Abstract
In this paper, porous sintered glass bead packings are studied, using Xray Computed Tomography (XRCT) images at \(16\,\upmu \hbox {m}\) voxel resolution, to obtain not only the porosity field, but also other properties like particle sizes, pore throats and the permeability. The influence of the sintering procedure and the original particle size distributions on the microstructure, and thus on the hydraulic properties, is analyzed in detail. The XRCT data are visualized and studied by advanced image filtering and analysis algorithms on to the extracted subsystems (cubes of different sizes) to determine the correlations between the microstructure and the measured macroscopic hydraulic parameters. Since accurate permeability measurements are not simple, special focus lies on the experimental set up and procedure, for which a new innovative multipurpose cell based on a modular concept is presented. Furthermore, segmented voxelbased images (defining the microstructure) are used for 3D (threedimensional) lattice Boltzmann simulations to directly compute some of the properties in the creeping flow regime. A very good agreement between experimental and numerical porosity and permeability could be achieved, in most cases, validating the numerical model and results. Porosity and permeability gradients along the sample height could be related to gravity acting during sintering. Furthermore, porosity increases in the outer zones of the samples due to the different contact geometry between the beads and the confining cylinder wall during sintering (which is replaced by a membrane during permeability testing to close these pores at the surface of the sample). The influence of different filters on the gray scale distributions and the impact of the segmentation procedure on porosity and permeability is systematically studied. The complex relationships and dependencies between numerically determined permeabilities and hydraulic influence parameters are investigated carefully. In accordance to the wellknown Kozeny–Carman model, a similar trend for local permeability values in dependence on porosity and particle diameter is obtained. Other than statistical models, which estimate the pore throat distribution on the basis of the particle size distribution, in this study XRCT scans are used to determine the pore throats in sintered granular systems, which are finally linked to the intrinsic permeability through the lattice Boltzmann simulations. From the \(\mu \)XRCT analysis two distinct peaks in pore throat distributions could be identified, which can be clearly assigned to typical pore throat areas occurring in polydisperse granular systems. Moreover, a linear dependency between average pore throat diameter and porosity as well as between permeability and pore throat diameter is reported. Furthermore, almost identical mean values for porosity and permeability are found from subsystem and fullsystem REV analysis. For sintered granular systems, the empirical constant in the classical Kozeny–Carman model is determined to be 131, while a value of 180 is expected for perfect monodisperse sphere packings.
Similar content being viewed by others
Avoid common mistakes on your manuscript.
1 Introduction
Numerical and experimental investigations of fluid flow in porous and granular media are of crucial importance in many research areas, such as the recovery of hydrocarbons from oil reservoirs [4, 5], ground water flow [6] or gas diffusion in fuel cells [7]. In spite of extensive scientific research, there are still many open questions namely which and how macroscopic transport factors other than porosity affect the fluid flow in a porous medium with a given microstructure [7,8,9,10,11]. An experimentally and numerically determinable parameter of porous materials is the intrinsic permeability which is highly sensitive to the underlying microstructure. The effective intrinsic permeability depends only on the pore structure of the medium, that is independent of the properties of the fluid. Therefore, a comparison with numerical determined permeability values based on MicroXRayComputerTomographic (\(\mu \)XRCT) images can increase the understanding of the effects of microstructure on the intrinsic permeability [12,13,14]. The typical workflow of \(\mu \)XRCTbased permeability investigations comprises

1.
the \(\mu \)XRCTscanning and reconstruction of the porous material;

2.
the filtering and segmentation of the image data;

3.
the implementation of image data in numerical simulations;

4.
validation of numerical calculations with experimental data;

5.
finding new correlations between microstructure and macroscopic properties by combining the previous steps and insights.
The presented workflow clearly demonstrates that a numerical simulation based on real data sets and the correlation between microscopic and macroscopic properties can be only be as good as the preceding filtering and segmentation procedure [15,16,17,18,19]. Therefore, a special focus lies on this topic. Possible ways are presented how to filter, segment and finally extract essential features of a porous material, which determine the intrinsic permeability.
In this work we investigate, both experimentally and numerically, the intrinsic permeability of artificial produced samples composed of sintered glass beads showing different particle diameters, porosities and degree of polydispersity. In contrast to common rock samples, like e.g. dolomite, sintered glass bead samples are characterized by their chemical stability and inertness, in addition to their relatively simple pore structure. Nevertheless, the pore structure, and thus the intrinsic hydraulic permeability can be influenced by the selection of certain glass beads and special sintering treatments. Another crucial advantage of sintered glass bead samples, in contrast to most rock samples, is the improved grayscale contrast between the pore space and the solid phase, which considerably simplifies the image segmentation process and thus ensures a better comparability of experimentally and numerically determined permeability values. The filtering and segmentation procedure of sintered glass bead packings is further simplified by single phase composition of the solid matrix. In this respect, sintered glass bead samples can serve as replacement material for soil and rock specimen to provide a benchmark in permeability calculations.
The present paper focuses on the hydraulic properties of porous sintered glass bead systems. The influence of the sintering process on the microstructure, and thus on the permeability of the sintered samples are analyzed in detail by using appropriate XRCT data analysis and visualization methods (AVIZO Fire 8.0.1 and 9.0). In Sect. 2 the wellknown Darcy’s law is introduced to define the intrinsic permeability of porous materials in general. Furthermore, the semiempirical Kozeny–Carman equation, which is often used to determine the intrinsic permeability of granular systems, is presented and discussed in terms of microstructural parameters. In Sect. 3 the Lattice Boltzmann (LB) method and the numerical setup, which is used to determine the local intrinsic permeabilities of the extracted data sets, is described briefly. For a better understanding of the underlying microstructure, the sintering procedure is described in Sect. 4.1. For validation of numerical data based on discretized \(\mu \)XRCT/voxel data sets of the produced sintered glass bead samples, the experimental setup and procedure of permeability measurements are described in Sect. 4.2. The developed multipurpose measuring cell is proposed in Sect. 4.3. Section 5 focuses on the elaborate processing of \(\mu \)XRCT scans, whereby possible ways are introduced, how to filter, segment and extract essential features, which highly influences the hydraulic properties of porous sintered granular systems. Section 6 starts with presentations and discussion of results obtained from numerical and experimental porosity and permeability measurements. In addition, the results from REV analysis for porosity and permeability and the peripheral porosity development of the samples are depicted and discussed in Sect. 6.1. Moreover, the numerically determined local permeability values are qualitatively and quantitatively compared with the theoretical predictions according to the Kozeny–Carman model. The results for pore throats and their dependency on the porosity and intrinsic permeability is presented and discussed in Sect. 6.2. The study of hydraulic properties of porous sintered granular packings is concluded inSect. 7.
