3.1 Geochemistry
The trace element and mineralogical composition of the lithologic units are given in Tables 1 and 2 respectively. The coal comprises pyrite, amorphous, and clays (Table 4.2). Quartz, copper, and zinc are also observed in the SEM result.
3.1.1 Trace Element Concentration
The total concentration of trace elements in coals samples from the study area is represented in Table 1. Among all the trace elements in the coal samples studied, Ba was the highest (22.68−78.63 ppm), followed by Cr (10.92−37.75 ppm), Zn (3.10-24.35 ppm), Ni (3.47−27.32 ppm), V (9.68-13.01 ppm), Cu (6.13-7.30 ppm) and Pb (3.48-5.15 ppm). The trace elements analyzed can be grouped into compatible and incompatible (Ajayi et al., 2006). The compatible trace elements include Cr, Ni, and Zn while the remaining elements (As, Ba, Cd, Co, Cu, Hg, Mn, Pb, Se, Mo, and V) are incompatible.
3.1.2 Paleoredox depositional conditions
Trace element concentrations in coal have been used by different authors (Hart and Leahy, 1983; Swaine, 1983; Orem and Finkelman, 2003) as indicators of depositional environments. Chou (1984) and Goodarzi (1987, 1988) studied geochemistry, concentration, and elemental distribution in coal seams and cited elements such as Mo, Mg, B, Cl, Br, Na, Y, and U as indicators of marine influence. Redox-sensitive elements Mo, U, V, Cr, Fe, Mn, Ni, Co, Ba, Pb, Cd, Zn, Cu, and their ratios have been used to assess paleoredox depositional conditions in sedimentary rocks (Algeo and Maynard, 2004; Tribovillard et al., 2006; Saez et al., 2011). In this study, V/(V+Ni), V/Cr, Ni/Co, V/Ni, and Cu/Zn were used to evaluate the paleoredox conditions of depositional environments during sediment accumulation. According to Jones and Manning (1994), Ni/Co ratios < 5 and V/Cr ratios < 2 suggest oxic conditions; 5-7 and 2-4.25 (dysoxic conditions) and > 7 and > 4.25 (suboxic to anoxic conditions) respectively. The Ni/Co and V/Cr ratios of the Okaba coal sample have a value of 2.12 and 1.19 respectively while The Ni/Co and V/Cr ratios of the Ute coal sample have a value of 7.61 and 0.26 respectively (Table 2), indicating mainly oxic depositional environment for Okaba coal and oxic – suboxic for Ute coal. Hatch and Leventhal (1992), proposed V/(V+Ni) ratios > 0.84 for euxinic conditions, 0.54 – 0.82 (anoxic waters) and 0.46 – 0.60 (dysoxic conditions). Therefore, V/(V+Ni) can be related to redox conditions in source rock's depositional environment (Moldowan et al., 1986; Hatch and Leventhal, 1992; Killops and Killops 2005; Peters et al., 2005). Low V/(V+Ni) porphyrin ratios in marine Toarcian rocks reflect oxic suboxic conditions, while high ratios reflect anoxic sedimentation (Moldowan et al., 1986; Killops and Killops 2005). The concentrations of vanadium in the Okaba and Ute coal is 13.01ppm and 9.68ppm respectively as shown in (Table 1). The low vanadium content of the coal suggests a low mature and marine/terrestrial sourced coal (Adedosu et al., 2007). Low V/Ni ratios (< 0.5) are expected for petroleum-derived from marine organic matter, with high to moderate sulphur content, while V/Ni ratios (1-10) are expected from petroleum-derived from lacustrine and terrestrial organic matter (Barwise, 1990). The value of the V/Ni ratio of the studied coal ranges from 0.35 to 3.75 (Table 2). The source rock depositional environment determines the proportionality of vanadium to nickel. The V/Ni ratios (0.35 to 3.75; Table 2) for the coal samples suggest the same depositional environment. Also, plots of V/Cr and Ni/Co ratios (table 4.1 and Fig. 4.3a); Jones and Manning, 1994) indicate predominantly oxic conditions during sediment accumulation. Based on Hatch and Leventhal (1992) published thresholds, the V/(V+Ni) ratios for the Okaba and Ute coal samples (Table 1 and Fig. 5a) indicate oxic and euxinic condition respectively. However, V/(V+Ni) ratios predict lower oxygen bottom-water conditions (anoxic) than either Ni/Co or V/Cr (Peters et al., 2005). The V/(V+Ni) ratio can be linked to redox conditions in source rock and low ratios reflect oxicity while high ratios (> 0.9) reflect the anoxic condition in the depositional environment of coal (Peters et al., 2005). The low V/(V+Ni) ratio (0.26- 0.0.79; Table 1; Fig. 5b) shows that the coal samples are deposited under oxic conditions. This is typical of a coal depositional environment and in agreement with earlier work done by Akande et al., (1992).
