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Article

Synergy of Parameters Determining the Optimal Properties of Coal as a Natural Sorbent

1
The Strata Mechanics Research Institute of the Polish Academy of Sciences, Reymonta 27, 30-059 Kraków, Poland
2
Faculty of Geology, Geophysics and Environmental Protection, AGH University of Science and Technology; al. Mickiewicza 30, 30-059 Kraków, Poland
*
Author to whom correspondence should be addressed.
Energies 2020, 13(8), 1967; https://doi.org/10.3390/en13081967
Submission received: 20 March 2020 / Revised: 10 April 2020 / Accepted: 12 April 2020 / Published: 16 April 2020

Abstract

:
Selection of the optimal properties of coal as a natural sorbent, both as a sample collected from a seam or of the coal seam itself, requires various parameters to be determined and may not be based on the knowledge of metamorphism degree only. In order to improve the predictions of sorption capacity and the kinetics, analyses of correlation and multiple regression based on the results of laboratory studies were performed for 15 coal samples with various coal rank. The maximum vitrinite reflectance (R0) for low-rank coals was 0.78%–0.85%, and 0.98%–1.15% and 1.85%–2.03% for medium- and high-rank coals, respectively. Coal samples were subjected to technical and petrographic analysis. The gravimetric method was used to perform sorption tests using methane, in order to determine the sorption capacity and the effective diffusion coefficient for each of the coals. Pycnometric methods were used to determine the textural parameters of coals, such as the percentage porosity and specific pore volume. The studies were further supplemented with an evaluation of the mechanical properties of the coals, Vickers micro-hardness, and elastic modulus. This work shows that the statistical multiple regression method enables a computational model including the selected petrophysical parameters displaying synergy with the specific sorption property—capacity or kinetics—to be created. The results showed the usefulness of this analysis in providing improved predictions of the optimal sorption properties of coal as a natural sorbent.

Graphical Abstract

1. Introduction

Coal is a natural, microporous material with an extended pore structure, surrounded by cracks and splitting planes. This material shows high sorption affinity to gases genetically related to coal deposits: carbon dioxide and methane [1]. Even though CO2 is naturally present in nature, its excessive emission into the environment as a result of anthropogenic activity places it among gases with the strongest influence on climate warming. Because of the significant emissions into the environment, generated mainly by the power sector, field studies and tests aimed at sequestration of CO2 in geological formations are undertaken [2]. Processes included in carbon capture and storage (CCS) are still considered in the case of yet unused coal deposits [3]. The enhanced coal bed methane recovery process (ECBM), despite many difficulties, is an attractive method cancelling out the adverse effects of CO2 because of the additional benefit in the form of obtained valuable energy source. Further, as ecological fuel, coalbed methane has been used over the years in North America and Australia, as well as in other countries. Coal has recently been considered as a low-cost sorbent, selective towards CO2, especially at low pressures [4], and still, all topics related to this fossil fuel are extremely desirable from the practical point of view in this context [5,6,7].
Selection of coal with optimal properties is a complex and time-consuming process. Comprehensive characteristics of the coal material, including identification of the sorbent structure and its quality parameters, play an important role in this process. Various groups of parameters are determined, including technical, petrographic, textural, sorption, and strength. These parameters vary with changes of the metamorphism degree of the coal and may be dictated by different geneses and origins [8].
The sorption capacity of coal and the effective diffusion coefficient of gas in the coal are used in quantitative determination of sorption properties, accumulative and kinetic, respectively [9,10]. These parameters are determined based on constant pressure sorption test under specified pressure and temperature [11]. Most researchers claim that the metamorphism degree of the organic substance in coal determines its sorption properties [12,13,14,15,16,17,18]. However, the discrepancies of results of experimental studies show that using the coal rank as the only factor evaluating the sorption capacity of coal is a controversial approach [9,19]. Additionally, the petrographic composition of coal [20,21,22], the porous structure [23], or the tectonic disturbances affecting the structural and textural features of the coal seam [24] disturb the clear picture of the relationships described in the literature. It is also known that various petrophysical parameters of coal may have different influences on the sorption properties of coal, and the impact of one of the parameters may limit the influence of another [25]. It is thus difficult to be sure that knowing only the degree of metamorphism will be sufficient to predict (reproduce) other sorbent properties. This may be possible using multiple regression, performed on the results of studies on coal parameters [26]. Multiple analysis enables the so-called synergistic effect to be shown, involving the interaction of two or more parameters, enabling a better effect of the combined interaction to be achieved in comparison with the effects of individual factors. This statistical method may be an optimal tool of coal selection as a sorbent for potential applications.
The objective of this work was to attempt to use multiple analysis of the results of laboratory studies performed on coals with various rank. We expected to find trends in the influence of individual coal parameters on the sorption capacity of coal towards methane and the effective diffusion coefficient of methane in coal during this work. The use of multiple analysis enabled us to study the usefulness of the synergistic effect in understanding the variability of the specific sorption property of coal (capacity or kinetics) as a function of rank.

