Arnold J. T. M. Mathijssen’s research while affiliated with University of Pennsylvania and other places

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Publications (52)


Dynamics of a pour-over coffee. (a) Image of a pour-over coffee. (b) Parameters associated with a pour-over coffee, including the bed height, h, and water height, H, as well as the pour-over jet height, D, the jet radius, R, and the flow velocity, v. We keep h and H constant throughout the experiments. (c) Erosion of the coffee bed at the bottom of the cone caused by the impinging jet. (d) Image of experimental system with laser sheet and high-speed camera. The solid line circle is the glass funnel used as the coffee cone in this experiment. Circled in the dotted line is the high-speed camera equipped with a macro lens. Circled in the dashed line is the laser sheet pointing orthogonally toward the funnel and high-speed camera.
Mixing at the top of the coffee cone vs pour height. Keeping the water jet pour rate constant, the intensity of the water layer above the silica gel is measured over various pour heights. (a) An image of the cone while a water jet impinges from above. The red box shows the analysis area above the granular bed. (b) An intensity histogram in the area encircled in (a). Lower intensities are cut out to exclude empty black areas. This is plotted for each frame, leading to (c) a plot of the mean intensity, normalized to the intensity histogram at t = 0, over time. The normalized mean intensity is redefined in this plot as the degree of mixing. (d) A plot of the maximum value of the degree of mixing, redefined as the mixing index, for different pour heights. Multimedia available online. 10.1063/5.0257924.1
Silica with floating polystyrene layer intensity vs height. (a) Image of a pour-over featuring many floating granules. Image by Matthew Henry, licensed under Burst Some Rights Reserved. (b) A floating polystyrene monolayer cast on top of the silica gel before the pour-over. (c) A plot of the mixing index vs pour height. Multimedia available online. 10.1063/5.0257924.2
Erosion of granules at the bottom of the cone vs pour height. (a) The bottom of the cone, in the red square, is analyzed to determine how many granules there are dug out. (b) The histogram for the intensities in the enclosed area in (a) is plotted. (c) The normalized mean intensity redefined simply to density is monitored over time. (d) The minimum of the density, redefined as the density index, is plotted over different pour heights, for both the plain silica gel experiment and the silica gel with a polystyrene monolayer experiment.
Smaller jet diameter impact on dynamics. (a) Image of jet with halved diameter impacting bed at 2.5 cm above the bed. (b) Jet impacting bed at 22.5 cm above the bed. (c) Jet with lower flow velocity impacting bed at 2.5 cm above the bed. Multimedia available online. 10.1063/5.0257924.3 10.1063/5.0257924.4 10.1063/5.0257924.5

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Pour-over coffee: Mixing by a water jet impinging on a granular bed with avalanche dynamics
  • Article
  • Publisher preview available

April 2025

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534 Reads

Ernest Park

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Margot Young

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Arnold J. T. M. Mathijssen

Coffee is one of the most consumed beverages in the world. However, issues such as climate change threaten the growth of the temperature-sensitive Coffea arabica plant, more commonly known as Arabica coffee. Therefore, it is crucial to make beverages more efficient by using less coffee while still meeting the high demand for the beverage. Here, we explore pour-over filter coffees, in which a water jet impinges on a water layer above a granular bed. To reveal its internal dynamics, we first substitute opaque coffee grounds with silica gel particles in a glass cone, imaged with a laser sheet and a high-speed camera. We discover an avalanche effect that leads to strong mixing at various pour heights, even with a gentle pour-over jet. We also find that this mixing is not significantly impacted by a layer of floating grains, which is often present in pour-overs. Next, we perform experiments with real coffee grounds to measure the extraction yield of total dissolved solids. Together, these results indicate that the extraction of the coffee can be tuned by prolonging the mixing time with slower but more effective pours using avalanche dynamics. This suggests that instead of increasing the amount of beans, the sensory profile and the strength of the beverage can be adjusted by varying the flow rate and the pour height. In this way, the extraction efficiency could be better controlled to help alleviate the demand on coffee beans worldwide.

