Generation and characterization of coal-based needle coke produced by the co-carbonization of coal liquefaction pitch and anthracene oil

In this study, we studied the feasibility of preparing high-quality needle coke from coal liquefaction pitch. Nine types of blending pitch (coal liquefaction pitch and anthracene oil mixed with different ratios) were used as raw materials to generate needle coke via the co-carbonization method. Optical microscopy, X-ray diffraction, Raman spectroscopy and scanning electron microscopy were employed to determine the properties (microstructure, distribution of carbon microcrystals, true density and micro-strength) of the needle coke derived by the co-carbonization method. Actually, the co-carbonization of coal liquefaction pitch and anthracene oil was an essential method to control the micro-structure and property of the derived needle coke. Briefly, the needle coke derived by the co-carbonization of coal liquefaction pitch and anthracene oil had a lower content of mosaic structure of 14.17%, ideal carbon crystal content of 82.67%, and true density of 2.296 g cm−3. Briefly, the addition of anthracene oil is a suitable method to adjust the property of coal liquefaction pitch, which is also a good method to produce high-quality needle coke via the co-carbonization of coal liquefaction pitch and anthracene oil. Thus, the use of coal liquefaction pitch and anthracene oil as raw materials to generate high-quality needle coke is a considerable method to realize the clean and high value-added utilization of coal liquefaction pitch.


Introduction
Needle coke is generally accepted as a type of multi-functional carbon material with a low coefficient of thermal expansion (CTE), high true density, low specic surface area and good resistance. 1,2 Generally, needle coke is used as an optimizing material to produce ultra-high power graphite electrodes, high power graphite electrodes, anode materials for lithium ion batteries, electrode materials for supercapacitors, etc. [3][4][5] However, the production of high-quality needle coke requires raw materials with a higher basic property of. Generally, aromatic precursors with a high degree of aromatic condensation, low content of sulfur, lower insolubility in quinoline and good viscosity are suitable to generate high-quality needle coke. 6,7 It is generally accepted that the property of raw materials is one of the most important factors inuencing the quality of the derived needle coke. Actually, the co-carbonization method (using blending pitch as raw materials to produce needle coke) is recognized as a good way to adjust the molecular structure distribution and viscosity, and then enhance the quality of the derived needle coke. Specically, the molecular structure and viscosity of pitch can be controlled by blending different pitches, and the needle coke produced via the co-carbonization method has high quality. For example, Li et al. 8 produced highquality needle coke via the co-carbonization of coal tar and biomass tar pitch. Yu et al. 9 produced high-quality needle coke (coefficient of thermal expansion value not more than 1.62 Â 10 À6 / C) via the co-carbonization of ethylene tar and uid catalytic cracking of decant oil. Tian et al. 10 blended mediumand low-temperature pitch and coal-based hydrogenated diesel oil for co-carbonization to produce needle coke. Lin et al. 11 adjusted the molecular distribution of pitch by mixing coal tar pitch and bio-asphalt. Cheng et al. 12 synthesized needle coke with a coefficient of thermal expansion value (CTE) in the range of 3.2 Â 10 À6 / C to 0.3 Â 10 À6 / C. Mochida et al. 13,14 also produced high-quality needle coke with a low CTE via the cocarbonization of petroleum vacuum residue and FCC decant oil.
Coal liquefaction pitch (CLP) is a type of complex organic rich in polycyclic aromatic hydrocarbons, 15,16 which is generally obtained from the extraction of direct coal liquefaction residue. 17,18 The molecules of CLP mainly consist of carbon, then hydrogen and some heteroatoms (such as oxygen, sulfur and nitrogen). [19][20][21] However, to enhance the efficiency and added value of CLP, researchers have used CLP as a raw material to synthesize mesocarbon microbeads (MCMBs), porous carbon, carbon foam, and needle coke. [22][23][24][25] As reported in the literature, 24,25 CLP has an extremely high soening point, which makes the viscosity of the liquid-phase carbonization system higher. The higher viscosity of the liquid-phase carbonization system is easy to generate "foam coke", which reduces the derived needle coke. 26 Furthermore, the aromatic condensation degree of CLP is very high (Lin et al. 27 has reported the average molecule formula as C 133 H 106 O 4 N 1 ) to produce high-quality needle coke. Specically, controlling the molecular structure distribution and viscosity of CLP is a suitable method to prepare high-quality needle coke.
Coal liquefaction pitch is a type of complex polycyclic aromatic hydrocarbon with a high molecular weight and viscosity, which is produced via the extraction of coal direct liquefaction residue and can be employed as a raw material to produce needle coke in theory. 24,25 However, the high viscosity of coal liquefaction pitch makes it difficult to produce highquality needle coke via direct liquid-phase carbonization. Anthracene oil is a signicant aromatic component in the coal tar fraction with a low narrow molecular weight distribution and good viscosity. In theory, the blending of CLP and anthracene oil at a suitable rate is a good means to control the molecular structure and decrease the viscosity of blending pitch. Thus, in this study, the co-carbonization of CLP and anthracene oil (blended in varied ratios) was employed to produce high-quality needle coke. Briey, polarized microscopy, X-ray diffraction, scanning electron microscopy, and Raman spectroscopy were used to examine the microstructure and distribution of the carbon microcrystals. Also, the true density and micro-strength of each needle coke sample were also studied in this work.