Table 1
Concentration of trace elements contents in Ute and Okaba Coals with certified value.
S/No
|
Coal Mine Sites
|
Sample code
|
Lithology
|
As
Ppm
|
Ba
ppm
|
Cd
ppm
|
Co
ppm
|
Cr
ppm
|
Cu
Ppm
|
Hg
Ppm
|
Mn
Ppm
|
Ni
ppm
|
Pb
Ppm
|
Se
ppm
|
Mo
ppm
|
Zn
ppm
|
V
ppm
|
1
|
Okaba
|
OB-1
|
Coal
|
5.00
|
78.63
|
0.16
|
1.64
|
10.92
|
7.30
|
2.33
|
20.17
|
3.47
|
3.48
|
3.13
|
0.42
|
3.10
|
13.01
|
2
|
Ute
|
UT-1
|
Coal
|
3.78
|
22.68
|
0.15
|
3.59
|
37.75
|
6.13
|
1.12
|
12.59
|
27.32
|
5.15
|
2.40
|
0.32
|
24.35
|
9.68
|
Table 2
Concentration of trace elements contents in Ute and Okaba Coals with some elemental ratios
Sample Name
|
Ni
|
Co
|
V
|
Cr
|
Cu
|
Zn
|
V/Ni
|
Ni/Co
|
Cu/Zn
|
V/Cr
|
V/(V+Ni)
|
Okaba
|
3.47
|
1.64
|
13.01
|
10.92
|
7.3
|
3.1
|
3.75
|
2.12
|
2.35
|
1.19
|
0.79
|
Ute
|
27.32
|
3.59
|
9.68
|
37.75
|
6.13
|
24.35
|
0.35
|
7.61
|
0.25
|
0.26
|
0.26
|
4.4 Environment of Deposition
Sulphur content in coal differs from one coal bed to another, it is still an important factor to consider in coal classification. Geochemical studies of sulfur in coals comprise several major aspects relating to the nature and origin of sulfur in coals, including the abundance and distribution of sulfur in coal seams, abundance of sulfur in coal lithotypes and macerals, characteristics and geochemical significance of sulfur-containing organic compounds, sulfur isotopic studies relating to the sources of sulfur in coals, and sedimentary environments controlling the geochemistry of sulfur in coal. variation of sulfur in coals is closely related to the depositional environments of coal seams. For low sulfur coal (< 1% S), sulfur is derived primarily from parent plant material. For medium-sulfur (1 to < 3% S) and high-sulfur (≥ 3% S) coals, there are two major sources of sulfur: 1) parent plant material, and 2) sulfate in seawater that flooded peat swamps (Chou, 2012). Abundances of sulfur in coal are largely controlled by the degree of seawater influence during peat accumulation and by post-depositional changes (diagenesis). In high-sulfur coals, seawater sulfate diffuses into the peat, which is subsequently reduced by bacteria into hydrogen sulfide, polysulfides, and elemental sulfur. The total sulfur content of Okaba Coal is 0.85% and Ute coal is 2.33% (Table 3). These data allow classifying the Okaba and Ute coal as low-sulfur and medium-sulfur coal respectively. Coals with low sulfur content are usually formed in the lacustrine environment based on co-occurrence of fluvio-marine (Ehinola et al., 2012) while high-sulfur coals are deposited in the environment affected by seawater (Chou, 2012). By implication, the sulfur content in the Okaba and Ute coal originated from parent plant material deposited in a lacustrine environment.
