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Journal ArticleDOI

Deposition of magnetite particles from flowing suspensions under flow‐boiling and single‐phase forced‐convective heat transfer

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TLDR
In this article, the authors measured the deposition rate of colloidal magnetite particles under both single-phase forced-convective and flow-boiling conditions, and found that particle removal rates were significantly lower than deposition rates; analysis using the theory of turbulent bursts suggests a removal efficiency of only 10−9% for each turbulent burst.
Abstract
The deposition rate of colloidal magnetite particles was measured under both single-phase forced-convective and flow-boiling conditions. All measurements were made at alkaline pH where both the heat transfer surface and the surface of the magnetite particles appear to be negatively charged. For single-phase forced convection, the deposition rate constant is lower than the mass transfer coefficient for colloidal particles, and the difference is attributed to the force of repulsion between the negatively charged surfaces of the particle and substrate. The deposition rate measured under flow-boiling conditions is lower than that reported for the deposition of colloidal particles at neutral pH. The difference is, again, attributed to the force of repulsion between the particle and substrate. Particle removal rates were significantly lower than deposition rates; analysis using the theory of turbulent bursts suggests a removal efficiency of only 10−9% for each turbulent burst. The low removal efficiency is consistent with the particle diameter being significantly smaller than the thickness of the laminar sublayer in these tests. On a mesure la vitesse de deposition de particules de magnetite colloidales dans des conditions de convection forcee et d'ebullition monophasique. Toutes les rnesures ont ete prises a un pH alcalin ou la surface de transfert de chaleur et la surface des particules de magnetite semblent chargees negativement. Pour la convection forcee monophasique, la constante de vitesse de deposition est inferieure au coefficient de transfert de matiere pour les particules colloidales, et la difference est attribuee a la force de repulsion entre les surfaces chargees negativement de la particule et du substrat. La vitesse de deaposition mesuree dans des conditions d'ebullition est inferieure a celle publiee pour la deposition des particules colloidales a pH neutre. La difference est, de nouveau, attribuee a la force de repulsion entre la particule et le substrat. Les vitesses de retrait des particules sont considerable-ment plus petites que les vitesses de deposition; l'analyse par la theorie des elatements turbulents suggere une efficacite de retrait de seutement 10−9% pour chaque elatement turbulent. La faible efficacite de retrait est consistante avec le diametre des particules qui est nettement plus petit que l'epaisseur de la sous-couche laminaire dans ces essais.

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Citations
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Journal ArticleDOI

Influences of bubble formation on different types of heat exchanger fouling

TL;DR: In this article, a comparison of fouling of suspended particles under forced convective and sub-cooled flow boiling heat transfer is performed to investigate the effect of hydraulic parameters such as fluid velocity and also bubble generation.
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Surface properties of magnetite in high temperature aqueous electrolyte solutions: A review.

TL;DR: A generalized overview of existing experimental data on surface characteristics of magnetite at high temperatures is presented to provide evidences for interaction between particles, probability of deposition and eventual attachment to the steel surface at various pH and temperatures and can serve as a foundation for future surface studies aimed at optimizing plant performances and reducing of magnetites deposition.
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Experimental study of micro-particle fouling under forced convective heat transfer

TL;DR: In this article, a mathematical model is developed to formulate the asymptotic fouling resistance in terms of the mass transfer coefficient, thermophoresis velocity, and fluid shear rate.
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Migration–deposition coupling characteristics and influence of corrosion products on heat transfer in steam generators

TL;DR: In this paper , a comprehensive model of impurity migration and deposition, which considered deposition and removal processes under boiling conditions, was established to simulate the fouling characteristics of steam generators.
Journal ArticleDOI

Characterization of the deposition and transport of magnetite particles in supercritical water

TL;DR: In this paper, several online and offline techniques for characterizing the deposition and transport of magnetite particles in supercritical water were investigated using a once-through flow apparatus, where ferrous chloride and ferrous sulfate precursor solutions were injected into a 1.8m heated test section at temperatures ranging from 200°C to 400°C.
References
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Journal ArticleDOI

Formation of uniform spherical magnetite particles by crystallization from ferrous hydroxide gels

TL;DR: In this article, the formation of iron oxides by aging ferrous hydroxide gels at elevated temperatures was studied as a function of various parameters, including the nature of the anions present in the system.
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A sub layer model for the deposition of particles from a turbulent flow

TL;DR: In this article, the problem of deposition of particles from a turbulent gas stream is examined and the prediction for deposition, in both inertial and diffusional-controlled situations, are compared with available experimental data and show satisfactory agreement.
Journal ArticleDOI

Thermophoresis in liquids

TL;DR: In this paper, the thermophoretic velocity, vth, was related to the particle and liquid properties by an expression similar to Epstein's gas equation: V th =-0.26 kμ 2k+k p ρT ▽T.
Journal ArticleDOI

Rate of deposition of Brownian particles under the action of London and double-layer forces

TL;DR: In this paper, the rate of collection of Brownian particles under the influence of interaction forces between the collector surface and the particles is calculated by incorporating the interaction forces in the rate constant of a virtual, first order, chemical reaction taking place on the surface of the collector, and by solving the convective diffusion equation subject to that chemical reaction as a boundary condition.