Continuous polymerization production process of high-viscosity polyamide 6

A production process, polyamide technology, applied in the field of polyamide 6 continuous polymerization production process, which can solve the problems of high-viscosity polyamide 6 chip internal quality evaluation, retention, and application impact, and achieve stable and reliable product quality

Active Publication Date: 2012-07-04
湖南岳化化工股份有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0022] Through the above process analysis, it can be seen that the current production method of high-viscosity polyamide 6 chips is quite different from the production process of conventional polyamide 6 chips with a relative viscosity of 2.6 to 3.0, whether it is the process flow or the addition of additives, so its implementation Difficult to implement in conventional industrial-scale VK tubes, or implementation requires major modifications to existing conventional devices
More importantly, the above-mentioned processes are currently still in the stage of conception and industrialization, and there is no evaluation of the intrinsic quality of the obtained high-viscosity polyamide 6 chips, which will undoubtedly directly affect downstream applications, especially in high-end fields. Therefore, the industrial application effect of the above process is also unknown

Method used

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  • Continuous polymerization production process of high-viscosity polyamide 6
  • Continuous polymerization production process of high-viscosity polyamide 6
  • Continuous polymerization production process of high-viscosity polyamide 6

Examples

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Embodiment 1

[0035] Example 1: After the solid caprolactam is melted in the melting tank or directly from the caprolactam manufacturer’s liquid caprolactam and 1-4% deionized water, it is poured into the caprolactam intermediate tank, mixed uniformly and stored in the intermediate tank, and used The feed pump preheats the mixed caprolactam to 200℃ through the preheater and then transports it to the prepolymerizer (VK tube) for hydrolysis and ring opening and prepolymerization of caprolactam. The pressure of ring opening and prepolymerization is 2.50bar and the temperature is 275℃, the flow rate of caprolactam is 2000kg / h, and then the polymer is discharged by the front polymer discharging pump to the rear polymerizer; the pressure of post polymer is 0.2bar, the temperature is 245~270℃, and the polymer melt is melted with the discharging gear pump. Discharge outward; polymer melt is sliced ​​after polymer filter, casting head, underwater pelletizer, and vibrating screen; put slices into pre-e...

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Abstract

The invention relates to a continuous polymerization process of high-viscosity polyamide 6, comprising the following steps of: preparing caprolactam with de-ionized water; pre-heating the mixed caprolactam to a temperature in a range of 220+ / -30 DEG C by a pre-heater and conveying the mixed caprolactam into a pre-polymerizer by a feeding pump to carry out hydrolyzed ring opening and pre-polymerization on the caprolactam, wherein the pressure of the ring opening and the pre-polymerization is 2.50+ / -0.50 bar, the temperature is in a range of 270+ / -15 DEG C and the flow of the caprolactam is 2200+ / -500 kg / h; then, discharging materials into a post-polymerizer to carry out post-polymerization to obtain a polymer melt, wherein the pressure of the post-polymerization is 0.35+ / -0.25 bar and the temperature is 250+ / -30 DEG C; treating the polymer melt by a polymer filter, a casting strip head, an underwater granulator and a vibrating screen to obtain slices; adding the slices into a pre-extracting water pot to carry out pre-extraction with hot water at the temperature in a range of 115+ / -10 DEG C; then, conveying the treated slices into an extracting tower and extracting with the hot water at the temperature in a range of 100+ / -20 DEG C; conveying the extracted slices into a drying tower and carrying out counter-current drying by nitrogen gas; drying at the temperature in a range of 120+ / -30 DEG C and discharging the dried slices into a slice cooling bin; and conveying the cooled slices into a slice storage bin and a slice packaging bin by the nitrogen gas and packaging to obtain the high-viscosity polyamide 6 slices with the relative viscosity of 3.4-4.0.

Description

Technical field [0001] The invention relates to a high-viscosity polyamide 6 continuous polymerization production process; in particular, a large-scale continuous production of high-viscosity polyamide 6 chips with a relative viscosity of 3.4 to 4.0. Background technique [0002] For the same polymer, high melt viscosity is a reflection of high molecular weight, and high molecular weight means higher physical and mechanical properties. Therefore, high-viscosity polyamide 6 has application advantages in extrusion and blow molding to prepare pipes, bottles, sheets, films, engineering plastics and high-performance fibers. In the above applications, the high melt viscosity has a beneficial effect on the processing performance and the properties of the resulting product. [0003] The method of producing polyamide 6 has long been known. For example, it is published in "Handbook of Plastics Industry-Polyamide", Chemical Industry Press, Beijing, 2001, P54-55. According to these methods,...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C08G69/16C08G69/46
Inventor 龙清明任兴波
Owner 湖南岳化化工股份有限公司
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