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FIG. 1. (a) Schematic of a confined active carpet (yellow) between two fluid interfaces: the air-water interface at the top and a fluidfluid interface at the bottom. The active carpet is composed of microswimmers located at a fixed distance σ above the bottom fluid-fluid interface (green). These microswimmers generate hydrodynamic fluctuations (orange arrows) which stir the fluid and suspended particles within the confined layer. (b) Conceptual model for a single microswimmer confined between the free surface (top) and the fluid-fluid interface (bottom). The microorganism swims in the x-y plane at z = σ (green), creating two image swimmers (yellow) positioned at rs FS and rs FF , respectively. Inset: The flow field generated in the x-z plane by a single puller-type microswimmer in a film of thickness H = 3, with κ = −30 and a viscosity ratio of λ = 1.5, computed from Eq. (9). Streamlines (black arrows) illustrate typical fluid parcel trajectories around the swimmer, and contours represent the velocity field's intensity, with higher intensity near the singularity (white) and lower intensity further away (purple).
FIG. 2. Anisotropic hydrodynamic fluctuation driven by active carpets. (a) Variance of the flow field driven by an active carpet in the horizontal and vertical directions (green and red solid lines), as defined in Eq. (11). Markers are simulation points obtained from Eq. (14). The star marks the intersection between theoretical variances v 2 z (z ) = =v 2 xy (z ). Regions I, II, and III indicate the dominance of fluctuations according to the distance from the active carpet. Here H = 40 and λ = 1.5. Inset: Theoretical variances for H = 20, and three different values of λ, λ = 0.1, 0.5, 1.5, denoted by dashed, dotted, and dash-dotted lines, respectively. Stars are cross-points. (b) Ellipsoids represent the average displacement of tracer particles computed from Eq. (15) for each fluctuation region. In green, tracer particles start at z 0 < z , while in red, they start at z 0 < z < H . In ginger, they start exactly at z 0 = z .
FIG. 3. The impact of confinement on the localization of z . Analytical solutions for the cross-point height z for a domain of the parameters λ and H . We described the domain showing the cases of thicker and thinner films and for more and less viscous films, where λ = μ 2 /μ 1 with μ 1 the fluid viscosity where the AC resides.
FIG. 5. Active carpets can drive large-scale recirculations. [(a)-(c)] Average vorticity exerted by an active carpet on fluid parcels across the confinement space, in the plane x-z, for puller microswimmers H = 20, λ = 1.5, κ = −30, and σ = 1. The color code for vortical flows is the following: clockwise rotations (blue) and counterclockwise rotations (red); the magnitude of the vorticity is indicated in the legends of each component. (d) The average vertical flow in the examined region. The orange and blue arrows show the direction of the mean flow. (e) Regions A, B, and C were used to evaluate the circulation Eq. (13) over the confinement space. Squares with side were utilized in each area to measure the circulation. (f) Circulation is associated with the vorticity in the y direction, divided by the area 2 .
Layered aquatic microenvironments control fluctuations generated by active carpets

February 2025

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89 Reads

Physical Review Research

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Gabriel Aguayo

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[...]

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In Earth's aquatic environments and the human body, microbial swimmers often accumulate at interfaces within layered systems, forming colonies known as . These bioactive layers enhance mass transport and diffusion in fluid media. Here we study the hydrodynamic behavior induced by within confined semi-infinite fluid layers, such as the one found in the sea surface microlayer. By deriving analytical expressions and performing numerical simulations, we explore how geometrical and viscous confinement (layer thickness and viscosity ratio) influence hydrodynamic fluctuations and passive tracer dynamics. Our findings reveal anisotropic distributions of fluctuations, characterized by three distinct regions: near the and fluid-fluid interface (Region I), vertical fluctuations dominate; in an intermediate region (Region II), fluctuations become isotropic; and near the free surface (Region III), horizontal fluctuations prevail. The results also demonstrate the emergence of coherent vortical structures in highly confined systems, with roll-like patterns governed by the thickness of the confined layer and the sharpness in viscosity transitions. The insights provided by this work have implications for understanding biogenic flow patterns and transport processes in natural and engineered environments, offering potential applications in areas such as microbial ecology, biofilm management, and microfluidic technologies. Published by the American Physical Society 2025


