The aerodynamics of aerosols and their deposition on face masks play a critical role in determining the effectiveness of respiratory protection. While existing studies have focused on the risks associated with aerosol dispersion during exhalation, little attention has been paid to aerosol aerodynamics in an open environment, where aerosols can circumvent masks, during inhalation. This is because mask performance has primarily been evaluated by the particle filtration efficiency in closed pipe setups, which do not account for the aerodynamics of aerosols around the wearer's face. In this study, we conduct experiments in an open environment to investigate the aerosol flow around a face mask and the aerosol deposition under varying inhalation pressures. Our results indicate that an aerosol flow near a mask surface behaves like a viscous flow, stagnating within the range of human inhalation. Within this range, we find that the amount of aerosol deposited can be predicted by modifying existing aerodynamics theory. Using a theoretical model, a critical inhalation pressure is identified at which water aerosols begin to penetrate through a mask. Finally, we propose the aerosol circumvention efficiency as a new metric to assess mask performance in open environments by taking into account the effects of aerosol circumvention.

Respiratory droplets produced during exhalation, vocalization, coughing, and sneezing are carriers of infectious viruses.1–3 These respiratory droplets can vary in size, and their travel ranges are often classified into different categories depending on their diameters.4,5 Large respiratory droplets (>5μm) tend to settle on surfaces quickly within a short distance of about 1m from the source.6 In contrast, small respiratory droplets, also known as water aerosols (<5μm), can remain suspended in the air for longer periods and may travel farther than larger droplets, contributing significantly to the transmission of respiratory infections.1,7,8 For example, when water aerosols are ejected by a forceful cough, they can be dispersed over distances of up to 4 m, which exceeds the social distancing range, within a time span of 50 s.9 These dispersed aerosols then remain in the air for more than an hour while airborne, potentially infecting individuals who come into contact with them.10 Viral genomes are found in aerosols of various sizes, with the greatest concentration observed in aerosols smaller than 5μm instead of larger respiratory droplets.11 

Reflecting growing concerns about the transmission of such respiratory droplets, the use of masks has become a ubiquitous practice in many communities worldwide.12–14 Masks serve as effective barriers, reducing both the travel range and total amount of dispersed respiratory droplets, thereby mitigating the risk of transmission in crowded places such as hospitals.15,16 Studies have shown that mask-wearing can substantially decrease the distance traveled by respiratory droplets and reduce the overall dispersion of infectious particles in the environment.17–19 For instance, the distance traveled by respiratory droplets decreased by up to 92% as a result of mask-wearing in one study, with the masks preventing the ejection of droplets produced by respiratory activities.9 However, despite the effectiveness of masks in mitigating direct transmission through respiratory droplets, small airborne water aerosols remain a persistent concern because they can remain afloat in the air for a long time.

Due to the continuing use of masks and the associated risks of infection by airborne aerosols, numerous studies have investigated the effectiveness of masks during inhalation. Konda et al. tested the filtration performance of masks made of various fabrics and types of cotton.20 Similarly, Drewnick et al. studied the influence of material properties and particle sizes on the filtration efficiency of masks.21 However, these previous studies are limited in that they did not sufficiently explore aerosol aerodynamics in an open environment. Closed environment studies make it hard to replicate aerosol movement in the real world, such as the dynamics of aerosol circumvention around a mask during inhalation. In the traditional mask performance measurement method, known as particle filtration efficiency (PFE), tests are conducted in a closed pipe setup, as illustrated in Fig. 1(a). In this configuration, all aerosols are forced to flow directly toward the mask surface due to the pressure-driven environment. In the PFE method, two different quantities of aerosols are measured: those deposited on and penetrating through masks in a closed environment. Here, only the penetrating aerosols were considered hazardous. However, deposited aerosols are also known to cause infection, as infectious viruses can survive on a mask surface and potentially be inhaled.22–26 It is evident that, from the perspective of infection prevention, aerosols that are neither deposited on a mask nor penetrate through it are the only ones that are truly safe. However, this perspective could not be explored in the closed setups of previous studies.

FIG. 1.

Schematics of (a) the traditional mask performance evaluation in a closed pipe setup20,21 and (b) the aerosol circumvention phenomenon observed in an open environment.

FIG. 1.

Schematics of (a) the traditional mask performance evaluation in a closed pipe setup20,21 and (b) the aerosol circumvention phenomenon observed in an open environment.

