Multiphase polymer suspension and use thereof

1. An aqueous particulate multiphase suspension comprising:

15 to 60% by weight of at least one water-soluble polymer in the form of solid particles with average size comprised between 5 and 500 μm;

15 to 45% by weight of a mixture of CaCl 2 and CaBr 2 having a weight ratio CaCl 2 :CaBr 2 of between 10:1 and 1:2;

at least one viscosifying agent other than the water-soluble polymer;

at least 10% by weight of water; and

said suspension having a Brookfield viscosity comprised between 500 and 20,000 cps, and

said suspension having a density comprised between 1.1 and 2 kg/l.

2. The particulate multiphase suspension according to claim 1 , wherein the particulate multiphase suspension contains less than 1% by weight of solvent, and less than 0.5% by weight of surfactant.

3. The multiphase particulate suspension according to claim 1 , wherein the average size of the particles of water-soluble polymer is between 10 μm and 400 μm.

4. The multiphase particulate suspension according to claim 1 , wherein the water-soluble polymer is an acrylamide-based anionic polymer, optionally at least partially post-hydrolyzed, and wherein the water-soluble polymer has a molecular weight of between 2 and 40 million g/mol.

5. The multiphase particulate suspension according to claim 1 , wherein the viscosifying agent other than the water-soluble polymer is a cellulose derivative.

6. The multiphase particulate suspension according to claim 1 , wherein the quantity of viscosifying agent other than the water-soluble polymer is between 0.01 and 5%.

7. The multiphase particulate suspension according to claim 1 , wherein the density of the suspension is between 1.3 and 1.9 kg/l.

8. A process for enhanced oil recovery comprising the following steps:

preparing an injection fluid by mixing an aqueous particulate multiphase suspension according to claim 1 with water or a brine;

injecting the injection fluid into a reservoir; and

recovering an aqueous and oily and/or gaseous mixture.

9. The process according to claim 8 , wherein the mixing of the suspension and the water or brine is done for less than 1 hour.

10. The process according to claim 8 , wherein the multiphase suspension is mixed with water or a brine containing fewer salts than the multiphase suspension to yield an intermediate composition, said intermediate composition next being mixed with water or a brine containing fewer salts than the multiphase suspension to yield the injection fluid.

11. The process according to claim 8 , wherein the multiphase suspension is added on-line in a pipe transporting water or a brine forming an injection fluid, said injection fluid being injected directly into the reservoir, with no mixing step other than the turbulences in the pipe.

12. The process according to claim 8 , wherein the mixing between the multiphase suspension and the water or brine is done partially in a static or dynamic mixer, or in an agitated tank, or in a dispersion device for particulate polymer suspension.

13. The process according to claim 8 , wherein the mixing of the suspension and the water or brine is done for less than 10 minutes.

14. The multiphase particulate suspension according to claim 1 , wherein the ratio between CaCl 2 ) and CaBr 2 is between 8:1 and 2:1.

15. The multiphase particulate suspension according to claim 5 , wherein the viscosifying agent other than the water-soluble polymer is hydroxyethyl cellulose.

16. A process for treating a mining effluent, comprising the following steps:

combining the suspension according to claim 1 , or an aqueous solution prepared from said suspension, with a mining effluent; and

discharging the effluent thus treated into an aquatic zone, near the water level or below the water level, such that the treated effluent flows and falls into the aquatic zone in which the solid part settles at the bottom and the aqueous part is in the water of the aquatic zone.

17. The multiphase particulate suspension according to claim 1 , wherein the average size of the particles of water-soluble polymer is between 50 μm and 200 μm.

18. The multiphase particulate suspension according to claim 4 , wherein the water-soluble polymer is selected from a copolymer of acrylamide and acrylamide tertiary butyl sulfonic acid (ATBS) optionally at least partially post-hydrolyzed, and a terpolymer of acrylamide, acrylic acid and acrylamide tertiary butyl sulfonic acid (ATBS), optionally at least partially post-hydrolyzed.