1959
DOI: 10.1063/1.3060727
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Fluid Dynamics and Heat Transfer

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Cited by 299 publications
(224 citation statements)
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“…It is important that the flow be laminar so that the sample environment can be accurately determined. Poiseuille flow within the chamber results in a parabolic velocity profile due to the wall separation being small compared to the cylinder radii (Knudsen and Katz, 1958). In the older horizontal flat plate designs, the aerosol laminar remained centred between the plates, but with vertical chambers there is the added complication of buoyant circulation due to the temperature gradient, (Sinnarwalla and Alofs, 1973): air near the cold wall will tend to sink; air near the warm wall will tend to rise.…”
Section: Principle Of Operationmentioning
confidence: 99%
“…It is important that the flow be laminar so that the sample environment can be accurately determined. Poiseuille flow within the chamber results in a parabolic velocity profile due to the wall separation being small compared to the cylinder radii (Knudsen and Katz, 1958). In the older horizontal flat plate designs, the aerosol laminar remained centred between the plates, but with vertical chambers there is the added complication of buoyant circulation due to the temperature gradient, (Sinnarwalla and Alofs, 1973): air near the cold wall will tend to sink; air near the warm wall will tend to rise.…”
Section: Principle Of Operationmentioning
confidence: 99%
“…Graetz in 1885 developed an infinite series solution to the analogous problem of heat transfer under the condition of constant wall temperature [Knudsen & Katz, 1958]. The solution can be immediately applied to mass transfer with constant wall concentration, simply substituting the Sherwood and Smidth numbers to the Nuselt and Prandtl numbers.…”
Section: Mass Transfer In Hollow Fibre Lumenmentioning
confidence: 99%
“…Mass or heat transport for laminar flow in various geometries and under various boundary conditions was investigated by several authors, beginning with the classical work of Graetz for heat transfer in circular ducts with constant wall temperature [Knudsen & Katz, 1958]. Reference can be made to the work of [Siegel et al, 1958] for heat transfer in circular duct with uniform heat flux, [Hatton & Quarmby, 1962] for annular ducts and [Nunge and Gill, 1966] for a tube in tube heat exchanger.…”
Section: Mass Transfer In Hollow Fibre Contactorsmentioning
confidence: 99%
“…The friction factor varies for different ratios of ⁄ , see Figure 2 for explanation. Equation (23) shows the equation from Cornish, Lea and Tadros, reproduced in Knudsen and Katz [13] for calculation of the friction factor for rectangular conduits. The equation has been adjusted by a factor 4 because the Darcy friction factor is 4 times larger than the friction factor defined in [12].…”
Section: Pressure Dropmentioning
confidence: 99%