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球磨时间对浆态床CO甲烷化Ni-Al_2O_3催化剂性能的影响
引用本文:莫文龙,肖艳,马凤云,钟梅,刘景梅,艾沙&#;努拉洪.球磨时间对浆态床CO甲烷化Ni-Al_2O_3催化剂性能的影响[J].分子催化,2017,31(4):356-364.
作者姓名:莫文龙  肖艳  马凤云  钟梅  刘景梅  艾沙&#;努拉洪
作者单位:煤炭洁净转化与化工过程新疆维吾尔自治区重点实验室新疆大学化学化工学院,新疆乌鲁木齐,830046
基金项目:国家高技术研究发展计划(863计划)项目(2015AA050502);新疆大学自然科学基金项目(BS160221).
摘    要:结合行星式球磨机,采用低温固相法制备Ni-Al_2O_3催化剂,考察了球磨时间对Ni-Al_2O_3催化剂晶相结构(XRD)、还原特征(H2-TPR)、孔道结构(BET)、粒径分布(PSD)、表面形貌(SEM)和浆态床CO甲烷化性能的影响.结果表明,球磨时间为60 min,催化剂(CT-60)平均粒径最小,为141 nm;比表面积最大,为329 m2/g.随球磨时间延长,Ni-Al_2O_3催化剂的甲烷化性能(CO转化率、CH_4选择性和CH_4收率)均先增加后减少.其中,球磨时间为60 min制备的催化剂(CT-60)甲烷化性能最佳,其CO转化率、CH_4选择性和CH_4收率分别达87.9%、8 6.8%和74.3%.结合催化剂表征可知,CT-60优异的性能与其具有较小的颗粒尺寸(141 nm)和较大的比表面积(329 m2·g-1)有很大的关联.即,催化剂颗粒尺寸越小,比表面积越大,其性能越好.

关 键 词:甲烷化  Ni-Al2O3催化剂  低温固相法  浆态床
收稿时间:2017/7/16 0:00:00
修稿时间:2017/7/20 0:00:00

Influence of Milling Time on the Performance of Ni-Al2O3 Catalyst for CO Methanation Based on Slurry-bed Reactor
MO Wen-long,XIAO Yan,MA Feng-yun,ZHONG Mei,LIU Jing-mei and AISHA&#;Nulahong.Influence of Milling Time on the Performance of Ni-Al2O3 Catalyst for CO Methanation Based on Slurry-bed Reactor[J].Journal of Molecular Catalysis (China),2017,31(4):356-364.
Authors:MO Wen-long  XIAO Yan  MA Feng-yun  ZHONG Mei  LIU Jing-mei and AISHA&#;Nulahong
Institution:Key Laboratory of Coal Clean Conversion & Chemical Engineering Process(Xinjiang Uyghur Autonomous Region), College of Chemistry and Chemical Engineering, Xinjiang University, Urumqi 830046, China,Key Laboratory of Coal Clean Conversion & Chemical Engineering Process(Xinjiang Uyghur Autonomous Region), College of Chemistry and Chemical Engineering, Xinjiang University, Urumqi 830046, China,Key Laboratory of Coal Clean Conversion & Chemical Engineering Process(Xinjiang Uyghur Autonomous Region), College of Chemistry and Chemical Engineering, Xinjiang University, Urumqi 830046, China,Key Laboratory of Coal Clean Conversion & Chemical Engineering Process(Xinjiang Uyghur Autonomous Region), College of Chemistry and Chemical Engineering, Xinjiang University, Urumqi 830046, China,Key Laboratory of Coal Clean Conversion & Chemical Engineering Process(Xinjiang Uyghur Autonomous Region), College of Chemistry and Chemical Engineering, Xinjiang University, Urumqi 830046, China and Key Laboratory of Coal Clean Conversion & Chemical Engineering Process(Xinjiang Uyghur Autonomous Region), College of Chemistry and Chemical Engineering, Xinjiang University, Urumqi 830046, China
Abstract:With planetary ball mill, the low temperature solid-state reaction method was used to prepare catalyst. The influence of milling time on the crystal structure (XRD), reduction performance (H2-TPR), pore structure (BET), particle size distribution (PSD), surface morphology (SEM) and CO methanation performance in slurry bed was investigated in this paper. Results showed that, at the milling time of 60 min, the average particle size of the catalyst (CT-60) was only about 141 nm, and the specific surface area was up to 329 m2/g. With the extension of milling time, the methanation performance (CO conversion, CH4 selectivity and CH4 yield) of the Ni-Al2O3 ca-talyst (CT-60) was increased firstly and then decreased as the milling time over 60 min. That is, the CT-60 catalyst prepared at the milling time of 60 min presented the best methanation performance, with CO conversion, CH4 selectivity and CH4 yield of 87.9%, 86.8% and 74.3% respectively. The excellent performance of CT-60 was strongly correlated with its small particle size (141 nm) and its specific surface area (329 m2·g-1). That is, the smaller the particle size of the catalyst, the larger the specific surface area, the better the performance.
Keywords:methanation  Ni-Al2O3  low temperature solid-state reaction  slurry-bed reactor
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