Table 3
Total sulfur content in Ute and Okaba Coals from Nigeria
S/No
|
Coal Mine Sites
|
Sample code
|
Lithology
|
Total Sulfur
(%)
|
1
|
Okaba
|
OB-1
|
Coal
|
0.85
|
2
|
Ute
|
UT-1
|
Coal
|
2.33
|
4.5 Mineral composition
The Okaba and Ute coal generally contain a high content of detrital minerals, mainly quartz (25%) and total clay (52.7) (Table 4). In the analyzed samples, quartz content ranges from significant to moderate. Quartz content is an important factor affecting fracture development; thus, the quartz-rich coal sections are more brittle and therefore make it easy for them to develop fractures. Mineral matters occur in coal in a different mode of occurrences. Many different minerals behave differently. The main minerals are quartz, kaolinite, mullite, and rutile, while the common fluxing minerals are anhydrite, acid plagioclases, K feldspars, Ca silicates, and hematite (Creelman et al. 2013; Mishra et al. 2016a, b). Table 4 represents the XRD diffractogram result of two samples (Okaba and Ute coal). It indicates the presence of quartz (Q), kaolinite (K), as major mineral phases in both samples. The XRD patterns of both coals are found to show almost similar mineral compositions. The identification of minor minerals only by XRD in a multi-component system like coal is difficult due to the detection limits (normally at about 0.5–1%) and peak overlapping (Mishra et al., 2016a). Brittle mineral content is an important factor of matrix porosity, micro-fracture development, gas-bearing, and fracturing reformation of shales. The low content of clay minerals and high content of brittle minerals make rocks more brittle. In such circumstances, rocks are more easily to create natural fractures and induced fractures under artificial fracturing forces to form structural joints with tree networks, which is conducive to coal gas exploration (Zou Caineng et al., 2010). Okaba and Ute Coal are rich in brittle minerals, thus conducive to fracturing.
Table 4
X-ray Diffractogram results in the Nigeria Coals.
S/No
|
Coal Mine Sites
|
Sample code
|
Lithology
|
Quartz
|
Pyrite
|
Amorphous
|
Total Clay
|
1
|
Okaba
|
OB-1
|
Coal
|
25.0
|
1.4
|
20.9
|
52.7
|
2
|
Ute
|
UT-1
|
Coal
|
13.8
|
1.2
|
37.7
|
46.1
|
4.6 Morphological and Microstructural Properties
The surface morphology and microstructure of the coal samples were examined by SEM spectroscopy. Figure 4.4 present the high-resolution SEM micrographs of Okaba and Ute coals examined at a magnification of ×1100. The SEM morphological and microstructural analysis presents valuable insights into the chemical composition, pore structure, orientation of particles, and surface composition of solid materials (JEOL 2017; Sengupta et al., 2008). It also provides an indication of the mineral components present in the structure of coals examined during the process (Nyakuma 2019). As observed in Figure 6, the morphology of each coal is characterized by a rough, contoured, and sintered surface with evident macro- or micro-pores along. The coal particles observed in the SEM micrographs also exhibited a glassy sheen at the edges. (figure 6). The glassy or reflective nature of the surface particles observed on the coal surfaces could be due to the presence of aluminosilicate and iron-containing minerals such as quartz, kaolinite, calcite, and pyrite (Akinyemi et al. 2012; Querol et al. 1995; Liu et al. 2005). It is also observed that the Ute and Okaba coals contain copper and zinc (figure 6).