Raw materials
Coal liquefaction pitch (CLP) was obtained via the extractiondistillation method with the coal direct liquefaction residue as the raw material, and the coking washing oil as the solvent. CLP was obtained from China Shenhua Coal To Liquid and Chemical Co., Ltd, and coking washing oil from Angang Steel Group Co., Ltd. Anthracene oil was purchased from Anshan Xingde Materials Technology Co. Ltd. Toluene and quinoline were obtained from Sinopharm Chemical Reagent Beijing Co., Ltd. Proximate analysis and ultimate analysis are recognized as the common parameters for the characterization of the physical-chemical properties of pitch. The physical-chemical properties of the blending pitches (mixture of CLP and anthracene oil) are shown in Table 1.
As listed in Table 1, with an increase in the content of anthracene oil, the proximate analysis (soening point, toluene insoluble, quinoline insoluble and coking value) obviously decreased. CLP-A 160% had the lowest SP, TI, QI and CV of 36 C, 8.80%, 0.03% and 47.10%, respectively. This phenomenon can be attributed to the properties of anthracene oil. Anthracene oil is one of the important components in coal tar. Anthracene oil has good mobility, lower aromatic condensation, and extreme insolubility in toluene than CLP. Consequently, the greater the content of anthracene oil in the blending pitch, the lower its proximate analysis.
The additive of anthracene oil had little inuence on the content of N and S, but had a great inuence on the distribution of H and O. Actually, the additive of anthracene oil had an obvious inuence on the C/H ratio (R C/H ). Briey, the greater the content of anthracene oil in the blending pitch, the lower its R C/ H . Actually, CLP had the highest R C/H of 1.42, while CLP-A 160% had the R C/H of 1.31.

Preparation of needle coke by co-carbonization of CLP and anthracene oil
25 g blending pitch (mixture of CLP and anthracene oil at different ratios) was placed in a neck glass tube. The glass tube was then placed in a pit resistance furnace, and then the pit resistance furnace was heated from room temperature to 500 C and held for 4 h (the heating rate of 1 C min À1 ) for the cocarbonization process. Aer the co-carbonization process, the green needle coke was obtained. The green needle coke was transferred to a tube-type resistance furnace for calcination. Briey, the green needle coke was heated to 1400 C for 1 h at a heating rate of 5 C min À1 , and pure N 2 was used as an inert atmosphere. Needle coke was obtained aer the calcination, which was denoted as CLP-A X -C (X represents the added content of anthracene oil). A ow diagram of the process for the preparation of needle coke is presented in Fig. 1.  28,29 The element content (C, H, N, and S) distribution was determined using an elemental analyzer (Vario ELIII, Elmentar, German) via the combustion method. Actually, the content of O was calculated using the difference method.
2.3.2 FTIR spectrum analysis of blending pitches. CLP is a type of complex compound, where its functional groups have a signicant inuence on its thermal conversion behavior. FTIR is usually used as an efficient method to judge the molecular structure of pitch. The blending pitches were determined using a NICOLETIS5 FT-IR spectrometer (Thermo Nicolet Corporation, America).

