Composition and method for breaking friction reducing polymer for well fluids
A polymer breaking solution usable in fracking and other downhole applications comprises a solution of aqueous hydrogen peroxide, an anionic surfactant, a metal chelating agent, an acidic pH buffer, a soluble zinc compound, and in some embodiments, a viscosifying agent. In other embodiments, the solution may additionally comprise a linear hydrophobic surfactant. At treatment concentrations of between 500 ppm to 1,500 ppm, the solution is non-toxic and usable at a wide range of downhole temperatures (32° C. to 82° C.).
1 . An aqueous polymer breaking fluid comprising a solution of:
hydrogen peroxide, in a concentration between 7 wt % and 20 wt %;
a soluble zinc compound, in a concentration between 0.05 wt % and 0.5 wt %;
a metal chelating agent;
an acidic pH buffer; and
an alkyl sulfate surfactant,
wherein the solution is diluted in the aqueous polymer breaking fluid at a level of 0.2 to 3.0 gallons of solution per thousand gallons of the aqueous polymer breaking fluid.
2 . The fluid of claim 1 , wherein the soluble zinc compound is selected from the group consisting of: zinc sulfate, zinc acetate, zinc citrate, zinc oxide, zinc chloride, of and zinc gluconate.
3 . The fluid of claim 1 , wherein the metal chelating agent is present in the solution at a concentration between 0.1 wt % and 0.5 wt %.
4 . The fluid of claim 1 , wherein the metal chelating agent is selected from the group consisting of: diethylenetriaminepentaacetate, n-(hydroxyethyl)-ethylenediaminetriacetic acid, ethylenediaminetetracetic acid, iminodissuccinic acid, itaconic acid, iminodiacetic acid, glutamic acid n,n-diacetic acid, polyaspartic acid, nitrilotriacetic acid, citric acid, erythorbic acid, ascorbic acid, and any sodium or potassium salts thereof.
5 . The fluid of claim 1 , wherein the alkyl sulfate surfactant is present in the solution at a concentration between 0.1 wt % to 0.8 wt %.
6 . The fluid of claim 1 , wherein the alkyl sulfate surfactant is selected from the group consisting of: sodium lauryl sulfate er and sodium lauryl ethoxy sulfate.
7 . The fluid of claim 1 , wherein the pH buffer is present in the solution at a concentration between 0.1 wt % to 0.8 wt %.
8 . The fluid of claim 1 , wherein the pH buffer is selected from the group consisting of: acetic acid, oxalic acid, sulfonic acid, sulfamic acid, toluene sulfonic acid, 2-ethyl hexanoic acid, methane sulfonic acid, tartaric acid, lactic acid, and propionic acid.
9 . The fluid of claim 1 , wherein the solution further comprises a linear hydrophobe surfactant.
10 . The fluid of claim 9 , wherein the linear hydrophobe surfactant is present in the solution at a concentration between 0.1 wt % to 0.8 wt %.
11 . The fluid of claim 9 , wherein the linear hydrophobe surfactant is selected from the group consisting of: disodium decyl(sulfophenoxy)benzenesulfonate, disodium oxybis(decylbenezenesulfonate), sodium alkyl diphenyl oxide disulfonate, sodium C10 (linear) diphenyl oxide disulfonate, sodium decyl diphenyl oxide disulfonate, sodium hexadecyldiphenyloxide disulfonate, sodium C16 (linear) diphenyl oxide disulfonate, and disodium dihexyldiphenyloxide disulfonate.
12 . The fluid of claim 1 , wherein the solution further comprises polyethylene oxide.
13 . The fluid of claim 12 , wherein the polyethylene oxide is present in a concentration between 0.005 wt % to 0.1 wt %.
14 . The solution of claim 12 , wherein the polyethylene oxide has a molecular weight between one million and eight million.