Close modal

In this work, we explore aerosol aerodynamics in an open environment to accurately represent the features of aerosol motion in human life. We then investigate their deposition on and penetration through a mask under varying inhalation pressures. We find that a water aerosol flow near a mask surface stagnates within the range of human inhalation. Additionally, we find that the amount of deposited aerosol can be predicted by modifying existing aerodynamic theory. Using this modified theory, we identify a critical inhalation pressure at which deposited aerosols start to penetrate through a mask and suggest a new metric for evaluating mask performance.

We quantified the dynamics of aerosols that circumvent a face mask under the dynamic conditions of inhalation in an open environment using a breath simulator, as illustrated in Fig. 2(a). The breath simulator was connected to a linear stage (SL1-2020-4S, ST1 Inc.) to simulate human inhalation. The linear stage was set to gradually move back and forth, mimicking the human breath cycle. The simulated breath flow rate was measured using a velocimeter (MiniAir 20, Schiltknecht Inc.) and was found to closely approximate the human breath cycle models for both normal and heavy inhalation conditions, respectively, as plotted in Fig. 3. Note that the terms “normal inhalation” and “heavy inhalation” refer to human breathing during daily activities (840L/min)27 and during exercise (5872L/min),28 respectively. The linear stage was operated in a 2 s inhalation cycle, which is representative of a normal respiratory rate.29 The nose of mannequin head was then connected to the breath simulator to replicate nasal breathing. We used single-layer polypropylene (PP) masks with three different fabric densities of 50 g/m2 (coarse PP mask), 100 g/m2 (medium PP mask), and 150 g/m2 (dense PP mask), as well as two representative commercial masks: a surgical mask (3M surgical, 3M Inc.) and an N95 mask (3M 9210, 3M Inc.). The detailed properties of these masks are listed in Table I. The masks were then worn tightly on a mannequin head and sealed to minimize any gaps. Gaps can vary significantly depending on factors such as face shape, mask type, and fit, affecting airflow differently across various areas of the face, particularly around the nose, cheeks, and chin. Although these gaps are a critical factor influencing aerosol flow, this study focuses on near-ideal conditions with minimal gaps in order to isolate and analyze the key mechanisms of aerosol deposition.

FIG. 2.

(a) A schematic of experimental setup to measure the amounts of deposited and penetrating water aerosols during inhalation in an open environment with (b) mask-wearing mannequin mounted on a breath simulator. (c) and (d) Experimentally measured velocity fields of the aerosol flow in front of the mannequin wearing a surgical mask under (c) normal inhalation (p¯=40g/m2·s) and (d) heavy inhalation (p¯=220g/m2·s). Here, p¯ is the mask-wearing inhalation pressure, defined in Eq. (11), and will be discussed in detail later in the text. The color map indicates the absolute value of the ratio of the vertical and horizontal components of the aerosol velocity (|uy/ux|).

FIG. 2.

(a) A schematic of experimental setup to measure the amounts of deposited and penetrating water aerosols during inhalation in an open environment with (b) mask-wearing mannequin mounted on a breath simulator. (c) and (d) Experimentally measured velocity fields of the aerosol flow in front of the mannequin wearing a surgical mask under (c) normal inhalation (p¯=40g/m2·s) and (d) heavy inhalation (p¯=220g/m2·s). Here, p¯ is the mask-wearing inhalation pressure, defined in Eq. (11), and will be discussed in detail later in the text. The color map indicates the absolute value of the ratio of the vertical and horizontal components of the aerosol velocity (|uy/ux|).

Close modal
FIG. 3.

(a) The breath flow rate generated by the breath simulator with a mannequin head is controlled to simulate two different inhalation conditions: normal inhalation and heavy inhalation. (b) The corresponding inhalation flow rates from the literature are presented for comparison.30,31

FIG. 3.

(a) The breath flow rate generated by the breath simulator with a mannequin head is controlled to simulate two different inhalation conditions: normal inhalation and heavy inhalation. (b) The corresponding inhalation flow rates from the literature are presented for comparison.30,31

Close modal
TABLE I.

The properties of the masks used in the experiments.

