Mild hydrocracking with a catalyst containing an intermediate pore molecular sieve

Claim 2

A process for mild hydrocracking a hydrocarbon feedstock comprising contacting said feedstock containing feed components boiling above 700° F. under conditions of elevated temperature and pressure less than about 1,500 p.s.i.g. with a particulate catalyst comprising at least one active hydrogenation metal component selected from the group consisting of Group VIB and Group VIII metals in combination with (1) a dispersion of silica-alumina in a matrix consisting essentially of alumina and (2) a crystalline intermediate pore molecular sieve comprising a silicoaluminophosphate having a pore size between about 5 and 7 angstroms, said conditions yielding about a 10 to about a 50 volume percent conversion of said feed components boiling above 700° F. to product components boiling at or below 700° F.

Claim 3

The process defined in claim 1 wherein said conditions include a hydrogen partial pressure less than about 1,200 p.s.i.g.

Claim 4

A process as defined in claim 1 wherein the hydrogen partial pressure is less than about 1475 p.s.i.g. and the conversion is between 15 and 30 volume percent.

Claim 5

A process as defined in claim 3 wherein the hydrogen partial pressure is less than about 1,450 p.s.i.g.

Claim 6

The process defined in claim 1 wherein said intermediate pore molecular sieve comprises SAO-11.

Claim 7

The process defined in claim 1 wherein the hydrogen partial pressure is less than about 1,000 p.s.i.g.

Claim 8

The process defined in claim 1 wherein said conversion is between about 15 and about 35 volume percent.

Claim 9

The process defined in claim 6 wherein said conversion is between about 15 and about 35 volume percent.

Claim 10

The process defined in claim 5 wherein said conversion is between about 15 and about 35 volume percent.

Claim 11

The process defined in claim 1 wherein said conversion is between about 15 and about 30 volume percent.

Claim 12

The process defined in claim 10 wherein said hydrogenation component comprises a combination of a Group VIB and Group VIII metals.

Claim 13

The process defined in claim 5 wherein said hydrogenation metal component comprises at least one metal selected from the group consisting of nickel and cobalt and at least one metal selected from the group consisting of molybdenum and tungsten.

Claim 14

The process defined in claim 6 wherein said hydrogenation metal component comprises at least one metal selected from the group consisting of nickel and cobalt and at least one metal selected from the group consisting of molybdenum and tungsten.

Claim 15

The process defined in claim 9 wherein said hydrogenation metal component comprises at least one metal selected from the group consisting of nickel and cobalt and at least one metal selected from the group consisting of molybdenum and tungsten.

Claim 16

A process for mild hydrocracking a hydrocarbon feedstock comprising feed components boiling above 700° F. comprising contacting said feedstock under conditions of elevated temperature and a hydrogen partial pressure less than about 1,500 p.s.i.g. with a particulate catalyst comprising at least one Group VIII active metal hydrogenation component and at least one Group VIB active metal hydrogenation component on a support comprising (1) a dispersion of silica-alumina in a matrix consisting essentially of gamma alumina and (2) a crystalline intermediate pore silicoaluminophosphate molecular sieve of about 5 to about 7 angstroms pore size, said conditions yielding between about a 10 and 50 volume percent conversion of the feed components boiling above 700° F. to product components boiling at or below 700° F.

Claim 17

A process for mild hydrocracking a hydrocarbon feedstock comprising feed components boiling above 700° F. comprising contacting said feedstock under conditions of elevated temperature and a hydrogen partial pressure less than about 1,500 p.s.i.g. with a particulate catalyst comprising at least one Group VIII active metal hydrogenation component and at least one Group VIB active metal hydrogenation component on a support comprising (1) a dispersion of silica-alumina in a matrix consisting essentially of gamma alumina and (2) a crystalline intermediate pore silicoaluminophosphate molecular sieve of about 5 to about 7 angstroms pore size, said conditions yielding between about a 10 and 50 volume percent conversion of the feed components boiling above 700° F. to product components boiling at or below 700° F.

Claim 18

The process defined in claim 15 wherein said hydrogen partial pressure is less than 1,200 p.s.i.g.

Claim 19

The process defined in claim 15 wherein said intermediate pore molecular sieve comprises SAPO-11.

Claim 20

The process defined in claim 17 wherein the hydrogen partial pressure is less than about 1,000 p.s.i.g.

