Investigating methane dry reforming on Ni and B promoted Ni surfaces: DFT assisted microkinetic analysis and addressing the coking problem

被引:30
作者
Mohan, Ojus [1 ,2 ]
Shambhawi [3 ]
Lapkin, Alexei A. [3 ,4 ]
Mushrif, Samir H. [2 ]
机构
[1] Nanyang Technol Univ, Interdisciplinary Grad Sch, Energy Res Inst NTU, Singapore 637335, Singapore
[2] Univ Alberta, Dept Chem & Mat Engn, 9211-116 St Northwest, Edmonton, AB T6G 1H9, Canada
[3] Univ Cambridge, Dept Chem Engn & Biotechnol, Cambridge CB3 0AS, England
[4] Cambridge Ctr Adv Res & Educ Singapore Ltd, 1 Create Way,Create Tower 05-05, Singapore 138602, Singapore
基金
新加坡国家研究基金会; 加拿大自然科学与工程研究理事会;
关键词
WATER-GAS SHIFT; CRACKING REACTION; NI(111) SURFACE; CARBON-DIOXIDE; CATALYSTS; OXIDATION; SYNGAS; CH4; CO2; STABILITY;
D O I
10.1039/d0cy00939c
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
Dry reforming of methane (DRM) has incited significant academic and industrial attention in the past couple of decades. Although Ni-based catalysts have shown good activity for DRM, deactivation due to carbon formation is a serious concern. Several strategies are proposed, including doping by other metals and metalloids, to improve the stability of Ni, and hence we investigated boron-doped Ni (NiB) as a potential catalyst for DRM. In this work, we combined DFT and microkinetic modeling to identify the dominant reaction pathways and kinetically relevant steps of the DRM reaction system on Ni and NiB surfaces. We considered a detailed reaction network involving multiple CO2 and CH4 dissociation routes, side reactions (H2O formation, Boudouard reaction) and desorption of products on both surfaces. Our DFT calculations suggest that both Ni and NiB share similar CO2 (direct dissociation to CO*) and CH4 (sequential dehydrogenation to C*) activation routes. Compared to Ni, the CO2 activation barrier on NiB is higher by 44 kJ mol(-1) but the barriers in CH4 activation routes are significantly lower. Subsequently, the DFT-calculated energies were used to derive kinetic rate constants of the elementary reaction steps. These rate constants were employed to develop a microkinetic model of the DRM process over Ni (111) and NiB catalysts. At low CH4 and CO2 partial pressures (<10 kPa) and low total reaction pressure (1 bar) both CH4 dissociative adsorption and CO2 adsorption dominate the overall reaction rate. However, at high total reaction pressure (10 bar) and low reaction temperatures (873 and 973 K) only CH4 dissociation dominates the overall rate. As the temperature is increased (1073 K), it is dominated by the CH* oxidation. It was observed that the dominant pathway on Ni causes carbon formation on the catalyst surface. Whereas the dominant reaction pathway on NiB includes CH2* oxidation, that prevents carbon formation, making it a more stable catalyst. Furthermore, the forward rate constant of Boudouard reaction (CO2* + C* -> 2CO*) was significantly higher on NiB and hence the carbon formed is consumed at a faster rate. Thus, we believe that NiB is a potential catalyst that can resist deactivation during the DRM process.
引用
收藏
页码:6628 / 6643
页数:16
相关论文
共 42 条
[1]   Recent advances in dry reforming of methane over Ni-based catalysts [J].
Abdullah, Bawadi ;
Ghani, Nur Azeanni Abd ;
Vo, Dai-Viet N. .
JOURNAL OF CLEANER PRODUCTION, 2017, 162 :170-185
[2]   A review on catalyst development for dry reforming of methane to syngas: Recent advances [J].
Abdulrasheed, Abdulrahman ;
Jalil, Aishah Abdul ;
Gambo, Yahya ;
Ibrahim, Maryam ;
Hambali, Hambali Umar ;
Hamill, Muhamed Yusuf Shahul .
RENEWABLE & SUSTAINABLE ENERGY REVIEWS, 2019, 108 :175-193
[3]  
[Anonymous], 2009, Density Funct. Theory, DOI DOI 10.1002/9780470447710.CH2
[4]   Chemisorption of methane on Ni(100) and Ni(111) surfaces with preadsorbed potassium [J].
Bengaard, HS ;
Alstrup, I ;
Chorkendorff, I ;
Ullmann, S ;
Rostrup-Nielsen, JR ;
Norskov, JK .
JOURNAL OF CATALYSIS, 1999, 187 (01) :238-244
[5]   CO2 reforming of CH4 [J].
Bradford, MCJ ;
Vannice, MA .
CATALYSIS REVIEWS-SCIENCE AND ENGINEERING, 1999, 41 (01) :1-42
[6]   Descriptor Design in the Computational Screening of Ni-Based Catalysts with Balanced Activity and Stability for Dry Reforming of Methane Reaction [J].
Chen, Shuyue ;
Zaffran, Jeremie ;
Yang, Bo .
ACS CATALYSIS, 2020, 10 (05) :3074-3083
[7]   Identifying systematic DFT errors in catalytic reactions [J].
Christensen, Rune ;
Hansen, Heine A. ;
Vegge, Tejs .
CATALYSIS SCIENCE & TECHNOLOGY, 2015, 5 (11) :4946-4949
[8]   Controlling the CO oxidation rate over Pt/TiO2 catalysts by defect engineering of the TiO2 support [J].
Chua, Y. P. Gavin ;
Gunasooriya, G. T. Kasun Kalhara ;
Saeys, Mark ;
Seebauer, Edmund G. .
JOURNAL OF CATALYSIS, 2014, 311 :306-313
[9]   Microkinetic Modeling and Reduced Rate Expression of the Water-Gas Shift Reaction on Nickel [J].
de Carvalho, Thiago P. ;
Catapan, Rafael C. ;
Oliveira, Amir A. M. ;
Vlachos, Dionisios G. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2018, 57 (31) :10269-10280
[10]   Ni-Fe catalysts based on perovskite-type oxides for dry reforming of methane to syngas [J].
de Lima, SM ;
Assaf, JM .
CATALYSIS LETTERS, 2006, 108 (1-2) :63-70