Density (g/m2) Permeability (m2) Thickness (mm) Porosity (%)
Coarse PP mask  50  5.31  ×1010  210  82 
Medium PP mask  100  2.88  ×1010  320  75 
Dense PP mask  150  1.57  ×1010  500  65 
Surgical  240  7.13  ×1011  520  65 
N95  320  1.51  ×1011  670  56 
Density (g/m2) Permeability (m2) Thickness (mm) Porosity (%)
Coarse PP mask  50  5.31  ×1010  210  82 
Medium PP mask  100  2.88  ×1010  320  75 
Dense PP mask  150  1.57  ×1010  500  65 
Surgical  240  7.13  ×1011  520  65 
N95  320  1.51  ×1011  670  56 

The aerosol deposition experiment was designed to replicate the aerosol flow that a walking individual would encounter. In this context, the aerosol jet was expelled at a speed of 1.5m/s, which corresponds to the average walking speed of a healthy adult.32 The humidifier was positioned 1 m away from the mask to fully expose the mask and mannequin head to the aerosol jet. This distance also aligns with the social distancing guidelines during the COVID-19 pandemic, which recommended maintaining a minimum distance of 1 m or more between individuals.33 Additionally, the average speed of water aerosols expelled during conversation between individuals is generally in the range of 15m/s at the moment of expulsion.34,35 The aerosol weights deposited on and penetrating through the mask were then measured using an electronic scale (GF-603A, AND Inc.) with 1 mg resolution. The pressure difference across the mask was measured using a pressure meter (FCO560, Furness Controls Inc.) in the flow rate range of 872L/min.

The average diameter of the water aerosols (dw) ejected from the humidifier was measured to be 4.5  μm, which closely matches the size range of human respiratory aerosols, as shown in Fig. 4.36,37 The size of water aerosols plays an important role in determining whether they settle on surfaces or travel a long distance while remaining airborne. We used a high-speed camera (Fastcam Mini UX50, Photron Inc.) attached to an optical microscope (BX53M, Olympus Inc.) equipped with a 50  × objective lens to assess the size distribution of the water aerosols. The water aerosols suspended in the air were recorded at a frame rate of 12000Hz, resulting in a spatial resolution of 0.4  μm per pixel, as shown in Fig. 4(a). During the recording of 4000 frames, we detected a total of 7800 water aerosols within a field of view of 512 × 96  μm2. To determine the size distribution of these water aerosols in our recordings, we used an in-house MATLAB code built upon the imfindcircles function, which is widely used for cell detection in various contexts.38–40  Figure 4(a) shows that the MATLAB code detected water aerosols when they were optically focused and hence measurable in size, as indicated by the red dotted circles. Moreover, our in-house MATLAB code was enhanced to prevent duplicate counting of these water aerosols in consecutive frames, ensuring an accurate size distribution analysis. Figure 4(b) shows that the water aerosol size distribution had its highest peak in the range of 24μm and the average size of the aerosols was calculated to be 4.5μm. This size distribution is similar to that of small respiratory droplets (<5μm), which can remain airborne for a long time.1,7,8

FIG. 4.

(a) Experimental images of water aerosols recorded by a high-speed camera mounted on an optical microscope. (b) The size distribution of the water aerosols has a maximum peak in the range of 2–4  μm, with the average size of the water aerosols calculated to be 4.5  μm.

FIG. 4.

(a) Experimental images of water aerosols recorded by a high-speed camera mounted on an optical microscope. (b) The size distribution of the water aerosols has a maximum peak in the range of 2–4  μm, with the average size of the water aerosols calculated to be 4.5  μm.

Close modal

In typical daily environments, where the ambient temperature is around 20–25 °C and the relative humidity is generally between 40% and 60%,35 water aerosols evaporate at a rate that can alter their size and mass during transit. According to Fick's law of diffusion,41 the rate of evaporation is proportional to the vapor pressure difference between the water aerosol and the surrounding air. For aerosols with an average size of 4.5μm, the evaporation time tevap can be estimated as tevapd02/8α(RH),42 where d0 is the initial aerosol diameter, and α(RH) is the evaporation rate constant that depends on relative humidity (RH). At 50% RH, the evaporation time for a 4.5μm water aerosol is on the order of seconds, and research shows that under this condition, such aerosols can lose up to 50% of their mass within seconds of being airborne.43,44 This indicates that, during interpersonal communication, while a portion of the aerosol's mass can evaporate before it reaches the other person's mask, a considerable fraction still can reach the mask within typical conversation distances. In our experimental setup, we maintained a controlled environment with a temperature of 20±2°C and a relative humidity of 80±5% to minimize such evaporation effects. Under these conditions, the evaporation rate was significantly reduced due to the smaller vapor pressure difference between the aerosol and the surrounding air. To be specific, at 80% relative humidity (RH), a 4.5μm aerosol would experience only about 10% mass loss over the same time and distance.45 This allowed us to focus on the aerosol flow and deposition mechanisms themselves, which is the main focus of this study, with less influence from changes in aerosol size or mass.

