1 Introduction

Understanding of coal surface physic and chemical properties is the prerequisite to better know the unique characteristic of coal that is easily affected by the oxidation process. A conventional method of characterizing microscale coal surface properties is by using images microscopy such as scanning electron microscopy and transmitting electron microscopy. Several electron microscopy methods are limited to understanding the adhesion force characteristics that serve as an indirect way to determine coal surface morphology and its structure.

AFM is one of the available tools for measuring the surface physical properties with various applications such in material sciences and mineral engineering (O’Brien and Hermann 1973; Fuji et al. 1999; Karoussi et al. 2000; Sedin and Rowlen 2000; Jones et al. 2002; Farquhar et al. 2003; Leite et al. 2003; Butt et al. 2005; Das et al. 2010; Petrus et al. 2011). The method has an advantage of having simple sampling procedures, very high-resolution imaging and involving quantitative analyses. An early application of AFM technique on coal observed the surface topography and characteristics of the coal pore structure (Yumura et al. 1993). Even though the observing range and area of AFM is limited, its wide range of applications on coal pore sciences and physical structure has been well studied (Yordan and Yoon 1988; Drelich et al. 1997; Lawrie et al. 1997; Cohen et al. 1998; Datta et al. 2000; Bruening and Cohen 2005; Ozdemir et al. 2009; Liu et al. 2010; Morga 2011; Wu et al. 2014; Xia and Xie 2014; Xia and Yang 2014; Pan et al. 2015). AFM images could support some evidence for the presence of the porosity in coal observed for both the vitrinites and inertinites (Lawrie et al. 1997). At early stage artificially peat coalification, AFM is used for surface roughness characterization at micrometer scale (Cohen et al. 1998). Coking coal structural alteration was resulting from heat treatment at 400–1200 °C could change surface roughness of semifusinite and fusinite (Morga 2011). The coal sample after oxidation using H2O2, AFM images show more area of lower topography (resulting from loss of material) (Bruening and Cohen 2005). A recent report on nanometer scale AFM images of anthracite as results of the differences in the degree of metamorphism, the macromolecular polymerization is enhanced, and micropores are predominant (Pan et al. 2015). Using the method and results described by the previous researchers, AFM can provide significant information relative to physical properties of coal surface. However, the last results did not report adhesion force phenomenon resulting from coal surface during oxidation as valuable information for further study of coal surface contact angle and its chemical properties.

The use of FTIR in the study of coal functional groups change during oxidation and weathering process has also recently attracted more attention (Liotta et al. 1983; Rhoads et al. 1983; Gethner 1985; Yürüm and Altuntas 1998; Wang et al. 2010). Typically, the chemical structure of coal changes with increased oxidation temperature process, while the functional groups show differences. Depending on the oxidation temperatures, there was different relative proportions increase in carbonyl and carboxyl groups (Rhoads et al. 1983). Oxidation of coal can also lead to the formation of new carbonyl species (Gethner 1985). Coal is complex, predominantly organic-containing porous solid which is important both as an energy and as a chemical source material. The physical and chemical properties of most coals are extremely sensitive to air oxidation and their mechanism studied by In Situ FTIR Difference Spectroscopy technique (Gethner 1987). Investigations of the different air oxidation temperature, the absorption in the aliphatic C–H stretching region decreased, while the absorption in the C=O stretching region presented a significant increase (Yürüm and Altuntas 1998). The chemical structure of coal is extremely complex, and at the initial stage of coal, oxidation shows the increase of oxygen-containing groups and reduction of aliphatic groups in the FTIR spectrograms (Wang et al. 2010). Therefore, understanding oxygen functional groups changes in coal structure also infer changes in the physicochemical properties of coal surface.