Claim 21

The process defined in claim 18 wherein said conversion is between about 15 and about 35 volume percent.

Claim 22

The process defined in claim 18 wherein said conversion is between about 15 and about 30 volume percent.

Claim 23

A process for mild hydrocracking a hydrocarbon feedstock selected from the group consisting of a gas oil and residuum containing a substantial proportion of feed components boiling below about 1100° F. with a least some of said feed components boiling above 700° F., under conditions of elevated temperature and a hydrogen partial pressure between about 500 p.s.i.g. and about 1,500 p.s.i.g. with a catalyst comprising at least one Group VIII active metal hydrogenation component and at least one Group VIB active metal hydrogenation component on a support comprising in combination (1) a dispersion of silica-alumina in a matrix consisting essentially of gamma alumina and (2) a crystalline intermediate pore silicoaluminophosphate molecular sieve of about 5 to 7 angstroms pore size, said conditions being such that between about 10 and 50 percent by volume of said feed components boiling above 700° F. are converted to product components boiling at or less than 700° F.

Claim 24

A process for mild hydrocracking a hydrocarbon feedstock selected from the group consisting of a gas oil and residuum containing a substantial proportion of feed components boiling below about 1100° F. with a least some of said feed components boiling above 700° F., under conditions of elevated temperature and a hydrogen partial pressure between about 500 p.s.i.g. and about 1,500 p.s.i.g. with a catalyst comprising at least one Group VIII active metal hydrogenation component and at least one Group VIB active metal hydrogenation component on a support comprising in combination (1) a dispersion of silica-alumina in a matrix consisting essentially of gamma alumina and (2) a crystalline intermediate pore silicoaluminophosphate molecular sieve of about 5 to 7 angstroms pore size, said conditions being such that between about 10 and 50 percent by volume of said feed components boiling above 700° F. are converted to product components boiling at or less than 700° F.

Claim 25

A process as defined in claim 21 wherein between about 15 and 35 percent by volume of said feed components boiling above 700° F. are converted to product components boiling at or below 700° F.

Claim 26

A process as defined in claim 22 wherein said hydrogen partial pressure is less than about 1,200 p.s.i.g.

Claim 27

A process as defined in claim 21 wherein said intermediate pore molecular sieve has a pore size between about 5 and 6 angstroms.

Claim 28

A process for mild hydrocracking a hydrocarbon feedstock comprising said feedstock containing feed components boiling above 700° F. under conditions of elevated temperature and pressure less than about 1,500 p.s.i.g. with a particulate catalyst comprising at least one active hydrogenation metal component selected from the Group consisting of Group VIB and Group VIII metals in combination with (1) a dispersion of silica-alumina in a matrix consisting essentially of alumina and (2) an intermediate pore molecular sieve comprising a crystalline silica having a pore size between about 5 and 7 angstroms, said conditions yielding about a 10 to a 50 volume percent conversion of said feed components boiling above 700° F. to product components boiling at or below 700° F.

Claim 29

A process for mild hydrocracking a hydrocarbon feedstock comprising said feedstock containing feed components boiling above 700° F. under conditions of elevated temperature and pressure less than about 1,500 p.s.i.g. with a particulate catalyst comprising at least one active hydrogenation metal component selected from the Group consisting of Group VIB and Group VIII metals in combination with (1) a dispersion of silica-alumina in a matrix consisting essentially of alumina and (2) an intermediate pore molecular sieve comprising a crystalline silica having a pore size between about 5 and 7 angstroms, said conditions yielding about a 10 to a 50 volume percent conversion of said feed components boiling above 700° F. to product components boiling at or below 700° F.

Claim 30

A process as defined in claim 25 wherein said catalyst comprises both Group VIII and Group VIB active hydrogenation components.

Claim 31

A process as defined in claim 26 wherein said pressure is above 500 p.s.i.g.

Claim 32

A process as defined in claim 27 wherein said catalyst comprises both nickel and tungsten hydrogenation components.

Claim 33

A process as defined in claim 28 wherein said intermediate pore molecular sieve is silicalite.

Claim 34

A process as defined in claim 29 wherein said conversion is between 15 and 35 volume percent.

Claim 35

A process as defined in claim 30 wherein the hydrogen partial pressure is less than about 1,000 p.s.i.g.

Claim 36

A process as defined in claim 29 wherein the hydrogen partial pressure is between 500 and 1,200 p.s.i.g.