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Catalysts Contaminants
Contaminants
that cannot be removed by conventional regeneration methods are considered
as permanent poisons. They deactivate the catalyst either by an effect
of porosity plugging or/and occupation of the active sites. It is therefore
difficult to attribute a precise deactivation effect of a given poison
for all catalysts, as it depends on the catalyst type(NiMo, CoMo, NiW,
Pd, Pt), catalyst porosity, metals content, dispersion of active sites.
Some general ideas can however be given.
The most common poisons for hydrotreating
catalysts are :
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Vanadium,
contained in heavy petroleum fractions such as Vacuum Gas Oils, Atmospheric
or Vacuum Resids. Poisoning effect can be noticed at concentrations
above 5000ppm, on standard NiMo, CoMo catalysts. On specific resid
hydroprocessing catalysts, the metal up take capacity is much higher,
and in some case the catalyst can still be regenerated even with a
V concentration of 20 wt% (see
the article). |
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Arsenic,
contained in light to heavy oil fractions of specific crudes (Russian,
African for example) strongly affects CoMo/NiMo as well as Palladium
catalysts, by means of a direct adsorption on the active sites. This
poison is badly affecting hydrotreating catalysts activity, at relatively
low concentrations. For CoMo/NiMo catalysts Deactivation effect is
already observed from concentration around 3000 ppm. Poisoning effect
on Pd catalysts is more sever, but, in that specific case, regeneration
can help restoring activity. |
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Sodium,
contained in insufficiently desalted crudes also affect catalysts
activity by porosity plugging and potentially modification of active
phase dispersion state. Na content should remain below 1500 ppm. |
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Silicon,
generally originating from antifoaming agents often affects hydrotreating
catalysts treating coker naphthas. Some fresh catalysts contains Silicium
as a constituent, that is important to distinguish from the silicon
brought by the feed. It is generally admitted that the ex feed Silicium
content should be below 3 wt%. |
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Iron
is not a real poison for hydrotreating catalysts, as it does
not have a direct deactivation effect. However, iron may accelarate
coking reactions. |


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Low
metals content catalysts (Palladium, Platinum) are sometimes
sensitive to poisons at much lower concentration, and a particular
attention must be paid when evaluating such a catalyst before regeneration.
For instance, Hg, Cl, Si can have a strong de activation effect at
concentrations in the range of 50 to 100 ppm. |
Catalyst contaminants detection is one of the
important items that Eurecat provide in the field of catalyst expertise
services.
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