2 Theory
Darcy’s law is the most commonly used empirical relationship for calculation of the pressure drop across a homogeneous, isotropic and nondeformable porous medium [20, 21]. It states that, at the macroscopic level and in the creeping flow regime, the measured pressure drop \(\varDelta p/l\) per length applied to a porous medium, and the fluid flux per area \(Q_{z}/A\) have a linear relationship given by
where \(\mu ^{fR}, A\) and l are dynamic viscosity of the fluid, crosssectional area and length of the sample [22]. The proportionality constant \(k_{z}^{s}\) describes the intrinsic permeability of the porous medium in flow direction z, which strongly depends on the porosity and the microstructure (e.g. particle shape, tortuosity and connectivity of pore channels). The term \(\rho ^{fR}\,g\) represents the gravity forcedensity, driving the fluid flow. The expression given in brackets is often referred to as the hydraulic gradient i.
The semiempirical approach of Kozeny–Carman is one of the most wellknown theories, which relates macroscopic parameters, like the intrinsic permeability, to microstructural parameters, like particle arrangement, shape and orientation or tortuosity (flow path) [20, 23,24,25]. For granular media, the Kozeny–Carman permeability reads
where \(S_v\) and \(\alpha \) are the volumebased specific surface area and tortuosity of the fluid path. The porosity of the sample is denoted as \(\phi \). For monodisperse granular media consisting of particles with diameter \(d_p\) the intrinsic permeability is given by
Since in most investigated cases the granular medium consists of nonuniform spheres, Carrier [26] have introduced an effective diameter \(d_r\) which can be reliably determined on basis of the particle size distribution in accordance with
where \(f_{i}\) is the fraction of particles between two sieve sizes and \(\bar{d}_{i}\) corresponds to the geometrical average particle size between the minimum and maximum sieve size (\(d_{min,i}, d_{max,i}\))
For monodisperse granular media the median diameter \(d_{50}\) is commonly used as effective diameter due to the little variation in grain size. The median diameter is the value of the particle diameter at 50% in the cumulative distribution. In the case of a nearly symmetric particle size distribution, the median diameter is often replaced by the arithmetic mean value.
Several approaches have been introduced in recent years to describe the tortuosity (fluid path) in Eq. (2) through porous media [11, 23, 24, 27].
3 The lattice Boltzmann method
For the determination of the numerical intrinsic permeabilities of the extracted differently sized subsets of glass beads the lattice Boltzmann method is used. We follow the procedure to measure permeabilities as described in Narváez et al. [28, 29], Frijters [30] and Frijters and Harting [31]. The LB method itself has proven to be very successful for modeling fluid flow in porous media [32]. It enables a straightforward implementation of complex boundary conditions and is suitable for use in parallel computation due to the high degree of locality of the algorithm. For the LB simulations the Boltzmann equation
in discretized form is solved to simulate creeping fluid flow through porous media. Equation (6) describes the evolution of a singleparticle probability density \(f(\mathbf x ,\mathbf c ,t)\), whereby \(\mathbf x \in \mathbb {R}^3\) is the position vector, \(\mathbf c \in \mathbb {R}^3\) is the velocity vector, t\(\in \mathbb {R}\) is the time and \(\varOmega (f(\mathbf x ,\mathbf c ,t))\) is the collision operator describing binary collisions between particles. The time discretization is performed by using a time step \(\varDelta t\), whereas for the lattice velocities a finite set of vectors \(\mathbf c _i\) with \(i=1 \ldots 19\) lattice points is applied. The position vector \(\mathbf x \) is discretized by using a threedimensional structured cubic lattice with a lattice constant \(\varDelta x\). For the permeability calculations the simulation parameters are chosen in accordance to Narvaez et al. [29], Frijters [30] and Frijters and Harting [31]. As in those publications the wellknown D3Q19 lattice for velocities, providing adequate accuracy at moderate computational cost is applied [33]. For the collision matrix \(\varOmega \) in Eq. (6) a standard two relaxation time (TRT) model is used, cf. Refs. [29, 34]. Narváez et al. [28, 29] have shown that relaxation times of \(\tau =1\) and \(\tau _{bulk}=0.84\) provide useful results for permeability calculations.
The porous sample is positioned between two fluid chambers which serve as in and output to avoid artifacts, cf. Fig. 4a. The onsite boundary condition introduced by Zou and He [35] and later extended to three dimensions and nineteen velocities (D3Q19) by Hecht and Harting [36] is applied to generate a gradient in flow direction (zdirection) by defining the fluid densities at the in and outlet of the system,
whereby \(n_{z}\) indicates the total number of lattice nodes in flow direction and \(\varDelta \rho ^{fR}\) the difference of the fluid density between in and outlet. To ensure creeping flow with low Reynolds numbers the density difference is chosen in the order of 10\(^{4}\) in lattice units. Furthermore, the computational domain is surrounded by walls in x and ydirections to prevent flow over boundaries orthogonal to the pressure gradient. The pressure gradient in flow direction z reads then as
The intrinsic permeability \(k^{s}_{z}\) in flow direction z can be expressed in terms of the lattice Boltzmann relaxation time as
whereby \(A=n_{z} \,n_{y}\) represents the crosssectional area of the extracted subset, \(n_{z}\) the sample length and \(Q_{z}\) the volume flux in zdirection. The system has reached steady state when the mass flux and the permeability are constant over the geometry [29, 30]. For the determination of the permeability of the differently sized samples in flow direction z the permeabilities are averaged over the lattice surfaces in flow direction z.
4 Experiments
4.1 Sintering
In this study various types of glass with different chemical compositions and characteristic particle diameters were used for sintering, see Table 1. The characteristic diameters in Table 1 are obtained from laser granulometry measurements (Mastersizer 2000, Malvern Instruments Ltd.) before the glass beads were sintered. The glass beads were supplied from Muehlmeier GmbH & Co. KG, Germany.
Depending on the composition, the deformation temperature of the used glass particles varied between 575 and \(680~^\circ \hbox {C}\). The used glass beads showed different particle sizes and degree of polydispersity, cf. Table 1. The specific density of the sintered glass beads was at \(2.5~\hbox {g/cm}^3\).
It was attempted to generate cylindrical samples and at the same time to ensure the smallest possible deformation of the beads during the sintering process, see also Ref. [39]. The produced cylindrical samples had bulk diameters of 30 and 50 mm, and the lengths of the specimens were 50 mm. Figure 1a shows the experimental sintering setup for the glass beads.
