Method for the production of ABS compositions having an improved surface following storage in a warm-humid environment
US-9714324-B2 · Jul 25, 2017 · US
US9976029B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9976029-B2 |
| Application number | US-201414764619-A |
| Country | US |
| Kind code | B2 |
| Filing date | Feb 5, 2014 |
| Priority date | Feb 7, 2013 |
| Publication date | May 22, 2018 |
| Grant date | May 22, 2018 |
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The invention relates to a method for producing compositions containing vinylaromatic copolymers which are obtained in an emulsion polymerization process and comprise production-related salt inclusions. Said compositions are characterized by an improved surface quality once the extruded polymer, before being granulated, or the granulate, after being granulated, has been moistened by bringing the polymer in contact with liquid water in a water bath, a tube system filled with water, or a dipping tank, thus making the compositions suitable for producing molded articles having a class A surface that remains flawless over time.
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The invention claimed is: 1. A process for producing a composition comprising A) 0 to 98 parts by weight, based on the sum total of A and B, of a thermoplastic polymer or a mixture of a plurality of thermoplastic polymers different from B and B) 2 to 100 parts by weight, based on the sum total of A and B, of B1) at least one graft polymer prepared in an emulsion polymerization process, B2) optionally at least one graft polymer prepared by the bulk, suspension or solution polymerization process, B3) optionally at least one rubber-free vinyl (co)polymer and C) 0 to 30 parts by weight, based on the sum total of A and B, of at least one commercially available polymer additive, where the sum total of parts by weight A and B is 100, component B, comprises at least one inorganic salt consisting of a cation selected from the group of the alkali metals, alkaline earth metals and aluminum and an anion selected from the group consisting of chloride, sulfate, nitrate, phosphate, acetate and formate, in a concentration of the salt or salt mixture of 100 to 5000 mg/kg based on the composition, and wherein a) in a first process step the entirety of the component(s) containing the salt from B, optionally together with a portion or the entirety of the remaining components from B, A and C is processed in a compounding system, preferably an extruder, to give a polymer blend melt, then this polymer melt is discharged from the extruder and, in the form of polymer strands prior to pelletization or alternatively in the form of pellets after the pelletization, is contacted with water completely by contact with liquid water in a water bath, a water-filled pipe system or a dip bath, b) in a second process step the pellets which have been contacted with water in this way are separated from water not adhering to the surface of the pellets and then are stored under surface-moist conditions, c) in a third process step the pellets thus stored under moist conditions are melted and kneaded in the molten state and/or d) in a fourth process step the component thus prepared is mixed with the remaining components of the composition, the mixture is melted again and kneaded, and the components of the mixture are interdispersed in this way, where a reduced pressure is applied at least in one of steps c) and d) and, in this way, the water introduced into the process in process step a) is removed again from the product, and where the mean storage time of the surface-moist pellets in step b) is at least 24 h. 2. The process as claimed in claim 1 , wherein component B1 contains B1.1) 5% to 95% by weight, based on component B1, of a mixture of B1.1.1) 65% to 85% by weight, based on B1.1, of at least one monomer selected from the group consisting of styrene, a-methylstyrene and methyl methacrylate, and B1.1.2) 15% to 35% by weight, based on B1.1, of at least one monomer selected from the group consisting of acrylonitrile, maleic anhydride and methyl methacrylate, and B1.2) 95% to 5% by weight, based on component B1, of at least one elastomeric graft base. 3. The process as claimed in claim 1 , wherein component B1 contains the inorganic salt as a production-related impurity. 4. The process as claimed in claim 1 , wherein the residence time of the strands or the pellets in the water bath in process step a) is between 1 second and 60 minutes. 5. The process as claimed in claim 1 , wherein the contacting with liquid water in process step a) is effected within the temperature range from 5 to 95° C. 6. The process as claimed in claim 1 , wherein the amount of water in the surface-moist pellets is at least 1% by weight and at most 30% by weight, based on the sum total of water and pellets. 7. The process as claimed in claim 1 , wherein process step b) is conducted continuously. 8. The process as claimed in claim 1 , wherein process step b) is conducted batchwise. 9. The process as claimed in claim 1 , wherein the storage time in process step b) is at least 24 h. 10. The process as claimed in claim 1 , wherein the storage according to process step b) is followed downstream by a further process step for removing the surface water from the pellets discharged. 11. The process as claimed in claim 1 , wherein the contacting with liquid water in process step a) and storage of the moist pellets in process step b) takes place within a temperature range from 5° C. to 95° C. 12. The process as claimed in claim 1 , wherein the component(s) B containing the salt are in the form of pellets. 13. The process as claimed in claim 1 , wherein the compositions comprise A) 30 to 85 parts by weight, based on the sum total of A and B, B) 15 to 70 parts by weight, based on the sum total of A and B, C) 0.3 to 7 parts by weight, based on the sum total of A and B. 14. The process as claimed in claim 1 , wherein the salt is an alkali metal chloride, alkaline earth metal chloride or aluminum chloride or an alkali metal sulfate, alkaline earth metal sulfate or aluminum sulfate, preferably magnesium sulfate, or a mixture thereof. 15. The process as claimed in claim 1 , wherein the composition comprises, as component C, at least one representative selected from the group consisting of flame retardants, flame retardant synergists, smoke-inhibiting additives, antidripping agents, internal and external lubricants and demolding agents, flowability aids, antistats, conductivity additives, UV stabilizers, light stabilizers, thermal stabilizers, antioxidants, transesterification inhibitors, hydrolysis stabilizers, antibacterial additives, scratch resistance-improving additives, IR absorbents, optical brighteners, fluorescent additives, fillers and reinforcers, acids, and dyes and pigments. 16. A composition produced by a process as claimed in claim 1 . 17. A shaped body or molding composed of a polymer composition produced by a process as claimed in claim 1 having a class A surface and a partial or full high-gloss finish, characterized by a gloss level in said high-gloss regions of at least 95, determined by reflection in accordance with DIN 67530 at a measuring angle of 60°, which may optionally have been subjected partly or fully to a further surface treatment step. 18. The shaped body or molding as claimed in claim 17 which, after treatment under warm and moist conditions, does not have any blisters having a diameter of greater than 300 μm and having a relative area of defects having blister topography based on the surface size studied (A rel ) less than 50 ppm. 19. The process as claimed in claim 1 , wherein the concentration of the salt or salt mixture is 150 to 2000 mg/kg, based on the composition, wherein the reduced pressure is at least 500 mbar, wherein the residence time of the strands or the pellets in the water bath in process step a) is between 2 seconds and 10 minutes, wherein the contacting with liquid water in process step a) is effected within the temperature range from 10 to 90° C., wherein the storage time in process step b) is at least 48 h, and wherein the contacting with liquid water in process step a) and storage of the moist pellets in process step b) takes place within a temperature range from 10° C. to 90° C. 20. The process as claimed in claim 1 , wherein the concentration of the salt or salt mixture is 200 to 1000 mg/kg, based on the composition, wherein the reduced pressure is at least 800 mbar, wherein the residence time of the strands or the pellets in the water bath in process step a) is between 3 seconds and 60 seconds, where
Purification · CPC title
Use of inorganic substances as compounding ingredients · CPC title
containing four or more polymers in a blend · CPC title
Compositions of polycarbonates; Compositions of derivatives of polycarbonates · CPC title
Treatment of solid polymer wetted by water or organic solvents, e.g. coagulum, filter cakes · CPC title
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