"An investigation of nucleate boiling heat transfer in saturated pools of Normal Pentane, Normal Hexane and several mixtures of the two was conducted. The fluids were boiled from gold-plated, copper, cylindrical heat transfer surfaces, 4.96 inches long, and 1.048 inch in diameter. The heat transfer elements were boiled in varying vertical tube arrays at a pressure of 14.70 psia.
It was found that the mixtures boiled with a lower heat transfer coefficient than that for either pure component when boiled alone. When boiling in any of the tube bundle arrangements, the heat transfer coefficients for the upper tubes in the bundle were larger than the heat transfer coefficients for the same heaters in single tube tests. The extent of this increase depends upon the number of tubes in the array and the fluid being boiled.
A semi-emphirical [sic] single tube nucleate boiling correlation which correlates the heat flux as a function of reduced properties is derived and discussed"--Abstract, page iii.
Primrose, Russell A.
Flanigan, V. J.
Gaddy, J. L.
Johnson, James W., 1930-2002
Chemical and Biochemical Engineering
Ph. D. in Chemical Engineering
Phillips Petroleum Company
Atlantic Richfield Co.
University of Missouri--Rolla
viii, 198 pages
© 1974 Kenneth Wayne Wall, All rights reserved.
Dissertation - Restricted Access
Library of Congress Subject Headings
Heat -- Transmission
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Electronic access to the full-text of this document is restricted to Missouri S&T users. Otherwise, request this publication directly from Missouri S&T Library or contact your local library.http://laurel.lso.missouri.edu/record=b1067288~S5
Wall, Kenneth Wayne, "Nucleate boiling of N-Pentane, N-Hexane and several mixtures of the two from various tube arrays" (1974). Doctoral Dissertations. 309.
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