Other phenomena of coal oxidation process that will be addressed in this study are the effects of hydrophobicity and hygroscopic properties on coal surface, contact angle and coal combustion properties. Contact angle has been used to analyze and evaluate the hydrophobic nature of coal, first by Brady and Gauger (1940), Horsley and Smith (1951), Sun (1954), Apian (1983) who showed that the hydrophobicity varied with rank; the relationship between the contact angle and rank as well as relating the contact angle to coal floatability. The reaction of oxygen in the presence of water and constant relative humidity possibly takes place on the oxidized coal surface. Weathering process of anthracite coal could produce more hydrophilic surface and not only changed the surface chemical properties of anthracite coal, but also changed the surface morphology of anthracite coal (Xia and Yang 2014). The contact angles of anthracite coals, when heated at the high-temperature process of 600 °C, decrease quickly with the increase of contact time (Xia and Xie 2014). The water is advancing, and receding contact angles were measured on coal surfaces by varying the bubble size, using the captive-bubble technique (Drelich et al. 1997). The TGA, DTG and DTA curves provided parameters which characterize the tendency of a given coal towards oxidation. Several parameters can also be used to approximate the specific active surface area of coal in reaction with oxygen due to the negative effects of coal oxidation, such as self-oxidation, and tested by analysis of the above specified thermoanalytical curves by TGA (Matyjaszczyk and Przeliorz 1985). Vaporization of moisture on coal surface was express for the endothermic reaction at around 60 °C shown by DTA data (Umar et al. 2005). The exotherm increases with increasing of low-temperature oxidation and is most pronounced for the coal most prone to spontaneous combustion (Clemens et al. 1990). The correlation of contact angle and hydrophilicity index is also studied. In this paper, we discuss the character change by using drop master contact angle and TG–DTA.

The aim of the present work is to measure, evaluate and describe changes of surface characteristic of coal sample during the oxidation treatment in the atmospheric air at 105–400 °C, and to obtain a better understanding of the relationship between changes in oxygen-containing carbon functional groups and the order of related hydrophobicity of contact angle, adhesion force and hygroscopic properties of coal surface to the combustion characteristic.

2 Experimental

2.1 Geological setting and material, apparatus and experimental procedure

The coal sample obtained from Painan area in West Sumatra, Indonesia was classified as semi-anthracite to anthracite. The investigated area is tectonically included in the forearc basin as shown in Fig. 1. The coal-bearing Painan Formation was deposited during the Oligo-Miocene. It consists of breccia, sandstone, claystone, black silt, coaly shale, clayey sand, sandy clay, and conglomerate. This area is commonly covered by sedimentary rock including one shale and carbonaceous shales with thin coal intercalation; laterally and limited distribution and locally lenses and mostly affected by normal faults and also strike-slip faults.

Fig. 1
figure 1

Geological map of Painan area (modified from (Rosidi et al. 1996) and the location of the main coal fields

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Regionally, the primary fault affecting this area is the Sumatran fault which is heading to the sliding faults and normal faults, trending northwest-southeast. In this area, the coals were also locally intruded by granitic sills. The Painan area is situated in a tectonically active region. The coal-bearing strata were subjected to at least one period of folding and faulting and later affected by extrusive and intrusive magmatic activity.

Coals from this area are premium ones, which have been used for metallurgical coking coal and as a blending coal material. Typically, this kind of coal contained high fixed carbon of 92.3 wt%, the energy content of 8294 kcal/kg and very low ash content of 1.6 wt% as well as sulfur contents of 0.6 wt%. Selection of low oxygen content of coal is suitable for studying the oxidation process at elevated temperature. The typical properties of semi-anthracitic coal from the study site are described in Tables 1 and 2.

Table 1 Proximate analysis and calorific value of Painan coal
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Table 2 Ultimate analysis of Painan coal and oxidized coal
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A diamond saw cut selected coal sample grains of about 5 cm2 area and they were given rough to fine wet polish on a series of abrasive papers on slow speed (35 rev min−1), rotating laps using 220, 400, 800, 1500, 2000 mesh and 1200/JIS 4000 Si–C (Maruto). The samples were then washed vigorously to remove any adhering coal and Si–C particles and two final dry polishes on DP-Mol and DP-Nap (Struers), sprayed gently by N2 gas and stored inside the desiccators and maintained in dry conditions. Oxidation experiments were conducted in a conventional oven and furnace simultaneously (Eyela WFO-500 and TMF-2200) in the atmospheric forced convection air flow system at 105 to 400 °C for 30 min.

2.2 Analysis

A vitrinite reflectance measurement was performed by Carl Zeiss microscope, Axioimager A1 m model. Reflectance was measured on telinite using a 50 × magnification objectives lens under oil immersion (n = 1.518 at 23 °C). The vitrinite reflectance determination was obtained from at least 100 points according to AS 2856-3. Maceral analysis procedure was based on AS 2856-2 and conducted in reflected white light and fluorescence irradiated by blue light. Five hundred points were counted on each polished sample. Maceral classification groups were based on AS 2856.

