Single-phase thermal and hydraulic performance of embedded silicon micro-pin fin heat sinks using R245fa
- Authors
- Kong, D.; Jung, K.W.; Jung, S.; Jung, D.; Schaadt, J.; Iyengar, M.; Malone, C.; Kharangate, C.R.; Asheghi, M.; Goodson, K.E.; Lee, H.
- Issue Date
- Oct-2019
- Publisher
- Elsevier Ltd
- Keywords
- Embedded cooling; Heat transfer; Micro-pin fin; Microfluidic cooling; Pressure drop; Thermal management
- Citation
- International Journal of Heat and Mass Transfer, v.141, pp 145 - 155
- Pages
- 11
- Journal Title
- International Journal of Heat and Mass Transfer
- Volume
- 141
- Start Page
- 145
- End Page
- 155
- URI
- https://scholarworks.bwise.kr/cau/handle/2019.sw.cau/34081
- DOI
- 10.1016/j.ijheatmasstransfer.2019.05.073
- ISSN
- 0017-9310
1879-2189
- Abstract
- Aggressive thermal management strategies such as liquid cooling have become essential for high-performance three-dimensional (3D) integrated circuit (IC) chips. Micro-pin fin arrays integrated between stacks can provide superior thermal performance with relatively less pumping power compared to microchannel cooling. In this work, we experimentally studied the single-phase heat transfer and pressure drop characteristics of micro-pin fin arrays. Three different samples consisting of 31–131 rows of cylindrical micro-pin fins with pin diameters Dh = 45–100 μm, center-to-center pin spacings S = 74–298 μm, and pin height Hf ∼ 200 μm were tested. Dielectric fluid R245fa was used as the working fluid with mass flow rates ṁ = 14.7–181.6 g/min and corresponding Reynolds numbers Re = 35–481.3. The heat fluxes ranged from 2.5 W/cm2 to 48.7 W/cm2, and the inlet fluid temperature was maintained at ambient temperature in the range of 22.2–25.3 °C. The local heater temperature distributions, average heat transfer characteristics, and pressure drops for various geometries of the embedded microfluid pin–fin arrays were determined. The experimentally determined heat transfer coefficient varied with both the mass flow rate and pin spacing with an averaged heat transfer coefficient of up to 18.2 kW/(m2·K). Full-scale conjugate simulations with a turbulence model were conducted using ANSYS Fluent to validate the experimental results for the three cases. A comparison with the numerical model showed mean absolute errors of 9.1% for the heat transfer and 14.3% for the pressure drop. © 2019 Elsevier Ltd
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