US4788374A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Zeolite catalysis
Assignee: Mobil Oil AS
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Filing: 1987-12-23
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Granted: 1988-11-29
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Expires: 2007-12-23
Abstract
Abstract A surface-inactive shape selective metallosilicate catalyst, useful for the conversion of lower molecular weight olefins to liquid hydrocarbons such as gasoline, distillate, and high viscosity lube oils, is prepared by a process comprising forming a silica shell on a metallosilicate core by crystallizing silica in the presence of fluoride ion onto the surface of the core.
Inventors
- 👤 Pochen Chu
- 👤 William E. Garwood
- 👤 Albert B. Schwartz
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-04 22:46
CPC Classifications
B; B01; B01J; B01J29/00; B01J29/04; B01J29/06; B01J29/40; B01J29/90; C; C07; C07C; C07C2/00; C07C2/02; C07C2/04; C07C2/06; C07C2/08; C07C2/12; C10; C10G; C10G50/00; B01J2229/00; B01J2229/10; B01J2229/12; B01J2229/123; B01J2229/16; B01J2229/30; B01J2229/32; C07C2529/00; C07C2529/04; C07C2529/06; C07C2529/40; C07C2529/70; Y; Y02; Y02P; Y02P20/00; Y02P20/50; Y02P20/584
Claims Analysis
Total Claims: 13
Claim 1
Independent Claim
168 words
A process for preparing hydrocarbons boiling in the gasoline and/or distillate range by contacting a feedstock comprising lower molecular weight olefins in a reaction zone under conditions of elevated temperature and pressure with a shape selective crystalline aluminosilicate catalyst, comprising: reducing the non-shape selective surface-cracking and/or surface isomerization activity of the aluminosilicate catalyst by a process comprising: preparing an aqueous solution comprising colloidal silica, optionally an organic directing agent, and a source of hydroxide ions; mixing the aqueous solution with an aqueous dispersion of shape-selective crystalline aluminosilicate to form a homogeneous mixture which is subsequently heated; adding an aqueous solution comprising a source of fluoride ions to the homogeneous mixture to form a reactive composition; heating the reactive composition at a temperature to effectively form a surface-deactivated catalyst comprising a crystalline fluoride-containing silica outer shell on an aluminosilicate; withdrawing the surface-deactivated catalyst from the reactive composition for washing, drying, and calcining of the catalyst; and removing the catalyst to the reaction zone for contact with the olefin feedstock.
Claim 2
Dependent Claim
168 words
A process for preparing hydrocarbons boiling in the gasoline and/or distillate range by contacting a feedstock comprising lower molecular weight olefins in a reaction zone under conditions of elevated temperature and pressure with a shape selective crystalline aluminosilicate catalyst, comprising: reducing the non-shape selective surface-cracking and/or surface isomerization activity of the aluminosilicate catalyst by a process comprising: preparing an aqueous solution comprising colloidal silica, optionally an organic directing agent, and a source of hydroxide ions; mixing the aqueous solution with an aqueous dispersion of shape-selective crystalline aluminosilicate to form a homogeneous mixture which is subsequently heated; adding an aqueous solution comprising a source of fluoride ions to the homogeneous mixture to form a reactive composition; heating the reactive composition at a temperature to effectively form a surface-deactivated catalyst comprising a crystalline fluoride-containing silica outer shell on an aluminosilicate; withdrawing the surface-deactivated catalyst from the reactive composition for washing, drying, and calcining of the catalyst; and removing the catalyst to the reaction zone for contact with the olefin feedstock.
Claim 3
Dependent Claim
15 words
A process according to claim 1 wherein the crystalline aluminosilicate catalyst comprises medium pore zeolite.
Claim 4
Dependent Claim
14 words
A process according to claim 2 wherein the medium pore aluminosilicate catalyst comprises ZSM-5.
Claim 5
Dependent Claim
95 words
A process for preparing a high viscosity index lube oil from a feedstock comprising lower molecular weight olefins comprising: contacting the feedstock at reaction conditions in a reaction zone with a catalyst comprising an inner portion and an outer portion disposed as a porous shell around the inner portion, the inner portion comprising a medium pore shape-selective crystalline acidic metallosilicate, and the outer portion comprising a fluoride-containing crystalline silica shell substantially free of acid sites; and withdrawing from the reaction zone a hydrocarbon liquid comprising a high viscosity index lube oil and higher boiling hydrocarbons.
Claim 6
Dependent Claim
95 words
A process for preparing a high viscosity index lube oil from a feedstock comprising lower molecular weight olefins comprising: contacting the feedstock at reaction conditions in a reaction zone with a catalyst comprising an inner portion and an outer portion disposed as a porous shell around the inner portion, the inner portion comprising a medium pore shape-selective crystalline acidic metallosilicate, and the outer portion comprising a fluoride-containing crystalline silica shell substantially free of acid sites; and withdrawing from the reaction zone a hydrocarbon liquid comprising a high viscosity index lube oil and higher boiling hydrocarbons.
Claim 7
Dependent Claim
21 words
A process according to claim 4 wherein the lube oil is separated and recovered as product boiling above about 340° C.
Claim 8
Dependent Claim
20 words
A process according to claim 5 wherein the product lube oil has a viscosity index of at least about 110.
Claim 9
Dependent Claim
21 words
The process according to claim 4 wherein the catalyst inner portion consists essentially of aluminosilicate zeolite having the structure of ZSM-5.
Claim 10
Dependent Claim
21 words
The process according to claim 4 wherein the catalyst inner portion consists essentially of aluminosilicate zeolite having the structure of ZSM-23.
Claim 11
Dependent Claim
22 words
A process according to claim 7 or 8 wherein the porous shell has substantially the same crystalline structure as the inner portion.
Claim 12
Dependent Claim
61 words
A process for the shape-selective conversion of hydrocarbons comprising; contacting the hydrocarbons at reaction conditions with a catalyst comprising an inner portion and an outer portion disposed as a porous shell around the inner portion, the inner portion comprising a shape-selective tetrahedrally coordinated crystalline acidic metallosilicate, and the outer portion comprising a fluoride-containing crystalline silica shell substantially free of acid sites.
Claim 13
Dependent Claim
61 words
A process for the shape-selective conversion of hydrocarbons comprising; contacting the hydrocarbons at reaction conditions with a catalyst comprising an inner portion and an outer portion disposed as a porous shell around the inner portion, the inner portion comprising a shape-selective tetrahedrally coordinated crystalline acidic metallosilicate, and the outer portion comprising a fluoride-containing crystalline silica shell substantially free of acid sites.
References Cited (Backward Citations)
US4203869A
Cited
US4670614A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1991-11-29 | 1992-05-30 | 1992-11-29 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1995-11-29 | 1996-05-30 | 1996-11-29 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1999-11-29 | 2000-05-30 | 2000-11-29 | $7700.00 | Window Closed / Lapsed |