Fluoropolymer compositions and purification methods thereof
US-2016362508-A1 · Dec 15, 2016 · US
US10934371B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10934371-B2 |
| Application number | US-201616348623-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 22, 2016 |
| Priority date | Dec 22, 2016 |
| Publication date | Mar 2, 2021 |
| Grant date | Mar 2, 2021 |
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A process of stripping a dispersion of organic extender particles with volatile organic compounds and a method of reducing volatile organic compounds.
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What is claimed is: 1. A process of stripping a dispersion of core-shell organic extender particles with volatile organic compounds, comprising: providing a dispersion of core-shell organic extender particles with volatile organic compounds, which particles comprise, when dry, one or more voids; mixing the dispersion of core-shell organic extender particles with a binder comprising, as polymerized units, an acetoacetyl functional monomer, and having an average particle size of from 30 nm to 400 nm to form an aqueous polymer composition; and steam stripping the aqueous polymer composition. 2. The process of claim 1 , wherein the dry weight ratio of the binder to the dispersion of core-shell organic extender particles is in the range of 5:95 to 90:10. 3. The process of claim 1 , wherein the binder has an average particle size of from 30 nm to 200 nm. 4. The process of claim 1 , wherein the binder further comprises adipic dihydrazide, oxalic dihydrazide, isophthalic dihydrazide, polyacrylic polyhydrazide, or mixtures thereof. 5. The process of claim 1 , wherein the binder is an acrylic emulsion polymer. 6. The process of claim 1 , wherein the binder has a glass transition temperature of from −50° C. to 100° C. 7. The process of claim 1 , wherein the core-shell organic extender particles comprises polymerized units of styrene in the shell. 8. The process of claim 1 , wherein steam stripping is a continuous or batch process. 9. The process of claim 1 , wherein steam stripping the aqueous polymer composition is conducted by feeding the aqueous polymer composition and steam into a stripper under vacuum or under atmospheric pressure; removing at least a portion of the volatile organic compounds from the aqueous polymer composition; transferring the portion of the volatile organic compounds to the steam; and separating the steam from the aqueous polymer composition.
Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters · CPC title
from polymer solutions, suspensions, dispersions or emulsions without recovery of the polymer therefrom · CPC title
Flash degasification (the other groups take precedence) · CPC title
with one or more auxiliary substances · CPC title
Steam distillation · CPC title
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