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首页> 外文期刊>Catalysis Letters >Precious Metal Doped Ni-Mg/Ceria-Zirconia Catalysts for Methane Conversion to Syngas by Low Temperature Bi-reforming
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Precious Metal Doped Ni-Mg/Ceria-Zirconia Catalysts for Methane Conversion to Syngas by Low Temperature Bi-reforming

机译:贵金属掺杂Ni-Mg /二氧化铈 - 氧化锆催化剂通过低温双重塑进行甲烷转化为合成气的催化剂

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摘要

Low temperature (450-600 A degrees C) bi-reforming of methane was studied over platinum (0.16 wt%) or palladium (0.13 wt%) along with nickel (1.4 wt%) and magnesium (1.0 wt%) immobilized onto a ceria-zirconia support (termed 0.16Pt and 0.13Pd). Bi-reforming studies using a feed ratio of 3:1:2 for CH4:CO2:H2O, respectively, showed that the H-2:CO ratio neared the desired ratio of 2 between 500 and 600 A degrees C for the 0.16Pt catalyst and consistent with bi-reforming at more traditional conditions. This H-2:CO ratio was desirable (near 2) compared to dry or steam reforming alone, as well as to other CH4:CO2:H2O ratios. Reaction studies showed that CH4 conversion decreased with increasing GHSV (68,000-272,000 h(-1)) at 500 A degrees C and increased with increasing temperature at a GHSV of 136,000 h(-1) for both catalyst systems. However, the Pt-based catalyst had more consistent H-2:CO ratios between 1.9 and 2.2 (T aeyen 500 A degrees C) compared to its Pd counterpart (H-2:CO ratios of 1.6-3.0), which was linked to the increased rWGS activity and stronger CO2 adsorption. This study indicates reasonable CH4 conversions and H-2:CO ratio near 2 can be achieved despite operating in this low temperature regime and may enable intensified processes for the conversion of methane to value-added products.
机译:在铂(0.16 wt%)或钯(0.13 wt%)以及镍(1.4 wt%)和镁(1.0 wt%)固定在氧化铈-氧化锆载体(称为0.16Pt和0.13Pd)上,研究了甲烷的低温(450-600℃)铋重整。分别使用CH4:CO2:H2O的进料比为3:1:2的Bi重整研究表明,对于0.16Pt催化剂,H-2:CO比在500到600摄氏度之间接近理想的2比,并且与更传统条件下的Bi重整一致。与单独的干重整或蒸汽重整以及其他CH4:CO2:H2O比率相比,该H-2:CO比率是理想的(接近2)。反应研究表明,对于两种催化剂系统,CH4转化率在500℃时随GHSV(68000-272000 h(-1))的增加而降低,在136000 h(-1)的GHSV下随温度的升高而升高。然而,与钯催化剂(H-2:CO比为1.6-3.0)相比,铂基催化剂的H-2:CO比在1.9和2.2之间(T ae;yen;500摄氏度)更稳定,这与rWGS活性增加和CO2吸附更强有关。这项研究表明,尽管在这种低温条件下运行,仍可以实现合理的CH4转化率和接近2的H-2:CO比率,并可能实现甲烷转化为增值产品的强化过程。

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