A particle image velocimetry (PIV) experiment was performed to analyze the velocity field of the aerosol flow around a mask, as shown in Fig. 5. A 10 W, 532 nm continuous wave DPSS laser system (GL532T9, Shanghai Laser & Optics Century) was used in conjunction with a Powell lens (Thorlabs) to create the laser sheet and illuminate the water aerosols. To minimize 3D effects, the laser sheet was made as thin as feasible, with a thickness less than 1 mm. A high-speed camera (FASTCAM Nova S9, Photron) with a resolution of 1024  × 1024 pixels and a frame rate of 6000 Hz was used to capture the aerosol flow. Here, it is worth noting that the water aerosols themselves were used as seeding particles in the PIV measurements, allowing us to directly capture their flow. While the main focus of this study is on aerosol flow, the very low Stokes number near the mask surface (St=9.3×105) indicates that the aerosol flow in this region closely followed the air flow. Here, the Stokes number is known to serve as an indicator of how well the seeding particles align with the fluid flow.46 The images were then post-processed using PIVlab,47 a MATLAB-based open-source software, to determine the velocity field of the aerosol flow. The image pairs were analyzed using the fast Fourier transform window deformation algorithm, with a final interrogation window size of 4  × 4 pixels and 50% window overlap during four-step passes, resulting in a spatial resolution of 130  μm × 130  μm. The subpixel displacement was estimated through a 2  × 3 Gaussian point fit. Spurious vectors were eliminated using our in-house MATLAB code built upon a median filter with 5  × 5 vectors per 3 frames and universal outlier detection and replaced through interpolation. The filtered vectors were then averaged within 3  × 3 vectors. The velocity fields in Figs. 2(c) and 2(d), as well as Figs. 7(c) and 7(d), were obtained by averaging the instantaneous flow fields over 12 000 frames, which corresponds to one cycle of 2 s at 6000 Hz.

FIG. 5.

A schematic of the PIV experimental setup to analyze the velocity field of the aerosol flow around a mask.

FIG. 5.

A schematic of the PIV experimental setup to analyze the velocity field of the aerosol flow around a mask.

Close modal

The velocity fields obtained from the PIV experiment near the masks were compared under normal inhalation conditions (840L/min)27 and heavy inhalation conditions (5872L/min),28 as shown in Figs. 2(c) and 2(d), respectively. In these figures, the colors represent the absolute value of the ratio of the vertical components to the horizontal components of the aerosol velocity (|uy/ux|) toward the mask surface. A reduced ux, represented by the decreased size of the vector arrows, was observed under normal inhalation conditions. This flow pattern resembles the well-known pattern of flow stagnation near a solid wall48,49 and is more clearly shown in the magnified images of Figs. 2(c) and 2(d). This flow stagnation weakened as the inhalation strength increased under heavy inhalation conditions, under which aerosols were pulled more directly toward the mask.

To theoretically explore the relationship between the flow stagnation, inhalation pressure, and surface curvature κ, we conducted an experiment with a curvature-controllable mask head (CC head) mounted on the breath simulator, as shown in Fig. 6. As shown in Fig. 6(b), face masks, particularly around the nose area, tend to exhibit significantly larger horizontal curvature (κh) compared to vertical curvature (κv). Specifically, masks like the N95, as depicted in Fig. 6(a), typically have near-zero vertical curvature.50,51 In this regard, we simplified the analysis of the complex curvature of face masks using the CC heads [Fig. 6(c)], which allowed us to independently test the effects of horizontal and vertical curvatures. The horizontal curvature was set at 0.08 mm−1 based on the measurement from a mannequin wearing an N95 mask. This CC head setup provided a simplified geometry in which both the flow stagnation and aerosol circumvention could be more clearly identified. The CC head had a 25 mm diameter to approximate the size of the human nose and mouth region.52 

FIG. 6.

