Investigation on Component Separation and Structure Characterization of Medium-Low Temperature Coal Tar

Two medium-low temperature coal tars (MLCTs) derived from the pyrolysis of low-grade bituminous coal were separated into 11 narrow fractions by true boiling distillation. The primary property and chemical composition analysis of MLCTs and their distillate narrow fractions were investigated at the macroscopic and molecular level by gas chromatography-mass spectrometer (GC-MS) and proton nuclear magnetic resonance (1H NMR). The two MLCTs show obvious characteristics of medium-low temperature coal tar, including a high H/C, high-oxygen and nitrogen, low-sulfur, low-density, and low viscosity. As the boiling point increases, the molecular weight of each distillate fraction increases continuously. Meanwhile, the yield of each distillate fraction increases gradually, except for the 270–300 ◦C distillate fractions. The oxygen content in the 170–230 ◦C distillate fractions is much higher than that of the other distillate fractions. The dominant groups of compounds in the MLCTs were saturates, aromatics, and resins, and the resin content was above 24.5 wt%. The molecular composition of the below 170 ◦C fractions mainly consists of benzene, toluene, and xylene, and the main phenolic compounds in the 170–230 ◦C distillate fraction are low-rank phenols, such as phenol, cresol, and xylenol. Although the macroscopic properties of the MLCT-Z and MLCT-S were quite similar, the molecular composition, the group composition and hydrogen distribution in each MLCT and its narrow distillate fractions are still different. The present work has contributed to our present understanding of the composition of MLCTs and to the guiding of the efficient processing of MLCTs.


Introduction
The main fossil fuels, petroleum, natural gas, and coal are not only important energy sources but also feedstock for the modern chemical industry [1]. However, with the decline of crude oil prices and the sharp fluctuations of global oil prices, there is an urgent need to find alternative energy sources and solutions [2]. China, as the biggest developing country in the world, has significant reserves of low-rank coal deposits [3]. Through pyrolysis technology, low-rank coal is converted into semi-coke, coal tar, and carbonized gas to realize the comprehensive utilization of resources [4]. As the only liquid by-product, medium-low temperature coal tar (MLCT) can provide abundant information about the medium-low temperature pyrolysis process [5]. Through the analysis of the molecular composition and structure of coal tar, the relationship between the product characteristics and process parameters level, which will provide theory and data foundation for the utilization of medium-low temperature coal tar, including the technology selection, catalyst design, process development, and optimization. Meanwhile, the molecular level simulation optimization of the production process, the molecular level blending, and optimization of oils and refinement management of processing processes will be realized through the molecular level characterization of medium-low temperature coal tar.

Materials
The two MLCT samples (denoted as MLCT-Z and MLCT-S) were obtained by pyrolysis of low-grade bituminous coal in northern Shaanxi, China. The temperature of the pyrolytic reaction varied from 650 • C to 850 • C. The typical properties of MLCT analyzed according to Chinese national standards are shown in Table 1.

GC-MS Analysis
The GC-MS analysis was carried out on an Agilent 7890A-5975C GC-MS equipped with an HP-5 MS column (30 m × 0.25 mm × 0.25 µm). The GC oven was held at 40 • C for 5 min, programmed to 300 • C at 3 • C/min, and then held constant at 300 • C for 15 min. Both the injector and transfer line were held at 300 • C. Helium was used as a carrier gas at a flow rate of 1 mL/min. The MS ion source was set at 230 • C. The MS ionizing voltage was 70 eV, and the mass range was 35-550 Da with a 0.5 s scan period.

1 H NMR Analysis
A Bruker-AC 400 MHz NMR spectrometer was used to analyze the 1 H NMR of the narrow distillate fractions. All the experiments were performed at 25 • C, and the experimental parameters were set as follows: The sample concentration was 10 mg/mL. In addition, deuterated chloroform (CDCl 3 ) and tetramethylsilane (TMS) were used as the solvent and internal standard in the 1 H NMR spectra, respectively.

