Introduction

Particle aggregation in suspensions is a fundamental process for the behavior and transport of particulate matter in both natural and industrial settings. It is a key element for ecological balance in nature, as it contributes to sediment transport, water purification, and the nutrient cycle of oceans, lakes, and rivers1. On the other hand, in industry, aggregation is targeted for applications in water treatment, mining, pharmaceutical production, food processing, and battery manufacturing2,3,4.

The aggregation process of suspended particles consists of two parts: first, two or more particles come very close together (accumulation) and possibly in contact (collision), and second, the particles stay together, forming a floc5 due to surface forces in direct contact, material properties that form bridges, or interlocking due to the shape of the particles6. The physical process of bringing particles together and facilitating aggregation is attributed to three mechanisms: (i) Brownian motion, (ii) differential settling and (iii) fluid shear7. Brownian motion is a colloidal behavior and important for small particles (≤2μm) in quiescent fluid, where individual entities collide with fluid molecules and undergo a direction-independent random walk8. The intensity of particle movement decreases with increasing particle size and fluid viscosity. As the length scale of the particle size increases, differential settling and fluid shear become more relevant8,9,10. Differential settling describes the process of particles and aggregates settling at different velocities caused by varying particle properties such as size, density, solid volume fraction and shape5,11,12,13. This mechanism is predominant when the fluid is at rest or as long as settling is dominant for particle motion. Once fluid flow becomes the dominant driving force of particle motion, aggregation is governed mainly by fluid shear, where particles move at different speeds due to velocity gradients in the flow field5. All three mechanisms, Brownian motion, differential settling, and fluid shear, increase the probability of particle collisions with subsequent aggregation by inducing relative motion between two or more particles.

A key property of particles for aggregation is cohesion, an attractive force between particles due to electrochemical forces. Cohesion is known to strengthen the bonds between particles, increasing the stability of aggregates and allowing the formation of larger structures12,14. Under Earth-bound conditions, cohesive forces dominate over gravitational forces for fine particles, typically clay and silt, up to a characteristic size of approximately 63 μm15. However, as aggregates grow in size, their effective mass increases, leading to a transition, in which gravitational forces exceed cohesive interactions and ultimately govern particle dynamics16. This gravity-induced limitation significantly constrains the ability to isolate and investigate the long-term effects of cohesion on the aggregation behavior of particles. In contrast, microgravity environments offer a unique opportunity to overcome this constraint, as the suppression of gravity may not only extend the range over which cohesive interactions dominate, but also increase the maximum particle size for which cohesion remains an effective interaction mechanism17. Given the omnipresence of gravity on Earth, various methods such as drop towers or parabolic flights have increasingly gained attention in recent decades to investigate the characteristics of particulate suspensions in weightlessness18. However, these experiments provide weightless conditions for only a few seconds, significantly restricting the scope of investigation.

It is against this background that long-term experiments on board the International Space Station (ISS) have allowed new possibilities for investigating particle behavior in microgravity. The facilities on board the ISS have already been used for a large number of studies to investigate crystal formation19,20 or colloidal aggregation21,22. The conditions on board the ISS are almost weightless, as the gravitational field is several orders of magnitude weaker than on Earth. However, it needs to be taken into account that inertia effects still exist due to the presence of onboard accelerations. According to Monti & Savino23, these accelerations can be caused by three factors: (i) external sources, e.g., forces acting on the space station due to aerodynamics and operational procedures, (ii) mass ejections, due to rocket-powered activities such as docking or reboost maneuvers, and (iii) internal causes arising from the presence of crew members and machinery, including fans, compressors, and pumps24. The effects of these accelerations can be divided into constant accelerations and oscillating accelerations23,25,26. The latter is referred to as g-jitter and has gained a lot of attention in the recent past. Crystallization experiments in the first International Microgravity Laboratory (IML-1)27 and on board the ISS28,29,30 have shown that the effects of g-jitter can lead to random particle motion in microgravity, known as an inertial random walk31. Tracing the trajectories of individual randomly moving particles showed that the effect of g-jitter causes convective flows that lead to higher particle velocities than those obtained by diffusion18. These flows lead to clustering of particles due to the inertia of the particles, characterized by high particle concentrations in local regions of the surrounding fluid, generally termed inertial clustering32.

The crystallization process in microgravity has been extensively studied since the first experiments in the early seventies. During the past decades, more than 500 studies have explored the effects of microgravity on crystal formation. These investigations have significantly advanced both experimental techniques and the understanding of crystal manufacturing and aggregation dynamics19,20. This has generated valuable expertise on controlled growth processes and the influence of g-jitter, which contributes to a wide range of scientific and technical applications beyond crystallization33. However, most studies focused mainly on manufactured materials and experimental durations of only a few days. Although these conditions were completely sufficient for the intended applications, this opens up the questions of the extent to which the aggregate behavior of natural materials changes and how this behaves over a long period of time.

