Separating agent
US-2015343420-A1 · Dec 3, 2015 · US
US9809706B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9809706-B2 |
| Application number | US-201414915326-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 1, 2014 |
| Priority date | Aug 30, 2013 |
| Publication date | Nov 7, 2017 |
| Grant date | Nov 7, 2017 |
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The present invention relates to a process for the separation of enantiomers or resolution of racemic mixtures using high surface area core-shell polymer beads. The present invention further relates to a core-shell functionalized polymer comprising a core which comprises copolymer made from monomers selected from non-aromatic acrylate, ethylene dimethacrylate and divinyl-benzene, a shell which comprises monomers selected from glycidyl ethers of methacrylate and a chiral selector selected from tartaric acid derivatives and amino acids.
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We claim: 1. A core-shell functionalized polymer comprising: i. a core comprising a crosslinked copolymer made from monomers, said monomers selected from vinyl cyanide, vinylidene cyanide, non-aromatic acrylate, ethylene dimethacrylate and divinylbenzene; ii. a shell, comprising a polymer made from monomers selected from glycidyl ethers of methacrylate; and iii. a chiral selector selected from tartaric acid derivatives and amino acids. 2. The core-shell functionalized polymer as claimed in claim 1 , wherein the proportion of shell polymer is 5 to 90% by weight based on the total amount of the monomers of the core copolymer. 3. The core-shell functionalized polymer as claimed in claim 1 , wherein the core comprises crosslinked copolymers selected from poly(MMA-co-DVB) and poly(MMA-co-EDMA). 4. The core-shell functionalized polymer as claimed in claim 1 , wherein glycidyl ethers of methacrylate is glycidyl methacrylate. 5. The core-shell functionalized polymer as claimed in claim 1 , wherein the core-shell functionalized polymer is in the form of beads. 6. The core-shell functionalized polymer as claimed in claim 1 , wherein chiral selectors are selected D-(−)-ditoluoyl tartaric acid and D-(−)-dibenzoyl tartaric acid and amino acid is L-proline. 7. The core-shell functionalized polymer as claimed in claim 1 , wherein said polymer is useful for the separation or resolution of enantiomers of racemic mixtures by using high performance liquid chromatography. 8. The core-shell functionalized polymer as claimed in claim 7 , wherein the racemic mixture is a drug racemic mixture selected from β2-adrenergic receptor agonist drugs. 9. The core-shell functionalized polymer of claim 8 , wherein the β2-adrenergic receptor agonist drugs are selected from (±)-terbutaline and (±)-salbutamol. 10. The core-shell functionalized polymer as claimed in claim 1 , wherein efficiency of chiral selectors is in the range of 20 to 70% in the period of 2 to 50 h. 11. The core-shell functionalized polymer of claim 1 , wherein the non-aromatic acrylate is selected from ethyl acrylate, propyl acrylate, butyl acrylate, cyclohexyl acrylate, 2-ethyl hexyl acrylate, methyl acrylate, methyl methacrylate, and butyl methacrylate. 12. The core-shell functionalized polymer of claim 1 , wherein vinyl cyanide or vinylidene cyanide is selected from acrylonitrile and methacrylonitrile. 13. A process for the preparation of core-shell functionalized polymer as claimed in claim 1 , comprising the steps of: a) providing porous crosslinked copolymer, wherein the crosslinked copolymer is made from monomers selected from vinyl cyanide, vinylidene cyanide, non-aromatic acrylate, ethylene dimethacrylate and divinylbenzene; b) providing linear polymer containing oxiranyl groups, wherein the linear polymer is made from monomers selected from glycidyl ethers of methacrylate; c) adding the crosslinked copolymer of step a) with the linear polymer of step b) in a ratio ranging between 0.3 to 0.7 wt % at a temperature in the range of 20 to 40° C. for a period in the range of 10 to 20 min followed by drying at a temperature in the range of 50 to 80° C. for a period in the range of 6 to 10 h to obtain epoxy coated polymer; d) crosslinking partially the oxiranyl groups present on the epoxy coated polymer of step c) with amine groups by adding crosslinker 1,6-hexamethylene diamine with the linear polymer containing oxiranyl groups in a ratio range of 3 to 7 mol % at a temperature in the range of 20 to 40° C. for a period in the range of 10 to 20 min followed by drying at a temperature in the range of 40 to 80° C. for a period in the range of 6 to 10 hours to obtain core-shell polymer; and e) modifying epoxy groups of the polymer product of step d) with 1 to 2 mmol/g chiral tartaric acid derivatives or L-proline derivatives to obtain core-shell functionalized polymer. 14. The process of claim 13 , wherein the non-aromatic acrylate is selected from ethyl acrylate, propyl acrylate, butyl acrylate, cyclohexyl acrylate, 2-ethyl hexyl acrylate, methyl acrylate, methyl methacrylate, and butyl methacrylate. 15. The process of claim 13 , wherein vinyl cyanide or vinylidene cyanide is selected from acrylonitrile and methacrylonitrile.
Divinylbenzene · CPC title
comprising organic material · CPC title
Suspension polymerisation · CPC title
Methyl esters {, e.g. methyl (meth)acrylate} · CPC title
N-Vinyl-pyrrolidone · CPC title
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