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Boreskov Institute of Catalysis of the Siberian Branch of Russian ...

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PP-IV-33THE CATALYTIC HYDROGENATION OF COAL WITH ADDITIVESOF WIDE FRACTION OF COAL PITCHBaikenov M.I. 1 , Omarbekov T.B. 1 , Khrupov V.A. 2 , Meiramov M.G. 2 ,Amerkhanova Sh.K. 1 , Baikenova G.G. 3 , Shliyapov R.M. 1 , Uali A.S. 11 Buketov Каraganda state university, Karaganda, Kazakhstan2 OC «<strong>Institute</strong> <strong>of</strong> organic syn<strong>the</strong>sis and coal chemistry», Karaganda, Kazakhstan3 Kazakhstan -<strong>Russian</strong> university, Universitetskaya str., 28, Karaganda, 100028, Kazakhstan,tel./fax: 87212770374, e-mail: amerhanova@ok.kzNowadays works on processing coals to obtain liquid syn<strong>the</strong>tic fuel by destructivehydrogenation method is widely spread. According to this search <strong>of</strong> effective technologies <strong>of</strong>chemical processing heavy and hard hydrocarbon raw-material is actual. The aim <strong>of</strong> <strong>the</strong>nesearch was studying processes <strong>of</strong> <strong>the</strong> catalytic hydrogenation <strong>of</strong> coal with catalytic additives.As a hydrogen processes don a wide fraction <strong>of</strong> coal pitch from Shubarkol coalfield’s(Kazakhstan) coals was used in half-cocking process. Before carrying out <strong>the</strong> catalytichydrogenation <strong>the</strong> coal pitch was mechanochemically processed in cavitation-wave field.By <strong>the</strong> obtained data we can talk about high conversion degree <strong>of</strong> organic mass <strong>of</strong> coal andoutput <strong>of</strong> liquid products <strong>of</strong> coal: yield <strong>of</strong> fraction until 300°C is 60,4%, hydrogenate – 40,5%.Pyrite is an active catalyst, stechiometric pyrrotine is a working state <strong>of</strong> iron-sulfidecatalyst in <strong>the</strong> process <strong>of</strong> hydrogenation and as a result <strong>of</strong> reaction with molecular hydrogenatomic hydrogen is generated. However in /1-2/ works it is shown that iron sulfate is moreactive and surface sulfateFe O [ SO2−4] that is formed by oxidation <strong>of</strong> sulfide is active site <strong>of</strong>catalyst on <strong>the</strong> base <strong>of</strong> iron in coal hydrogenation processes. Thus, high activity <strong>of</strong> catalysts isalso explained by formation <strong>of</strong> iron complex23Fe O [ SO] . Formation <strong>of</strong> given complexacting as an active catalyst it is determined that with <strong>the</strong> help <strong>of</strong> electronic microscopy.Thus, comparative analysis <strong>of</strong> data on process <strong>of</strong> coal hydrogenation shows that chosenfraction <strong>of</strong> coal pitch by donor ability can be compared with traditional donor <strong>of</strong> hydrogen –tetraline. Also, it is determined that possibility <strong>of</strong> using new bifunctional catalysts for coalhydrogenation and wide fraction <strong>of</strong> coal pitch which have high selectivity to output <strong>of</strong> lightand middle fraction (300°C) with low amount <strong>of</strong> polycyclic hydrocarbons.References1. Wang Li, Huang Peng, Huang Mu-jie, Zheng jian-guo// Meiton xuebaoj <strong>of</strong> China Coal Soc. -1999.-Vol. 24.№4. –P. 420-423.2. Wei XY., Ogata E., Zong ZM., Zhou Sl., Liu JZ.// Fuel Process Technol. -200.-62.-P.103.232−4454

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