Multiple catalyst system for hydrodenitrogenation of high nitrogen feeds

Claim 2

A process for hydrodenitrogenation of high nitrogen content hydrocarbon feeds comprising contacting the feed with hydrogen under hydrodenitrogenation conditions in the presence of a multiple catalyst system comprising a first hydrodenitrogenation catalyst of apparent higher order reaction kinetics and lower rate constant for hydrodenitrogenation and at least one subsequent hydrodenitrogenation catalyst of apparent lower order reaction kinetics and higher rate constant for hydrodenitrogenation, wherein the volume of the first hydrodenitrogenation catalyst in said system is effective to reduce the nitrogen content of the feed to a level at which the instantaneous hydrodenitrogenation reaction rate of at least one aforesaid subsequent hydrodenitrogenation catalyst approximates the instantaneous hydrodenitrogenation reaction rate of the first hydrodenitrogenation catalyst, the remainder of catalyst volume in said system comprising said subsequent hydrodenitrogenation catalyst.

Claim 3

The process of claim 1 wherein the high nitrogen hydrocarbon feed contains at least about 0.4 wt% nitrogen.

Claim 4

The process of claim 1 wherein hydrodenitrogenation conditions include a temperature of about 650° to about 820° F., hydrogen pressure of about 800 to about 2500 psi, LHSV of about 0.2 to about 3 and hydrogen addition rate of about 2000 to about 20,000 SCFB.

Claim 5

The process of claim 1 wherein the first hydrodenitrogenation catalyst of apparent higher order reaction kinetics and lower rate constant for hydrodenitrogenation comprises a weakly or moderately acidic support.

Claim 6

The process of claim 4 wherein the first hydrodenitrogenation catalyst comprises a hydrogenating component comprising at least one metal of Group VIB or VIII or both deposed on a nonzeolitic porous refractory inorganic oxide support of low or moderate acidity.

Claim 7

The process of claim 5 wherein the hydrogenating component of the first hydrodenitrogenation catalyst comprises nickel-molybdenum, phosphorus-promoted nickel-molybdenum, cobalt-chromium-molybdenum, phosphorus-promoted cobalt-chromium-molybdenum, nickel-chromium-molybdenum or phosphorus-promoted nickel-chromium-molybdenum and the support component of the first hydrodenitrogenation catalyst comprises alumina.

Claim 8

The process of claim 1 wherein the subsequent hydrodenitrogenation catalyst of apparent lower order reaction kinetics and higher rate constant for hydrodenitrogenation comprises a moderately or strongly acidic support of greater acidity than that of the first hydrodenitrogenation catalyst.

Claim 9

The process of claim 7 wherein the subsequent hydrodenitrogenation catalyst comprises a hydrogenating component comprising at least one metal of Group VIB or VIII or both deposed on a zeolitic or nonzeolitic support comprising silica.

Claim 10

The process of claim 8 wherein the hydrogenating component of the subsequent hydrodenitrogenation catalyst comprises nickel-molybdenum, phosphorus-promoted nickel-molybdenum, cobalt-chromium-molybdenum, phosphorus-promoted cobalt-chromium-molybdenum, nickel-chromium-molybdenum or phosphorus-promoted nickel-chromium-molybdenum and the support of the subsequent hydrodenitrogenation catalyst comprises silica-alumina, a crystalline molecular sieve zeolite, a dispersion of said zeolite in a nonzeolitic porous refractory inorganic oxide or a combination thereof.

Claim 11

The process of claim 6 wherein the hydrogenating component of the first hydrodenitrogenation catalyst comprises phosphorus-promoted nickel-molybdenum.

Claim 12

The process of claim 9 wherein the hydrogenating component of the subsequent hydrodenitrogenation catalyst comprises cobalt-chromium-molybdenum and the support of the subsequent hydrodenitrogenation catalyst comprises a crystalline molecular sieve zeolite.

Claim 13

The process of claim 1 wherein the multiple catalyst system is a two catalyst system and the volume of the subsequent hydrodenitrogenation catalyst is sufficient to reduce product nitrogen level to the desired level.