Enhancement of bacterial rheotaxis in non-Newtonian fluids

December 2024

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25 Reads

Proceedings of the National Academy of Sciences

Many microorganisms exhibit upstream swimming, which is important to many biological processes and can cause contamination of biomedical devices and the infection of organs. This process, called rheotaxis, has been studied extensively in Newtonian fluids. However, most microorganisms thrive in non-Newtonian fluids that contain suspended polymers such as mucus and biofilms. Here, we investigate the rheotactic behavior of Escherichia coli near walls in non-Newtonian fluids. Our experiments demonstrate that bacterial upstream swimming is enhanced by an order of magnitude in shear-thinning (ST) polymeric fluids relative to Newtonian fluids. This result is explained by direct numerical simulations, revealing a torque that promotes the alignment of bacteria against the flow. From this analysis, we develop a theoretical model that accurately describes experimental rheotactic data in both Newtonian and ST fluids.


Floating active carpets drive transport and aggregation in aquatic ecosystems

September 2024

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90 Reads

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1 Citation

Journal of Fluid Mechanics

Communities of swimming microorganisms often thrive near liquid-air interfaces. We study how such 'active carpets' shape their aquatic environment by driving biogenic transport in the water column beneath them. The hydrodynamic stirring that active carpets generate leads to diffusive upward fluxes of nutrients from deeper water layers, and downward fluxes of oxygen and carbon. Combining analytical theory and simulations, we examine the biogenic transport by studying fundamental metrics, including the single and pair diffusivity, the first passage time for particle pair encounters and the rate of particle aggregation. Our findings reveal that the hydrodynamic fluctuations driven by active carpets have a region of influence that reaches orders of magnitude further in distance than the size of the organisms. These non-equilibrium fluctuations lead to a strongly enhanced diffusion of particles, which is anisotropic and space dependent. Fluctuations also facilitate encounters of particle pairs, which we quantify by analysing their velocity pair correlation functions as a function of distance between the particles. We found that the size of the particles plays a crucial role in their encounter rates, with larger particles situated near the active carpet being more favourable for aggregation. Overall, this research broadens our comprehension of aquatic systems out of equilibrium and how biologically driven fluctuations contribute to the transport of fundamental elements in biogeochemical cycles.


Enhancement of bacterial rheotaxis in non-Newtonian fluids

August 2024

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61 Reads

Bacteria often exhibit upstream swimming, which can cause the contamination of biomedical devices and the infection of organs including the urethra or lungs. This process, called rheotaxis, has been studied extensively in Newtonian fluids. However, most microorganisms thrive in non-Newtonian fluids that contain suspended polymers such as mucus and biofilms. Here, we investigate the rheotatic behavior of E. coli near walls in non-Newtonian fluids. Our experiments demonstrate that bacterial upstream swimming is enhanced by an order of magnitude in shear-thinning polymeric fluids relative to Newtonian fluids. This result is explained by direct numerical simulations, revealing a torque that promotes the alignment of bacteria against the flow. From this analysis, we develop a theoretical model that accurately describes experimental rheotatic data in both Newtonian and shear-thinning fluids.


Giant enhancement of bacterial upstream swimming in macromolecular flows

August 2024

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71 Reads

Many bacteria live in natural and clinical environments with abundant macromolecular polymers. Macromolecular fluids commonly display viscoelasticity and non-Newtonian rheological behavior; it is unclear how these complex-fluid properties affect bacterial transport in flows. Here we combine high-resolution microscopy and numerical simulations to study bacterial response to shear flows of various macromolecular fluids. In stark contrast to the case in Newtonian shear flows, we found that flagellated bacteria in macromolecular flows display a giant capacity of upstream swimming (a behavior resembling fish swimming against current) near solid surfaces: The cells can counteract flow washing at shear rates up to ~65 s1s^{-1}, one order of magnitude higher than the limit for cells swimming in Newtonian flows. The significant enhancement of upstream swimming depends on two characteristic complex-fluid properties, namely viscoelasticity and shear-thinning viscosity; meanwhile, increasing the viscosity with a Newtonian polymer can prevent upstream motion. By visualizing flagellar bundles and modeling bacterial swimming in complex fluids, we explain the phenomenon as primarily arising from the augmentation of a "weathervane effect" in macromolecular flows due to the presence of a viscoelastic lift force and a shear-thinning induced azimuthal torque promoting the alignment of bacteria against the flow direction. Our findings shed light on bacterial transport and surface colonization in macromolecular environments, and may inform the design of artificial helical microswimmers for biomedical applications in physiological conditions.