The sintering of the glass beads were performed in a tubular furnace with heat power of 0.7 kW and a nominal target temperature of \(1000~^\circ \hbox {C}\) under atmospheric conditions. The induction furnace was equipped with three programmable temperature controllers (type West 5010) regulating the inner temperature at three different furnace zones. The temperature progression within the furnace was monitored continually at five different places during the sintering process using thermocouples (type K), see Fig. 1a. The measured temperature curves are depicted in Fig. 1b. The glass beads were filled in a quartz glass cylinder (with inner diameters of approximately 30 and 50 mm) and completely enclosed with graphite paper. The melting temperature of the quartz glass cylinder is around \(1713~^\circ \hbox {C}\) and thus certainly higher than the deformation temperature of the glass beads (\({\approx } 690~^\circ \hbox {C}\)). The graphite paper prevented an adhesion or sticking between the beads and the cylinder. The glass beads were manually shaken prior to sintering to reach the closest glass bead packing. The samples were subsequently loaded from the top with different masses ranging between 100 and 300 g corresponding to pressures of 1.39 and \(4.16~\hbox {kN/m}^2\) for samples with 30 mm diameter or 0.50 and \(1.50~\hbox {kN/m}^2\) for samples with 50 mm diameter, respectively. As can be seen in Fig. 1b the glass beads were heated up with a constant temperature rate of \(300~^\circ \hbox {C}\) per hour until the required sintering temperature of \(695~^\circ \hbox {C}\) was reached. Holding the beads at this temperature for approximately 2.5 h, the specimen was finally cooled down in an uncontrolled manner by switching off the furnace, cf. temperature curve at position 3 in Fig. 1b. Since the prepared samples were placed centrally in the furnace, only the temperature curve at position 3 is of major relevance. The preprogrammed target temperature of \(695~^\circ \hbox {C}\) in the outer zones (position 1 and 5) was not reached due to large heat losses at the top and bottom of the furnace whereas the target temperature at positions 2 and 4 was reached, but delayed by approximately 1–2 h.
Depending on the chemical composition, bead diameter, dead loads of the used masses and sintering duration, the initial heights of the untreated specimens shrank by 1–5 mm. After sintering the samples were cut by a diamond disc to the desired length of 50 mm.
4.2 Permeability measurement setup
Technical requirements on precise hydraulic measurements are very high [40,41,42]. Therefore, an elaborate setup was built for the stationary permeability measurements, to guarantee proper comparability between numerical and experimental permeabilities, see Fig. 2a.
To minimize the content of air bubbles and to guarantee for reproducible experimental results, use was made of filtered and deaired water. For this purpose, the water was mechanically filtered in various filter stages until reaching a degassing tank, where the filtered water was deaired.
The measuring cell including the hose connections were rinsed with carbon dioxide before the cell was flooded with filtered and deaired water. The carbon dioxide easily dissolves in water. In this way, the content of air bubbles in the cell was minimized and an optimal water saturation of the sample was achieved.
The stationary permeability experiments were performed by controlling the volumetrical flux through the pressure regulator of the degassing tank. During the permeability measurements, the volume flux was stepwise increased by increasing the inertial pressure of the degassing tank through a pressure regulator, cf. Fig. 3a. The pressure regulator ensured that the atmospheric pressure in the degassing tank remained constant. In this manner, different measuring ranges for fluid flux and pressure difference were driven to determine the intrinsic permeability of the produced sintered specimens, see Fig. 3. The measured values for pressure difference and fluid flux were continuously recorded (digital data acquisition, sampling rate 0.5 Hz) during each measurement and subsequently sent to a computer. Depending on the porosity and glass bead diameter of the sintered specimens, different fluid fluxes ranging between 30 and 245 ml/min. were observed. With these volume flows pressure differences up to 35 mbar could be generated. For each measurement the water temperature was measured and found to be in the narrow range of \(20~^\circ \hbox {C}<\hbox {T}<22^\circ \).
4.3 Measuring cell
The developed measuring cell has been designed according to a modular concept in order to use it in various applications. Figure 2b shows an illustration of the measuring cell in operating mode for stationary permeability measurements.
It consists of an inner and outer cylinder. The inner cylinder is made of an acrylic glass (PMMA) and produced in various sizes, whereas the outer cylinder is made of aluminium (AlCu4PbMgMn alloy) to stabilize the measuring cell. As can be seen from Fig. 2b, the sintered sample was positioned at the center of the cell and pneumatically fixed by a specially developed specimen holder coated with a 1mmthick latex membrane. During flow measurements a static air pressure on the latex membrane was applied which fixed the specimen in the current position and prevented a surrounding fluid flow. At the same time, the latex membrane ensured a hermetically sealing off the measuring cell to the outside. The pressure difference, mainly resulting from the viscous friction of the fluid passing through the porous sintered sample, could be taken via the upper and lower pressure port and measured by a highprecision differential pressure transducer (type FDW2JA, ALTHEN, Germany) capturing differential pressures up to 35 mbar (with an accuracy of 0.25%).
5 \(\mu \)XRCT data processing
\(\mu \)XRCT data processing is a crucial step towards understanding of fluid flow through complex morphologies like sintered glass beads. It is a important tool for visualization and quantification of parameters, such as porosity, particle sizes or pore throats, determining the hydraulic conductivity of a porous medium [43,44,45]. The correct procedure of the \(\mu \)XRCTdata including an adequate filtering and thresholding method is essential for a proper comparison between experimental and numerical determined permeabilities [17, 46].
The XRCT device used for imaging of the sintered samples is a ‘nanotom 180’ device provided by the petrophysics laboratory at the Leibniz Institute for Applied Geophysics in Hannover, Germany. The device is equipped with a special watercooled nanofocus Xray tube with a maximum 180 kV and 15 W. The minimal focus size is about \(0.6~\upmu \hbox {m}\), which results in a detail detectability of \(0.2~\upmu \hbox {m}\) [13]. The measurement parameters for the investigated scans are 107 kV and \(200~\upmu \)A. XRCT images at 900 angles on \(360^\circ \) are performed with an integration time of \(10 \times 0.1\) s per angle. The initial voxel resolution of the XRCT scans is \(16~\upmu \hbox {m}\) and remained constant during the whole \(\mu \)XRCT data processing.
Figure 4b shows the main image processing steps. Starting from raw data, the image file is filtered in several stages until the desired gray scale distribution is reached. For better visualization of the filter effect, Fig. 5 demonstrates exemplarily the filtering procedure on the basis of slices applied onto the original raw data with the corresponding grayscale value distribution. For the sake of clarity, during filtering the image is interpreted and processed as a three dimensional volume, and the grayvalues of each voxel are numbers of decimals obtained from 16bit binary representation of the gray level. In the initial state (state A), the grayscale distribution of the raw data show two peaks which can be clearly attributed to the pore space and the glass beads. Starting from the original raw data a simple logical operator with the socalled “arithmetic” module is applied to remove bright spots from the image file. These bright spots highlighted by a red circle in state A are caused by density fluctuations and chemical impurities of the beads and can be clearly assigned to greater grayscale values. In the first filtering step, the gray values belonging to these bright spots are lowered artificially by setting a defined maximum threshold for grayscale values. As highlighted in the example, a maximum threshold of 26,818 is used, cf. Fig. 5b.
Since the grayscale values belonging to the glass beads and pore space overlap due to their wide distributions, the segmentation procedure becomes difficult. Therefore, in the second step of the filtering procedure the socalled “delineate” filter is applied to enhance the edges of the glass beads and to adjust the contrast between the pore space and the glass beads. Local changes in intensity of grayscale values constitute a common issue during segmentation. The “delineate” filter, which is based on a phase contrast method, can detect sharp transitions between different phases to finally enhance and contrast the edge of an object to be segmented. As a result, the grayscale distributions between the glass beads and the pore space are clearly separated from each other (state C), which simplifies the further separation of the glass beads from the pore space.
