Reduced corrosion iron sulfide scale removing fluids
US-10457850-B2 · Oct 29, 2019 · US
US11026420B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11026420-B2 |
| Application number | US-201916559894-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 4, 2019 |
| Priority date | Dec 15, 2016 |
| Publication date | Jun 8, 2021 |
| Grant date | Jun 8, 2021 |
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Peroxyformic acid compositions for treatment and removal of biofilm growth and mineral deposits on membranes for energy services applications are disclosed. In particular, peroxyformic acid compositions are generated in situ or on site generation for the reduction and prevention, of biofilms and the mitigation of mineral buildup on the membranes. The compositions according to the invention are compatible with the membranes under application of use conditions.
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What is claimed is: 1. A method for removing mineral deposits from a membrane system comprising: contacting a membrane fouled with mineral deposits comprising sulfate, sulfur, and/or sulfide with a peroxyformic acid composition comprising peroxyformic acid and hydrogen peroxide, wherein the ratio of the peroxyformic acid to the hydrogen peroxide in the peroxyformic acid composition is from about 5:1 to about 40:1; and removing the mineral deposits from the membrane; wherein the contacting occurs not more frequently than once every 24 hours, and wherein the peroxyformic acid composition contacts the membrane for less than about 12 hours; and wherein the peroxyformic acid composition is membrane compatible and does not damage the membrane as measured by a decrease in flux of the membrane. 2. The method of claim 1 , wherein the membrane is a reverse osmosis membrane, nanofiltration membrane, ultrafiltration membrane, or a microfiltration membrane. 3. The method of claim 1 , wherein the membrane comprises cellulose, cellulose acetate, nitrocellulose, polysulfone, polyethersulfone, fully aromatic polyamide, polyvinylidene fluoride, polytetrafluoroethylene, polyacrylnitrile, polypropylene, carbon, alpha-aluminum oxide, zirconium oxide, ceramic and/or stainless steel. 4. The method of claim 1 , wherein the treatment with the peroxyformic acid composition does not negatively impact the pressure on the membrane or decrease the lifespan of the membrane in comparison to a membrane treated with other oxidizer chemistries. 5. The method of claim 1 , wherein the membrane system treats a water source. 6. The method of claim 5 , wherein the water source is freshwater, sea water, produced water, brackish water, transport water, and/or water used in oil and gas production systems. 7. The method of claim 5 , wherein the mineral deposits comprise calcium sulfate, barium sulfate, strontium sulfate, and/or iron sulfide. 8. The method of claim 1 , wherein the treatment with the peroxyformic acid composition further removes microorganisms from the membrane system. 9. The method of claim 8 , wherein the microorganisms comprise sulfur- and/or sulfate-reducing bacteria. 10. The method of claim 1 , wherein the concentration of hydrogen peroxide in the peroxyformic acid composition is between about 0.001% (w/w) to about 5% (w/w). 11. The method of claim 1 , further comprising at least one additional step of a first product removal step before the membrane is contacted with the peroxyformic acid composition, a pre-rinse step of washing the membrane with water, a soak step of washing the membrane, and/or an additional treatment cycle(s) comprising an acidic treatment, an enzymatic treatment, an alkaline treatment and/or a neutral treatment either before or after the peroxyformic acid composition contacts the membrane. 12. The method of claim 1 , wherein the membrane is contacted with from about 0.00001% (w/w) to about 0.1% (w/w) active peroxyformic acid. 13. The method of claim 1 , wherein the membrane is contacted with peroxyformic acid for at least 15 minutes. 14. The method of claim 1 , wherein the membrane is contacted with an additional peroxyacid, chelant, solvent, surfactant and/or other additive which may be dosed separately or simultaneously with the peroxyformic acid composition. 15. The method of claim 1 , wherein the membrane is contacted with the peroxyformic acid composition at a temperature of from about 2° C. to about 70° C. 16. The method of claim 1 , wherein the peroxyformic acid composition is generated in situ by contacting formic acid with hydrogen peroxide, wherein before said contacting, the ratio between the concentration of said formic acid (w/v) and the concentration of said hydrogen peroxide (w/v) is about 2 or higher, and the ratio between the concentration of said peracid (w/w) and the concentration of hydrogen peroxide (w/w) in said formed resulting aqueous composition reaches about 2 or higher within about 1 hour of said contacting. 17. The method of claim 1 , further comprising a step of reducing the concentration of the hydrogen peroxide in the peroxyformic acid composition. 18. The method of claim 1 , wherein contacting step includes contacting the membrane with at least about 1 ppm to about 300 ppm actives of peroxyformic acid composition.
containing the group [IMAGE cpc-sch-A01N-0934.gif]; Thio analogues thereof · CPC title
Combination with washing or cleaning means · CPC title
Peroxide solutions · CPC title
Liquid substances · CPC title
Prevention of biofouling · CPC title
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