AFM examination was carried out on a polished coal sample, using NanoNavi II (SII) atomic force microscope in the contact mode. All measurements were performed in atmospheric air at room temperature using rectangular micro silicon cantilevers of a nominal elastic constant of 0.02 and 0.08 N/m and a typical resonance frequency of 10.9 kHz. Scanning mode measurement was used in 2 channels simultaneously with scanning speed of 0.35 and 1.00 Hz and force reference of 1.0 nm in a measurement area of 5 µm × 5 µm. Adhesion force analysis was employed using the Scanning Image Probe Processor SPIPTM 5.1.7 software (Petrus et al. 2011).

The water sessile drop contact angle measurement was identified using contact angle meter type drop master (Kyowa interFAce Measurement and Analysis System FAMAS) of a small drop of ultrapure water with the electrical resistivity of 18.2 M Ω cm at 25 °C. The freshly polished coal sample was quickly dried with N2 gas and immediately placed on the measuring place. A very few drops of ultrapure water of 0.2 µL were deposited on the flat coal surface with a speed of 1000 ms for 10 s contact. The contact angle was measured for ten drops on the different polished coal surface and oxidized surface to ensure reproducibility.

The primary components and chemical structure of the coal were analyzed by FTIR using diffuse reflectance infrared Fourier transform spectroscopy (DRIFTS) and JASCO IR Mentor Pro 6.5 software for spectral analysis and other methods previously described by the authors and detailed operation, and band assignments can be found elsewhere (Mursito et al. 2010, 2011; Mursito and Hirajima 2012). A TG–DTA test was conducted using a TG–DTA analyzer (DTG–60 Bruker AXS) specifically for studying the combustible organic matter on coal surface at early stage. Briefly, the semi-anthracitic coal sample and treated coal was milled to less than 75 µm and it passed through 200 mesh screens. Prior to the analysis, hygroscopy test was examined to have a constant humidity environment of a treated coal samples at about 90% humidity and room temperature. A 5 mg sample was then placed in a platinum cell and subjected to an air flow rate at 25 mL/min and a heating rate at 10 °C/min. The maximum experimental temperature was 800 °C. A number of parameters were derived from the curves, which are defined by (Ma et al. 1989; Ohki et al. 1999; Mahidin et al. 2003; Umar et al. 2005), including the ignition temperature (Tig), maximum combustion rate temperature (Tmax), maximum combustion rate (Rmax) and char burn-out temperature (Tbo).

3 Results and discussion

3.1 Coal sample and products properties

Based on 1.93% vitrinite reflectance, the rank of coal is classified as semi-anthracite. As described in Fig. 2, macerals were composed predominantly of vitrinite 95.1%, while liptinite 2.35% and inertinite 1.71% group macerals were less abundant. Minerals were found in small amounts of 0.84%, and most of them were pyrite and clay.

Fig. 2
figure 2

Under reflecting light microscope, the polished coal samples showing a.telinite (Tl); b. telinite cross cutting by resinite (Rs) and inertodetrinite (In) veinlet; c. branching of veinlet compossed inertodetrinite, resinite and micrinite (Mic); d. diseminated of sporinite (Sp) within telinite

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As expected, the oxygen content increased with the oxidation temperature. Table 2 shows that the chemical properties of oxidized coal were mainly affected by the oxidation temperature at 105–400 °C. With the increase of temperature, significant increase in O and decrease C contents were observed in the studied coals. The increase of oxygen content in oxidized products revealed that the oxidation process took place directly in the coal sample. The apparent increase in the oxygen content shown in Table 2 is a measurement of total oxidation and should not be interpreted directly as an increase in oxygen functionality on particle surfaces. The oxygen content increased from 3.8% to 22.9 wt% and the oxidation process influenced the decreased carbon content from 90.7% to 72.4 wt%. The variations of H and N contents in coals were insignificant. Carbon content was lost by approximately 20% in oxidized coal relative to semi-anthracitic coal sample at 400 °C, which was possibly due to partial destruction and conversion of reactive materials into some oxidized components in the products into gaseous products (CO, CO2) and stable solid complexes (Wang et al. 2010). Air oxidation of the coal can result in the uptake of oxygen and the conversion of hydrocarbon constituents into oxygen-containing functional groups (Bouwman and Freriks 1980; Rhoads et al. 1983; Huffman et al. 1985).

