US2014008271A1PendingUtilityA1
Hydrocarbons recovery
Est. expirySep 10, 2030(~4.1 yrs left)· nominal 20-yr term from priority
E21B 43/40B01D 17/0214C10G 31/08C10G 2300/4081B01D 17/08B01D 17/085C10G 33/04B01D 17/047
35
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Claims
Abstract
Methods and systems of separating a hydrocarbon phase from a mixture comprising an emulsion of water and hydrocarbons in the presence of a surfactant, comprising adjusting the salinity of the mixture to release hydrocarbons and water from the emulsion into a hydrocarbon phase and a salt-containing aqueous phase respectively; and separating at least a part of the hydrocarbon phase from the salt-containing aqueous phase wherein at least a part of the salt-containing aqueous phase is recovered for further use.
Claims
exact text as granted — not AI-modified1 . A method of separating a hydrocarbon phase from a mixture comprising an emulsion of water and hydrocarbons in the presence of a surfactant, the method comprising:
adjusting the salinity of the mixture to release hydrocarbons and water from the emulsion into a hydrocarbon phase and a salt-containing aqueous phase respectively; and separating at least a part of the hydrocarbon phase from the salt-containing aqueous phase, wherein at least a part of the salt-containing aqueous phase is recovered for further use.
2 . A method according to claim 1 , further comprising reusing at least a part of the salt-containing aqueous phase to adjust the salinity of the mixture.
3 . A method according to claim 1 , wherein the salinity of the mixture is adjusted by increasing the salinity of the mixture.
4 . A method according to claim 1 further comprising desalinating the salt-containing aqueous phase to provide a first stream having a relatively high salinity and a second stream having a relatively low salinity.
5 . A method according to claim 4 further comprising reusing the high salinity stream to increase the salinity of the mixture.
6 . A method according to claim 4 further comprising reusing the low salinity stream to wash the hydrocarbon phase to recover surfactant.
7 . A hydrocarbons separation system comprising:
an inlet for introducing a mixture comprising an emulsion of water and hydrocarbons in the presence of a surfactant; a salinity adjustment station for adjusting the salinity of the mixture; separating means for separating from the mixture a hydrocarbon phase and a salt-containing aqueous phase; and recovery means for recovering at least a part of the salt-containing aqueous phase for further use.
8 . A system according to claim 7 wherein the recovery means comprises a conduit for recycling at least a part of the salt-containing aqueous phase to the salinity adjustment station to adjust the salinity of the mixture.
9 . A system according to claim 7 comprising a membrane for separating the hydrocarbon phase from the aqueous phase.
10 . A system according to claim 9 , wherein the membrane acts as the separating means, either alone or in combination with a phase separation vessel.
11 . A system according to any one of claim 7 , further comprising desalination means for desalinating the salt-containing aqueous phase to provide a first stream with a relatively high salinity and a second stream with a relatively low salinity.
12 . A system according to claim 11 , wherein the desalination means comprises a reverse osmosis unit, a nanofiltration unit, or a nanofiltration unit upstream of a reverse osmosis unit.
13 . A system according to claim 11 further comprising washing means for washing the hydrocarbon phase and recovering a surfactant recycle stream, and a conduit for channelling the second, low salinity stream to the washing means.
14 . A chemical enhanced oil recovery process comprising injecting surfactant recovered by the method of claim 5 into a hydrocarbon-bearing formation.
15 . A chemical oil recovery process according to claim 14 wherein the surfactant is combined with salt from the high salinity stream.Join the waitlist — get patent alerts
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