Hydroprocessing catalyst, preparation method thereof and use of same

US2016008799A1 · US · A1

Patent metadata
FieldValue
Publication numberUS-2016008799-A1
Application numberUS-201514859888-A
CountryUS
Kind codeA1
Filing dateSep 21, 2015
Priority dateJan 20, 2005
Publication dateJan 14, 2016
Grant date

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  1. Title

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Abstract

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The invention relates to a hydrocarbon hydroprocessing catalyst comprising a support based on at least one refractory oxide, at least one metal from group VIII and at least one metal from group VIB. The inventive catalyst is characterized in that it also comprises at least one organic compound having formula (I) or (II): in which each R 1 represents independently an alkyl group at C 1-18 , an alkenyl group at C 2-18 , an aryl group at C 6-18 , a cycloalkyl group at C 3-8 , an alkylaryl or arylalkyl group at C 7-20 , or the two R 1 groups together form a divalent group at C 2-18 , and R 2 represents an alkylene group at C 1-18 , an arylene group at C 6-18 , a cycloalkylene group at C 3-7 , or a combination of same. The invention also relates to a method of preparing one such catalyst and to the use thereof for hydroprocessing or hydrocracking.

First claim

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1 . An activated hydroprocessing catalyst comprising a carrier based on at least one refractory oxide, at least one metal of group VIII and at least one metal of group VIB of the Periodic Table of Elements, and at least one organic compound represented by formula (I) or (II), the at least one organic compound having at least two carboxylic ester functions and wherein the activated catalyst is prepared by bringing the at least one organic compound in contact with the at least one refractory oxide, at least one metal of group VIII and at least one metal of Group VIB followed by activation by sulfurization, in which each R 1 independently represents a C 1 -C 18 alkyl, C 2 -C 18 alkenyl, C 6 -C 18 aryl, C 3 -C 8 cycloalkyl, C 7 -C 20 alkylaryl or C 7 -C 20 arylalkyl group, or the two R 1 groups together form a C 2 -C 18 divalent group, and R 2 represents a C 1 -C 18 alkylene, C 6 -C 18 arylene or C 3 -C 7 cycloalkylene group, or a combination thereof, it being possible for the carbon chain of the hydrocarbon-based groups represented by R 1 and R 2 to contain or bear one or more heteroatoms selected from N, S and O, and for each of the groups R 1 and R 2 to bear one or more substituents of formula —C(═O)O—R 1 or —O—C(═O)—R 1 where R 1 has the meaning indicated above. 2 . The activated catalyst as claimed in claim 1 , wherein the organic compound of formula (I) or (II) is selected from alkyl ortho-phthalates, alkyl isophthalates, alkyl terephthalates, malonic acid esters, adipic acid esters, glutaric acid esters, 1,6-dioxacyclodecane-2,5-dione, dimethyl 2-(methoxymethyl)-succinate, dibutyl itaconate, diethyl 2,3-diacetylsuccinate, dimethyl cyclohexane-1,4-dicarboxylate, dimethyl 3,3′-dithiodipropionate, glycerol triacetate, propylene glycol diacetate, ethylene glycol dimethacrylate and pentaerythritol tetrakis(3-mercaptopropionate). 3 . The activated catalyst as claimed claim 1 , wherein the number of carbon atoms separating the two groups >C═O of formulae (I) and (II) is equal to 1, 2 or 4. 4 . The activated catalyst as claimed in claim 3 , wherein the organic compound of formula (I) is a C 1 -C 4 dialkyl succinate. 5 . The activated catalyst as claimed in claim 1 , wherein the catalyst comprises at least 0.001 mol of at least one organic compound per mole of metals of groups VIB and VIII. 6 . The activated catalyst as claimed in claim 5 , wherein the catalyst comprises from 0.001 to 10 mol of at least one organic compound per mole of metals of groups VIB and VIII. 7 . A method for preparing an activated hydroprocessing catalyst, comprising in this order: a step of bringing a catalyst comprising a carrier based on at least one refractory oxide, at least one metal of group VIII in the oxide state and at least one metal of group VIB in the oxide state into contact with at least one organic compound of formula (I) or (II) in which each R 1 independently represents a C 2 -C 18 alkyl, C 2 -C 18 alkenyl, C 6 -C 18 aryl, C 3 -C 8 cycloalkyl, C 7 -C 20 alkylaryl or C 7 -C 20 arylalkyl group, or the two R 1 groups together form a C 2 -C 18 divalent group, and R 2 represents a C 2 -C 18 alkylene, C 6 -C 18 arylene or C 3 -C 7 cycloalkylene group, or a combination thereof, it being possible for the carbon chain of the hydrocarbon-based groups represented by R 1 and R 2 to contain or bear one or more heteroatoms selected from N, S and O, and for each of the groups R 1 and R 2 to bear one or more substituents of formula —C(═O)O—R 1 or —O—C(═O)—R 1 where R 1 has the meaning indicated above, and a step of activating the catalyst by sulfurization. 