Schematics of the mannequin head and the curvature-controllable (CC) head: (a) Side and top views of the mannequin head, illustrating the vertical curvature, κv, and horizontal curvature, κh, respectively. (b) These two principal curvatures are also shown in the oblique view of the mannequin head. (c) Two different CC heads, each reflecting the two distinct curvatures. Here, the specific values of κv and κh are obtained from measurements of the mannequin head wearing an N95 mask.

FIG. 6.

Schematics of the mannequin head and the curvature-controllable (CC) head: (a) Side and top views of the mannequin head, illustrating the vertical curvature, κv, and horizontal curvature, κh, respectively. (b) These two principal curvatures are also shown in the oblique view of the mannequin head. (c) Two different CC heads, each reflecting the two distinct curvatures. Here, the specific values of κv and κh are obtained from measurements of the mannequin head wearing an N95 mask.

Close modal
In a theoretical point of view, a stagnation flow is characterized by its viscous flow-like behavior due to its very low inertial contribution.53,54 The flow stagnation can be quantified by comparing the inertial term, ρa(u·u), and the viscous term, μa2u, in the Navier–Stokes equation, yielding the inertial-viscous ratio as
(1)
where ρa is the air density, u is the flow velocity, and μa is the air viscosity. The numerical value of η was then calculated using PIV data acquired from the experiments for both the CC head and mannequin. Figures 7(a) and 7(b) show η as a function of different mask-wearing inhalation pressures, p¯, in the range of 872L/min for two representative curvatures of κv=0 [Fig. 7(a)] and κh=0.08mm1 [Fig. 7(b)]. The definition of the mask-wearing pressure p¯ will be discussed in Sec. III C. Figure 7(a) shows that, under normal inhalation conditions, the value of η was consistently low, measuring less than 0.025 for experiments with a curvature value of 0mm1. Masks with a coarser density exhibited a slight increase in η during heavy inhalation, but the value still remained below 0.1. This ensured that the aerosol flow in the close vicinity of the mask surface behaved like a viscous flow. This viscous-like behavior from stagnation is more clearly shown in the velocity field near the flat CC head [Fig. 7(c)] and is similar to that in front of the mannequin head [Figs. 2(c) and 2(d)]. In contrast, Fig. 7(d) shows that the magnitude of the aerosol velocity, represented by the vector arrow size, did not decrease. This illustrates that water aerosols rarely stagnated on the convex CC head. Instead, in this case, the water aerosols circumvented the convex CC head, which is represented by the gray region. Due to the reduced stagnation, in experiments with a curvature value of 0.08mm1 [Fig. 7(d)], the value of η was measured to be relatively high, increasing to 0.5 for coarser density masks. This shows that the convex CC head can explain the aerosol circumvention around the mask-wearing mannequin head. Thus, aerosol deposition on face masks could be representatively expressed and simplified using flat CC head experiments. Similarly, while the Reynolds number (=ρauxdw/μa) in the vicinity of the convex CC head was calculated to be large (>0.4), the Reynolds number in the vicinity of the mask for both the mannequin and the flat CC head was found to be small (<0.1). Here, it is worth to mention that the characteristic length for calculating the Reynolds number was chosen to be the aerosol droplet diameter dw, as our primary focus is on the near-surface dynamics where aerosol deposition occurs. In this regard, the water aerosol flow near the flat CC head can be described by the Stokes equation55 
(2)
FIG. 7.

(a) and (b) A comparison of the inertial-viscous ratio (η) from the PIV data in the range of 1256g/m2·s. (c) and (d) The experimentally measured velocity fields of the aerosol flow in front of a surgical mask on a curvature-controllable head under normal inhalation (46g/m2·s) and heavy inhalation (256g/m2·s). Here, p¯ is the mask-wearing inhalation pressure, defined in Eq. (11).

FIG. 7.

(a) and (b) A comparison of the inertial-viscous ratio (η) from the PIV data in the range of 1256g/m2·s. (c) and (d) The experimentally measured velocity fields of the aerosol flow in front of a surgical mask on a curvature-controllable head under normal inhalation (46g/m2·s) and heavy inhalation (256g/m2·s). Here, p¯ is the mask-wearing inhalation pressure, defined in Eq. (11).

