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首页> 外文期刊>Fuel Processing Technology >Integrated coal pyrolysis with CO2 reforming of methane over Ni/MgO catalyst for improving tar yield
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Integrated coal pyrolysis with CO2 reforming of methane over Ni/MgO catalyst for improving tar yield

机译:Ni / MgO催化剂上的煤热解与CO2重整甲烷甲烷以提高焦油收率

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摘要

A new process to integrate coal pyrolysis with CO2 reforming of methane over Ni/MgO catalyst was put forward for improving tar yield. And several Chinese coals were used to confirm the validity of the process. The experiments were performed in an atmospheric fixed-bed reactor containing upper catalyst layer and lower coal layer to investigate the effect of pyrolysis temperature, coal properties, Ni loading and reduction temperature of Ni/MgO catalysts on tar, water and char yields and CH4 conversion at fixed conditions of 400 ml/min CH4 flow rate, 1:1 CH4/CO2 ratio, 30 min holding time. The results indicated that higher tar yield can be obtained in the pyrolysis of all four coals investigated when coal pyrolysis was integrated with CO2 reforming of methane. For PS coal, the tar, water and char yield is 33.5,25.8 and 69.5 wt.%, respectively and the CH4 conversion is 16.8%, at the pyrolysis temperature of 750 °C over 10 wt.% Ni/MgO catalyst reduced at 850 °C. The tar yield is 1.6 and 1.8 times as that in coal pyrolysis under H2 and N2, respectively.
机译:提出了在Ni / MgO催化剂上将煤热解与甲烷CO2重整相结合的新工艺,以提高焦油收率。并使用了几种中国煤来确认该过程的有效性。在包含上催化剂层和下煤层的常压固定床反应器中进行实验,以研究热解温度,煤性质,Ni负载量和Ni / MgO催化剂的还原温度对焦油,水和焦炭收率和CH4转化率的影响。在固定条件下,CH4流速为400 ml / min,CH4 / CO2比为1:1,保持时间为30分钟。结果表明,将煤热解与甲烷的CO2重整结合使用时,在所研究的所有四种煤的热解中均可获得更高的焦油收率。对于PS煤,在750°C的热解温度下,在850℃下还原10%(重量)的Ni / MgO催化剂时,焦油,水和焦炭的产率分别为33.5、25.8和69.5 wt。%,CH4转化率为16.8%。 ℃。在H2和N2下,焦油产率分别是煤热解的1.6倍和1.8倍。

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