Process for production of elastomer agglomerate composition, elastomer agglomerate composition and its use
US-10843144-B2 · Nov 24, 2020 · US
US11090837B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11090837-B2 |
| Application number | US-201716466507-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 6, 2017 |
| Priority date | Dec 9, 2016 |
| Publication date | Aug 17, 2021 |
| Grant date | Aug 17, 2021 |
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A process for the production of an elastomer agglomerate composition wherein the process comprises the steps in this order: (a) providing a slurry comprising elastomeric particles having an average particle size of ≤150 nm in water; and (b) forcing the slurry from (a) through an aperture at a flow velocity of at least 500 m/s. The elastomer agglomerate compositions produced via such process demonstrate a particularly desirable high average particle size.
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The invention claimed is: 1. A process for the production of an elastomer agglomerate composition wherein the process comprises the steps in this order: (a) providing a slurry comprising elastomeric particles having an average particle size of ≤150 nm in water; and (b) forcing the slurry from (a) through an aperture at a flow velocity of at least 500 m/s. 2. The process according to claim 1 , wherein the material flow through the aperture is confined by a flat first surface and a flat second surface together forming a channel. 3. The process according to claim 1 , wherein the slurry is introduced at a pressure of ≥40 and ≤60 MPa. 4. The process according to claim 1 , wherein the slurry comprises ≥20.0 wt % of elastomeric particles with regard to the total weight of the slurry. 5. The process according to claim 1 , wherein the elastomeric particles are selected from polybutadiene particles, poly(styrene-butadiene) particles, poly(acrylonitrile butadiene) particles or polybutylacrylate particles. 6. The process according to claim 1 , wherein the process is performed using a valve assembly comprising the aperture, the valve assembly further comprising a seat, a flow channel through which the slurry flows at a certain pressure towards the aperture, and a valve subjected to a pressure in the direction opposite the flow direction of the slurry, wherein the seat comprises a central opening forming the flow channel, and wherein the valve pressure and the pressure of the slurry are arranged such that the slurry is forced through the aperture at a flow velocity of at least 500 m/s. 7. The process according to claim 6 , wherein the seat is a circular seat comprising a circular opening. 8. The process according to claim 1 , wherein the slurry is forced through the aperture at a flow velocity of at least 700 m/s and at most 1000 m/s. 9. The process according to claim 1 , wherein the elastomeric particles account for at least 98.0 wt % of the total weight of solid ingredients in the slurry. 10. An elastomer agglomerate composition produced according to the process of claim 1 , wherein the elastomer agglomerate composition comprises less than 0.02 wt %, with regard to the total weight of the elastomer agglomerates in the elastomer composition, of agglomerates having a particle size of >3000 nm; and less than 30 wt % of elastomer agglomerates having a particle size of <200 nm, with regard to the total weight of the elastomer agglomerates. 11. The elastomer agglomerate composition according to claim 10 , wherein the elastomer agglomerate composition comprises less than 25 wt % of elastomer agglomerates having a particle size of <200 nm, with regard to the total weight of the elastomer agglomerates. 12. The elastomer agglomerate composition according to claim 10 , wherein the elastomer agglomerate composition comprises ≥60 wt % with regard to the total weight of the elastomer agglomerates, of agglomerates having a particle size of >200 nm and ≤1000 nm. 13. The elastomer agglomerate composition according to claim 10 , wherein the elastomer agglomerate composition comprises ≤10.0 wt % of elastomer agglomerates having a particle size of >1000 nm, with regard to the total weight of the elastomer agglomerates. 14. The elastomer agglomerate composition according to claim 10 , wherein the elastomer agglomerate composition comprises ≤1.0 wt % of elastomer agglomerates having a particle size of >1500 nm, with regard to the total weight of the elastomer agglomerates. 15. Acrylonitrile-butadiene-styrene copolymer produced using the elastomer agglomerate composition according to claim 10 . 16. The process according to claim 1 , wherein the material flow through the aperture is confined by a flat first surface and a flat second surface together forming a channel; wherein the slurry is introduced at a pressure of ≥40 and ≤60 MPa; wherein the slurry comprises ≥20.0 wt % of elastomeric particles with regard to the total weight of the slurry; and wherein the elastomeric particles are selected from polybutadiene particles, poly(styrene-butadiene) particles, poly(acrylonitrile butadiene) particles or polybutylacrylate particles. 17. The process according to claim 16 , wherein the process is performed using a valve assembly comprising the aperture, the valve assembly further comprising a seat, a flow channel through which the slurry flows at a certain pressure towards the aperture, and a valve subjected to a pressure in the direction opposite the flow direction of the slurry, wherein the seat comprises a central opening forming the flow channel, and wherein the valve pressure and the pressure of the slurry are arranged such that the slurry is forced through the aperture at a flow velocity of at least 700 m/s and at most 1000 m/s. 18. The process according to claim 16 , wherein the elastomeric particles account for at least 98.0 wt % of the total weight of solid ingredients in the slurry.
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