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	<title>Rayleigh number &#8211; Science</title>
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	<title>Rayleigh number &#8211; Science</title>
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		<title>Tilted isotherms, not Rayleigh number, drive hidden convection in drying droplets</title>
		<link>https://scienmag.com/tilted-isotherms-not-rayleigh-number-drive-hidden-convection-in-drying-droplets/</link>
		
		<dc:creator><![CDATA[Denise Maddox]]></dc:creator>
		<pubDate>Sun, 25 Oct 2026 06:22:05 +0000</pubDate>
				<category><![CDATA[Technology and Engineering]]></category>
		<category><![CDATA[buoyancy]]></category>
		<category><![CDATA[buoyancy-driven flow in evaporating sessile droplets]]></category>
		<category><![CDATA[curved isothermal contours and droplet stability]]></category>
		<category><![CDATA[destabilization of fluid flow in curved geometries]]></category>
		<category><![CDATA[drying patterns]]></category>
		<category><![CDATA[evaporating droplet convection]]></category>
		<category><![CDATA[evaporation]]></category>
		<category><![CDATA[fluid dynamics]]></category>
		<category><![CDATA[geometry-induced fluid instability in small droplets]]></category>
		<category><![CDATA[hidden natural convection in drying droplets]]></category>
		<category><![CDATA[impact of droplet shape on internal fluid flow]]></category>
		<category><![CDATA[isothermal contours]]></category>
		<category><![CDATA[limitations of Rayleigh number for microscale fluids]]></category>
		<category><![CDATA[Marangoni flow]]></category>
		<category><![CDATA[microfluidics]]></category>
		<category><![CDATA[microscale heat and mass transfer in drying droplets]]></category>
		<category><![CDATA[natural convection]]></category>
		<category><![CDATA[plasma droplet]]></category>
		<category><![CDATA[Rayleigh number]]></category>
		<category><![CDATA[role of droplet tilt in convection onset]]></category>
		<category><![CDATA[sessile droplet]]></category>
		<category><![CDATA[thermal engineering]]></category>
		<category><![CDATA[tilted isotherms in microfluidics]]></category>
		<guid isPermaLink="false">https://scienmag.com/?p=339307</guid>

					<description><![CDATA[New simulations and theory show that natural convection in small evaporating droplets is triggered by the inclination angle of internal isotherms rather than by the classical critical Rayleigh number.]]></description>
										<content:encoded><![CDATA[<p>A tiny evaporating droplet sitting on a glass slide should, according to a century-old rule of thumb, remain perfectly still inside. The temperature difference across it is far too small, and the droplet far too shallow, to push its Rayleigh number anywhere near the classical threshold that separates a quiescent fluid from one stirred by buoyancy. Yet a new combined numerical and theoretical study reports that such droplets do circulate, with internal speeds of a few micrometers per second, and that the familiar criterion used to predict the onset of this natural convection simply does not apply at these scales. The culprit, the researchers find, is geometry: the curved, tilted isothermal contours that inevitably form inside a small evaporating droplet destabilize the fluid in a way that the classical Rayleigh criterion, built for flat horizontal layers, cannot capture.</p>
<p>Natural convection is the buoyancy-driven flow that arises when a fluid&#8217;s density varies with temperature in a gravitational field. It governs heat and mass transport in systems ranging from thermal energy storage units to microfluidic chips. At the microscale, where evaporating sessile droplets serve as a canonical fluidic unit, weak buoyancy-induced flows can dominate transport behavior and determine drying quality and solute distribution. Understanding exactly when and why such convection starts is therefore central to controlling microscale heat and mass transfer, from printing and coating to the drying patterns left behind by biological fluids.</p>
<p>Internal flows in an evaporating aqueous droplet on a smooth horizontal substrate have long been attributed to two mechanisms. Because evaporation is strongest near the droplet&#8217;s pinned edge, an outward capillary flow replenishes the water lost there and preserves the sessile configuration. Meanwhile, the non-uniform evaporation flux cools the surface unevenly, creating surface tension gradients that drive Marangoni flow along the air-droplet interface. The same surface cooling also establishes a temperature gradient through the bulk liquid, which in principle should trigger a third flow: natural convection. Experiments have indeed revealed such convection in plasma droplets, but not in pure water droplets. The distinction arises because adsorbed plasma proteins at the air-droplet interface remove the inhibitory effect that Marangoni flow otherwise exerts on buoyancy-driven motion. All droplets discussed in the new work are therefore plasma droplets, and the authors note that natural convection in an evaporating sessile droplet had not been reported before their earlier publications.</p>
