Volume 39 Issue 4
Jul.  2019
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YI Tianhao, CHEN Chaoyue, LEI Zuosheng, ZHAO Jianfu. Numerical Simulation of Bubble Dynamics and Heat Transfer during Pool Boiling in Microgravity[J]. Journal of Space Science, 2019, 39(4): 469-477. doi: 10.11728/cjss2019.04.469
Citation: YI Tianhao, CHEN Chaoyue, LEI Zuosheng, ZHAO Jianfu. Numerical Simulation of Bubble Dynamics and Heat Transfer during Pool Boiling in Microgravity[J]. Journal of Space Science, 2019, 39(4): 469-477. doi: 10.11728/cjss2019.04.469
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Numerical Simulation of Bubble Dynamics and Heat Transfer during Pool Boiling in Microgravity

doi: 10.11728/cjss2019.04.469

  • 1. State Key Laboratory of Advanced Special Steel, School of Materials Science and Engineering, Shanghai University, Shanghai 200444;

  • 2. Sino-European School of Technology, Shanghai University, Shanghai 200444;

  • 3. CAS Key Laboratory of Microgravity, Institute of Mechanics, Chinese Academy of Sciences, Beijing 100190;

  • 4. School of Engineering Science, University of Chinese Academy of Sciences, Beijing 100049

  • Received Date: 2019-05-06
  • Publish Date: 2019-07-15
    Abstract
  • A two-dimensional model of the single bubble is performed. The surface tension and Marangoni force are included in the momentum equation. In addition, the continuity equation and energy equation are modified to allow for the phase change. A thin superheated layer is considered in the numerical model. The vapor-liquid interface is captured by the phase field method. The variations of bubble dynamics and heat transfer during subcooling pool boiling in microgravity can be obtained by solving the coupled equations. The results show that the bubble changes from a hemisphere to an ellipsoid and eventually becomes a pear shape. The bubble can randomly move on the surface. Besides, the bubble exhibits non-axisymmetrical shape during growth period. Due to the effect of fluid flow, the temperature field above the bubble appears to be a mushroom shape. The bubble departure diameter and departure time are proportional to g-0.488 and g-1.113 respectively. The average heat flux on the heater surface is proportional to g0.229.

     

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