Close modal
The substitution of the stream function (ψ/y=ux, ψ/x=uy) into the Stokes Eq. (2) gives the following equation for the x-momentum components:
(3)
The separation of variables can then be applied to solve Eq. (3), where ψ is expressed as a product of functions of individual spatial coordinates, such as X(x) and Y(y): ψ=X(x)Y(y). The specific forms of X(x) and Y(y) were assumed based on their experimental results from the PIV experiment. Figures 8(a) and 8(b) show that the PIV data of ψ/y[=X(x)((dY(y)/dy)] followed an exponential trend while the numerical solution of ψ/x[=Y(y)((dx(x)/dx)] exhibited a linear trend. From this, X(x) and Y(y) were assumed to be an exponential function and a linear function, respectively,
(4)
FIG. 8.

(a) The horizontal component of the aerosol velocity, ψ/y, vs x. (b) The vertical component of the aerosol velocity, ψ/x, vs y. Here, the color bar indicates the mask-wearing inhalation pressure. (c) Streamline of the aerosols circumventing a mask during inhalation with boundary conditions for x= and x = 0 in an open environment. (d) and (e) Corresponding decomposed streamlines of (d) the aerosols passing straight through the mask and (e) aerosols detouring around the mask.

FIG. 8.

(a) The horizontal component of the aerosol velocity, ψ/y, vs x. (b) The vertical component of the aerosol velocity, ψ/x, vs y. Here, the color bar indicates the mask-wearing inhalation pressure. (c) Streamline of the aerosols circumventing a mask during inhalation with boundary conditions for x= and x = 0 in an open environment. (d) and (e) Corresponding decomposed streamlines of (d) the aerosols passing straight through the mask and (e) aerosols detouring around the mask.

Close modal
Substituting Eq. (4) into Eq. (3) yields the following equation:
(5)
Boundary conditions were applied to determine the unknown coefficients c1 and c2, as illustrated in Fig. 8(c). The boundary conditions were set as follows. At a sufficiently distant point to the right of the boundary, the horizontal velocity component ux should approach zero, i.e., ux(,y)=0. The pressure at the far-right boundary was constrained to match the atmospheric pressure as p(,y)=patm. At the left boundary, corresponding to x=0, there existed a pressure difference relative to the atmospheric pressure, represented as p(0,y)patm=Δp. To apply these boundary conditions, Eq. (5) was integrated from x= to x=0, resulting in the following equation:
(6)
Finally, recalling that the velocity components ux and uy were expressed as functions of the stream function (ψ/y=ux,ψ/x=uy), Eq. (6) gives a solution for the velocity components ux and uy as follows:
(7)
To determine the unknown coefficient λ1, we applied the well-known aerodynamic theory used in the field of aerosol-harvesting research, developed by Rivera,56 which decomposes the flow into two components to describe the aerodynamics of water aerosols circumventing a solid body. According to this theory, the water aerosol flow can be divided into two components: one flows through the mask and the other detours around it, as illustrated in Figs. 8(c)–8(e). A schematic of the model [Figs. 8(c)–8(e)] illustrates that the horizontal component of the aerosol velocity near a mask, denoted as ux, can be described as a sum of velocities,
(8)
For the aerosol component passing directly through a mask [Fig. 8(d)], the velocity upass can be calculated using the empirical equation upass=(1/μa)(Φ/h)Δp following previous studies on mask filtration,57–59 where Φ is the permeability and h is the mask thickness. For the aerosol component detouring around the mask [Fig. 8(e)], particularly in the low Reynolds number flow regime where drag forces dominate, the velocity udetour can be expressed as udetour=(1/μa)(dw/12)Δp.60 Note that the equations for upass and udetour were adapted from previous literature,57–60 with the notation and format modified to align with the symbols and expressions defined in the present study. Given that ux(0,y)=(λ1/μa)Δp from Eq. (7), the unknown coefficient can be determined using Eq. (8) as
(9)
The aerosol deposition rate per unit area (ṁw) can then be calculated as
(10)
To observe the aerosol deposition pattern on a mask, the water aerosols were dyed red, and the inhalation experiment was conducted using the 3-D printed mannequin head, as shown in the oblique view of Fig. 9. In this figure, it can be observed that the water aerosols were primarily deposited along the centerline. This is because the water aerosols experienced flow stagnation following the centerline of the mask-wearing mannequin, as confirmed by Figs. 2(c) and 2(d), resulting in dominant deposition along that line. This was also observed in the experiment with the flat CC head [Fig. 7(c)]. On the contrary, fewer aerosols were deposited on the cheek as they circumvented it, as shown in front of the convex CC head [Fig. 7(d)].
FIG. 9.

