US4310409A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Thermal cracking of heavy fraction of hydrocarbon hydrogenate
Assignee: Linde GmbH
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Filing: 1980-10-16
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Granted: 1982-01-12
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Expires: 2000-10-16
Abstract
Abstract To obtain olefins by the thermal cracking of hydrocarbons, e.g., vacuum gas oil, by hydrogenation and subsequent steam cracking, an intermediate fractionation of the hydrogenate is provided so that the light fraction enriched in branched isomers can be used as fuel and the heavy fraction only is subjected to the steam cracking.
Inventors
- 👤 Hans J. Wernicke
- 👤 Walter Kreuter
- 👤 Claus Schliebener
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-08 16:27
CPC Classifications
C; C10; C10G; C10G69/00; C10G69/02; C10G69/06; C10G2400/00; C10G2400/20
Claims Analysis
Total Claims: 4
Claim 1
Independent Claim
129 words
In a process for the cracking of heavy liquid hydrocarbon feed mixtures having a normal boiling point over 200° C. and containing monoaromatics and polyaromatics by hydrogenation of said feed and subsequent thermal cracking of resultant feed to obtain olefins, the improvement comprising the hydrogenation step being conducted under conditions such that the polyaromatics are extensively hydrogenated, and wherein between the hydrogenation step and the thermal cracking stage, there is provided an intermediate step of separating the hydrogenation product into a (i) light fraction containing the major proportion of the monoaromatics and (ii) a heavy liquid fraction, said heavy liquid fraction being substantially less isomerized than said light fraction, and subjecting only said heavy liquid fraction to the thermal cracking stage to obtain a product stream rich in ethylene.
Claim 2
Dependent Claim
129 words
In a process for the cracking of heavy liquid hydrocarbon feed mixtures having a normal boiling point over 200° C. and containing monoaromatics and polyaromatics by hydrogenation of said feed and subsequent thermal cracking of resultant feed to obtain olefins, the improvement comprising the hydrogenation step being conducted under conditions such that the polyaromatics are extensively hydrogenated, and wherein between the hydrogenation step and the thermal cracking stage, there is provided an intermediate step of separating the hydrogenation product into a (i) light fraction containing the major proportion of the monoaromatics and (ii) a heavy liquid fraction, said heavy liquid fraction being substantially less isomerized than said light fraction, and subjecting only said heavy liquid fraction to the thermal cracking stage to obtain a product stream rich in ethylene.
Claim 3
Dependent Claim
17 words
A process according to claim 1, said heavy fraction contains only components boiling at above 340° C.
Claim 4
Dependent Claim
23 words
A process according to claim 1, where the heavy hydrocarbon mixture used as feed to the hydrogenation step is a vacuum gas oil.
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) | 1985-01-11 | 1985-07-13 | 1986-01-12 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1989-01-11 | 1989-07-13 | 1990-01-12 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1993-01-11 | 1993-07-13 | 1994-01-12 | $7700.00 | Window Closed / Lapsed |