Relative Average Molecular Weight Analysis
The relative average molecular weight (Mn) of the narrow distillate fraction was determined by KNAUER K-7000 vapor pressure osmometry (VPO) to distinguish the composition of the narrow distillate fractions.

Hydrocarbon-Group-Type Analysis
Hydrocarbon-group-type analysis was carried out on the Agilent 7890A-5975C GC-MS according to the Chinese national standard SH/T 0606-2005. The analysis process was as follows: First, the MLCT was separated into a diesel fraction (<350 ºC fraction) and a heavy oil fraction (>350 • C fraction) by atmospheric distillation. Second, the diesel fraction (0.1 ml) was separated into two fractions by a solid extraction column packed with 2 g silica gel. N-pentane and dichloromethane/alcohol (5:1, v/v) were used to elute saturates and aromatics, respectively. GC analysis was carried out on an Agilent 7890A equipped with a 0.25 mm × 0.25 µm × 30 m silica capillary column and a flame ionization detector (FID). The GC injector and detector temperature were 300 • C and 350 • C, respectively. MS analysis was carried out on an Agilent 5975C equipped with a 0.25 mm × 0.25 µm × 30 m silica capillary column. The oven was kept at 60 • C for 2 min, programmed to 300 • C at a rate of 40 • C/min, and then held constant for 5 min. The transfer line temperature was 290 • C. The MS ionizing voltage was 70 eV, and the mass range was 50-300 Da with a 0.5 s scan period. Third, the heavy oil fraction (0.1 g) was separated into three fractions by a solid extraction column packed with 4 g of silica gel. N-hexane, dichloromethane, and alcohol/dichloromethane (1:1, v/v) were used to elute saturates, aromatics and resin, respectively. A 0.25 mm × 0.25 µm × 40 m silica capillary column was used to transfer the hydrocarbons into the MS. The GC injector temperature was 350 • C, and the oven temperature was kept at 60 • C for 2 min, programmed to 350 • C at a rate of 40 • C/min, and then held constant for 5 min. The transfer line temperature was at 340 • C. The MS ionizing voltage was 70 eV, and the mass range was 50-700 Da with a 0.5 s scan period. At last, the hydrocarbon-group-type of diesel fraction and heavy oil fraction were counted up by mass yield. Table 1 shows the main properties of the MLCTs. The density of MLCT-Z and MLCT-S are 1.032 g/cm 3 and 1.038 g/cm 3 (after dehydration at 20 • C), the H/C ratios are 1.339 and 1.314, and the molecular weights are 203 and 187, respectively. It can be seen that they have a relatively high H/C ratio, low contents of the insoluble fraction, and a high content of oxygen and nitrogen. Meanwhile, the elements with higher content are Fe, Ca, and Al, mainly exist in the form of different salts. Compounds containing oxygen are key characteristic components of MLCT, accounting for 4.11% and 4.96% of the MLCTs, and mainly exist in phenolic compounds. The chemical instability of the MLCTs is caused by heteroatomic compounds containing oxygen, nitrogen, and metal. Fortunately, the low sulfur is very favorable for the deep processing of coal tar. The initial boiling point and temperature of the 80% distillate of MLCT were relatively high, implying that heavy components still occupied a large proportion of the fraction. MLCT-Z and MLCT-S show obvious characteristics of medium-and low-temperature coal tars, such as a high H/C ratio, low contents of sulfur and insoluble fractions, a low density, and a low viscosity, while the contents of ash and carbon residue are high. Figures 1 and 2 show the yields and molecular weights of the narrow distillate fractions, respectively. Different compounds in MLCT have different boiling points, so that the distillate fractions can be separated according to their boiling points. Moreover, true boiling point distillation can effectively control the carbon number of compounds in each narrow distillate fraction. The total fraction of MLCT was fractionated into 11 distillate fractions. As the boiling point increases, the yield of each distillate fraction increases gradually, except for the 270-300 • C distillate fractions. With the boiling point temperature increasing from IBP-170 • C to >360 • C, the molecular weight of each distillate fraction increases continuously. In the same boiling range, the relative molecular mass of different MLCT fractions is different. According to the boiling point temperatures of MLCT-Z and MLCT-S, the yields are as follows: Naphtha fraction (IBP-170 • C) 1.15 and 0.93 wt %, phenol oil fractions (170-230 • C) 8.36 and 11.45 wt %, and diesel fraction (230-360 • C) 36.52 and 35.86 wt %. The yield of the >360 • C distillate fraction of MLCT-Z is 2.21% higher than that of MLCT-S, but the yield of the 170-230 • C distillate fraction of the MLCT-Z is 3.09%, which is relatively low. The >360 • C heavy distillate fraction (distillation residue) accounted for about half mass of the total MLCT, which belongs to coal tar pitch (mainly composed of polycyclic aromatic hydrocarbons), and was the main component of the MLCT. Researches [7,8,36,37] have shown that the >360 • C heavy distillate fraction is exceedingly difficult to hydrogenate and has a low economic value. Figure 3 shows the elemental composition analysis of the narrow distillate fractions. The elemental composition is the basic data reflecting the chemical essence of coal tar. The comparison between MLCT-Z and MLCT-S shows that there is no difference in the type of elements in the narrow fractions, and the variation trend of the elemental content is basically the same. Each narrow distillate fraction has a certain amount of nitrogen and sulfur. Hence, the full enrichment of nitrogen and sulfur in certain distillates was not reached through distillation. By contrast, the total heteroatom content of MLCT-Z is higher than that of MLCT-S. In particular, the difference in the nitrogen and oxygen contents is mainly due to the difference in coal properties and pyrolysis conditions. Appl. Sci. 2019, 9, 11 FOR PEER REVIEW 5 of 12 Table 1 shows the main properties of the MLCTs. The density of MLCT-Z and MLCT-S are 1.032 g/cm 3 and 1.038 g/cm 3 (after dehydration at 20 °C), the H/C ratios are 1.339 and 1.314, and the molecular weights are 203 and 187, respectively. It can be seen that they have a relatively high H/C ratio, low contents of the insoluble fraction, and a high content of oxygen and nitrogen. Meanwhile, the elements with higher content are Fe, Ca, and Al, mainly exist in the form of different salts. Compounds containing oxygen are key characteristic components of MLCT, accounting for 4.11% and 4.96% of the MLCTs, and mainly exist in phenolic compounds. The chemical instability of the MLCTs is caused by heteroatomic compounds containing oxygen, nitrogen, and metal. Fortunately, the low sulfur is very favorable for the deep processing of coal tar. The initial boiling point and temperature of the 80% distillate of MLCT were relatively high, implying that heavy components still occupied a large proportion of the fraction. MLCT-Z and MLCT-S show obvious characteristics of medium-and low-temperature coal tars, such as a high H/C ratio, low contents of sulfur and insoluble fractions, a low density, and a low viscosity, while the contents of ash and carbon residue are high. Figures 1 and 2 show the yields and molecular weights of the narrow distillate fractions, respectively. Different compounds in MLCT have different boiling points, so that the distillate fractions can be separated according to their boiling points. Moreover, true boiling point distillation can effectively control the carbon number of compounds in each narrow distillate fraction. The total fraction of MLCT was fractionated into 11 distillate fractions. As the boiling point increases, the yield of each distillate fraction increases gradually, except for the 270-300 °C distillate fractions. With the boiling point temperature increasing from IBP-170 °C to >360 °C, the molecular weight of each distillate fraction increases continuously. In the same boiling range, the relative molecular mass of different MLCT fractions is different. According to the boiling point temperatures of MLCT-Z and MLCT-S, the yields are as follows: Naphtha fraction (IBP-170 °C) 1.15 and 0.93 wt %, phenol oil fractions (170-230 °C) 8.36 and 11.45 wt %, and diesel fraction (230-360 °C) 36.52 and 35.86 wt %. The yield of the >360 °C distillate fraction of MLCT-Z is 2.21% higher than that of MLCT-S, but the yield of the 170-230 °C distillate fraction of the MLCT-Z is 3.09%, which is relatively low. The >360 °C heavy distillate fraction (distillation residue) accounted for about half mass of the total MLCT, which belongs to coal tar pitch (mainly composed of polycyclic aromatic hydrocarbons), and was the main component of the MLCT. Researches [7,8,36,37] have shown that the >360 °C heavy distillate fraction is exceedingly difficult to hydrogenate and has a low economic value.   Figure 3 shows the elemental composition analysis of the narrow distillate fractions. The elemental composition is the basic data reflecting the chemical essence of coal tar. The comparison between MLCT-Z and MLCT-S shows that there is no difference in the type of elements in the narrow fractions, and the variation trend of the elemental content is basically the same. Each narrow distillate fraction has a certain amount of nitrogen and sulfur. Hence, the full enrichment of nitrogen and sulfur in certain distillates was not reached through distillation. By contrast, the total heteroatom content of MLCT-Z is higher than that of MLCT-S. In particular, the difference in the nitrogen and oxygen contents is mainly due to the difference in coal properties and pyrolysis conditions.