The aerosol deposition rate (ṁw) as a function of the mask-wearing inhalation pressure (p¯) compared to the result from the stagnation-based theory of Eq. (10), shown as a black line. The gray dashed line represents the total mass flow rate of water aerosols (ṁtotal) injected from the humidifier. The inset photo shows an oblique view of the mannequin wearing a surgical mask with a concentrated aerosol deposition line along the y axis. The open symbols represent the total amounts of aerosols that were both deposited on and penetrated through the mask, while the filled symbols represent the amount of aerosols that were deposited on the mask only.

FIG. 9.

The aerosol deposition rate (ṁw) as a function of the mask-wearing inhalation pressure (p¯) compared to the result from the stagnation-based theory of Eq. (10), shown as a black line. The gray dashed line represents the total mass flow rate of water aerosols (ṁtotal) injected from the humidifier. The inset photo shows an oblique view of the mannequin wearing a surgical mask with a concentrated aerosol deposition line along the y axis. The open symbols represent the total amounts of aerosols that were both deposited on and penetrated through the mask, while the filled symbols represent the amount of aerosols that were deposited on the mask only.

Close modal
Figure 9 shows the aerosol deposition rate of ṁw as a function of the mask-wearing inhalation pressure p¯, which is defined as
(11)
The black line represents the theoretical model of Eq. (10) without any fitting parameters. The gray dashed line indicates the total mass flow rate of water aerosols (ṁtotal) injected from the humidifier. The vertical gap between the gray dashed line and the aerosol deposition rate dataset represents the degree of aerosol circumvention. In this plot, the open symbols represent the total amounts of aerosols that were deposited on or penetrated through the mask, while the filled symbols represent the quantity of deposited aerosols only. Note that there are only open symbols when p¯>34g/m2·s because the aerosols were unable to penetrate at pressures weaker than this critical value. The plot shows that all the data collected from the flat CC head experiments were strongly consistent with the theory. It is worth noting that the filled symbols started to deviate once the critical pressure of p¯c=34g/m2·s was surpassed, while the open symbols continued to adhere closely to the theory. This increasing discrepancy in the filled symbols indicates that more aerosols penetrated the mask as p¯ increased, increasing the risk to human health. It is particularly interesting to note that, when we measured the critical pressure, p¯c, in terms of the mask-wearing pressure, this value was observed to be relatively consistent in the range of 34–50  g/m2·s across different types of masks. When expressed in pascals, this critical pressure exhibited a wider range, varying from 5 to 47 Pa. This is presumably because the mask-wearing pressure defined in this study effectively normalizes the force involved in inhaling aerosols into the mask, accounting for both aerosol and mask properties. Additionally, in Fig. 9, the data obtained along the centerline region from the mask-wearing mannequin (represented as triangles) shows patterns consistent with the flat CC head experiments, whereas the aerosol deposition rate in experiments with κh=0.08mm1 deviates significantly from the theory due to substantial aerosol circumvention caused by its curvature. This is consistent with the results of Sec. III A, indicating that the flat CC head experiments appropriately represented aerosol deposition on the mask, while the convex CC head experiments accurately described aerosol circumvention.

In addition to the aerosol deposition, the temporal evolution of the impact speeds of the aerosols was studied for different types of masks and inhalation conditions, as plotted in Fig. 10. The impact speed was calculated by averaging ux over a field of view measuring 10  × 10 mm2 near the mask surface. The black curves are included in the plots as reference data for comparison, as the experiment was conducted without a mask. Note that the experiments were conducted under the same operating conditions in the linear stage for each plot. The beginning and end of the plot (t=0 s and t=2 s) represent the moments at which the linear stage began operating and stopped, respectively. After t=0 s, the impact speed rapidly increased when the water aerosols influenced by inhalation reached the mask. The arrival time was delayed with a lower p¯, as can be seen by comparing Figs. 10(a) and 10(b). In each panel of this figure, it can also be observed that denser masks delayed the moment at which the impact speed rapidly increased. This indicates that the onset of the impact speed was delayed by the thickening of the mask. In addition, the plots show that as the mask thickened, the inhalation time span also decreased. These trends were consistently observed across all inhalation conditions.

FIG. 10.