To address this, we performed microgravity experiments on board the ISS to investigate the aggregation process of natural clay particles in saline suspensions over a time period that exceeds previous campaigns by far. The setup design allowed the exclusion of differential settling and fluid shear as driving factors for particle contact. The impact of g-jitter was monitored and investigated in detail. We supplement these experiments with a campaign of particle-resolved direct numerical simulations (pr-DNS) to further investigate the governing mechanisms responsible for the long-term dynamics of particle aggregation. This allows elucidating potential aggregation mechanisms beyond differential settling and fluid shear and to show how these mechanisms scale with varying properties of the fluid and suspended particles, respectively.

Methods

Experimental setup

Microgravity experiments were conducted on board the ISS to investigate the long-term flocculation behavior of clay particles in saline water. For this purpose, ten cuvettes were prepared on Earth and loaded with varying material compositions (cf. Applied materials). Each cuvette was also equipped with a magnetic bead for stirring purposes to homogenize the suspension. Before transport to the ISS, the cuvettes were installed in the Binary Colloidal Alloy Test (BCAT) apparatus, a rack in which the cuvettes are arranged in two rows. An image of the BCAT system is presented in §1 of the Supplementary Information (SI). After arrival at the ISS, the system was installed in the Japanese Pressurized Module (JPM), which is part of the Japanese Experiment Module (JEM). The initial stirring was performed by the astronaut applying a second external magnet and swirling the bead inside the suspension for 60 seconds for each cuvette. Preliminary tests in an Earth-bound environment showed that this strategy is useful for preparing samples on the ISS34. After initial homogenization, the cuvettes were left undisturbed for a period of 99 days and monitored throughout the experiment.

Applied materials

Each cuvette was filled with a specified clay composition and salt water, where the latter was the same mixture of purified sodium chloride and deionized water for all cuvettes. The mixture had a salt concentration of 35 [PSU] that represents the salinity of seawater35, where PSU is the practical salinity unit equivalent to parts per thousand (ppt). The suspensions contained defined concentrations of kaolinite, montmorillonite, and sand, representing different sediment compositions with precisely characterized grain size distributions34,36. Based on our preliminary earth-bound studies34,35, we decided not to vary the salt concentration because its influence is evident only in a very narrow salt concentration range. Hence, we decided to apply a high salinity to maximize cohesion and suppress the electric double layer force that can potentially have a repulsive effect. The specifications of the different compositions are summarized in Table 1 and further details on the applied materials are specified in §1 of the SI.

Table 1 Concentrations of the sediment compositions in [ppt]

Image recording and analysis

The samples were continuously recorded by photographs for the entire duration of the experiment. A Nikon D2Xs camera was installed in front of the rack together with a SB-800 flash on the rear side. The camera was equipped with the Nikon AF Micro-Nikkor 105/2.8 D lens, which was used in manual focus mode. Remote shutter release was applied for the recordings to avoid disturbances caused by manually pressing the shutter release. The interval of image recording was adjusted during the experiments. Initially, images were taken every 30 minutes for the first week, then every 2 hours for the next two weeks, before switching to every 4 hours for the remainder of the experiments. The images were analyzed by performing an autocorrelation function to obtain the evolution of the mean floc size37,38. Based on the gray scale of the pixel intensity of the 2D images, a one-dimensional radial autocorrelation is computed to quantify the aggregate sizes over the course of the experiment. More details on image analysis and applied autocorrelation functions are described in §2 of SI.

Acceleration measurements

The effects of g-jitter on the experiments were monitored by two accelerometers of the Space Accelerometer Measurement System (SAMS), which were located together with the setup in the JEM of the ISS for the entire duration of the experiment. The recorded data was made available by the Glenn Research Center(GRC) of the National Aeronautics Space Administration (NASA), based on which the frequency ranges were determined. Fig. 1 presents the analyzed data of the g-jitter of the sensors SAMS 121f02 (Fig. 1a) and SAMS 121f05 (Fig. 1b) along the x-direction. This direction is parallel to the center line of the laboratory module with its origin in the center of mass of the spacecraft and pointing to the forward direction39. The spectral plots show the minimum, maximum, and average accelerations expressed as a fraction of the gravitational acceleration \(\left(g=9.81\,m/{s}^{2}\right)\) for a frequency range between 0 and 250 Hz, with local peaks indicating dominant frequencies. A match of the local peaks in both accelerometers indicates the presence of a decisive source that may have significantly affected the experiments. This is the case, for example, at around 60 Hz. The complementary plots of the remaining coordinate directions, i.e., the y- and z-direction, are presented in §1 of SI.

Fig. 1: Spectra plots of the acceleration and frequency ranges of the g-jitter on board the ISS, considering exclusively the x-direction, which is aligned with the central axis of the laboratory module.
figure 1

The acceleration is expressed as a fraction of the gravitational acceleration g. a presents the data of accelerometer SAMS 121f02 and (b) of SAMS 121f05.

Numerical simulations

Numerical simulations were performed as a complementary approach to the experiments, with the specific aim of isolating and examining the fundamental mechanisms of oscillation-induced particle aggregation under microgravity conditions. Although the experimental setup serves as a conceptual reference, the simulations are intentionally designed with a simplified scope to facilitate systematic investigation of the underlying physical processes. This comprises the following key aspects: (i) representation of the random three-dimensional nature of the g-jitter as a monochromatic unidirectional oscillation, (ii) amplification of the oscillation amplitude with respect to the measured acceleration data, and (iii) intentional increase in the particle volume fraction relative to the experimental conditions. The application of these amplified parameters emphasizes the effects of oscillation-induced interactions to better identify the governing effects.

