Method for producing polyacetal copolymer

Patent metadata

Field	Value
Publication number	US-9546241-B2
Application number	US-201414786249-A
Country	US
Kind code	B2
Filing date	Apr 4, 2014
Priority date	Apr 25, 2013
Publication date	Jan 17, 2017
Grant date	Jan 17, 2017

Abstract

A high-quality polyacetal copolymer produced by a simple process in an economical manner. The process includes supplying a raw material including trioxane and the like to a reaction device; setting the polymerization environmental temperature to no more than 100° C. until the reaction device conversion rate becomes 0.5, and then carrying out further polymerization; vaporizing and separating unreacted monomers from the reaction mixture at an environmental temperature of at least 115° C. and less than 140° C.; supplying the separated monomers to the raw material supply; and recovering the polyacetal copolymer from the reaction mixture.

First claim

The invention claimed is:

1. A method for producing a polyacetal copolymer. comprising:
supplying a raw material comprising trioxane, a comonomer which copolymerizes with the trioxane, and a non-volatile protonic acid to a continuous stirring mixer type reaction device having two parallel shafts which rotate in the same or in opposite directions, a plurality of paddles mounted on each shaft, and a barrel which comes close to an outer circumference of the paddles, wherein a long axis end of a paddle periodically comes close to a short axis end of a companion side, wherein the raw material is charged from an introduction opening provided at one end in an axial direction, and a reaction mixture and an unreacted monomer are obtained from a plurality of removal openings provided at the other end;
carrying out a polymerization reaction of the raw material, and obtaining a reaction mixture;
vaporizing and separating an unreacted monomer from the reaction mixture at an environmental temperature of at least 115° C. and less than 140° C.;
supplying the unreacted monomer to the raw material supply; and
recovering the polyacetal copolymer from the reaction mixture,
wherein the polymerization reaction is carried out at a polymerization environmental temperature set to no more than 100° C. until a weight ratio D/C of the polyacetal copolymer D with respect to a total supplied monomer C which is defined as a sum of a monomer A which is newly supplied to the reaction device and a monomer B which is recovered from the reaction device and re-supplied, becomes 0.5, and then carrying out further polymerization;
wherein the D/C is no less than 0.7;
and a weight ratio D/A of the polyacetal copolymer D with respect to the monomer A which is newly supplied to the reaction device is no less than 0.85.

2. The method for producing a polyacetal copolymer according to claim 1 , wherein the non-volatile protonic acid comprises at least one selected from the group consisting of a heteropoly acid, an isopoly acid, and an acid salt thereof.

3. The method for producing a polyacetal copolymer according to claim 1 , wherein the non-volatile protonic acid is a heteropoly acid shown by formula (1) below or an acid salt thereof:
H x [M m .M′ n O l ].y H 2 O   Formula (1)

wherein, in the formula (1), M is a central element selected from the group consisting of P and/or Si, M′ is one or more coordination element selected from the group consisting of W, Mo, and V, and
1 is 10 to 100, m is 1 to 10, n is 6 to 40, x is 1 or more, and y is 0 to 50.

4. The method for producing a polyacetal copolymer according to claim 3 , wherein the heteropoly acid or acid salt thereof comprises at least one compound selected from the group consisting of phosphomolybdic acid, phosphotungstic acid, phosphomolybdotungstic acid, phosphomolybdovanadic acid, phosphomolybdotungstovanadic acid, phosphotungstovanadic acid, silicotungstic acid, silicomolibdic acid, silicomolybdotungstic acid, silicomolybdotungstovanadic acid, and acid salts thereof.

5. The method for producing a polyacetal copolymer according to claim 1 , wherein the non-volatile protonic acid comprises an isopoly acid shown by formula (2) or (3) below or an acid salt thereof:
x M I 2 O. p M V 2 O 6 .y H 2 O   Formula (2)

x M I 2 O. p M VI 2 O 6 .y H 2 O   Formula (3)

wherein, in the formulas (2) and (3), M I is hydrogen, which may be partially substituted with a metal,
M V is at least one selected from the group consisting of V, Nb, and Ta of the V group of the periodic table,
M VI is at least one selected from the group consisting of Cr, Mo, W, and U of the VI group of the periodic table,
p and x are 1 or more, and y is 0 to 50.

6. The method for producing a polyacetal copolymer according to claim 5 , wherein the isopoly acid or acid salt thereof comprises at least one compound selected from the group consisting of paratungstic acid, metatungstic acid, paramolybdic acid, metamolybdic acid, paravanadic acid, metavanadic acid, and acid salts thereof.

7. The method for producing a polyacetal copolymer according to claim 1 , wherein the comonomer comprises at least one selected from the group consisting of 1,3-dioxolane, diethylene glycol formal, 1,4-butanediol formal, and ethylene oxide.

Assignees

• Polyplastics Co

Inventors

• Monma Tomohiro
• Masuda Eiji
• Sanada Shoji

Classifications

• C08G2/10 Primary

  Polymerisation of cyclic oligomers of formaldehyde · CPC title

• C08L59/04

  Copolyoxymethylenes · CPC title

• C08G2/06

  Catalysts (Catalysts in general B01J) · CPC title

• C08G2/24 Primary

  with acetals · CPC title

• C08G4/00

  Condensation polymers of aldehydes or ketones with polyalcohols; Addition polymers of heterocyclic oxygen compounds containing in the ring at least once the grouping —O—C—O— (of cyclic oligomers of aldehydes C08G2/00) · CPC title