Method and system for enhancing oil recovery (EOR) by injecting treated water into an oil bearing formation

1. A method for enhancing oil recovery (EOR) from an oil bearing formation, the method comprising:

filtering at least some solids from a source water having a total dissolved solids content of from 10000 ppm to 50000 ppm in a filtration assembly to produce a first pre-treated water;

treating the first pre-treated water with a nano-filtration (NF) assembly to produce a second pre-treated water wherein the second pre-treated water has reduced hardness and sulphate concentration relative to the source water; treating the second pre-treated water in a capacitive de-ionisation (CDI) assembly comprising at least one flowpath for the second pre-treated water arranged between a pair of oppositely charged electrodes which adsorb and thereby remove at least some ions from the second pre-treated water flowing through the flowpath, thereby producing treated water with a reduced salinity and solids content; and

injecting the treated water with reduced salinity and solids content into the oil bearing formation to mobilize crude oil and enhance oil recovery.

2. The method of claim 1 , wherein the electrodes comprise substantially parallel porous plates comprising activated carbons that are electrically charged by a direct current (DC) electrical power source connected to the plates.

3. The method of claim 2 , wherein the porous plates comprise carbon aerogel.

4. The method of claim 1 , wherein the second pre-treated water produced by the nano-filtration assembly has less than 1 parts per million (ppm) oil and less than 1 part per million(ppm) total suspended solids (TSS).

5. The method of claim 1 , wherein the source water has a total dissolved solids (TDS) content between 30,000 and 40,000 mg/Liter and the treated water has a TDS content between 1,000 and 5,000 parts per million (ppm).

6. The method of claim 5 , wherein the treated water has a total dissolved solids (TDS) between 2,000 and 5,000 parts per million (ppm).

7. The method of claim 6 , wherein the treated water has a lower salinity than pore water present in the formation before initiation of treated water injection.

8. The method of claim 6 , wherein the treated water has a lower ionic strength than pore water present in the formation before initiation of treated water injection.

9. The method of claim 1 wherein the source water is selected from the group consisting of seawater, brackish water, water produced from the oil bearing formation, saline aquifer water, and mixtures thereof.

10. A system for enhancing oil recovery (EOR)from an oil bearing formation, the system comprising:

a filtration assembly for filtering at least some solids from a source water having a total dissolved solids content of from 10000 ppm to 50000 ppm to produce a first pre-treated water;

a nano-filtration (NF) assembly configured to receive the first pre-treated water and configured to produce a second pre-treated water having a reduced hardness and sulphate concentration relative to the source water;

a capacitive de-ionisation (CDI) assembly configured to receive the second pre-treated water, comprising at least one flowpath for the second pre-treated water arranged between a pair of substantially parallel oppositely charged electrodes which adsorb and thereby remove at least some ions from the second pre-treated water flowing through the flowpath, for producing treated water with a reduced salinity and solids content relative to the source water; and

an injection well for injecting the treated water with reduced salinity and solids content into the oil bearing formation to mobilize crude oil and thereby enhance crude oil recovery from the formation.

11. The system of claim 10 , wherein the electrodes comprise substantially parallel porous plates comprising activated carbons that are electrically charged by a direct current (DC) electrical power source connected to the plates.

12. The system of claim 11 , wherein the porous plates comprise carbon aerogel.

13. The system of claim 10 , wherein the nano-filtration (NF) assembly is configured to produce the second pre-treated with less than 1 parts per million (ppm) oil and less than 1 parts per million(ppm) of total suspended solids (TSS).