In the last step, the “median” filter is applied to denoise and smooth the image data. This filter uses morphological operators to set the grayscale value of a voxel to the median for a defined neighborhood [47]. The grayscale value distribution from state C is changed only slightly compared to the distribution in state D. Because of the high data quality, which comprises also the high grayscale contrast between pore space and solid matrix, there is no need to use the socalled “nonlocal means” filter, which is commonly used to denoise image data especially at the edge of an object to be segmented [17, 48, 49]. The algorithm of this filter compares the neighborhood of a voxel in a given search window with neighbors of the current voxel. A weight is determined from the similarity between the neighbors, with which the values of the voxel value in the search window will influence the new value of the current voxel. The final weight result by applying a Gaussian kernel to the similarity values [48, 49].
In accordance with the process flow chart shown in Fig. 4b, the filtered grayscale image data is thresholded to generate a binary map. The threshold is selected manually for each sample in a way that the solid glass beads are assigned to values of unity and the pore space voxels are set to zero. For the determination of porosity and visualization of the pore space the binarized image data is inverted.
5.1 Particle number distribution
For the determination of the particle size distribution, the segmented glass beads are separated using a highlevel combination of watershed, distance transform and numerical reconstruction algorithms. After separation, the segmented beads are numerated with the “labeling” module. In this module, each voxel of the same object is assigned to the same value, and each object gets a different value. Based on the labeled system a quantitative analysis is performed to determine the volumeequivalent diameter of each particle object. The equivalent particle diameter \(d_p\) is computed by
where \(V_{p}\) is the voxelbased volume of the particle. As a result, Fig. 6 shows (from state A to C) the volume rendered sample in the form of a cuboid with the dimensions \(1024 \times 1024 \times 2048\) voxel\(^3\) (\(16.384 \times 16.384 \times 32.768\) mm\(^3\)) in the raw, and the segmented and labeled state. In the labeled state different colors are used to distinguish optically between the identified glass particles. It should be stated, that the coloring of the particles occurs randomly. After a certain number of beads the coloring is repeated and the same colors are assigned again to different identified objects. The initial cuboid shown in Fig. 6 contains more than 78,000 particles with diameters ranging mostly between 0.4 and 0.6 mm. The corresponding particle number distributions of the initial cuboid and different sized subsets taken from the initial cuboid are depicted in Fig. 6d. For all investigated subsets a monomodal distribution with maximum around 500 \(\upmu \hbox {m}\) occurs, which confirms the representativeness of the investigated subsets, except for the smallest one. The arithmetic mean values and the standard deviations of the particle number distributions shown in Fig. 6d are given in Table 2.
5.2 Pore throat determination
A decisive factor, which determines the intrinsic permeability in granular porous systems is the pore throat area. Micro tomographic imaging techniques enable to localize, visualize and quantify such determining areas.
Therefore, Fig. 7a illustrates exemplarily the main image processing steps for determination of pore throats using a 256 voxelsided cube showing glass bead diameters between 2.0 and 2.5 mm. As denoted in Fig. 7a for the determination of the pore throat areas of the subsets, the pore space was first computed by inverting the segmented glass beads. After inversion the segmented pore space is separated in various pore voids by using the tool of “binseparate”. This module computes the watershed lines of a binary image. In the separation process voxels with at least one common edge are considered as connected and the separation takes place at the narrowest places of the pore space. In the next step, the separated pore space is deducted from the unseparated pore space by using the “arithmetic” function, in order to determine the split planes, which also represent the pore throat areas. After labeling typical pore throat areas formed by three or four particles result, see Fig. 7b. From the computed pore throat areas an equivalent pore throat diameter
is determined, whereby \(A_{pt}\) represents the pore throat area. The pore throat distribution in granular packings was also theoretically investigated by To et al. [50], Jaafar and Likos [3], Reboul et al. [1] and Shire et al. [51], where the pore throat distribution is estimated from the given particle size distribution of the granular packing. To et al. [50] and Reboul et al. [1] considered the flow process of suspensions in porous granular packings and therefore the pore throat areas were described by circular voids, which were smaller than the real constrictions sizes.
In this study, the fluid flow of water in granular sintered packings were investigated, and thus the identified pore throat areas were replaced by circular voids with same area as shown in Fig. 7b. Even when the identified pore throat areas are not close to circular shape, the determination of the pore throat diameter according to Eq. (12) is sufficient to quantify the sizes of the pore throat areas and to investigated their dependency on the permeability or porosity of the investigated differently sized subsets.
6 Results and discussion
In this section the results of the determining parameters of the intrinsic permeability, described in previous sections, obtained from \(\mu \)XRCT analysis and LB simulations are presented successively, discussed and compared with experimental results. Moreover, the dependency of the intrinsic permeability on different parameters and on the localizations and sizes of the investigated subsets are analyzed qualitatively and quantitatively. Please note that the results are only extensively showed for the sintered sample with \(d_p=0.4{}0.6\) mm due to the large amount of data. All other samples were produced in the same way as the sample with \(d_p=0.4{}0.6\) mm and thus show qualitatively the same results.