The simulations are based on a pr-DNS framework that solves the Navier-Stokes and continuity equations for an incompressible Newtonian fluid12,40,41. The motion of the non-Brownian particles is calculated by integrating the Newton-Euler equations, with fluid-particle and particle-particle interactions captured through the immersed boundary method (IBM)40,42,43 and a suitable discrete element model that accounts for contact, friction, lubrication and cohesion, respectively12,40. The computational domain is a cubic container of size Lx,y,z = 20dp, where dp denotes the particle diameter, with periodic boundary conditions applied in all directions to eliminate wall effects. The suspended particles are represented as rigid monodisperse spheres with no-slip boundary conditions on their surface and cohesive properties based on a cohesive force model12. The initial arrangement of the particles ensures a non-contact random distribution. In addition, gravitational acceleration is neglected, while both fluid and particle inertia are explicitly resolved. Consequently, the applied oscillation represents the only external force term that acts in the x-direction and is characterized by \({u}_{f}=-A{{\Omega }}\sin {{\Omega }}t\). Here, uf represents the velocity of the oscillatory fluid, A the distance amplitude, AΩ the velocity amplitude, t the time, Ω = 2πf the angular frequency, and f the frequency41. High spatial and temporal resolutions were achieved by discretizing each particle with dp/h = 20 and each oscillation with Δt = Tf/200, where h denotes the cell size of the uniform grid, Δt the time step, and Tf = 1/f the oscillation period. Details of the governing equations and further information about the applied pr-DNS are elaborated in §3 of SI.

Computational scenario

The simulations employed material properties consistent with the experimental conditions, adopting a fluid density of ρf = 1000 kg/m3 and a kinematic viscosity of νf = 1.002 10−6 m2/s, along with a particle density of ρp = 2600 kg/m3. The initial particle diameter is set to dp = 115 μm as derived from the sizes observed during early stages of aggregate formation in the ISS experiments (cf. Results, ISS Experiments), thereby representing higher-order aggregates44. The frequency was chosen as f = 60 Hz according to the measurements of the accelerometers on board. If f is considered along with the measured accelerations, which are on the order of \(| {A}_{x}(f)| ,g={\mathcal{O}}(1{0}^{-5})\,m/{s}^{2}={\mathcal{O}}(1{0}^{1})\,\mu m/{s}^{2}\) (cf. Fig. 1), the corresponding oscillation amplitude is computed by \(A=| {A}_{x}(f)| ,g\,/\,{{{\Omega }}}^{2}={\mathcal{O}}(1{0}^{-5})\,\mu m\). To assess the relative scale of oscillation, the amplitude is compared to the particle diameter, yielding an amplitude ratio of \(\epsilon =A/{d}_{p}={\mathcal{O}}(1{0}^{-7})\). The oscillation amplitude was increased to \(A={\mathcal{O}}(1{0}^{1})\,\mu m\) to enhance particle motion and thereby increasing the probability of particle collisions to facilitate aggregation. Similarly, the particle volume fraction was increased from ϕ = 0.008 (see cuvettes no. 2 and 7, highlighted in Table 1) to approximately \(\phi ={\mathcal{O}}(1{0}^{-1})\) to reduce the mean free path between suspended particles.

Non-dimensional quantities

We introduce characteristic scales to non-dimensionalize the numerical properties. For this purpose, we choose dp and 1/Ω as relevant length and time scales, as well as ρf as density reference. This yields:

$$\begin{array}{ll}\ell\,=\,{d}_{p}\tilde{\ell }\,,\quad t=\tilde{t}/{\Omega }\,,\quad {\bf{u}}={d}_{p}{\Omega }\tilde{{\bf{u}}}\,,\\\qquad\quad{\bf{D}}\,=\,{d}_{p}^{2}{\Omega }\tilde{{\bf{D}}}\,,\quad \rho ={\rho }_{f}\tilde{\rho }\end{array}$$
(1)

The tilde symbol indicates the dimensionless variables and represents a typical length. u = (u, v, w)T is the fluid velocity vector and \({\bf{D}}={({D}_{x},{D}_{y},{D}_{z})}^{T}\) the main diagonal of the diffusion tensor.

In addition, we use non-dimensional numbers to generalize the flow properties and to identify dominant physical effects. Important for the present study are the Reynolds number Re, the non-dimensional frequency S, and the Stokes number St. The Reynolds number defined as Re = uf,maxdp/νf represents the ratio of inertia and viscous forces, where uf,max = AΩ is the velocity amplitude. The non-dimensional frequency describes the characteristics of the oscillations41,45,46,47 and we define it as \(S=SlRe={{d}_{p}}^{2}{\Omega }/(36{\nu }_{f})\), which is a product of the Strouhal number Sl = Ωdp/(9uf) and Re. The Stokes number constitutes the ability of the immersed particles to respond to changes in the fluid flow and is defined as St = τp/τf = ρs − 1 2S by comparing the particle response time \({\tau }_{p}=| {\rho }_{s}-1| {d}_{p}^{2}/(18{\nu }_{f})\) to a characteristic time scale of the fluid flow τf = 1/Ω41. Here, ρs = ρp/ρf represents the density ratio between the density of the particle and the fluid.

