Apparatus for preparing polymer latex resin powder and method of preparing polymer latex resin powder using the same
US-9504972-B2 · Nov 29, 2016 · US
US10882940B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10882940-B2 |
| Application number | US-201716096879-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 13, 2017 |
| Priority date | Apr 29, 2016 |
| Publication date | Jan 5, 2021 |
| Grant date | Jan 5, 2021 |
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The present invention relates to a process for the production of copolymers comprising: (i) forming a reaction mixture comprising an elastomer and a vinyl aromatic compound; (ii) introducing the reaction mixture to a reaction vessel; and (iii) performing a polymerisation reaction wherein steps (i)-(iii) are performed in that order to obtain a copolymer comprising: (a) a phase comprising a reaction product of the elastomer with the vinyl aromatic compound; and (b) a phase comprising a reaction product of the vinyl aromatic compound wherein a sample of the reactor contents is obtained during step (iii) to determine of the formed copolymer: the content of phase (b); and/or ● the molecular weight of phase (b) wherein the determination of the content of phase (b) in the formed copolymer and the molecular weight of phase (b) is performed by a method comprising isolation of phase (b) from the sample of the formed copolymer and subjecting the obtained phase (b) to molecular analysis. Such process allows for the determination of the content of the phase (b) and of the molecular weight thereof in a quick and efficient manner, allowing for adjustment of process parameters such that the production of products that not correspond to the desired product quality is minimised.
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The invention claimed is: 1. A process for the production of copolymers comprising: (i) forming a reaction mixture comprising an elastomer and a vinyl aromatic compound; (ii) introducing the reaction mixture to a reaction vessel; and (iii) performing a polymerization reaction; wherein steps (i) (iii) are performed in that order; thereby obtaining a copolymer comprising: (a) a phase comprising a reaction product of the elastomer with the vinyl aromatic compound; and (b) a phase comprising a reaction product of the vinyl aromatic compound; wherein a sample from the reaction vessel is obtained during step (iii) to determine of the formed copolymer: the content of phase (b); and/or the molecular weight of phase (b); wherein the determination of the content of phase (b) in the formed copolymer and the molecular weight of phase (b) is performed by a method comprising isolation of phase (b) from the sample of the formed copolymer by (1) preparing a solution of the formed copolymer in a solvent; and (2) removing an insoluble fraction from the solution obtained in step (1) by filtration to obtain phase (b) as a filtered sample and subjecting the obtained phase (b) to molecular analysis, wherein the filtration is in a filter system comprising at least the following filtration layers through which the solution is transported in this order; a layer 1 comprising glass fibres such that particles of ≥1.00 μm do not pass these layers; a layer 2 comprising a membrane filter such that particles of ≥0.45 μm do not pass this layer; and the molecular analysis is performed by gel permeation chromatography in accordance with ASTM D5296-11. 2. The process according to claim 1 , wherein the elastomer is one or more selected from poly(butadiene), poly(styrene-butadiene), poly(butylacrylate), poly(butadiene-acrylonitrile) or poly(isoprene); and/or the vinyl aromatic compound is selected from styrene, α-methyl styrene, halogenated styrene, vinyltoluene, butylstyrene, p-hydroxystyrene or methoxy styrene. 3. The process according to claim 1 , wherein the reaction mixture further comprises a comonomer selected from acrylonitrile, itaconic acid, acrylamide, methacrylamide, maleic anhydride, maleimide, substituted maleimides, methacylonitrile, α-chloroacrylonitrile, β-chloroacrylonitrile, α-bromoacrylonitrile, acrylic acid, methyl(meth)acrylate, ethyl(meth)acrylate, n-butyl(meth)acrylate, t-butyl(meth)acrylate, n-propyl(meth)acrylate, isopropyl(meth)acrylate, 2-ethylhexyl(meth)acrylate, or glycidyl(meth)acrylates, wherein phase (a) comprises a reaction product of the elastomer with the vinyl aromatic compound and the comonomer, and wherein phase (b) comprises a reaction product of the vinyl aromatic compound and the comonomer. 4. The process according to claim 1 , wherein the filter system comprises a further layer positioned between layer 1 and layer 2, this layer being such that particles of ≥0.70 μm do not pass this layer. 5. The process according to claim 1 , wherein the step of preparing the solution involves preparing a solution of ≥1.0 and ≤7.0 mg/ml of the formed copolymer in a solvent, wherein the solvent is selected from chloroform, tetrahydrofuran, methylene chloride, chlorobenzene, diethyl ether, dimethyl formamide, dimethyl sulfoxide, ethyl acetate, toluene, n-methyl-2-pyrrolidinone, 1-butanol, 2-butanol, acetonitrile, benzene, methyl-ethyl ketone or acetone. 6. The process according to claim 1 , wherein a chromatogram having an elution peak is obtained by the gel permeation chromatography and the content of phase (b) is determined by comparison of the elution peak of the chromatogram of the filtered sample obtained using a refractive index detector to detect the response with a reference sample having a defined content of phase (b), wherein the ratio of the surface of the peak of the filtered sample to the surface of the peak of the reference sample corresponds to the ratio of the content of phase (b) in the filtered sample to the content of phase (b) in the reference sample. 7. The process according to claim 1 , wherein the process is a continuous process wherein the determined content of phase (b) in the formed copolymer and the molecular weight of phase (b) are used as control inputs for the process. 8. The process according to claim 3 , wherein: the elastomer is poly(butadiene); the vinyl aromatic compound is styrene; and/or the comonomer is acrylonitrile; wherein the copolymer comprises ≥5.0 and ≤98.0 wt % of phase (b) with regard to the total weight of the copolymer. 9. The process according to claim 1 , wherein the copolymer obtained from the process is an acrylonitrile-butadiene-styrene copolymer. 10. The process according to claim 5 , wherein the solvent is tetrahydrofuran. 11. A method for determination of the quantity of a phase of a copolymer and the molecular weight of the phase of the copolymer, wherein the phase of the copolymer comprising the reaction product of a vinyl aromatic compound and a compound comprising a vinyl moiety and a nitrile moiety, the method comprising: (1) preparing a solution of the copolymer in a solvent of ≥1.0 and ≤7.0 mg/ml; (2) filtering the solution obtained from (1) in a filter system comprising at least four filtration layers, wherein the filtration layers are constructed as follows: a layer 1 and 2 comprising glass fibres such that particles of ≥1.00 μm do not pass these layers; a layer 3 comprising glass fibres such that particles of ≥0.70 μm do not pass this layer; and a layer 4 comprising a membrane filter such that particles of ≥0.45 μm do not pass this layer; to obtain a filtered sample; (3) subjecting the filtered sample to gel permeation chromatography in accordance with ASTM D5296-11; wherein the solution is filtered in the filter system by passing the solution through the filtration layers of the filter system in such way that the solution passes layer 1, layer 2, layer 3 and layer 4 in this order.
Polymerisation in bulk · CPC title
Vinyl aromatic monomers and nitriles as the only monomers · CPC title
Organic solvent · CPC title
Control or adjustment of polymerization parameters · CPC title
Treatment of polymer solutions {(C08F6/001, C08F6/006, C08F6/008, C08F6/02, C08F6/04 take precedence)} · CPC title
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