Patent US4357232A successfully refreshed from Google Patents.
← Back to Patent Explorer
US4357232A Expired / Lapsed US ⏱️ 0.0 years remaining

Method for enhancing catalytic activity

Assignee: Mobil Oil AS
•
Filing: 1981-01-15
•
Granted: 1982-11-02
•
Expires: 2001-01-15
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

Abstract Catalytically dewaxed lubricating base stock oils that have improved resistance to oxidation are produced by pretreating the waxy furfural raffinate with a zeolite sorbent prior to dewaxing with a zeolite catalyst such as ZSM-5, and conducting the dewaxing at a reduced temperature not to exceed about 675 DEG -700 DEG F.

Inventors

  • 👤 Robert E. Holland
  • 👤 Samuel A. Tabak

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-01 23:01
CPC Classifications
C; C10; C10G; C10G67/00; C10G67/02; C10G67/06; C10G2400/00; C10G2400/10

Claims Analysis

Total Claims: 9
Claim 1
Independent Claim 307 words
In a process for preparing a high quality lube base stock oil having a predetermined pour point in the range of about -25° to +30° F. from waxy crude oil, which process comprises: extracting a distillate fraction that boils within the range of 450° to 1100° F. or a deasphalted short residuum fraction of said waxy crude with a solvent selective for aromatic hydrocarbons to yield a raffinate from which undesirable compounds have been removed; contacting the raffinate and hydrogen gas with a dewaxing catalyst under dewaxing conditions effective to impart said predetermined pour point, said catalyst comprising a first crystalline zeolite having a dry crystal framework density of not less than about 1.6 grams per cubic centimeter and a constraint index of about 1 to about 12, thereby converting wax contained in the raffinate to lower boiling hydrocarbons; and, topping the dewaxed raffinate to remove therefrom components of a low molecular weight; the improvement, whereby the resistance to oxidation of said dewaxed raffinate is increased, which comprises: pretreating said raffinate, prior to dewaxing, with a sorbent comprising a second crystalline zeolite having an effective pore diameter equal to or larger than said first crystalline zeolite, said pretreating being conducted under a combination of conditions selected from a temperature of about 35° to about 350° F., a pressure of 0 to 3000 psig, and a contact time equivalent to a LHSV of 0.1 to 100 hr. -1 , said combination being effective to provide a pretreated raffinate characterized by an initial equilibrium temperature not exceeding about 675° to 700° F. and at least 25° F. lower than that obtained with said raffinate without pretreatment when dewaxed at about 1 LHSV; and dewaxing said raffinate at a temperature not to exceed the lesser of said equilibrium temperature of said raffinate without pretreatment minus 25° F., or 700° F.
Claim 2
Dependent Claim 307 words
In a process for preparing a high quality lube base stock oil having a predetermined pour point in the range of about -25° to +30° F. from waxy crude oil, which process comprises: extracting a distillate fraction that boils within the range of 450° to 1100° F. or a deasphalted short residuum fraction of said waxy crude with a solvent selective for aromatic hydrocarbons to yield a raffinate from which undesirable compounds have been removed; contacting the raffinate and hydrogen gas with a dewaxing catalyst under dewaxing conditions effective to impart said predetermined pour point, said catalyst comprising a first crystalline zeolite having a dry crystal framework density of not less than about 1.6 grams per cubic centimeter and a constraint index of about 1 to about 12, thereby converting wax contained in the raffinate to lower boiling hydrocarbons; and, topping the dewaxed raffinate to remove therefrom components of a low molecular weight; the improvement, whereby the resistance to oxidation of said dewaxed raffinate is increased, which comprises: pretreating said raffinate, prior to dewaxing, with a sorbent comprising a second crystalline zeolite having an effective pore diameter equal to or larger than said first crystalline zeolite, said pretreating being conducted under a combination of conditions selected from a temperature of about 35° to about 350° F., a pressure of 0 to 3000 psig, and a contact time equivalent to a LHSV of 0.1 to 100 hr. -1 , said combination being effective to provide a pretreated raffinate characterized by an initial equilibrium temperature not exceeding about 675° to 700° F. and at least 25° F. lower than that obtained with said raffinate without pretreatment when dewaxed at about 1 LHSV; and dewaxing said raffinate at a temperature not to exceed the lesser of said equilibrium temperature of said raffinate without pretreatment minus 25° F., or 700° F.
Claim 3
Dependent Claim 30 words
The process described in claim 1 wherein said first crystalline zeolite is selected from the group consisting of ZSM-5, ZSM-11, intergrowths of ZSM-5 and ZSM-11, ZSM-12, ZSM-23, ZSM-38 and ZSM-48.
Claim 4
Dependent Claim 35 words
The process described in claim 1 wherein said first and said second crystalline zeolite are each individually selected from the group consisting of ZSM-5, ZSM-11, intergrowths of ZSM-5 and ZSM-11, ZSM-12, ZSM-23, ZSM-38 and ZSM-48.
Claim 5
Dependent Claim 19 words
The process described in claim 3 wherein said first and said second crystalline zeolite have the same crystal structure.
Claim 6
Dependent Claim 23 words
The process described in claim 3 wherein said first and said second zeolite have the same crystal structure and the same chemical compositions.
Claim 7
Dependent Claim 28 words
The process described in claim 2 or 3 or 4 or 5 wherein said crystalline zeolites are selected from the group consisting of ZSM-5, ZSM-11 and intergrowths thereof.
Claim 8
Dependent Claim 14 words
The process described in claim 2 wherein said second crystalline zeolite is hydrogen mordenite.
Claim 9
Dependent Claim 23 words
The process described in claim 7 wherein said first crystalline zeolite is selected from the group consisting of ZSM-5, ZSM-11 and intergrowths thereof.

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1985-11-01 1986-05-03 1986-11-02 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1989-11-01 1990-05-03 1990-11-02 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1993-11-01 1994-05-03 1994-11-02 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag