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Sequential production of H_2 and CO over supported Ni catalysts

机译:负载型Ni催化剂上H_2和CO的顺序生产

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Methane decomposition into H_2 and carbon nanofibers at 823 K and subsequent gasification of the carbon nanofibers with CO_2 into CO at 923 K were performed over supported Ni catalysts (Ni/SiO_2, Ni/TiO_2 and Ni/Al_2O_3). Supported Ni catalysts were deactivated for CH_4 decomposition with time on stream due to deposition of a large amount of carbon nanofibers. Subsequent contact of CO_2 with carbon nanofibers on the deactivated catalysts resulted in the formation of CO with a conversion of the carbons higher than 95%. In addition, gasification with CO_2 regenerated the activity of supported Ni catalysts for CH_4 decomposition, indicating that H_2 formation through CH_4 decomposition and CO formation through gasification with CO_2 could be carried out repeatedly. Conversions of carbon nanofibers into CO were kept higher than 95% in the repeated gasification over all the catalysts, while change in the catalytic activity for CH_4 decomposition with the repeated cycles depended on the kind of catalytic supports. Catalytic activity of Ni/SiO_2 for CH_4 decomposition was high at early cycles, however, the activity decreased gradually with the repeated cycles. On the other hand, Ni/TiO_2 and Ni/Al_2O_3 showed high activity for CH_4 decomposition and the activity was kept high during the repeated cycles. These changes of catalytic activities for CH_4 decomposition could be explained by changes in particle sizes of Ni metal, i.e. Ni metal particles in Ni/SiO_2 aggregated into ones larger than 150 nm with the repeated cycles, while the particle sizes of Ni metal in Ni/TiO_2 and Ni/Al_2O_3 remained at an effective range for CH_4 decomposition (60-100 nm).
机译:在负载型Ni催化剂(Ni / SiO_2,Ni / TiO_2和Ni / Al_2O_3)上,甲烷在823 K分解为H_2和碳纳米纤维,然后在923 K用CO_2将碳纳米纤维气化为CO。由于沉积了大量的碳纳米纤维,负载型Ni催化剂因在生产过程中随时间的流逝CH_4分解而失活。随后CO_2与碳纳米纤维在失活催化剂上的接触导致形成CO,且碳的转化率高于95%。另外,CO_2气化再生了负载型Ni催化剂的CH_4分解活性,表明CH_4分解生成H_2和CO_2气化生成CO可以重复进行。在所有催化剂上进行重复气化时,碳纳米纤维向CO的转化率均保持在95%以上,而随着重复循环的进行,CH_4分解的催化活性变化取决于催化载体的种类。 Ni / SiO_2对CH_4分解的催化活性较高,但随着循环次数的增加,活性逐渐降低。另一方面,Ni / TiO_2和Ni / Al_2O_3显示出对CH_4分解的高活性,并且在重复循环中保持高活性。 CH_4分解的催化活性的这些变化可以用Ni金属的粒径变化来解释,即Ni / SiO_2中的Ni金属颗粒在重复循环中聚集成大于150 nm的颗粒,而Ni / SiO TiO_2和Ni / Al_2O_3保持在CH_4分解的有效范围内(60-100 nm)。

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