Isomerization process to produce low pour point distillate fuels and lubricating oil stocks

Claim 2

A process for dewaxing a hydrocarbon feedstock with a relatively high pour point and containing paraffins selected from the group of normal paraffins and slightly branched paraffins which comprises (a) subjecting said feedstock to catalytic dewaxing at catalytic dewaxing conditions including a temperature of 200° to 500° C., pressure from atmospheric to 25,000 kPa, the presence of 20 to 4,000 nll -1 of hydrogen per volume of liquid feed, and a liquid hourly space velocity of 0.1 to 10 hr. -1 by passing said feedstock, along with hydrogen, over a dewaxing catalyst comprising zeolite beta having a noble metal hydrogenation/dehydrogenation component to produce a partially dewaxed product and (b) subjecting said partially dewaxed product to catalytic dewaxing at catalytic dewaxing conditions including a temperature of 200° to 500° C., and pressure from atmospheric to 25,000 kPa, the presence of 20 to 4,000 nll -1 of hydrogen per volume of liquid feed, and a liquid hourly space velocity of 0.1 to 10 hr. -1 by passing said partially dewaxed product over catalyst comprising zeolite beta having a base metal hydrogenation/dehydrogenation component comprising at least one non-noble metal of Group VIA or VIIIA to recover a substantially dewaxed product as a product of the process.

Claim 3

Process of claim 1 in which the feedstock also includes aromatic components.

Claim 4

Process of claim 2 in which the proportion of aromatic components is from 10 to 60 weight percent of the feedstock.

Claim 5

Process of claim 1 in which the zeolite beta has a silica:alumina ratio over 30:1.

Claim 6

Process of claim 1 in which the zeolite beta has a silica:alumina ratio of at least 100:1.

Claim 7

Process of claim 1 in which the noble metal comprises 0.01 to 10 weight %, on an elemental basis, of said catalyst.

Claim 8

Process of claim 1 in which said base metal component comprises 0.1 to 25 weight %, on an elemental basis, of said catalyst.

Claim 9

Process of claim 1 in which said noble metal is platinum or palladium and said base metal is at least one of cobalt, nickel, molybdenum, tungsten and mixtures thereof.

Claim 10

Process of claim 1 in which said noble metal catalyst contains 0.6 weight % Pt, on an elemental basis, and said base metal catalyst contains 4 weight % nickel and 10 weight % tungsten, on an elemental metal basis.

Claim 11

Process of claim 1 in which said noble metal dewaxing catalyst comprises 10 to 90 weight % of the total amount of dewaxing catalyst and said base metal dewaxing catalyst comprises 90 to 10 weight % of the total amount of dewaxing catalyst.

Claim 12

A process for dewaxing a hydrocarbon feedstock oil with a relatively high pour point and containing aromatics and at least 10 weight percent waxy paraffins selected from the group of normal paraffins and slightly branched paraffins and sulfur and nitrogen compounds which comprises (a) subjecting said oil to hydrotreating in a hydrotreating zone containing a conventional hydrotreating catalyst operated at hydrotreating conditions including a temperature of 250° to 400° C., a hydrogen partial pressure of atmospheric to 15,000 kPa, and a liquid hourly space velocity of 0.1 to 10, to remove at least a portion of said sulfur and nitrogen compounds; (b) subjecting said hydrotreated oil to catalytic dewaxing at catalytic dewaxing conditions including a temperature of 200° to 500° C., pressure from atmospheric to 25,000 kPa, the presence of 20 to 4,000 nll -1 of hydrogen per volume of liquid feed, and a liquid hourly space velocity of 0.1 to 10 hr. -1 by passing said hydrotreated oil, along with hydrogen, over a dewaxing catalyst comprising zeolite beta having a noble metal hydrogenation/dehydrogenation component to produce a partially dewaxed product and (c) subjecting said partially dewaxed product to catalytic dewaxing at catalytic dewaxing conditions including a temperature of 200° to 500° C., pressure from atmospheric to 25,000 kPa, the presence of 20 to 4,000 nll -1 of hydrogen per volume of liquid feed, and a liquid hourly space velocity of 0.1 to 10 hr. -1 by passing said partially dewaxed product over catalyst comprising zeolite beta having a base metal hydrogenation/dehydrogenation component comprising at least one non-noble metal of Group VIA or VIIIA to recover a substantially dewaxed product as a product of the process.

Claim 13

A process for dewaxing a hydrocarbon feedstock oil with a relatively high pour point and containing aromatics and at least 10 weight percent waxy paraffins selected from the group of normal paraffins and slightly branched paraffins and sulfur and nitrogen compounds which comprises (a) subjecting said oil to hydrotreating in a hydrotreating zone containing a conventional hydrotreating catalyst operated at hydrotreating conditions including a temperature of 250° to 400° C., a hydrogen partial pressure of atmospheric to 15,000 kPa, and a liquid hourly space velocity of 0.1 to 10, to remove at least a portion of said sulfur and nitrogen compounds; (b) subjecting said hydrotreated oil to catalytic dewaxing at catalytic dewaxing conditions including a temperature of 200° to 500° C., pressure from atmospheric to 25,000 kPa, the presence of 20 to 4,000 nll -1 of hydrogen per volume of liquid feed, and a liquid hourly space velocity of 0.1 to 10 hr. -1 by passing said hydrotreated oil, along with hydrogen, over a dewaxing catalyst comprising zeolite beta having a noble metal hydrogenation/dehydrogenation component to produce a partially dewaxed product and (c) subjecting said partially dewaxed product to catalytic dewaxing at catalytic dewaxing conditions including a temperature of 200° to 500° C., pressure from atmospheric to 25,000 kPa, the presence of 20 to 4,000 nll -1 of hydrogen per volume of liquid feed, and a liquid hourly space velocity of 0.1 to 10 hr. -1 by passing said partially dewaxed product over catalyst comprising zeolite beta having a base metal hydrogenation/dehydrogenation component comprising at least one non-noble metal of Group VIA or VIIIA to recover a substantially dewaxed product as a product of the process.

