US4292166A
Expired / Lapsed
US
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Catalytic process for manufacture of lubricating oils
Assignee: Mobil Oil AS
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Filing: 1980-07-07
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Granted: 1981-09-29
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Expires: 2000-07-07
Abstract
Abstract A method is disclosed for converting an asphalt-free heavy hydrocarbon oil to high V.I. low pour point lube base stock and naphtha. The heavy oil is first catalytically dewaxed with a catalyst such as Ni-ZSM-5 and the dewaxed oil is then hydrocracked, or hydroconverted with a large pore zeolite catalyst such as dealuminized Y or ZSM-20 associated with palladium. The V.I. is controlled by the severity of the hydroconversion step.
Inventors
- 👤 Robert L. Gorring
- 👤 Rene B. La Pierre
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-30 01:32
CPC Classifications
C; C10; C10G; C10G45/00; C10G45/44; C10G45/46; C10G45/54; C10G2400/00; C10G2400/10
Claims Analysis
Total Claims: 24
Claim 1
Independent Claim
175 words
A method for catalytically converting a hydrocarbon oil feedstock boiling above 650° F. (343° C.) and selected from the group consisting of vacuum gas oils, deasphalted oils, and mixtures thereof, to low-pour, high V.I. lube basestock, which method comprises contacting said feedstock and hydrogen with a dewaxing catalyst comprising a zeolite having a Constaint Index of 1 to 12, said contacting conditions being effective to reduce the pour point of the +650° F. (+343° C.) fraction of said feedstock to less than about +15° F. (-9° C.); contacting said dewaxed feedstock and hydrogen with a hydroconversion catalyst comprising a platinum group metal and a zeolite having a silica to alumina ratio of at least 6, said zeolite being selected from the group consisting of Dealuminized Y and ZSM-20, said contacting with said hydroconversion catalyst being at a temperature of 400°-1000° F. (204°-537° C.), a pressure of 500-3500 psig, and at a space velocity of 0.1 to 10 L.H.S.V.; and recovering said lube oil base stock having a pour point not higher than about 25° F.
Claim 2
Independent Claim
175 words
A method for catalytically converting a hydrocarbon oil feedstock boiling above 650° F. (343° C.) and selected from the group consisting of vacuum gas oils, deasphalted oils, and mixtures thereof, to low-pour, high V.I. lube basestock, which method comprises contacting said feedstock and hydrogen with a dewaxing catalyst comprising a zeolite having a Constaint Index of 1 to 12, said contacting conditions being effective to reduce the pour point of the +650° F. (+343° C.) fraction of said feedstock to less than about +15° F. (-9° C.); contacting said dewaxed feedstock and hydrogen with a hydroconversion catalyst comprising a platinum group metal and a zeolite having a silica to alumina ratio of at least 6, said zeolite being selected from the group consisting of Dealuminized Y and ZSM-20, said contacting with said hydroconversion catalyst being at a temperature of 400°-1000° F. (204°-537° C.), a pressure of 500-3500 psig, and at a space velocity of 0.1 to 10 L.H.S.V.; and recovering said lube oil base stock having a pour point not higher than about 25° F.
Claim 3
Dependent Claim
27 words
The method described in claim 1 wherein said zeolite having a Constraint Index of 1 to 12 is selected from the group consisting of ZSM-5 and ZSM-11.
Claim 4
Dependent Claim
24 words
The method described in claim 1 wherein said contacting with said hydroconversion catalyst is conducted at a pressure of 750 to about 2000 psig.
Claim 5
Dependent Claim
24 words
The method described in claim 2 wherein said contacting with said hydroconversion catalyst is conducted at a pressure of 750 to about 2000 psig.
Claim 6
Dependent Claim
12 words
The method described in claim 2 wherein said hydroconversion catalyst is ZSM-20.
Claim 7
Dependent Claim
12 words
The method described in claim 3 wherein said hydroconversion catalyst is ZSM-20.
Claim 8
Dependent Claim
12 words
The method described in claim 4 wherein said hydroconversion catalyst is ZSM-20.
Claim 9
Dependent Claim
26 words
The method described in claim 1 or 2 or 3 or 4 or 5 or 6 or 7 wherein said feedstock is a vacuum gas oil.
Claim 10
Dependent Claim
25 words
The method described in claim 1 or 2 or 3 or 4 or 5 or 6 or 7 wherein said platinum group metal is palladium.
Claim 11
Dependent Claim
29 words
The method described in claim 1 wherein is included the step of hydrotreating said dewaxed feedstock whereby its organic nitrogen content is reduced to less than about 200 ppm.
