Separations With Ionic Liquid Solvents
US-2016096784-A1 · Apr 7, 2016 · US
US2021229033A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2021229033-A1 |
| Application number | US-201816972020-A |
| Country | US |
| Kind code | A1 |
| Filing date | Jul 4, 2018 |
| Priority date | Jul 4, 2018 |
| Publication date | Jul 29, 2021 |
| Grant date | — |
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Polyethylenimine coated polymeric beads comprising a polymer that comprises, based on the weight of the polymer, from 25% to 75% by weight of structural units of an acetoacetoxy or acetoacetamide functional monomer, and from 25% to 75% by weight of structural units of a polyvinyl monomer; the polyethylenimine having a number average molecular weight of 300 g/mol or more; the polyethylenimine coated polymeric beads having a specific surface area in the range of from 20 to 400 m2/g; a process of preparing the polyethylenimine coated polymeric beads; a gas filter device comprising the polyethylenimine coated polymeric beads as a filter medium; and a method of removing aldehydes from air containing aldehydes, comprising contacting the air with the polyethylenimine coated polymeric beads.
Opening claim text (preview).
What is claimed is: 1 . Polyethylenimine coated polymeric beads comprising a polymer, wherein the polymer comprises, based on the weight of the polymer, from 25% to 75% by weight of structural units of an acetoacetoxy or acetoacetamide functional monomer, and from 25% to 75% by weight of structural units of a polyvinyl monomer; wherein the polyethylenimine has a number average molecular weight of 300 g/mol or more; and wherein the polyethylenimine coated polymeric beads have a specific surface area in the range of from 20 to 400 m 2 /g. 2 . The polyethylenimine coated polymeric beads of claim 1 , wherein the polymeric beads have a specific surface area in the range of from 40 to 250 m 2 /g. 3 . The polyethylenimine coated polymeric beads of claim 1 , wherein the polyethylenimine has a structure of formula (II), where n, m, p, and x are each independently an integer of from 0 to 1,000, provided that n+m+p+x>5. 4 . The polyethylenimine coated polymeric beads of claim 1 , wherein the number average molecular weight of the polyethylenimine is in the range of from 300 to 10,000 g/mol. 5 . The polyethylenimine coated polymeric beads of claim 1 , wherein the acetoacetoxy or acetoacetamide functional monomer is selected from the group consisting of acetoacetoxyethyl methacrylate, acetoacetoxyethyl acrylate, acetoacetoxypropyl methacrylate, allyl acetoacetate, acetoacetoxybutyl methacrylate, and 2,3-di(acetoacetoxy)propyl methacrylate. 6 . The polyethylenimine coated polymeric beads of claim 1 , wherein the polyvinyl monomer is selected from the group consisting of divinylbenzene, trivinyl benzene, divinylnaphthalene, trimethylolpropane trimethacrylate, allyl (meth)acrylate, tripropylene glycol dimethacrylate, diethylene glycol dimethacrylate, ethylene glycol di(meth)acrylate, 1,6-hexanediol di(meth)acrylate, 1,3-butylene glycol dimethacrylate, and 1,4-butylene glycol di(meth)acrylate. 7 . The polyethylenimine coated polymeric beads of claim 1 , wherein the polymer comprises, based on the weight of the polymer, from 30% to 70% by weight of structural units of the acetoacetoxy or acetoacetamide functional monomer, from 30% to 70% by weight of structural units of the polyvinyl monomer, and from 0 to 20% by weight of structural units of a monovinyl aromatic monomer. 8 . The polyethylenimine coated polymeric beads of claim 1 , having a number average particle size of from 200 to 5,000 μm. 9 . A process for preparing the polyethylenimine coated polymeric beads of claim 1 , comprising, (i) suspension polymerization of monomers in the presence of a porogen, wherein the monomers comprise, based on the total weight of monomers, from 25% to 75% by weight of an acetoacetoxy or acetoacetamide functional monomer, and from 25% to 75% by weight of a polyvinyl monomer; and (ii) contacting the obtained polymer from step (i) with a polyethylenimine to give the polyethylenimine coated polymeric beads; wherein the polyethylenimine has a number average molecular weight of 300 g/mol or more; and wherein the polyethylenimine coated polymeric beads have a specific surface area in the range of from 20 to 400 m 2 /g. 10 . The process of claim 9 , wherein the polyethylenimine is used in an amount of from 0.1% to 15%, by weight based on the weight of the polymer. 11 . The process of claim 9 , wherein the polyethylenimine has a structure of formula (II), where n, m, p, and x are each independently an integer of from 0 to 1,000, provided that n+m+p+x>5. 12 . The process of claim 9 , wherein the number average molecular weight of the polyethylenimine is in the range of from 300 to 10,000 g/mol. 13 . The process of claim 9 , wherein the porogen is selected from the group consisting of diisobutyl ketone, toluene, butyl acetate, isooctane and methyl butyl ketone. 14 . A gas filter device comprising the polyethylenimine coated polymeric beads of claim 1 as a filter medium. 15 . A method of removing aldehydes from air containing aldehydes, comprising contacting the air with the polyethylenimine coated polymeric beads of claim 1 .
being less than 100 m2/g · CPC title
Polymers obtained by reactions otherwise than involving only carbon to carbon unsaturated bonds · CPC title
consisting of a polymer obtained by reactions involving only carbon to carbon unsaturated bonds · CPC title
being in the range 100-500 m2/g · CPC title
Sorbent size or size distribution, e.g. particle size · CPC title
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