Effect of Ce and Zn on Cu-Based Mesoporous Carbon Catalyst for Methanol Steam Reforming

被引:17
作者
Bepari, Sujoy [1 ]
Khan, Mudasar [1 ]
Li, Xin [1 ,2 ]
Mohammad, Nafeezuddin [2 ]
Kuila, Debasish [1 ,2 ]
机构
[1] North Carolina A&T State Univ, Chem Dept, Appl Sci & Technol, Greensboro, NC 27411 USA
[2] North Carolina A&T State Univ, Joint Sch Nanosci & Nanoengn, Greensboro, NC 27411 USA
基金
美国国家科学基金会;
关键词
Steam reforming; Hydrogen; Mesoporous carbon; Cu-Zn; Cu-Ce catalyst; FUEL-CELL; HYDROGEN-PRODUCTION; CO OXIDATION; LOW-TEMPERATURE; H-2; PRODUCTION; SN CATALYSTS; PERFORMANCE; NI; ETHANOL; PHASE;
D O I
10.1007/s11244-022-01772-6
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
Hydrogen is a clean renewable energy with potential for future environmental sustainability. The main challenge in hydrogen production via methanol steam reforming (MSR) is carbon monoxide (CO) formation that deactivates the catalyst. In this study, the effect of zinc (Zn) and cerium (Ce) on copper-mesoporous carbon (MC)-catalyst (Cu-MC) for MSR was investigated. The highest surface area (380.5 m(2)/g), observed for the Cu-MC prepared by one-pot (OP), decreased after incorporation of Ce and Zn. The temperature programmed reduction (H-2-TPR) studies showed a decrease in the reduction temperature of CuO. The metal oxides were well distributed over the MC support based on scanning electron microscopy (SEM) and transmission electron microscopy (TEM) studies. The MSR studies yielded methanol conversion of 65 and 68% for Ce-loaded Cu-MC prepared by OP and wet-impregnation (WI) methods at 300 & DEG;C and 250 ?, respectively. Addition of Zn to Cu-MC decreased methanol conversion, significantly, to 46%, at 300 ?. Both catalysts showed higher hydrogen selectivity, > 90%, with a lower CO selectivity for the Zn-Cu-MC catalyst. The Ce-Cu-MC (WI) catalyst showed good stability for 42 h with high H-2 selectivity, > 90%, and methanol conversion of 40% at 250 ?. [Graphics]
引用
收藏
页码:375 / 392
页数:18
相关论文
共 83 条
[51]   Atomic Layer Deposition of Cobalt Catalyst for Fischer-Tropsch Synthesis in Silicon Microchannel Microreactor [J].
Mohammad, Nafeezuddin ;
Aravamudhan, Shyam ;
Kuila, Debasish .
NANOMATERIALS, 2022, 12 (14)
[52]   Scale-up of high-pressure F-T synthesis in 3D printed stainless steel microchannel microreactors: Experiments and modeling [J].
Mohammad, Nafeezuddin ;
Chukwudoro, Chiemeka ;
Bepari, Sujoy ;
Basha, Omar ;
Aravamudhan, Shyam ;
Kuila, Debasish .
CATALYSIS TODAY, 2022, 397 :182-196
[53]   Fischer-Tropsch studies in a 3D-printed stainless steel microchannel microreactor coated with cobalt-based bimetallic-MCM-41 catalysts [J].
Mohammad, Nafeezuddin ;
Abrokwah, Richard Y. ;
Stevens-Boyd, Robert G. ;
Aravamudhan, Shyam ;
Kuila, Debasish .
CATALYSIS TODAY, 2020, 358 :303-315
[54]   Kinetics of Fischer-Tropsch Synthesis in a 3-D Printed Stainless Steel Microreactor Using Different Mesoporous Silica Supported Co-Ru Catalysts [J].
Mohammad, Nafeezuddin ;
Bepari, Sujoy ;
Aravamudhan, Shyam ;
Kuila, Debasish .
CATALYSTS, 2019, 9 (10)
[55]  
Monshi A., 2012, World J.Nano Sci. Eng, V02, P154, DOI [DOI 10.4236/WJNSE.2012.23020, https://doi.org/10.4236/wjnse.2012.23020]
[56]   TEMPERATURE-PROGRAMMED REDUCTION - PARAMETRIC SENSITIVITY AND ESTIMATION OF KINETIC-PARAMETERS [J].
MONTI, DAM ;
BAIKER, A .
JOURNAL OF CATALYSIS, 1983, 83 (02) :323-335
[57]   Steam reforming of methanol over Cu/CeO2/ZrO2 catalysts [J].
Oguchi, H ;
Nishiguchi, T ;
Matsumoto, T ;
Kanai, H ;
Utani, K ;
Matsumura, Y ;
Imamura, S .
APPLIED CATALYSIS A-GENERAL, 2005, 281 (1-2) :69-73
[58]   Production of hydrogen via partial oxidation of methanol over bimetallic Au-Cu/TiO2 catalysts [J].
Ou, Ti-Cheng ;
Chang, Feg-Wen ;
Roselin, L. Selva .
JOURNAL OF MOLECULAR CATALYSIS A-CHEMICAL, 2008, 293 (1-2) :8-16
[59]   Methanol steam reforming for hydrogen production [J].
Palo, Daniel R. ;
Dagle, Robert A. ;
Holladay, Jamie D. .
CHEMICAL REVIEWS, 2007, 107 (10) :3992-4021
[60]   Synthesis and characteristics of MCM-41 supported CoRu catalysts [J].
Panpranot, J ;
Goodwin, JG ;
Sayari, A .
CATALYSIS TODAY, 2002, 77 (03) :269-284