Claim 14

A process for hydrodenitrogenation, with a volume of catalyst, of high nitrogen hydrocarbon feeds containing at least about 0.4 wt% nitrogen comprising contacting the feed with hydrogen under hydrodenitrogenation conditions in a first step in the presence of a catalyst having a weakly or moderately acidic support, and contacting an effluent from such first step with hydrogen under hydrodenitrogenation conditions in at least one subsequent step in the presence of a hydrodenitrogenation catalyst having a moderately or strongly acidic support of greater acidity than that of the first catalyst, wherein the volume of catalyst employed in the first step is effective to reduce nitrogen content of the feed to a level at which the instantaneous hydrodenitrogenation rate constant of the subsequent step catalyst approximates the instantaneous hydrodenitrogenation rate constant of the first step catalyst, the remaining volume of catalyst comprising said subsequent step catalyst.

Claim 15

A process for hydrodenitrogenation, with a volume of catalyst, of high nitrogen hydrocarbon feeds containing at least about 0.4 wt% nitrogen comprising contacting the feed with hydrogen under hydrodenitrogenation conditions in a first step in the presence of a catalyst having a weakly or moderately acidic support, and contacting an effluent from such first step with hydrogen under hydrodenitrogenation conditions in at least one subsequent step in the presence of a hydrodenitrogenation catalyst having a moderately or strongly acidic support of greater acidity than that of the first catalyst, wherein the volume of catalyst employed in the first step is effective to reduce nitrogen content of the feed to a level at which the instantaneous hydrodenitrogenation rate constant of the subsequent step catalyst approximates the instantaneous hydrodenitrogenation rate constant of the first step catalyst, the remaining volume of catalyst comprising said subsequent step catalyst.

Claim 16

The process of claim 12 wherein hydrodenitrogenation conditions include a temperature of about of about 650° to about 820° F., hydrogen pressure of about 800 to about 2500 psi, LHSV of about 0.2 to about 3 and hydrogen rate of about 2000 to about 20,000 SCFB.

Claim 17

The process of claim 14 wherein the first step catalyst comprises a hydrogenating component comprising at least one metal of Group VIB or VIII or both deposed on a nonzeolitic porous refractory inorganic oxide support of low or moderate acidity.

Claim 18

The process of claim 15 wherein the hydrogenating component of the first step catalyst comprises at least one metal selected from the group consisting of nickel, cobalt, molybdenum and chromium and the support component of the first step catalyst comprises alumina.

Claim 19

The process of claim 16 wherein the hydrogenating component of the first step catalyst comprises a phosphorus component in addition to said metal.

Claim 20

The process of claim 13 wherein the subsequent step catalyst comprises a hydrogenating component comprising at least one metal of Group VIB or VIII or both deposed on a nonzeolitic or zeolitic support comprising silica.

Claim 21

The process of claim 18 wherein the hydrogenating component of the subsequent step catalyst comprises at least one metal selected from the group consisting of nickel, cobalt, molybdenum and chromium and the support component of the subsequent step catalyst comprises silica-alumina, a crystalline molecular sieve zeolite, a dispersion of said zeolite in a nonzeolitic porous refractory inorganic oxide or a combination thereof.

Claim 22

The process of claim 19 wherein the hydrogenating component of the subsequent step catalyst contains a phosphorus component in addition to said metal.

Claim 23

The process of claim 15 wherein the hydrogenating component of the first step catalyst comprises nickel-molybdenum, phosphorus-promoted nickel-molybdenum, cobalt-chromium-molybdenum, phosphorus-promoted cobalt-chromium-molybdenum, nickel-chromium-molybdenum or phosphorus-promoted nickel-chromium-molybdenum and the support component of the first step catalyst comprises alumina.

Claim 24

The process of claim 21 wherein the hydrogenating component of the first step catalyst comprises phosphorus-promoted nickel-molybdenum.

Claim 25

The process of claim 18 wherein the hydrogenating component of the subsequent step catalyst comprises nickel-molybdenum, phosphorus-promoted nickel-molybdenum, cobalt-chromium-molybdenum, phosphorus-promoted cobalt-chromium-molybdenum, nickel-chromium-molybdenum or phosphorus-promoted nickel-chromium-molybdenum and the support comprises silica-alumina, a crystalline molecular sieve zeolite, a dispersion of said zeolite in a nonzeolitic porous refractory inorganic oxide or a combination thereof.

