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焙烧温度对球状Ni-Al纳米催化剂结构及生物质催化热解的影响研究
引用本文:王士铎,张晓东,杨双霞,冯洪庆,周于翔,王迪. 焙烧温度对球状Ni-Al纳米催化剂结构及生物质催化热解的影响研究[J]. 太阳能学报, 2022, 43(9): 376-381. DOI: 10.19912/j.0254-0096.tynxb.2020-1365
作者姓名:王士铎  张晓东  杨双霞  冯洪庆  周于翔  王迪
作者单位:1.中国石油大学(华东)新能源学院,青岛 266580;2.集美大学机械与能源工程学院,厦门 361021;3.齐鲁工业大学(山东省科学院)能源研究所山东省生物质气化技术重点实验室,济南 250014
基金项目:国家自然科学基金(51876108)
摘    要:采用水热法制备三维Ni-Al纳米结构催化剂,并利用多种表征手段和稻壳催化热解实验研究焙烧温度(500~800 ℃)对催化剂的整体结构及催化性能的影响。结果表明:催化剂为球状结构,活性位点分布均匀,焙烧温度对材料结构有显著影响,800 ℃焙烧条件下球状结构有向内塌陷的趋势。相较于无催化条件下的稻壳热解产物,催化热解后焦油产率明显减小,产气量大幅提高。500 ℃焙烧制备的Ni-Al催化剂作用条件下,稻壳热解气体产物中H2/CO最大可达2.66,600 ℃焙烧条件下可获得最大合成气产量737 mL/g,而700 ℃焙烧条件下可获得最低的焦油产率(13.5%)。材料表征发现,反应后的催化剂仍具有稳定的球状结构与活化性能。

关 键 词:焙烧  Ni-Al催化剂  生物质  热解  
收稿时间:2020-12-21

EFFECT OF CALCINATION TEMPERATURES ON STRUCTURE AND BIOMASS CATALYTIC PYROLYSIS OF SPHERE-LIKE Ni-Al NANOCATALYSTS
Wang Shiduo,Zhang Xiaodong,Yang Shuangxia,Feng Hongqing,Zhou Yuxiang,Wang Di. EFFECT OF CALCINATION TEMPERATURES ON STRUCTURE AND BIOMASS CATALYTIC PYROLYSIS OF SPHERE-LIKE Ni-Al NANOCATALYSTS[J]. Acta Energiae Solaris Sinica, 2022, 43(9): 376-381. DOI: 10.19912/j.0254-0096.tynxb.2020-1365
Authors:Wang Shiduo  Zhang Xiaodong  Yang Shuangxia  Feng Hongqing  Zhou Yuxiang  Wang Di
Affiliation:1. College of New Energy, China University of Petroleum (East China), Qingdao 266580, China;2. College of Mechanical and Energy Engineering, Jimei University, Xiamen 361021, China;3. Shandong Provincial Key Laboratory of Biomass Gasification Technology, Energy Research Institute, Qilu University of Technology (Shandong Academy of Sciences), Ji'nan 250014, China
Abstract:Four three-dimensional Ni-Al catalysts with different calcination temperatures (500-800 ℃) were prepared by a hydrothermal method, and the structure and catalytic performance of synthesized catalysts were studied by various characterizations and rice husk catalytic pyrolysis experiments. The results show that the catalyst has a sphere-like structure with uniform distribution of Ni-based active sites, but the spherical structure tends to collapse inward when the calcination temperature was 800 ℃. Compared with non-catalytic pyrolysis, the tar yield decreased and the syngas increased significantly after catalytic pyrolysis. The maximum H2/CO ratio of 2.66 could be obtained when the Ni-Al catalysts was calcined at 500 ℃ and the maximum syngas yield of 737 mL/g could be obtained at 600 ℃, and the minimum liquid yield percentage of 13.5% could obtained at 700 ℃. The used Ni-Al catalyst exhibited a stable spherical structure and active performance after reaction based on the structure characterization.
Keywords:calcination  Ni-Al catalyst  biomass  pyrolysis  
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