CFU counts from biofilm with SARS-CoV-2 Delta variant and biofilm without SARS-CoV-2 Delta variant samples on stainless steel, PVC, and tile chips
(A-I) CFU counts for biofilm with SARS-CoV-2 Delta variant and biofilm without SARS-CoV-2 Delta variant samples on stainless steel, PVC, and tile chips (A-C) from Plant A, (D-F) from Plant B, and (G-I) from Plant C. Each sample was plated in duplicate. Results in this figure are the mean values and standard deviations (error bars) from three independent experiments. Statistical significance was analyzed by unpaired t-test. *: p < 0.05; **: p < 0.01; ***: p < 0.001; ****: p < 0.0001.
RT-qPCR analysis of SARS-CoV-2 Delta variant mixed with biofilm organisms and pre-incubated for 5 days on stainless steel, PVC, and ceramic tile chips
(A-C) RT-qPCR analysis of SARS-CoV-2 Delta variant mixed with environmental biofilm organisms from Plant A on stainless steel, PVC and on ceramic tile chips, (D-F) RT-qPCR analysis of SARS-CoV-2 Delta variant mixed with environmental biofilm organisms from Plant B on stainless steel, PVC, and on ceramic tile chips, (G-I) RT-qPCR analysis of SARS-CoV-2 Delta variant mixed with environmental biofilm organisms from Plant C on stainless steel, PVC, and on ceramic tile chips. 1.0 x 10⁴ PFU of SARS-CoV-2 Delta variant were added to a stainless steel, PVC, or ceramic tile chip along with a floor drain biofilm sample collected from the cooler of meat packaging plant A, B, or C. The RT-qPCR samples were analyzed in duplicate. Gene copy numbers were calculated from a standard curve of known quantities of SARS-CoV-2 Delta variant RNA in a 25 μL qPCR reaction. Results in this figure are the mean values and standard deviations (error bars) from three independent experiments. Statistical significance was analyzed by unpaired t-test. ns: not significant; **: p < 0.01; ***: p < 0.001.
Plaque assay results from biofilm with SARS-CoV-2 Delta variant and SARS-CoV-2 Delta variant without biofilm samples on stainless steel, PVC, and ceramic tile chips
(A-I) Results from plaque assays on samples collected from (A-C) stainless steel, (D-F) PVC, and (G-I) ceramic tile chips. Each sample was filtered through a 0.45 μm filter and plated on Vero CCL-81 cells in duplicate. Results in this figure are the mean values and standard deviations (error bars) from three independent experiments. Statistical significance was analyzed by unpaired t-test. **: p < 0.01; ****: p < 0.0001.
Schematic representation of floor drain biofilm and virus experiment
(A and B): Experimental set up with Biofilm with SARS-CoV-2 Delta variant, Biofilm without SARS-CoV-2 Delta variant, SARS-CoV-2 Delta variant—Biofilm, and Negative Control in duplicate. The experimental set is incubated at 7°C for 5 days. (C). After 5 days, the biofilm was harvested from SS, PVC, or ceramic tile chips using a cell lifter and forceps and rinsed with 1000 μL of LB-NS. (D) Harvested cells were stored in a screw-cap tube at -80°C until needed.
Results from evaporation dynamics assays of water droplets inoculated on different substrates: stainless steel (red, circles), PVC (green, diamonds) and ceramic tile (blue, triangles) samples
(A) Weight fraction of liquid remaining on the substrates as a function of time (hours) after inoculation. The data points represent mean values over N = 6 replicates, and the error bars show the standard error (SE) over these replicates. The curves show exponential decay fits to these data points. (B) Half-life time of evaporation from the different materials, obtained from these exponential decay fits. This gives 88 ± 9 hours, 110 ± 16 hours, 127 ± 10 hours, respectively, where the error bars are quantified by the standard error (SE) of the data sets.
SARS-CoV-2 Delta variant remains viable in environmental biofilms found in meat packaging plants