1 H-NMR analysis of blending pitches.
An NMR spectrometer (AVANCE III, Bruker, German) was used to examine the aromatic index (f a ) of the blending pitches. Actually, the f a of the blending pitches was determined using 1 H-NMR, with deuterated dimethyl sulfoxide as the solvent. Actually, the hydrogen type of pitch in 1 H-NMR is generally classied into H g (chemical shi from 0 to 1.0 ppm), H b (chemical shi from 1.0 ppm to 2.0 ppm), H a (chemical shi from 2.0 ppm to 4.5 ppm), and H ar (chemical shi from 6.5 ppm to 9.5 ppm). The method for the calculation of f a was according to the literature, 30-32 and presented as eqn (1), as follows: where X means for the ratio of saturated hydrogen to carbon atoms on the aromatic ring, which is usually 2.4 for coal pitch.
2.3.4 Polarized microscopy analysis of needle coke derived from the co-carbonization of CLP and anthracene oil. Polarized microscopy is one of the most important measurements to judge the microstructure of needle coke. Actually, the optical microstructure of coke (including metallurgy coke, pitch coke and needle coke) usually consists of mosaic structures (coarse mosaic structure, medium mosaic structure and ne mosaic structure), brous structures (coarse brous structures and ne brous structures) and leaet microstructures. The optical microstructure of the needle coke was determined using a polarized microscope (Axio Scope A1 pol, Carl Zeiss, German), and the identication standard of the optical microstructure of the needle coke was according to the literature. [33][34][35] 2.3.5 XRD analysis of needle coke derived from the cocarbonization of CLP and anthracene oil. The carbon microcrystalline parameters including content of ideal carbon crystal and stacking height of the carbon crystal are generally accepted as a common index to judge the quality of needle coke. Actually, the carbon microcrystal of the needle coke derived by the cocarbonization of CLP and anthracene oil was tested via the combination of a powder X-ray diffraction (PANalytical B.V., Netherlands) and the curve-tting method. The curve-tting standard was according to our previous studies. [33][34][35] 2.3.6 Raman spectrum analysis of needle coke derived from the co-carbonization of CLP and anthracene oil. The Raman spectroscopy and curve-tting method are usually used as a useful method to characterize the distribution of carbon microcrystals. Actually, the carbon microcrystals (determined by the combination of Raman spectroscopy and curve-tting method) include graphite crystals and amorphous carbon. The Raman spectrum of the needle coke was measured on a Raman spectrometer (LabRAM HR Evolution, JOBIN YVON, France), and the curve-tting standard was according to our previous research. [33][34][35] 2.3.7 SEM analysis of needle coke derived from the cocarbonization of CLP and anthracene oil. The morphology of the needle coke derived from the co-carbonization of CLP and anthracene oil was characterized by scanning electron microscopy ( P IGMA-HD, Carl Zeiss, Germany).

Results and discussion
3.1 FTIR analysis (molecular structure analysis) of the blending pitches FTIR was used to determine the molecular structure of the blending pitch. The FTIR spectra are presented in Fig. 2.
As shown in Fig. 2, the absorption peaks were extremely similar in the different blending pitch samples. As listed in the literature, 30-32 the absorption peak at around 3450 cm À1 is attributed to the vibration of the -OH functional groups. The vibration of the functional groups of aromatic hydrogen corresponds to the absorption peaks at around 3050 cm À1 . The absorption peaks in the range of 2800 cm À1 to 3000 cm À1 are caused by the vibration of -CH 3 and -CH 2 -. Furthermore, the oxygen-containing functional groups (C]O, C-O, and C]OOH) correspond to the absorption peaks at around 1000-1800 cm À1 . Actually, as shown in Fig. 2, the species of functional groups in the blending pitches were similar.