6.1 Porosity and permeability
Figure 8a, b illustrates the numerical results of porosity and permeability values of extracted subsets with edge lengths of 256 voxel (4.096 mm) in each spatial direction obtained from \(\mu \)XRCT analysis of the sintered sample with bead diameters ranging between 0.4 and 0.6 mm. In total, \(4 \times 4 \times 8 = 128\) cubes with edge lengths of 256 voxel are extracted from the initial cuboid shown in Fig. 6a–c and investigated in terms of porosity and intrinsic permeability. After evaluating the porosity and permeability values of the extracted subsets, the cubes with edge lengths of 256 voxels are arranged in compliance with their spatial coordinates within the initial cuboid depicted in Fig. 6. For both, the porosity and permeability, a clear gradient with sample height can be observed. The permeability and porosity decrease with increasing depth due to the gravitational forces acting on the beads during sintering. The porosities vary only between 0.32 and 0.39, whereas the permeability fluctuations within the initial cuboid are considerably higher (\(1.29 \times 10^{10}{}2.75 \times 10^{10}\) m\(^2\)), see also Fig. 9 (ab, REV analysis). The porosity fluctuations are around the trend (porosity gradient in flow direction) so that even the relative change of approximately 18% for 256 voxelsided cubes is overexaggerated. In Fig. 10a, b the intrinsic permeability increases nonlinearly with increasing porosity, which confirms the higher relative variation in permeability and that it is compatible with the variation in porosity. In comparison, the effective porosity of the cylindrical specimen is experimentally determined from the bulk and bead densities by
whereby the \(\rho ^s\) and \(\rho ^{sR}\) represent the bulk density and the effective true density of the beads, which the sintered sample is composed of. The experimentally determined effective porosity value lies within the porosity range determined from the segmentation of 256 voxelsided cubes. The differences between experimentally determined porosities and voxelbased local porosities result especially from the spatial porosity gradient across sample height z and that the XRCT data do not capture pore spaces smaller than the resolution limit. Since the phasecontrast between the porous skeleton composed of sintered glass beads and pore space is high, the influence of the segmentation procedure on the voxelbased porosity is assessed to be negligibly small. The permeability values at the top of the initial cuboid are more than twice greater than the permeabilities in the lower regions of the initial cuboid. The higher permeability fluctuations are confirmed in the conventional REV analysis as shown in Fig. 9a, b. The illustrations in Fig. 9a, b show the REV analysis for porosity and permeability of differently sized subsets taken from the initial cuboid. Please note that the REV analysis is constrained to subsets, which were also analyzed in terms of the local permeabilities via LB method and further concerning different parameters, such as pore throat or particle size distributions. Due to the high computation effort of permeability calculations according to the LB method, we have renounced a larger spread of cuboid or cube sizes like in Ref. [52] and considered four different REV sizes. Due to the varying degrees of fluctuations of porosity and permeability, the relative standard deviations related to the arithmetic mean value seem to be a sensible quantity to investigate the effect of the size of REV edges. The percentage values in Fig. 9a, b show the relative standard deviations relative to the arithmetic mean values of the permeabilities being considerably higher than those of the porosities. For example, the standard deviation of porosity for cubes with edge length 256 voxel is only about 5%, while the standard deviation of permeability is significantly higher at 17.77%. This indicates that the permeability in general is more sensitive to the size of the representative volume element than the porosity. Furthermore, the findings from the REV analysis confirm that the mean values for porosity and permeability are (almost) identical to that of the initial cuboid with dimensions of \(1024 \times 1024 \times 2048\) voxel\(^3\) (\(16.384 \times 16.384 \times 32.768\) mm\(^3\)). A consequence of this result is that, either a few calculations of smaller sided cubes with low costs and computation time requirements can be performed or one cost intensive calculation on the initial cuboid with approximately 78,300 particles can be carried out.
Please note that the geometrical tortuosity determined from the centroids of twodimensional slices of 256 voxelsided cubes obtained from XRCT scans shows no spatial gradient along the sample height and no correlation is found with the porosity and permeability, cf. Ref. [53].
Figure 10a shows the permeabilities of the subsets as function of their porosities, for three different theoretical estimates, increasing according to Kozeny–Carman.^{Footnote 1} Figure 10b shows the intrinsic permeabilities normalized by the square of the mean particle diameter, confirming the nonlinearly increasing trend of the intrinsic permeability with increasing porosity. The colored data points in Fig. 10a represent the predictions according to the Kozeny–Carman model, cf. Eq. (3), whereby the arithmetic (red), harmonic (green) and effective (black) diameter according to Eq. (4) from the particle size distribution are used as representative values to predict the permeabilities of the differently sized subsets. The permeabilities determined from the lattice Boltzmann simulations (open data points) and the predictions according to Kozeny–Carman using the arithmetic mean diameter show a similar increasing trend, whereby the numerically determined permeabilities are higher by a factor of approximately 1.3. The permeability predictions according to Kozeny–Carman using the harmonic or effective diameter according to Eq. (4) (green and black data points) show stronger fluctuations and clearly underestimate the numerically determined permeabilities. Fitting the predicted permeability values depicted in red into numerical results by using the empirical constant \(c_1\) as fit parameter, yields a value of 131, see Fig. 10b. This constant contains and reflects the effect of the microstructure (particle shape, tortuosity) as a result of the sintering process on the intrinsic permeability of the glass bead samples.
It is worth noting that the most glass beads show sphericity values around 0.95 after sintering, cf. Ref. [53]. The sphericity values near 1 determined from XRCT scans indicate that the glass beads are almost spherical after the moderate sintering. This confirms also the applicability of the Kozeny–Carman equation, which is predominantly used to predict the intrinsic permeability of sphere packings.
Besides the porosity analysis on differently sized cubes extracted from different regions of the entire scanned region, subvolumes in the form of tubes with varying mean crosssection diameters were segmented to investigate the porosity distribution across the crosssection of the cylindrical sintered samples, cf. Fig. 11 (state b). To guarantee the investigation of meaningful representative volume elements, the pipe thickness is chosen as 3 mm, which is equivalent to 187.5 voxels.
Figure 11c shows the resulting porosity distribution in dependence on the mean pipe crosssection radius of the investigated specimens showing different glass bead diameters and degree of polydispersity. Starting from the center of the investigated samples, the porosities remain relatively constant up to a mean crosssection radii of 11.5 mm and then increase to higher porosities for the largest investigated pipes in the external area of the produced samples. In these outer zones a clear increase of the porosity values for investigated samples can be seen due to the different contact between beads and cylinder wall during the sintering procedure and the gaps remaining between particles and walls. The clear porosity increase on the edges of the sintered samples is a consequence of the sintering procedure caused mainly by the presence of the walls.
Figure 12 summarizes the experimental results from permeability measurements for a sintered sample with bulk diameter of 30 mm showing glass bead diameter between 0.4 and 0.6 mm. The measurements were repeated eight times in order to attain mean reliable results and understand the variation and reproducibility. The almost linear relationship between the filter velocity \(Q_{z}/A\), and the pressure drop \(\varDelta p/l\), depicted in Fig. 12a, and the nearly constant values of the effective intrinsic permeability \(k_{z}^s\) over the test duration t, shown in Fig. 12b, confirm the applicability of Darcy’s law (1) and that the permeability measurements have taken place in the laminar Darcy regime. The measurement of water flow and pressure difference is captured with a sample frequency of 0.5 Hz. For the sake of clarity, only each 150th measuring point is plotted in both figures. The intrinsic permeability of each measurement is determined from the slope of the linear regression lines, cf. Fig. 12a. Measurement uncertainties of the used flow meter and the differential pressure transducer as well as some presence of air bubbles causes the permeability differences between each experiment. Pressure fluctuations and thus permeability differences are additionally enhanced by buckling of the used water hoses. Please note that examined permeabilities for each measurement in Fig. 12 are still in the same order magnitude, which confirms the robustness and reliability of the permeability experiment. For the sintered sample with bead diameters ranging between 0.4 and 0.6 mm, a mean effective permeability of \(k_{z}^s= 9.87 \times 10^{11}\pm \varDelta 1.65 \times 10^{11}~\hbox {m}^2\) is determined.
