Method of removing iron-containing scale from a wellbore, pipe, or surface using a biodegradable descaler solution
A method of removing iron-containing scale from a wellbore, pipe, or metal-containing surface involving contacting the iron-containing scale with a biodegradable descaler solution of water, hydrochloric acid, formic acid, citric acid, a corrosion inhibitor, a corrosion inhibitor intensifier, and a surfactant. The method is performed at a pressure of 14 to 400 psi and a temperature of 100 to 150° C. The method removes iron-containing scale made of iron sulfide, iron carbonate, iron oxyhydroxide, and calcium carbonate. The method meets industry standard steel corrosion rates of less than 0.049 lb/ft 2 per day. Also disclosed is a biodegradable descaler solution of water, hydrochloric acid, formic acid, citric acid, a corrosion inhibitor, a corrosion inhibitor intensifier, and a surfactant that meets OECD 301B thresholds for ready biodegradability.
1. A method for removing an iron-containing scale from a wellbore, pipe, or other metal-containing surface, the method comprising:
contacting the iron-containing scale with a biodegradable descaler solution comprising
55.75 to 80.49 wt % of water,
16.0 to 22.5 wt % of hydrochloric acid,
0.75 to 7.5 wt % of formic acid,
0.75 to 7.5 wt % of citric acid,
1.0 to 3.0 wt % of a corrosion inhibitor,
1.0 to 3.0 wt % of a corrosion inhibitor intensifier, and
0.01 to 0.75 wt % of a surfactant, each based on a total weight of the biodegradable descaler solution;
wherein the biodegradable descaler solution is contacted with the iron-containing scale at a pressure of 14 to 400 psi, and
wherein the iron-containing scale has a solubility of 75 to 95 g/L in the biodegradable descaler solution at a temperature of 100 to 150° C.,
wherein 70% of dissolved oxygen content is removed and 60% of theoretical CO 2 is produced by the biodegradable descaler solution according to OECD 301B biodegradation test.
2. The method of claim 1 , wherein the iron-containing scale comprises iron sulfide, iron carbonate, iron oxyhydroxide, and calcium carbonate.
3. The method of claim 2 , wherein the iron sulfide is one or more selected from the group consisting of pyrrhotite (Fe 7 S 8 ), troilite (hexagonal FeS), pyrite, (cubic FeS 2 ), mackinawite (tetragonal FeS), and marcasite (orthorhombic FeS 2 ).
4. The method of claim 1 , wherein the corrosion inhibitor is at least one selected from the group consisting of a salt of a N,N-diallyl-N-benzyl dodecyl ammonium cation and 3,5-diiodotyrosine.
5. The method of claim 1 , wherein the surfactant is an ionic surfactant.
6. The method of claim 5 , wherein the ionic surfactant is sodium dodecyl sulfate.
7. The method of claim 1 , wherein the corrosion inhibitor intensifier is at least one selected from the group consisting of tetrahydro-3,5-dimethyl-2H-1,3,5-thiadiazine-2-thione, methyl formate, and potassium iodide.
8. The method of claim 1 , wherein the biodegradable descaler solution has a density of 0.90 to 1.25 g/cm 3 at 20 to 30° C.
9. The method of claim 1 , wherein the biodegradable descaler solution has a viscosity of 1.4 to 1.8 cP at 20 to 30° C. and a surface tension of 30 to 33 mN/m at 20 to 30° C.
10. The method of claim 1 , wherein the biodegradable descaler solution has a pH of −1.5 to −1.1 at 20 to 30° C.
11. The method of claim 1 , wherein the contacting is performed at a temperature of 100 to 150° C.
12. The method of claim 1 , wherein the contacting is performed for 1 to 48 hours.
13. The method of claim 1 , wherein the method removes the iron-containing scale while causing a corrosion rate of steel of less than 0.049 lb/ft 2 per day at 100 to 150° C.
14. The method of claim 1 , wherein the biodegradable descaler solution is present at an initiation of the contacting in an amount of 1 L of biodegradable descaler solution per every 75 to 100 g of iron-containing scale.
15. The method of claim 1 , wherein the biodegradable descaler solution reaches a plateau of 75 to 99% of theoretical CO 2 by day 40 according to OECD 301B biodegradation test.