Hydroprocessing of low temperature coal tar on NiW/γ-Al2O3catalyst
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摘要: 以γ-Al2O3为载体,采用等体积浸渍法制备了不同Ni/W原子比的低温煤焦油加氢处理催化剂,并以BET、XRD、H2-TPR和TG对催化剂进行表征。在固定床反应器中,以低温煤焦油小于350 ℃馏分作为原料对催化剂进行了加氢性能的评价,并采用蒸馏、GC/MS、荧光指示剂吸附及元素分析对原料及产物的馏分分布及组成进行了分析。结果表明,NiO和WO3在载体上形成了均匀分散,NiO含量较低时与γ-Al2O3有较强的作用力而难以还原。当Ni/W原子比为0.38时,酚类化合物的转化率、航煤馏分选择性以及产物中环烷烃和氢化芳烃的含量均最高,加氢脱硫(HDS)活性、加氢脱氮(HDN)活性及产物的H/C原子比也最高,说明Ni/W原子比为0.38时,NiW/γ-Al2O3催化剂对煤焦油加氢处理具有较好的效果。Abstract: γ-Al2O3 supported catalysts with different Ni/W atomic ratios for the hydroprocessing of low temperature coal tar (LTCT) were prepared and characterized by BET, XRD, H2-TPR and TG analysis. The hydroprocessing of <350 ℃ fraction of LTCT was carried out in a fixed-bed reactor. The product distribution and composition were analyzed by distillation, GC/MS, fluorescent indicator adsorption and elementary analysis. The results show that NiO and WO3 are evenly distributed on the support surface; and low-loading NiO is difficult to reduce since the strong force is formed with the support surface. The phenol conversion, the selectivity of kerosene fraction and the content of naphthene and hydro-aromatic in the product are the highest at a Ni/W atomic ratio of 0.38, while the activities of HDS and HDN and the H/C atomic ratio in the product are also the best. It indicates that the NiW/γ-Al2O3 catalyst with an optimum Ni/W atomic ratio of 0.38 is appropriate for the hydroprocessing of LTCT.
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Key words:
- low temperature coal tar /
- hydroprocessing /
- catalyst
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肖瑞华. 煤焦油化工学[M]. 北京: 冶金工业出版社, 2002. (XIAO Rui-hua. Chemical engineering of coal tar[M]. Beijing: Metallurgical Industry Press, 2002.) 舒歌平, 史士东, 金嘉璐. 气化焦油加氢制汽油、柴油研究[J]. 煤化工, 1998, (2): 34-39. (SHU Ge-ping, SHI Shi-dong, JIN Jia-lu. Study on hydrogenation of gasification tar to produce gasoline and diesel oil[J]. Coal Chemical Industry, 1998, (2): 34-39.) 黄谦昌. 煤气化焦油加工制取汽油和柴油的研究[J]. 煤炭转化, 1995, 18(4): 75-83. (HUANG Qian-chang. Study on making gasoline and diesel fuel from coal-gasified tar[J]. Coal Conversion, 1995, 18(4): 75-83.) 何国峰, 陈贵峰, 关北峰, 史士东. 低温热解焦油馏分加氢精制的研究[J]. 煤炭转化, 1998, 21(1): 49-53. (HE Guo-feng, CHEN Gui-feng, GUAN Bei-feng, SHI Shi-dong. Study on hydrogen refining coal tar fractions distilled[J]. Coal Conversion, 1998, 21(1): 49-53. 燕京, 吕才山, 刘爱华, 达建文. 高温煤焦油加氢制取汽油和柴油[J]. 石油化工, 2006, 35(1): 33-36. (YAN Jing, LV Cai-shan, LIU Ai-hua, DA Jian-wen. Production of gasoline and diesel oil by hydrogenation of high temperature coal tar[J]. Petrolchemical Technology, 2006, 35(1): 33-36.) 付晓东. 煤气化副产品焦油的加氢转化[J]. 化学工程师, 2005, (4): 53-56. (FU Xiao-dong. Hydrogenization transform for coal tar’s[J]. Chemical Engineer, 2005, (4): 53-56.) 吕子胜, 王守峰. 用低温煤焦油生产柴油的研究[J]. 燃料与化工, 2002, 33(2): 81-82. (LV Zi-sheng, WANG Shou-feng. Production of diesel from low temperature coal tar[J]. Fuel & Chemical Processes, 2002, 33(2): 81-82.) 屈明达, 鄂忠明. 煤焦油的加氢处理[J]. 化工技术经济, 2005, 23(6): 49-53. (QU Ming-da, E Zhong-ming. Coal tar oil hydrogenation[J]. Chemical Techno-Economics, 2005, 23(6): 49-53.) 李增文. 煤焦油加氢工艺技术[J]. 化学工程师, 2009, (10): 57-62. (LI Zeng-wen. Hydrogenation technology of coal tar[J]. Chemical Engineer, 2009, (10): 57-62.) 陈松, 许杰, 方向晨. 煤焦油联合加氢裂化处理工艺及其专用催化剂[J]. 