Results 161 to 170 of about 661 (214)

On axial dispersion in fixed beds

Chemical Engineering and Processing: Process Intensification, 1993
Abstract The primary purpose of this paper is to show that the criticisms by Tsotsas and Schlunder (1988) of an earlier paper (Gunn, 1969) are based upon elementary mathematical errors of the part of Tsotsas and Schlunder. A summary of experimental data on axial dispersion in liquids and gases shows that the dependence of the axial dispersion ...
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Dispersion of Axially Symmetric Waves in Elastic Rods

Journal of Applied Mechanics, 1962
The relation between frequency and propagation constant, for axially symmetric waves in an infinitely long, isotropic, circular rod, as given by Pochhammer’s equation, is explored. A spectrum, covering a large range of frequencies, is developed for real, imaginary, and complex propagation constants, and the influence of Poisson’s ratio is described.
Onoe, M., McNiven, H. D., Mindlin, R. D.
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Axial dispersion in packed fiber beds

The Chemical Engineering Journal and the Biochemical Engineering Journal, 1995
Abstract The application of fibrous sorbent materials in gas and liquid separations as an alternative to conventional granular sorbents has attracted increased attention over the last decade. Though axial dispersion of flow in granular beds has been investigated extensively, published experimental data concerning the dispersion phenomena in porous ...
G. van Zee, R. Veenstra, J. de Graauw
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Axial dispersion in beds of small particles

The Chemical Engineering Journal, 1972
Abstract Axial dispersion coefficients (EA) in beds of small (0.1–1 mm) particles are often needed to interpret reaction rate data. A chromatographic technique was used to evaluate such coefficients for beds of porous catalyst particles and beds of non-porous glass beads over a wide range of velocities (Rep = 0. 00237 to 11.9).
Motoyuki Suzuki, J.M. Smith
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Axial Dispersion of Sedimented Colloids

Separation Science and Technology, 1982
Abstract After an ensemble of identical particles has had time to settle along the y-axis to their equilibrium distribution in a field of potential energy %oS(y) by gravity, but prevented from adsorbing by double-layer repulsion, their dispersion by Poiseuille flow between two horizontal plates is predicted. The residence-time distribution of particles
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Axial dispersion in a reciprocating plate column

The Canadian Journal of Chemical Engineering, 1996
AbstractAxial mixing in a reciprocating plate column with different amplitudes has been investigated for single‐phase and two‐phase (air‐water) systems. Experiments were performed in water in a semi‐batch scheme (no water flow) in a 1.26 m high and 101.6 mm internal diameter column.It was found that the axial dispersion coefficient is a strong function
Mustapha Lounes, Jules Thibault
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Dynamics Of Axially Dispersed Reactors

Industrial & Engineering Chemistry Research, 2008
Axially dispersed reactors with simultaneous convection, dispersion, and reaction might be used to approximate real reactors. While the steady-state solution to an axially dispersed reactor is well-described in the literature, its dynamic behavior is not often discussed.
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Danckwerts' degree of segregation for the axial dispersion model

Chemical Engineering Science, 1991
Abstract Danckwerts' degree of segregation for the axial dispersion model has been calculated using some values of the Peclet number. The Monte Carlo technique has been applied to simulate a random walk, which is the discrete approximation of the axial dispersion model. The axial dispersion model's degree of mixing does not reach the state of maximum
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Axial dispersion through tube constrictions

AIChE Journal, 1980
AbstractTracer gas dispersion was measured for laminar flow through three different tube constrictions, at orifice Reynolds numbers between 10 and 5000 and Schmidt numbers of 0.213 and 0.769. Each constriction generates a confined jet which significantly enhances axial dispersion at intermediate Reynolds numbers ranging from 100 to 1000.
David W. Weaver, James S. Ultman
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Axial dispersion in coiled tubular reactors

Analytica Chimica Acta, 1986
Abstract A theoretical and experimental treatment of axial dispersion in coiled tubes is presented. The dispersion, δ, is related to the theoretical plate height divided by four times the radius of the tube (H/4r). This parameter, when plotted against the product of the Reynolds number and the Schmidt number (ReSc), accurately predicts maxima in ...
Denys F. Leclerc, Carr J. Smith, E.Clifford Toren   +2 more
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