Properties of the MLCTs and Their Narrow Distillate Fractions.
The H/C atomic ratio is a vital parameter to characterize the average structure of coal tar, which is related to its chemical structure and molecular weight. It is obvious that, relative to the feedstock (Table 1), the H/C atomic ratio of the <360 °C distillate fractions increased, while that of the >360 °C distillate fractions (1.17 and 1.14) decreased significantly. The oxygen contents in 170-190 °C, 190-210 °C and 210-230 °C distillate fractions are much higher than those of the other distillate fractions, which is consistent with the fact that these fractions are rich in phenolic compounds.   Table 2 shows the hydrocarbon type analysis of the MLCT. The results show that the MLCTs have three dominant groups of compounds: saturates, aromatics, and resins. The saturates are made up of paraffins and cycloalkanes, and the majority of the cycloalkane compounds are 1-3 ring cycloalkanes. The large amount of saturates is an important feature of MLCT. However, the amount of saturates is notably distinct. The total amount of alkanes and olefins is approximately 10 wt% and as high as 30 wt%. By contrast, the content of saturates in MLCT-Z is 6.8% higher than that in MLCT-  Figure 3 shows the elemental composition analysis of the narrow distillate fractions. The elemental composition is the basic data reflecting the chemical essence of coal tar. The comparison between MLCT-Z and MLCT-S shows that there is no difference in the type of elements in the narrow fractions, and the variation trend of the elemental content is basically the same. Each narrow distillate fraction has a certain amount of nitrogen and sulfur. Hence, the full enrichment of nitrogen and sulfur in certain distillates was not reached through distillation. By contrast, the total heteroatom content of MLCT-Z is higher than that of MLCT-S. In particular, the difference in the nitrogen and oxygen contents is mainly due to the difference in coal properties and pyrolysis conditions.

