The effect of catalyst pellet size on nickel carbonyl-induced particle sintering under low temperature CO methanation

被引:14
作者
Barrientos, J. [1 ]
Gonzalez, N. [1 ]
Lualdi, M. [1 ]
Boutonnet, M. [1 ]
Jaras, S. [1 ]
机构
[1] KTH Royal Inst Technol, Chem Sci & Engn, Chem Technol, Teknikringen 42,Plant 6, SE-10044 Stockholm, Sweden
关键词
Methanation; Deactivation; Nickel carbonyl; Sintering; Heat and mass transfer; Alumina; FISCHER-TROPSCH SYNTHESIS; ALUMINA-SUPPORTED NICKEL; THERMAL-CONDUCTIVITY; NATURAL-GAS; DEACTIVATION; TRANSPORT; HEAT; HYDROGENATION; SELECTIVITY; KINETICS;
D O I
10.1016/j.apcata.2015.12.034
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
The present work aims to evaluate the effect of catalyst pellet size on deactivation due to nickel carbonyl induced particle sintering. For that purpose, a gamma-Al2O3-supported nickel catalyst was prepared and tested under low temperature and high CO partial pressure. A total of four different pellet sizes were employed in the present study. It was found that the deactivation rate decreases with increasing pellet size. A very severe deactivation was observed when using small pellets. Large pellets exhibited instead a more stable performance. This difference in catalyst stability was explained by X-ray diffraction analyses which revealed that the growth of the nickel particles was very severe when using small pellets. An evaluation of heat and mass transfer phenomena in these four pellets was also conducted. It was found that, under the present low temperature reaction conditions, the temperature at the catalyst external surface can greatly differ from that in the bulk gas when using sufficiently large pellets. It was also shown that, for large pellets, the major part of the interior of the catalyst is exposed to negligible CO partial pressures and high temperatures, fact that can reduce the potential for nickel carbonyl formation. (C) 2016 Elsevier B.V. All rights reserved.
引用
收藏
页码:91 / 102
页数:12
相关论文
共 54 条
[1]   CO HYDROGENATION ON A NICKEL-CATALYST .1. KINETICS AND MODELING OF A LOW-TEMPERATURE SINTERING PROCESS [J].
AGNELLI, M ;
KOLB, M ;
MIRODATOS, C .
JOURNAL OF CATALYSIS, 1994, 148 (01) :9-21
[2]   Structure sensitivity of the methanation reaction:: H2-induced CO dissociation on nickel surfaces [J].
Andersson, M. P. ;
Abild-Pedersen, F. ;
Remediakis, I. N. ;
Bligaard, T. ;
Jones, G. ;
Engbwk, J. ;
Lytken, O. ;
Horch, S. ;
Nielsen, J. H. ;
Sehested, J. ;
Rostrup-Nielsen, J. R. ;
Norskov, J. K. ;
Chorkendorff, I. .
JOURNAL OF CATALYSIS, 2008, 255 (01) :6-19
[3]  
[Anonymous], 2007, TRANSPORT PHENOMENA
[4]   The sintering of Ni/Al2O3 methanation catalyst for substitute natural gas production [J].
Bai, Xiaobo ;
Wang, Sheng ;
Sun, Tianjun ;
Wang, Shudong .
REACTION KINETICS MECHANISMS AND CATALYSIS, 2014, 112 (02) :437-451
[5]   CO methanation over TiO2-supported nickel catalysts: A carbon formation study [J].
Barrientos, J. ;
Lualdi, M. ;
Paris, R. Suarez ;
Montes, V. ;
Boutonnet, M. ;
Jaras, S. .
APPLIED CATALYSIS A-GENERAL, 2015, 502 :276-286
[6]   Deactivation of supported nickel catalysts during CO methanation [J].
Barrientos, J. ;
Lualdi, M. ;
Boutonnet, M. ;
Jaras, S. .
APPLIED CATALYSIS A-GENERAL, 2014, 486 :143-149
[7]  
Bartholomew C.H., 2010, FUNDAM IND CATAL PRO
[8]  
Bartholomew C.H., 2010, FUNDAM IND CATAL PRO, P24
[9]   Mechanisms of catalyst deactivation [J].
Bartholomew, CH .
APPLIED CATALYSIS A-GENERAL, 2001, 212 (1-2) :17-60
[10]   SINTERING OF ALUMINA-SUPPORTED NICKEL AND NICKEL BIMETALLIC METHANATION CATALYSTS IN H2/H2O ATMOSPHERES [J].
BARTHOLOMEW, CH ;
PANNELL, RB ;
FOWLER, RW .
JOURNAL OF CATALYSIS, 1983, 79 (01) :34-46