Leaching of heavy metals under ambient resembling conditions from hydrotreating spent catalysts

作者: S. Ramírez , P. Schacht , R. Quintana-Solórzano , J. Aguilar

DOI: 10.1016/J.FUEL.2012.09.005

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摘要: Abstract Spent hydrotreating catalysts are not inert to air, humidity and temperature, as the combination of these factors may gradually leach metals from catalyst causing contamination land groundwater. In order investigate combined effect ambient variables on leaching, a spent is placed in tin can heated at 40–50 °C then treated for 1000 h under continuous flow wet air. Said contains 10.68 wt.% V, 0.43 wt.% Fe, 2.67 wt.% Ni 3.78 wt.% Mo well 14.7 wt.% coke 19.4 wt.% sulfur, latter basically form metallic sulfides. During leaching experiment, samples taken different times track evolution coke/sulfur content. At end test, even though relatively low temperatures used, fully removed, V partially extracted (around 25% each metal) while Fe content increases. Practically no observed sulfur/coke-free fresh subjected an identical experimental procedure. The presence sulfur clearly enhances leaching. oxides produced oxidation sulfides with water, results formation acidic species, which have strong positive influence catalyst.

参考文章(21)
Antony Stanislaus, Edward Furimsky, Meena Marafi, Handbook of spent hydroprocessing catalysts : regeneration, rejuvenation and reclamation Elsevier. ,(2010)
Anna Leśniewicz, Anna Szymczycha-Madeja, Władysława Mulak, PHYSICOCHEMICAL STUDY OF SPENT HYDRODESULPHURIZATION (HDS) CATALYST Physicochemical Problems of Mineral Processing. ,vol. 41, pp. 125- 132 ,(2007)
F. Albert Cotton, Advanced Inorganic Chemistry ,(1999)
Júlio Carlos Afonso, Tatiana Siqueira de Lima, Paula Constante Campos, Degradation of a spent hydrotreating catalyst: interaction with environment Studies in Surface Science and Catalysis. ,vol. 130, pp. 2849- 2854 ,(2000) , 10.1016/S0167-2991(00)80903-9
Calvin H Bartholomew, Mechanisms of catalyst deactivation Applied Catalysis A-general. ,vol. 212, pp. 17- 60 ,(2001) , 10.1016/S0926-860X(00)00843-7
F TREJO, M RANA, J ANCHEYTA, CoMo/MgO–Al2O3 supported catalysts: An alternative approach to prepare HDS catalysts Catalysis Today. ,vol. 130, pp. 327- 336 ,(2008) , 10.1016/J.CATTOD.2007.10.105
S EIJSBOUTS, A BATTISTON, G VANLEERDAM, Life cycle of hydroprocessing catalysts and total catalyst management Catalysis Today. ,vol. 130, pp. 361- 373 ,(2008) , 10.1016/J.CATTOD.2007.10.112
Mohan S. Rana, Elsa M.R. Capitaine, Carolina Leyva, Jorge Ancheyta, Effect of catalyst preparation and support composition on hydrodesulfurization of dibenzothiophene and Maya crude oil Fuel. ,vol. 86, pp. 1254- 1262 ,(2007) , 10.1016/J.FUEL.2006.09.015
Pierre Dufresne, Hydroprocessing catalysts regeneration and recycling Applied Catalysis A-general. ,vol. 322, pp. 67- 75 ,(2007) , 10.1016/J.APCATA.2007.01.013