Hydrocarbon Type Analysis.
The H/C atomic ratio is a vital parameter to characterize the average structure of coal tar, which is related to its chemical structure and molecular weight. It is obvious that, relative to the feedstock (Table 1), the H/C atomic ratio of the <360 °C distillate fractions increased, while that of the >360 °C distillate fractions (1.17 and 1.14) decreased significantly. The oxygen contents in 170-190 °C, 190-210 °C and 210-230 °C distillate fractions are much higher than those of the other distillate fractions, which is consistent with the fact that these fractions are rich in phenolic compounds.   Table 2 shows the hydrocarbon type analysis of the MLCT. The results show that the MLCTs have three dominant groups of compounds: saturates, aromatics, and resins. The saturates are made up of paraffins and cycloalkanes, and the majority of the cycloalkane compounds are 1-3 ring cycloalkanes. The large amount of saturates is an important feature of MLCT. However, the amount of saturates is notably distinct. The total amount of alkanes and olefins is approximately 10 wt% and as high as 30 wt%. By contrast, the content of saturates in MLCT-Z is 6.8% higher than that in MLCT- The H/C atomic ratio is a vital parameter to characterize the average structure of coal tar, which is related to its chemical structure and molecular weight. It is obvious that, relative to the feedstock (Table 1), the H/C atomic ratio of the <360 • C distillate fractions increased, while that of the >360 • C distillate fractions (1.17 and 1.14) decreased significantly. The oxygen contents in 170-190 • C, 190-210 • C and 210-230 • C distillate fractions are much higher than those of the other distillate fractions, which is consistent with the fact that these fractions are rich in phenolic compounds. Table 2 shows the hydrocarbon type analysis of the MLCT. The results show that the MLCTs have three dominant groups of compounds: saturates, aromatics, and resins. The saturates are made up of paraffins and cycloalkanes, and the majority of the cycloalkane compounds are 1-3 ring cycloalkanes. The large amount of saturates is an important feature of MLCT. However, the amount of saturates is notably distinct. The total amount of alkanes and olefins is approximately 10 wt% and as high as 30 wt%. By contrast, the content of saturates in MLCT-Z is 6.8% higher than that in MLCT-S. The paraffin and cycloalkane compounds could be used as a cracking feed. The aromatics are mainly composed of 1-5 aromatic-ring compounds and heteroatomic compounds such as sulfur compounds. The abundant aromatic compounds are mainly 1-3 aromatic-ring compounds with and without short side chains. The main monoaromatic hydrocarbons are alkylbenzenes and indans, followed byindenes. Naphthalenes, acenaphthenes, and acenaphthylenes account for more than 90% of the diaromatics. Meanwhile, the amount of monoaromatics in MLCT-Z is 10.6% less than that in MLCT-S. Although the two MLCT samples come from different production processes, the resin content is the same. As shown in Table 2, the resins content is 24.7 wt%, which is almost 1/4 of the raw MLCT material.

Hydrocarbon Type Analysis
In general, resins are the most complex and heaviest fraction of MLCTs. However, the research found that compared to resins from crude oils, the resins from MLCT have essential differences in chemical composition. The hydrocarbon type of MLCT largely determines the performance of MLCT and its products, therefore, the hydrocarbon type results can be used as an important basis for selecting a suitable processing technology.  Figure 4 shows the GC-MS chromatograms of narrow distillate fractions obtained by true boiling distillation. Distillation is a very convenient method for separating and concentrating components of liquid fossil fuels. However, ordinary distillation methods are not suitable for the easy-coking and thermal sensitive materials in MLCT. True boiling distillation can be operated under vacuum pressure and helps minimize property changes. As shown in Figure 4, as the distillate boiling point temperature increases, the narrow distillate fractions become heavier, and the peak residence time changes from short to long. Compared with the full-range, the narrow distillate fractions have a simpler composition and a more concentrated carbon distribution. The overlap of adjacent components indicates that the components of MLCT cannot be separated completely by true boiling distillation.

