An extrusion process for preparing a low molecular weight polytetrafluoroethylene micropowder
US-2024017445-A1 · Jan 18, 2024 · US
US9427889B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9427889-B2 |
| Application number | US-201013382252-A |
| Country | US |
| Kind code | B2 |
| Filing date | Aug 20, 2010 |
| Priority date | Sep 29, 2009 |
| Publication date | Aug 30, 2016 |
| Grant date | Aug 30, 2016 |
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The present invention relates to a process for producing colored plastics molding compositions with aqueous liquid colors, where an aqueous liquid color is added to a molten plastics molding composition. The present invention also describes a system for conducting the said process.
Opening claim text (preview).
The invention claimed is: 1. A process or producing a color plastic molding composition, the process comprising: adding an aqueous solution comprising a colorant and water to a molten plastic molding composition in an extruder, wherein the extruder comprises one or more vent zones, and the aqueous solution is added after all of the one or more vent zones. 2. The process of claim 1 , wherein the molten plastic molding composition comprises a poly(meth)acrylate. 3. The process of claim 1 , a content of the colorant in the aqueous solution is from 0.5% to 50% by weight based on a total weight of the aqueous solution. 4. The process of claim 1 , wherein the aqueous solution further comprises a dispersing agent at a content from 5% to 50% by weight based on a total weight of the aqueous solution. 5. The process of claim 4 , wherein the dispersing agent is a polyacrylate comprising a hydrophilic or an ionic group. 6. The process of claim 4 , wherein a ratio by weight % of water to the dispersing agent is in a range from 2:1 to 1:2. 7. The process of claim 1 , wherein the adding is performed under pressure. 8. The process of claim 7 , wherein a pressure of the aqueous solution is in a range from 0.1 to 200 bar. 9. The process of claim 7 , wherein a difference between a first pressure at an aqueous solution feed site in the extruder and a second pressure of the aqueous solution is in a range from 0.1 to 100 bar. 10. The process of claim 9 , wherein a temperature of the molten plastic molding composition at the aqueous solution feed site is in a range from 180 to 330° C. 11. The process of claim 10 , wherein the temperature and the pressure at the aqueous solution feed site are such that an equilibrium state of water is gaseous. 12. The process of claim 1 , wherein a ratio by weight of the aqueous solution to the molten plastic molding composition is in a range from 1:10 to 0.0001:10. 13. The process of claim 1 , further comprising, prior to the adding: continuously polymerizing a reaction mixture comprising monomers in an extruder, to obtain the molten plastic molding composition. 14. The process of claim 1 , which is performed as a continuous process. 15. The process of claim 1 , wherein the extruder comprises one vent zone and the aqueous solution is added after the one vent zone. 16. The process of claim 1 , wherein the extruder comprises a plurality of vent zones and the aqueous solution is added after the last of the plurality of vent zones.
using two or more parallel screws {or at least two parallel non-intermeshing screws}, e.g. twin screw extruders · CPC title
Flow or feed rate · CPC title
Auxiliary unit, e.g. for external melt filtering, re-combining or transfer between units · CPC title
Barrel or housing · CPC title
rotary (B29B7/52 takes precedence) · CPC title
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