<p>The puzzle is quantitative. Lord Rayleigh argued in 1916 that a liquid can retain stable equilibrium even when denser fluid overlays lighter fluid, provided its viscosity is high enough; a critical temperature difference is needed to overcome viscous drag. In 1926, Jeffries derived critical Rayleigh numbers for fluid layers between two infinite parallel surfaces: 1708 for two rigid, no-slip boundaries and 670 for a rigid lower boundary with a free upper surface. For a water layer with a characteristic length of one millimeter, these thresholds correspond to critical temperature differences of about 11 degrees Celsius and 4.3 degrees Celsius, respectively. A sessile droplet differs fundamentally from both configurations, since its free air-liquid surface is curved rather than horizontal. In the new simulations of an evaporating droplet with a volume of roughly 5 microliters, a contact angle of 36 degrees and a contact radius of 2 millimeters, the largest temperature difference between the substrate and the air-droplet interface is only about 0.38 to 0.46 degrees Celsius, giving a Rayleigh number below 1, orders of magnitude beneath any classical threshold.</p>
<p>Despite this, the simulations show active circulation. For a plasma droplet of 5.5 microliters with a 36-degree contact angle evaporating on a glass slide, the maximum temperature of 295 kelvin occurs near the droplet edge and the minimum of 294.62 kelvin near the apex, and the resulting flow reaches a maximum velocity of 7.25 micrometers per second. When the contact angle is reduced to 20 degrees, shrinking the volume to 2.2 microliters and cutting the characteristic length by roughly a factor that pushes the Rayleigh number essentially to zero, convection persists at 1.35 micrometers per second. These results are consistent with the team&#8217;s earlier experimental observations, which recorded natural convection throughout the whole evaporation period of plasma droplets. On that basis, the authors conclude that a critical Rayleigh number is not a feasible criterion for the onset of natural convection in droplet evaporation.</p>
<p>To isolate the effect, the researchers also simulated a cylindrical enclosure, 2 millimeters by 1 millimeter, sized to the droplet&#8217;s characteristic length. With its upper and lower walls held at the droplet&#8217;s minimum and maximum temperatures, 294.62 kelvin and 295 kelvin, and its side walls adiabatic, the enclosure developed flat, horizontal isothermal contours, and the liquid between the walls remained quiescent, exactly as Jeffries&#8217;s analysis predicts for this configuration, whose critical temperature difference is 11 degrees Celsius. But when the two side walls were instead held at the constant temperature of 294.62 kelvin, the isothermal contours became non-horizontal, and active convection appeared, with a maximum flow velocity of 11.3 micrometers per second. Crucially, both cylinder configurations share the same Rayleigh number as conventionally defined, yet exhibit opposite flow states. The droplet, with its inherently non-horizontal isotherms, behaves like the second case. The authors therefore propose that the critical Rayleigh number criterion is fundamentally inapplicable to systems featuring non-horizontal isothermal contours.</p>
<p>The finding echoes classical theory that has largely been overlooked in droplet studies. Goldstein&#8217;s theoretical analysis showed that the stability of fluid systems with non-horizontal isothermal contours depends primarily on the curvature of the density stratification rather than on fluid viscosity, and he termed the resulting weak, conduction-dominated flows oscillatory motions. Sparrow and colleagues similarly demonstrated that the stability of a quiescent steady state is strongly modulated by the geometric morphology of the temperature distribution, with non-horizontal isotherms amplifying perturbations that fluid motion then acts to mitigate. Physically, a tilted isotherm decomposes gravity into a vertical component, along which the usual Rayleigh analysis still applies, and a horizontal component that renders the system non-equipotential. The fluid moves to restore horizontal, equal-density contours and minimize gravitational potential energy, regardless of the global Rayleigh number. The direction of circulation follows the sign of the cosecant of the isotherm inclination angle: counterclockwise when that quantity is positive, clockwise when it is negative.</p>
<p>The team also derived a quantitative scaling law. Under the Boussinesq approximation, the tilted isotherm generates an effective horizontal buoyancy component proportional to the product of density, gravity, the thermal expansion coefficient, the temperature difference and the sine of the inclination angle. Balancing this driving force against viscous dissipation in a steady boundary-layer-type flow yields a characteristic convection velocity that scales with the sine of the angle. Numerical simulations of a rotated two-dimensional rectangular enclosure, swept through inclination angles from 0.1 to 90 degrees, confirmed the prediction: a zero-intercept linear regression gave a maximum velocity of 131.27 times the sine of the angle in micrometers per second, with a coefficient of determination of 0.9989 and a root-mean-square residual of 2.42 micrometers per second. Strikingly, even the smallest tested tilt of 0.1 degree immediately drove the system into an unsteady flow state, and within the explored parameter space the researchers identified no distinct critical angle at which convection switches on.</p>