Claim 26

The process of claim 23 wherein the hydrogenating component of the subsequent step catalyst comprises cobalt-chromium-molybdenum and the support of the subsequent step catalyst comprises a crystalline molecular sieve zeolite.

Claim 27

A process for hydrodenitrogenation with a volume of catalyst, of high nitrogen content hydrocarbon feeds containing at least about 0.4 wt% nitrogen comprising contacting the feed with hydrogen under hydrodenitrogenation conditions in a first step in the presence of a catalyst comprising a hydrogenating component comprising at least one metal of Group VIB or VIII or both deposed on a nonzeolitic support comprising alumina or silica-alumina, and contacting an effluent from said first step with hydrogen under hydrodenitrogenation conditions in at least one subsequent step with a catalyst comprising a hydrogenating component comprising at least one metal of Group VIB or VIII or both deposed on a support of greater acidity than that of the first step catalyst comprising silica-alumina, a crystalline molecular sieve zeolite, a dispersion of said zeolite in a nonzeolitic porous refractory inorganic oxide or a combination thereof, wherein the volume of the first step catalyst is effective to reduce nitrogen content of the feed to a level at which the instantaneous hydrodenitrogenation reaction rate of the subsequent step catalyst approximates the instantaneous hydrodenitrogenation reaction rate of the first step catalyst, the remainder of catalyst volume comprising said subsequent step catalyst.

Claim 28

A process for hydrodenitrogenation with a volume of catalyst, of high nitrogen content hydrocarbon feeds containing at least about 0.4 wt% nitrogen comprising contacting the feed with hydrogen under hydrodenitrogenation conditions in a first step in the presence of a catalyst comprising a hydrogenating component comprising at least one metal of Group VIB or VIII or both deposed on a nonzeolitic support comprising alumina or silica-alumina, and contacting an effluent from said first step with hydrogen under hydrodenitrogenation conditions in at least one subsequent step with a catalyst comprising a hydrogenating component comprising at least one metal of Group VIB or VIII or both deposed on a support of greater acidity than that of the first step catalyst comprising silica-alumina, a crystalline molecular sieve zeolite, a dispersion of said zeolite in a nonzeolitic porous refractory inorganic oxide or a combination thereof, wherein the volume of the first step catalyst is effective to reduce nitrogen content of the feed to a level at which the instantaneous hydrodenitrogenation reaction rate of the subsequent step catalyst approximates the instantaneous hydrodenitrogenation reaction rate of the first step catalyst, the remainder of catalyst volume comprising said subsequent step catalyst.

Claim 29

The process of claim 25 wherein the hydrogenating component of said first or subsequent step catalyst or both comprises a phosphorus component in addition to said metal or metals of Group VIB or VIII or both.

Claim 30

The process of claim 25 wherein the hydrogenating component of the first step catalyst comprises nickel-molybdenum, phosphorus-promoted nickel-molybdenum, cobalt-chromium-molybdenum, phosphorus-promoted cobalt-chromium-molybdenum, nickel-chromium-molybdenum or phosphorus-promoted nickel-chromium-molybdenum and the support component of the first step catalyst comprises alumina.

Claim 31

The process of claim 27 wherein the hydrogenating component of the first step catalyst comprises phosphorus-promoted nickel-molybdenum.

Claim 32

The process of claim 8 wherein the hydrogenating component of the subsequent step catalyst comprises nickel-molybdenum, phosphorus-promoted nickel-molybdenum, cobalt,-chromium-molybdenum, phosphorus-promoted cobalt-chromium-molybdenum, nickel-chromium-molybdenum or phosphorus-promoted nickel-chromium-molybdenum and the support of the subsequent step catalyst comprises silica-alumina, a crystalline molecular sieve zeolite, a dispersion of said zeolite in a nonzeolitic porous refractory inorganic oxide or a combination thereof.

Claim 33

The process of claim 29 wherein the hydrogenating component of the subsequent step catalyst comprises cobalt-chromium-molybdenum and the support of the subsequent step catalyst comprises a crystalline molecular sieve zeolite.