The aromatic index (f a ) of the blending pitches
In our previous studies, 27 aromatic index (f a ) was one of the key indices reecting the feasibility of raw pitch to produce highquality coal-based needle coke. Generally, the rened coal pitch with f a of 0.95-0.98 was suitable to prepare high-quality needle coke. The method for the calculation of f a for the raw pitch is according to eqn (1), which is also presented in the literature. [30][31][32] The 1 H-NMR graph of CLP and the distribution of f a in the series blending pitches are shown in Fig. 3.
As presented in Fig. 3(a-i), the 1 H-NMR spectra of the raw pitches can be divided into 4 types, corresponding to the aliphatic hydrogens in methyl or methylene groups in the gposition to an aromatic ring (H g ), aliphatic hydrogen in the methyl or methylene groups in the b-position to an aromatic ring (H b ), aliphatic hydrogen in methyl or methylene groups in the a-position to an aromatic ring (H a ) and aromatic hydrogen (H A ), respectively. The f a of each blending pitches was calculated according to the literature [30][31][32] and listed in Fig. 3(j). The f a of the blending pitches is in the range of 0.9507 to 0.9586, which is in the range of 0.95-0.98. Thus, these blending pitches are suitable to generate coal-based needle coke.

Preparation of green needle coke from blending pitches
The green needle coke was synthesized using different blending pitches via the co-carbonization method. A picture of the green needle coke is shown in Fig. 4.
As shown in Fig. 4, the green needle coke derived from the sole coal liquefaction pitch overowed at the mouth of the  mouth-tube, which is oen considered a "foam-like coke phenomenon". This phenomenon is attributed to the extremely reactive nature or ultra-high viscosity of the reaction system during the liquid-phase carbonization process. 37,38 In fact, the coal liquefaction pitch (CLP) was obtained from the coal direct liquefaction residue, and thus the average molecular weight of the CLP was relatively higher than that of the common pitch (such as high-temperature coal tar pitch and medium-lowtemperature pitch). Consequently, the reactivity of the pitch molecules in CLP was relatively low. Actually, the soening point and toluene insoluble but quinoline insoluble (b resin) of CLP were 158 C and 20.41% (listed in Table 1), respectively. Specically, the "foam-like coke phenomenon" in the needle coke derived from CLP was caused by the high viscosity of the reaction system in the liquid-phase carbonization process.
The green needle coke from the blending pitch of CLP-A 20% reached the mouth of the mouth-tube. The "foam-like coke phenomenon" of CLP-A 20% -C was obviously less than that of CLP-C. Furthermore, the more additive of anthracene oil in the blending pitch, the lower the "foam-like coke phenomenon" in the derived green needle coke. This phenomenon can be illustrated by the viscosity of the blending pitches. As listed in Table  1, the SP and TI of the blending pitch obviously decreased with an increase in the content of anthracene oil added (SP and TI of CLP-A 160% were 36 C and 8.80%, respectively). Consequently, the viscosity of the pitch system during the liquid-phase carbonization process was gradually reduced with an increase in the content of anthracene oil additive. The pyrolysis gas from the blending pitch during the liquid-phase carbonization could escape from the system, and thus the "foam-like coke phenomenon" of the green needle coke disappeared with the addition of anthracene oil.

