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Featured researches published by Chunhua Sun.


Physics of Fluids | 2013

On the spatial stability of a liquid jet in the presence of vapor cavities

Ming Lü; Zhi Ning; Mei Lu; Kai Yan; Juan Fu; Chunhua Sun

A dispersion equation describing the effect of temperature differences on the stability of three-dimensional cylindrical liquid jets in the presence of vapor cavities is presented by the use of linear stability analysis. The mathematical model and its solving method are verified by comparing them with the data in the literature, and then the effect of temperature differences between jet and surrounding gas on the spatial stability of liquid jet is investigated. Some conclusions can be drawn from the results of this investigation: (1) the temperature difference destabilizes the liquid jet when the jet liquid is cooler than the surrounding gas, (2) the smallest atomized droplet without taking into account the effect of temperature differences is significantly larger than that when the effect of temperature differences is taken into account, (3) the effect of temperature differences on the stability of liquid jet has little relationship with azimuthal wave modes, (4) cavitation destabilizes the liquid jet wh...


Physics of Fluids | 2015

Spatial instability in annular swirling viscous liquid sheet

Kai Yan; Zhi Ning; Ming Lü; Chunhua Sun; Juan Fu; Yuanxu Li

The spatial linear instability of an annular swirling viscous liquid sheet moving in an inviscid gas medium was investigated. With both para-sinuous and para-varicose modes analyzed, results show that under certain conditions the mode difference for the maximum disturbance growth rate is small. However, the para-sinuous mode is always the dominant mode for an annular swirling viscous liquid sheet in the parameter range studied here. Liquid swirls have a stabilizing effect at low swirling strengths. Two regions were identified: the initial region, where the maximum disturbance growth rate decreases with increasing dimensionless liquid swirling strength, and a region of monotonic increase of maximum disturbance growth rate with increasing liquid swirling strength. The non-axisymmetric mode is the dominant mode when swirling strength is large in an annular liquid sheet. The drop in axial size of non-axisymmetric mode is larger than that for the axisymmetric mode. Liquid viscosity suppresses increases in the ...


Chinese Journal of Mechanical Engineering | 2014

Breakup of cavitation bubbles within the diesel droplet

Ming Lü; Zhi Ning; Kai Yan; Juan Fu; Yunchao Song; Chunhua Sun

Supercavitation in the diesel nozzle increases the instability of droplets in part due to the two-phase mixture, while the effect of cavitation bubbles on the instability of drops is still unclear. In order to investigate the breakup of cavitation bubbles within the diesel droplet, a new mathematical model describing the disturbance growth rate of the diesel bubble instability is developed. The new mathematical model is applied to predict the effects of fluids viscosity on the stability of cavitation bubbles. The predicted values reveal that the comprehensive effect of fluids viscosity makes cavitation bubbles more stable. Compared with the viscosities of air and cavitation bubble, the diesel droplet’s viscosity plays a dominant role on the stability of cavitation bubbles. Furthermore, based on the modified bubble breakup criterion, the effects of bubble growth speed, sound speed, droplet viscosity, droplet density, and bubble-droplet radius ratio on the breakup time and the breakup radius of cavitation bubbles are studied respectively. It is found that a bubble with large bubble-droplet radius ratio has the initial condition for breaking easily. For a given bubble-droplet radius ratio (0.2), as the bubble growth speed increases (from 2 m/s to 60 m/s), the bubble breakup time decreases(from 3.59 μs to 0.17 μs) rapidly. Both the greater diesel droplet viscosity and the greater diesel droplet density result in the increase of the breakup time. With increasing initial bubble-droplet radius ratio (from 0.2 to 0.8), the bubble breakup radius decreases (from 8.86 μm to 6.23 μm). There is a limited breakup radius for a bubble with a certain initial bubble-droplet radius ratio. The mathematical model and the modified bubble breakup criterion are helpful to improve the study on the breakup mechanism of the secondary diesel droplet under the condition of supercavitation.


Entropy | 2015

Study on Droplet Size and Velocity Distributions of a Pressure Swirl Atomizer Based on the Maximum Entropy Formalism

Kai Yan; Zhi Ning; Ming Lü; Chunhua Sun

A predictive model for droplet size and velocity distributions of a pressure swirl atomizer has been proposed based on the maximum entropy formalism (MEF). The constraint conditions of the MEF model include the conservation laws of mass, momentum, and energy. The effects of liquid swirling strength, Weber number, gas-to-liquid axial velocity ratio and gas-to-liquid density ratio on the droplet size and velocity distributions of a pressure swirl atomizer are investigated. Results show that model based on maximum entropy formalism works well to predict droplet size and velocity distributions under different spray conditions. Liquid swirling strength, Weber number, gas-to-liquid axial velocity ratio and gas-to-liquid density ratio have different effects on droplet size and velocity distributions of a pressure swirl atomizer.


Journal of Visualization | 2018

Study of effervescent jet breakup under gas expansion disturbance

Chunhua Sun; Zhi Ning; Xinqi Qiao; Ming Lv; Juan Fu; Jin Zhao; Xintao Wang

Effervescent jet breakup-based gas expansion disturbance was studied by the combination of experiment and numerical methods. A transparent outside-in-type atomizer was used to observe both internal and external gas–liquid flow behavior. Effects of internal flow patterns and flow rates on gas expansion bulge were experimentally studied. Further analysis on the disturbance of gas expansion on jet breakup was conducted through the numerical method. The present work showed the results of gas expansion disturbance exiting under various internal flow regimes. Increasing gas–liquid flow rates enlarges spray angle and gas expansion bulge, decreases adjacent gas bulges’ distance, and leads to a more stable spray. Detailed numerical results demonstrated that the gas expansion advancing jet breakup was enhanced by enlarging instantaneous gas volume and internal pressure. For efficient utilization of gas expansion potential energy, small bubble formation is suggested.Graphical Abstract


Meccanica | 2016

Temporal and spatial stability of liquid jet containing cavitation bubbles in coaxial swirling compressible flow

Ming Lü; Zhi Ning; Kai Yan; Juan Fu; Chunhua Sun


International Journal of Multiphase Flow | 2016

Acoustic performance of effervescent sprays by time–frequency method with different atomizer structures under different operating conditions

Chunhua Sun; Zhi Ning; Ming Lv; Kai Yan; Juan Fu


European Journal of Mechanics B-fluids | 2015

Interface instability mechanism of an annular viscous liquid sheet exposed to axially moving inner and outer gas

Kai Yan; Zhi Ning; Ming Lü; Chunhua Sun; Juan Fu; Yuanxu Li


Meccanica | 2018

Temporal analysis of breakup for a power law liquid jet in a swirling gas

Xintao Wang; Zhi Ning; Ming Lü; Chunhua Sun


Chinese Journal of Chemical Engineering | 2015

Instability and breakup of cavitation bubbles within diesel drops

Ming Lü; Zhi Ning; Kai Yan; Juan Fu; Chunhua Sun

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Zhi Ning

Beijing Jiaotong University

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Juan Fu

Beijing Jiaotong University

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Kai Yan

Beijing Jiaotong University

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Ming Lü

Beijing Jiaotong University

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Ming Lv

Beijing Jiaotong University

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Xintao Wang

Beijing Jiaotong University

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Yuanxu Li

Beijing Jiaotong University

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Jin Zhao

Beijing Jiaotong University

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Xinqi Qiao

Shanghai Jiao Tong University

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Yunchao Song

Beijing Jiaotong University

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