The bar diagrams in Fig. 13 show a direct comparison between experimentally and numerically determined porosities and permeabilities of the investigated samples with different glass bead diameters and degrees of polydispersity. The numerical porosity and permeability results, represented by black bars, are obtained from 1024 voxelsided cubes taken from the center part of the entire scanned regions of the samples and used in LB simulations. The effective permeability results obtained from laboratory experiments, represented by white bars, are averaged values from 5 (or 8) independent permeability measurements, whereby 10 to 15 different measuring ranges for volume fluxes and pressure differences are run during each measurement, cf. Fig. 3. While the porosity values show a good agreement, the permeability results show much larger nonsystematic deviations. It should be noticed that small deviations in porosity and particle size can lead to significant deviations in permeabilities due their exponential influence, see Eq. (3). Larger deviations between experimental and numerical permeability results occur for 1.5–2.0 mm and larger particles, since the representativeness of the investigated subsets for numerical permeability calculation decreases with increasing particle diameter. Furthermore, it can be seen from Fig. 13b that the error bars in experimental permeability determinations are small compared to their averaged values, which indicates high reliability, repeatability and robustness of the used experimental permeability setup.
Moreover, the good agreement between voxelbased local and experimental determined global porosity values of the investigated different sintered samples in Fig. 13a proves the correctness of the filtering and segmentation procedure despite the underlying porosity gradient across the sample height. A proper filtering and segmentation procedure is surely essential for subsequent permeability simulations. Incorrect porosity determination during segmentation procedure can lead to substantial errors in permeability calculations, see Eq. (3). In this context sintered glass bead samples as simple replacement material for natural sandstones are suitable to set a benchmark for permeability calculations. Taking into account the porosity and permeability gradients with the sample height, the deviations between experimental and numerical results is insignificant. The maximum deviation factor of 2.4 that is obtained for glass bead diameters of 3.0 mm due to low representativity of the investigated subset is quite reasonable.
From the REV analysis, we have come to the important conclusion that the average value for porosity and permeability of smaller sided cubes is (almost) identical to results obtained from the initial cuboid, cf. Fig. 8. We have found out that the averaged values for permeability are almost equal independent from the size of the investigated subsets.
6.2 Pore throats
In addition to porosity and particle size, the intrinsic permeability in sintered glass samples is also affected by pore throats [11, 54]. The strong influence of pore throats in simple pore systems, consisting of cylinder pores, on the intrinsic permeability can be derived analytically, cf. Ref. [55]. Numerous statistical models for determination of pore throat distribution from particle size distributions of granular packings exist, cf. Refs. [2, 3, 50, 51]. However, the applied models are often inaccurate to determine the constriction size distribution. In addition, the direct link to the intrinsic permeability is missing. Furthermore, the influence of the sintering process remains unconsidered. In such cases, the \(\mu \)XRCT analysis provide an efficient tool for visualization and quantification of pore throat areas and to investigate their impact on the intrinsic permeability [56]. Therefore, this section presents a simple methodology for the determination of the pore throat areas from \(\mu \)XRCT data. Moreover, the correlations between the mean pore throat diameter \(\langle \hbox {d}_{pt} \rangle \), the porosity \(\phi \) and the numerical determined intrinsic permeabilities \(k^{s}_{z}\) are investigated in detail.
Figure 14a illustrates the local distribution of mean pore throat diameter from 256 voxelsided cubes within the cuboid for the sintered sample with bead diameters between 0.4 and 0.6 mm. The normalized pore throat distribution gained from the initial cuboid in Fig. 14b depicted in red shows two distinct peaks which can be clearly assigned to pore throat areas formed by either three or four particles. The larger peak at smaller diameters results from pore throat areas which are formed by three particles whereas the smaller peak at larger diameters is due to fourparticleconstellations. The probability of occurrence of pore throats formed by three particles is certainly higher compared to pore throat areas resulting from fourparticleconstellations. Downscaling to smaller volume elements (up to 256 voxelsided cubes) showed qualitatively the same pore throat distributions. In accordance with local distributions for porosity and permeability, the equivalent mean pore throat diameter also shows a spatial gradient along the sample height z, see Fig. 14a, decreasing from top to bottom about 14% due to compaction in deeper layers.
The correlation of the permeability, the porosity and the mean pore throat diameter for the sintered sample with bead diameters of 0.4–0.6 mm is plotted in Fig. 15, displaying the porosities \(\phi \) (a) and the normalized intrinsic permeabilities \(k_{z}^s/\langle d_{p}\rangle ^2\) (b) of differently sized subsets taken from the initial cuboid in dependence on their normalized mean pore throat diameters \(\langle d_{pt} \rangle /\langle d_{p} \rangle \). For both, the porosity and the normalized permeability a clear linear dependency on the normalized mean pore throat diameter \(\langle d_{pt} \rangle /\langle d_{p} \rangle \) can be seen, with correlation coefficients of the fits of 0.9378 and 0.9675, respectively. The higher mean pore throat diameters correlating with the higher porosity and the higher permeability values are located at the top of the investigated cuboid and decrease towards deeper layers.
7 Conclusion
In summary, we have demonstrated that the hydraulic properties of sintered glass beads are highly affected by the pore throats, in addition to the porosities and particle sizes. In this respect, the nondestructive Xray Computed Tomography is an efficient tool, which enables the visualization and quantification of internal (microstructural) parameters including the (voxelbased) morphometry of the porous sample. The way \(\mu \)XRCT data are processed is crucial. In this study, different ways have been introduced in order to identify the essential control parameters for the hydraulic properties of the sintered glass bead systems. The presented framework can in future be used to evaluate also the hydraulic characteristics of other kinds of porous media.
The main findings of this study can be summarized as:

The intrinsic permeability in sintered granular packings depends not only on the porosity, but also correlates with the equivalent pore throat mean diameter.

The pore throat distributions in polydisperse packings show two distinct peaks arising from typical three or fourparticle constellations.

In the given narrow porosity and permeability range, a linear dependency of the permeability with the equivalent pore throat diameter is observed.

The quantitative comparison between experimental and numerical permeability values requires a proper filtering and segmentation procedure and an appropriate domain size, and then can lead to good agreement, even there are a few unexplained outliers, possibly due to channeling (higher permeability) or due to particularly dense samples (lower porosity).
For the examined sintered glass bead samples a clear spatial gradient of microscopic porosity, permeability and mean pore throat diameter along the sample height could be detected as a result of gravitational compaction during sintering.
Local REV analysis has revealed that the averaged values for porosity and intrinsic permeability of smaller sided cubes are (almost) identical to results of larger subsets obtained from the cuboid. A consequence of this result is that, we can either perform many cost effective and timesaving computations on small subsets, which are less representative, or compute one cost and time intensive large subset. For the calculations of effective quantities new strategies can be developed on the basis of results gained from the REV analysis.
From the REV data, the porosity development across the radial direction was analyzed. A slight increase of porosity at peripheral outer zones could be identified due to the contacts of the beads with the cylinder wall during sintering. Rotational sintering under pressurecontrolled gas atmosphere may eventually lead to more homogeneous samples avoiding spatial gradients of porosity and permeability. From the experimental point of view, the presence of air bubbles in the measuring cell poses a big challenge, which can highly affect the measurement of pressure differences, and thus of the intrinsic permeability. Taking into account these difficulties, a comparison between numerical and experimental determined intrinsic permeability values gives us the possibility to better understand the system. Eventually, we have achieved qualitatively and quantitatively a good agreement between experiment, microstructural analysis and numerical simulations.