Systematic investigations on the effects of f and ρs on the aggregation behavior of particles in oscillations have already been conducted by Kleischmann et al.41. Therefore, S = 0.14, St = 0.44, and ρs = 2.6 remain constant in all numerical configurations of the present study. However, the effects of oscillation amplitude and volume fraction on aggregation behavior are largely unexplored. The increase in amplitude is expected to increase the mobility of the particles and the increase in volume fraction to reduce the mean free path. This indicates that both variables might have the potential to significantly enhance aggregate formation. To investigate this in detail, both parameters were systematically varied within the ranges ϵ = [0.05, 0.2] and ϕ = [0.042, 0.164]. The variation of ϵ results in Reynolds numbers spanning the range Re = [0.25, 1].

Simulation campaign

The variation of ϵ and ϕ results in different numerical setups, which are shown in Table 2. For both parameters, three different values were considered, ϵ = 0.05, 0.1, and 0.2, as well as ϕ = 0.042, 0.084, and 0.164. The latter results in varying numbers of particles Np = 641, 1283, and 2502. A reference setup (Ref) with ϕ = 0.084 and ϵ = 0.10 was defined, to establish a baseline for the comparison of the different parameters. Based on this, four modified setups were created: a setup each with halved (LoPhi) and doubled volume fraction (HiPhi), while maintaining ϵ = 0.10; and a setup each with halved (LoAmp) and doubled amplitude ratio (HiAmp), while keeping ϕ = 0.084 constant.

Table 2 Key parameters of numerical simulation scenarios

Results

ISS experiments

Selected photographs of cuvette no. 2 over the course of the experiments on board the ISS are presented in Fig. 2. Photographs of cuvette no. 7 and detailed close-ups of both cuvettes are shown in §1 of SI.

Fig. 2: Selected photographs of cuvette no. 2 over the duration of the experiment on board the ISS.
figure 2

The magnetic bead is at the bottom of the cuvette.

A qualitative visual evaluation already reveals that, originating from a homogeneous suspension, pattern formation emerges. Apparently, the presence of the magnetic bead has a considerable effect on the nearby suspension. During the course of the experiment, the region close to the magnetic bead is characterized by low particle volume fractions on the left and right edges, while a thin particle strip exists in the center above the magnet. We hypothesize that this is driven by a flow generated through viscous streaming, induced by the presence of the magnetic bead in the oscillating environment48,49,50. Kleischmann et al.41 have shown that such a streaming mechanism can lead to particle aggregation. Therefore, it can be expected that the viscous flow is present not only around the large magnetic bead, but also around the clay particles far away from it. Since the focus of this study is not the impact of the magnetic bead on the flocculation, we decided to crop the images so that this effect does not play a role in the analysis we present in the following. Therefore, we restrict our analysis to a region of each cuvette image that begins approximately 1 cm away from the stirrer. According to classical analyses of oscillatory flow51, fluid motion outside a viscous boundary layer of characteristic thickness \({({\nu }_{f}/{{\Omega }})}^{1/2}\) becomes irrotational. Beyond this layer, the velocity field induced by an oscillating body decays rapidly with distance, following a scaling \({(\lambda /{d}_{s})}^{-3}\)52, where λ denotes the distance from the stirrer and ds its characteristic diameter along the oscillation direction. This theoretical expectation aligns with the visual observations in Fig. 2, where the flow disturbances are confined to a region close to the stirrer. Furthermore, the areas close to the walls and the shaded area at the top of the images are excluded from the analysis.

Data processing was performed for cuvettes no. 2 and 7 (see in bold in Table 1). These two are the only configurations that satisfy the requirements of a sufficient black and white contrast, while the remaining cuvettes carried too much sediment and appeared largely opaque in the image analysis. Based on this, a quantitative evolution of the aggregate size over time is calculated for those two cuvettes, as presented in Fig. 3, where the black and gray circles represent cuvettes no. 2 and 7, respectively. The image conditions in the initial state of cuvette no. 7 do not allow for a reliable analysis, which is the reason why the results are only shown from day 4 onward.

Fig. 3: Experimental aggregate growth of cuvettes no. 2 and 7 in the ISS-experiments.
figure 3

The dashed line represents the scaling t1/2 of (2). For comparison purposes, the dotted line denotes the scaling t1/3 resulting from Brownian motion.

