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US3996129A Expired / Lapsed US ⏱️ 0.0 years remaining

Reaction product effluent separation process

Assignee: Universal Oil Products Co
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Filing: 1975-05-12
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Granted: 1976-12-07
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Expires: 1995-05-12
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Abstract

Abstract A reaction product effluent, containing hydrogen, normally gaseous hydrocarbons and normally liquid hydrocarbons, is separated into desired component streams in a system which incorporates a low-pressure flash zone, a debutanizer and a deethanizer. The net overhead vaporous product from the deethanizer is introduced into the flash zone, the liquid phase from which serves as a portion of the feed to the debutanizer. Preferably, the net overhead vaporous product from the debutanizer is also introduced into the flash zone.

Inventors

  • 👤 James D. Weith

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-06 03:22
CPC Classifications
C; C10; C10G; C10G35/00; C10G35/04

Claims Analysis

Total Claims: 12
Claim 1
Independent Claim 237 words
A process for separating a hydrocarbon conversion reaction product effluent containing (i) hydrogen, (ii) normally gaseous hydrocarbons and, (iii) normally liquid hydrocarbons, which process comprises the sequential steps of: a. introducing said effluent into a first separation zone, at a lower temperature, to provide a hydrogen-rich first vaporous phase and a first liquid phase; b. introducing said first liquid phase into a second separation zone, at substantially the same temperature and a reduced pressure, to provide a second liquid phase and to recover a C 1 /C 2 concentrated second vaporous phase; c. separating said second liquid phase, in a first fractionation zone, at fractionation conditions selected to provide (i) a C 5 -plus concentrated normally liquid hydrocarbon stream and, (ii) a C 4 -minus concentrated third vaporous phase; d. condensing and separating said third vaporous phase to recover a C 1 /C 2 concentrated fourth vaporous phase and to provide a first C 3 /C 4 concentrated stream; e. separating at least a portion of said first C 3 /C 4 concentrated stream, in a second fractionation zone, at fractionation conditions selected to recover a second C 3 /C 4 concentrated stream and to provide a C 1 /C 2 concentrated fifth vaporous phase; and, f. combining at least a portion of said C 1 /C 2 concentrated fifth vaporous phase with said first liquid phase and introducing the resulting mixture into said second separation zone.
Claim 2
Dependent Claim 237 words
A process for separating a hydrocarbon conversion reaction product effluent containing (i) hydrogen, (ii) normally gaseous hydrocarbons and, (iii) normally liquid hydrocarbons, which process comprises the sequential steps of: a. introducing said effluent into a first separation zone, at a lower temperature, to provide a hydrogen-rich first vaporous phase and a first liquid phase; b. introducing said first liquid phase into a second separation zone, at substantially the same temperature and a reduced pressure, to provide a second liquid phase and to recover a C 1 /C 2 concentrated second vaporous phase; c. separating said second liquid phase, in a first fractionation zone, at fractionation conditions selected to provide (i) a C 5 -plus concentrated normally liquid hydrocarbon stream and, (ii) a C 4 -minus concentrated third vaporous phase; d. condensing and separating said third vaporous phase to recover a C 1 /C 2 concentrated fourth vaporous phase and to provide a first C 3 /C 4 concentrated stream; e. separating at least a portion of said first C 3 /C 4 concentrated stream, in a second fractionation zone, at fractionation conditions selected to recover a second C 3 /C 4 concentrated stream and to provide a C 1 /C 2 concentrated fifth vaporous phase; and, f. combining at least a portion of said C 1 /C 2 concentrated fifth vaporous phase with said first liquid phase and introducing the resulting mixture into said second separation zone.
Claim 3
Dependent Claim 22 words
The process of claim 1 further characterized in that said methane/ethane concentrated fourth vaporous phase is introduced into said second separation zone.
Claim 4
Dependent Claim 29 words
The process of claim 1 further characterized in that said first separation zone is maintained at a pressure at least about 50 psig. higher than said reaction product effluent.
Claim 5
Dependent Claim 29 words
The process of claim 1 further characterized in that said second separation zone is maintained at a pressure at least about 75 psig. lower than said first separation zone.
Claim 6
Dependent Claim 50 words
The process of claim 1 further characterized in that said reaction product effluent is separated at substantially the same pressure and at a lower temperature, in an initial separation zone, the vapor phase and liquid phase from which are increased in pressure, admixed and introduced into said first separation zone.
Claim 7
Dependent Claim 40 words
The process of claim 5 further characterized in that said initial separation zone is maintained at a temperature in the range of about 60° F. to about 140° F. and a pressure from about 100 psig. to about 300 psig.
Claim 8
Dependent Claim 40 words
The process of claim 1 further characterized in that said first separation zone is maintained at a temperature of about 60° F. to about 140° F. and a pressure in the range of about 150 psig. to about 400 psig.
Claim 9
Dependent Claim 37 words
The process of claim 1 further characterized in that said second separation zone is maintained at a temperature of about 60° F. to about 140° F. and a pressure of about 75 psig. to about 325 psig.
Claim 10
Dependent Claim 39 words
The process of claim 1 further characterized in that the methane/ethane concentration in said fourth vaporous phase is at least about 50.0%, and that the C 3 /C 4 concentration in said first stream is at least about 65.0%.
Claim 11
Dependent Claim 44 words
The process of claim 1 further characterized in that the concentration of C 1 /C 2 in said fifth vaporous phase is at least about 65.0% and that the concentration of C 3 /C 4 in said second stream is at least about 95.0%.
Claim 12
Dependent Claim 20 words
The process of claim 1 further characterized in that said reaction product effluent emanates from a catalytic reforming reaction zone.

References Cited (Backward Citations)

US3477946A Cited
US3520800A Cited
US3574089A Cited
US3753892A Cited
US3801494A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1979-12-07 1980-06-07 1980-12-07 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1983-12-07 1984-06-07 1984-12-07 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1987-12-07 1988-06-07 1988-12-07 $7700.00 Window Closed / Lapsed

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