We have demonstrated through 3D LB simulations that a proper filtering and segmentation procedure during \(\mu \)XRCT analysis is essential for porosity determinations and to obtain accurate permeability results. We have found that an almost linear correlation between both intrinsic permeability and porosity with the pore throat equivalent diameter can be observed if systematic errors during filtering and segmentation are avoided. Our numerical and experimental permeabilities are in general agreement with permeability predictions according Kozeny–Carman, although the validity of the Kozeny–Carman equation is limited to monodisperse and nonsintered granular packings. In contrast to the factor \(c_{1}=180\) for idealized sphere packings, a value of \(c_{1}=131\) for the empirical constant, which takes into account microstructural effects resulting from the sintering treatment of the polydisperse glass bead packing, could be determined by fitting the predicted permeability values to numerical results from LB simulations.
In this study XRCT structural and permeability analysis have been performed for several polydisperse sintered glass bead samples with different primary particle average diameters. The observed micromacro relations scale with the average diameters of the rather large particles. Further work is needed to extend the study towards systems with smaller particles, higher polydispersity or systems with longer sintering duration time and thus lower porosity. It has to be seen if the presented approach for the processing of the XRCT data and the resulting main findings, for instance the linear dependency of the intrinsic permeability with the pore throats, can be also found in those systems, and in natural porous materials like sandstone.
Notes
With second and third power of porosity.
References
Reboul, N., Vincens, E., Cambou, B.: A statistical analysis of void size distribution in a simulated narrowly graded packing of spheres. Granul. Matter 10(6), 457–468 (2008)
Scheuermann, A., Bieberstein, A.: Determination of the soil water retention curve and the unsaturated hydraulic conductivity from the particle size distribution. In: Schanz, T. (ed.) Experimental Unsaturated Soil Mechanics, pp. 421–433. Springer, NewYork (2007)
Jaafar, R., Likos, W.J.: Estimating water retention characteristics of sands from grain size distribution using idealized packing conditions. Geotech. J. 34(5), 1–14 (2011)
Cantisano, M.T.: Relative permeability in a shale formation in colombia using digital rock physics. In: Unconventional Resources Technology Conference (URTEC), Colombia (2013)
Hilfer, R.: Transport and relaxation phenomena. Adv. Chem. Phys. 92, 299–424 (1996)
Bear, J., Verruijt, A.: Modeling Groundwater Flow and Pollution, vol. 2. Springer, New York (1987)
Hilfer, R.: Transport and relaxation phenomena. Adv. Chem. Phys. 92, 299 (2009)
Dullien, F.A.: Porous Media: Fluid Transport and Pore Structure. Academic press, New York (2012)
Gaiselmann, G., Neumann, M., Schmidt, V., Pecho, O., Hocker, T., Holzer, L.: Quantitative relationships between microstructure and effective transport properties based on virtual materials testing. AIChE J. 60(6), 1983–1999 (2014)
Manwart, C., Hilfer, R.: Numerical simulation of creeping fluid flow in reconstruction models of porous media. Phys. A Stat. Mech. Its Appl. 314(1), 706–713 (2002)
Stenzel, O., Pecho, O., Holzer, L., Neumann, M., Schmidt, V.: Predicting effective conductivities based on geometric microstructure characteristics. AIChE J. 62(5), 1834–1843 (2016)
Halisch, M.: The REV challenge–estimating representative elementary volumes and porous rock inhomogeneity from high resolution microCT data sets, In: Proceedings of International Symposium of the Society of Core Analysts, Napa Valley, California, USA, 1619 September, 2013, SCA2013069 (2013)
Halisch, M.: Application and Assessment of the Lattice Boltzmann Method for Fluid Flow Modeling in Porous Rocks. Ph.D. thesis (2013)
Halisch, M., Vogt, E., Müller, C., CanoOdena, A., Pattyn, D., Hellebaut, P., van der Kamp, K.: Capillary flow porometryassessment of an alternative method for the determination of flow relevant parameters of porous rocks. In: Proceedings of International Symposium of the Society of Core Analysts, Napa Valley, California, USA, 1619 September, 2013, SCA2013007 (2013)
Cil, M.B., Alshibli, K., Kenesei, P., Lienert, U.: Combined highenergy synchrotron Xray diffraction and computed tomography to characterize constitutive behavior of silica sand. Nucl. Instrum. Methods Phys. Res. Sect. B Beam Interact. Mater. Atoms 324, 11–16 (2014)
Fonseca, J., O’Sullivan, C., Coop, M.R., Lee, P.: Noninvasive characterization of particle morphology of natural sands. Soils Found. 52(4), 712–722 (2012)
Houston, A., Otten, W., Baveye, P., Hapca, S.: Adaptivewindow indicator kriging: a thresholding method for computed tomography images of porous media. Comput. Geosci. 54, 239–248 (2013)
Lenoir, N., Bornert, M., Desrues, J., Bésuelle, P., Viggiani, G.: Volumetric digital image correlation applied to Xray microtomography images from triaxial compression tests on argillaceous rock. Strain 43(3), 193–205 (2007)
Schlüter, S., Sheppard, A., Brown, K., Wildenschild, D.: Image processing of multiphase images obtained via Xray microtomography: a review. Water Resour. Res. 50(4), 3615–3639 (2014)
Yazdchi, K.: Micro–Macro Relations for Flow Through Fibrous Media. Ph.D. thesis, University of Twente, Enschede, Netherlands (2012)
Yazdchi, K., Luding, S.: Upscaling and microstructural analysis of the flowstructure relation perpendicular to random, parallel fiber arrays. Chem. Eng. Sci. 98, 173–185 (2013)
Hassanizadeh, S.M.: Derivation of basic equations of mass transport in porous media, part 1. Macroscopic balance laws. Adv. Water Resour. 9(4), 196–206 (1986)
Duda, A., Koza, Z., Matyka, M.: Hydraulic tortuosity in arbitrary porous media flow. Phys. Rev. E 84, 036319 (2011)
Sivanesapillai, R., Steeb, H., Hartmaier, A.: Transition of effective hydraulic properties from low to high reynolds number flow in porous media. Geophys. Res. Lett. 41(14), 4920–4928 (2014)
Nguyen, T.T., Indraratna, B.: Hydraulic behaviour of parallel fibres under longitudinal flow: a numerical treatment. Can. Geotech. J. 53(999), 1–12 (2016)
Carrier, W.D.: Goodbye, Hazen; Hello. KozenyCarman. J. Geotech. Geoenviron. Eng. 129, 1054–1056 (2003)