<p>The velocities involved are tiny, on the order of micrometers per second, and their consequences are scale-dependent. In large systems such as the atmosphere, such motion is negligible, but in millimeter- and sub-millimeter-scale systems, including sessile droplets, microfluidic devices and thin-film processes, it can contribute considerably to heat and mass transfer and to the drying patterns and deposit morphologies that engineers seek to control. The authors situate the work relative to earlier studies of drying colloidal droplets with small initial contact angles, in which natural convection&#8217;s influence on solute distribution and deposit morphology was found to be negligible and capillary-flow-driven horizontal motion dominated. The new mechanism matters instead for droplets with larger contact angles or conditions favoring turbulent-like fluctuations, where surface skin or crust layers introduce interfacial constraints that can favor buoyancy-driven flow.</p>
<p>The study carries clear limitations that the authors state explicitly. All simulations use a quasi-steady framework, justified because thermal diffusion within the droplet adjusts in roughly half a second while evaporation takes minutes to hours. The free surface is idealized as a rigid boundary to exclude surface tension and Marangoni interference, which isolates the convection induced purely by non-horizontal isotherms but neglects real-time interface deformation. The predicted velocities are so weak that they are sensitive to numerical discretization and convergence, even after mesh-independence checks showing relative deviations below 1 percent. Direct experimental validation of the angle-dependent convection mechanism is currently lacking, and because the simulations assume plasma droplet conditions in which interfacial protein adsorption eliminates Marangoni suppression, the conclusions cannot be directly extended to pure water droplets. Within those boundaries, the work redefines the stability paradigm for confined thermal flows, shifting attention from a single scalar threshold to a vector analysis of temperature contours, and offers a fundamental explanation for long-observed but poorly understood convective motions inside small-scale systems such as sessile droplets.</p>
<p><strong>Subject of Research:</strong> Natural convection driven by non-horizontal isothermal contours in evaporating sessile droplets</p>
<p><strong>Article Title:</strong> Natural convection driven by the non-horizontal isothermal contours in an aqueous sessile droplet</p>
<p><strong>Article References:</strong> Du, F., Zhang, X., Yang, G., &amp; Li, H. (2026). Natural convection driven by the non-horizontal isothermal contours in an aqueous sessile droplet. <em>Results in Engineering, 32</em>, Article 113658. <a href="https://doi.org/10.1016/j.rineng.2026.113658" rel="noopener noreferrer">https://doi.org/10.1016/j.rineng.2026.113658</a></p>
<p><strong>Image Credits:</strong> AI Generated</p>
<p><strong>DOI:</strong> <a href="https://doi.org/10.1016/j.rineng.2026.113658" rel="noopener noreferrer">10.1016/j.rineng.2026.113658</a></p>
<p><strong>Keywords:</strong> natural convection, sessile droplet, evaporation, Rayleigh number, isothermal contours, microfluidics, buoyancy, Marangoni flow, plasma droplet, drying patterns, fluid dynamics, thermal engineering</p>
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		<post-id xmlns="com-wordpress:feed-additions:1">339307</post-id>	</item>
		<item>
		<title>Hypergravity Supercharges Heat-Storing Materials, but Fin Design Holds the Key</title>
		<link>https://scienmag.com/hypergravity-supercharges-heat-storing-materials-but-fin-design-holds-the-key/</link>
		
		<dc:creator><![CDATA[Grant Pearson]]></dc:creator>
		<pubDate>Mon, 05 Oct 2026 21:38:22 +0000</pubDate>
				<category><![CDATA[Space]]></category>
		<category><![CDATA[advanced thermal engineering for extreme acceleration environments]]></category>
		<category><![CDATA[aerospace]]></category>
		<category><![CDATA[buoyancy-driven convection]]></category>
		<category><![CDATA[CFD simulation]]></category>
		<category><![CDATA[design considerations for heat storage systems in maneuvering spacecraft]]></category>
		<category><![CDATA[effects of hyper]]></category>
		<category><![CDATA[energy storage density]]></category>
		<category><![CDATA[fin configuration optimization in heat transfer systems]]></category>
		<category><![CDATA[fins]]></category>
		<category><![CDATA[heat exchanger design for hypergravity conditions]]></category>
		<category><![CDATA[heat transfer]]></category>
		<category><![CDATA[heat-storing materials under high gravity]]></category>
		<category><![CDATA[hypergravity]]></category>
		<category><![CDATA[hypergravity effects on phase change materials]]></category>
		<category><![CDATA[impact of hypergravity on melting behavior of phase change materials]]></category>
		<category><![CDATA[influence of hypergravity on thermal buffering materials]]></category>