2. Materials and Methods

2.1. Materials

The authors prepared 15 coal samples for the study, obtained from the Polish and the Czech part of the Upper Silesian Coal Basin (USCB) (Figure 1).
The studied samples included three groups with different metamorphism degree and were labelled as follows:
  • Low-rank coal samples: 35, 97, 141, 143, and 148 with R0 in the range of 0.78%–0.85% (0.82%);
  • Medium-rank coal samples: 227/2, 227/6, 227/9, 227/10, and 227/22 with R0 in the range of 0.98%–1.15% (1.08%);
  • High-rank coal samples: 4006, 4030, 4031, 4032, and 4033 with R0 in the range of 1.85%–2.03% (1.94%).

2.2. Methodology

2.2.1. Technical Analysis

Technical analysis of coals was performed, including determination of the content of volatile matter and of ash. The gravimetric method was used, including procedures provided in the standards related to tests of solid fuels and coal [33,34]. Samples intended for testing were pre-dried at 105 °C. The analysis was supplemented by measurements of absolute and apparent density of coals, as described below.

2.2.2. Texture Studies Using Densimetric Methods

The evaluation of porous spaces in coal samples was performed using AccuPyc 1340 (helium) and GeoPyc 1360 (quasi-liquid) pycnometers made by Micromeritics, USA. Pycnometric measurements enabled estimation and comparison of texture properties, such as specific pore volume Vp and sample percentage porosity ε. The measurements were performed at a constant temperature on coal samples dried at 80 °C. Percentage porosity ε and specific pore volume Vp were determined according to the following formula:
ε = 100 ( 1 ρ p ρ r )
and
V p = 1 ρ p 1 ρ r
where
ρp—apparent density, g/cm3;
ρr—absolute density, g/cm3.

2.2.3. Petrographic Analyses

Microscopic studies were performed on granular polished sections according to the recommendations provided in [35,36]. An AXIOPLAN polarization microscope by ZEISS and a computer operated mechanical XYZ table were used in the petrographic analyses. The analysis of coal macerals is one of the basic analyses carried out manually [37], automatically [38], or supported by artificial intelligence methods [39,40]. This work is based on traditional manual methods. The analyses were performed using white, reflected light with oil immersion, at 500× magnification. Point-type quantitative analysis was performed for 1500 measurement points in order to determine the level of petrographic coal ingredients (main maceral groups and mineral substances). The average reflectance (R0) was also measured for each of the coals, using contamination- and inclusion-free parts of a maceral from the vitrinite group—colotelinite [41]. An Olympus BX50 polarization microscope was used in reflectance measurements, at 400× magnification. The polished sections were analysed in monochromatic light, using oil immersion. The results were obtained using an image analysis system “LUCIA Vitrinite” [42].

2.2.4. Sorption Studies Using Methane

Sorption measurements were performed using the IGA-001 gravimetric sorption analyser made by Hiden Isochema, UK. Coal samples with grain size of 0.16 ÷ 0.25 mm were used in the studies, after outgassing the sample at 80 °C for 10 h (p = 10−6 mbar). Methane sorption isotherms were determined for coals at 20 °C following determination of the sorption capacity at atmospheric pressure of 1 bar (a1), 3 bar, and 10 bar. Thus, the maximum value of sorption capacity (am) was obtained after fitting the Langmuir Equation [43]:
a a m ( p , T ) = b p 1 + b p
where a—methane adsorbed at pressure p, cm3CH4/g; p—equilibrium pressure of methane, bar; T—temperature, °C; am—the maximum sorption capacity at p approaching ∞, cm3CH4/g; and b—Langmuir constant, bar−1.
The results were recalculated to standard conditions (STP) and to dry-ash-free basis.
The effective methane diffusion coefficient of methane in coal (De) was determined on the basis of the solution of a unipore diffusion model in a grain coal sample [44] and the Timofejew formula [45]:
D e = 0.308   R z 2 π 2 t 0.5
where De—effective diffusion coefficient, cm2/s; t0.5—the half-time of the sorption process, s; and Rz—the equivalent radius, cm.

