US2025198260A1PendingUtilityA1
Method for carbon dioxide injection into a subterranean reservoir
Est. expiryMar 15, 2042(~15.6 yrs left)· nominal 20-yr term from priority
Inventors:Søren Mylius Davidsen
E21B 47/10E21B 47/06E21B 47/07E21B 43/164E21B 43/166E21B 41/0064
46
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Claims
Abstract
The present invention relates to a method for CO 2 storage, the method comprising injecting a CO 2 composition into a well of a subterranean reservoir, wherein the CO 2 composition is formed by combining a stream of vapor CO 2 and a stream of liquid CO 2 at a vapor CO 2 to liquid CO 2 ratio, wherein the vapor CO 2 to liquid CO 2 ratio varies over time. The invention also relates to an installation for CO 2 storage.
Claims
exact text as granted — not AI-modified1 . A method for CO 2 storage, the method comprising injecting a CO 2 composition into a well of a subterranean reservoir, wherein the CO 2 composition is formed by combining a stream of vapor CO 2 and a stream of liquid CO 2 at a vapor CO 2 to liquid CO 2 ratio, wherein the vapor CO 2 to liquid CO 2 ratio varies over time.
2 . The method according claim 1 , comprising a step of measuring a flow rate of the stream of liquid CO 2 or a flow rate of the stream of vapor CO 2 during injection into the subterranean reservoir and adjusting the vapor CO 2 to liquid CO 2 ratio as a result of this measurement.
3 . The method according to claim 1 , comprising a step of initially injecting only a stream of vapor CO 2 into the well.
4 . The method according to claim 1 , wherein the vapor CO 2 to liquid CO 2 ratio gradually decreases over time.
5 . The method according to claim 1 , comprising a subsequent step of injecting only liquid CO 2 into the well.
6 . The method according to claim 1 , wherein the pressure of the CO 2 composition during injection, at the inlet of the injection well, initially lies between 3 MPa and 7 MPa.
7 . The method according to claim 1 , wherein the temperature of the CO 2 composition, at the inlet of the injection well, lies between 0° C. and 30° C.
8 . The method according to claim 1 , wherein the subterranean reservoir is at an initial pressure between 2 MPa and 20 MPa.
9 . The method according to claim 1 , wherein adjustments to the vapor CO 2 to liquid CO 2 ratio are made in real-time.
10 . The method according to claim 1 , comprising a step of directly measuring the bottomhole pressure in the well and adjusting the vapor CO 2 to liquid CO 2 ratio as a result of this measurement.
11 . The method according to claim 1 , comprising a step of measuring a topside temperature and adjusting the vapor CO 2 to liquid CO 2 ratio as a result of this measurement.
12 . The method according to claim 1 , comprising a step of measuring a topside pressure in the well and adjusting the vapor CO 2 to liquid CO 2 ratio as a result of this measurement.
13 . The method according to claim 1 , wherein the vapor CO 2 is obtained by evaporating liquid CO 2 by means of an evaporator.
14 . The method according to claim 1 , wherein the well has a length that lies between 100 m and 5 km.
15 . The method according to claim 1 , wherein the CO 2 composition comprises other compounds, including nitrogen and hydrocarbons in addition to CO 2 .
16 . The method according to claim 1 , wherein the subterranean reservoir is onshore or offshore.
17 . An installation for CO 2 storage, the installation comprising:
an injection well in a subterranean reservoir; a liquid CO 2 injection line connected to an inlet of the injection well; a vapor CO 2 injection line connected to an inlet of the injection well; a flow meter and an adjustable valve positioned along either or both of the liquid CO 2 injection line and vapor CO 2 injection line; a control unit configured to modify a ratio of vapor CO 2 to liquid CO 2 fed to the injection well.
18 . The installation according to claim 17 , wherein at least one pressure sensor is positioned along the well or at at least one bottomhole location.
19 . The installation according to claim 17 , wherein at least one temperature sensor is positioned along the well or at at least one bottomhole location.
20 . The installation according to claim 17 , wherein an evaporator is positioned along the vapor CO 2 injection line, and configured to evaporate liquid CO 2 into vapor CO 2 .
21 . (canceled)Join the waitlist — get patent alerts
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