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Process for preparing copolyamide without encrustation in autoclave

A technology of copolyamide and polyamide, applied in the field of preparation of copolyamide, which can solve the problems of high cost, lower product yield, unsatisfactory solution, etc.

Active Publication Date: 2020-08-14
POLYTECHNYL SAS
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Collectively, these side effects lead to costly and time-consuming downtime
[0005] Also, a common problem is that the resulting polymers are not fluid enough for injection molding applications at the temperatures required by the different polymerization methods
Attempts to increase fluidity by raising the temperature often result in at least a portion of the polymer decomposing and thus reducing the yield of the desired product
[0006] To date, these issues have not been satisfactorily resolved

Method used

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  • Process for preparing copolyamide without encrustation in autoclave

Examples

Experimental program
Comparison scheme
Effect test

example 1

[0090] Example 1 (invention)

[0091] Preparation of copolyamide 66 / 6T in an industrial-scale batch plant comprising an evaporator of the external recirculation type and an agitated autoclave, both equipped to supply heat by suitable means and under pressure-controlled conditions Evaporated process steam is discharged below. The following manufacturing processes are used:

[0092] - 52% by weight of an aqueous solution of the N-salt (a stoichiometric aqueous solution of hexamethylenediamine and adipic acid) was charged together with 40% by weight of an aqueous solution of the 6T salt (a stoichiometric aqueous solution of hexamethylenediamine and terephthalic acid) to evaporate In the container, the ratio of the two solutions is selected to obtain a composition (mixed salt) containing 6T salt with a molar fraction equal to 35% in the resulting mixed salt. Some additives were also added to the salt mixture: acetic acid (1.65 mol per 100 mol of mixed salt), hexamethylenediamine...

example 2

[0101] Example 2 (comparative example)

[0102] The process of Example 1 was repeated with the main difference that the pressure release phase in the autoclave started when the mass temperature reached 268°C instead of 288°C. Some other process parameters were modified accordingly:

[0103] - Stress Polymerization has a duration of 61 minutes instead of 85 minutes

[0104] - Mass temperature at the end of the 35 minute pressure release phase is 288°C instead of 293°C

[0105] - The refining stage at atmospheric pressure lasted 14 minutes instead of 7 minutes, the polymer mass temperature at the end of this stage was 291 °C. This longer refining stage is offset by a slightly lower refining temperature and shorter pressure polymerization time, resulting in a final polymer with the same molecular mass as in Example 1.

[0106] All other process features remained unchanged compared to Example 1.

[0107] Thus, a polymerization cycle of 8 consecutive batches was carried out in ...

example 3

[0109] Example 3 (comparative example)

[0110] The process of Example 1 was repeated with the main difference that the pressure release phase in the autoclave started when the mass temperature reached 277°C instead of 288°C. Some other process parameters were modified accordingly:

[0111] - Stress Polymerization has a duration of 70 minutes instead of 85 minutes

[0112] - Mass temperature at the end of the 35 minute pressure release phase is 290°C instead of 293°C

[0113] - The refining stage at atmospheric pressure lasted 12 minutes instead of 7 minutes, the polymer mass temperature at the end of this stage was 292°C. This longer refining stage is offset by a slightly lower refining temperature and shorter pressure polymerization time, resulting in a final polymer with the same molecular mass as in Example 1.

[0114] All other process features remained unchanged compared to Example 1.

[0115] Thus, polymerization cycles of 10 consecutive batches were carried out in ...

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Abstract

Process for preparing a copolyamide without encrustation in the autoclave. The present invention relates to a novel process for the production of a copolyamide comprising a polymerization product of hexamethylene diamine, adipic acid and terephthalic acid.

Description

technical field [0001] The present invention relates to a process for the preparation of copolyamides by polymerizing the monomers adipic acid, hexamethylenediamine and terephthalic acid. Background technique [0002] Polyamides are a subclass of specialty polymers. They are both naturally occurring and man-made. Synthetically obtained polyamides are of great importance in the chemical industry and for society in general due to their extraordinary properties. In the chemical industry, polyamides are usually obtained by condensation of their monomers in a stepwise growth reaction. The resulting product consists of monomeric units under dehydration. In the product, the monomer units are linked by amide bonds. Sometimes the monomer can itself be an amide, as in caprolactam. In general, however, the monomers exhibit amino and / or carboxyl groups. [0003] According to the composition of their backbone, which can be aliphatic, semiaromatic or aromatic, synthetic polyamides a...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C08G69/26C08G69/28
CPCC08G69/265C08G69/28C08G69/46C08K5/5415
Inventor J-F.蒂埃里C.穆瓦诺R-G.奥贝尔
Owner POLYTECHNYL SAS