Method of using nanofiltration and reverse osmosis to remove chemical contaminants
US-11926534-B2 · Mar 12, 2024 · US
US12330958B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12330958-B2 |
| Application number | US-202418429699-A |
| Country | US |
| Kind code | B2 |
| Filing date | Feb 1, 2024 |
| Priority date | Feb 28, 2020 |
| Publication date | Jun 17, 2025 |
| Grant date | Jun 17, 2025 |
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A method of removing chemical contaminants from a composition comprising an active, a solvent, and a contaminant can include providing an initial feed supply, wherein the initial feed supply comprises the active, the solvent, and the contaminant, wherein the contaminant can include 1,4 dioxane, dimethyl dioxane, or a combination thereof; including filtering the initial feed stock through a nanofilter.
Opening claim text (preview).
What is claimed is: 1. A method of reducing the amount of a chemical contaminant in a composition, comprising; a) providing an initial feed supply comprising a composition comprising an active and a chemical contaminant comprising 1,4-dioxane; dimethyl dioxane; diethylene oxide sulfate; or a combination thereof; and, optionally, a solvent; b) providing a nanofilter; and c) filtering the initial feed supply through the nanofilter to form a retentate comprising at least a portion of the active and a filtrate comprising at least a portion of the chemical contaminant and at least a portion of the solvent; d) subjecting the filtrate to reverse osmosis to form a reverse osmosis permeate and a reverse osmosis concentrate comprising at least a portion of the chemical contaminant, wherein at least a portion of the filtrate is further processed to destroy at least a portion of the chemical contaminant in the filtrate. 2. The method of claim 1 , wherein the process to destroy at least a portion of the chemical contaminant comprises advanced oxidation processing, Fenton reaction, photo-Fenton reaction, activated carbon adsorption, catalyst processing, alcohol dehydration reaction, ozone treatment, ultra-violet/TiO 2 treatment, incineration, or a combination thereof. 3. The method of claim 1 , wherein the initial feed has a viscosity of about 1000 cP or less. 4. The method of claim 1 , wherein the initial feed has a viscosity of about 300 cP or less. 5. The method of claim 1 , wherein the nanofilter filters a weight average molecular weight which includes the molecular weight of the contaminant and excludes the molecular weight of the active. 6. The method of claim 5 , wherein nanofilter filters a weight average molecular weight of about 250 Da or less. 7. The method of claim 1 , wherein the active comprises an ethoxylated surfactant, a sulfated ethoxylated surfactant, an ethoxylated polymer, a propoxylated surfactant, a propoxylated sulfated surfactant, a propoxylated polymer, or a combination thereof. 8. The method of claim 1 , wherein the initial feed has a pH of about 10 or more. 9. The method of claim 1 , wherein the nanofilter can filter about 80% or more of the initial feed before needing to be replaced.
Multistep processes comprising different kinds of membrane processes selected from reverse osmosis, hyperfiltration or nanofiltration · CPC title
to feed side · CPC title
At least two polymers of same structure but different molecular weight · CPC title
Use of permeate · CPC title
Oxidation · CPC title
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