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
Your Session has timed out. Please sign back in to continue.



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




Some tools below are only available to our subscribers or users with an online account.

Related Content

Customize your page view by dragging and repositioning the boxes below.

Related Journal Articles
Related eBook Content
Topic Collections

Sorry! You do not have access to this content. For assistance or to subscribe, please contact us:

  • TELEPHONE: 1-800-843-2763 (Toll-free in the USA)
  • EMAIL: asmedigitalcollection@asme.org
Sign In