Claim 14

Process of claim 11 in which the proportion of aromatic components is from 10 to 60 weight percent of the feedstock.

Claim 15

Process of claim 11 in which the zeolite beta has a silica:alumina ratio over 30:1.

Claim 16

Process of claim 11 in which the zeolite beta has a silica:alumina ratio of at least 100:1.

Claim 17

Process of claim 11 in which the noble metal comprises 0.01 to 10 weight %, on an elemental basis, of said catalyst.

Claim 18

Process of claim 11 in which said base metal component comprises 0.1 to 25 weight %, on an elemental basis, of said catalyst.

Claim 19

Process of claim 11 in which said noble metal is platinum or palladium and said base metal is at least one of cobalt, nickel, molybdenum, tungsten and mixtures thereof.

Claim 20

Process of claim 11 in which said noble metal catalyst contains 0.6 weight % Pt, on an elemental basis, and said base metal catalyst contains 4 weight % nickel and 10 weight % tungsten, on an elemental metal basis.

Claim 21

Process of claim 11 in which said noble metal dewaxing catalyst comprises 10 to 90 weight % of the total amount of dewaxing catalyst and said base metal comprises 90 to 10 weight % of the total amount of dewaxing catalyst.

Claim 22

A process for dewaxing a hydrocarbon feedstock oil with a relatively high pour point and containing at least 10 weight percent waxy paraffins selected from the group of normal paraffins and slightly branched paraffins and sulfur and nitrogen compounds which comprises (a) subjecting said oil to hydrotreating in a hydrotreating zone containing a conventional hydrotreating catalyst operated at hydrotreating conditions including a temperature of 250° to 450° C., a hydrogen partial pressure of atmospheric to 15,000 kPa, and a liquid hourly space velocity of 0.1 to 10, to remove at least a portion of said sulfur and nitrogen compounds; (b) subjecting said hydrotreated oil to catalytic dewaxing including a temperature of 200° to 500° C., pressure from atmospheric to 25,000 kPa, the presence of 20 to 4,000 nll -1 of hydrogen per volume of liquid feed, and a liquid hourly space velocity of 0.1 to 10 hr. -1 over a noble metal promoted zeolite beta catalyst followed by catalytic dewaxing including a temperature of 200° to 500° C., pressure from atmospheric to 25,000 kPa, the presence of 20 to 4,000 nll -1 of hydrogen per volume of liquid feed, and a liquid hourly space velocity of 0.1 to 10 hr. -1 over a base metal hydrogenation/dehydrogenation component promoted zeolite beta dewaxing catalyst, wherein said noble metal promoted beta catalyst comprises 10 to 90 wt % of said dewaxing catalyst and said base metal promoted beta catalyst comprises 90 to 10 wt % of said dewaxing catalyst and wherein there is no separation of products or byproducts intermediate said noble metal dewaxing and said base metal dewaxing, and wherein said noble metal catalyst contains 0.1 to 2 wt % platinum or palladium and said base metal catalyst contains 1 to 5 wt % nickel and 2 to 20 wt % tungsten, on an elemental metal basis.

Claim 23

A process for dewaxing a hydrocarbon feedstock oil with a relatively high pour point and containing at least 10 weight percent waxy paraffins selected from the group of normal paraffins and slightly branched paraffins and sulfur and nitrogen compounds which comprises (a) subjecting said oil to hydrotreating in a hydrotreating zone containing a conventional hydrotreating catalyst operated at hydrotreating conditions including a temperature of 250° to 450° C., a hydrogen partial pressure of atmospheric to 15,000 kPa, and a liquid hourly space velocity of 0.1 to 10, to remove at least a portion of said sulfur and nitrogen compounds; (b) subjecting said hydrotreated oil to catalytic dewaxing including a temperature of 200° to 500° C., pressure from atmospheric to 25,000 kPa, the presence of 20 to 4,000 nll -1 of hydrogen per volume of liquid feed, and a liquid hourly space velocity of 0.1 to 10 hr. -1 over a noble metal promoted zeolite beta catalyst followed by catalytic dewaxing including a temperature of 200° to 500° C., pressure from atmospheric to 25,000 kPa, the presence of 20 to 4,000 nll -1 of hydrogen per volume of liquid feed, and a liquid hourly space velocity of 0.1 to 10 hr. -1 over a base metal hydrogenation/dehydrogenation component promoted zeolite beta dewaxing catalyst, wherein said noble metal promoted beta catalyst comprises 10 to 90 wt % of said dewaxing catalyst and said base metal promoted beta catalyst comprises 90 to 10 wt % of said dewaxing catalyst and wherein there is no separation of products or byproducts intermediate said noble metal dewaxing and said base metal dewaxing, and wherein said noble metal catalyst contains 0.1 to 2 wt % platinum or palladium and said base metal catalyst contains 1 to 5 wt % nickel and 2 to 20 wt % tungsten, on an elemental metal basis.