Enhanced emulsion liquid membranes for extraction of pollutants from water
US-11648512-B2 · May 16, 2023 · US
US2021121825A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2021121825-A1 |
| Application number | US-202017083699-A |
| Country | US |
| Kind code | A1 |
| Filing date | Oct 29, 2020 |
| Priority date | Oct 29, 2019 |
| Publication date | Apr 29, 2021 |
| Grant date | — |
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Described herein are novel emulsion liquid membranes useful for extracting pollutants from industrial wastewater and water. The emulsion liquid membranes include, in various phases, at least one of nanoparticles, an ionic liquid, and combinations of nanoparticles and ionic liquids. Use of the present emulsion liquid membranes enhances the separation and the stability of the ELM method for pollutant extraction and recovery from wastewater and water.
Opening claim text (preview).
What is claimed is: 1 . An emulsion liquid membrane comprising: an emulsion phase comprising a stripping aqueous phase dispersed in an organic membrane phase, wherein the stripping aqueous phase comprises nanoparticles and the organic phase optionally comprises an ionic liquid. 2 . The emulsion liquid membrane of claim 1 , wherein the nanoparticles are magnetic. 3 . The emulsion liquid membrane of claim 1 , wherein the nanoparticles comprise a compound selected from the group consisting of FeO, Fe 2 O 3 , Fe 3 O 4 , Y 3 Fe 5 O 12 , SrFe 12 O 19 , SmCo 5 , Al 2 O 3 , MgO, SiC, CuO, and combinations thereof. 4 . The emulsion liquid membrane of claim 1 , wherein the nanoparticles have a diameter in the range of from about 1 nm to about 60 nm. 5 . The emulsion liquid membrane of claim 1 , wherein the ionic liquid is selected from the group consisting of 1-butyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide ([BMIM][NTf 2 ]), 1-Methyl-3-octylimidazolium hexafluorophosphate ([OMIM]PF 6 ), and combinations thereof. 6 . An emulsion liquid membrane comprising: an emulsion phase comprising a stripping aqueous phase dispersed in an organic membrane phase, wherein the organic membrane phase comprises an ionic liquid and the stripping aqueous phase optionally comprises nanoparticles. 7 . The emulsion liquid membrane of claim 1 , wherein the nanoparticles are magnetic. 8 . The emulsion liquid membrane of claim 1 , wherein the nanoparticles comprise a compound selected from the group consisting of FeO, Fe 2 O 3 , Fe 3 O 4 , Y 3 Fe 5 O 12 , SrFe 12 O 19 , SmCo 5 , Al 2 O 3 , MgO, SiC, CuO, and combinations thereof. 9 . The emulsion liquid membrane of claim 1 , wherein the nanoparticles have a diameter in the range of from about 1 nm to about 60 nm. 10 . The emulsion liquid membrane of claim 1 , wherein the ionic liquid is selected from the group consisting of 1-butyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide ([BMIM][NTf 2 ]), 1-Methyl-3-octylimidazolium hexafluorophosphate ([OMIM]PF 6 ), and combinations thereof. 11 . A method for removing and/or extracting at least one pollutant, the method comprising: dispersing an emulsion phase of an emulsion liquid membrane in an external aqueous phase (W2), wherein the emulsion phase of the emulsion liquid membrane comprises a stripping aqueous phase (W1) dispersed in an organic membrane phase, wherein the stripping aqueous phase comprises nanoparticles and a stripping agent, and removing and/or extracting the at least one pollutant wherein the at least one pollutant is transferred from the external aqueous phase (W2) through the organic membrane phase to the stripping aqueous phase (W1) and the at least one pollutant reacts with the stripping agent in the stripping aqueous phase (W1) and is removed from the external aqueous phase (W2). 12 . The method of claim 11 , wherein the organic membrane phase optionally comprises an ionic liquid and wherein the external aqueous phase (W2) comprises at least one pollutant. 13 . The method of claim 11 , wherein the organic membrane phase comprises an ionic liquid and wherein the external aqueous phase (W2) comprises nanoparticles and at least one pollutant. 14 . The method of claim 11 , wherein the at least one pollutant is selected from the group consisting of at least one metal, at least one hydrocarbon, and combinations thereof. 15 . The method of claim 11 , wherein the at least one metal is selected from the group consisting of lead (II), vanadium (V), and combinations thereof. 16 . The method of claim 11 , wherein the at least one hydrocarbon is selected from the group consisting of 4-nitrophenol, benzoic acid, and combinations thereof. 17 . The method of claim 11 , wherein the nanoparticles are magnetic. 18 . The method of claim 11 wherein the nanoparticles comprise a compound selected from the group consisting of FeO, Fe 2 O 3 , Fe 3 O 4 , Y 3 Fe 5 O 12 , SrFe 12 O 19 , SmCo 5 , Al 2 O 3 , MgO, SiC, CuO, and combinations thereof. 19 . The method of claim 11 , wherein the nanoparticles have a diameter in the range of from about 1 nm to about 60 nm. 20 . The method of claim 12 , wherein the ionic liquid is selected from the group consisting of 1-butyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide ([BMIM][NTf 2 ]), 1-Methyl-3-octylimidazolium hexafluorophosphate ([OMIM]PF 6 ), and combinations thereof.
by extraction · CPC title
Nanoparticles or nanotubes · CPC title
Heavy metals or heavy metal compounds · CPC title
Phenols · CPC title
for separation of magnetic materials, e.g. magnetic flocculation · CPC title
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