Process for stabilizing lube base stocks derived from bright stock

• US 4,627,908 A
• Filed: 10/24/1985
• Issued: 12/09/1986
• Est. Priority Date: 10/24/1985
• Status: Expired due to Term

• Current Assignee: Chevron Research Company (Chevron Corp.)
• Original Assignee: Chevron Research Company (Chevron Corp.)
• Inventors: Miller, Stephen J.
• Primary Examiner(s): Metz, Andrew H.
• Assistant Examiner(s): McFarlane, Anthony
• Application Number:
  US06/790,704
• Time in Patent Office: 411 Days
• Field of Search: 208/57, 208/58, 208/18, 208/95, 208/97, 208/89, 208/254 H, 208/143
• US Class Current: 208/58
• CPC Class Codes: C10G 45/08 in combination with chromium, molybdenum, or tungsten metals, or compounds thereof
• CPC Class Codes: C10G 45/10 containing platinum group metals or compounds thereof
• CPC Class Codes: C10G 65/12 including cracking steps and other hydrotreatment steps

Abstract

A process for stabilizing a lubricating oil base stock derived from a nitro-aromatic-containing hydrocracked bright stock, comprising a two-step stabilizing process utilizing hydrodenitrification followed by mild hydrofinishing.

Claims

1. An improved process for stabilizing a nitro-aromatic-containing lubricating oil base stock derived from a hydrocracked bright stock, comprising:

(a) contacting said hydrocracked bright stock with hydrogen in the presence of a catalyst having hydrodenitrification activity under conditions effective to reduce the nitrogen content of said stock and to minimize cracking to produce a substantially nitrogen-free product; and

(b) contacting said substantially nitrogen-free product with hydrogen in the presence of a catalyst having hydrogenation activity under mild conditions to produce a stabilized lubricating oil base stock having improved oxidation stability as shown by oxidator BN.

2. A process according to claim 1 wherein the catalyst having hydrodenitrification activity comprises at least metal from Group VIIIA and at least one metal from Group VIA or tin supported on an alumina or siliceous matrix.

3. A process according to claim 2 wherein said Group VIIIA metal is nickel or cobalt and said Group VIA metal is molybdenum or tungsten.

4. A process according to claim 3 wherein said catalyst is sulfided.

5. A process according to claim 1 wherein said hydrodenitrification is carried out at a temperature ranging from about 600°

F. to about 850°

F., a pressure ranging from about 500 psig to about 4000 psig, an LHSV ranging from about 0.1 hr.^-1 to about 3 hr.^-1, and a substantial hydrogen partial pressure.

6. A process according to claim 5 wherein said LHSV is from about 0.1 hr.^-1 to about 0.8 hr^-1.

7. A process according to claim 6 wherein said LHSV is about 0.25 hr.^-1.

8. A process according to claim 1 wherein said catalyst having hydrogenation activity comprises at least one Group VIIIA noble metal supported on a refractory oxide.

9. A process according to claim 8 wherein said noble metal is palladium.

10. A process according to claim 1 wherein said hydrogenation of the substantially nitrogen free product is carried out at a temperature ranging from about 300°

F. to about 600°

F. and is below the temperature at which the hydrodenitrification is carried out, a pressure ranging from about 500 psig to about 4000 psig, and an LHSV ranging from about 0.1 hr.^-1 to about 2 hr.^-1 and a substantial hydrogen partial pressure.

11. A process according to claim 10 wherein said LHSV ranges from about 0.1 hr.^-1 to about 0.5 hr.^-1.

12. A process according to claim 11 wherein said LHSV is about 0.25 hr.^-1.

13. A process according to claim 1 wherein the hydrodenitrification catalyst is a sulfided catalyst comprising nickel and molybdenum on an alumina support and said hydrodenitrification process is carried out at a temperature of about 725°

F., a pressure of about 2000 psig and an LHSV of about 0.25 hr.^-1 ; and

said catalyst having hydrogenation activity comprises palladium on a siliceous support and said hydrogenation is carried out at a temperature of about 400°

F. and an LHSV of about 0.25 hr.^-1.

14. A process according to claim 13 wherein said nitro-aromatic-containing stock is a dewaxed hydrocracked bright stock derived from a vacuum residuum fraction of a topped crude oil.