...). Furnaces and Combustors Numerical Methods Radiation 01 February 1995 01 August 1995 05 12 2007 22.5 20.0 E= 0 ° z 17.5 ls.o I= .~ 12.5 = 100 t = 7.5 Pr =0.71 y = 0.01~, c o 5.0 ¢J ~, 2.5 0.01 0.0 0.1 0.2 0.3 0.6 0.5 0.6 0.7 Dimensionless vertical distance, X Fig. 4 Convective...

...: Furnaces and Combustors, Measurement Techniques, Thermophysical Properties. Associate Technical Edi- tor: W. L. Grosshandler. B~CKBOO~ ~ x1 QUARTZ TUBE I~- 95 mm ID x 100 rnm OD x 1.8 m LONG H20 IS ORDER SORTING FILTER FOCUSING LENS . . . . . . . . ~ ~R~.RO~rOR R [~ H20 OUT COPPER COOLING TE if'w,) Fig, 1...

... Materials, Vol. 3: Ferrous Alloys, Thermophysical Properties Research Cen- ter, Purdue Univ., McMillan. Vu, B. T., and Gouldin, F. C , 1982, "Flow Measurements in a Model Swirl Combustor," AlAA Journal, Vol. 20, pp. 642-651. Transactions of the ASME Forced Convection Furnaces and Combustors Rotating...

... equivalence ratios. 01 August 1991 01 January 1993 23 05 2008 Combustion Furnaces and Combustors Porous Media P.-F. Hsu J. R. Howell R. D. Matthews Department of Mechanical Engineering, The University of Texas at Austin, Austin, TX 78712 A Numerical Investigation of Premixed...

... actually increase the overall heat transfer rate under certain conditions. 01 February 1992 01 November 1992 23 05 2008 Furnaces and Combustors High-Temperature Phenomena Liquid Metals R. H. Hurt T. H. Fletcher1 Combustion Research Facility, Sandia National Laboratories...

...R. Siegel 01 February 1992 01 June 1992 23 05 2008 Furnaces and Combustors Radiation I 0.07 0.06 0.05 - 0.04 0.03 0.02 0.01 0.00 0.01 Dimensionless Time Fig. 6 Comparisons of buildup of solidified layer in a pipe based on integral method, one-dimensional, and two...

... that account for the physical properties. 01 April 1991 01 January 1992 23 05 2008 Furnaces and Combustors Heat Exchangers Radiation Interactions J. R. Markham P. E. Best1 P. R. Solomon Z. Z. Yu Advanced Fuel Research, Inc., East Hartford, CT 06108 Measurement of Radiative...

...R. Siegel 27 November 1989 22 March 1990 23 05 2008 Furnaces and Combustors Radiation Nusselt number decreases rapidly for A < 5, especially for large Ra° values. Beyond this value, the decrease becomes less, which suggests that the Nusselt number could reach an asymp...

... to its surface and an infinite parallel slab radiating to one of its surfaces are presented to demonstrate quantitatively the mathematical behavior of the two mean beam lengths. Furnaces and Combustors Modeling and Scaling Radiation 11 October 1988 23 05 2008 W. W. Yuen Department...

...B. T. F. Chung; M. M. Kermani 26 May 1988 20 10 2009 Furnaces and Combustors Radiation Hale, N. W., and Viskanta, R., 1980, "Solid-Liquid Phase-Change Heat Transfer and Interface Motion in Materials Cooled or Heated From Above or Below," International Journal of Heat and Mass...

... Conditioning, The Technical University of Denmark, Lyngby, Denmark. Contributed by the Heat Transfer Division for publication in the JOURNAL OF HEAT TRANSFER. Manuscript received by the Heat Transfer Division January 5, 1988. Keywords: Furnaces and Combustors, Radiation, Radiation Interac- tions. Fig, 1...

..., Contributed by the Heat Transfer Division and presented at the ASME Winter Annual Meeting, Boston, Massachusetts, December 13-18, 1987. Manuscript received by the Heat Transfer Division May 1, 1988. Keywords: Furnaces and Combustors, Measurement Techniques. 1970; Gopalsami and Raptis, 1984; O'Fallon, 1984...