l . Therefore, change of velocity across the interface can be written as 24 : …”
Section: Numerical and Validation Studymentioning
confidence: 99%
“…The mass flux because of phase change at the interface boundary can be assessed using mass conservation at the droplet interface (droplet liquid–gas) , here, υ̅ is the velocity at the interface and being normal to the surface of liquid phase and n̅ is the unit vector, which points outward from the interface of liquid–gas (water–air), and g (subscripts) represents the gas phase. Hence, interfacial velocity jump ( u̅ – u ̅ g ) is …”
Section: Numerical Modelingmentioning
confidence: 99%
“…The mass flux because of phase change at the interface boundary can be assessed using mass conservation at the droplet interface (droplet liquid−gas) 36,37 ρ υ…”
mentioning
confidence: 99%