2.2.5. Strength Studies in the Micro Scale

A micro hardness tester CSM Instruments device was used in micro-hardness analyses, including a conical Vickers indenter made of diamond, an XY table, and the microscope part, additionally provided with image analysis software. After each measurement, the computer recorded the experimental parameters and the attached software enabled processing of the obtained results. This work included several measurements for each tested sample. The load used in coal analysis was 0.5 N. For image analysis, Nikon NIS Elements software was used.
The following parameters were analysed:
  • Vickers micro-hardness (Hv), calculated according to the following formula:
    H v = F m a x 9.81 A c ( h c )
    where
    Fmax—maximum force, N;
    hc—indentation depth, μm;
    Ac—surface area of the formed imprint, μm2.
  • standard elastic modulus (EIT) calculated according to the Power Law Method described by [46] after [47]:
    E I T = 1 v s 2 1 E r 1 v i 2 E i
    where
    Ei—elastic modulus of the indenter (constant), (1141 GPa);
    vi—Poisson’ ratio of the indenter, (0.07);
    Er—reduced modulus of the indentation contact;
    νs—Poisson’ ratio of the sample (user’s selection).
  • the rate and nature of cracks and other damage caused by the Vickers indenter being pressed into the analysed material. This parameter enabled us to determine the sample behaviour under the used force and how it breaks or deforms, among others.

2.2.6. Statistical Analysis Methods

The statistical analysis was performed for 17 variables comprising the results of measurements of the coal samples different parameters: technical (4), petrographic (6), sorption (3), strength (2), and texture (2), describing the coal-methane system. They were intended to be used in the analysis of the relationship between the values of various petrophysical parameters of coal (one or multiple) and the value of the sorption parameter—the capacity a1, am, or the kinetic parameter De, respectively.
The existence of linear relationships between the variables was estimated using Pearson’s correlation coefficient (R) and a significance test of the obtained results; the existence of non-linear relationships was also determined using the Spearman’s rank correlation method [48]. The existence of functional relationships between variables was also evaluated, together with the ability to predict the sorption parameters using other variables, using the least squares multiple regression method [48,49].
Models taking into account the non-linear relationship between sorption parameters and the explaining variables were also prepared. The MARSpline model and neuron network with a multiple layer perceptron with one layer of hidden neurons were used for this purpose [50].

3. Results

3.1. General Characteristics of Coals

The results obtained during laboratory tests are presented in Table 1. The tested coals differed in their volatile matter content (12.80%   V d a f   40.97%) and ash content (4.99%   A a   21.28%). The absolute density of the tested coals varied between 1.324 g/cm3 and 1.495 g/cm3 (Table 1). The highly metamorphized coal 4032 was characterised by the highest porosity among the studied coal samples, at ε = 6.6%, with absolute pore volume Vp = 0.051 cm3/g. Medium-rank coal samples, 227/9 and 227/22, were characterised by the lowest porosity—3.4% and 3.8%, respectively. These coals were also characterised by the smallest pore ratio of approximately Vp = 0.03 cm3/g.

3.2. Results of Petrographic Analyses

Measured reflectance encompassed the characteristic values of medium-rank hard coal—types A, B, and C according the UN-ECE classification [51]. Thus, for the purpose of the study, the samples were divided into low-, medium-, and high-rank coals. Depending on the metamorphism degree, the coal is characterised by different optical characteristics, clearly visible under a microscopic, mainly as the shades of grey of individual maceral groups (Figure 2a–f). The darkest shade of grey is present in low-rank coals (Figure 2a,b), while highly metamorphized coals are the lightest (Figure 2e,f). Liptinite group macerals in highly metamorphized coals are not visible under the microscope (Figure 2e,f). This effect is caused by the second coalification jump (R0~1.3–1.4%), during which the microscopic properties of liptinite changed [52]. Regardless of the metamorphism degree, almost all of the analysed coal samples showed vitrinite as the dominant maceral; only the 227/22 sample showed the domination of inertinite group macerals (53.28 %) over vitrinite (43.39%) (Table 1, Figure 3). Liptinite group macerals are the most abundant in low-rank coals. Coal samples no. 141 and 148 contained over 13% of these macerals. Medium-rank coal samples contained less than 6% of this component.
Another petrographic parameter distinguishing coals with various metamorphism degree is the mineral matter content. Young coal deposits usually contain much higher levels of mineral matter compared with mature deposits (Table 1, Figure 4). Medium- and high-rank coals contain no more than 4% of minerals and reach almost 15% in coal with low R0 (cf. 97, Figure 2b).