		<category><![CDATA[latent heat thermal energy storage]]></category>
		<category><![CDATA[melting time]]></category>
		<category><![CDATA[numerical simulation of heat transfer under hypergravity]]></category>
		<category><![CDATA[phase-change material]]></category>
		<category><![CDATA[Rayleigh number]]></category>
		<category><![CDATA[thermal energy storage in extreme environments]]></category>
		<category><![CDATA[thermal management]]></category>
		<category><![CDATA[thermal management in aerospace and high-performance aircraft]]></category>
		<guid isPermaLink="false">https://scienmag.com/?p=239328</guid>

					<description><![CDATA[New simulations show that hypergravity accelerates phase change material melting by nearly half, but only when fins are placed to enhance, rather than block, buoyancy-driven convection.]]></description>
										<content:encoded><![CDATA[<p>Phase change materials have long been the quiet workhorses of thermal engineering, absorbing enormous quantities of heat as they melt and releasing it again as they solidify. From spacecraft avionics bays to battery packs in high-performance aircraft, these substances promise compact thermal buffering without moving parts. Yet a fundamental question has lingered: what happens to their carefully tuned melting behavior when the system experiences not the gentle pull of Earth&#8217;s gravity but the crushing acceleration of a maneuvering jet or a spinning mechanism? A new numerical study from researchers at the National Institute of Technology Raipur in India, published in the International Journal of Aeronautical and Space Sciences, provides one of the most detailed answers yet, and the findings upend some intuitive assumptions about how to design heat exchangers for extreme environments.</p>
<p>The research team, led by Dixit Arya together with Nisha Netam and Anuj Kumar Shukla, simulated the melting of a phase change material inside a closed rectangular enclosure fitted with conducting fins, comparing configurations with one, two, and three fins while holding the total fin area constant. Crucially, they ran the simulations not only at normal Earth gravity but also at five and ten times standard gravitational acceleration, conditions representative of aerial flight maneuvers and rotating machinery. The central insight is deceptively simple but consequential: gravity does not merely press down on the material, it fundamentally rewrites the physics of melting, and the fin geometry that works best at one gravity may underperform at another.</p>
<p>To understand why, one must appreciate the role of buoyancy-driven convection in latent heat thermal energy storage. When a phase change material melts next to a heated wall, the liquid layer that forms does not sit still. Warmer liquid is less dense, so it rises, while cooler liquid descends, creating circulating currents that ferry heat away from the melting front far more efficiently than conduction alone. The strength of this convective stirring is captured by the Rayleigh number, a dimensionless quantity that scales directly with gravitational acceleration. Multiply gravity by five or ten, and the Rayleigh number climbs accordingly, intensifying the internal flow and accelerating the melt. The simulations quantified this effect dramatically: maximum velocity magnitudes within the liquid increased by a factor of three to five under hypergravity compared with the baseline case.</p>
<p>The headline result concerns melting time. Under five times normal gravity, the finned configurations melted the material up to 47.8 percent faster than an unfinned enclosure, and at ten times gravity the improvement reached 48.2 percent. In practical terms, a thermal storage unit that would take minutes to fully charge at Earth gravity could accomplish the same task in roughly half the time during aggressive flight maneuvers. For aerospace engineers, this is more than a curiosity. Thermal management systems on high-speed aircraft and spacecraft must absorb transient heat loads quickly, and a storage medium that charges faster under acceleration effectively buys safety margin precisely when thermal stress is greatest.</p>
<p>Yet the study&#8217;s most provocative finding concerns fin placement and number, and here the conventional wisdom takes a beating. Engineers often assume that more fins mean better heat transfer, since each fin extends the heated surface into the material. The simulations tell a subtler story. A single, longer fin positioned in the lower region of the enclosure delivered the best performance among all cases examined. The reason lies in fluid dynamics: the lower fin sits where buoyant plumes originate, and its length allows it to channel warm liquid upward along its surface, feeding and reinforcing the convective circulation. Multiple shorter fins, by contrast, fragment the liquid domain into smaller cells, and fins placed in the upper region can act as barriers that suppress the very fluid motion that hypergravity amplifies. In effect, poorly placed fins strangle the convection that gravity is trying to supercharge.</p>
