Treating agent for decomposing unstable terminal group, stabilized polyacetal resin produced with the same, production process, composition, and molded object
A polyacetal resin and terminal group technology, applied in the fields of unstable terminal group decomposition treatment agents, stabilized polyacetal resins using the same, manufacturing, compositions and moldings, can solve environmental problems, Thermal instability, reduced residual amount of end groups, etc.
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[0256] The present invention will be described below by way of examples, but the present invention is not limited by these examples.
[0257] Hereinafter, the cases of using the quaternary ammonium salt of (I), the quaternary ammonium salt of (II), and the quaternary ammonium salt of (III) are divided into cases, and further, for each case, it is divided into examples of production and comparison of stabilized polyacetal resins. Production examples, examples and comparative examples of compositions using stabilized polyacetal resins and molded articles thereof will be described.
[0258] Example using the quaternary ammonium salt of (I)
[0259] (1) Implementation and Comparative Production Examples of Stabilized Polyacetal Resin (Copolymer)
[0260] [Preparation of Crude Polyacetal Copolymer (A) for Stabilization Treatment]
[0261] Use a cylinder with a partially overlapping cross-sectional shape of two circles, a jacket with a hot (cold) medium passing through the outside...
Embodiment manufacture example 1-1~7
[0265] 0.3 parts by weight of triethylene glycol [3-(3-tert-butyl-5-methyl-4-hydroxyphenyl) propionate], and 2 parts by weight of an aqueous solution of a quaternary ammonium salt of the following acidic cyclic amide compound adjusted to a predetermined concentration as a decomposition treatment agent (in terms of quaternary ammonium nitrogen, with respect to 1 kg of crude polyacetal copolymer, the addition of the quaternary ammonium salt rate of 1.4mmol) and uniformly mixed.
[0266] Then, the mixture was supplied to a twin-screw extruder (diameter 30mm) provided with one exhaust port, under an exhaust vacuum degree of 2.7kPa (20mmHg), a barrel temperature of 200°C, and an average residence time of 300 seconds. , the volatile matter is removed from the (exhaust port) degassing port, and melt kneading simultaneously to obtain a pellet-like stabilized polyacetal copolymer (implementation of manufacturing example 1-1 (a-1) to implementation of manufacturing example 1-7 (a-7)). ...
Embodiment manufacture example 1-8
[0277] 0.3 parts by weight of triethylene glycol [3-(3-tert-butyl-5-methyl-4-hydroxyphenyl) propionate], and 2 parts by weight of an aqueous solution of the quaternary ammonium salt (A-1) of the above-mentioned acidic cyclic amide compound adjusted to a predetermined concentration as a decomposition treatment agent (in terms of quaternary ammonium nitrogen, with respect to every 1 kg of crude polyacetal copolymer, quaternary Ammonium salt was added at a rate of 0.7 mmol) and mixed uniformly.
[0278] Next, it melt-kneaded with the twin-screw extruder similarly to the above-mentioned production example, and obtained the pellet form stabilized polyacetal copolymer (a-8).
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