3.2 Atomic Force Microscope examination results

Observations of coal surface morphology, force curve profile, and adhesion force are shown in Figs. 3, 4 and 5. A contact mode 2D image and 3D surface morphology revealed a change in a selection of evaluation of curving force due to the development of debris and spotted curved obtained in oxidized coal surface. Selection of the micro silicon cantilevers tip area on the oxidized coal surface at 400 °C increased the difficulty and resulted in a wide difference on the cantilever deflection as described in Fig. 4. An extremely small area of cantilevers tip measurement could give the most important information and the critical analysis of the adhesion force results. Once the tip is in contact with the oxidized coal surface, cantilever deflection will increase as the fixed end of the cantilever is brought closer to the sample. The increase in the oxidation temperature of coal, the wider the piezo displacement as well as, the deeper the deflected and retraction value were obtained from the cantilevers.

Fig. 3
figure 3

A contact mode of 2D AFM selected images and surface morphology of a coal surface as a function of oxidation treated temperature

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Fig. 4
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Selected force curve profile of a coal surface as a function of oxidation treated temperature

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Fig. 5
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Adhesion force s as a function of oxidation treated temperature measured on 3–4 spots for 10 times examination

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Another critical measurement of the AFM force curve is the point at which the adhesion is broken, and the cantilever deflects from the surface. Measuring the rupture force required breaking the bond or adhesion depends on the value of displacement and deflection of cantilevers. Figure 5 shows that oxidation temperature increases exponentially with the adhesion forces. Adhesion force at semi-anthracitic coal and oxidized coal at 400 °C was on average about 0.6–8.6 nN respectively. A very slight decrease was observed at 200 and 250 °C while a sharp increase could be seen at 1.9–8.6 nN when heated at 300 and 400 °C. The phenomenon of adhesion force under ambient conditions at semi-anthracitic coal arises because the formation of a water layer on the hydrophobic surface is insufficient and in comparison, to the oxidized coal at 400 °C would possibly more hydrophilic surface properties (Butt et al. 2005; Das et al. 2010).

3.3 FTIR examination results

FTIR spectrograms of the semi-anthracitic coal samples at different oxidation temperatures are shown in Fig. 6. The results showed the change of oxygen functional groups and absorption relative intensity of the FTIR spectrograms with an increase in oxidation temperature. The increase of oxidation temperature resulted in a significant increase in the concentration of oxygen-containing functional groups. Aromatic carbon remained relatively unchanged under the increasing of oxidation temperature conditions, while aliphatic hydrogen decreased significantly at higher temperature.

Fig. 6
figure 6

Typical FTIR spectrogram of a semi-anthracitic coal sample and oxidized coal as a function of oxidation treated temperature

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The aliphatic hydrocarbon absorbance decreased with the increase of oxidation temperature. Both the methylene unsymmetrical and symmetrical stretching vibrations peaking at 3040 and 2920 cm−1 relative intensity declined with the increase in oxidation temperature, which showed that the aliphatic hydrocarbon had the least difficulty in reacting with the absorbed oxygen. Since the oxidation temperature increased, the reaction of the side chains of aliphatic hydrocarbon with oxygen was difficult, resulting in unstable aliphatic hydrocarbon absorbance and producing carbonyl groups. The presence of a significant amount of active oxygen-containing functional groups led to increasing tendency of coal to further oxidation. Also, the higher level of the oxidation temperature is, the easier the re-oxidation occurs (Liang et al. 2015).