Characterization of Narrow Distillate Fractions by GC-MS
The results show that phenols and alkylbenzenes are the main compounds in the distillate fractions below 170 • C, especially phenol and BTX (benzene, toluene, and xylene) in the fractions below 170 • C, the content of BTX in MLCT-Z is approximately 27.2%, while the content of phenol in MLCT-S is approximately 33.6%. The fractions below 170 • C are a suitable feedstock for chemical products rich in BTX aromatics. In the fractions of 170-230 • C, phenolic substances are dominant, and the content of phenols is more than 60%. However, the other compounds, such as the homologs of benzene and naphthalene compounds are also present. The main phenolic compounds in the170-230 • C distillate fraction are low-rank phenols, such as phenol, cresol, and xylenol. The higher-rank phenols (such as C 3 -C 4 alkyl phenols), indenols, naphthols, and alkyl naphthols, are concentrated in fractions above 230 • C. Naphthalene is in the190-210 • C and 210-230 • C distillate fractions, and its homologs are in the 230-250 • C and 250-270 • C distillate fractions. Fluorenes, dibenzofuran and octadecane are in the 270-300 • C distillate fractions. Alkyl fluorenes and alkyl naphthols, phenanthrene, nonadecane are in the 300-320 • C distillate fractions. Phenanthrenes, eicosane, and heneicosane are in the 320-340 • C distillate fractions. Alkanes, pyrene, anthracene, phenanthrene, and its homologs are in the 340-360 • C distillate fractions. The MLCT middle distillates (170-230 • C) are rich in phenols, which are the main raw chemical materials in the chemical industry and should be extracted from coal tar before hydrogenation. As is known, phenolic compounds generate water during the hydrotreating process. The generation of water will shorten the service life of catalysts and increase energy consumption and hydrogen consumption in the hydrogenation process, and equipment corrosion is a serious issue. Therefore, the removal of phenolic compounds before refining is not only beneficial to the hydrogenation process, but can also help to obtain abundant chemical materials. products rich in BTX aromatics. In the fractions of 170-230 °C, phenolic substances are dominant, and the content of phenols is more than 60%. However, the other compounds, such as the homologs of benzene and naphthalene compounds are also present. The main phenolic compounds in the170-230 °C distillate fraction are low-rank phenols, such as phenol, cresol, and xylenol. The higher-rank phenols (such as C3-C4 alkyl phenols), indenols, naphthols, and alkyl naphthols, are concentrated in fractions above 230 °C. Naphthalene is in the190-210 °C and 210-230 °C distillate fractions, and its homologs are in the 230-250 °C and 250-270 °C distillate fractions. Fluorenes, dibenzofuran and octadecane are in the 270-300 °C distillate fractions. Alkyl fluorenes and alkyl naphthols, phenanthrene, nonadecane are in the 300-320 °C distillate fractions. Phenanthrenes, eicosane, and heneicosane are in the 320-340 °C distillate fractions. Alkanes, pyrene, anthracene, phenanthrene, and its homologs are in the 340-360 °C distillate fractions. The MLCT middle distillates (170-230 °C) are rich in phenols, which are the main raw chemical materials in the chemical industry and should be extracted from coal tar before hydrogenation. As is known, phenolic compounds generate water during the hydrotreating process. The generation of water will shorten the service life of catalysts and increase energy consumption and hydrogen consumption in the hydrogenation process, and equipment corrosion is a serious issue. Therefore, the removal of phenolic compounds before refining is not only beneficial to the hydrogenation process, but can also help to obtain abundant chemical materials.

