Method for treating production water from a method for enhanced oil and/or gas recovery

Patent metadata

Field	Value
Publication number	US-11046601-B2
Application number	US-201716316815-A
Country	US
Kind code	B2
Filing date	Jul 27, 2017
Priority date	Jul 28, 2016
Publication date	Jun 29, 2021
Grant date	Jun 29, 2021

Abstract

The present invention concerns a method for treating the production water originating from enhanced hydrocarbon recovery, and containing one or more water-soluble polymers and Fe 2+ ions, consisting of at least partially oxidizing the Fe 2+ ions by introducing at least one reaction activator and oxygen into said production water, the molar ratio of introduced oxygen to Fe 2+ ions being less than or equal to 0.25.

First claim

The invention claimed is:

1. A method for treating production water originating from enhanced hydrocarbon recovery, and containing one or more water-soluble polymers and Fe 2+ ions, the method comprising at least partially oxidizing the Fe 2+ ions by introducing at least one reaction activator and oxygen into said production water, the molar ratio of introduced oxygen to Fe 2+ ions being less than or equal to 0.25.

2. The method according to claim 1 , wherein the activator is introduced into the production water according to one of the following introduction modes:
before the introduction of the oxygen;
during the introduction of the oxygen;
after the introduction of the oxygen;
before and during the introduction of the oxygen;
before and after the introduction of the oxygen;
during and after the introduction of the oxygen;
before, during and after the introduction of the oxygen.

3. The method according to claim 2 , wherein the activator is chosen from the group consisting of: stearyl citrate, monoammonium citrate, calcium citrate, calcium disodium ethylenediaminetetraacetate, monocalcium phosphate, tricalcium phosphate, calcium phytate, citric acid, disodium ethylenediaminetetraacetate, glycine, sodium tripolyphosphate, phosphoric acid, monopotassium phosphate, tetrapotassium pyrophosphate, dipotassium phosphate, sodium acid pyrophosphate, sodium citrate, tetrasodium pyrophosphate, monosodium phosphate, disodium phosphate, sodium hexametaphosphate, N,N′-bis(2-hydroxybenzyl)-ethylenediamine-N,N′-diacetic acid, N-(1,2-dicarboxyethyl)-D,L aspartic acid, diethylene triamine pentacetic acid, humic acid, fulvic acid, polyacrylate, polyitaconate, polymaleate, and polyaspartate.

4. The method according to claim 2 , wherein between 1 and 30 ppm of activator is introduced into the production water, relative to the weight of the production water.

5. The method according to claim 2 , wherein between 0.25 and 7 ppm of oxygen is introduced into the production water, relative to the weight of the production water.

6. The method according to claim 1 , wherein the activator is chosen from the group consisting of: stearyl citrate, monoammonium citrate, calcium citrate, calcium disodium ethylenediaminetetraacetate, monocalcium phosphate, tricalcium phosphate, calcium phytate, citric acid, disodium ethylenediaminetetraacetate, glycine, sodium tripolyphosphate, phosphoric acid, monopotassium phosphate, tetrapotassium pyrophosphate, dipotassium phosphate, sodium acid pyrophosphate, sodium citrate, tetrasodium pyrophosphate, monosodium phosphate, disodium phosphate, sodium hexametaphosphate, N,N′-bis(2-hydroxybenzyl)-ethylenediamine-N,N′-diacetic acid, N-(1,2-dicarboxyethyl)-D,L aspartic acid, diethylene triamine pentacetic acid, humic acid, fulvic acid, polyacrylate, polyitaconate, polymaleate, and polyaspartate.

7. The method according to claim 6 , wherein between 1 and 30 ppm of activator is introduced into the production water, relative to the weight of the production water.

8. The method according to claim 6 , wherein between 0.25 and 7 ppm of oxygen is introduced into the production water, relative to the weight of the production water.

9. The method according to claim 1 , wherein between 1 and 30 ppm of activator is introduced into the production water, relative to the weight of the production water.

10. The method according to claim 9 , wherein between 0.25 and 7 ppm of oxygen is introduced into the production water, relative to the weight of the production water.

11. The method according to claim 10 , wherein the production water is successively treated by:
separation of the production water and residual hydrocarbons;
flotation of the production water and/or decanting of the production water and/or coalescence of the production water and/or centrifugation of the production water;
filtration of the production water;
and wherein the oxygen is introduced during the separation step.

12. The method according to claim 10 , wherein the production water is successively treated by:
separation of the production water and residual hydrocarbons;
flotation of the production water and/or decanting of the production water and/or coalescence of the production water and/or centrifugation of the production water;
filtration of the production water;
and wherein the oxygen is introduced between the separation and the flotation and/or decanting and/or coalescence and/or centrifugation steps.

13. The method according to claim 10 , wherein the production water is successively treated by:
separation of the production water and residual hydrocarbons;
flotation of the production water and/or decanting of the production water and/or coalescence of the production water and/or centrifugation of the production water;
filtration of the production water;
and wherein the oxygen is introduced during the flotation and/or decanting and/or coalescence and/or centrifugation step.

14. The method according to claim 10 , wherein the concentration in Fe 2+ ions initially present in the production water is at least 1 ppm relative to the weight of the production water; or if prior to the introduction of the oxygen, the quantity of Fe 2+ ions is less than 1 ppm, then Fe 2+ ions are introduced before the introduction of the oxygen.

15. The method according to claim 1 , wherein between 0.25 and 7 ppm of oxygen is introduced into the production water, relative to the weight of the production water.

16. The method according to claim 1 , wherein the production water is successively treated by:
separation of the production water and residual hydrocarbons;
flotation of the production water and/or decanting of the production water and/or coalescence of the production water and/or centrifugation of the production water;
filtration of the production water;
and wherein the oxygen is introduced during the separation step.

17. The method according to claim 1 , wherein the production water is successively treated by:
separation of the production water and residual hydrocarbons;
flotation of the production water and/or decanting of the production water and/or coalescence of the production water and/or centrifugation of the production water;
filtration of the production water;
and wherein the oxygen is introduced between the separation and flotation and/or decanting and/or coalescence and/or centrifugation steps.

18. The method according to claim 1 , wherein the production water is successively treated by:
separation of the production water and residual hydrocarbons;
flotation of the production water and/or decanting of the production water and/or coalescence of the production water and/or centrifugation of the production water;
filtration of the production water;
and wherein the oxygen is introduced during the flotation and/or decanting and/or coalescence and/or centrifugation step.

19. The method according to claim 1 , wherein the concentration in Fe′ ions initially present in the production water is at least 1 ppm relative to the weight of the production water; or if prior to the introduction of the oxygen, the quantity of Fe 2+ ions is less than 1 ppm, then Fe 2+ ions are introduced before the introduction of the oxygen.

20. An enhanced hydrocarbon recovery method comprising injecting a polymer solution into an underground formation and recovering the hydrocarbons, wherein the polymer solution contains treated production water containing one or more water-soluble polymers and Fe 2+ ions, wherein the treated production water is obtained

Assignees

• Spcm Sa

Inventors

• Favero Cédrick
• Gil Ludwig

Classifications

• C09K8/588

  characterised by the use of specific polymers {(polymeric surfactants C09K8/584)} · CPC title

• C02F2303/08

  Corrosion inhibition · CPC title

• C02F2209/09

  Viscosity · CPC title

• C02F2103/10

  from quarries or from mining activities · CPC title

• C02F1/24

  by flotation (C02F1/465 takes precedence) · CPC title