Method for controlling accretion of scale
The present disclosure provides an improved scale inhibiting formulation that is effective, environmentally friendly, and does not add any organic compounds or traditional polymeric compounds to treated water. The scale inhibiting composition includes molecular clusters of polyammonium bisulfate (PABS), which can interact physically, chemically, or physio-chemically with one or more ions in the water or water-containing system being treated. That interaction inhibits scale accretion and/or removes previously formed scale.
1. A method for inhibiting scale accretion in water-containing systems, comprising:
adding water, sulfuric acid, and molecular clusters of polyammonium bisulfate (“PABS clusters”) to a water-based liquid in a water-containing system to form a treated water-containing system,
wherein a concentration of the PABS clusters in the treated water-containing system is from about 0.01 ppm to about 10,000 ppm, and
wherein the PABS clusters comprise ammonium bisulfate, sulfuric acid, and water according to Formula I
((R a NH 4−a ) 2 SO 4 ) x ·(H 2 SO 4 ) y ·(H 2 O) z ·((R a NH 4−a )HSO 4 ) n (I)
wherein each R independently is alkyl or aryl; a is 1, 2, or 3; x is at least 1, y is 0 to 5; and z is 0 to 5; and n is 1 to 20.
2. The method of claim 1 , further comprising combining the water, the sulfuric acid, and the PABS clusters to form an aqueous formulation and adding the aqueous formulation comprising the water, the sulfuric acid, and the PABS clusters to the water-containing system.
3. The method of claim 1 , wherein the concentration of the PABS clusters in the water-based liquid ranges from 0.1 ppm to 4 ppm, and wherein the concentration of the sulfuric acid in the water-based liquid ranges from 0.15 ppm to 0.6 ppm.
4. The method of claim 2 , wherein the aqueous formulation further comprises a second inorganic acid, and wherein the second inorganic acid comprises phosphoric acid (H 3 PO 4 ), phosphonic acid (H 3 PO 3 ), nitric acid (HNO 3 ), hydrochloric acid (HCl), or methane sulfonic acid (CH 4 O 3 S).
5. The method of claim 2 , wherein the aqueous formulation comprises 2 wt. % to 50 wt. % PABS clusters and 1 wt. % to 50 wt. % sulfuric acid.
6. The method of claim 2 , wherein adding the aqueous formulation comprises adding from 0.01 to 100 parts of the aqueous formulation per million parts of water-based liquid in the water-containing system (ppm) on a volume to volume basis.
7. The method of claim 2 , further comprising adding phosphoric acid to the water-containing system, wherein the aqueous formulation and the phosphoric acid are added simultaneously, or wherein the aqueous formulation is added before the phosphoric acid is added, or wherein the phosphoric acid is added before the aqueous formulation.
8. The method of claim 7 , wherein adding the aqueous formulation to the water-containing system comprises adding 0.5 to 5 ppm of the aqueous formulation to the water-containing system, and wherein adding the phosphoric acid to the water-containing system comprises adding 0.01 to 0.5 ppm of the phosphoric acid to the water-containing system.
9. The method of claim 2 , further comprising adding an aqueous urea hydrochloride solution to the water-containing system, wherein the aqueous urea hydrochloride solution comprises from 1 wt. % to 45 wt. % urea hydrochloride.
10. The method of claim 1 , wherein the method inhibits accretion of calcium carbonate (CaCO 3 ), calcium sulfate (CaSO 4 ), strontium sulfate (SrSO 4 ), barium sulfate (BaSO 4 ), calcium phosphate [Ca 3 (PO 4 ) 2 ], calcium fluoride (CaF 2 ), oxides of manganese (Mn), oxides of iron (Fe), or any combination thereof.
11. The method of claim 2 , wherein the water-based liquid has a calcium hardness in a range of 0 to 1,200 milligrams per liter (mg/L) of the water-based liquid.
12. The method of claim 2 , wherein the water-based liquid has a total salt concentration in a range of 0 to 40 wt. %.
13. The method of claim 2 , wherein the water-based liquid is used for oil or gas recovery and/or oil or gas processing.
14. The method of claim 2 , wherein the aqueous formulation is added to a water-containing system comprising a desalination system, cooling tower, water purification system, boiler, heat-exchange unit, membrane filter system, irrigation system, or chlorinator system.
15. The method of claim 2 , wherein the aqueous formulation is added to an oil or gas well to prevent disruption of liquid or gas flow in the oil or gas well as a result of formation and/or deposition of scale.
16. The method of claim 2 , wherein the aqueous formulation is added to remove previously formed scale deposits while preventing formation and/or deposition of new scale deposits.
17. The method of claim 16 , wherein a concentration of the PABS clusters in the water-based liquid ranges from 1 ppm to 10,000 ppm, and wherein a concentration of the sulfuric acid in the water-based liquid ranges from 1.5 ppm to 15,000 ppm.
18. The method of claim 1 , wherein the PABS clusters have diameters in a range of from 1 nm to 4 μm.
19. The method of claim 2 , wherein the aqueous formulation further comprises at least one additive comprising an anticorrosion additive, biocide, pH control substance, coagulant, flavor or odor control additive, or propellant.