Qingfei Bian , Yanwei Xie , Dagang Huang , Yao Zhao , Wei Li
{"title":"低速冲击下凝固阻力和液滴扩散动力学的相场模拟","authors":"Qingfei Bian , Yanwei Xie , Dagang Huang , Yao Zhao , Wei Li","doi":"10.1016/j.ijheatfluidflow.2025.110031","DOIUrl":null,"url":null,"abstract":"<div><div>Prediction of the droplet spreading process on a supercooled wall surface is important for advancing engineering applications. However, the complexity of this issue is exacerbated by multiple factors, including initial kinetic energy, wettability, physical properties of droplet, and the resistance force generated during the solidification process under wall supercooled conditions. After considering the phase field method, equivalent heat capacity model, and Kistler’s approach, we establish a numerical model to track the droplet spreading evolution bottomed on laminar flow governing equations in this paper. The droplet sectional shape and spreading length under various conditions are systematically investigated, with a focus on the evolution of solidification resistance and its dissipative effects on the spreading dynamics. Results reveal a distinct morphological evolution of the droplet spreading process, transitioning sequentially from a “spherical shape” to a “rounded cap”, followed by “pancake/cylinder” configurations, and ultimately stabilizing as a “shallow-tray” morphology. Solidification resistance dissipation critically modulates these transitions, with elevated supercooling suppressing droplet retraction kinetics while amplifying maximum spreading lengths and prolonged spreading durations. Under the interaction effect of solidification rate and velocity, the solidification resistance and dissipation first increase, then gradually decrease, ultimately approaching zero along with droplet spreading. Besides, reduced initial impact velocities also attenuate the sensitivity of spreading dynamics to variations in supercooled temperature. Notably, a total solidification resistance dissipation computation method assisted by numerical results is developed. Quantitative result demonstrates its efficacy in modifying the isothermal spreading length prediction model, achieving a maximum error of 10% and an average error of 4.8%.</div></div>","PeriodicalId":335,"journal":{"name":"International Journal of Heat and Fluid Flow","volume":"117 ","pages":"Article 110031"},"PeriodicalIF":2.6000,"publicationDate":"2025-09-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"Phase-field modeling of solidification resistance and droplet spreading dynamics under low-velocity impact\",\"authors\":\"Qingfei Bian , Yanwei Xie , Dagang Huang , Yao Zhao , Wei Li\",\"doi\":\"10.1016/j.ijheatfluidflow.2025.110031\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<div><div>Prediction of the droplet spreading process on a supercooled wall surface is important for advancing engineering applications. However, the complexity of this issue is exacerbated by multiple factors, including initial kinetic energy, wettability, physical properties of droplet, and the resistance force generated during the solidification process under wall supercooled conditions. After considering the phase field method, equivalent heat capacity model, and Kistler’s approach, we establish a numerical model to track the droplet spreading evolution bottomed on laminar flow governing equations in this paper. The droplet sectional shape and spreading length under various conditions are systematically investigated, with a focus on the evolution of solidification resistance and its dissipative effects on the spreading dynamics. Results reveal a distinct morphological evolution of the droplet spreading process, transitioning sequentially from a “spherical shape” to a “rounded cap”, followed by “pancake/cylinder” configurations, and ultimately stabilizing as a “shallow-tray” morphology. Solidification resistance dissipation critically modulates these transitions, with elevated supercooling suppressing droplet retraction kinetics while amplifying maximum spreading lengths and prolonged spreading durations. Under the interaction effect of solidification rate and velocity, the solidification resistance and dissipation first increase, then gradually decrease, ultimately approaching zero along with droplet spreading. Besides, reduced initial impact velocities also attenuate the sensitivity of spreading dynamics to variations in supercooled temperature. Notably, a total solidification resistance dissipation computation method assisted by numerical results is developed. Quantitative result demonstrates its efficacy in modifying the isothermal spreading length prediction model, achieving a maximum error of 10% and an average error of 4.8%.</div></div>\",\"PeriodicalId\":335,\"journal\":{\"name\":\"International Journal of Heat and Fluid Flow\",\"volume\":\"117 \",\"pages\":\"Article 110031\"},\"PeriodicalIF\":2.6000,\"publicationDate\":\"2025-09-01\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"\",\"citationCount\":\"0\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"International Journal of Heat and Fluid Flow\",\"FirstCategoryId\":\"5\",\"ListUrlMain\":\"https://www.sciencedirect.com/science/article/pii/S0142727X25002899\",\"RegionNum\":3,\"RegionCategory\":\"工程技术\",\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"Q2\",\"JCRName\":\"ENGINEERING, MECHANICAL\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"International Journal of Heat and Fluid Flow","FirstCategoryId":"5","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S0142727X25002899","RegionNum":3,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q2","JCRName":"ENGINEERING, MECHANICAL","Score":null,"Total":0}
Phase-field modeling of solidification resistance and droplet spreading dynamics under low-velocity impact
Prediction of the droplet spreading process on a supercooled wall surface is important for advancing engineering applications. However, the complexity of this issue is exacerbated by multiple factors, including initial kinetic energy, wettability, physical properties of droplet, and the resistance force generated during the solidification process under wall supercooled conditions. After considering the phase field method, equivalent heat capacity model, and Kistler’s approach, we establish a numerical model to track the droplet spreading evolution bottomed on laminar flow governing equations in this paper. The droplet sectional shape and spreading length under various conditions are systematically investigated, with a focus on the evolution of solidification resistance and its dissipative effects on the spreading dynamics. Results reveal a distinct morphological evolution of the droplet spreading process, transitioning sequentially from a “spherical shape” to a “rounded cap”, followed by “pancake/cylinder” configurations, and ultimately stabilizing as a “shallow-tray” morphology. Solidification resistance dissipation critically modulates these transitions, with elevated supercooling suppressing droplet retraction kinetics while amplifying maximum spreading lengths and prolonged spreading durations. Under the interaction effect of solidification rate and velocity, the solidification resistance and dissipation first increase, then gradually decrease, ultimately approaching zero along with droplet spreading. Besides, reduced initial impact velocities also attenuate the sensitivity of spreading dynamics to variations in supercooled temperature. Notably, a total solidification resistance dissipation computation method assisted by numerical results is developed. Quantitative result demonstrates its efficacy in modifying the isothermal spreading length prediction model, achieving a maximum error of 10% and an average error of 4.8%.
期刊介绍:
The International Journal of Heat and Fluid Flow welcomes high-quality original contributions on experimental, computational, and physical aspects of convective heat transfer and fluid dynamics relevant to engineering or the environment, including multiphase and microscale flows.
Papers reporting the application of these disciplines to design and development, with emphasis on new technological fields, are also welcomed. Some of these new fields include microscale electronic and mechanical systems; medical and biological systems; and thermal and flow control in both the internal and external environment.