๐”– Bobbio Scriptorium
โœฆ   LIBER   โœฆ

Turbulent diffusion in the core of a pipe with uniform transverse flow at the walls

โœ Scribed by S. K. Suneja; R. H. Shea; D. T. Wasan


Publisher
American Institute of Chemical Engineers
Year
1972
Tongue
English
Weight
741 KB
Volume
18
Category
Article
ISSN
0001-1541

No coin nor oath required. For personal study only.

โœฆ Synopsis


An onolysia of point source turbulent diffusion of o gaseous tracer in the core of o circulor straight porous pipe with uniform tronsverse flow ot the walls is presented. Time overoged concentrotion distributions were measured ot four distances downstream from a point source locoted a t the axis of o fully developed turbulent flow of air in o 6-in. pipe. Experiments were run at overage velocities between 4.36 and 23.0 ft./sec. (corresponding to Reynolds numbers 12, OOO to 66,000) with injection velocities ranging from 0 to 0.170 ft./sec. and suction velocities from 0 to 0.048 ft./sec. The highest injection rate corresponded to 58% by volume of the moin streom. Good agreement is obtained between the experiment01 and the colculoted concentrotion profiles.

The present study shows thot the plume width of the dispersing tracer is considerably affected by the transverse flow. It olso shows thot the eddy diffusivity in the pipe core ond the radial moss flux increose with fluid injection and decrease with suction through the pipe walls. Also, for increasing values of ospect ratio, they increose in the cose of injection and decreose in the cose of fluid suction.


๐Ÿ“œ SIMILAR VOLUMES


Radial distribution of diffusivity in th
โœ B.J. Brinkworth; P.C. Smith ๐Ÿ“‚ Article ๐Ÿ“… 1973 ๐Ÿ› Elsevier Science ๐ŸŒ English โš– 541 KB

Tests are described which yield the radial distribution of the turbulent diffusivity for enthalpy (eddy diffusivity) for fully-developed flow of water in a smooth straight pipe, with Reynolds number 105. It is found that this closely resembles the distribution of the turbulent diffusivity for moment

Turbulent flow of gas through a circular
โœ E.H. Wissler; R.S. Schechter ๐Ÿ“‚ Article ๐Ÿ“… 1962 ๐Ÿ› Elsevier Science ๐ŸŒ English โš– 771 KB

Abstra&--A scheme is developed for computing concentration profiles when an arbitrary reaction occurs at the wall of a tubular reactor. Solutions are constructed using complete sets of orthogonal functions. For reactions which are not first order, it is necessary to solve an integral equation for th

THE BOUNDARY CONDITION AT AN IMPEDANCE W
โœ W. EVERSMAN ๐Ÿ“‚ Article ๐Ÿ“… 2001 ๐Ÿ› Elsevier Science ๐ŸŒ English โš– 221 KB

The boundary condition at an impedance wall in a duct with a steady mean #ow requiring the speci"cation of the normal component of acoustic particle velocity is examined. It is found that when implemented in the weak formulation of the "nite element method it can be considerably simpli"ed. The bound