Methanation of CO2 over zeolite-promoted Ni/Al2O3 nanocatalyst under atmospheric pressure

被引:5
作者
Isah, Abdullahi [1 ,2 ]
Akanyeti, Ime [1 ,3 ]
Oladipo, Akeem Adeyemi [4 ]
机构
[1] Cyprus Int Univ, Environm Res Ctr, Via Mersin 10, Nicosia, North Cyprus, Turkey
[2] Cyprus Int Univ, Inst Grad Studies & Res, Environm Sci, Via Mersin 10, Nicosia, North Cyprus, Turkey
[3] Cyprus Int Univ, Engn Fac, Environm Engn, Via Mersin 10, Nicosia, North Cyprus, Turkey
[4] Eastern Mediterranean Univ, Fac Arts & Sci, Dept Chem, Polymer Mat Res Lab, Via Mersin 10, Famagusta, Tr North Cyprus, Turkey
关键词
CO2; methanation; Zeolite-promoter; Ni-based catalysts; Atmospheric pressure; CARBON-DIOXIDE; CATALYTIC-PROPERTIES; HYDROGENATION; CONVERSION; OXIDES; REDUCTION; CYCLE; GAS;
D O I
10.1007/s11144-020-01785-w
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Zeolite was added at different weight percentages as a promoter to 10% Ni/Al2O3 and tested under atmospheric pressure for CO2 methanation for the first time. The influence of operational conditions and stability of the catalysts were investigated. The highest CO2 conversion of 99% and CH4 selectivity of 56% were achieved with 2% zeolite added catalyst at 350 degrees C reaction temperature. The textural and morphological characteristics of the non-promoted and zeolite promoted catalysts were established with Scanning electron microscopy, Fourier transform infrared spectrophotometer, BET analyser and X-Ray diffractometer. The addition of 2% zeolite increased the specific surface area of the catalyst while sustaining similar Ni metal surface area to the non-promoted one. However, at higher zeolite content, the CH4 selectivity reduced considerably due to the reduced Ni dispersion and specific surface area. The calcination temperature of 400 degrees C, H-2/CO2 ratio of 4, GHSV of 72,000 SmL(gcat h)(-1) resulted in the highest CH4 selectivity. The 2% zeolite added catalyst demonstrated superior resistance to deactivation in comparison to the non-promoted catalyst showing potential as a low-cost catalyst for further optimization studies.
引用
收藏
页码:217 / 228
页数:12
相关论文
共 36 条
[1]   High-loaded nickel-alumina catalyst for direct CO2 hydrogenation into synthetic natural gas (SNG) [J].
Abello, Sonia ;
Berrueco, Cesar ;
Montane, Daniel .
FUEL, 2013, 113 :598-609
[2]   Sequential impregnation vs. sol-gel synthesized Ni/Al2O3-CeO2 nanocatalyst for dry reforming of methane: Effect of synthesis method and support promotion [J].
Aghamohammadi, Sogand ;
Haghighi, Mohammad ;
Maleki, Mahin ;
Rahemi, Nader .
MOLECULAR CATALYSIS, 2017, 431 :39-48
[3]   Synthesis of lanthanide series (La, Ce, Pr, Eu & Gd) promoted Ni/γ-Al2O3 catalysts for methanation of CO2 at low temperature under atmospheric pressure [J].
Ahmad, Waciar ;
Younis, Muhammad Naeem ;
Shawabkeh, Reyad ;
Ahmed, Shakeel .
CATALYSIS COMMUNICATIONS, 2017, 100 :121-126
[4]   CeO2 Promoted Ni-MgO-Al2O3 nanocatalysts for carbon dioxide reforming of methane [J].
Akbari, Ehsan ;
Alavi, Seyed Mehdi ;
Rezaei, Mehran .
JOURNAL OF CO2 UTILIZATION, 2018, 24 :128-138
[5]  
Aksoylu AE, 1997, APPL CATAL A-GEN, V164, P1
[6]   Sustainable Conversion of Carbon Dioxide: An Integrated Review of Catalysis and Life Cycle Assessment [J].
Artz, Jens ;
Mueller, Thomas E. ;
Thenert, Katharina ;
Kleinekorte, Johanna ;
Meys, Raoul ;
Sternberg, Andre ;
Bardow, Andre ;
Leitner, Walter .
CHEMICAL REVIEWS, 2018, 118 (02) :434-504
[7]   CO2 Hydrogenation Over Ni-Based Zeolites: Effect of Catalysts Preparation and Pre-reduction Conditions on Methanation Performance [J].
Bacariza, M. C. ;
Graca, I. ;
Westermann, A. ;
Ribeiro, M. F. ;
Lopes, J. M. ;
Henriques, C. .
TOPICS IN CATALYSIS, 2016, 59 (2-4) :314-325
[8]  
Bol RA, 1995, USE ZEOLITE MOL SIEV, P643
[9]  
Choe K, 2013, STUDY TRAPPING CO2 M, P421
[10]   Effect of sulfur on the catalytic performance of Fe-Ni/Al2O3 catalysts for light olefins production [J].
Feyzi, Mostafa ;
Khodaei, Mohammad Mehdi ;
Shahmoradi, Jahangir .
JOURNAL OF THE TAIWAN INSTITUTE OF CHEMICAL ENGINEERS, 2014, 45 (02) :452-460