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Reverse osmosis process for recovery of C3 -C6 aliphatic hydrocarbon from oil

Assignee: ExxonMobil Technology and Engineering Co
•
Filing: 1991-06-27
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Granted: 1992-07-28
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Expires: 2011-06-27
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Abstract

Abstract Solvents comprising C3, C4, C5 and C6 aliphatic hydrocarbons (i.e. propane, propylene, butane, butylene, pentane, cyclopentane, pentene, hexane, cyclohexane, hexene and their isomers) and mixtures thereof, preferably C3 and C4 hydrocarbons and mixtures thereof are recovered from hydrocarbon oils in the liquid phase by the reverse osmosis permeation of said solvent through a polyimide reverse osmosis membrane at low temperature.

Inventors

  • 👤 Lucie Y. LaFreniere

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-10 02:02
CPC Classifications
B; B01; B01D; B01D61/00; B01D61/02; B01D61/025; C; C10; C10G; C10G31/00; C10G31/11

Claims Analysis

Total Claims: 10
Claim 1
Independent Claim 81 words
A method for recovering solvents selected from the group consisting of C 3 , C 4 , C 5 and C 6 aliphatic hydrocarbons and mixtures thereof from oil, said method comprising contacting the solvent containing oil with one side of a reverse osmosis membrane under reverse osmosis conditions and a temperature between about 20° C. and the cloud point of the oil feed to thereby selectively permeate the solvent through the membrane, and recovering the solvent as permeate for reuse.
Claim 2
Independent Claim 81 words
A method for recovering solvents selected from the group consisting of C 3 , C 4 , C 5 and C 6 aliphatic hydrocarbons and mixtures thereof from oil, said method comprising contacting the solvent containing oil with one side of a reverse osmosis membrane under reverse osmosis conditions and a temperature between about 20° C. and the cloud point of the oil feed to thereby selectively permeate the solvent through the membrane, and recovering the solvent as permeate for reuse.
Claim 3
Dependent Claim 24 words
The method of claim 1 wherein the solvent is selected from the group consisting of C 3 and C 4 hydrocarbons and mixtures thereof.
Claim 4
Dependent Claim 17 words
The method of claim 2 wherein the solvent is selected from propane and butane and mixtures thereof.
Claim 5
Dependent Claim 31 words
The method of claim 1, 2 or 3 wherein the reverse osmosis process is conducted at a temperature of between about -10° C. and the cloud point of the oil feed.
Claim 6
Dependent Claim 27 words
The method of claim 1, 2 or 3 wherein the reverse osmosis process is practiced at an apparent pressure differential of between about 50 to 1500 psi.
Claim 7
Dependent Claim 15 words
The method of claim 1, 2 or 3 wherein the reverse osmosis membrane is polyimide.
Claim 8
Dependent Claim 22 words
The method of claim 6 wherein the polyimide reverse osmosis membrane has a pore size in the range 0.0001 to 0.00 μm.
Claim 9
Dependent Claim 14 words
The method of claim 4 wherein the polyimide reverse osmosis membrane is asymmetric polyimide.
Claim 10
Dependent Claim 25 words
The method of claim 4 wherein the reverse osmosis membrane is asymmetric polyimide and has a pore size in the range 0.0001 to 0.001 μm.

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1995-07-28 1996-01-27 1996-07-28 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1999-07-28 2000-01-27 2000-07-28 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2003-07-28 2004-01-27 2004-07-28 $7700.00 Window Closed / Lapsed

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