June 2024

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34 Reads

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1 Citation

To determine why SARS-CoV-2 appears to thrive specifically well in meat packaging plants, we used SARS-CoV-2 Delta variant and meat packaging plant drain samples to develop mixed-species biofilms on materials commonly found within meat packaging plants (stainless steel (SS), PVC, and ceramic tile). Our data provides evidence that SARS-CoV-2 Delta variant remained viable on all the surfaces tested with and without an environmental biofilm after the virus was inoculated with the biofilm for 5 days at 7°C. We observed that SARS-CoV-2 Delta variant was able to remain infectious with each of the environmental biofilms by conducting plaque assay and qPCR experiments, however, we detected a significant reduction in viability post-exposure to Plant B biofilm on SS, PVC, and on ceramic tile chips, and to Plant C biofilm on SS and PVC chips. The numbers of viable SARS-CoV-2 Delta viral particles was 1.81–4.57-fold high than the viral inoculum incubated with the Plant B and Plant C environmental biofilm on SS, and PVC chips. We did not detect a significant difference in viability when SARS-CoV-2 Delta variant was incubated with the biofilm obtained from Plant A on any of the materials tested and SARS-CoV-2 Delta variant had higher plaque numbers when inoculated with Plant C biofilm on tile chips, with a 2.75-fold difference compared to SARS-CoV-2 Delta variant on tile chips by itself. In addition, we detected an increase in the biofilm biovolume in response to SARS-CoV-2 Delta variant which is also a concern for food safety due to the potential for foodborne pathogens to respond likewise when they come into contact with the virus. These results indicate a complex virus-environmental biofilm interaction which correlates to the different bacteria found in each biofilm. Our results also indicate that there is the potential for biofilms to protect SARS-CoV-2 from disinfecting agents and remaining prevalent in meat packaging plants.



Floating active carpets drive transport and aggregation in aquatic ecosystems

December 2023

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71 Reads

Communities of swimming microorganisms often thrive near liquid-air interfaces. We study how such 'active carpets' shape their aquatic environment by driving biogenic transport in the water column beneath the active carpet. The collective flows that these organisms generate lead to diffusive upward fluxes of nutrients from deeper water layers and downward fluxes of oxygen and carbon. Combining analytical theory and simulations, we examine the key transport metrics including the single and pair diffusivity, the first passage time for particle pair encounters, and the rate of particle aggregation. Our findings reveal that the hydrodynamic fluctuations driven by active carpets have a region of influence that reaches orders of magnitude further in distance than the size of the organisms. These non-equilibrium fluctuations lead to a strongly enhanced diffusion of particles, which is anisotropic and space-dependent. The fluctuations also facilitate encounters of particle pairs, which we quantify by analyzing their velocity pair correlation functions as a function of distance between the particles. We found that the size of the particles plays a crucial role in their encounter rates, with larger particles situated near the active carpet being more favourable for aggregation. Overall, this research has broadened our comprehension of aquatic systems out of equilibrium, particularly how biologically driven fluctuations contribute to the transport of fundamental elements in biogeochemical cycles.