The impact speed of aerosols vs time for each mask under two different inhalation conditions: (a) normal and (b) heavy inhalation conditions.

FIG. 10.

The impact speed of aerosols vs time for each mask under two different inhalation conditions: (a) normal and (b) heavy inhalation conditions.

Close modal
We finally compared the mask performance results measured in the present study with values from previous literature under normal inhalation conditions for two different commercial masks, as summarized in Table II. Recall that the previous metric of mask performance, known as the particle filtration efficiency (PFE), was developed for a closed experimental setup. In this work, as an alternative, the aerosol circumvention efficiency (ACE) is proposed as a mask performance metric for open environments,
(12)
TABLE II.

An evaluation of mask performance as a function of the aerosol circumvention efficiency (ACE) in an open environment and as a function of the particle filtration efficiency (PFE) in a closed setting. Note that ACE and PFE are fundamentally different metrics and are hard to directly compare.

Mask performance Surgical (%) N95 (%)
ACE in the present work (open environment)  92.5  98.3 
PFE (closed environment)  Drewnick et al.21   69.5  98.0 
Hill et al.61   87.0  97.0 
Shah et al.62   47.0  95.0 
Pei et al.63   80.0  98.0 
Morias et al.64   85.5  98.5 
Mask performance Surgical (%) N95 (%)
ACE in the present work (open environment)  92.5  98.3 
PFE (closed environment)  Drewnick et al.21   69.5  98.0 
Hill et al.61   87.0  97.0 
Shah et al.62   47.0  95.0 
Pei et al.63   80.0  98.0 
Morias et al.64   85.5  98.5 

As the ACE accounts for aerosols not deposited on the mask surface, it is a more challenging metric to use than the conventional PFE. Table II suggests that PFE measurements may underestimate the performance of surgical masks for use in an open environment. According to the ACE, 92.5% of water aerosols failed to reach the surface of the surgical mask, meaning that only 7.5% of the aerosols were deposited on it. In contrast, the PFE data show that, within the closed setup where 100% of water aerosols were deposited, 13.0%53.0% ended up penetrating through the mask. For the N95 mask, both the ACE and the PFE measures showed a high mask performance of over 95%, owing to its excellent circumvention capability and penetration resistance. The ACE data also show that, compared to surgical masks, only 1.7% of aerosols were deposited on the N95 mask. This is because the curvature of the N95 mask was larger than that of the surgical mask, facilitating aerosol circumvention. This suggests that geometric factors may influence mask performance in addition to filtration capabilities. Recent studies have explored various modifications to mask shapes to enhance infection prevention,65,66 including duckbill and axe-shaped masks.67 Thus, the use of wires or frames to keep masks in a circumvention-favorable shape is encouraged.

In this study, we have examined the aerodynamics of water aerosols and their deposition on a mask under varying inhalation pressures in an open environment. Particle image velocimetry (PIV) data showed that a water aerosol flow near a mask surface exhibits characteristics similar to a viscous flow, leading to stagnation within the range of typical human inhalation. A stagnation-based theory showed that the rate of aerosol deposition on a face mask can be described using the inhalation pressure and mask properties. A critical inhalation pressure of p¯c=34g/m2·s was also identified at which the deposited aerosols begin to penetrate the mask. Finally, we introduced a new metric, the aerosol circumvention efficiency (ACE), to estimate mask performance in an open environment, which is a better reflection of real-life conditions.

This work was supported by a KIST internal project (2E33202). S.C. also acknowledges support from the Samsung Research Funding & Incubation Center of Samsung Electronics under Project No. SRFC-IT1901-51.

The authors have no conflicts to disclose.

Y. J. Lee: Conceptualization (equal); Data curation (lead); Formal analysis (lead); Investigation (lead); Methodology (lead); Software (lead); Validation (lead); Visualization (lead); Writing – original draft (lead); Writing – review & editing (lead). M. W. Moon: Funding acquisition (lead); Project administration (equal); Validation (supporting); Writing – review & editing (supporting). S. Chung: Funding acquisition (equal); Supervision (equal); Validation (equal); Writing – review & editing (equal). S. J. Kim: Conceptualization (equal); Formal analysis (equal); Funding acquisition (equal); Investigation (equal); Methodology (equal); Project administration (equal); Supervision (equal); Validation (equal); Visualization (equal); Writing – review & editing (equal).

The data that support the findings of this study are available from the corresponding author upon reasonable request.

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