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Journal ArticleDOI

Direct method for the prediction of expanded bed height in liquid‐solid fluidization

TLDR
In this article, a simple correlation has been developed to predict the expansion of a liquid fluidized bed, consisting of particles varying in size and/or density, which is valid over the voidage range from ϵmf to ϵr = 0.96 and gives directly the expanded bed height.
Abstract
A simple correlation has been developed to predict the expansion of a liquid fluidized bed, consisting of particles varying in size and/or density, which is of the following form: The relationship is valid over the voidage range from ϵmf to ϵr = 0.96 and gives directly the expanded bed height Le without the determination of the bed porosity ϵe as in existing correlations. The size and density of the solids varied from 30/40 to 72/80 mesh BSS and from 1.67 to 4.33 gm/cm3 respectively while the range of Ret varied from 0.12 to 43.66. The standard deviation for measurements on unicomponent and multicomponent systems has been calculated to be 11.5% and 19.6% respectively at an L/D ratio of 2.0. On a etabli une correlation simple pour prevoir l'expansion d'un lit fluidise en phase liquide, forme de particules de dimensions et/ou de densite variables; cette correlation est de la forme suivante: Cette relation est valable sur une gamme de degre de vide de ϵmf a ϵe = 0.96, et fournit directement la hauteur Le du lit, sans qu'on ait a determiner la porosite ϵe du lit, comme c'est le cas pour les autres correlations existantes. Les dimensions des solides variaient entre 30/40 et 72/80 mailles BSS et leurs densites etaient comprises entre 1.67 et 4.33 g/cc, alors que Ret variait entre 0.12 et 43.66. On a calcule que pour un rapport L/D de 2, les ecarts normaux dans le cas des mesures effectuees dans des systemes a composants simples et multiples etaient respectivement de 11.5% et 19.6.%

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Citations
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Journal ArticleDOI

Oscillatory electrodissolution of metals

TL;DR: In this paper, the authors propose a method to solve the problem of the problem: 1.1.11.1] and 2.2.1:1.5.
Journal ArticleDOI

Predicting bed voidage in solid-liquid fluidization.

TL;DR: In this paper, the Richardson-Zaki18 equation (eRZ) was used to predict voidage in solid-liquid fluidization data and new experimental data were correlated to develop an explicit expression for bed voidage.
Journal ArticleDOI

Studies on the expansion characteristics of fluidised beds with silica-based adsorbents used in protein purification☆

TL;DR: The results confirm that the optimisation of the dynamic capacities as well as the dynamic adsorption rates of adsorbents in expanded-bed systems must take into account column design characteristics aswell as the physical/chemical features of the adsorbent particles, if the highest productivities of expanded- bed/fluidisation procedures are to be achieved with crude feedstocks from biotechnological applications.
Journal ArticleDOI

Design of a fluidized bed bioartificial liver.

TL;DR: The efficient fluidization, under optimized conditions, was proven through the follow-up of the head losses generated by the fluidized bed, and criteria for scaling up were determined.
Journal ArticleDOI

Fluidized bed reactors operating with immobilized enzyme systems: Design model and its experimental verification

TL;DR: A general model for the design of fluidized bed reactors operating with immobilized enzymes in spherical porous particles was presented and was solved for monosubstrate reactions following reversible Michaelis-Menten kinetics as well as competitive inhibition by the product.
References
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Journal ArticleDOI

Viscous flow in multiparticle systems: Slow motion of fluids relative to beds of spherical particles

TL;DR: In this paper, a mathematical treatment is developed on the basis that two concentric spheres can serve as the model for a random assemblage of spheres moving relative to a fluid, and the appropriate boundary conditions resulting from these assumptions enable a closed solution to be obtained satisfying the Stokes-Navier equations omitting inertia terms.
Journal ArticleDOI

The sedimentation of suspensions of closely-sized spherical particles

TL;DR: In this article, the Stokes stream function for flow past a single sphere is used in order to obtain an equation relating the settling velocity of a suspension of monosize spherical particles to the volume concentration of the solid phase.