Self-Dispersing Additive System, Composition, and Method for Treating Bodies of Water
US-2016304367-A1 · Oct 20, 2016 · US
US9707520B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9707520-B2 |
| Application number | US-201615237052-A |
| Country | US |
| Kind code | B2 |
| Filing date | Aug 15, 2016 |
| Priority date | Jan 18, 2012 |
| Publication date | Jul 18, 2017 |
| Grant date | Jul 18, 2017 |
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A composition for treating a water system or membrane fluid system, such as a reverse osmosis system, to remove scale, microorganisms and biofilm, and corrosion by-products. The composition comprises chelating agents and a surfactant. The composition may be a solid dissolved by water or solvent in the system being treated or may be a pre-mixed foam or aerosol. A method for using such a treatment composition comprises contacting the treatment composition with substantially all parts of the water system and draining the treatment composition from the system before resuming normal operations. For certain systems, the method also comprises draining some existing water in the water system to remove prior treatment compositions and filling or rinsing the system with fresh water prior to adding the treatment composition.
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We claim: 1. A method of removing biofilm and treating a fluid system containing a membrane, the method comprising the steps of: adding a surfactant, a first chelating agent, and a second chelating agent or other ingredient that will react with the first chelating agent to produce a second chelating agent to the fluid system in amounts sufficient to provide concentrations of at least 0.00015 M for the surfactant, about 0.001M to 0.01M for the first chelating agent, and about 0.0005 M to 0.005M for the second chelating agent when mixed with a volume of fluid in the fluid system containing the membrane or portion thereof being treated; removing biofilm by circulating the fluid containing the surfactant and chelating agents through at least a portion of the fluid system to contact the membrane; wherein the membrane is a nanofiltration, ultrafiltration, microfiltration, forward osmosis, reverse osmosis, or particle filtration membrane; wherein the fluid system is a water system and the fluid comprises water; and wherein the first chelating agent is citric acid, the second chelating agent is sodium citrate, and the other ingredient is sodium bicarbonate. 2. The method of claim 1 further comprising the steps of: adding a corrosion inhibitor and a biocide to the fluid in the fluid system; and circulating the fluid containing the corrosion inhibitor and the biocide through at least a portion of the fluid system. 3. The method according to claim 1 wherein the surfactant is an ammonium bromide compound, an ammonium chloride compound, or a sodium sulfonate compound. 4. The method of claim 1 wherein the fluid system is a reverse osmosis system comprising the membrane, a feed line for feeding the fluid to the membrane, a concentrate line exiting the membrane and a permeate line exiting the membrane, the method further comprising the step of: flowing the fluid containing the surfactant and chelating agents from the feed line to the concentrate line to contact the membrane. 5. The method of claim 2 wherein the corrosion inhibitor is added and circulated for a period of time prior to adding the surfactant. 6. The method of claim 2 wherein the surfactant is added and circulated for a period of time prior to adding the first chelating agent. 7. The method of claim 2 wherein the surfactant and chelating agents circulate for a period of time prior to adding the biocide. 8. The method of claim 2 wherein the surfactant, the first chelating agent, the second chelating agent or other ingredient that will react with the first chelating agent to produce a second chelating agent, and biocide are added at the same time. 9. The method of claim 4 further comprising the step of removing substantially all of the fluid containing the surfactant and chelating agents from the reverse osmosis system after the circulating step; and rinsing the reverse osmosis system. 10. The method according to claim 4 wherein the surfactant is in a range of about 0.00015 M to 0.0015 M when mixed with the volume of fluid in the reverse osmosis system being treated. 11. The method of claim 4 further comprising the step of filtering the fluid as it circulates through the reverse osmosis system to remove dislodged biofilm material. 12. The method according to claim 4 wherein the surfactant, the first chelating agent, and the second chelating agent or other ingredient that will react with the first chelating agent to produce a second chelating agent are in solid form prior to being added to the fluid of the reverse osmosis system being treated. 13. The method of claim 4 wherein the adding step comprises diverting at least some fluid from the concentrate line to a treatment system comprising a feeder containing the surfactant and chelating agents in dry or powdered form and adding the surfactant and chelating agents to the diverted fluid. 14. The method of claim 13 wherein the circulating step further comprises returning the diverted fluid with the surfactant and chelating agents to the feed line to flow from the feed line to the concentrate line to contact the membrane.
by means of halogens other than chlorine or of halogenated compounds containing halogen other than chlorine · CPC title
with halogens or compounds of halogens {(C02F1/4674 takes precedence)} · CPC title
Hydroxy carboxylic acids-salts thereof · CPC title
Reverse osmosis; Hyperfiltration · CPC title
containing at least one carboxylic group or a thio analogue, or a derivative thereof, and a singly bound oxygen or sulfur atom attached to the same carbon skeleton, this oxygen or sulfur atom not being a member of a carboxylic group or of a thio analogue, or of a derivative thereof, e.g. hydroxy-carboxylic acids · CPC title
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