8 . The method as claimed in claim 7 , wherein the catalyst comprising a carrier based on at least one refractory oxide, at least one metal of group VIII in the oxide state and at least one metal of group VIB in the oxide state is a regenerated catalyst. 9 . The method as claimed in claim 7 , wherein the step of bringing the at least one organic compound in contact with the catalyst is followed by at least one maturation step, at a temperature from 0 to 100° C., the duration of which is between a few minutes and a few years, said maturation step being optionally followed by at least one heat treatment step, at a temperature of from 50 to 250° C., and lasting from a few minutes to several days. 10 . The method as claimed in claims 7 , wherein the catalyst is brought into contact with the compound(s) of formula (I) or (II) in the presence of at least one solvent and/or of at least one acid. 11 . The method as claimed in claim 7 , wherein the organic compound(s) of formula (I) or (II) are at least partially soluble in the solvent. 12 . The method as claimed in claim 10 , wherein the solvent is selected from water, toluene, xylenes, ethylene glycol, diethylene glycol, triethylene glycol, glycerol, ethanol, tert-butanol, polyethylene glycol (PEG) white spirit and petroleum ether. 13 . The method as claimed in claim 7 , wherein the catalyst is brought into contact with the compound(s) of formula (I) or (II) ex situ, outside the hydroprocessing reactor. 14 . The method as claimed in claim 7 , wherein the activation step comprises placing the catalyst in the presence of hydrogen and of at least one sulfurization agent preferably selected from hydrogen sulfide, elemental sulfur, CS 2 , mercaptans, sulfides and/or polysilfides, and hydrocarbon fractions with a boiling point of less than 400° C. containing sulfur compounds. 15 . The method as claimed in claim 7 , wherein the sulfurization agent is dimethyl disulfide. 16 . A method of using the activated hydroprocessing catalyst of claim 1 , the method comprising a step of bringing the activated catalyst in contact with hydrocarbons derived from petroleum fractions with a boiling point of between 40° C. and 560° C. 17 . The activated hydroprocessing catalyst as claimed in claim 2 , wherein the organic compound of formula (I) or (II) is a diester. 18 . The catalyst as claimed in claim 3 , wherein the number of carbon atoms separating the two groups >C═O of formulae (I) and (II) is equal to 1 or 2. 19 . The catalyst as claimed in claim 4 , wherein the organic compound of formula (I) is dimethyl succinate. 20 . The method of preparation as claimed in claim 12 , wherein the solvent is has a molecular weight from 118 to 1000. 21 . The method of preparation as claimed in claim 20 , wherein the solvent is triethylene glycol. 22 . The method of claim 11 , wherein the solvent is polyethylene glycol having a molecular weight from 118 to 1000. 23 . The method of claim 22 , wherein the solvent is triethylene glycol.

Assignees

Inventors

Classifications

  • Sulfiding · CPC title

  • in combination with chromium, molybdenum, or tungsten metals, or compounds thereof · CPC title

  • Esters of carboxylic or carbonic acids · CPC title

  • containing in addition, inorganic metal compounds not provided for in groups B01J31/02 - B01J31/24 · CPC title

  • Chromium, molybdenum or tungsten · CPC title

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What does patent US2016008799A1 cover?
The invention relates to a hydrocarbon hydroprocessing catalyst comprising a support based on at least one refractory oxide, at least one metal from group VIII and at least one metal from group VIB. The inventive catalyst is characterized in that it also comprises at least one organic compound having formula (I) or (II): …
Who is the assignee on this patent?
Total Marketing Services, IFP Energies Nouvelles
What technology area does this patent fall under?
Primary CPC classification B01J31/0209. Mapped technology areas include Operations & Transport.
When was this patent published?
Publication date Thu Jan 14 2016 00:00:00 GMT+0000 (Coordinated Universal Time) (A1). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 8 related publications on this page (citations in our corpus or others sharing the same primary CPC).