2015
DOI: 10.1016/j.cep.2015.05.009
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Pressure drop and axial dispersion in industrial millistructured heat exchange reactors

Abstract: A B S T R A C THydrodynamic characterization by means of pressure drop and residence time distribution (RTD) experiments is performed in three millistructured heat exchange reactors: two Corning reactors (further referred to as Corning HP and Corning RT) and a Chart reactor. Pressure drop is measured for different flow rates and fluids. Fanning friction factor is then calculated and its evolution versus Reynolds number is plotted for each reactor, showing the influence of the geometrical characteristics of the… Show more

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Cited by 25 publications
(11 citation statements)
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“…There are several types of HEs, designed for specific applications: concentric tube HE, shell-and-tube HE, plate HE, shell-and-plate HE, among others. Recently, HE reactors have been considered as promising technologies for thermal control of exothermic reactions [56]. These allow fast mixing of reagents and temperature control, preventing undesirable generation of by-products [57].…”
Section: Heat Exchangersmentioning
confidence: 99%
“…There are several types of HEs, designed for specific applications: concentric tube HE, shell-and-tube HE, plate HE, shell-and-plate HE, among others. Recently, HE reactors have been considered as promising technologies for thermal control of exothermic reactions [56]. These allow fast mixing of reagents and temperature control, preventing undesirable generation of by-products [57].…”
Section: Heat Exchangersmentioning
confidence: 99%
“…It is well known that for a cylindrical channel, its value is 16/Re in laminar flow. Moreau et al [51] have reported some values of the Fanning factor for different milli-structured reactors.…”
Section: Pressure Dropmentioning
confidence: 99%
“…Moreau et al confirmed this assumption by performing residence time distribution (RTD) experiments in single-phase flow at liquid flow rates ranging between 50 and 183 mL min À 1 . [10] They correlated the plug flow behavior to the reactor geometry, designed to generate mixing structures that allow homogenization of the tracer over the cross-section. However, no RTD study about the influence of gas on the axial dispersion and liquid residence time in gasliquid flows is currently available.…”
Section: Introductionmentioning
confidence: 99%