Abstract
The present work explores experimentally bubble dynamics in a single trapezoid microchannel with a hydraulic diameter of 41.3 μm. The fabrication process of the microchannel employs a silicon bulk micromachining and anodic bounding process. Bubble nucleation, growth, departure size, and frequency are observed using a high speed digital camera and analyzed by the Image-Pro. The results of the study indicates that the bubble nucleation in the microchannel may be predicted from the classical model with microsized cavities and the bubble typically grows with a constant rate from 0.13 to 7.08 μm/ms. Some cases demonstrate an extraordinarily high growth rate from 72.8 to 95.2 μm/ms. The size of bubble departure from the microchannel wall is found to be governed by surface tension and drag of bulk flow and may be fairly correlated by a modified form of Levy equation. The bubble frequency in the microchannel is comparable to that in an ordinary sized channel. The traditional form of frequency-departure-diameter relationship seems to be inexistent in the microchannel of this study.
| Original language | English |
|---|---|
| Pages (from-to) | 5575-5589 |
| Journal | International Journal of Heat and Mass Transfer |
| Volume | 47 |
| Issue number | 25 |
| Online published | 17 Sept 2004 |
| DOIs | |
| Publication status | Published - Dec 2004 |
| Externally published | Yes |
UN SDGs
This output contributes to the following UN Sustainable Development Goals (SDGs)
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SDG 9 Industry, Innovation, and Infrastructure
Research Keywords
- Boiling heat transfer
- Bubble dynamics
- Microchannel
- Onset nucleate boiling
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