4.6.1 Evolution Mechanism of Micro-Nano Scale Pores in Coals
Coal is a complex organic rock that consists of fractures and pores. Pore-fracture systems in coal are very complicated. The main space to store CBM is pore. fracture is the bridge of communication among pores, and it is also the migration channel for gas. Fractures strengthen the connectivity among all kinds of pores so that larger pores and pore-fracture systems can be formed (Ju et al., 2005; Ju and LI, 2009). The evolution of pore structures in coals is related to many factors. The coal's degree of metamorphism, degree of deformation, macerals, minerals, (Pan et al., 2015), and coalification (coal rank) are the main factors influencing the evolution of micro-nano scale pores in coals. (Nie et al., 2015b; Song et al., 2014). Levine, 1993 showed that micropores were related to carbon content and that, in general, micrometer-scale pores increased as coal rank increase. Ozdemir and Schroeder, 2009 also found that as coal rank increases, pore size generally decreases. The physical and chemical properties of coal vary enormously during coalification, (Chen et al., 2015) forming a series of pores from macrometer-scale pores to nanometer-scale pores. The physical properties of coal reservoirs play a very important role in gas adsorption and migration. Cleats and fractures in coals induced by coalification are connected to the development of micro-nano scale pores (Pan et al., 2015), although their formation is complex. Fractures and cleats in lower rank coals were short and randomly distributed, according to Prinz and Littke, 2005; however, they formed better and were spread more regularly in higher rank coals, according to Chen et al., 2015. Temperature, stress, and the combined influence of these two elements are the key indicators of coalification.
The pore or fracture diameter observed on the SEM image of the study area was measured and it was observed that the diameter of pore and fracture from the Okaba and Ute coal ranges from 3,600nm to 31,500nm and 9,400nm to 65,600nm respectively.
According to the pore diameter classification method of Hodot, 1996 and Yao et al., 2006:2008 the pores or fractures are divided into two types, that is, microfractures (>10,000 nm), macropores (1000-10,000 nm). Macropores belong to seepage pores, while transition pores and micropores belong to adsorption pores. Gas transport is via laminar flow or turbulent flow in the seepage pores and via capillary condensation, physical adsorption, and diffusion in the adsorption pores Hodot, 1996, Yao et al., 2006:2008. It is to be of note that the fracture in Okaba and Ute coal are wide fracture which extends from the Northwestern part to the southeastern part of the SEM image (Figure 7a and b) which by implication, can serve as a reservoir for coal bed methane (CBM) and the linkage of the fractures and the pores make it to have high permeability that could result to the coal to easily release the gas it's storing upon heating.
4.7 Coal Gasification (Syngas Extraction)
Gasification is governed by the same rules that regulate combustion processes. Wood and paper are among the solid biomass fuels suitable for gasification, as are peat, lignite, and coal. All of these solid fuels are essentially carbon-based, with minor amounts of hydrogen, oxygen, and impurities including sulphur, ash, and moisture. Therefore, coals constituents from Ute and Okaba were transformed completely into gaseous forms leaving ashes and inert material as remains.
According to the conventional view of producing gas, the gasification reaction occurs in four zones. Oxidation, reduction, pyrolysis, and distillation are the four zones. The Gasification process is based on the controlled generation of highly flammable gas from air and water vapour. From the bottom to the top of the gas generator, some chain chemical processes are thought to occur. Combustion, reduction, pyrolysis, and drying are examples of these reactions.
