US3950241A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method for upgrading a wide cut naphtha to full range gasoline
Assignee: Mobil Oil AS
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Filing: 1974-06-24
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Granted: 1976-04-13
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Expires: 1994-06-24
Abstract
Abstract Upgrading a full boiling range naphtha by the combination of reforming only a low boiling portion of the naphtha followed by contacting the reformate product thereof combined with the high boiling portion of the naphtha over a ZSM-5 type catalyst conversion operation is described.
Inventors
- 👤 John C. Bonacci
- 👤 William E. Garwood
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-31 20:06
CPC Classifications
C; C10; C10G; C10G59/00; C10G59/02
Claims Analysis
Total Claims: 12
Claim 1
Independent Claim
117 words
A method for improving the octane rating of a full boiling range naphtha to gasoline produce which comprises, separating a full range naphtha to recover a low boiling naphtha fraction thereof substantially free of dicyclic naphthenes from a higher boiling naphtha fraction containing said dicyclic naphthenes, reforming said low boiling fraction under conditions of severity selected to increase the octane rating of gasoline boiling range product, combining the product of the reforming operation with said higher boiling naphtha fraction containing dicyclic naphthenes and passing the combined materials comprising product of reforming and said higher boiling naphtha fraction in contact with a ZSM-5 type crystalline zeolite catalyst under exothermic temperature conditions within the range of 500° to 900°F.
Claim 2
Independent Claim
117 words
A method for improving the octane rating of a full boiling range naphtha to gasoline produce which comprises, separating a full range naphtha to recover a low boiling naphtha fraction thereof substantially free of dicyclic naphthenes from a higher boiling naphtha fraction containing said dicyclic naphthenes, reforming said low boiling fraction under conditions of severity selected to increase the octane rating of gasoline boiling range product, combining the product of the reforming operation with said higher boiling naphtha fraction containing dicyclic naphthenes and passing the combined materials comprising product of reforming and said higher boiling naphtha fraction in contact with a ZSM-5 type crystalline zeolite catalyst under exothermic temperature conditions within the range of 500° to 900°F.
Claim 3
Dependent Claim
31 words
The method of claim 1 wherein the high boiling naphtha fraction is relied upon to cool the product of reforming to a temperature suitable for contact with the crystalline zeolite catalyst.
Claim 4
Dependent Claim
32 words
The method of claim 1 wherein reforming of the low boiling naphtha fraction is accomplished in not more than two separate beds of reforming catalyst before contact with said crystalline zeolite catalyst.
Claim 5
Dependent Claim
17 words
The method of claim 1 wherein the combined material catalyst is promoted with a metal hydrogenating component.
Claim 6
Dependent Claim
34 words
The method of claim 1 wherein the reforming of the low boiling naphtha fraction is accomplished under conditions providing a reformate product of an octane rating in the range of 92 to 96 (R+O).
Claim 7
Dependent Claim
19 words
The method of claim 1 wherein the total product of reforming is combined with said higher boiling naphtha fraction.
Claim 8
Dependent Claim
24 words
The method of claim 1 wherein only the normally liquid portion of the product of reforming is combined with the higher boiling naphtha fraction.
Claim 9
Dependent Claim
25 words
The method of claim 1 wherein a heavy naphtha product of hydrocracking is combined with combined material passed in contact with said crystalline zeolite catalyst.
Claim 10
Dependent Claim
30 words
The method of claim 1 wherein a blend of heavy naphtha with the normally liquid product of reforming is restricted to within the range of 10 to 30 volume percent.
Claim 11
Dependent Claim
46 words
The method of claim 1 wherein the blend of heavy naphtha and the product of reforming is subjected to a ZSM-5 zeolite catalyst conversion conditions including a temperature within the range of 500° to 900°F. at a pressure within the range of 200 to 600 psig.
Claim 12
Dependent Claim
18 words
The method of claim 1 wherein the crystalline zeolite conversion is accomplished in a fluid catalyst bed operation.
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) | 1979-04-13 | 1979-10-13 | 1980-04-13 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1983-04-13 | 1983-10-13 | 1984-04-13 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1987-04-13 | 1987-10-13 | 1988-04-13 | $7700.00 | Window Closed / Lapsed |