<p>This trade-off between conduction enhancement and convection suppression is the intellectual heart of the paper. Fins excel at conducting heat into solid regions that convection cannot reach, but every fin is also an obstacle in the flow path. Under hypergravity, where convective currents are the dominant heat-transfer mechanism, the penalty for obstructing flow grows correspondingly. The researchers&#8217; comparative analysis of single-, double-, and triple-fin arrangements demonstrates that the optimal design is not the one with the most metal but the one that cooperates with the buoyant flow field. A long lower fin guides the flow; a cluster of short upper fins fights it.</p>
<p>The energy accounting reveals further nuances that any system designer must confront. Because fins displace a small volume of phase change material, the total energy stored in the finned enclosures decreased slightly, by between 0.38 and 1.32 percent, relative to the unfinned case. That loss is modest, but the gains in charging speed are not: the mean power delivered during melting increased by up to 90.8 percent in the best configurations. In other words, fins transform the storage unit from a slow, capacious reservoir into a fast, responsive one. However, the study also reports a reduction in energy storage density of roughly 7.5 percent, a metric that matters where every kilogram and every liter counts, as it always does in aerospace applications. The trade-off between storage capacity and heat-transfer performance is therefore not eliminated by hypergravity but reshaped by it.</p>
<p>These results arrive amid a growing body of research on phase change behavior across the gravity spectrum. Previous experimental work has documented accelerated melting under hypergravity in pin-fin heat sinks for airborne electronics, while other studies have explored the opposite extreme, where microgravity nearly eliminates buoyant convection and melting stalls into a slow, conduction-dominated process. Numerical investigations have examined metal foam composites, topologically optimized fins, and even magnetic field coupling under variable gravity. The new study contributes a systematic comparison of fin number and placement at constant total fin area, a controlled variable that isolates the geometric question from the material question. Its findings complement earlier work showing that fin length arrangements and enclosure inclination strongly influence melting at normal gravity, and extend that framework into a regime where the Rayleigh number is an order of magnitude larger.</p>
<p>The practical implications reach beyond aircraft. Rotating systems, from centrifugal thermal storage units to machinery on space stations with artificial gravity, all impose effective accelerations on their thermal storage media. Battery thermal management, a pressing concern for electric aviation, has already seen proposals combining phase change materials with fin structures under variable gravity environments. The new results suggest that such systems should be designed with the gravity vector in mind: orienting fins to nurture, rather than obstruct, buoyant circulation could yield charging-rate improvements approaching a factor of two, while naive fin layouts might deliver far less than expected. The finding that a single well-placed fin outperforms multiple shorter ones could also simplify manufacturing and reduce mass, a rare case where the better design is also the lighter one.</p>
<p>As with any numerical study, the results rest on modeling assumptions, and the authors note that the data underlying their findings are available upon reasonable request. Experimental validation under sustained hypergravity, which requires centrifuge facilities or parabolic flight campaigns, remains the necessary next step before these design rules enter flight hardware. Still, the study offers a clear and actionable principle for engineers racing to manage ever-growing heat loads in fast-moving machines: in the world of latent heat storage, gravity is not an obstacle to be engineered around but a fluid-dynamic resource to be harnessed, and the humble fin, placed with an eye on the flow, is the lever that unlocks it.</p>
<p><strong>Subject of Research:</strong> Fin-enhanced melting of phase change materials for latent heat thermal energy storage under hypergravity conditions</p>
<p><strong>Article Title:</strong> Impact of Multiple Fins on the Melting Characteristics of PCM in a Closed Enclosure Under Hypergravity Conditions</p>
<p><strong>Article References:</strong> Arya, D., Netam, N., &amp; Shukla, A. K. (2026). Impact of Multiple Fins on the Melting Characteristics of PCM in a Closed Enclosure Under Hypergravity Conditions. <em>International Journal of Aeronautical and Space Sciences</em>. <a href="https://doi.org/10.1007/s42405-026-01240-5" rel="noopener noreferrer">https://doi.org/10.1007/s42405-026-01240-5</a></p>
<p><strong>Image Credits:</strong> AI Generated</p>
<p><strong>DOI:</strong> <a href="https://doi.org/10.1007/s42405-026-01240-5" rel="noopener noreferrer">10.1007/s42405-026-01240-5</a></p>
<p><strong>Keywords:</strong> phase change material, hypergravity, latent heat thermal energy storage, fins, buoyancy-driven convection, Rayleigh number, thermal management, aerospace, melting time, energy storage density, CFD simulation, heat transfer</p>
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