In the combustion zone charcoal was ignited to burn and produce flame to ignite the coal, this process is in the presence of air with the aid of a blower which supplies air into the reactor. The coal burns for about 60 minutes where all the water in it has been expelled and the system is closed, which will lead to the producer gas being moved to the reduction zone. The partial combustion products CO2 and H2O obtained from the oxidation zone now move through the reduction zone. By absorbing heat from the oxidation zone, CO2 and H2O are reduced to carbon monoxide (CO) and hydrogen (H2). To boost the carbon/steam gasification reaction, which has larger activation energy, the oxidation zone raises the temperature of the reduction zone. This reaction requires a temperature of 9000C and above. Over 90% of CO2 was reduced to CO at temperatures above 900ºC. and in the pyrolysis zone, the remaining oil occurs as a stain in the upper part of the reactor due to burning in the absence of air, and syngas and impurities were collected into the cyclone filter where the gas is separated from the impurities. The gas collected is a mixture of N2, H2, CO2, and CH4.
Table 4.5: Experimental Results
Experiments were carried out to find out the amount of gas that coals from Okaba and Ute will generate at maximum temperature.
Sample Name
|
Sample weight (kg)
|
Weight of empty cylinder (kg)
|
Burning temp. of the reactor (0C)
|
Time to complete combustion
|
Weight of cylinder after gasification(kg)
|
Okaba
|
1
|
5
|
500-1000
|
1hr
|
6.55
|
Ute
|
1
|
5
|
500-1000
|
1hr
|
6.09
|
Temperature of burning coal = 900 0C-1000 0C
Temperature of reduction zone =548 0C
Temperature of drying zone = 1310C
4.8 Environmental Impact
Coal gasification is a well-proven technology that started with the production of coal gas for urban areas, progressed to the production of fuels, such as oil and synthetic natural gas (SNG), chemicals, and most recently, to large-scale Integrated Gasification Combined Cycle (IGCC) power generation. IGCC is an innovative electric power generation concept that combines modern coal gasification technology with a both gas turbine (Brayton cycle) and steam turbine (Rankine cycle) power generation. The technology is highly flexible and can be used for new applications, as well as for repowering older coal-fired plants, significantly improving their environmental performance. IGCC provides feedstock and product flexibility, greater than 40 percent thermal efficiency, and very low pollutant emissions. IGCC plants have achieved the lowest levels of criteria pollutant air emissions (NOx, SOx, CO, PM10) of any coal-fueled power plants in the world. Emissions of trace hazardous air pollutants are extremely low, compared with those from direct-fired combustion plants that use advanced emission control technologies. Discharge of solid byproducts and wastewater is reduced by roughly 50% versus other coal-based plants, and the by-products generated (e.g., slag and sulfur) are environmentally benign and can potentially be sold as valuable products. Another significant environmental benefit is the reduction of carbon dioxide (CO2) emissions, by at least 10% per equivalent net production of electricity, due to higher operating efficiency compared to conventional pulverized coal-fired power plants.
The EPA-designated criteria air pollutants produced by the conversion of coal and other solid carbonaceous fuels (e.g., petroleum coke) in gasification-based power cycles are SO2, NOx, particulates, and CO. The environmental benefits of the gasification steam from the capability to achieve extremely low SOx, NOx, and particulate emissions from burning coal-derived gases sulfur in coal, for example, is converted to hydrogen sulfide and can be captured by processes present use in the chemical industry. Among the environmental benefit of coal gasification is the production of significantly lower quantities of criteria air pollutants, reduce the environmental impact of waste disposal because it can use waste products as feedstocks—generating valuable products from materials that would otherwise be disposed of as wastes, gasification's byproducts are non-hazardous and are readily marketable, gasification plants use significantly less water than traditional coal-based power generation, and can be designed so they recycle their process water, discharging none into the surrounding environment, carbon dioxide (CO2) can be captured from an industrial gasification plant using commercially proven technologies. In fact, since 2000, the Great Plains Substitute Natural Gas plant in North Dakota has been capturing the same amount of CO2 as a 400 MW coal power plant would produce and sending that CO2 via pipeline to Canada for Enhanced Oil Recovery.