Method for the production of ABS compositions having an improved surface following storage in a warm-humid environment

Patent metadata

Field	Value
Publication number	US-9714324-B2
Application number	US-201414764618-A
Country	US
Kind code	B2
Filing date	Feb 5, 2014
Priority date	Feb 7, 2013
Publication date	Jul 25, 2017
Grant date	Jul 25, 2017

Abstract

The invention relates to a method for producing compositions containing vinyl-aromatic copolymers that are obtained in an emulsion polymerization process and comprise production-related salt inclusions. Said compositions are characterized by improved surface quality following storage in a warm-humid environment and are therefore suitable for producing molded articles having a class A surface that remains flawless over time.

First claim

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 on A and B, of at least one commercially available polymer additive,
where the sum total of parts by weight A and B is 100, and
component B, optionally component B1 or a pre-compound composed of component B1 with at least one of components B2 and B3 or with a portion of at least one of components B2 and B3, more preferably a pre-compound composed of component B1 and the entirety or a portion of component B3, 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 contacted in a shaft drier, air circulation drier or climate-controlled silo with a water vapor-containing atmosphere having a relative air humidity of at least 70%,
b) in a second process step the component(s) thus contacted with water are melted and kneaded in the molten state and/or
c) in a third 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 of at least 200 mbar is applied at least in one of steps b) and c) and, in this way, the water introduced into the process in process step a) is removed again from the product.

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, α-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, optionally selected from the group consisting of polybutadiene rubber and styrene-butadiene block copolymer rubber.

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 vessels, silos and/or containers are charged continuously with water vapor or else with water vapor admixed optionally heated air in countercurrent or crosscurrent relative to granule flow.

5. The process as claimed in claim 1 , wherein the process is conducted continuously.

6. The process as claimed in claim 1 , wherein the process is conducted batchwise.

7. The process as claimed in claim 1 , wherein polymer granules are fed in on one side of the interior and removed again at another side.

8. The process as claimed in claim 1 , wherein storage in a shaft drier, air circulation drier or climate-controlled silo takes place within a temperature range from 20 to 95° C.

9. The process as claimed in claim 1 , wherein, a shaft drier, air circulation drier and/or climate-controlled silo is heated isothermally or has sufficient thermal insulation for an isothermal mode of operation.

10. The process as claimed in claim 1 , wherein granules are additionally contacted at an outlet of a shaft drier, air circulation drier and/or climate-controlled silo with dry and/or heated air.

11. The process as claimed in claim 1 , wherein the contacting with water vapor-containing atmosphere in a) is followed downstream by a further process step for removing surface water from granules discharged.

12. The process as claimed in claim 1 , wherein the mean residence time of granules in a silo or shaft drier is at least 24 h.

13. The process as claimed in claim 1 , wherein not more than 10% of granules experience a residence time of less than 72 h and not more than 1% of granules experience a residence time of less than 24 h.

14. The process as claimed in claim 1 , wherein the component(s) B containing the salt are in the form of granules.

15. 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.

16. 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.

17. 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.

18. The process as claimed in claim 1 , wherein the composition comprises:
A) 1 to 95 parts by weight, based on the sum total of A and B, of the thermoplastic polymer or the mixture of the plurality of thermoplastic polymers different from B and
B) 5 to 99 parts by weight, based on the sum total of A and B, of
B1) the at least one graft polymer prepared in an emulsion polymerization process,
B2) optionally the at least one graft polymer prepared by the bulk, suspension or solution polymerization process,
B3) optionally the at least one rubber-free vinyl(co)polymer and

C) 0.1 to 20 parts by weight, based on the sum total on A and B, of the at least one commercially available polymer additive.

19. The process as claimed in claim 1 , wherein the composition comprises:
A) 30 to 85 parts by weight, based on the sum total of A and B, of the thermoplastic polymer or the mixture of the plurality of thermoplastic polymers different from B and
B) 15 to 70 parts by weight, based on the sum total of A and B, of
B1) the at least one graft polymer prepared in an emulsion polymerization process,
B2) optionally the at least one graft polymer prepared by the bulk, suspension or solution polymerization process,
B3) optionally the at least one rubber-free vinyl(co)polymer and

C) 0.3 to 7 parts by weight, based on the sum total on A and B, of the at least one commercially available polymer additive.

20. The process as claimed in claim 1 , wherein t

Assignees

• Covestro Deutschland Ag

Inventors

• Thiem Hans-Juergen
• Hermsdorfer Ingmar
• Mannel Birgit
• Seidel Andreas
• Wenz Eckhard
• Klankers Hans-Juergen
• Frye Lars
• Kempkes Hartwig

Classifications

• C08J3/203

  Solid polymers with solid and/or liquid additives · CPC title

• C08F6/28

  Purification · CPC title

• C08L69/00

  Compositions of polycarbonates; Compositions of derivatives of polycarbonates · CPC title

• C08J2369/00

  Characterised by the use of polycarbonates; Derivatives of polycarbonates · CPC title

• C08J2433/20

  Homopolymers or copolymers of acrylonitrile (C08J2455/02 takes precedence) · CPC title