Characterization of Narrow Distillate Fractions by 1 H NMR
The main virtue of NMR analysis is its ability to associate resonances in specific chemical shift ranges with particular structural features. Based on this, the chemical shifts of hydrogen in the MLCT-Z and MLCT-S and their narrow fractions were measured by 1 H NMR. The division of the H Ar , (Aromatic ring protons and aromatic ring hydroxyl, polynuclear aromatic hydrogen, δ = 6.0-9.0), H α (α-CH 2 , α-CH 3 alkyl protons in aromatic rings, alcohols and mercaptan hydroge, δ = 2.0-4.0), H N (-CH/CH 2 in cycloalkanes, normal alkanes and iso-alkanes, δ = 1.4-2.0), H β (β-CH 2 , β-CH 3 alkyl protons in aromatic ring, β-CH 2 groups in longer alkyl chain, δ = 1.0-1.4), H γ (γ-CH 3 in aromatic cyclic alkyl protons, cycloalkanes, and alkanes, δ = 0.5-1.0) regions of the 1 H NMR spectrum, as shown in Table 3, provided qualitative and quantitative information about different types of hydrogen. Data were expressed as the mean of three separate calculations.
From the data in Table 3, it can be seen that the distribution of hydrogen in the MLCT-Z and its narrow fraction was approximately the same as that in the MLCT-S and its narrow fraction, and the components of the two kinds of coal tar were quite similar. With the increase of the distillation temperature, the variation of the hydrogen content in the MLCT-Z and MLCT-S distillates was inconsistent. Overall, the naphthenic hydrogen peak areas of the narrow fractions of the two coal tars were the lowest, indicating that the naphthenic structure components in the coal tar samples were relatively small. The fractions with the highest H N content of MLCT-Z and MLCT-S were greater than 360 • C and 340-360 • C, respectively, indicating that H N had different distillation ranges in different coal tars. In contrast, the H α content was the most in the fractions within the range of 210-250 • C, manifesting that there were more methyl ethyl benzenes in this segment in the form of α-CH 2 alkyl protons andα-CH 3 alkyl protons. Compared to the peak areas of different hydrogen in the narrow fraction of each coal tar, it was found that the fractions with IBP-170 • C and above 300 • C in the distillation range contain more H β , showing that a high amount of hydrogen in the β or further positions of the aromatic ring were in the form of CH 2 and -CH-, or in the form of -CH-attached to methyl groups. The data showed that the H β content of the MLCT-Z was much higher than that of the MLCT-S when the distillation range was 340-360 • C. Combined with the results of GC-MS analysis, the contents of long-chain alkanes and methyl phenols of this narrow fraction in MLCT-Z were higher than those of MLCT-S. The fraction of 170-210 • C in the distillation range was mainly composed of H Ar , indicating that there were more components with an aromatic ring structure. Combined with the results of element analysis, it was found that the O content in this segment was relatively high, which proved that this narrow fraction was mainly composed of phenolic compounds such as methyl phenol and dimethyl phenol. It was reported that the boiling range of phenol oil was 170-210 • C, which proved the reliability of the 1 HNMR analysis of coal tar. However, H Ar had the largest peak area, and the degree of branching was smaller than the other narrow fractions in the two coal tar distillates, the distillation range of which was higher than 340 • C, which meant that there were fewer alkyl side chains in its components, but polycyclic aromatic compounds were the main components. As shown in Figure 2, the higher molecular weight of the distillation range above 340 • C indicated that H in this narrow fraction was mainly polycyclic aromatic hydrogen and existed in the form of polycyclic aromatic compounds, while the polycyclic aromatic compounds of MLCT-Z were mainly concentrated in the distillation range greater than 360 • C fractions. The significant difference in the H distribution of the narrow fractions of MLCT-Z and MLCT-S was mainly reflected in the content of H β , H γ, and H Ar in the distillates above 360 • C. The experimental results indicated that the chemical composition of heavy oil in the MLCT-Z and the MLCT-S was still very different.

Conclusions
The two MLCTs derived from the pyrolysis of low-grade bituminous coal, which had a high H/C ratio, high-oxygen and nitrogen, low-sulfur, low density and low viscosity, show obvious characteristics of medium-low temperature coal tar. The fractions below 170 • C, mainly consisting of benzene, toluene, and xylene, are suitable feedstock for chemical products rich in BTX aromatics. The 170-230 • C distillate fractions of MLCT have high oxygen content and are rich in phenols, which are the main raw chemical materials in the chemical industry and should be extracted from coal tar before hydrogenation. The >360 • C heavy distillate fraction, which belongs to coal tar pitch, accounted for about half of the total mass, is exceedingly difficult to hydrogenate, and has a low economic value. Although the macroscopic properties of the MLCT-Z and MLCT-S are quite similar, the molecular composition, group composition, and hydrogen distribution in each MLCT and their narrow distillate fractions are still different.