Figure 1. (a) Schematic of droplet propulsion mechanism and a zoomed in region around the droplet interface showing surfactant monomers, empty micelles and oil-filled micelles. (b) Schematic of the dual-channel microscopy set-up simultaneously visualising flow fields (camera 1) using fluorescent tracers and filled micelle concentration (camera 2) using Nile red dye in the oil droplet. (c) Illustration of a small, spherical self-propelling droplet vs a larger droplet immobilised by squeezing it between the glass top and bottom of the cell. (d) Emission from fluorescent tracers (top) and Nile red (bottom). Scale bar: 50 μm.
Figure 2. Streak visualisation of flow fields generated by pumping active droplets for increasing droplet radius a, with superimposed streamlines from PIV analysis. We observe a shift of the vortex pair from the droplet posterior to the anterior in the top row, corresponding to a = 61 μm, a = 80 μm and a = 102 μm, and on further increase of a, a bistable regime between a dipolar (a = 185 μm) and a quadrupolar flow mode (a = 148 μm). For larger radii, we only see the quadrupolar mode (a = 243 μm). See also supplementary material and movies S1 and S2.
Figure 6. (a) Time evolution of streamlines around a pumping droplet at Pe = 241 and a = 201 μm. As time increases, the inactive region starting from the rear stagnation point grows around the interface due to saturation by filled micelles. This leads to droplet inactivity at long time. Scale bar: 100 μm. (b) Time evolution of filled micelle concentration around the droplet interface. Here, θ = 0 indicates the anterior stagnation point. (c) Time evolution of the tangential velocity around the droplet interface. The colour bar also applies to the interfacial speeds plotted in (a). See also supplementary material and movie S3.
Interfacial activity dynamics of confined active droplets

July 2023

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350 Reads

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10 Citations

Journal of Fluid Mechanics

Active emulsions can spontaneously form self-propelled droplets or phoretic micropumps. However, it remains unclear how these active systems interact with their self-generated chemical fields, which can lead to emergent chemodynamic phenomena and multistable interfacial flows. Here, we simultaneously measure the flow and chemical concentration fields using dual-channel fluorescence microscopy for active micropumps, i.e. immobilised oil droplets that dynamically solubilise in a supramicellar aqueous surfactant solution. With increasing droplet radius, we observe (i) a migration of vortices from the posterior to the anterior, analogous to a transition from pusher- to puller-type swimmers, (ii) a bistability between dipolar and quadrupolar flows and, eventually, (iii) a transition to multipolar modes. We also investigate the long-time dynamics. Together, our observations suggest that a local build-up of chemical products leads to a saturation of the surface, which controls the propulsion mechanism. These multistable dynamics can be explained by the competing time scales of slow micellar diffusion governing the chemical buildup and faster molecular diffusion powering the underlying transport mechanism. Our results are directly relevant to phoretic micropumps, but also shed light on the interfacial activity dynamics of self-propelled droplets and other active emulsion systems.


Citations (27)


... Biogenic hydrodynamic stirring has been shown to enhance active diffusion [43][44][45][46][47][48][49][50], generate persistent flows for feeding processes in both collective and single microswimmers [1,9,51], induce aggregation [14,[52][53][54][55][56], and trigger long-range hydrodynamic fluctuations in homogeneous fluid columns [57]. Recently, Aguayo et al. [53] studied the hydrodynamic fluctuations caused by active carpets formed by dipole microswimmers organized into a monolayer beneath the free surface of a semi-infinite homogeneous fluid. ...

Reference:

Layered aquatic microenvironments control fluctuations generated by active carpets
Floating active carpets drive transport and aggregation in aquatic ecosystems

Journal of Fluid Mechanics

... New variants are also concern for food safety. For instance, recently it was proved that biofilms could be a reservoir for SARS-CoV-2 Delta variant to spread it throughout meat packaging plants [Featherstone et al., 2024). Therefore, more attention needs to be given to increase the preparedness for pandemic scenarios by the food industry Dai et al., 2023) Zoonotic viruses may transmit through respiration, contact during the production, processing, storage, transportation, and retail of food products . ...

SARS-CoV-2 Delta variant remains viable in environmental biofilms found in meat packaging plants

... Over time, these droplets solubilise into surfactant micelles [29], a process that locally increases the interfacial tension between oil and aqueous phases. Due to an advection-diffusion instability in the surfactant dynamics [21,26,30], higher modes in the interfacial tension arise with increasing Péclet number Pe. Pe increases with viscosity [31], surfactant concentration [32] and droplet radius [33,34]. While small droplets at low surfactant concentration solubilise isotropically (interfacial mode n = 0) and remain inactive, they self-propel as very persistent Brownian (or almost ballistic) swimmers once Pe exceeds the instability threshold for the dipolar n = 1 mode [21]. ...