现代化工, 2009, 29(3): 64-69. (CHEN Song, XU Jie, FANG Xiang-chen. United hydrocracking process for treating coal tar oil and its special catalyst[J]. Modern Chemical Industry, 2009, 29(3): 64-69.) BALSTER L M, CORPORAN E, DeWITT M J, EDWARDS J T, ERVIN J S, GRAHAM J L, LEE S Y, PAL S, PHELPS D K, RUDNICK L R, SANTORO R J, SCHOBERT H H, SHAFER L M, STRIEBICH R C, WEST Z J, WILSON G R, WOODWARD R, ZABARNICK S. Development of an advanced, thermally stable, coal-based jet fuel [J]. Fuel Process Technol, 2008, 89(4):364-378. ESER S, SONG C, COPENHAVER R, PERISON J, SCHOBERT H. Production of jet fuels from coal-derived liquids.DOE Report DOE/PC/90014, Washington DC, 1988: 1-3. SONG C, LAI W C, SCHOBERT H H. Hydrogen transferring pyrolysis of long-chain alkanes and thermal stability improvement of jet fuels by hydrogen donors [J]. Ind Eng Chem Res, 1994, 33(3): 548-557. YOON E M, SELVARAJ L, SONG C, STALLMAN J B, COLEMAN M M. High-temperature stabilizers for jet fuels and similar hydrocarbon mixtures: 1 Comparative studies of hydrogen donors[J]. Energy Fuels, 1996, 10(3): 806-811. YOON E M, SELVARAJ L, ESER S, COLEMAN M M. High-temperature stabilizers for jet fuels and similar hydrocarbon mixtures: 2 Kinetic studies [J]. Energy Fuels, 1996, 10(3): 812-815. STROHM J J, BUTNARK S, KEYSER T L, ANDRSEN J M, BADGER M W, SCHOBERT H H, SONG C. The use of coal pyrolysis products for the development of thermally stable jet fuels[J]. Prepr Pap Am Chem Soc Div Fuel Chem, 2004, 47(1): 177-178. SCHOBERT H H, BADGER M W, SANTORO R J. Progress toward coal-based JP-900 [J]. Prepr Pap Am Chem Soc Div Pet Chem, 2002, 47(3): 192-194. GRANGE P, VANHAEREN X. Hydrotreating catalysts, an old story with new challenges [J]. Catal Today, 1997, 36(4):375-391. DING L, ZHENG Y, ZHANG Z, RING Z, CHEN J. Hydrotreating of light cycle oil using WNi catalysts containing hydrothermally and chemically treated zeolite Y [J]. Catal Today, 2007, 125(3/4): 229-238. 黄华, 尹笃林, 文建军, 张茂昆, 徐斌. Ni含量对镍催化剂芳烃加氢抗硫性能的影响[J]. 工业催化, 2005, 13(1): 13-16. (HUANG Hua, YIN Zhu-lin, WEN Jian-jun, ZHANG Mao-kun, XU Bin. Effect of nickel content on sulfur tolerance of nickel-based catalysts for aromatic hydrogenation[J]. Industry Catalysis, 2005, 13(1): 13-16.) ZUO D, LI D, NIE H,SHI Y, LACROIX M, VRINAT M. Acid-base properties of NiW/Al2O3 sulfided catalysts: Relationship with hydrogenation, isomerization and hydrodesulfurization reactions[J]. J Mol Catal A, 2004, 211(1/2): 179-189. ZUO D, VRINAT M, NIE H, MAUGF, SHI Y, LACROIX M, LI D. The formation of the active phases in sulfided NiW/Al2O3catalysts and their evolution during post-reduction treatment[J]. Catal Today, 2004, 93-95: 751-760. DUGULAN A I, HENSEN E J M, van VEEN J A R. Effect of pressure on the sulfidation behavior of NiW catalysts: A 182W Mössbauer spectroscopy study[J]. Catal Today, 2010, 150(3/4): 224-230. ALSOBAAI A M, ZAKARIA R, HAMEED B H. Gas oil hydrocracking on NiW/USY catalyst: Effect of tungsten and nickel loading[J]. Chem Eng J, 2007, 132(1/3): 77-83. SAHOO S K, VISWANADHAM N, RAY N, GUPTA J K, SINGH I D. Studies on acidity, activity and coke deactivation of ZSM-5 during n-heptane aromatization[J]. Appl Catal A, 2001, 205(1/2):1-10. ANTUNES A P, RIBEIRO M F, SILVA J M, RIBEIRO F R, MAGNOUX P, GUISNET M. Catalytic oxidation of toluene over CuNaHY zeolites: Coke formation and removal[J]. Appl Catal B, 2001, 33(2): 149-164.
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