US4121996A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Hydrocracking process for the production of LPG
Assignee: Honeywell UOP LLC
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Filing: 1977-09-30
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Granted: 1978-10-24
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Expires: 1997-09-30
Abstract
Abstract Hydrocarbons are converted with a catalyst comprising a Group VIII metal component combined with an extruded support containing alumina and mordenite. Key feature of the process involves the critical quantities of mordenite and alumina present in the composition, thereby effecting and maximizing some basic enhancement of the ability of the resultant catalyst to accelerate hydrocarbon conversion reactions that depend on carbonium ion intermediates; i.e., the activity level of the resultant composite is markedly increased. The aforementioned critical quantities of alumina are about 15 to about 40 weight percent and that of mordenite are about 85 to about 60 weight percent, wherein both are calculated on the basis of the total weight of the carrier material.
Inventors
- 👤 Lee Hilfman
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-28 12:23
CPC Classifications
B; B01; B01J; B01J29/00; B01J29/04; B01J29/06; B01J29/18; B01J29/20; B01J29/22; C; C10; C10G; C10G2400/00; C10G2400/28
Claims Analysis
Total Claims: 7
Claim 1
Independent Claim
170 words
A hydrogen-consuming process for selectively producing LPG from a hydrocarbon charge stock boiling below about 600° F., which comprises contacting said charge stock and hydrogen with a catalyst comprising a Group VIII metal component combined with an extruded mordenite-alumina carrier material containing a uniform distribution of about 15 to about 40 weight percent of finely divided alumina particles, said mordenite being present in the range of about 85 to about 60 weight percent based on the total weight of said carrier material and having been treated to reduce the sodium content to less than about 5 weight percent Na 2 O and subsequently having been treated with an aqueous ammoniacal solution at a pH of at least about 9.5, at hydrocracking conditions including a pressure of about 300 to about 1800 psig., a temperature of about 600° F. to about 850° F., a LHSV of about 1 to about 60 hr. -1 and a hydrogen circulation rate of about 5000 SCFB to about 15,000 SCFB based on fresh charge stock.
Claim 2
Dependent Claim
170 words
A hydrogen-consuming process for selectively producing LPG from a hydrocarbon charge stock boiling below about 600° F., which comprises contacting said charge stock and hydrogen with a catalyst comprising a Group VIII metal component combined with an extruded mordenite-alumina carrier material containing a uniform distribution of about 15 to about 40 weight percent of finely divided alumina particles, said mordenite being present in the range of about 85 to about 60 weight percent based on the total weight of said carrier material and having been treated to reduce the sodium content to less than about 5 weight percent Na 2 O and subsequently having been treated with an aqueous ammoniacal solution at a pH of at least about 9.5, at hydrocracking conditions including a pressure of about 300 to about 1800 psig., a temperature of about 600° F. to about 850° F., a LHSV of about 1 to about 60 hr. -1 and a hydrogen circulation rate of about 5000 SCFB to about 15,000 SCFB based on fresh charge stock.
Claim 3
Dependent Claim
20 words
The process of claim 1 further characterized in that said Group VIII metal component is platinum or a platinum compound.
Claim 4
Dependent Claim
20 words
The process of claim 1 further characterized in that said Group VIII metal component is palladium or a palladium compound.
Claim 5
Dependent Claim
27 words
The process of claim 1 further characterized in that said Group VIII metal component is present in an amount from about 0.05 to about 1.5 weight percent.
Claim 6
Dependent Claim
20 words
The process of claim 1 further characterized in that said catalyst contains about 0.05 to about 1.5 weight percent halogen.
Claim 7
Dependent Claim
20 words
The process of claim 1 further characterized in that said catalyst contains about 0.1 to about 1.5 weight percent sulfur.
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) | 1981-10-23 | 1982-04-24 | 1982-10-24 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1985-10-23 | 1986-04-24 | 1986-10-24 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1989-10-23 | 1990-04-24 | 1990-10-24 | $7700.00 | Window Closed / Lapsed |