Milutin
Chemical
- Jul 7, 2006
- 152
Dear all,
Our naphtha hydrotreater feed is straight run naphtha from ADU unit, it prepare naphtha for platformer unit. Lead content is all time below detection, below 10ppb.
There is an idea to process slop oil which contain lead on ADU by blending small quantities of slop oil together with crude oil to keep naphtha lead content up to 10ppb. 10ppb is quantity of maximum lead content in naphtha feed set by process licensor.
I am aware if we introduce lead that catalyst poisoning will be permanent or in other words, catalyst regeneration wouldn't recover activity lost by lead poisoning.
Is it a way how to calculate catalyst life and cycle length if we introduce lead to naphtha feed?
I suppose that mechanism of catalyst poisoning is similar to poisoning with mercury, so if anybody can provide some literature about I welcome.
Regards,
Milutin
Our naphtha hydrotreater feed is straight run naphtha from ADU unit, it prepare naphtha for platformer unit. Lead content is all time below detection, below 10ppb.
There is an idea to process slop oil which contain lead on ADU by blending small quantities of slop oil together with crude oil to keep naphtha lead content up to 10ppb. 10ppb is quantity of maximum lead content in naphtha feed set by process licensor.
I am aware if we introduce lead that catalyst poisoning will be permanent or in other words, catalyst regeneration wouldn't recover activity lost by lead poisoning.
Is it a way how to calculate catalyst life and cycle length if we introduce lead to naphtha feed?
I suppose that mechanism of catalyst poisoning is similar to poisoning with mercury, so if anybody can provide some literature about I welcome.
Regards,
Milutin