Experimental characterization of random packed spheres, cylinders and rings, and their influence on pressure drop

2020 ◽  
Vol 222 ◽  
pp. 115644 ◽  
Author(s):  
Jennie von Seckendorff ◽  
Normen Szesni ◽  
Richard Fischer ◽  
Olaf Hinrichsen
1985 ◽  
Vol 39 (6) ◽  
pp. 916-920 ◽  
Author(s):  
R. K. Skogerboe ◽  
S. J. Freeland

This paper describes the results of the first stage of an investigation designed to extend present knowledge of the factors affecting aerosol production, transport, vaporization, and atomization in analytical spectroscopy systems. It focuses on factors controlling aspiration of aqueous solutions. The results demonstrate that the effect of gas flow on the pressure drop induced at the tip of the solution draw tube can be described by a simple linear equation; that the relationship between gas flow rate and solution nebulization rate can also be modelled by a simple equation; and that these relationships are not adequately represented by the Hagen-Poiseulle equation, as is often claimed.


2017 ◽  
Vol 173 ◽  
pp. 578-587 ◽  
Author(s):  
Zehua Guo ◽  
Zhongning Sun ◽  
Nan Zhang ◽  
Ming Ding ◽  
Jiming Wen

2003 ◽  
Vol 125 (1) ◽  
pp. 171-180 ◽  
Author(s):  
J. A. Mathias ◽  
J. Cao ◽  
M. E. Ewing ◽  
R. N. Christensen

This paper presents experimental pressure drop and heat transfer results of compact heat exchangers made with plain rectangular fins of short flowlengths tested with air at very low Reynolds numbers. Experiments were performed at sea level and at simulated elevated altitudes up to 25,298 m (83,000 ft). From the experimental results, the additional pressure drop of the air caused by the developing boundary layers and the hydrodynamic entrance length were determined. An equation was produced that predicted the average Nusselt number of the air, which significantly decreased with nondimensional length. The experimental results varied with respect to the aspect ratio of the rectangular duct and nondimensional length, which is inversely related to the Reynolds number.


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