Methods and apparatus for controlling metals in liquids
US-2015360206-A1 · Dec 17, 2015 · US
US10017401B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10017401-B2 |
| Application number | US-201515116553-A |
| Country | US |
| Kind code | B2 |
| Filing date | Feb 4, 2015 |
| Priority date | Feb 7, 2014 |
| Publication date | Jul 10, 2018 |
| Grant date | Jul 10, 2018 |
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The present invention relates to aluminum-doped chelate resins containing iminodiacetic acid groups, to a production process for aluminum-doped chelate resins containing iminodiacetic acid groups, and to a device comprising at least one layer of at least one aluminum-doped chelate resin containing iminodiacetic acid groups, and to the uses of this device and of the chelate resins for removal of fluoride from water.
Opening claim text (preview).
What is claimed is: 1. An aluminum-doped chelate resin for absorption of anions, the resin comprising a polymer comprising a plurality of phenyl groups functionalized at a first substitution level of 0.6 to 1.5 with functional groups represented by the structural formula (I) —CH 2 —NR 2 , (I) where each R is independently —H or —CH 2 COO − ; the nitrogen is functionalized with acetate groups at a functionalization level of 1.4 to 1.65; and the acetate ions are conjugated with AIX, where X is any monovalent anion. 2. The resin according to claim 1 , wherein the first substitution level is 0.6 to 1.2. 3. The resin according to claim 1 , wherein the first substitution level is 0.7 to 0.9. 4. The resin according to claim 1 , wherein: the polymer comprises repeat units derived from at least one monovinylaromatic compound and at least one polyvinylaromatic compound; and X is nitrate, nitrite, hydrogensulfate, hydrogencarbonate or a halide. 5. The resin according to claim 1 , wherein: the monovinylaromatic compounds include styrene, vinyltoluene, ethylstyrene, α-methylstyrene, chlorostyrene, chloromethylstyrene, alkyl acrylates or alkyl methacrylates; the polyvinylaromatic compounds include divinylbenzene, divinyltoluene, trivinylbenzene, divinylnaphthalene, trivinylnaphthalene, 1,7-octadiene, 1,5-hexadiene, ethylene glycol dimethacrylate, trimethylolpropane trimethacrylate or allyl methacrylate; and X is halide. 6. The resin according to claim 3 , wherein the monovinylaromatic compound is styrene; the polyvinylaromatic compound divinylbenzene; and X is chlorine. 7. A process for producing the chelate resin as claimed in claim 1 , the process comprising: converting monomer droplets composed of at least one monovinylaromatic compound, at least one polyvinylaromatic compound, at least one porogen, and at least one initiator to a crosslinked bead polymer; phthalimidomethylating aromatic groups of the crosslinked bead polymer at the first substitution level of 0.6 to 1.5 with phthalimide derivatives to produce phthalimidomethylated bead polymer; converting the phthalimidomethylated bead polymer to aminomethylated bead polymer to produce aminomethylated bead polymer; reacting the aminomethyl groups of the aminomethylated bead polymer with chloroacetic acid or salts thereof to produce chelate resins having iminoacetate groups at the functionalization level of 1.4 to 1.65; and contacting the chelate resin containing aminoacetate groups with an aluminum salt solution of a trivalent aluminum ion to produce the chelate resin. 8. The process according to claim 7 , wherein: the phthalimidomethylation reaction comprises a molar ratio of phthalimide derivative to bead polymer of 0.7 mol to 1.7 mol; and the reaction with chloroacetic acid comprises a molar ratio of chloroacetic acid or salts thereof to aminomethylated bead polymer of 1.8:1 to 2.5:1 for functionalization of amino groups at the functionalization level of 1.4 to 1.65. 9. The process according to claim 8 , wherein the phthalimidomethylation is conducted at a temperature of 60° C. to 80° C. 10. The process according to claim 9 , wherein the phthalimidomethylation comprises a condensation of the phthalimide derivative with the bead polymer using a catalyst in a molar ratio of 0.1:1 to 0.45:1 in relation to the amount of bead polymer used. 11. The process as claimed in claim 10 , wherein the contacting of the chelate resin containing iminoacetate groups with an aluminum salt solution comprises contacting the resin with 2 to 6 mol of aluminum based on one liter of chelate resin containing iminoacetate groups. 12. The process according to claim 7 , wherein: the phthalimidomethylation reaction comprises a molar ratio of phthalimide derivative to bead polymer of 0.7 mol to 1.35 mol; and the reaction with chloroacetic acid comprises a molar ratio of chloroacetic acid or salts thereof to aminomethylated bead polymer of 1.8:1 to 2.5:1 for functionalization of the amino groups at the functionalization level of 1.4 to 1.65. 13. A device for removing fluoride from water, the device comprising at least one layer of at least one aluminum-doped chelate resin containing iminoacetate groups as claimed in claim 1 . 14. A method for removing fluoride from water, the method comprising contacting water containing fluoride with the aluminum-doped chelate resin of claim 1 to absorb fluoride ions from the water.
from semiconductor processing, e.g. waste water from polishing of wafers · CPC title
from the silicate or ceramic industries, e.g. waste waters from cement or glass factories · CPC title
Fluorine or fluorine-containing compounds · CPC title
by addition of complex-forming compounds · CPC title
using synthetic organic sorbents · CPC title
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