Both configurations reveal a similar process of aggregate growth that can be divided into an initial phase, steady growth, and a saturation phase. The transition from the initial phase to the steady growth phase occurs after approximately 7 days for no. 2 and after around 15 days for no. 7. To define the particle diameter used in the numerical simulations, we selected the transition point of cuvette no. 2 and applied the aggregate size observed at that time, yielding dp ≈ 115 μm. For both sets of conditions, the steady growth phase lasts until day 50, after which the aggregate growth slows down and saturates. The dashed line represents an empirical fit of the growth phase given by

$${d}_{a}(t)=\sqrt{\frac{2}{\pi }Dt+{{d}_{a,0}}^{2}}\ ,$$
(2)

with da the aggregate size and da,0 the initial aggregate size. Since the measured oscillations on board the ISS are isotropic (cf. Fig. 2 in §1 of SI), it is assumed that the diffusion process is isotropic as well. This yields the diffusion coefficient D as a scalar that is constant during the steady growth phase, resulting in a time scale of t1/2. Based on the least-squared method, we find D = 3.17 × 10−2 [μm2/s] and da,0 = 5.43 [μm] for the empirical fit whose derivation is provided in §4 of the SI. The dotted line represents the aggregate growth that can be expected from Brownian motion, for which a size-dependent diffusion coefficient is applied DB = kbT/(6πμ)53. Here, kB is the Boltzmann constant, T the temperature, and μ the dynamic viscosity. The size dependence of the diffusion yields a slowdown of the aggregate growth with increasing aggregate size that scales to t1/3. Clearly, our data do not follow the scaling due to Brownian motion, suggesting that D is independent of the aggregate size. This suggests that the diffusion of the particles is a hydrodynamic effect that may be caused by the g-jitter. This will be discussed in more detail below.

Numerical simulation

In this section, the numerical results of the reference setup Ref (cf. Table 2) are presented, before we proceed with the analysis of the setups with modified parameters in the next section. Note that for all sections of the numerical simulations, the results, equations, and quantities are presented in a dimensionless form according to (1). Therefore, we drop the tilde symbol for the sake of brevity.

The wealth of data provided by pr-DNS yields detailed recordings of the individual particle positions at each time step, which allows us to trace and analyze particle trajectories. To obtain the actual displacement ri,n of each particle n with respect to its initial position xi,n(0) in all coordinate directions i = (x, y, z), we subtract xi,n(0) and the instantaneous mean drift of all particles \({\bar{r}}_{i}\)41 from the actual position of the particle xi,n at a given time t:

$${r}_{i,n}(t)={x}_{i,n}(t)-{x}_{i,n}(0)-{\bar{r}}_{i}(t)$$
(3)

The total distances traveled by the particles throughout the entire simulation (t = 25,000) are presented in Fig. 4 for the xy-plane, where the concentric circles indicate the distances traveled. The illustration shows a more pronounced expansion of the particle displacements in the direction of oscillation, namely the x-direction, which is about twice as large as in the other directions. The displacements also reveal the randomness of the particle motion with each particle following a unique path. Illustrations of the displacements separated for each coordinate direction are shown in §5 of SI.

Fig. 4: Inertial random walk of all particles of the numerical reference setup Ref by illustrating ri,n in a xy-plane.
figure 4

The concentric circles serve as a measure of the distance traveled.

We compute the mean particle displacements by the mean square displacement 〈r2(t)〉54 to characterize the dynamics of the particles

$$\langle {r}^{2}(t)\rangle =\mathop{\sum }\limits_{i=1}^{3}\left[\frac{1}{N}\mathop{\sum }\limits_{n=1}^{N}{\left\vert {r}_{i,n}(t)\right\vert }^{2}\right]\,,$$
(4)

where N is the total number of particles. The resulting evolution of 〈r2(t)〉 over time is illustrated in Fig. 5. The figure shows an initial trend characterized by 〈r2(t)〉 t2 highlighted by the quadratic function (orange dotted line). This trend is generally classified as ballistic motion, where the particles tend to move without interacting with each other. As soon as particle-particle collisions occur, the trend transitions to a linear progression (〈r2(t)〉 t) which is defined as diffusive motion and illustrated by the linear function (blue dashed line)55,56,57. The transition from ballistic to diffusive motion becomes evident at t ≈ 7500.

Fig. 5: Mean square displacement 〈r2(t)〉 for the numerical simulation case Ref.
figure 5

The characteristic regimes of particle motion are indicated by the orange dotted line representing ballistic motion ( t2), and the blue dashed line corresponding to diffusive behavior ( t). The transition between these two regimes occurs at t ≈ 7500.

In addition to the quantitative and empirical analysis of the particle motion, we also qualitatively analyze the particle behavior. To this end, we visualize the volume fractions, which provide information on the distributions of the particles and allow the identification of structures of aggregated particles. Fig. 6 shows the volume fraction averaged in the z-direction in a 2D plane in the upper panel and the 1D volume fraction along the x-direction averaged in the y- and z-directions in the lower one. For the 2D planes, the volume fractions are indicated by the gray scale, ranging from 0 to 0.3, where Fig. 6a presents the initial arrangement and Fig. 6b the final state after 25, 000 oscillation periods. The profile of the 1D volume fraction fluctuates around the value ϕ = 0.084 in the initial arrangement, accompanied by an almost homogeneous particle arrangement in the 2D representation. In the final state, on the other hand, we observe the formation of distinct chain-like structures that form perpendicular to the oscillation direction. Elongated clusters of particles (2D), accompanied by local peaks in the 1D representation, are adjacent to less populated sections, visualized by local troughs.

Fig. 6: Volume fractions of the numerical simulation setup Ref in a two-dimensional xy − plane (upper) and in a one-dimensional representation along the x − axis (lower).
figure 6

a shows the initial setup at t = 0 and (b) the final arrangement at t = 25,000.

