Polymer of 2-acrylamido-2-methylpropane sulphonic acid and use thereof

1 . A water-soluble polymer of 2-acrylamido-2-methylpropane sulfonic acid and/or one of its salts,

wherein said 2-acrylamido-2-methylpropane sulfonic acid and/or one of its salts being at least partially of renewable and non-fossil origin,

wherein said 2-acrylamido-2-methylpropane sulfonic acid and/or one of its salts comprises a biobased carbon content of between 5% by weight and 100% by weight relative to the total weight of carbon in said 2-acrylamido-2-methylpropane sulfonic acid, the biobased carbon content being measured according to method B of standard ASTM D6866-21, and

wherein the water-soluble polymer has a weight-average molecular weight of between 11 and 40 million Daltons.

2 . The water-soluble polymer according to claim 1 , wherein the water-soluble polymer has a filter-ratio FR of less than 1.2.

3 . The water-soluble polymer according to claim 2 , wherein the filter-ratio FR is less than 1.1.

4 . The water-soluble polymer according to claim 1 , wherein the water-soluble polymer is obtained by gel polymerization or by inverse emulsion polymerization.

5 . The water-soluble polymer according to claim 1 , wherein the water-soluble polymer has a weight-average molecular weight of between 15 million and 40 million daltons.

6 . The water-soluble polymer according to claim 1 , wherein the water-soluble polymer contains at least 20 mol % 2-acrylamido-2-methylpropane sulfonic acid and/or one of its salts being at least partially of renewable and non-fossil origin.

7 . The water-soluble polymer according to claim 1 , wherein the water-soluble polymer contains at least 90 mol % 2-acrylamido-2-methylpropane sulphonic acid and/or one of its salts being at least partly of renewable and non-fossil origin.

8 . The water-soluble polymer according to claim 1 , wherein the water-soluble polymer contains between 20% and 99% molar, of a first monomer, said first monomer being 2-acrylamido-2-methylpropane sulfonic acid and/or one of its salts which is at least partially of renewable and non-fossil origin, and between 1% and 80% molar of at least one second monomer comprising an unsaturated ethylene monomer, said second monomer being different from the first monomer, and being at least partially of renewable and non-fossil origin.

9 . A method for enhanced oil or gas recovery by flushing a subterranean formation comprising injecting into the subterranean formation an aqueous composition comprising:

a. preparing an injection fluid from a water-soluble polymer according to claim 1 , with water or brine,

b. injecting the injection fluid into a subterranean formation,

c. sweeping the subterranean formation using the injected fluid,

d. recovering an aqueous, oily, and/or gaseous mixture.

10 . The method for enhanced oil or gas recovery according to claim 9 , wherein the injection fluid contains between 0.03 and 0.4 wt % of water-soluble polymer, based on the total weight of the injection fluid.

11 . A method of hydraulic fracking of underground oil or gas reservoir comprising:

a. preparing an injection fluid from a polymer according to claim 1 , with water or brine, and optionally with at least one proppant,

b. injecting said fluid into the underground reservoir and fracking at least one part thereof in order to recover the oil and/or the gas.

12 . The hydraulic fracking method according to claim 11 , wherein the injection fluid comprises between 0.025% and 1%, by weight of water-soluble polymer, relative to the total weight of the injection fluid.

13 . A method to treat a slurry of solid particles in water resulting from mining or oil sands operations, comprising contacting said slurry with at least one polymer according to claim 1 .

14 . The treatment method according to claim 13 , wherein the suspension of solid particles contains between 5 and 60% by weight of solid particles, relative to the total weight of said suspension.

15 . The treatment method according to claim 13 , wherein the suspension of solid particles contains between 20 and 50% by weight of solid particles, based on the total weight of said suspension.

16 . The treatment method according to claim 13 , wherein the quantity of polymer brought into contact with the suspension is between 50 and 5,000 g per ton of solid particles of the suspension.