Berryman, J.G.: Confirmation of Biot’s theory. Appl. Phys. Lett. 37(4), 382–384 (1980)
Narváez, A., Yazdchi, K., Luding, S., Harting, J.: From creeping to inertial flow in porous media: a lattice Boltzmannfinite element study. J. Stat. Mech. Theory Exp. 2013(02), P0 2038 (2013)
Narváez, A., Zauner, T., Raischel, F., Hilfer, R., Harting, J.: Quantitative analysis of numerical estimates for the permeability of porous media from latticeBoltzmann simulations. J. Stat. Mech. Theory Exp. 2010(11), P11026 (2010)
Frijters, S.: Liquid–Liquid and Liquid–Solid Interactions at the Mesoscale. Ph.D. thesis, Technical University of Eindhoven, Eindhoven, Netherlands (2017) (in preparation)
Frijters, S., Harting, J.: SelfAssembled Porous Media from ParticleStabilized Emulsions. arXiv:1408.2974 (2014)
Liu, H., Kang, Q., Leonardi, C.R., Schmieschek, S., Narváez, A., Jones, B.D., Williams, J.R., Valocchi, A.J., Harting, J.: Multiphase lattice boltzmann simulations for porous media applications. Comput. Geosci. 20(4), 777–805 (2016)
Qian, Y.H., d’Humières, D., Lallemand, P.: Lattice BGK models for NavierStokes equation. Europhys. Lett. 17, 479 (1992)
d’Humières, D., Ginzburg, I., Krafczyk, M., Lallemand, P., Luo, L.S.: Multiplerelaxationtime lattice Boltzmann models in three dimensions. Philos. Trans. R. Soc. Lond. A 360, 437 (2002)
Zou, Q., He, X.: On pressure and velocity boundary conditions for the lattice Boltzmann BGK model. Phys. Fluids 9, 1591 (1997)
Hecht, M., Harting, J.: Implementation of onesite velocity boundary condition for D3Q19 lattice Boltzmann simulations. J. Stat. Mech. 10, 1742–5468 (2010)
Alderliesten, M.: Mean particle diameters: from statistical definition to physical understanding. J. Biopharm. Stat. 15(2), 295–325 (2005)
Alderliesten, M.: Mean Particle Diameters: From Statistical Definition to Physical Understanding. Ph.D. thesis, TU Delft, Delft University of Technology (2008)
Gueven, I., Luding, S., Steeb, H.: Hydraulic and acoustic investigation of sintered glass beads. AIP Conf. Proc. 1542(1), 581–584 (2013)
Boomsma, K., Poulikakos, D.: The effects of compression and pore size variations on the liquid flow chracteristics in metal foams. J. Fluids Eng. 124, 263–272 (2002)
Du Plessis, J.P., Woudberg, S.: Pore scale derivation of the Ergun equation to enhance its adaptability and generalization. Chem. Eng. Sci. 63, 2576–2686 (2008)
Dukhan, N., Minjeur II, C.A.: A twopermeability approach for assessing flow properties in metal foam. J. Porous Mater. 18(4), 417–424 (2011)
Porter, M.L., Wildenschild, D.: Image analysis algorithms for estimating porous media multiphase flow variables from computed microtomography data: a validation study. Comput. Geosci. 14(1), 15–30 (2010)
Wildenschild, D., Sheppard, A.P.: Xray imaging and analysis techniques for quantifying porescale structure and processes in subsurface porous medium systems. Adv. Water Resour. 51, 217–246 (2013)
Wildenschild, D., Vaz, C., Rivers, M., Rikard, D., Christensen, B.: Using Xray computed tomography in hydrology: systems, resolutions, and limitations. J. Hydrol. 267(34), 285–297 (2002)
Zhang, S., Klimentidis, R.E., Barthelemy, P.: Micron to millimeter upscaling of shale rock properties based on 3d imaging and modeling. In: International Symposium of the Society of Core Analysts, pp. 27–30 (2012)
Schalkoff, R.J.: Digital Image Processing and Computer Vision. Wiley, New York (1989)
Buades, A., Coll, B., Morel, J.M.: A nonlocal algorithm for image denoising. In: IEEE Computer Society Conference on Computer Vision and Pattern Recognition, 2005. CVPR 2005. vol. 2, pp. 60–65, IEEE (2005)
Buades, A., Coll, B., Morel, J.M.: A review of image denoising algorithms, with a new one. Multiscale Model. Simul. 4(2), 490–530 (2005)
To, H.D., Scheuermann, A., Williams, D.J.: A new simple model for the determination of the pore constriction size distribution. In: 6th International Conference on Scour and Erosion (ICSE6), pp. 295–303, Société Hydrotechnique de France (SHF) (2012)
Shire, T., O’Sullivan, C., Barreto, D., Gaudray, G.: Quantifying stressinduced anisotropy using intervoid constrictions. Géotechnique 63(1), 85–91 (2013)
CostanzaRobinson, M.S., Estabrook, B.D., Fouhey, D.F.: Representative elementary volume estimation for porosity, moisture saturation, and airwater interfacial areas in unsaturated porous media: data quality implications. Water Resour. Res. 47(7), W07513 (2011)
Güven, I.: Hydraulical and Acoustical Properties of Porous Sintered Glass Bead Systems: Experiments, Theory, & Simulations. Ph.D. thesis, Enschede, Netherlands (2016)
Dong, H., Blunt, M.J.: Porenetwork extraction from microcomputerizedtomography images. Phys. Rev. E 80(3), 036307 (2009)
Ma, S., Morrow, N.R.: Relationships between porosity and permeability for porous rocks. In: International Symposium of the Society of Core Analysts, September, pp. 8–10 (1996)
Taylor, H., O’Sullivan, C., Sim, W.: A new method to identify void constrictions in microct images of sand. Comput. Geotech. 69, 279–290 (2015)
Acknowledgements
We acknowledge support from the Stichting voor Fundamenteel Onderzoek der Materie (FOM), which was financially supported by the “Nederlandse Organisatie voor Wetenschappelijk Onderzoek” (NWO) (Project Number: 09iPOG141/2), and partial support by the NWO STWVICI (Project Number: 10828). We also thank Matthias Halisch from the Leibniz Institute for Applied Geophysics (LIAG) in Hannover, Germany for performing and providing \(\mu \)XRCT scans, as well as the Jülich Supercomputing Centre for providing the CPU time for the lattice Boltzmann simulations.
Author information
Authors and Affiliations
Corresponding author
Ethics declarations
Conflict of interest
There is no conflict of interest.
Rights and permissions
Open Access This article is distributed under the terms of the Creative Commons Attribution 4.0 International License (http://creativecommons.org/licenses/by/4.0/), which permits unrestricted use, distribution, and reproduction in any medium, provided you give appropriate credit to the original author(s) and the source, provide a link to the Creative Commons license, and indicate if changes were made.
About this article
Cite this article
Gueven, I., Frijters, S., Harting, J. et al. Hydraulic properties of porous sintered glass bead systems. Granular Matter 19, 28 (2017). https://doi.org/10.1007/s100350170705x
Received:
Published:
DOI: https://doi.org/10.1007/s100350170705x