3.3. Results of Micro-Hardness Tests

Micro-hardness parameters change with the metamorphism degree and with the structural and textural characteristics of coal. This relationship, described by many authors [52,53,54,55,56], can also be seen in the coals from the USCB area described in this work.
The results of micro-hardness tests led to a conclusion that the analysed samples belong to three “ranges” (Table 1). These ranges overlap with the division of samples according to their metamorphism degree. Low-rank coal samples are characterised by the highest micro-hardness of vitrinite (average Hv = 69.25; Figure 5, Table 1). The Vickers cone leaves a relatively small mark on the samples, which means that low-rank coal does not show a tendency to crack under the load of 0.5 N. The samples are only lightly deformed and show some plastic behaviour (Figure 6a), while displaying high values of the micro-hardness parameter (Hv). Medium-rank coal samples show a significant decrease of micro-hardness (average Hv = 58.5; Figure 5, Table 1), and the pressure of the Vickers cone leaves noticeable marks after the measurement. All analysed samples showed extensive cracks from the tops of the impressions, and sometimes detached parts of the material (Figure 6b). The damage visible on the coal surface indicates that this material is easily crushed. High-rank coal samples are characterised by a further decrease of micro-hardness (average Hv = 55.9; Figure 5, Table 1). Clear marks left by the Vickers pyramid are visible on the vitrinite surface after the micro-hardness test, but cracks around the impression are not as spectacular as in the case of medium-rank coal samples. Cracks and detached material parts are still visible, but a larger part of the deformed coal is concentrated within the impression and around it (Figure 6c).

3.4. Sorption Test Results

Figure 7 presents example changes of the amount of adsorbed methane over time, determined under the pressure of 1 bar at 20 °C. Normalisation of the obtained data to the [0, 1] range enables determination of the effective diffusion coefficient De of methane in coal, according to Formula [4]. On the basis of methane sorption isotherms (Figure 8) and of the Langmuir Equation [3], the sorption capacity a1 and the maximum sorption capacity am values were determined. The results are presented in Table 1.
Highly metamorphized coals are excellent sorbents of methane. Sorption capacity a1 varies between 2.8 and 4.3 cm3CH4/g. The maximum sorption capacity am of these coals varies between approximately 23.5 and approximately 26 cm3CH4/g. In the case of low-rank coals, the sorption capacity a1 does not exceed 2.5 cm3CH4/g, while the maximum sorption of methane for low- and medium-rank coals is not higher than slightly above 19 cm3CH4/g. At a constant temperature, an increase in methane sorption capacity was observed from lower rank coals towards those with a higher degree of metamorphism. According to [12], the minimum of sorption capacity value falls on the reflectance R0 around 1.0, which corresponds to the lowest volume of micropores in dry coals (see Table 1).
In the case of high-rank coal samples, the kinetics included approximately 150 h of the saturation process (Figure 7), while in the case of low- and medium-rank coal samples, methane sorption takes less than 20 h. The variation ranges of the effective diffusion coefficient De in the group of highly metamorphized coals correspond to the range of 1.13 × 10−10 cm2/s to 3.46 × 10−10 cm2/s. In the group of medium-rank coals, the value of effective diffusion coefficient De varies between 4.00 × 10−10 cm2/s and 9.77 × 10−10 cm2/s, while in the group of low-rank coals, it varies between 4.18 × 10−10 cm2/s and 8.90 × 10−10 cm2/s. At 20 °C, medium-rank coals show the best ability to transport methane (Table 1). Undoubtedly, the degree of metamorphism significantly influences the development of the porous structure of coal, which affects the kinetics of sorption processes [8,13].

4. Discussion

The discussion part includes a statistical analysis of the results obtained from the performed laboratory measurements. The ability to estimate sorption parameters a1, am, and De using other petrophysical parameters was analysed.