Optical microstructure of needle coke derived from blending pitches
Polarized microscopy and the carbon theory are generally accepted as the common and useful method to determine the optical microstructure of needle coke. Generally, the distribution of the optical structure is accepted as one of the key indices to judge the quality of needle coke. Actually, the optical microstructure of the needle coke consisted of mosaic structures (including coarse mosaic structure, medium mosaic structure and ne mosaic structure), brous structures (coarse brous structure and ne brous structure) and leaet structures. 39 The typical optical microstructure of needle coke derived from blending pitch is presented in Fig. 5.
As reported in the literature, 39 the combination of polarized microscopy and carbon theory is recognized as a suitable method to statistically determine the content of each type of optical microstructure of the needle cokes. Actually, the classi-ed and statistic method was according to the literature, and the effective collection points were more than 500 points to guarantee the accuracy. The distribution of the optical microstructures of the needle coke derived from the different blending pitch samples is listed in Table 2.
As listed in the Table 2, the content of mosaic structure in CLP-C was 26.15%, which is the highest among the needle cokes derived from the co-carbonization of CLP and anthracene oil. In fact, the mosaic structure in needle coke is recognized as the component that is difficult to undergo graphitization during graphitization treatment. Specically, a lower content of mosaic structure in needle coke indicates a good graphitization property. Actually, the pitch coke with a content of mosaic structure lower than 24% can be classed as needle coke, where the lower content of mosaic structure indicates the good quality of the needle coke. As presented in Table 2, the content of mosaic structure gradually decreased with an increase in the ratio of the additive anthracene oil. This phenomenon can be attributed to the good viscosity of the blending pitches. In fact, the greater the ratio of anthracene oil, the lower the SP and TI in the blending pitches. A lower SP and TI always indicate a lower viscosity of the blending pitch. With an increase in the liquidphase carbonization temperature, the mobility of the pitch is enhanced. Consequently, the pyrolysis gas during the cocarbonization process easily escapes from the system in the same direction. Furthermore, the escape of the pyrolysis gas may promote the formation of a "domain-type mesophase" during the liquid-phase carbonization process. Thus, the content of mosaic structure obviously decreased with an increase in the content of anthracene oil.

The carbon microcrystalline of needle coke from X-ray diffraction
X-ray diffraction is usually used to characterize the carbon microcrystalline of needle coke. Generally, the combination of XRD and the curve-tting method is recognized as a suitable method for the quantitative analysis of the carbon microcrystalline of needle coke. The XRD graph and curve-tting curve of the needle cokes are shown in Fig. 6.
As presented in Fig. 6(a), the asymmetrically broad peak at around 26 is the typical characteristic peak of the ungraphitized carbon, which is also called the (002) peak. The diffraction position and shape of the (002) peak are similar for the series of needle cokes, but the intensity and width of the (002) peak   obviously varied for each sample. Actually, the higher intensity and narrower width of the (002) peak indicate the regular carbon microcrystalline structure of the needle coke. As reported in the literature, 40 the carbon microcrystalline parameters of needle coke can be determined by the combination of XRD and the curve-tting method. Generally, the (002) peak consisted of two symmetric peaks at around 22 and 26 , which are called the g-band and p-band, respectively. The peak area and 2q value of the p-band are the key data to calculate the parameters including Ig, Lc, N and n. Briey, Ig represents the content of ideal graphite carbon and Lc is the lateral size of the needle coke. N and n represent parallel layers and average number of aromatic rings in each layer, respectively. The formula employed for the calculation was also according to the literature, [33][34][35] and the carbon microcrystalline parameters of the needle cokes derived from the liquid-phase carbonization of the blending pitches are shown in Table 3.
As listed in Table 3, the Ig of CLP-C was 77.07%, which was the lowest in the needle coke series. However, CLP-A 160% -C had the highest Ig of 80.55%. In fact, the Ig of the derived needle cokes obviously increased with an increase in the additive ratio of anthracene oil in the blending pitches. The structural parameters of Lc, N and n in the needle coke series showed a similar trend to Ig. Actually, the Lc, N and n of the derived   needle cokes were in the range of 1.91-1.96 nm, 8.27-8.72, and 21.87-24.33, respectively. Obviously, the CLP-C and CLP-A 160% -C presented as the endpoint data (the CLP-C has the lowest point and CLP-A 160% -C has the highest point). This phenomenon can be illustrated by the physical-chemical property of the blending pitch, especially the viscosity of the blending pitch. As reported in the literature, due to the lower viscosity and good mobility of the raw pitch during the liquid-phase carbonization process, it was easier to generate a "domain mesophase" structure in the needle coke. Consequently, the carbon microcrystalline structure of the derived needle coke with a greater ratio of anthracene oil in the blending pitch was more regular, which is consistent with the optical microstructure of the needle coke.

