Patent US5030339A successfully refreshed from Google Patents.
US5030339A
Expired / Lapsed
US
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Separation of gas and oil mixtures
Assignee: Costain Engineering Ltd
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Filing: 1989-10-13
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Granted: 1991-07-09
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Expires: 2009-10-13
Abstract
Abstract In the separation of a compressed multi-component hydrocarbon stream containing liquid and gas phases to produce a liquid product stream having a specified maximum vapor pressure and a gas product stream having a specified maximum cricondenbar, gas flaring can be reduced and other advantages obtained by the method of (i) separating the liquid and gas phases in one or more separation stages at progressively reduced pressures to produce said liquid product stream, and (ii) treating the recovered gas phase to obtain the gas product stream by partial condensation of the recovered gas phase and separation of the condensate so formed; wherein (iii) step (ii) includes the step of rectifying the recovered gas phase in a refluxing exchanger and separating the condensate so formed.
Inventors
- 👤 Bogdan A. Czarnecki
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-08 19:30
CPC Classifications
C; C10; C10G; C10G5/00; C10G5/06; F; F25; F25J; F25J3/00; F25J3/02; F25J3/0204; F25J3/0209; F25J3/0228; F25J3/0233; F25J3/0247; F25J2200/00; F25J2200/02; F25J2200/80; F25J2205/00; F25J2205/02
Claims Analysis
Total Claims: 5
Claim 1
Independent Claim
141 words
In a process for separating a compressed multi-component hydrocarbon stream containing liquid and gas phases to produce a liquid product stream having a specified maximum vapour pressure, a gas product stream having a specified maximum cricondenbar, and a further gas stream containing C 4 + hydrocarbons, the method of reducing the amount of said further gas stream which comprises: (i) separating the liquid and gas phases in one or more separation stages at progressively reduced pressures to produce said liquid product stream, and (ii) treating the recovered gas phase to obtain said gas product stream by partial condensation of said recovered gas phase and separation of the condensate so formed; wherein (iii) step (ii) includes the step of rectifying said recovered gas phase in a refluxing exchanger, separating the condensate so formed, and recovering said further gas stream from the condensate.
Claim 2
Dependent Claim
141 words
In a process for separating a compressed multi-component hydrocarbon stream containing liquid and gas phases to produce a liquid product stream having a specified maximum vapour pressure, a gas product stream having a specified maximum cricondenbar, and a further gas stream containing C 4 + hydrocarbons, the method of reducing the amount of said further gas stream which comprises: (i) separating the liquid and gas phases in one or more separation stages at progressively reduced pressures to produce said liquid product stream, and (ii) treating the recovered gas phase to obtain said gas product stream by partial condensation of said recovered gas phase and separation of the condensate so formed; wherein (iii) step (ii) includes the step of rectifying said recovered gas phase in a refluxing exchanger, separating the condensate so formed, and recovering said further gas stream from the condensate.
Claim 3
Dependent Claim
47 words
A method as claimed in claim 1 which further includes stripping condensate obtained from said rectification step (iii) to recover said further gas stream overhead, and including liquid bottoms from the stripping step in the feed to at least one of the separation stages of step (i).
Claim 4
Dependent Claim
24 words
A method as claimed in claim 2 in which said liquid bottoms is included in the feed to the last of said separation stages.
Claim 5
Dependent Claim
44 words
A method as claimed in claim 1 wherein said multi-component hydrocarbon stream comprises a wellhead gas/oil mixture, said liquid product stream comprises crude oil and said gas product stream comprises methane, ethane and propane substantially free of hydrocarbon containing four or more carbon atoms.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1994-07-08 | 1995-01-07 | 1995-07-09 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1998-07-08 | 1999-01-07 | 1999-07-09 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2002-07-08 | 2003-01-07 | 2003-07-09 | $7700.00 | Window Closed / Lapsed |