4.1. The Search for Estimation Models

The first stage included analysis of the presence of correlations between the am, a1, or De variables and other petrophysical parameters. The presence of both linear and non-linear correlations was estimated, determining Pearson’s linear correlation coefficients and Spearman’s rank correlation. The statistical significance level of p = 0.05 was assumed. The results of correlation analyses are included in Table 2 and Table 3.
The performed analysis shows that the maximum sorption capacity am displays linear relationships with petrophysical parameters. These relationships are statistically significant for the Vdaf, R0, Lmmf, M, Hv, Immf, and Vp variables. The am and EIT values show a slightly non-linear relationship (see Table 3). Linear relationships were obtained for the sorption capacity at the specified pressure (a1) for EIT and Hv and non-linear relationships for Vdaf, R0, and Lmmf. In the case of the effective diffusion coefficient De, linear relationships were shown for R0, Immf, and (Vt + L)mmf variables, while non-linear relationships applied to parameters such as Vdaf, Vtmmf, Lmmf, Immf, and Vp (Table 2 and Table 3).
The linear relationships between sorption parameters and the metamorphism degree characterised by reflectance R0 may be approximated:
a m = 8.24 + 8.3 R 0
a 1 = 1.24 + 1.30 R 0
D e * = 0.94 0.37 R 0
where De* = De × 109
Owing to the confirmation of the existence of linear and non-linear relationships between sorption and petrographic parameters, it is possible to create good quality models of sorption parameters using regression methods.

4.2. Use of Multiple Regression in the Development of Mathematical Models for Sorption Parameters

Correlation results were used to create multiple regression models for the selected sorption parameters. The first group of models applies to additive, linear relationships between the dependent variable am and the previously selected, independent variables. This model is presented using Equation (10).
am = 36.97 + 4.85·R0 − 3.94·EIT − 0.42·M − 0.1·Immf + 0.27·Aa
In the case of this model, all parameters are statistically significant for the assumed confidence interval. The determination coefficient R2 explains the 94% of the am value variability, and the average estimation error of this parameter is 1.425, that is, approximately 7.5%. A graphical comparison of the results of the maximum sorption capacity with the created regression model is presented in Figure 9. The regression model provides a good approximation of the sorption capacity am and may estimate its values with adequate accuracy.
A comparison of measurements with the linear model for sorption capacity under the set pressure a1 is presented in the Equation (11), and its graphical comparison with the obtained results is presented in Figure 10.
a1 = 7.56 − 0.06·Hv − 0.04·Vdaf
This model is statistically significant; however, it has an estimation error of 0.48, comprising 16% of the average level of the phenomenon. The quality of the model evaluated using the determination coefficient is 0.75. The model quality is adequately high for the model to be used as an approximation of a1 values.
In order to create a multiple regression model for the effective diffusion coefficient De, data were transformed by multiplying by 109. This transformation did not influence the model accuracy and the percentage of the explained data variance. This model is presented using Equation (12).
De* = 0.725 − 0.34·R0 + 0.009·Immf
A graphical comparison of the De diffusion coefficient results with the created regression model is presented in Figure 11. This model is statistically correct and explains 62% of data variability. The standard estimation error is 0.16, or about 35% of the average value.
A model taking into account non-linear relationships in MARSpline data was also created for the effective diffusion coefficient De. The obtained results are very similar to the results of multiple regression (R2 = 0.677, the estimation error was 0.151). The model of a multi-layer perceptron (MLP)-type neuron network also did not show a significantly higher value of the explained data variability R2: 0.67 and 0.72 for the best network architectures (MLP 2-8-1, MLP 2-10-1).

4.3. Optimisation of the Method for Prediction of Sorption Properties of a Natural Coal Sorbent Based on Multiple Regression

Table 4 provides a summary of the results obtained using multiple regression in order to predict sorption properties of coal: am, a1, and De. This summary includes the values of the determination coefficient R2 and Pearson’s linear correlation coefficient (R) for various configurations of parameters introduced into the model. Sets of petrophysical parameters resulting in models best fit to actual data are also presented, as well as a fit for independent variables R0 and Vdaf. This was intended to show whether the introduction of parameters often used interchangeably to the model in order to evaluate the metamorphism degree contributes to an improved predictive ability of the constructed model.
The increased number of independent variables had a positive influence on the quality of the developed model and the ability to estimate sorption parameters. Supplementing the a1 (R0) model with one adequate petrophysical parameter resulted in a noticeable improvement of the sorption capacity estimation under the set pressure (a1). The best results were obtained on the basis of the (R0, Hv) parameter pair, or alternatively using the (Vdaf, Hv) pair. As a result, the multiple regression model based on the parameter determining the metamorphism degree of the sorbent and its Vickers micro-hardness enables the sorption capacity a1 to be estimated in 86% of cases. The explanatory variables R0 and Vdaf may thus be alternatively introduced to the model, depending on the decision of the researcher regarding parameter selection or on how easy it is to determine. As the R0 and Vdaf parameters are intended to indicate the same coal property (metamorphism degree), implementation of both to the same model is redundant.
The performed statistical analysis showed that the R0 parameter adequately (R = 0.9, R2 = 0.82) enables correct conclusions related to the maximum coal capacity towards the adsorbed methane (am). Statistical methods decisively showed that the introduction of five different petrophysical parameters clearly influences the quality of the developed prediction model (almost 97% variability of data explained by the model).
In the case of kinetic aspects, it was shown that R0 as the sole parameter used in the conventional regression model enables approximation of the value of effective diffusion coefficient De on the level of 49% variability of the original variable. Introduction of an additional petrophysical parameter explains 62% of the variability of De. In the case of the kinetic parameter, the petrographic structure of coal and the content of vitrinite and inertinite maceral groups were particularly important. However, the standard estimation error (>30%) is very high, and the model accuracy may not be adequate for practical purposes. The development of an MLP-type neuron network (R2 = 0.67) and MARSpline (R2 = 0.72) did not improve the model quality significantly.

