US2011094939A1PendingUtilityA1

Process for activating a hydrotreating catalyst

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Assignee: JANSEN MARCEL ADRIAANPriority: Oct 3, 2003Filed: Dec 21, 2010Published: Apr 28, 2011
Est. expiryOct 3, 2023(expired)· nominal 20-yr term from priority
B01J 38/62B01J 23/85B01J 23/94B01J 23/882B01J 38/60C10G 2300/703B01J 31/0201B01J 37/0203C10G 45/08B01J 38/52B01J 23/883B01J 23/76B01J 23/90
41
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Claims

Abstract

The invention pertains to a process for activating an hydrotreating catalyst comprising a Group VIB metal oxide and a Group VIII metal oxide which process comprises contacting the catalyst with an acid and an organic additive which has a boiling point in the range of 80-500° C. and a solubility in water of at least 5 grams per liter (20° C., atmospheric pressure), optionally followed by drying under such conditions that at least 50% of the additive is maintained in the catalyst. The hydrotreating catalyst may be a fresh hydrotreating catalyst or a used hydrotreating catalyst which has been regenerated.

Claims

exact text as granted — not AI-modified
1 - 15 . (canceled) 
     
     
         16 . The hydrotreating catalyst obtainable by a process comprising contacting the catalyst with an acid and an organic additive which has a boiling point in the range of 80-500° C. and a solubility in water of at least 5 grams per liter (20° C., atmospheric pressure), optionally followed by drying under such conditions that at least 50 wt % of the additive is maintained in the catalyst. 
     
     
         17 . A hydrotreating catalyst comprising a Group VIII metal oxide and a Group VI metal oxide, which catalyst additionally comprises an acid and an organic additive which has a boiling point in the range of 80-500° C. and a solubility in water of at least 5 grams per liter (20° C., atmospheric pressure). 
     
     
         18 . The hydrotreating catalyst according to  claim 16 , wherein the catalyst is a regenerated used catalyst or a calcined fresh catalyst and wherein the catalyst comprises a crystalline fraction below 5 wt % (expressed as weight fraction of crystalline compounds of Group VIB and Group VIII metals relative to the total weight of the catalyst). 
     
     
         19 . A process for hydrotreating a hydrocarbon feed in which a hydrocarbon feed is contacted under hydrotreating conditions with a catalyst according to  claim 17 , which optionally has been (pre)sulfided before it is contacted with the hydrocarbon feed.

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