Claim 12
Dependent Claim
29 words
The method described in claim 2 wherein is included the step of hydrotreating said dewaxed feedstock whereby its organic nitrogen content is reduced to less than about 200 ppm.
Claim 13
Dependent Claim
29 words
The method described in claim 3 wherein is included the step of hydrotreating said dewaxed feedstock whereby its organic nitrogen content is reduced to less than about 200 ppm.
Claim 14
Dependent Claim
29 words
The method described in claim 4 wherein is included the step of hydrotreating said dewaxed feedstock whereby its organic nitrogen content is reduced to less than about 200 ppm.
Claim 15
Dependent Claim
29 words
The method described in claim 5 wherein is included the step of hydrotreating said dewaxed feedstock whereby its organic nitrogen content is reduced to less than about 200 ppm.
Claim 16
Dependent Claim
29 words
The method described in claim 6 wherein is included the step of hydrotreating said dewaxed feedstock whereby its organic nitrogen content is reduced to less than about 200 ppm.
Claim 17
Dependent Claim
29 words
The method described in claim 7 wherein is included the step of hydrotreating said dewaxed feedstock whereby its organic nitrogen content is reduced to less than about 200 ppm.
Claim 18
Dependent Claim
26 words
The method described in claim 10 or 11 or 12 or 13 or 14 or 15 or 16 wherein said feedstock is a vacuum gas oil.
Claim 19
Dependent Claim
25 words
The method described in claim 10 or 11 or 12 or 13 or 14 or 15 or 16 wherein said platinum group metal is palladium.
Claim 20
Dependent Claim
167 words
In a process for catalytically converting a waxy hydrocarbon oil boiling above 650° F. (343° C.) and substantially free of asphalt to a high V.I low pour point lube base stock, which process comprises catalytically dewaxing said oil, the improvement whereby an increased yield of said high V.I. low pour point lube base stock is obtained, which comprises, in combination: contacting said waxy hydrocarbon oil and hydrogen in a first reaction zone with a zeolite catalyst having a Constraint Index of 1 to 12 and a silica to alumina ratio above 12, said contacting being at a temperature of 400°-1000° F. (204°-537° C.), a pressure of 500-3500 psig, and a L.H.S.V. of 0.1-10 hr -1 , thereby dewaxing said oil; contacting said dewaxed oil and hydrogen in a second reaction zone with a large pore hydrocracking or a hydroconversion catalyst under conditions effective to increase the V.I. of the lube oil fraction of said dewaxed oil; and recovering said high V.I. low pour point lube base stock.
Claim 21
Dependent Claim
167 words
In a process for catalytically converting a waxy hydrocarbon oil boiling above 650° F. (343° C.) and substantially free of asphalt to a high V.I low pour point lube base stock, which process comprises catalytically dewaxing said oil, the improvement whereby an increased yield of said high V.I. low pour point lube base stock is obtained, which comprises, in combination: contacting said waxy hydrocarbon oil and hydrogen in a first reaction zone with a zeolite catalyst having a Constraint Index of 1 to 12 and a silica to alumina ratio above 12, said contacting being at a temperature of 400°-1000° F. (204°-537° C.), a pressure of 500-3500 psig, and a L.H.S.V. of 0.1-10 hr -1 , thereby dewaxing said oil; contacting said dewaxed oil and hydrogen in a second reaction zone with a large pore hydrocracking or a hydroconversion catalyst under conditions effective to increase the V.I. of the lube oil fraction of said dewaxed oil; and recovering said high V.I. low pour point lube base stock.
Claim 22
Dependent Claim
31 words
The process described in claim 19 wherein said zeolite catalyst having a Constraint Index of 1 to 12 is ZSM-5 or ZSM-11, and said contacting temperature is 450°-850° F. (232°-454° C.).
Claim 23
Dependent Claim
63 words
The process described in claim 20 wherein a hydroconversion catalyst is used, said catalyst comprising a platinum group metal and a zeolite having a silica to alumina ratio of at least six, said zeolite being selected from the group consisting of dealuminized Y and ZSM-20, and wherein contacting with said hydroconversion catalyst is conducted at a pressure of 750 to about 2000 psig.
Claim 24
Dependent Claim
41 words
The process described in claim 19 or 20 or 21 wherein said dewaxed oil from said first reaction zone is hydrotreated to reduce its nitrogen content to less than about 200 ppm prior to contact with said hydrocracking or hydroconversion catalyst.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1984-09-28 | 1985-03-30 | 1985-09-29 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1988-09-28 | 1989-03-30 | 1989-09-29 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1992-09-28 | 1993-03-30 | 1993-09-29 | $7700.00 | Window Closed / Lapsed |