5. Conclusions

The presented studies led to the conclusion that the use of multiple regression improves the quality of prediction of the sorption capacity of coal a1 and am, as well as of the kinetic parameter De. It was shown that the a1 parameter may be modelled on the basis of the R0 and Hv parameters, while the De parameter may be modelled on the basis of R0 and Wt or R0 and Immf pairs. Vickers micro-hardness, which may be considered a measure of the specific structure and behaviour of this natural sorbent, is a very important parameter in the estimation of the usefulness of coal as a methane sorbent. In some cases, the Vdaf and R0 parameters may be used interchangeably, depending on measurement capacity, for example, in order to determine the value of a1. It should be noted that the introduction of both of these parameters into the multiple regression model is redundant.
Thanks to the statistical method of multiple analysis, it is possible to develop a computational model enabling prediction of optimal sorption properties of coal and their subsequent use in specific applications. Contrary to the classical regression method, the multiple regression model includes at least two independent variables (here, petrophysical parameters), synergising with the specified sorption property—capacity or kinetics. The model may be optimised by selecting the adequate number of the best petrophysical parameters. An advantage of optimisation lies in the potential reduction of the number of parameters introduced into the model, and their introduction enables satisfactory evaluation of the sorption properties of coal (minimisation).

Author Contributions

Conceptualization, K.G., B.D., and M.M.; methodology, K.G., B.D., M.C., and M.M.; formal analysis, K.G., B.D., M.C., and M.M.; investigation, K.G., B.D., M.C., and M.M.; resources, K.G. and B.D.; writing—original draft preparation, K.G., B.D., and M.C.; writing—review and editing, B.D. and M.M; supervision, M.M. All authors have read and agreed to the published version of the manuscript.

Funding

This research received no external funding.

Acknowledgments

The presented work was supported through a statutory research fund by the Polish Academy of Sciences and by the AGH—University of Science and Technology, Faculty of Geology, Geophysics, and Environmental Protection. We would like to thank Alena Kozusnikova and Lucie Nemcova of the Institute of Geonics in Ostrava for their help in micro-hardness and reflectance analyses.

Conflicts of Interest

The authors declare no conflict of interest.