Distribution of carbon microcrystalline of needle coke from Raman spectroscopy
Raman spectroscopy is also accepted as a practical method to judge the distribution of carbon microcrystalline structure in needle coke. The Raman spectra of the needle coke series are shown in Fig. 7.
As shown in Fig. 7(a), there were two obvious "hump pattern" peaks at around 1360 cm À1 and 1580 cm À1 , which were denoted as the "D" band and "G" band, respectively. These two typical peaks are the characteristic peaks of ungraphitized carbon materials and caused by the vibration of disordered carbon and ideal carbon crystals, respectively. However, the intensity and width of the vibration peaks in each needle coke sample were mixed, making it difficult to judge the distribution of the carbon microcrystalline structure in each needle coke sample.
As reported in the literature, 41 the "hump pattern" peaks of the needle cokes consisted of 5 isolated symmetrical peaks, which were named as the D1 band, D2 band, D3 band, D4 band and G band. Briey, the D3 band was caused by the vibration of amorphous carbon and the G band is ascribed to the ideal carbon crystal (also called graphite carbon crystal). Furthermore, the D1 band, D2 band and D4 band are attributed to the defective carbon microcrystalline structures (these types of carbon microcrystalline structures easily undergo graphitization at the graphitization temperature). The Raman spectrum of each needle coke was curve-tted into 5 isolated peaks ( Fig. 7(b)) according to the literature, 35 and the distribution of the carbon microcrystalline structures of each needle coke is listed in Table 4 (the parameters were calculated using the peak area).
As shown in Table 4, I G /I All and I D3 /I All correspond to the content of graphite carbon and content of amorphous carbon in the needle coke, respectively. CLP-C had the lowest I G /I All of 7.78%, whereas CLP-A 160% -C had the highest I G /I All of 10.42%. Specically, the content of graphite carbon obviously increased with an increase in the content of anthracene oil additive. On the contrary, the I D3 /I All of CLP-C, CLP-A 20% -C, CLP-A 40% -C, CLP-A 50% -C, CLP-A 80% -C, CLP-A 100% -C, CLP-A 120% -C, CLP-A 140% -C and CLP-A 160% -C was 12.12%, 11.45%, 11.81%, 11.64%, 11.77%, 11.61%, 11.71%, 11.57% and 11.45%, respectively. Specically, the content of amorphous carbon gradually decreased with an increase in the ratio of anthracene oil additive in the derived needle coke. Furthermore, the distribution of carbon microcrystalline structures in the derived needle coke was consistent with the results of the optical microstructure and XRD analysis, and the distribution of I G /I All and I D3 /I All in the needle coke series showed the opposite data trend.

Morphology of needle coke from Raman spectroscopy
Needle coke is a type of graphitized carbon material, which has a dominant morphology of graphitic structure. Scanning electron microscopy (SEM) was used as an important tool to investigate the morphology of the needle coke, and the SEM images of each needle coke are shown in Fig. 8.
As presented in Fig. 8, the morphology of CLP-C was dominantly a graphitic lamellar structure but some mosaic structures were also present, as shown in Fig. 7(a). The morphology of the needle cokes derived from the co-carbonization of CLP and anthracene oil was dominantly brous structure, graphitic lamellar structure and leaet structure, and hardly any defect structures or mosaic structures were observed. Specically, the mosaic structure in the co-carbonization needle cokes was less than that in CLP-C, and this result is consistent with the results from the optical microstructure. Actually, the anthracene oil additive may reduce the viscosity of the reaction system during the liquid-phase carbonization process. Thus, the pyrolysis gas could escape smoothly from the system in a same direction. Consequently, due to the microstructure of the needle coke, it was easier to generate a brous structure during the latter stage of the carbonization process. Specically, the co-carbonization of CLP and anthracene oil is a good method to enhance the quality of the derived needle coke.

