1997
DOI: 10.1016/s0017-9310(96)00361-4
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The effects of chaotic advection on heat transfer

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Cited by 119 publications
(62 citation statements)
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“…While a specific value of Sh ∞ stat cannot be defined in these cases due to the continuing decrease of Sh(Z), it is instructive to note that Sh(Z) is similar in magnitude for the chaotic and non-chaotic flows. As noted by others (Acharya et al 2001, Ghosh et al 1998, Kirtland et al 2006, Mokrani et al 1997, Peerhossaini et al 1993, from a globally averaged Sherwood number or from a total integrated flux over the entire reactive interface, it is very difficult to distinguish the transport process in figure 6(a) from that in figure 6(b). The non-chaotic flow fails to exhibit modified Graetz behaviour for Pe > 10 5 , but this failure is subtle in the sense that in many cases it would not even be measurable from an external, global measurement.…”
Section: Transport To Stationary Reactive Interfacesmentioning
confidence: 98%
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“…While a specific value of Sh ∞ stat cannot be defined in these cases due to the continuing decrease of Sh(Z), it is instructive to note that Sh(Z) is similar in magnitude for the chaotic and non-chaotic flows. As noted by others (Acharya et al 2001, Ghosh et al 1998, Kirtland et al 2006, Mokrani et al 1997, Peerhossaini et al 1993, from a globally averaged Sherwood number or from a total integrated flux over the entire reactive interface, it is very difficult to distinguish the transport process in figure 6(a) from that in figure 6(b). The non-chaotic flow fails to exhibit modified Graetz behaviour for Pe > 10 5 , but this failure is subtle in the sense that in many cases it would not even be measurable from an external, global measurement.…”
Section: Transport To Stationary Reactive Interfacesmentioning
confidence: 98%
“…Heat and mass transfer to solid-liquid interfaces and across liquid-liquid interfaces are fundamental to heat exchanger design (Acharya et al 1992, 2001, Mokrani et al 1997, Peerhossaini et al 1993, electrochemical systems for analysis and energy production (Cohen et al 2005, Ferrigno et al 2002, Shrivastava et al 2008, separations with membranes (Shrivastava et al 2008) and without membranes (Aref andJones 1989, Brody andYager 1997), fabrication at fluid-fluid interfaces (Kenis et al 1999, and sensors involving interfacial reactions (Foley et al 2008, Golden et al 2007, Kamholz et al 1999, Squires et al 2008, Teles and Fonseca 2008, Vijayendran et al 2003. Many of these systems rely on the suppression of turbulence as a means of controlling fluid flow, whereas others are relegated to laminar flow by other constraints.…”
Section: Introductionmentioning
confidence: 99%
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“…Even if the flow in these pipes is steady, the chaotic character is obtained by elbows succession, where at sufficiently high Dean numbers, secondary vortices appear and promote chaotic advection [8,9]. This type of mixer is efficient at intermediate Reynolds numbers, roughly for 40 < Re < 2000, and is thus not suitable for highly viscous fluids such as the one addressed in the present study.…”
Section: Introductionmentioning
confidence: 84%