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Figure 1. Lithostratigraphic division of the Polish and Czech parts of the Upper Silesian Coal Basin, according to [27], modified by [28] and [29] (Polish part), and [30] modified by [31] and [32] (Czech part). Modified. In red frames, lithostratigraphic formations from which the samples were taken for research are shown.
Figure 1. Lithostratigraphic division of the Polish and Czech parts of the Upper Silesian Coal Basin, according to [27], modified by [28] and [29] (Polish part), and [30] modified by [31] and [32] (Czech part). Modified. In red frames, lithostratigraphic formations from which the samples were taken for research are shown.
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Figure 2. (a) Low-rank coal—a part of coal made of vitrinite, inertinite, and liptinite macerals, as well as smudges of mineral matter; (b) low-rank coal—carbominerite part—mineral matter (loam) overgrowing coal parts made of vitrinite maceral group; (c) medium-rank coal—cracked vitrinite—colotelinite and a part of a inertinite macerals; (d) medium-rank coal—a large inertinite (fusinite) part and a smaller part made of vitrinite; (e) high-rank coal—a lightly cracked part made of vitrinite with an inertinite lamella; and (f) high-rank coal—vitrinite and minerals; reflected light, immersion.
Figure 2. (a) Low-rank coal—a part of coal made of vitrinite, inertinite, and liptinite macerals, as well as smudges of mineral matter; (b) low-rank coal—carbominerite part—mineral matter (loam) overgrowing coal parts made of vitrinite maceral group; (c) medium-rank coal—cracked vitrinite—colotelinite and a part of a inertinite macerals; (d) medium-rank coal—a large inertinite (fusinite) part and a smaller part made of vitrinite; (e) high-rank coal—a lightly cracked part made of vitrinite with an inertinite lamella; and (f) high-rank coal—vitrinite and minerals; reflected light, immersion.
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Figure 3. Share of main maceral groups in samples of various metamorphism degree (recalculated to mineral matter-free (mmf)).
Figure 3. Share of main maceral groups in samples of various metamorphism degree (recalculated to mineral matter-free (mmf)).
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Figure 4. Mineral matter content in samples of various metamorphism degrees.
Figure 4. Mineral matter content in samples of various metamorphism degrees.
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Figure 5. Average micro-hardness values for samples with different metamorphism degree.
Figure 5. Average micro-hardness values for samples with different metamorphism degree.
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Figure 6. Photographs after the microhardness analysis, showing the nature of cracks and other damage caused by the Vickers indenter being pressed into the analysed material. (a) R0 = 0.8%; (b) R0 = 1.1%; (c) R0 = 2%. Reflected light.
Figure 6. Photographs after the microhardness analysis, showing the nature of cracks and other damage caused by the Vickers indenter being pressed into the analysed material. (a) R0 = 0.8%; (b) R0 = 1.1%; (c) R0 = 2%. Reflected light.
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Figure 7. Methane sorption kinetics after normalisation of the adsorbed amount (high-rank coal 4030).
Figure 7. Methane sorption kinetics after normalisation of the adsorbed amount (high-rank coal 4030).
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Figure 8. Methane sorption isotherm resulting from the fitting of the Langmuir model (low-rank coal 143).
Figure 8. Methane sorption isotherm resulting from the fitting of the Langmuir model (low-rank coal 143).
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Figure 9. Value comparison between the maximum sorption capacity am and the created regression model (Equation (10)).
Figure 9. Value comparison between the maximum sorption capacity am and the created regression model (Equation (10)).
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Figure 10. Value comparison between the sorption capacity under set pressure a1 with the created regression model (Equation (11)).
Figure 10. Value comparison between the sorption capacity under set pressure a1 with the created regression model (Equation (11)).
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Figure 11. Value comparison between the effective diffusion coefficient De and the created regression model (Equation (12)).
Figure 11. Value comparison between the effective diffusion coefficient De and the created regression model (Equation (12)).
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Table 1. Results of technical, petrographic, sorption, strength, and texture tests of the studied coal samples.
Table 1. Results of technical, petrographic, sorption, strength, and texture tests of the studied coal samples.
