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焙烧温度对Ni/CuO-ZrO2-CeO2-Al2O3催化剂在甲烷自热重整反应中积炭行为的影响
引用本文:蔡秀兰,李光炎,林维明. 焙烧温度对Ni/CuO-ZrO2-CeO2-Al2O3催化剂在甲烷自热重整反应中积炭行为的影响[J]. 化学物理学报, 2015, 28(2): 217-222
作者姓名:蔡秀兰  李光炎  林维明
作者单位:广东药学院药科学院,广州 510006,广东药学院药科学院,广州 510006,华南理工大学化学与化工学院,广州 510640
摘    要:
以Na2CO3为沉淀剂,在pH=9时,采用并流沉淀法制备了Ni/CuO-ZrO2-CeO2-Al2O3催化剂,催化剂中活性组分Ni的负载量(质量分数)为10%.采用TPO、SEM和XPS等方法研究了载体焙烧温度对催化剂积炭行为的影响.结果表明,载体焙烧温度为800 oC制备的Ni/CuO-ZrO2-CeO2-Al2O3催化剂不存在高温烧炭峰,可以避免由于积炭而降低反应的活性.反应40 h后,催化剂表面出现表面碳酸盐和非活性丝状积炭,这些物种可能会导致催化剂活性降低.

关 键 词:甲烷   自热重整   制氢   积炭
收稿时间:2014-11-10

Effect of Calcined Temperature on Coke Deposition for Autothermal Reforming of Methane with Ni-Cu Catalyst
Xiu-lan Cai,Guang-yan Li and Wei-ming Lin. Effect of Calcined Temperature on Coke Deposition for Autothermal Reforming of Methane with Ni-Cu Catalyst[J]. Chinese Journal of Chemical Physics, 2015, 28(2): 217-222
Authors:Xiu-lan Cai  Guang-yan Li  Wei-ming Lin
Affiliation:Guangdong Pharmaceutical University, Pharmacy College, Guangzhou 510006, China,Guangdong Pharmaceutical University, Pharmacy College, Guangzhou 510006, China and South China University of Technology, School of Chemistry and Chemical Engineering, Guangzhou 510640, China
Abstract:
Ni/CuO-ZrO2-CeO2-Al2O3 catalysts were prepared by co-precipitation method at pH=9 and using Na2CO3 as the precipitant. The Ni loading (mass fraction) of the catalysts was 10%. The catalysts were characterized by X-ray diffraction, temperature-programmed oxidation (TPO), scanning electron microscope (SEM), and X-ray photoelectron spectroscopy (XPS). The effects of calcined temperature of support on coke deposition were studied. TPO, SEM and XPS results indicated there was no peak of higher temperature oxygen consumption on Ni/CuO-ZrO2-CeO2-Al2O3catalyst (support was calcined at 800 oC), which could lead to the deactivation of the catalyst. The carbon species were carbonate and inactive carbon (filamentous carbon species) on the surface of catalyst reacting for 40 h which perhaps led to the deactivation of the catalyst.
Keywords:Methane   Autothermal reforming   Hydrogen   Coke deposition
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