Method for preparing a polymer from at least one cyclic monomer
US-9738751-B2 · Aug 22, 2017 · US
US10280258B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10280258-B2 |
| Application number | US-201414901783-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jun 30, 2014 |
| Priority date | Jul 1, 2013 |
| Publication date | May 7, 2019 |
| Grant date | May 7, 2019 |
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The present invention provides a method for producing an oxymethylene copolymer which involves polymerizing trioxane and a comonomer cationically at a polymerization temperature of 135° C. to 300° C. in the presence of a protic acid salt having the molecular weight of 1000 or less, and at least one polymerization initiator selected from the group consisting of protic acids, protic acid anhydrides, and protic acid ester compounds having the molecular weight of 1000 or less.
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The invention claimed is: 1. A method for producing an oxymethylene copolymer, the method comprising: cationically polymerizing trioxane and a comonomer at a polymerization temperature of 140° C. to 165° C. in the presence of at least one protic acid salt selected from the group consisting of perchloric acid salts and at least one polymerization initiator selected from the group consisting of perchloric acid, acid anhydrides thereof, and ester compounds thereof, and charging at least one polymerization terminator; wherein the content of the at least one polymerization initiator is 0.01 ppm by mass to 100 ppm by mass relative to the content of the trioxane, and the mole ratio of the at least one polymerization initiator to the at least one protic acid salt is in the range of 1:0.01 to 1:5; and wherein the polymerization reaction is performed while the polymerization temperature is maintained from charging of the at least one polymerization initiator till the charging of the at least one polymerization terminator so that a maximum temperature difference from the time of the charging the at least one polymerization initiator until the time of charging the at least one polymerization terminator is less than 20° C. 2. The method for producing an oxymethylene copolymer according to claim 1 , wherein the polymerization is performed in the presence of at least one ketone compound. 3. The method for producing an oxymethylene copolymer according to claim 1 , wherein the polymerization is performed in the presence of at least one molecular weight modifier, and the content of the at least one molecular weight modifier is 0.01 ppm by mass to 10% by mass relative to the content of the trioxane. 4. The method for producing an oxymethylene copolymer according to claim 1 , the method further comprising: adding all or part of the at least one polymerization initiator and the at least one protic acid salt that are diluted with a solvent having the boiling point at 1 atm of 115° C. or lower. 5. The method for producing an oxymethylene copolymer according to claim 1 , wherein the at least one polymerization terminator is at least one selected from the group consisting of amine compounds, hydroxides of alkali metals, alcoholates of alkali metals, hydroxides of alkaline earth metals, and alcoholates of alkaline earth metals. 6. The method for producing an oxymethylene copolymer according to claim 1 , wherein the amount of the at least one polymerization terminator added is 0.1 to 100 equivalents relative to the amount of the polymerization initiator. 7. The method for producing an oxymethylene copolymer according to claim 1 , the method further comprising: adding all or part of the at least one polymerization terminator that is diluted with a solvent having the boiling point at 1 atm of 115° C. or lower. 8. The method for producing an oxymethylene copolymer according to claim 1 , wherein the method continuously produces the oxymethylene copolymer using a continuous polymerization device in which a static mixer continuous polymerization machine having a static mixing element inside thereof and a polymerization terminator mixing machine are connected in series. 9. The method for producing an oxymethylene copolymer according to claim 1 , the method further comprising adding at least one stabilizer selected from the group consisting of sterically hindered phenol compounds and triazine compounds. 10. The method for producing an oxymethylene copolymer according to claim 1 , the method further comprising: removing, as a gas component, at least a portion of volatile components and thermally unstable portions of a polymerized mixture that has been polymerized at a temperature of 130 to 300° C. under a pressure of 0.00001 to 50 MPa in at least one degasifier selected from the group consisting of flash pots, single screw or twin screw extruders with a vent, and horizontal high viscosity liquid degasifiers with single screw or twin screw blade. 11. The method for producing an oxymethylene copolymer according to claim 10 , the method further comprising: liquefying the gas component to reuse a part or all of the gas component in a raw material trioxane.
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