Technical ParametersPetrographic ParametersSorption ParametersStrength Param.Textural Param.
Sampleρr [g/cm3]ρp [g/cm3]Vdaf [%]Aa [%]R0 [%]Vtmmf [%]Immf [%]Lmmf [%](Vt+L)mmf [%]M [%]am [cm3/g]a1 [cm3/gDe [cm2/s]EIT [GPa]Hv [N/mm2]ε [%]Vp [cm3/g]
35low-rank coals1.3951.33336.4510.540.85276.7116.446.8483.569.1317.192.474.18 × 10−105.87272.394.50.034
971.4291.37140.9714.580.78485.084.7610.1595.2414.7217.042.404.99 × 10−105.54763.544.00.030
1411.4951.42534.5121.280.84547.2339.4413.3360.5613.0414.251.948.90 × 10−105.73170.834.70.033
1431.3991.33640.167.220.84888.038.853.1291.1513.1210.781.184.46 × 10−106.17768.154.50.034
1481.3611.30436.614.990.79368.8217.8113.3682.191.9814.961.874.42 × 10−106.25871.354.20.032
227/2medium-rank coals1.3381.28024.7860.97772.7321.276.0078.730.7419.323.899.77 × 10−105.69754.334.30.034
227/61.3731.29623.256.311.10876.1218.505.3881.500.3916.292.586.83 × 10−106.15161.755.60.043
227/221.3261.27621.448.761.15343.3953.283.3346.720.7915.942.837.05 × 10−105.98060.393.80.030
227/91.3441.29820.797.541.09871.0923.805.1176.202.5618.463.315.75 × 10−106.05262.203.40.026
227/101.3241.25520.25.561.07187.559.782.6790.223.4316.422.724.00 × 10−105.94853.865.20.041
4006high-rank coals1.4031.31413.627.541.9491.298.71091.293.1123.492.861.13 × 10−106.22061.226.40.048
40331.3781.29513.918.831.8785.5114.49085.51024.603.233.46 × 10−105.75065.006.00.047
40311.3871.30112.86.872.0378.6021.40078.603.7524.624.311.7 × 10−105.15750.546.20.048
40321.4061.31313.519.022.0188.1811.82088.182.6223.944.252.26 × 10−105.55349.696.60.051
40301.4081.32714.2617.141.8582.4317.57082.430.4525.853.741.13 × 10−105.66559.135.70.043
ρr—absolute density, ρp—apparent density, V d a f —volatile matter yield, daf—dry-ash-free basis, A d —ash yield, d—dry basis, R 0 —vitrinite reflectance, V t m m f —vitrinite content, I m m f —inertinite content, L m m f —liptinite content, (Vt + L)mmf—sum of vitrinite and liptinite, M —mineral matter content, mmf—mineral matter-free, am—maximum sorption capacity for methane, a1—sorption capacity at 1 bar, De—effective diffusion coefficient of methane, EIT—elastic modulus, Hv—Vickers microhardness, ε   —porosity, V p —total pore volume.
Table 2. Pearson correlation coefficient for correlation between sorption and petrophysical parameters of the tested coals. Statistically significant correlations (for p < 0.05) are presented in bold type.
Table 2. Pearson correlation coefficient for correlation between sorption and petrophysical parameters of the tested coals. Statistically significant correlations (for p < 0.05) are presented in bold type.
ρrρpVdafAaR0VtmmfImmfLmmf(Vt + L)mmfMEITHvεVp
am [cm³/g]0.015−0.224−0.8220.0430.9040.394−0.201−0.6680.201−0.538−0.531−0.5600.6930.705
a1 [cm³/g]−0.232−0.398−0.797−0.1080.7210.1810.014−0.591−0.014−0.598−0.649−0.8090.4610.501
De [cm2/s]−0.0750.1420.4500.094−0.703−0.6630.5310.616−0.5310.1530.1580.239−0.639−0.642
Table 3. Spearman’s rank correlation between sorption and petrophysical parameters of the studied coal samples. Statistically significant correlations (for p < 0.05) are presented in bold type.
Table 3. Spearman’s rank correlation between sorption and petrophysical parameters of the studied coal samples. Statistically significant correlations (for p < 0.05) are presented in bold type.
ρrρpVdafAaR0VtmmfImmfLmmf(Vt + L)mmfMEITHvεVp
am [cm³/g]0.136−0.154−0.7500.2000.7290.382−0.107−0.6870.107−0.361−0.550−0.5430.5430.543
a1 [cm³/g]−0.139−0.425−0.8210.0040.8040.1640.214−0.658−0.214−0.429−0.532−0.7890.4250.454
De [cm2/s]−0.290−0.1200.629−0.101−0.593−0.6970.5080.735−0.5080.0140.1360.290−0.710−0.701
Table 4. Analysis of the fitting quality of various multiple regression models.
Table 4. Analysis of the fitting quality of various multiple regression models.
Independent VariablesDependent VariablesR2R
R0a10.5200.721
R0, M0.5930.770
R0, Vp0.5620.750
R0, Hv0.7440.863
Hv, Vdaf0.7540.868
R0am0.8180.904
R0, Vdaf0.8210.906
R0, M0.8260.910
Vdaf, Vp0.7050.839
Vdaf, Hv0.6780.823
R0, EIT, M, I, A0.9370.968
R0De0.4940.703
R0, Vdaf0.6190.786
R0, Vt0.6720.820
R0, I0.6770.823
R0, Vp0.5020.708
Vt, ε0.5570.746
I, ε0.5080.713

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Godyń, K.; Dutka, B.; Chuchro, M.; Młynarczuk, M. Synergy of Parameters Determining the Optimal Properties of Coal as a Natural Sorbent. Energies 2020, 13, 1967. https://doi.org/10.3390/en13081967

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Godyń K, Dutka B, Chuchro M, Młynarczuk M. Synergy of Parameters Determining the Optimal Properties of Coal as a Natural Sorbent. Energies. 2020; 13(8):1967. https://doi.org/10.3390/en13081967

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Godyń, Katarzyna, Barbara Dutka, Monika Chuchro, and Mariusz Młynarczuk. 2020. "Synergy of Parameters Determining the Optimal Properties of Coal as a Natural Sorbent" Energies 13, no. 8: 1967. https://doi.org/10.3390/en13081967

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