Significant changes in the oxygen content of the functional groups could also be observed in the 1900 and 1700 cm−1. The carboxyl was determined, and the spectrum of 1900 cm−1 at 400 °C was completely lost. The relative intensity of the carboxyl band C=O groups at 1700 cm−1 started to develop at 300 °C. The carboxyl band C=O groups at 1590 cm−1 and aromatic ring C=C stretch absorbance at 1420 cm−1 did not change much in the oxidation process. During operation, aromatic ring stretch absorption remained relatively unchanged up to 300 °C and decreased slightly after that because of some pyrolysis reactions that took place at higher temperatures (Tahmasebi et al. 2012). The carboxyl absorbance became apparent with the increased temperature, showing the gradual generation of carboxyl groups. The relative intensity of carboxyl absorbance at 1700 cm−1 was low at 300 °C and gradually increased at 400 °C, probably due to the active carboxyl-containing groups, including aldehyde, ketone and acid, which were easy to transform and difficult to accumulate (Wang et al. 2010).

C–O–R structures of ethers were observed at 1020 cm−1 and they remained stable with the increase of oxidation temperature. The distribution of aromatic C–H out of plane bending modes at 900–700 cm−1 was also observed during the oxidation process. Aromatic nuclei CH at 750–880 cm−1 tended to diminish sharply in its relative intensity at 400 °C. The stability of the aromatic nucleus during the coal oxidation express the core aromatic nucleus in the structural unit basically did not participate in the oxidation reaction (Wang et al. 2010).

3.4 Contact angle examination results

The contact angles at selected different contact times and spots were obtained and shown in Fig. 7. As shown in Fig. 8, the contact angle decreased due to the increase temperature of oxidation processes. The average contact angle of fresh and semi-anthracitic coal was about 78.3 °C, while the contact angle of oxidized coal decreased when heated only at about 26.8° at 400 °C in the oxidation. It indicated that the sessile water droplet was averagely hydrophobic to spread on the fresh coal surface along with the increase of contact time. Hydrophobicity of deeper coal surface layer might be higher as undisturbed condition. Meanwhile, the oxidized coal surface became more hydrophilic and had lower contact angle after oxidation processes. The contact angle of oxidized coal decreased faster at 200° to 400 °C. At the contact angle of 300 °C, oxidized coal decreased for about 23% at only 10 s of contact time and possibly decreased as the sessile water droplet adsorbed to the surface. However, the hydrophobicity of oxidized coal was obviously changed. Another phenomenon observed was the hydrophilicity index. Yordan et al. studied coal surface wettability and correlated very well with directly measured contact angles, and with the hydrophilicity index as obtained from the infrared measurements. This index is defined as follows:

$$ {\text{Hydrophilicity}}\;{\text{Index}} = \left( {{-}{\text{COOH}}} \right) + 2\left( {{-}{\text{OH}}} \right)/\left( {\text{RH}} \right) + \left( {{\text{Ar{-}H}}} \right) $$

where (–COOH), (–OH), (RH) and (Ar–H) are the values of the absorption intensity obtained using FTIR and diffuse reflectance technique. These results of hydrophilicity index defined by Yordan and Yoon (1988) corresponded very well to the correlation with directly measured contact angles as shown in Fig. 8. The increase in the number of polar groups on the coal surface was expected to cause the coal to become more hydrophilic. Consequently, the hydrophilicity index increased with increasing oxidation of about 1.3 and 2.9. The increase in the hydrophilicity of the oxidized coals can be attributed to increased interfacial attractive forces between polar oxygenate functionality on the coal surface and liquid water (Gray et al. 1991). The concentration of hydrophobic functional groups on the coal surface decreased as the oxidation increased, while the concentration of hydrophilic groups increased. Adhesion force as a function of selected functional group and selected oxidation temperature is shown in Fig. 9. The ratio of the adhesion force for different functional groups can be predicted from their surface energy (Berger et al. 1995). The absorbance intensity of selected functional group corresponded to the adhesion force and higher ratio of polar group increased the adhesion force. These results from macroscopic observations of contact angles were also done by the microscopic AFM observation, confirming that under oxidizing conditions the coal surfaces were rendered more hydrophilic due to the coverage by the oxygen complexes.

Fig. 7
figure 7

Selected water sessile drop contact angles as a function of oxidation treated temperature measured on 10 spots for 10 s examination

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Fig. 8
figure 8

Contact angles and the hydrophilicity index as a function of oxidation treated temperature

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Fig. 9
figure 9

Adhesion force as a function of selected functional group and oxidation treated temperature

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3.5 TG–DTA examination results

The DTAs and DTGs curves of the semi-anthracitic coal sample and oxidized coal products and its combustion characteristic are shown in Figs. 10 and 11. It is noted that by increasing the oxidation temperature not only increased the DTG peak intensity, but also accelerated the peak to lower temperatures, indicating a gradual change in the loss of mass and a change coal surface structure. The loss of coal organic matter during air combustion of oxidized coal was faster than of semi-anthracitic coal, which was likely associated with the coal matrix via oxygen functional groups, appeared to be mainly affected by the air combustion DTG at temperatures lower than 600 °C.

