Formation of drops at narrow slots in a centrifugal liquid-liquid contactor

In experiments on the dispersion of organic phases into aqueous phases, drops were generated continuously at narrow slots of width 12 μm ≤ w ≤ 125 μm mounted peripherally and normal to the radius in a ‘Hi‐Gee’ centrifugal contactor. The drops formed at an array of sources attributed to the Rayleigh‐...

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Veröffentlicht in:Canadian journal of chemical engineering 2000-10, Vol.78 (5), p.876-883
Hauptverfasser: Wadley, Robert, Lee, Jonathan G.M., Wraith, Albert E.
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description In experiments on the dispersion of organic phases into aqueous phases, drops were generated continuously at narrow slots of width 12 μm ≤ w ≤ 125 μm mounted peripherally and normal to the radius in a ‘Hi‐Gee’ centrifugal contactor. The drops formed at an array of sources attributed to the Rayleigh‐Taylor instability distributed an average distance apart where σ is the interfacial tension of the phases, Δρ their density difference and g the applied centrifugal acceleration. Measured Sauter mean drop diameters were in the range 0.48 to 1.00 mm. The average drop size, d, was given by where d̄* = 0.1538 ± 0.0016 m1/3 is a measured capillary factor. Drop size was marginally affected by inertial forces at the highest flow rates. Dans des expériences sur la dispersion de phases organiques dans des phases aqueuses, des gouttelettes ont été produites en continu sur des fentes étroites de 12 μm ≤ w ≤ 125 μm montées en périphérie et en position normale par rapport au rayon dans un contacteur centrifuge “Hi‐Gee”. Les gouttelettes qui forment un groupe de sources attribuées à l'instabilité de Rayleigh‐Taylor se répartissent à une distance moyenne de λ ≈︁ 2π(2σ/Δρg)1/2 où σ est la tension interfaciale des phases, Δρ la différence de masse volumique et g l'accélération centrifuge appliquée. Les diamètres de gouttelettes moyens de Sauter mesurés se situent dans la gamme de 0,48 à 1,00 mm. La taille de gouttes moyenne, d, est donnée par d ≈︁ d̄*3(σ/Δρg)1/3 où d̄* = 0.1538 ± 0.0016 m1/3 est un facteur capillaire mesuré. La taille de gouttes n'est que marginalement influencée par les forces inertes aux débits les plus grands.
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The drops formed at an array of sources attributed to the Rayleigh‐Taylor instability distributed an average distance apart where σ is the interfacial tension of the phases, Δρ their density difference and g the applied centrifugal acceleration. Measured Sauter mean drop diameters were in the range 0.48 to 1.00 mm. The average drop size, d, was given by where d̄* = 0.1538 ± 0.0016 m1/3 is a measured capillary factor. Drop size was marginally affected by inertial forces at the highest flow rates. Dans des expériences sur la dispersion de phases organiques dans des phases aqueuses, des gouttelettes ont été produites en continu sur des fentes étroites de 12 μm ≤ w ≤ 125 μm montées en périphérie et en position normale par rapport au rayon dans un contacteur centrifuge “Hi‐Gee”. Les gouttelettes qui forment un groupe de sources attribuées à l'instabilité de Rayleigh‐Taylor se répartissent à une distance moyenne de λ ≈︁ 2π(2σ/Δρg)1/2 où σ est la tension interfaciale des phases, Δρ la différence de masse volumique et g l'accélération centrifuge appliquée. Les diamètres de gouttelettes moyens de Sauter mesurés se situent dans la gamme de 0,48 à 1,00 mm. La taille de gouttes moyenne, d, est donnée par d ≈︁ d̄*3(σ/Δρg)1/3 où d̄* = 0.1538 ± 0.0016 m1/3 est un facteur capillaire mesuré. 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J. Chem. Eng</addtitle><description>In experiments on the dispersion of organic phases into aqueous phases, drops were generated continuously at narrow slots of width 12 μm ≤ w ≤ 125 μm mounted peripherally and normal to the radius in a ‘Hi‐Gee’ centrifugal contactor. The drops formed at an array of sources attributed to the Rayleigh‐Taylor instability distributed an average distance apart where σ is the interfacial tension of the phases, Δρ their density difference and g the applied centrifugal acceleration. Measured Sauter mean drop diameters were in the range 0.48 to 1.00 mm. The average drop size, d, was given by where d̄* = 0.1538 ± 0.0016 m1/3 is a measured capillary factor. Drop size was marginally affected by inertial forces at the highest flow rates. 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J. Chem. Eng</addtitle><date>2000-10</date><risdate>2000</risdate><volume>78</volume><issue>5</issue><spage>876</spage><epage>883</epage><pages>876-883</pages><issn>0008-4034</issn><eissn>1939-019X</eissn><coden>CJCEA7</coden><abstract>In experiments on the dispersion of organic phases into aqueous phases, drops were generated continuously at narrow slots of width 12 μm ≤ w ≤ 125 μm mounted peripherally and normal to the radius in a ‘Hi‐Gee’ centrifugal contactor. The drops formed at an array of sources attributed to the Rayleigh‐Taylor instability distributed an average distance apart where σ is the interfacial tension of the phases, Δρ their density difference and g the applied centrifugal acceleration. Measured Sauter mean drop diameters were in the range 0.48 to 1.00 mm. The average drop size, d, was given by where d̄* = 0.1538 ± 0.0016 m1/3 is a measured capillary factor. Drop size was marginally affected by inertial forces at the highest flow rates. 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subjects Applied sciences
capillary drop formation
centrifugal liquid-liquid contacting
Chemical engineering
Drops and bubbles
Exact sciences and technology
Fluid dynamics
Fundamental areas of phenomenology (including applications)
Hydrodynamics of contact apparatus
Nonhomogeneous flows
Physics
Rayleigh-Taylor sources
slot-nozzles
title Formation of drops at narrow slots in a centrifugal liquid-liquid contactor
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