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Effect of support materials on the performance of Ni-based catalysts in tri-reforming of methane

机译:载体载体对甲烷三重整镍基催化剂性能的影响

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Tri-reforming of methane (TRM) utilizing CO2, H2O and O-2 is an emerging technique for the production of synthesis gas and CO2 abatement. Nevertheless, formulation and design of low-cost, active and stable catalyst for TRM is a major challenge due to its complex reaction network and rapid catalyst deactivation. The support effect is a critical factor influencing the activity and stability of supported Ni catalyst. Thus, a series of supported Ni catalysts over different metal oxides such as Al2O3, ZrO2, TiO2, SBA-15, MgO and CeO2-ZrO2 were prepared. The catalysts were characterized by using N-2 - physisorption, XRD, EDX, SEM, TEM, TPR, CO2 - TPD, NH3 - TPD, H-2 - pulse chemisorption and TGA. The performance of these catalysts was evaluated at 800 degrees C, 1 atm, WHSV 17220 mLh(-1) g(-1) and molar feed composition CH4:CO2:H2O:O-2:N-2 = 1:0.23:0.46:0.07:0.28 in a fixed-bed reactor. The initial activity of these catalysts followed the order: Ni/Al2O3 Ni/SBA-15 Ni/ZrO2 Ni/CeO2-ZrO2 Ni/TiO2 Ni/MgO. Ni/Al2O3 derived from spinet precursor NiAl2O4 resulted in well-dispersed smaller Ni particles, stronger metal-support interaction, a higher degree of reducibility and higher basic sites concentration, which led to its superior activity with 8.72 x 10(-2) mmol/g(cat).s, 2.31 x 10(-2) mmol/g(cat).s and 4.2 x 10(-2) mmol/g(cat).s CH4, CO2, and H2O conversion rate respectively. On the contrary, the stability of SBA-15 and ZrO2 supported Ni catalysts was remarkably high. Hexagonal porous network of SBA-15 confined Ni particles that resulted in high resistance against metal sintering and carbon deposition whereas Ni/ZrO2 offered resistance to Ni re-oxidation owing to its oxophilic property. Experimental investigations reveal that Ni/TiO2 and Ni/MgO resulted in poor CH4, CO2 and H2O conversion rates for TRM due to lower degree of reducibility. Furthermore, Ni/CeO2-ZrO2 catalyst had weak metal-support interaction as observed from TPR studies. Due to larger Ni crystallite size, it exhibited lower conversion compared to Ni/Al2O3, Ni/SBA-15, and Ni/ZrO2.
机译:利用CO2,H 2 O和O-2的甲烷(TRM)的三重整是一种用于生产合成气和CO2削减的新兴技术。然而,由于其复杂的反应网络和快速催化剂失活,但TRM的低成本,活性和稳定的催化剂的配方和设计是一种重大挑战。支持效应是影响支持Ni催化剂活性和稳定性的关键因素。因此,制备了一系列在不同金属氧化物上的一系列支持的Ni催化剂,例如Al 2 O 3,ZrO 2,TiO 2,SBA-15,MgO和CeO 2-ZrO2。通过使用N-2 - 物理吸附,XRD,EDX,SEM,TEM,TPR,CO 2 - TPD,NH3 - TPD,H-2 - 脉冲化学吸附和TGA来表征催化剂。在800℃,1atm,WHSV 17220mLH(-1)G(-1)和摩尔进料组合物CH 4:CO 2:H 2 O:O-2:N-2 = 1:0.23:0.46,评估这些催化剂的性能。 :固定床反应器中的0.07:0.28。这些催化剂的初始活性随后是命令:Ni / Al2O3& NI / SBA-15> ni / zro2& NI / CEO2-ZRO2> ni / tio2& NI / MgO。 Ni / Al2O3衍生自尖丝前体Nial2O4,得到井分散的较小的Ni颗粒,较强的金属载体相互作用,更高的还原性和较高的基本位点浓度,导致其具有8.72×10(2)mmol / g(猫).s,2.31 x 10(-2)mmol / g(cat).s和4.2 x 10(-2)mmol / g(cat)。s ch4,co2和h2o转换率。相反,SBA-15和ZrO 2支持的Ni催化剂的稳定性显着高。 SBA-15的六边形多孔网络限制Ni颗粒,导致金属烧结和碳沉积的高抗性,而Ni / ZrO2由于其乳化性能提供对Ni再氧化的抗性。实验研究表明,由于较低的还原性,Ni / TiO2和Ni / MgO导致TRM的CH 4,CO 2和H2O转化率差。此外,Ni / CeO 2-ZrO2催化剂具有从TPR研究中观察到的金属支持相互作用。由于Ni / Al 2 O 3,Ni / SBA-15和Ni / ZrO2相比,它表现出较低的转化率。

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