Next, we examine the aggregate growth generated by the unidirectional oscillations by applying a normalized autocorrelation function (C) to the 1D volume fraction.

$$C(r)=\frac{{\sum }_{i}({\phi }_{i}-\bar{\phi })({\phi }_{i+r}-\bar{\phi })}{{\sum }_{i}{({\phi }_{i}-\bar{\phi })}^{2}}$$
(5)

Here, r is the position shift (lag) along the x-axis, i is the position index, and \(\bar{\phi }\) the mean of the 1D volume fraction. Applying (5) yields an autocorrelation ranging between − 1 and 1. Starting from C(0) = 1, the first local trough of the graph determines the characteristic length scale (da), which describes the size of an aggregate. More details and a graphical representation of C can be found in §2 of the SI.

The aggregate size da is evaluated for every 500th oscillation period and is presented in Fig. 7 by the black circles. The empirical fit (2) is presented by the dashed line, representing the expected growth rate that scales by t1/2. Its applicability is substantiated in the next section through a detailed discussion of the different variants. Here, da,0 is calibrated to achieve a successful agreement between the empirical fit and the numerical results of ref. We apply (4) to compute the trace of the main diagonal of the diffusion tensor to obtain the diffusion coefficient D given by53

$$\langle {r}^{2}(t)\rangle =2Dt\ .$$
(6)

In order to transfer the isotropic conditions of the experiments to the numerical simulations, we assume that the contributions of Dy and Dz would be equivalent to Dx in a 3D oscillation. Therefore, we simplify as follows:

$${D}^{\prime} ={D}_{x}+{D}_{y}+{D}_{z}\approx 3{D}_{x}\ .$$
(7)

Applying this assumption, we denote the numerical diffusion coefficient by \({D^{\prime}}\) to clarify the distinction from the resulting diffusion coefficient of the experiments.

Fig. 7: Aggregate size of the numerical reference setup Ref over time.
figure 7

The black circles represent the numerical results and the dashed line the empirical fit (2).

The trend of numerical aggregate growth presented in Fig. 7 can be divided into different growth phases, similar to the results of the ISS experiments. Starting with an initial phase, where aggregates begin to form rapidly, the growth rate progresses to a phase of constant growth.

Numerical variants

The numerical variants provide an opportunity to investigate the impact of the modifications of ϵ and ϕ on the aggregation mechanism. In this regard, the same analysis methods that generated the results of Ref were applied. In detail, we focus on the comparison of 〈r2(t)〉 and the growth rates of the aggregates together with the respective diffusion coefficients in this section.

Figure 8 shows 〈r2(t)〉 over time, where Ref is illustrated by the solid line (cf. Fig. 5), the cases with modified amplitude ratios LoAmp and HiAmp are shown as the dashed lines, and the cases with modified volume fractions LoPhi and HiPhi are represented by the dotted lines. The accompanying diffusion coefficients are calculated based on (6) and (7) and are presented in Table 3. The trend of the modified volume fractions is similar to Ref with almost the same progression of LoPhi and a flatter curve of HiPhi, where the slope of this curve is approximately half of those of Ref and LoPhi. This is reflected in the results of \({D^{\prime}}\), where the outcome of LoPhi (\({D^{\prime}} =10.72\cdot 1{0}^{-5}\)) is similar to Ref (\({D}^{\prime} =10.84\cdot 1{0}^{-5}\)), while HiPhi (\({D}^{\prime} =5.32\cdot 1{0}^{-5}\)) is almost half. In contrast, the modified amplitude ratios show clear differences compared to Ref. HiAmp shows a significantly higher increase at the beginning of the simulations, which is reflected in a higher value of \({D}^{\prime} =45.33\cdot 1{0}^{-5}\). After around 12, 500 oscillations, 〈r2(t)〉 starts to stagnate and converges to approximately 〈r2(t)〉 = 6.75. On the other hand, LoAmp shows a lower slope and is significantly below Ref with a smaller diffusion coefficient (\({D}^{\prime} =2.06\cdot 1{0}^{-5}\)).

Fig. 8: Comparison of the mean square displacements 〈r2(t)〉 of the numerical variants over time.
figure 8

The subfigures illustrate the 2D volume fractions ϕ of the respective setups in black and white according to the scale on the right. The left panel presents the initial setups, where Ref, LoAmp and HiAmp have the same configuration, and the right panel depicts the end of the simulations.

Table 3 Diffusion coefficients of the numerical variants based on the assumption in (7) in the scale of 10−5

Of particular importance here is the ratio of \({D}^{\prime}\) between each variant and Ref (\({D^{\prime} }_{Ref}\)). Figure 9 presents the ratios of the diffusion coefficients \(D^{\prime} /{D^{\prime} }_{Ref}\) for the different variants. These ratios are plotted against χ/χRef, which represents the ratio of the variable parameter to Ref (ϕ/ϕRef or ϵ/ϵRef), depending on the variant. The presentation of Ref is for the purpose of completeness unity. The result of LoPhi is also approximately 1, while the ratio of HiPhi is close to 0.5. The diffusion coefficient of LoAmp is almost five times smaller than Ref, yielding a ratio of 0.19. In contrast, HiAmp is more than four times larger with a ratio of 4.18.

