Method for preparing slices of nylon 6 in high viscidity

A high-viscosity and slicing technology, which is applied in the field of producing high-viscosity nylon 6 slices, can solve the problems of insufficient caprolactam hydrolysis ring-opening, less intense polymerization reaction, and affecting the whiteness of slices, etc., achieving high average molecular weight and wide application , the effect of reducing energy consumption and production cost

Inactive Publication Date: 2005-03-30
夏焕文
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Problems solved by technology

[0002] In the patent No. ZL00113446.9, a production method of ultra-high viscosity nylon 6 engineering plastics is mentioned. Although this method breaks through the traditional formula and technology, the relative viscosity of the polymer is increased to above 5.0, but because the method uses a single The catalyst makes the polymerization reaction less intense, the polymerization time is longer, and the hydrolysis and ring opening of caprolactam is not thorough enough, resulting in a high content of low molecular weight in the polymer before extraction. Due to the possibility of oxidation during the production process, directly affect the whiteness of slices,
[0003] In summary, although the above-mentioned method has improved the relative viscosity of the polymer to more than 5.0, it still has certain defects in the process of hydrolysis and polymerization.

Method used

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Examples

Experimental program
Comparison scheme
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Embodiment

[0031] Example: at 2m 3 In the polymerization kettle, it is produced with pure caprolactam, and the feeding amount is 1000 kg.

[0032] Calculated using the following formula:

[0033] Distilled water: 45 kg

[0034] 85% by weight phosphoric acid: 1.95 kg, diluted with 8 kg of distilled water,

[0035] Sodium hydroxide: 1 kg, dissolved in 10 kg of distilled water,

[0036] Phosphorous acid: 0.0625 kg, dissolved in 0.3 kg of distilled water,

[0037] First add caprolactam into the kettle, then put the prepared sodium hydroxide solution and the remaining distilled water, namely 45kg-8kg-10kg-0.3kg=26.7kg into the kettle, replace with nitrogen and start to heat up. After melting, start stirring, and press the prepared aqueous solution of phosphoric acid and phosphorous acid into the kettle with nitrogen from the additive tank at the top of the kettle. During the heating process, control the pressure of the kettle between 0.8 and 1.0Mpa. When the material temperature When it ...

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Abstract

The invention relates to a method for producing nylon 6 high-viscosity section. A first, to prepare various kinds of assistants, then to proceed materials input and displacing, after the materials are smitten, adding another two assistants and stirring to proceed hydrolysis ring-opening, pressure of boiler is 0.8-1.0 MPa, temp. of the materials is 250-290 deg.C, then to keep polymerization 60-180 minutes in vacuum -0.05-0.09 MPa, finally to static balance 60-120 minutes in pressure 0.2-0.4 MPa to produce nylon 6 high-viscosity section that relative viscosity is more than 5.0. The method is suitable for the nylon 6 high-viscosity section produced by raw materials of quality product caprolactam, substandard product caprolactam and recovered caprolactam.

Description

technical field [0001] The invention relates to a method for producing nylon 6 high-viscosity chips Background technique [0002] In the patent No. ZL00113446.9, a production method of ultra-high viscosity nylon 6 engineering plastics is mentioned. Although this method breaks through the traditional formula and technology, the relative viscosity of the polymer is increased to above 5.0, but because the method uses a single The catalyst makes the polymerization reaction less intense, the polymerization time is longer, and the hydrolysis and ring opening of caprolactam is not thorough enough, resulting in a high content of low molecular weight in the polymer before extraction. Due to the possibility of oxidation during the production process, directly affect the whiteness of slices, [0003] In summary, although the above-mentioned method has improved the relative viscosity of the polymer to more than 5.0, it still has certain defects in the process of hydrolysis and polymeri...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C08G69/14
Inventor 夏焕文
Owner 夏焕文
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