首页> 外文期刊>Journal of the Japan Petroleum Institute >Deep Hydrotreatment of Middle Distillates Obtained by Pyrolysis of Oil Shale and Oil Sands Bitumen
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Deep Hydrotreatment of Middle Distillates Obtained by Pyrolysis of Oil Shale and Oil Sands Bitumen

机译:油页岩和油砂沥青热解法获得的中间馏分的深度加氢处理

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Middle distillates obtained by pyrolysis of oil shale and oil sands bitumen were denitrogenated by complex formation with CuCl2·2H2O, which reduced the nitrogen contents from 9900 to 2700 wtppm and from 1300 to 700 wtppm, respectively, without any change in the sulfur contents. The original and denitrogenated oils were hydrotreated over a conventional NiMo catalyst in a fixed-bed continuous flow reactor. The pre-removal of nitrogen compounds greatly enhanced hydrodenitrogenation (HDN) and hydrodesulfurization (HDS), and the rate constants were increased by 4.9-27 for HDN and 2.8-5.4 for HDS. As a result, the nitrogen and sulfur contents of the denitrogenated oils were reduced to < 1 and < 10 wtppm, respectively, under the conditions of H2 8 MPa, LHSV 1 h~(-1) and 350℃.
机译:通过油页岩和油砂沥青热解获得的中间馏分与CuCl2·2H2O络合形成脱氮剂,氮含量分别从9900降低到2700 wtppm和从1300降低到700 wtppm,而硫含量没有任何变化。原始油和脱氮油在固定床连续流反应器中通过常规NiMo催化剂进行加氢处理。氮化合物的预去除大大提高了加氢脱氮(HDN)和加氢脱硫(HDS)的速度,HDN的速率常数提高了4.9-27,HDS的速率常数提高了2.8-5.4。结果,在H2 8 MPa,LHSV 1 h〜(-1)和350℃的条件下,脱氮油中的氮和硫含量分别降至<1和<10 wtppm。

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