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ADDITIONAL TECHNICAL PAPERS

Choosing Working Fluid for Two-Phase Thermosyphon Systems for Cooling of Electronics

[+] Author and Article Information
Björn Palm, Rahmatollah Khodabandeh

Royal Institute of Technology, Department of Energy Technology, Stockholm, Sweden

J. Electron. Packag 125(2), 276-281 (Jun 10, 2003) (6 pages) doi:10.1115/1.1571570 History: Received February 26, 2000; Revised May 17, 2002; Online June 10, 2003
Copyright © 2003 by ASME
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References

Figures

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Product of heat of vaporization and density versus saturation pressure
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Figure of merit for one-phase vapor flow pressure drop as a function of saturation pressure
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Figure of merit for one-phase vapor pressure drop as a function of saturation temperature
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Boiling heat transfer coefficients according to Cooper 3 and Gorenflo 2 versus reduced pressure for two fluids with different molecular weight
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Heat transfer coefficients according to Cooper’s pool boiling correlation versus saturation temperature for different fluids
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Critical heat flux of different fluids according to Lienhard and Dhir correlation 45
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Schematic drawing of simulated system
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Pressure drop in simulated system with 3 mm i.d. riser and downcomer and isobutane as refrigerant
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Vapor fraction in the riser vs. heat load for different fluids with 3 mm i.d. in riser and downcomer

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