Fig. 9
figure 9

Representation of \({D}^{\prime} /{D^{\prime} }_{Ref}\) against χ/χRef, where χ denotes the parameter of the respective numerical variant, resulting in ϕ/ϕRef or ϵ/ϵRef.

The mean square displacements of the particle motion (Fig. 8) show a similar behavior for all numerical variants despite obvious differences in the magnitudes of 〈r2(t)〉 and the results of \({D}^{\prime}\). Each trend starts with an initial ballistic phase (〈r2(t)〉 t2) before transitioning to a linear diffusive phase (〈r2(t)〉 t). In the case of HiAmp, this linear progression ends even during the course of the simulation and turns into stagnation. The other variants, which are Ref, LoAmp, LoPhi, and HiPhi, are still in the diffusive phase at the end of the simulations.

The subfigures of Fig. 8 illustrate the 2D volume fractions with the initial configurations on the left and the results after 25, 000 oscillations on the right. The tags indicate the affiliation of the configurations with the respective setup, where Ref, LoAmp, and HiAmp have the same initial particle arrangement. The resulting configurations are ordered according to the results of 〈r2(t)〉 and the gray scale is represented by the black and white scheme on the right. Note that the illustrations of Ref correspond to Fig. 6, but are shown again for comparison purposes. The resulting volume fractions of the variants highlight the impacts of the modified parameters. Fully developed chain structures are only present in HiAmp, where distinct gaps without particles are between the stripes. The setups of Ref and HiPhi show the first formations of chains, in which, however, many particles are still not assigned to any chain and are therefore located in the intermediate spaces. No obvious changes in the final particle arrangement are apparent for LoAmp and LoPhi compared to their initial condition.

Based on the 1D volume fractions shown for all variants in §6 of SI, da is calculated by applying (5). However, since recognizable structures are required for this analysis, only the setups Ref, HiAmp, and HiPhi are considered. The aggregate sizes over time, together with the respective empirical fits, are shown in Fig. 10. The results of Ref are the same as in Fig. 7 but are presented again for the sake of comparison. The results of the variants presented are tagged by the respective ID, where the aggregate sizes are given by the symbols, and the empirical fits are illustrated by the lines. For the latter, the diffusion coefficients of Table 3 are applied to (2) and calibrations are performed for da of the respective variants. The development of the aggregate size of HiPhi shows the same characteristics as in Ref, with an initial phase of rapid aggregate growth and a subsequent progression that shows a linear trend despite slight fluctuations. The aggregate growth of HiAmp represents three phases that have already been identified for the trend of 〈r2(t)〉 in Fig. 8. The process of aggregate growth starts with a short period of rapid increase, followed by a growth phase consistent with the associated empirical fit, before it decreases and reaches the saturation phase.

Discussion

The investigation of cohesive sediments immersed in salt water and subjected to g-jitter in microgravity shows that particle aggregation can occur solely due to the effect of oscillations. The design of the experiments on board the ISS enabled the exclusion of the aggregation mechanisms of shear flow and differential settling that are otherwise prevalent on Earth. Shear flow was eliminated by utilizing closed cuvettes and differential settling as a result of the microgravity environment, where particles and aggregates do not settle. The same conditions were imposed in the idealized numerical simulations, in which the monochromatic unidirectional oscillations constitute the sole source of particle aggregation. The evaluation of aggregate growth in both physical experiments and numerical simulations reveal a growth rate that scales with t1/2 (cf. Figs. 3, 7, and 10). The application of the empirical fit (2) showed that the diffusion coefficients D and \({D}^{\prime}\), respectively, were constant in both settings after an initial ballistic phase. This shows that the impact of oscillations exceeds the potential effect of Brownian motion in the ISS-experiments that would have been characterized by a growth rate that scales with t1/3 and a diffusion coefficient that varies over time depending on the actual size of the aggregates53. In this regard, it can be concluded that in addition to differential settling and liquid shear, Brownian motion is also not of significance for the aggregation process in the investigations presented.

In order to understand aggregation through oscillations, we first need to examine its effect on each individual particle. Therefore, we analyzed detailed recordings of the particle trajectories from the numerical simulations (cf. Fig. 4). The data showed that the impact of oscillations leads to a unique pattern of motion of each particle, known as an inertial random walk27. The randomness of their trajectories arises from the presence of neighboring particles, where the inertia of each individual particle causes its trajectory to deviate from the fluid flow, altering the surrounding flow field and affecting the behavior of adjacent particles32. In a dense system, the flow fields generated by the particles interact with each other, causing each particle to experience a unique flow condition and to promote collisions that might lead to aggregation. As soon as particles collide, they remain together due to cohesion and form larger aggregates. As aggregates grow in size, their inertia increases, causing greater deviations from the fluid flow, resulting in even larger flow structures around the respective aggregate. This expands the radius of influence on neighboring particles, increasing the likelihood of collisions and promoting further growth.

