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Book ChapterDOI

Direct Contact Heat Transfer Between Immiscible Liquids

TLDR
In this paper, heat transfer to drops moving in a constant-temperature field and continuously varying temperature field is discussed, and three models are taken into account: rigid drop, completely mixed drop, and drop with internal circulation.
Abstract
Publisher Summary The basic characteristics of heat transfer between dispersed and continuous media are of both scientific and practical interest. The advantages of direct-contact heat transfer over the conventional processes using metallic transfer surfaces have lately stimulated research on its utilization for water desalination projects. Despite intensive efforts toward better understanding of transfer phenomena between drops and continuous media, accurate prediction of the transfer coefficients for a given system can as yet only be hoped for. Nevertheless, accumulated experience may provide an indication of the transfer mechanism to be encountered and the relevant coefficients may be estimated accordingly. This chapter discusses heat transfer to drops moving in a constant-temperature field and continuously varying temperature field. Heat is transferred to drops and bubbles with simultaneous phase change. While discussing about constant-temperature field, three models are taken into account: rigid drop, completely mixed drop, and drop with internal circulation. Work on direct-contact heat exchangers was stimulated earlier by the quest for economic water-desalination units. Multiphase exchange, where latent heat is transferred among the immiscible fluids, has been effectively used in direct-contact freezing units in which a dispersed volatile fluid evaporates in the saline water with simultaneous freezing of part of the water.

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Citations
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Longitudinal dispersion in two-phase continuous-flow operations: solution and tables for cocurrent flow

TL;DR: In this article, the mathematical derivation of solutions for longitudinal dispersion in chemical-process equipment is extended to the case of cocurrent flow and the extent of completion of the process, in dimensionless form, is given as an analytical function of rates of dispersion.
Journal ArticleDOI

Investigation of flow and temperature patterns in direct contact condensation using PIV, PLIF and CFD

TL;DR: In this paper, the authors used Particle Image Velocimetry (PIV) and Planar Laser Induced Fluorescence (PLIF) to measure the velocity and temperature of steam injected centrally at the bottom of a vertical rectangular water vessel.
Journal ArticleDOI

Gas‐Liquid Direct‐Contact Evaporation: A Review

TL;DR: In this paper, a review of the literature regarding gas-liquid direct contact evaporators is presented, addressing classic and potential applications, bubble regimes, gas holdup and bubble size distributions, as well as mathematical models proposed for simulating the unit.
Book ChapterDOI

Direct Contact Condensation

TL;DR: Direct contact condensation (DCC) as mentioned in this paper is used in many chemical process industries, usually for quenching and partial or total condensation, particularly when corrosive vapors are involved.

Simulation of heat and mass transfer in spray drying

TL;DR: In this article, a survey of heat and mass transfer around droplets in spray dryers and the diffusional transport inside them is given, which includes variable diffusion coefficients in the drying liquid and swelling or shrinking of droplets.
References
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Longitudinal dispersion in two-phase continuous-flow operations: solution and tables for cocurrent flow

TL;DR: In this article, the mathematical derivation of solutions for longitudinal dispersion in chemical-process equipment is extended to the case of cocurrent flow and the extent of completion of the process, in dimensionless form, is given as an analytical function of rates of dispersion.
Journal ArticleDOI

Mass transfer from drops and bubbles

TL;DR: In this paper, the authors reported experimental values and semi-theoretical formulae for the rates of solution of drops and bubbles under forced convection conditions, and discussed the effect of surface active agents on the mass transfer rate.
Journal ArticleDOI

Longitudinal Dispersion in Two-Phase Continuous-Flow Operations

TL;DR: In this paper, a simplified diffusion model was developed for general and specific cases of longitudinal dispersion accompanying mass transfer or heat transfer, which assumes a mean longitudinaldispersion coefficient and a mean velocity for each phase.
Journal ArticleDOI

Mass transfer from a solid soluble sphere to a flowing liquid stream

TL;DR: The Sherwood number was found independent of the laminar-turbulent transition for pipe flow and the sphere-to-column-diameter ratio when the Reynolds number is based on the average fluid velocity and sphere diameter as discussed by the authors.
Journal ArticleDOI

Particle motions in sheared suspensions XI. Internal circulation in fluid droplets (experimental)

TL;DR: The circulation pattern inside fluid drops suspended in a liquid subjected to hyperbolic and to shear flow has been studied and compared with that predicted from a fluid mechanical theory which assumes that the drops remain spherical and that shear stresses are transmitted without diminution across the drop interface.
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