Fig. 10
figure 10

TG, DTA and DTG profile of a semi-anthracitic coal sample and oxidized coal as a function of oxidation treated temperature

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Fig. 11
figure 11

Tig, Tmax and Tbo profile of a semi-anthracitic coal sample and oxidized coal as a function of oxidation treated temperature

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The ignition temperature (Tig) is an important characteristic of coal combustion, especially for low rank coal, due to its high intensity of spontaneous combustion (Mahidin et al. 2003). The ignition temperature is taken as the extrapolated onset temperature of the first peak of the DTA curve, which also corresponds to the temperature at which the TG curve departs from the baseline. The ignition temperature in this study corresponded to the Tig of the volatile matter. The curves illustrate the heat differentiation that occurred during the analysis. The DTA peak appeared at around 561.5 to 571 °C (exothermic) represents the combustion of char (Ma et al. 1989). The shifting of the DTA peaks of the oxidized products at lower temperature demonstrated that significant heat release had occurred during the combustion of coal. Based on this fact, the calorific value of the peat fuel products likely decreased as the oxidizing temperature increased.

Figure 10 shows the effect of temperature on combustion parameters based on the DTA-TG analysis. The Tig of semi-anthracitic coal sample and oxidized coal was 452.9 °C and between 444.7 and 385.7 °C, respectively. The Tig of all oxidized coal progressively decreased as the temperature increased when compared to the Tig of semi-anthracitic coal. The decrease in Tig was ascribed to the increase in the volatile matter in oxidized coal. Therefore, it is apparent to cite a general comparison between semi-anthracitic coal sample and oxidized coal because the reactivity of oxygen primarily influenced their ignition and ascribed to the increase in the oxygen content of oxidized coal. Oxidized coal had a lower ignition temperature and relatively higher mass loss in the low temperature range, indicating that it was easy to ignite and burn out. Therefore, the liability or susceptibility to spontaneous combustion of oxidized coal was higher when compared to the semi-anthracitic coal.

The temperature at the maximum combustion rate (Tmax) is related to the coal reactivity, and reactive coal has a lower Tmax. As shown in Fig. 10, Tmax relatively decreased as the temperature increased when compared to semi-anthracitic coal. The Tmax of the semi-anthracitic coal sample and oxidized coal was observed at 571.6 °C and between 570.7 and 561.5 °C, suggesting that the reactivity of the oxidized coal decreased. The Tbo of the oxidized coal, which reflected their char characteristics, ranged from 652.3 to 648.5 °C. Conversely, the Tmax of all oxidized coal, which indicates the maximum combustion rate, was much lower than that of the semi-anthracitic coal. These findings suggest that it could be potentially easier for the high-quality coal to be oxidized due to the future application of inappropriate coal blending method with low rank coal which has high susceptibility to spontaneous combustion.

4 Conclusion

The effects of air oxidation treatment on physicochemical properties of coal surface present in several interesting phenomena on adhesion force and hydrophobicity properties. Data from the current study indicate that as the oxidation temperature increased, the hydrophobicity of coal decreased, which in turn increased the adhesion force value. The coverage of oxygen complexes was also affected by the decreasing of contact angle and least resistance to the hygroscopic properties. An indication of lowering ignition temperature of oxidized coal was mainly influenced by the reactivity of oxygen and ascribed to the increase in the oxygen content of oxidized coal.

It was found that significant changes occurred in the oxygen content of the functional groups. The aliphatic hydrocarbons decomposed most readily into unstable aliphatic hydrocarbon and produced carbonyl groups. The increase in oxidation temperature showed the gradual generation of carboxyl groups. Aromatic nuclei CH was the most diminished in its relative intensity at temperature of 400 °C. There was also a significant correlation between the development of C=O and COOH and C–O–R structures of ethers during the oxidation process.