Interfacial activity dynamics of confined active droplets

Journal of Fluid Mechanics

... If the water is poured too slowly, the jet can stick to the spout due to adhesion and surface tension, which is known as the teapot effect. 2,39 It is also known that water jets experience a Plateau-Rayleigh instability, 36 which can increase the amount of air entrainment of the jet as it impinges the surface, and therefore decrease the jet's momentum as it impacts the grounds below. 40 However, it is not known how this may impact the amount of agitation the coffee grounds experience in the context of pour-over brews. ...

Culinary fluid mechanics and other currents in food science

Review of Modern Physics

... Finally, this type of "kitchen flow" research 2 may also help make science more accessible, affordable, and curiosity-driven. 57 The experiments presented in this paper could be adapted for a typical classroom setting to encourage students to think about how the physics of fluids impacts their daily lives through food and beverages. 58,59 SUPPLEMENTARY MATERIAL See the supplementary material for details on the particle size distributions of silica gel particles and coffee grounds used in the paper. ...

Kitchen flows: Making science more accessible, affordable, and curiosity driven

... A microrobot swarm is an effective tool for the active exploration and reconstruction of vascular structures. With remote actuation, they can perform precise locomotion in physiological environments, including unstructured surfaces and flows of biological fluids [12][13][14][15][16][17] , and pass tortuous environments inside living bodies [18][19][20][21] . Minimally invasive surgery such as targeted delivery [22][23][24] , thrombolysis 25,26 , hyperthermia therapy 27,28 and embolization [29][30][31] using microrobot swarms has been achieved. ...

Artificial microtubules for rapid and collective transport of magnetic microcargoes

Nature Machine Intelligence

... In addition, microswimmers can be guided along AMTs before swimming the last stretch independently. Our design can be implemented at different scales to match the cargo dimensions for different application scenarios, including drug delivery 14,15,18 , magnetic tweezers 34,35 , lab-on-a-chip applications 36,37 and reconstituted cytoplasmic streaming 38 . Besides transport, AMTs can offer a method for separating microparticles by size, because the particles must be large enough to bridge between the embedded stepping stones, which may be useful in confinement geometries where gravitational separation is difficult. ...

Engineering reconfigurable flow patterns via surface-driven light-controlled active matter
  • Citing Article
  • December 2021

Physical Review Fluids

... The technology of object transport has broad applications across various fields, including drug delivery [1,2], soft robotics [3][4][5], surface self-cleaning [6][7][8] and cargo sorting [9,10]. The ability to control the velocity and direction of transport is of significant importance in these applications. ...

Amphibious Transport of Fluids and Solids by Soft Magnetic Carpets

... Though the solubilization process starts above the critical micellar concentration (CMC), it has been found that self-propulsion of the droplet happens only above a threshold total concentration of the surfactant in the outer fluid which is much greater than CMC. The self-propulsion of droplets with the inner fluid in the isotropic [24,27,30,35,37,38], nematic [18,25,26,29,32] or cholesteric phases [28,39] has been reported. Several mathematical models aiming to explain the mechanism behind self-propulsion have also been proposed in the literature [25,30,[40][41][42][43]. ...

Collective Entrainment and Confinement Amplify Transport by Schooling Microswimmers
  • Citing Article
  • August 2021

Physical Review Letters

... Activity restructures the topological environment of the colloid from a neutral colloid-companion complex to a positively charged colloid-companion complex to a particle in a gas of activity-induced defects. Our results begin to extend this understanding to active nematics, where spontaneous flows and self-propelled defects have already been shown to rectified motion in chiral inclusions [37,47], enhance mixing properties of tracers above active carpets [48], and generate complex motion in emulsions [33]. The introduction of anchoring in active nematics, as explored here, reveals a novel mechanism by which the colloid-defect interactions are fundamentally altered, leading to enhanced colloidal diffusivity and defect-mediated propulsion arising from topological kicks. ...

Active carpets drive non-equilibrium diffusion and enhanced molecular fluxes