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US 10,370,479 B2Granted
Process for making a polymer polyol
AssigneeBASF SE
InventorsChristian Koenig, Dejan Petrovic, Achim Loeffler, Andreas Bauder, Daniel Freidank, Dirk Opfermann, Isa Alexandra Queiroz Da Fonseca, Caroline Mages-Sauter, Chuan Long Fu, Shu Kui Wang
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Abstract
This invention relates to a continuous process for making a polymer polyol, the polymer polyol produced according to the said process and its applications.
Claims27
A continuous process for making a polymer polyol, the polymer polyol comprising:
- particles of a thermoplastic styrene-acrylonitrile-copolymer (TP);
- at least one polyol (P);
- and
- a stabilizer (S);
- wherein the stabilizer (S) comprises:
- from 10 to 70% by weight, based on the sum of all components, of at least one polyol P2, and
- at least one polyol CSP which is a reaction product of at least one macromere M, styrene and acrylonitrile in P2, optionally with an initiator and/or a chain transfer agent,
- wherein the macromere comprises one or more polymerizable double bonds and one or more hydroxyl-terminated polyether tails,
- a content of the macromere M in the stabilizer (S) is between 30-70 wt %, based on the sum of all components of the stabilizer,
- wherein the polyol CSP comprises two or more —OH groups,
- the process comprising:
- continuously feeding the TP, the P and the S to an extruder (E) having a plurality of process zones,
- preparing an initial dispersion of the TP, the P and the S in the extruder (E);
- continuously passing the initial dispersion obtained in the extruder into at least one rotor-stator device (RS) decoupled from the extruder comprising at least one rotor-stator combination;
- and
- cooling the rotor-stator treated dispersion below the glass transition temperature (Tg) of the thermoplastic styrene-acrylonitrile-copolymer (TP) after passing all of the rotor-stators (RS) to obtain the polymer polyol,
- wherein in the preparation of the initial dispersion, TP is continuously fed into a first process zone Z1 of the extruder E, S is continuously fed into a second process zone Z2 or a later process zone, and P is continuously fed into a process zone following the process zone of addition of S, wherein the terms “first” and “second” refer to a direction of flow of the reaction mixture through the extruder E.
14 more elements
Dependencies are inferred from the claim text.