The development of aggregate growth can be divided into three phases: an initial phase, steady growth, and a saturation phase. This categorization is identical in the experimental and numerical results, despite differences within the individual phases. For example, the tendency for aggregate growth differs between the experimental and numerical results in the initial phase. In the experiments, the particle dynamics in the initial phase is slower than in the steady growth phase, where we obtain the proportionality to t1/2. It can be assumed that the particles are more dispersed at the beginning of the experiment, i.e., after homogenization of the suspension, and therefore the particle collisions that are essential for aggregate growth do not occur as frequently. In contrast, the numerical results show the opposite behavior, in which the initial aggregation is characterized by rapid growth before it takes on a linear progression of the steady growth phase. This behavior can be attributed to the idealized nature of the unidirectional oscillations imposed in the numerical simulations, which induce a pronounced particle displacement along the direction of oscillation, as illustrated by the trajectories in Fig. 4.

As soon as aggregates are formed, two aspects become relevant that could be responsible for the reduction of the ongoing aggregation process. First, particle clusters might experience reduced accelerations due to their increased size that slow down the collision frequency. Second, the aggregates tend to align perpendicular to the oscillation direction, reducing their exposure to incoming particles and thus the probability of further collisions. The latter was shown by visualization of the particle volume fractions of the numerical simulations in Figs. 6 and 8, where the chain formations were already visible or even fully developed at the end of the simulation time. This phenomenon arises from the use of unidirectional oscillations, a mechanism previously examined in both experimental and numerical studies58,59,60,61. While not directly transferable to the experimental conditions on board the ISS, it provides a crucial basis for interpreting the observed particle dynamics and aggregate formation of the numerical simulations. As soon as particles belong to one chain, they move together and do not exchange with neighboring structures. In case of HiAmp, this causes the convergence of 〈r2(t)〉 to a constant value after t/Tf = 12, 500 (Fig. 8). After the chains have formed, the particles align themselves in such a way that the particles of a chain are as close to a line as possible. This in turn is recognized as a decrease in aggregate size after previous growth for HiAmp (Fig. 10), when determining aggregate size by applying the autocorrelation function (5) to the one-dimensional volume fractions. In the numerical setups Ref and HiPhi, the chain structures are only slightly recognizable if at all, and many particles are still widely dispersed. Therefore, 〈r2(t)〉 and da are still increasing and have not yet converged to a constant value.

Fig. 10
figure 10

Comparisons of the aggregate growths with the respective empirical fits for the numerical setups Ref, HiAmp, and HiPhi.

An examination of the two modified parameters ϕ and ϵ reveals that both have an impact on the particle kinematics in the numerical simulations. The frequency of particle collisions depends on the particle volume fraction ϕ, where an increase in ϕ tends to enhance, and a decrease tends to reduce, the probability of collisions. This is consistent with 〈r2(t)〉 of HiPhi, the configuration with a doubled volume fraction, where the displacement of the particles decreases due to the increase in the number of particles (cf. Fig. 8). This in turn results in slower aggregate growth (Fig. 10). The setup LoPhi with halved ϕ leads to a trend of 〈r2(t)〉 similar to the reference setup (Ref), although it would have been expected that the displacement would be greater due to a reduced number of particles. The available data do not provide conclusions about this behavior, but a hypothesis could be that the distances between the particles are of a size at which the existing flow conditions cause only minor interactions between the particles. In fact, our preliminary study41 confirms that there is an exponential decay of particle interaction due to viscous streaming induced by high-frequency oscillations. This could also explain the fact that almost no aggregates form within the simulation time for LoPhi, which is evident from the very similar initial and final configurations of the 2D volume fractions (cf. subfigures of Fig. 8). These findings suggest that there could be an optimal volume fraction for aggregate growth. Our results indicate that this critical volume fraction could possibly be close to the value of ϕRef.

The second parameter is the amplitude ratio ϵ = A/dp, in which A is decisive for the excursion of the oscillation and consequently for the motion of the particles. The probability of particle-particle interactions varies with the particle excursion, as the spatial extent of the surrounding flow field increases with the distance of the excursion. The results of the halved and doubled amplitude ratios, LoAmp and HiAmp, reflect this behavior. LoAmp has a significantly reduced 〈r2(t)〉 compared to Ref, while HiAmp shows a much more pronounced displacement of the particles (Fig. 8). The smaller particle displacements of LoAmp lead to fewer particle-particle interactions, which reduces the probability of aggregate formation. Similarly to LoPhi, this does not lead to apparent changes in the 2D volume fractions that are presented in the subfigures of Fig. 8. The increased amplitude of HiAmp results in significantly more pronounced and faster aggregate formation (Figs. 8 and 10). This reveals that the amplitude has a considerable influence on the behavior of the particles and may enhance aggregate formation. However, it is important to consider that aggregates can also break apart when hydrodynamic forces exceed cohesive binding forces62,63.

We can conclude that oscillations have a significant effect on particles immersed in a fluid and that they are promising in accelerating and controlling the aggregation of suspensions. The investigated parameters of the volume fraction and the oscillation amplitude demonstrate that several factors have an effect on the aggregation process. Therefore, there is the potential to perform precise analyses in future studies, on the basis of which the optimum conditions for aggregate formation could be derived. Such conditions would significantly improve this method, making it suitable for a wide range of applications.