首页> 外文会议>International Conference on Multi-functional Materials and Structures >Bimetallic LaNi_(1-x)Co_xO_3 (x=0, 0.3, 0.5, 0.7, and 1) Perovskite Catalysts for Tar Reforming to Syngas
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Bimetallic LaNi_(1-x)Co_xO_3 (x=0, 0.3, 0.5, 0.7, and 1) Perovskite Catalysts for Tar Reforming to Syngas

机译:双金属LANI_(1-X)CO_XO_3(x = 0,0.3,0.5,0.7和1)钙钛矿催化剂用于合成气的焦油重整

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Perovskite-type oxide with transition metal as active site presented a promising potential catalyst for tar elimination in gasification process. LaNi_(1-x)Co_xO_3 (x= 0, 0.3, 0.5, 0.7, and 1) were prepared by sol-gel method. The XRD profiles of the calcined catalysts revealed the mixed metal oxide forms including LaNiO_3 and LaCoO_3 rhombohedral structures. Good dispersion of La, Ni, and Co with homogenous structure was observed in synthesized catalyst. The particle size and surface area were in the range of 12.64-21.86 μm and 3.89-11.69 m~2 /g, respectively. Activity of prepared catalysts on tar elimination was carried out using steam reforming of toluene as tar model compound at 500, 600, 700, and 800°C. Product distributions obtained from reforming reaction with LaNi_(1-x)Co_xO_3 were between 40.24-88.84% of gas, 10.99-59.59% of liquid, and 0.15-0.17% of solid. Conversion to CO and H_2 were found to increase with the reaction temperature. The maximum carbon and hydrogen conversion to syngas, CO and H_2, of approximately 78.42% and 83.49% with acceptable heating value were occurred at 800°C using LaNiO_3 as catalyst. Crystal structure of used catalysts clearly showed destruction of perovskite structure and transformation to metallic Ni and Co at effective temperature.
机译:与过渡金属作为活性位点的钙钛矿型氧化物提出了焦油消除气化过程有希望的潜在催化剂。 LaNi_(1-X)Co_xO_3(X = 0,0.3,0.5,0.7,以及1)通过溶胶 - 凝胶法制备。煅烧的催化剂的XRD谱分析结果发现该混合的金属氧化物的形式,包括LaNiO_3和LaCoO_3菱形结构。在合成的催化剂,观察到与均匀结构的La,Ni和Co的良好分散。粒径和表面积分别为分别12.64-21.86微米和3.89-11.69米〜2 /克的范围内,。上消除焦油制备的催化剂的活性进行了使用蒸汽在500甲苯作为焦油模型化合物的重整,600,700,和800℃。从重整用LaNi_(1-x)的反应Co_xO_3获得的产物分布均气体的40.24-88.84%,液10.99-59.59%,而固体0.15-0.17%之间。转化成CO和H_2中发现以增加与反应温度。使用LaNiO_3作为催化剂在800℃下发生的最大碳和氢转化成合成气,CO和H_2,约78.42%和83.49%具有可接受的热值。使用的催化剂的晶体结构清楚地表明钙钛矿结构和转化成金属Ni和Co的破坏在有效温度。

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