Quantitative imaging of carbon in heterogeneous refining catalysts

被引:9
作者
Jolivet, L. [1 ,2 ]
Motto-Ros, V [2 ]
Sorbier, L. [1 ]
Sozinho, T. [1 ]
Lienemann, C-P [1 ]
机构
[1] IFP Energies Nouvelles, BP 3, F-69360 Solaize, France
[2] Univ Lyon 1, Univ Lyon, CNRS, Inst Lumiere Matiere UMR 5306, F-69622 Villeurbanne, France
关键词
INDUCED BREAKDOWN SPECTROSCOPY; ZEOLITE H-ZSM-5; ELEMENTS; COKE; DEACTIVATION; REGENERATION; SPECTROMETRY; PERFORMANCE; CONVERTERS; METHANOL;
D O I
10.1039/c9ja00434c
中图分类号
O65 [分析化学];
学科分类号
070302 ; 081704 ;
摘要
Heterogeneous catalyst materials are the core of crude oil purification process performance. Catalyst deactivation, which is a result of crude impurity deposits into catalyst pores during this process, is therefore a major concern during refining. However, deactivation mechanisms are not easily investigated, as they involve carbon transport phenomena over a large range of concentrations, typically from hundreds of ppm to tens of mass%. Spatially resolved analysis of carbon conducted at the entire grain scale (similar to mm(2)) with a micrometric resolution is therefore of primary importance to better predict, control, and further improve the purification processes. However, usual spatially resolved approaches are not easily suitable for mm(2)-scale analysis and/or not adequate in terms of carbon detection limits. In this work, we propose a quantitative methodology dedicated to carbon spatially resolved analysis and the evaluation of its analytical performance. This approach, based on laser-induced breakdown spectroscopy (LIBS), allows for the first time 2D imaging of carbon at different process times as well as quantitative profiling of carbon diffusion over more than two orders of magnitude in concentration.
引用
收藏
页码:896 / 903
页数:8
相关论文
共 40 条
[1]   Catalytic Behaviour of Ce-Doped Ni Systems Supported on Stabilized Zirconia under Dry Reforming Conditions [J].
Al-Fatesh, Ahmed Sadeq ;
Arafat, Yasir ;
Ibrahim, Ahmed Aidid ;
Kasim, Samsudeen Olajide ;
Alharthi, Abdulrahman ;
Fakeeha, Anis Hamza ;
Abasaeed, Ahmed Elhag ;
Bonura, Giuseppe ;
Frusteri, Francesco .
CATALYSTS, 2019, 9 (05)
[2]  
Ancheyta J., 2009, ASPHALTENE CHEM TRAN
[3]  
[Anonymous], RAFFINAGE CONVERSION
[4]  
[Anonymous], 2000, T60115 AFNOR NF
[5]   Heterogeneous Catalyst Deactivation and Regeneration: A Review [J].
Argyle, Morris D. ;
Bartholomew, Calvin H. .
CATALYSTS, 2015, 5 (01) :145-269
[6]   Asphaltenes Transport into Hydroconversion Catalysts at High Temperature: Role of the Alumina Nanoporous Texture [J].
Barbier, Jeremie ;
Gaulier, Florine ;
Guichard, Bertrand ;
Levitz, Pierre ;
Espinat, Didier .
ENERGY & FUELS, 2017, 31 (07) :7426-7437
[7]   Characterization of Coke on a Pt-Re/γ-Al2O3 Re-Forming Catalyst: Experimental and Theoretical Study [J].
Bare, Simon R. ;
Vila, F. D. ;
Charochak, Meghan E. ;
Prabhakar, Sesh ;
Bradley, William J. ;
Jaye, Cherno ;
Fischer, Daniel A. ;
Hayashi, S. T. ;
Bradley, Steven A. ;
Rehr, J. J. .
ACS CATALYSIS, 2017, 7 (02) :1452-1461
[8]   Mechanisms of catalyst deactivation [J].
Bartholomew, CH .
APPLIED CATALYSIS A-GENERAL, 2001, 212 (1-2) :17-60
[9]   Catalyst deactivation by coke formation in microporous and desilicated zeolite H-ZSM-5 during the conversion of methanol to hydrocarbons [J].
Bleken, Francesca Lonstad ;
Barbera, Katia ;
Bonino, Francesca ;
Olsbye, Unni ;
Lillerud, Karl Petter ;
Bordiga, Silvia ;
Beato, Pablo ;
Janssens, Ton V. W. ;
Svelle, Stian .
JOURNAL OF CATALYSIS, 2013, 307 :62-73
[10]  
Bonardet JL, 1996, ACS SYM SER, V634, P99