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3- PETROCHEMICALS<br />

Edited by: Vivek Patel<br />

Published by: InTech,<br />

Croatia, March 2012.<br />

ISBN: 978-953-51-0411-7<br />

www.intechopen.com<br />

Chapter 12 – New Trends<br />

in Hydroprocessing Spent<br />

Catalysts Utilization<br />

249<br />

Hoda S. Ahmed and<br />

Mohammed F. Menoufy<br />

Summary of the chapter:<br />

The objective of this<br />

chapter is to give academics, research scientists, research<br />

scholars, science and engineering students and industry<br />

professionals an overview of the different utilization technologies<br />

for hydrotreating spent catalysts.<br />

Hydrotreating catalysts consist of critical metals such as Mo, Co,<br />

and Ni, as active metals and are generally supported by alumina<br />

or silica alumina and are usually used in hydrotreating<br />

petroleums. These catalysts deactivate with time, and partial or<br />

complete regeneration can be carried out depending on the<br />

severity of the processes due to carbon or sulfides deposition. In<br />

the long term, the regeneration of these catalysts will become<br />

impossible due to irreversible deactivation, and spent catalysts<br />

would discard as solid wastes. The volume of these solid wastes<br />

has increased significantly worldwide and in <strong>Egyptian</strong> petroleum<br />

refining industries due to a steady increase in upgrading of<br />

feedstock or distillates to meet the environmental regulations for<br />

low sulfur fuels.<br />

Several alternative methods such as disposal in landfills,<br />

reclamation of metals, regeneration/ rejuvenation and reuse, and<br />

utilization as raw materials to produce other useful products are<br />

available to the refiners to deal with the spent catalyst problems.<br />

The choice between these options depends on technical<br />

feasibility and economic consideration.<br />

In recent years, increasing emphasis has been placed on the<br />

development of processes for recycling and recovering of the<br />

waste catalyst metals, as much as possible. In literature there are<br />

many applied researches for spent metals recovery, particularly<br />

for catalyst that contain high concentrations of valuable metals<br />

(Mo, Ni, V and Al2O3) However, fluctuations in the market prices<br />

of the recovered metals and their purity, together with the high<br />

costs of shipping significantly influence the economics of the<br />

metal reclamation process that making it less attractive.<br />

and metal contaminants. Therefore, many efforts were subjected<br />

to replace the conventional regeneration procedures in order to<br />

reactivate and rejuvenate the spent catalysts. The new<br />

procedures are conducted to remove contaminant metals<br />

selectively by chemical treatments without significantly affecting<br />

the chemical and physical characteristics of the original catalyst<br />

In experimental works, carried out by the authors of this<br />

chapter in EPRI (1), concerning spent catalysts, were succeeded<br />

in rejuvenating the spent catalyst Mo-Ni/Al2O3 using for rerefining<br />

of waste lube oil, and applied in Alexandria <strong>Petroleum</strong><br />

Company. Our data revealed that the treated spent catalyst could<br />

be restored nearly its fresh HDS activity levels by application of<br />

oxalic acid leaching technique in addition to H2O2 as an oxidizing<br />

agent. The most effective leaching agent was 4% oxidized oxalic<br />

acid, and the extent of metals recovered was dependent on acid<br />

concentrations or the specific reuse of the spent catalyst. The<br />

rejuvenation process promotes the formation of a<br />

hydroprocessing catalyst due to its improvements in surface area<br />

and average pore diameter (i.e. 87% and 63% of the fresh<br />

catalyst characteristics, respectively). These improvements<br />

caused recovery in the HDS activity of the treated catalyst in the<br />

ranges of 81–96 wt %<br />

Other utilization of spent catalysts, experimental data reveal<br />

that the treatment processes succeeded for extracting nickel,<br />

molybdenum and aluminum oxides in quantities of 25, 30, 45<br />

wt% as raw materials using in the production of other valuable<br />

industrial products. These results are attractive options from<br />

environmental and economical points of view.<br />

References of authors’ data:<br />

1- E. Z. Hegazy., M.Sc. Thesis, Tanta University, Tanta (2003)<br />

2- M. F. Menoufy, H. S. Ahmed, in Proc. of the OAPEC Seminar on<br />

Energy Conservation and Environmental Protection in<br />

<strong>Petroleum</strong> Industries, Cairo (2004).<br />

3- M. F. Menoufy, H. S. Ahmed, .Energy Sources, Part A, 30:1213–<br />

1222, (2008)<br />

4- H S. Ahmed, M.F. Menoufy., Chem. Eng Technol., 32, No. 6,<br />

873–880, (2009).<br />

Many literature review revealed that reactivation of spent<br />

catalysts technology did not reach to well developments.<br />

Spent catalysts lose their activities, and deactivated by pore<br />

blockage and fouling of the active surface with deposition of coke<br />

EPRI Annual Report 2012 24

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