US4547613A
Expired / Lapsed
US
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Process for converting olefins to high viscosity index lubricants
Assignee: Mobil Oil AS
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Filing: 1984-07-10
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Granted: 1985-10-15
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Expires: 2004-07-10
Abstract
Abstract Hydrocarbon streams containing primarily olefins such as ethylene up to and inclusive of C16 olefins are converted at elevated pressures to high viscosity index lube oil base stock by contacting them with a ZSM-5 type zeolite catalyst which has been conditioned by previous contact with a light olefin preferably of 3-6 carbon atoms per molecule under suitable conditions of temperature and pressure.
Inventors
- 👤 William E. Garwood
- 👤 Hans J. Schoennagel
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-01 08:02
CPC Classifications
C; C10; C10G; C10G50/00; C10G50/02; B; B01; B01J; B01J29/00; B01J29/04; B01J29/06; B01J29/40; B01J29/65; B01J29/70
Claims Analysis
Total Claims: 16
Claim 1
Independent Claim
159 words
A process of converting an olefinic stream containing light olefins having an average of 2 to 16 carbon atoms per molecule to a high viscosity index lube oil charge stock comprising: (a) passing a light hydrocarbon gas of 3 to 6 carbon atoms per molecule over a ZSM-5 type catalyst to condition said catalyst at treating conditions of 0-100 psig, a temperature between about 400° F. and about 1000° F., and a weight hourly space velocity of between 0.1 and about 5; (b) thereafter passing over said treated catalyst an olefin feedstock comprising olefins of an average number of carbon atoms per molecule of 2 to 16 at a pressure of 400-5000 psig, a temperature of 350° F. to 650° F., and a WHSV of 0.1-1.0; (c) collecting the effluent stream therefrom; and (d) fractionating said effluent stream into a high boiling point lube oil stock fraction, having a viscosity index greater than that produced by unconditioned fresh catalyst.
Claim 2
Dependent Claim
159 words
A process of converting an olefinic stream containing light olefins having an average of 2 to 16 carbon atoms per molecule to a high viscosity index lube oil charge stock comprising: (a) passing a light hydrocarbon gas of 3 to 6 carbon atoms per molecule over a ZSM-5 type catalyst to condition said catalyst at treating conditions of 0-100 psig, a temperature between about 400° F. and about 1000° F., and a weight hourly space velocity of between 0.1 and about 5; (b) thereafter passing over said treated catalyst an olefin feedstock comprising olefins of an average number of carbon atoms per molecule of 2 to 16 at a pressure of 400-5000 psig, a temperature of 350° F. to 650° F., and a WHSV of 0.1-1.0; (c) collecting the effluent stream therefrom; and (d) fractionating said effluent stream into a high boiling point lube oil stock fraction, having a viscosity index greater than that produced by unconditioned fresh catalyst.
Claim 3
Dependent Claim
35 words
The process of claim 1 wherein said crystalline zeolite is ZSM-5, ZSM-11, ZSM-12, ZSM-23, ZSM-35, ZSM-38, ZSM-48 or a zeolite having the X-ray diffraction pattern of Table 1 or Table 2 of the specification herein.
Claim 4
Dependent Claim
12 words
The process of claim 2 wherein said zeolite is an acid form.
Claim 5
Dependent Claim
13 words
The process of claim 1 wherein said zeolite consists essentially of HZSM-5 zeolite.
Claim 6
Dependent Claim
17 words
The process of claim 4 wherein the olefin in both step (a) and step (b) is propylene.
Claim 7
Dependent Claim
9 words
The product produced by the process of claim 1.
Claim 8
Dependent Claim
9 words
The product produced by the process of claim 2.
Claim 9
Dependent Claim
9 words
The product produced by the process of claim 3.
Claim 10
Dependent Claim
9 words
The product produced by the process of claim 4.
Claim 11
Dependent Claim
9 words
The product produced by the process of claim 5.
Claim 12
Dependent Claim
140 words
In the process for converting light olefin to lubricant stock by contacting the light olefin with an acidic crystalline zeolite catalyst having a silica-to-alumina mole ratio of at least 12 and a Constraint Index of about 1 to 12 at a reaction temperature of about 350° to 650° F., pressure of about 400 to 5000 psig and weight hourly space velocity of about 0.1 to 1, wherein the reaction effluent is fractionated to recover a high viscosity index lubricant oil base stock product having a boiling point above about 600° F.; the improvement which comprises: preconditioning said zeolite catalyst by contacting fresh catalyst with light olefin at elevated temperature above 450° F. at conditioning pressure below about 100 psig to provide a conditioned catalyst, whereby said lubricant product has increased viscosity index as compared to that produced by unconditioned catalyst.
Claim 13
Dependent Claim
140 words
In the process for converting light olefin to lubricant stock by contacting the light olefin with an acidic crystalline zeolite catalyst having a silica-to-alumina mole ratio of at least 12 and a Constraint Index of about 1 to 12 at a reaction temperature of about 350° to 650° F., pressure of about 400 to 5000 psig and weight hourly space velocity of about 0.1 to 1, wherein the reaction effluent is fractionated to recover a high viscosity index lubricant oil base stock product having a boiling point above about 600° F.; the improvement which comprises: preconditioning said zeolite catalyst by contacting fresh catalyst with light olefin at elevated temperature above 450° F. at conditioning pressure below about 100 psig to provide a conditioned catalyst, whereby said lubricant product has increased viscosity index as compared to that produced by unconditioned catalyst.
Claim 14
Dependent Claim
36 words
The process of claim 11 wherein the catalyst comprises ZSM-5 and wherein olefin or olefin mixture having an average of 3-6 carbon atoms is converted to an effluent containing at least 10 wt % lubricant oil.
Claim 15
Dependent Claim
23 words
The process of claim 12 wherein the catalyst consists essentially of acid ZSM-5 having a silica-to-alumina ratio of at least 40 to 1.
Claim 16
Dependent Claim
12 words
The process of claim 11 wherein the lubricant oil product is hydrogenated.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1988-10-14 | 1989-04-15 | 1989-10-15 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1992-10-14 | 1993-04-15 | 1993-10-15 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1996-10-14 | 1997-04-15 | 1997-10-15 | $7700.00 | Window Closed / Lapsed |