Micro-strength of needle coke
Micro-strength is usually used to judge the strength of the carbon skeleton of needle coke. The micro-strength of the needle coke samples is listed in Table 5. As listed in Table 5, CLP-C had the highest micro-strength of 70.0%, whereas the micro-strength of the other needle coke samples derived from the blending pitches was lower than 70% but higher than 61%. According to the literature, 42 the mosaic structures (coarse mosaic, medium mosaic and ne mosaic) in coke contribute more to the micro-strength than brous structures or leaet structures. Actually, the brous structure or leaet structure has a higher orientation degree than the mosaic structures. The mosaic structure in the needle coke was observed to exhibit optical anisotropy but macroscopic isotropy. Consequently, the greater content of mosaic structure, the higher the micro-strength. The strength of the carbon skeleton has an important inuence on the property of the derived carbon materials, and thus the needle cokes with a microstrength higher than 61% can be considered as high-quality needle cokes.

True density of needle cokes
True density is recognized as a key parameter to judge the quality of the needle coke. Actually, the needle cokes used as raw materials to produce ultra-high graphite electrodes require a true density of higher than 2.10 g cm À3 at the calcination  temperature of 1450 C. [42][43][44] Obviously, a higher calcination temperature always results in a higher true density of needle coke. The true density of the needle coke derived from the blending pitches is listed in Table 6. As listed in Table 6, CLP-C had the lowest true density of 1.867 g cm À3 . The true density of CLP-A 20% -C, CLP-A 40% -C, CLP-A 50% -C, CLP-A 80% -C, CLP-A 100% -C, CLP-A 120% -C, CLP-A 140% -C and CLP-A 160% -C was 1.958 g cm À3 , 1.986 g cm À3 , 1.988 g cm À3 , 2.021 g cm À3 , 2.070 g cm À3 , 2.180 g cm À3 , 2.240 g cm À3 and 2.296 g cm À3 , respectively. Specically, the co-carbonization of CLP and anthracene oil is an essential method to enhance the true density of needle coke. In fact, the needle coke with a lower content of mosaic structure possesses a higher true density. The content of mosaic structures in the co-carbonization needle coke was much lower than that in CLP-C. Consequently, CLP-A 160% -C had the highest true density of 2.296 g cm À3 , which is in the range of high-quality needle coke according to the literature. 44,45

Conclusions
A series of needle coke samples was produced via the cocarbonization of coal liquefaction pitch and anthracene oil. The addition of the anthracene oil had a signicant effect on the viscosity and mobility of the blending pitch during the liquidphase carbonization process. The microstructure (including optical microstructure and carbon microcrystalline structure), micro-strength and true density were used as factors to judge the quality of the derived needle coke employing polarized microscopy, XRD and Raman spectroscopy, respectively. Accordingly, the co-carbonization of CLP and anthracene oil (mixture of CLP and anthracene oil at a suitable ratio) was a good method to produce high-quality needle coke. In fact, the content of brous structure and leaet structure in derived needle coke with the co-carbonization of CLP and anthracene oil reached 85.83%, the content of graphite carbon was 10.42% and the true density was as high as 2.296 g cm À3 . Thus, the cocarbonization of CLP and a moderate ratio of anthracene oil are a good method to generate high-quality coal-based needle coke.

Conflicts of interest
The authors declare that there is no conict of interest regarding the publication of this paper.